Pacific® CSV – Cast Steel Valves by Crane CPE

NEW! Cast Steel Valves

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Brochure Datasheet Flyer IOM Video- Guided Wedge Video Video - Live Loading Price List Website

Next www.cranecpe.com Crane ChemPharma & Energy (within Crane’s Fluid Handling segment) designs and manufactures a variety of high performance products. Its trusted brands ALOYCO®, CENTER LINE®, COMPAC-NOZ®, CRANE®, DEPA®, DUO-CHEK®, ELRO®, FLOWSEAL®, JENKINS®, KROMBACH®, NOZ-CHEK®, PACIFIC VALVES®, RESISTOFLEX®, REVO®, SAUNDERS®, STOCKHAM®, TRIANGLE®, UNI-CHEK®, WTA®, and XOMOX® offer customers complete and innovative product portfolio designed for the most demanding corrosive, erosive, and high purity applications. Among the industries served are the chemical processing, biotechnology, pharmaceutical, oil & gas, refining, and power generation.

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PacificÂŽCSV Cast Steel Valves Overview

Crane ChemPharma & Energy

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Table of Contents A Continuing Story of Success Dependable Operation Engineers know they can trust Pacific速 Valves. They set the industry standard for dependable, consistent operation, even in the most adverse conditions with years of trouble-free performance. Customer Service Customers know they can depend on Pacific速 for after sales service and technical support from one of our many locally based sales associates and distribution partners.

Introduction to Crane 3 4 Comprehensive Product Portfolio Pacific速CSV Quality 5 Product Portfolio 6 Gate Valve Features 7 Globe Valve Features 8 Swing Check Valve Features 9 Applications 10 Engineering Approach 11

Global Compliance Pacific速CSV valves are fully compliant to all relevant global standards.

Crane ChemPharma & Energy

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Introduction to Crane • Crane Co.

FOUNDED IN 1855

Crane Co.

FLUID HANDLING AEROSPACE & ELECTRONICS MERCHANDISING SYSTEMS AND PAYMENT TECHNOLOGIES ENGINEERED MATERIALS

27%

37%

Crane Co.

27%

Crane Co. is a diversified global manufacturer of engineered industrial products traded on the New York Stock Exchange (NYSE: CR). One of its segments, Crane Fluid Handling, provides highly engineered products for fluid handling applications worldwide.

Aerospace & Electronics

The Fluid Handling Segment

Merchandising and Payment Technologies

Crane Fluid Handling provides highly-engineered products including valves, pumps, controls and water treatment equipment for fluid handling applications worldwide. Its operating units include Crane ChemPharma & Energy, Crane Nuclear, Crane Building Services, Crane Pumps & Systems, Crane Supply, Barksdale Control Products.

Engineered Materials

Crane ChemPharma & Energy (CPE) Crane CP&E designs and manufactures a variety of highperformance products including: highly-engineered check valves, sleeved plug valves, lined valves, process ball valves, high performance butterfly valves, bellows sealed globe valves, aseptic and industrial diaphragm valves, multi/ quarter-turn valves, actuation, sight glasses, lined pipe, fitting and hoses, and air-operated diaphragm and peristaltic pumps. Its trusted brands are in use worldwide in many industries, including Oil & Gas, Oil Refining, Petrochemical, Power Generation, Chemical Processing, Biotechnology, and Pharmaceutical.

Crane (CPE) Brands ALOYCO · CENTER LINE · COMPAC-NOZ · CRANE · DEPA DUO-CHEK · ELRO · FLOWSEAL · JENKINS · KROMBACH NOZ-CHEK · PACIFIC · RESISTOFLEX · REVO · SAUNDERS STOCKHAM · TRIANGLE · UNI-CHEK · WTA · XOMOX

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Fluid Handling

Key Markets 18% 9%

25%

23% 25% Chemical/Petrochemical Energy Building Services Municipal General Industry

Crane ChemPharma & Energy

Pacific® Valves Company History and Introduction Pacific® Valves was established in Signal Hill, California in 1934, as a company devoted to reconditioning all makes, models, types and sizes of valves. During this time, the manufacturing engineers quickly noticed a pattern of design flaws in the valves that consistently drove repair business. By using this unique experience, Pacific quickly developed its own line Launched line of Bolted Bonnet gates, globe & check valves

of Gate, Globe and Check valves and we’ve never looked back. The cornerstones of our success are continuous quality improvement, reliable service and support, and robust investment into product innovation. These are the hallmarks that have enabled Pacific Valves to become one of the most proven and respected brands in the world. Crane acquires Pacific Valves from Mark Controls

Parallel disc gate valve introduced

1934

1976 1941

1982 1979

Released pressure seal line of gates, globes & checks

Company founded in Signal Hill, CA

Pacific launches Pacific®Cast Steel

2009 1994

Y-globe design, 1st C12A material produced

2015 Pacific adds new facility in Viralimali, India

Manufacturing Locations

SIGNAL HILL, CALIFORNIA U.S.A

CULLMAN, ALABAMA U.S.A

Crane ChemPharma & Energy

VIRALIMALAI, INDIA

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Pacific Quality Crane is built on quality principles and practices to achieve the best safety, quality, performance, delivery, service and total cost. As such, all suppliers must abide by the policies set forth in the Crane Global Supplier Quality Manual.

Process-driven Results

Certified Quality

Years of research and development, together with practical experience in reconditioning all types of valves, have gone into design and manufacture of Pacific® Valves. High quality materials and workmanship, combined with the modern manufacturing methods used in producing these valves are your assurance of a dependable, uniform product. Pacific Valves are designed in accordance with the latest edition of industry requirements and design standards.

The following is a partial list held by Crane, and/or Crane affiliates. All certificates are available upon request. • API 622 • CE/PED • Indian Boiler Regulation (IBR) • ISO 15848-1 • ISO 9001:2008

Crane processes are audited by global customers.

Traceability

Process Failure Mode Effects Analysis (PFMEA) is a structured tool used to evaluate and document ways in which a product might fail to meet customers’ expectations.

Pacific®CSV has partnered with a world renowned foundry to deliver the highest quality valves within the industry. By being in a joint venture, Pacific now has control over the entire process flow map from the pour to delivery of assembled valve. Being in a joint venture provides confidence that the product we deliver will be assembled with the utmost care. With that care, also comes the ability to trace each and every component back to its original source, so if an error was to occur, we can get to the root of the problem to ensure that it will never happen again. Our world-class manufacturing and traceability processes from the pour to delivery of assembled valves, provide the highest quality assurance established to meet or exceed our customers’ requirements.

These valves comply with the applicable requirements of the following standards: • API 600 • API 623 • API 598 • ASME B 16.34 • ASME B 16.10 • ASME B 16.5 • ASME B 16.25

Process Flow Process Failure Modes Effect Analysis Address High RPN’s Control Plan

Scrap Sheet

Work First off Calibration Instruction Instructions Log

Gauges

Poka Yoke

TPM’s

Control Plan Process - Defining expectations before production.

Consistent Quality. Replicable Results.

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Crane ChemPharma & Energy

Product Portfolio and Customer Support Customer Support Our Cullman stocking and Long Beach locations allow us to provide: • Responsive Customer Service for Quotes and Project Support • Quick Ship Capabilities • Consistent On Time Delivery • US based Technical and Application Support • US Country of Origin option available via Long Beach facility

Peace of Mind. Pacific® Valves are a preferred supplier for OEMs, EPCs, and end users around the world because our customers know that we have a superior selection, offered in a wide array of materials, available in an almost unlimited variety of customizations. If you need a cast solution, our application engineers work with you to provide the right offering to meet your valve requirements.

Pacific®CSV • Proven designs available in WCB, LCB, LCC, WC6, WC9, C5, C12, CF3M, CF8, CF8M • Full product design range, sizes 2” – 24”, pressure classes #150 - #600 Valve Type & Class

2.5

100

150

200

250

300

350

400

450

500

600

• • •

150 Gate

300 600 150

Globe

300 600 150

Check

300 600

• • • • • • • • •

• • • • •

• • •

Larger sizes and higher pressure classes available upon request.

Crane ChemPharma & Energy

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Key Features - Gate Valve Stem and stem nuts have been designed to minimize torque

Gate Valve Cv 16000

15% increase

14000 12000 10000 8000 6000 4000 2000 0

2”

3”

4”

Pacific®CSV

6”

8”

10”

12”

Competitor

Fully-guided wedge ensures smooth operation in both horizontal and vertical orientations to help prevent sticking Live loading option extends fugitive emissions performance by eliminating the need for manual packing adjustment

T-slot stem designed for simple installation and maintenance

Modular stuffing box facilitates changeover for low fugitive emissions and monitoring port options

Available in solid or flexible wedge, which provides a better seal

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Crane ChemPharma & Energy

Key Features Globe Valve

Stem and stem nuts have been designed to minimize torque

Modular stuffing box facilitates changeover for low fugitive emissions and monitoring port options

Integral ISO 5210 mounting is available in larger sizes for ease of actuation

1 2

Uniquely designed line contact between disc and seat results in lower seating torque, permitting faster set up

Crane ChemPharma & Energy

The guided disc option facilitates seating and prevents vibration during high velocities and pressure drops

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Key Features Swing Check Swing Check Valve Cv 9000 8000 7000 6000 5000 4000 3000 2000 1000 0

Disc fastener is restrained by the bonnet to eliminate the risk of a displaced disc and prevent damage to downstream equipment

50% increase

2”

3”

4”

Pacific®CSV

6”

8”

10”

12”

Competitor

Internal hung disc pin arrangement eliminates leak path from pressure boundary

Anti rotation pins

Modular design enables easy change to an optional external pin arrangement if counterweights are required

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Crane ChemPharma & Energy

Applications Pacific® Valves valves offer economical solutions for the vast majority of refining applications while maintaining the highest possible degree of performance in terms of in-line leakage and fugitive emissions. Within these industries, Pacific valves have superior performance in the following applications • Oil • Steam • Sea Water • Ethylene

They are commonly used within the following industries: • Refining • Oil • Chemical • Petrochemical • Power • Pharmaceutical

FUNCTION

Performance Chart Gate

Globe

Check

Sizes

2 “ - 24” DN15/DN600

2 “ - 18” DN15/DN450

2 “ - 24” DN15/DN600

Pressure Ratings

Class 150, 300, 600

On / Off Throttling Diversion Flow Reversal Clean Liquids & Gasses Dirty Liquids & Gasses

MEDIA TYPES

Corrosive Liquids & Gasses Hazardous Liquids & Gasses Viscous Liquids Scaling Liquids & Slurries Abrasive Slurries Fibrous Slurries Dry Materials

APPLICATION REQUIREMENTS

Vacuum Service High Flow Capacity Low Torque Fugitive Emissions Control Reduced Maintenance Extended Service Life

Superior Performance

Limited Application

Crane ChemPharma & Energy

Not Applicable

Source: Crane Engineering

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Engineering Approach 



Concept Design Robust design methodology and use of world class engineering tools to design products based on customer needs. Full compliance of relevant industry standards like API 600. API 623, ASME B 16.34, ASME B16.10. Well structured design process followed for the entire product range. This enables us to provide engineering data, general arrangement drawings with high quality and accuracy.

                            

    



    



    

 



Calculations: Standard Templates Developed

Manufacturing Feasibility Manufacturing feasibility was proven for castings – both sand and investment parts.

Master Templates Developed Rigorous product testing.

Magma Flow simulation for superior quality castings.

Fugitive Emissions Pacific believes in ensuring a safer environment, and is taking a proactive approach towards reducing fugitive emissions. Fugitive emissions occur from spills, leaks, and evaporation. Pacific®CSV will ensure some of the lowest fugitive emission ratings within the industry. To make sure Pacific® Cast Steel valves will be industry leading in fugitive emission, API 622 packing will be a standard offering.

Analysis: Stress & Deflection Evaluation

API Standard 624, First Edition, 2014 Test Report

“Type Testing of Rising Stem Valves Equipped with Graphite Packing for Fugitive Emissions” Performed for

Crane Energy http://www.cranecpe.com

CV & Pressure drop Calculations

4 inch Class 150 Gate Valve Product Code: 2355

Project Number: 214276 Test Start Date: March 10, 2015 Performed by

YARMOUTH RESEARCH AND TECHNOLOGY, LLC 434 Walnut Hill Road North Yarmouth, ME 04097 USA (207) 829-5359 info@yarmouthresearch.com www.yarmouthresearch.com

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Drawings: General Arrangement Drawings

Crane ChemPharma & Energy

Crane ChemPharma & Energy Crane Energy Headquarters 4526 Research Forest Drive, Suite 400 The Woodlands, Texas 77381 U.S.A Phone: +1 936-271-6500 Fax +1 936-271-6510 www.cranecpe.com

Pacific Valves Customer Service 3201 Walnut Avenue Signal Hill, CA 90755 U.S.A Phone: +1 562-426-2531 Fax +1 562-595-9717

Crane Cast Steel Customer Service 2129 3rd Avenue, S.E. Cullman, Alabama 35055 U.S.A Phone: +1 256-775-3800 Fax: +1 256-775-3860

Crane Co., and its subsidiaries cannot accept responsibility for possible errors in catalogues, brochures, other printed materials, and website information. Crane Co. reserves the right to alter its products without notice, including products already on order provided that such alteration can be made without changes being necessary in specifications already agreed. All trademarks in this material are property of the Crane Co. or its subsidiaries. The Crane and Crane brands logotype, in alphabetical order, (ALOYCO®, CENTER LINE®, COMPAC-NOZ®, CRANE®, DEPA®, DUO-CHEK®, ELRO®, FLOWSEAL®, JENKINS®, KROMBACH®, NOZCHEK®, PACIFIC VALVES®, RESISTOFLEX®, REVO®, SAUNDERS®, STOCKHAM®, TRIANGLE®, UNI-CHEK®, WTA®, and XOMOX®) are registered trademarks of Crane Co. All rights reserved. © Crane ChemPharma & Energy

CPE-PACIFIC-CSV-BU-EN-LT-2017_03_28

brands you trust.

TECHNICAL DATASHEET PacificÂ®CSV Cast Steel Valves

Crane ChemPharma & Energy

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Gate, Globe and Check Features and Benefits

The new Pacific®CSV valves have been redesigned to improve performance and have undergone Crane’s rigorous development and testing process. These valves exceed industry fugitive emissions standards. Each Pacific valve is uniquely built and tested per API 598 standards, delivering superior performance in the most challenging conditions. Certifications: • API 624 • API RP 591 • API 622 • CE/PED • Indian Boiler Regulation (IBR) • ISO 15848-1 • ISO 9001:2008 These valves comply with the applicable requirements of the following standards: • API 600 • API 623 • API 594 • API 598 • ASME B 16.34 • ASME B 16.10 • ASME B 16.5 • ASME B 16.25

Crane ChemPharma & Energy

Gate Valve Features include: • Fully-guided wedge ensures smooth operation in both horizontal and vertical orientations to deliver improved resistance to sticking. • Modular stuffing box facilitates changeover for low fugitive emissions and monitoring port options. • Live loading option extends fugitive emissions performance by eliminating the need for manual packing adjustment. Globe Valve Features include: • Uniquely designed line contact between disc and seat results in lower seating torque, permitting faster set up. • The guided disc option facilitates seating during turbulent flow conditions. • Integral ISO 5210 mounting is available in larger sizes for ease of actuation. Swing Check Valve Features include: • Disc fastener is restrained by the bonnet to eliminate the risk of a displaced disc and prevent damage to downstream equipment. • Internal hung disc pin arrangement eliminates leak path from pressure boundary. • Modular design enables easy change to an optional external pin arrangement if counterweights are required.

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Gate Valve Materials of Construction Item

Description

Carbon Steel

Body

ASTM A216. WCB

Seat Ring

ASTM A106 Gr. B, w/ AWS 5.13 CrCo

Disc

ASTM A216, WCB W/ AWS 5.9 ER410

Stem

ASTM 182. F6a

Gasket

Class 150: AISI 1010 Corr. Class 300: Spiral Wound SS Class 600: Ring Type

Bonnet

ASTM A216, WCB

Nut

ASTM A194, 2H

Stud

ASTM A193, B7

Backseat Bushing

ASTM A276, T410

Spacer

ASTM A276, T410

Packing

Graphite: 2 braided; 3 Die-Formed

Packing Gland

ASTM A276, T410

Grease Fitting

Steel

Handwheel Nut

ASTM A536, Gr.65-45-12

Zinc Plated Steel

Eye Bolt

ASTM A 194 2H

Gland Flange

ASTM A216 WCB

Packing Nuts

ASTM 307 Zinc Plated

Stem Nut

ASTM A439 Gr. D2

Retainer Nut

ASTM A536 Gr. 65-45-12

Handwheel

Carbon Steel/Ductile Iron

13 20 19 18

17 16

11 10 9

6 5

3 2 1

Standard construction WCB-Trim 8. Other options are available per Materials of Construction on page 14.

Figure A1- Class 150 Figure A3- Class 300 Figure A6- Class 600

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Crane ChemPharma & Energy

Gate Valve Dimensions and Weights CLASS 150, 300 & 600 Valve Pressure L H H NB Class (Open) (Close) FE WE in (mm) 150 7 8.5 17 14 2" (50) 300 8.5 8.5 18 15 600 11.5 11.5 18.7 16 150 7.5 9.5 17 14 2.5" (65) 300 9.5 9.5 18 15 600 13 13 20 17 150 8 11.12 20 16 3" (80) 300 11.12 11.12 21 17 600 14 14 24 20 150 9 12 24 20 4" (100) 300 12 12 25 20 600 17 17 28 23 150 10.5 15.88 31 25 6" (150) 300 15.88 15.88 33 26 600 22 22 36 29 150 11.5 16.5 39 30 16.5 16.5 41 32 8" (200) 300 600 26 26 43 35 150 13 18 46 36 10" (250) 300 18 18 50 39 600 31 31 54 43 150 14 19.75 55 42 12" (300) 300 19.75 19.75 57 44 600 33 33 62 48

M 8 8 8 8 8 9 9 9 10 10 10 14 14 14 18 14 16 20 16 18 GO 18 20 GO

Weight (lbs.) FE

47 64 85 56 73 118 75 110 138 106 165 250 185 310 584 278 481 936 411 737 1502 622 1036 2043

42 55 72 48 59 98 66 91 113 97 136 197 179 256 472 263 400 793 396 614 1235 593 895 1740

Valve Pressure NB Class in (mm) 150 14" (350) 300 600 150 16" (400) 300 600 150 18" (450) 300 600 150 20" (500) 300 600 150 24" (600) 300 600

L FE

15 30 35 16 33 39 17 36 43 18 39 47 20 45 55

22.5 30 35 24 33 39 26 36 43 28 39 47 32 45 55

H H (Open) (Close) 62 65 65 70 73 79 76 80 84 86 90 93 99 101 110

48 51 51 54.41 56 63 58 62 66 66 70 72 75 77 86

M GO GO GO GO GO GO GO GO GO GO GO GO GO GO GO

Weight (lbs.) FE

842 1595 2618 1094 2040 3715 1389 2638 4490 1654 3564 6213 2396 5338 9385

816 1340 2285 1032 1813 3245 1418 2252 3911 1601 3089 5476 2334 4625 8342

FE: Flanged End Valve WE: Buttweld End Valve H (open): Valve center to Stem top in Valve open condition H (close): Valve center to Stem top in Valve close condition L: Face to Face dimension M: Handwheel Diameter GO: Gear Operator

Figure A1- Class 150 Figure A3- Class 300 Figure A6- Class 600

SECTION J-J

Crane ChemPharma & Energy

SECTION H-H

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Globe Valve Materials of Construction Item

Description

Carbon Steel

Body

ASTM A216. WCB

Seat Ring

Disc

Thrust Plate

ASTM A216. WCB

Stem

ASTM 182. F6a

Disc Nut

ASTM A276. T410

Gasket

Class 150: AISI 1010 Corr. Class 300: Spiral Wound SS Class 600: Ring Type

Bonnet

ASTM A216, WCB

Backseat

ASTM A276, T410

Packing Spacer

ASTM A276, T410

Packing

Graphite: 2 braided; 3 Die-Formed

Gland

ASTM A276, T410

Gland Flange

ASTM A216, WCB

Zinc Plated Steel

Eye Bolt

ASTM A307 Gr. A or Gr. B, Zinc Plt.

Nut

ASTM A194, 2H

Stud

ASTM A193, B7

Handwheel

Carbon Steel/Ductile Iron

Yoke Sleeve

ASTM A439, Gr. D2

Handwheel Nut

ASTM A194, 2H

Eyebolt Nut

ASTM A196 Gr. 24

A105 w/AWS 5.13 CrCo or WCB w/AWS 5.13 CrCo ASTM A216. GR WCB. w/AWS 5.9 ER 410 Figure B1- Class 150 Figure B3- Class 300 Figure B6- Class 600

18 21

10 16 7

5 6

SECTION A-A SCALE 1 : 1.4

Standard construction WCB-Trim 8. Other options are available per Materials of construction on page 14.

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Crane ChemPharma & Energy

Globe Valve Dimensions and Weights CLASS 150, 300 & 600 Valve NB Pressure in (mm) Class 2" (50)

2.5" (65)

3" (80)

4" (100)

6" (150)

8" (200)

150 300 600 150 300 600 150 300 600 150 300 600 150 300 600 150 300 600

L FE

8 10.5 11.5 8.5 11.5 13 9.5 12.5 14 11.5 14 17 16 17.5 22 19.5 22 26

H H (Open) (Close) 16 16 16.7 16.5 18 19.3 18 18 21 22 23 26 22 28 33 27 31 39

15 15 15.7 15.5 16.5 18 17 16.5 20 20.5 21 24.5 21 25 30.6 23 27 36

Weight (lbs.) Valve NB Pressure FE WE in (mm) Class

8 8 8 8 8 10 10 10 10 10 10 16 14 18 20 16 20 26

50 57 93 71 86 130 88 107 185 133 178 311 196 350 728 330 561 1269

45 49 80 54 72 107 74 88 164 116 146 256 172 299 618 295 488 1114

L FE

H H WE (Open) (Close)

Weight (lbs.) FE

14" (350)

150 300 600 150 300 600 150 300

24.5 24.5 24.5 24.5 31 31 27.5 27.5 28 28 33 33 31 31 33 33

29 36 45 34 41.4 56 40.6 47.4

25 31.4 41 28.5 36 50 36.7 41.7

GO 23.6 GO GO 23.6 GO GO GO

505 825 1610 724 1184 2264 1115 1739

453 720 1340 643 1015 1966 990 1485

16" (400)

150 300

36 34

43.6 59

38.4 51

GO GO

1399 2386

1250 2113

18" (450)

150 300

38.5 38.5 38.5 38.5

45 60.4

39 54

GO GO

1724 3105

1584 2740

10" (250)

12" (300)

Figure B1- Class 150 Figure B3- Class 300 Figure B6- Class 600

L G

Crane ChemPharma & Energy SECTION F-F

SECTION G-G

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Swing Check Materials of Construction Item

Description

Carbon Steel

Body

Seat Ring

Disc

4 5 6 7 8 9

Hinge Washer Disc Nut Hinge Pin Hinge Bracket Cap Screw

Gasket

11 12 13 14

Cap Cap Studs Cap Nuts Eye Bolt

ASTM A216. WCB ASTM A106 Gr. B, w/ AWS 5.13 CrCo [350 - 400 HB] ASTM A216. GR WCB. w/AWS 5.9 ER 410 ASTM A216 WCB ASTM A276, T410 ASTM A194, Gr. 2H ASTM A276, T410 ASTM A216, WCB ASTM A193, B7 Class 150: AISI 1010 Corr. Class 300: Spiral Wound Class 600: Ring Type ASTM A216, WCB ASTM A194, Gr. 2H ASTM A 193, B7 ASTM A 108 C1030

Standard construction WCB-Trim 8. Other options are available per Materials of construction on page 14.

9 8 7 6 14

12 13 11 10

5 4 3 2

Figure C1- Class 150 Figure C3- Class 300 Figure C6- Class 600

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Crane ChemPharma & Energy

Swing Check Dimensions and Weights CLASS 150, 300 & 600 Valve NB in (mm) 2" (50)

2.5" (65)

3" (80) 4" (100) 6" (150)

8" (200)

10" (250)

12" (300)

Pressure Class 150 300 600 150 300 600 150 300 600 150 300 600 150 300 600 150 300 600 150 300 600 150 300 600

L FE/ WE

8 10.5 11.5 8.5 11.5 13 9.5 12.5 14 11.5 14 17 16 17.5 22 19.5 21 26 24.5 24.5 31 27.5 28 33

6 6 7 6 7 8 7 7 8 8 12 12 12 14 15 14 15 18 16 18 21 18 20 24

32 43 71 45 66 100 62 87 101 92 132 211 148 267 475 273 438 801 401 633 1173 593 898 1677

25 33 57 34 52 80 47 68 82 75 101 153 124 215 364 233 355 656 351 515 922 512 728 1390

Valve NB in (mm) 14" (350)

16" (400)

18" (450) 20" (500) 24" (600)

Pressure Class

150 300 600 150 300 600 150 300 600 150 300 600 150 300 600

FE/ WE

31 33 35 36 34 39 38.5 38.5 43 38.5 40 47 51 53 55

22 22 25 25 25 29 25 27 35 25 27 35 25 27 40

866 1385 2228 1138 1625 2919 1560 2212 3820 1770 2831 4776 2455 4171 7661

741 1131 1896 981 1351 2449 1419 1808 3240 1551 2376 4038 2154 3461 6620

FE: Flanged End Valve WE: Buttweld End Valve H: Valve center to valve cap highest point L: Face to Face dimension

Figure C1- Class 150 Figure C3- Class 300 Figure C6- Class 600

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Crane ChemPharma & Energy SECTION E-E

Weight (lbs.)

H (Open)

Weight (lbs.)

H (Open)

SECTION F-F

Gate Valve Cv and Torque

655

757

655

728

630

1374

1188

1345

1163

1334

1154

3162

2735

3162

2735

3084

2668

5790

5008

5705

4935

5527

4781

9287

8034

9251

8002

8797

7610

13321

11523

13321

11523

12776

11052

16241

14049

16241

14049

15332

13263

22398

19375

22409

19385

20953

18126

28657

24790

27826

24071

26213

22676

35686

30870

34758

30068

32075

27747

54371

47033

53199

46019

48673

42105

75335

65169

2.5

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Torque (ft-lbs.)

757

Handwheel Diameter (in)

Number of Turns

425

Stem Travel (in)

265

491

Thread Pitch Radius (in)

306

445

Thread Lead (in)

281

515

Stem Diameter (in)

325

445

Differential Pressure (psi)

281

515

Size

324

Class 300

Class 150

Size 2 2.5

Pressure Class

Gate Valves - Torque Class 600

Gate Valves - Cv

150 300 600 150 300 600 150 300 600 150 300 600 150 300 600 150 300 600 150 300 600 150 300 600 150 300 600 150 300 600 150 300 600 150 300 600 150 300 600

325 825 1650 325 825 1650 325 825 1650 325 825 1650 325 825 1650 325 825 1650 325 825 1650 325 825 1650 325 825 1650 325 825 1650 325 825 1650 325 825 1650 325 825 1650

0.75 0.75 0.75 0.75 0.75 0.875 0.875 0.875 1 1 1 1.125 1.125 1.25 1.5 1.25 1.375 1.625 1.375 1.5 1.875 1.5 1.625 2 1.625 1.75 2.25 1.75 1.875 2.375 1.875 2 2.5 2 2.25 2.75 2.25 2.5 3

0.1667 0.1667 0.1667 0.1667 0.1667 0.1667 0.1667 0.1667 0.2 0.2 0.2 0.2 0.2 0.2 0.25 0.2 0.2 0.25 0.25 0.25 0.25 0.25 0.25 0.25 0.25 0.25 0.3333 0.25 0.25 0.3333 0.25 0.25 0.3333 0.25 0.3333 0.3333 0.3333 0.3333 0.5

0.3333 0.3333 0.3333 0.3333 0.3333 0.3958 0.3958 0.3958 0.45 0.45 0.45 0.5125 0.5125 0.575 0.6875 0.575 0.6375 0.75 0.625 0.6875 0.875 0.6875 0.75 0.9375 0.75 0.8125 1.0417 0.8125 0.875 1.0417 0.875 0.9375 1.1667 0.9375 1.0417 1.2917 1.0417 1.1667 1.375

2.4 3.2 2.7 2.9 3 3.1 3.4 3.9 3.7 4.5 5 4.6 6.6 6.6 6.4 8.3 8.3 8.2 10.5 10.6 11.2 12.7 12.4 13.1 13.7 14 13.9 16.1 17.1 15.9 18.3 17.8 18.1 20 20.3 21.1 24.1 23.9 23.3

14.5 19.2 16.1 17.1 18 18.7 20.4 23.3 18.5 22.4 25.1 23.2 32.8 33.2 25.6 41.8 33.3 32.9 41.6 42.3 44.7 50.5 49.6 52.4 54.9 56 41.7 64 68.4 47.7 73.4 71.2 54.4 80 61.2 63.2 72.2 71.8 46.7

8 8 8 8 8 9 9 9 10 10 10 14 14 14 18 14 16 20 16 18 GO 18 20 GO GO GO GO GO GO GO GO GO GO GO GO GO GO GO GO

6 11 18 7 13 29 10 20 46 18 37 80 35 89 219 61 159 373 103 268 628 154 402 932 198 517 1302 273 715 1756 365 957 2265 475 1381 2993 793 2171 4961

Crane ChemPharma & Energy

Globe & Swing Check Valve Cv and Torque

2.5

111

206

178

206

178

206

178

479

415

479

415

479

415

873

756

873

756

873

756

1419

1227

1419

1227

1353

1170

2046

1770

1650

1427

1960

1695

2491

2155

2490

2154

3435

2971

3435

2971

4402

3808

4268

3692

2 2.5 3 4 6

Swing Check Valve - Cv Size

Class 150

Class 300

Class 600

123

107

123

107

122

106

2.5

197

170

197

170

197

170

291

252

291

252

291

252

538

465

538

465

538

465

1240

1073

1240

1073

1240

1073

2278

1970

2278

1970

2211

1912

3700

3201

3700

3201

3519

3044

5335

4615

5335

4615

5110

4421

6498

5621

6496

5620

6133

5305

8964

7754

8964

7754

8381

7250

11463

9916

11141

9637

10485

9070

14274

12348

13903

12027

12830

11099

21748

18813

21272

18401

19469

16842

Crane ChemPharma & Energy

150 300 600 150 2.5 600 150 300 600 150 4 600 150 300 600 150 8

325 825 1650 325 825 1650 325 825 1650 325 825 1650 325 825 1650 325 825

0.75 0.75 0.75 0.75 0.75 0.875 0.875 0.875 1 1 1 1.125 1.125 1.25 1.5 1.25 1.375

0.166 0.166 0.166 0.166 0.166 0.166 0.166 0.166 0.2 0.2 0.2 0.2 0.2 0.2 0.25 0.2 0.2

.0.33 0.33 0.33 0.33 0.33 0.39 0.39 0.39 0.45 0.45 0.45 0.51 0.51 0.575 0.687 0.575 0.637

2.4 3.2 2.7 2.9 3 3.1 3.4 3.9 3.7 4.5 5 4.6 6.6 6.6 6.4 8.3 8.3

14.5 19.2 16.1 17.1 18 18.7 20.4 23.3 18.5 22.4 25.1 23.2 32.8 33.2 25.6 41.8 33.3

8 8 8 8 8 9 9 9 10 10 10 14 14 14 18 14 16

6 11 18 7 13 29 10 20 46 18 37 80 35 89 219 61 167

600

1650

1.625

0.25

0.75

8.2

32.9

373

150 300 600 150 12 600 150 300 600 150 16 600 150 300 600 150 20 600 150 300

325 825 1650 325 825 1650 325 825 1650 325 825 1650 325 825 1650 325 825 1650 325 825 1650

1.375 1.5 1.875 1.5 1.625 2 1.625 1.75 2.25 1.75 1.875 2.375 1.875 2 2.5 2 2.25 2.75 2.25 2.5 3

0.25 0.25 0.25 0.25 0.25 0.25 0.25 0.25 0.33 0.25 0.25 0.33 0.25 0.25 0.33 0.25 0.33 0.33 0.3333 0.3333 0.5

0.625 0.687 0.875 0.687 0.75 0.937 0.75 0.812 1.042 0.812 0.875 1.042 0.875 0.937 1.166 0.937 1.042 1.292 1.0417 1.1667 1.375

10.5 10.6 11.2 12.7 12.4 13.1 13.7 14 13.9 16.1 17.1 15.9 18.3 17.8 18.1 20 20.3 21.1 24.1 23.9 23.3

41.6 42.3 44.7 50.5 49.6 52.4 54.9 56 41.7 64 68.4 47.7 73.4 71.2 54.4 80 61.2 63.2 72.2 71.8 46.7

16 18 GO 18 20 GO GO GO GO GO GO GO GO GO GO GO GO GO GO GO GO

103 268 628 154 402 932 198 517 1302 273 715 1848 365 957 2265 475 1381 2993 793 2171 5736

Torque (ft-

lbs.)

Handwheel Diameter (in)

Number of Turns

Stem Travel (in)

Thread Pitch Radius (in)

Thread Lead (in)

Class 600

Stem Diameter (in)

Class 300

Differential Pressure (psi)

Class 150 Cv

Size (in.)

Size

Globe Valves - Torque Pressure Class

Globe Valves - Cv

www.cranecpe.com

Pressure / Temperature Range The following pressure-temperature charts are derived from ASME B16.34 – 2013 Version. They will cover the most commonly used body and bonnet materials in the industry. All Crane Valves are designed to operate through the pressure and temperature ranges shown in these charts for a particular ASME Class Rating and ASTM Material.

ASTM A216 GR WCB

°F -20 to 100 200 300 400 500 600 650 700 750 800

150 285 260 230 200 170 140 125 110 95 80

STANDARD CLASS B16.34 - 2013 MAXIMUM NON-SHOCK WORKING PRESSURE, PSIG 300 600 900 1500 740 1480 2220 3705 680 1360 2035 3395 655 1310 1965 3270 635 1265 1900 3170 605 1205 1810 3015 570 1135 1705 2840 550 1100 1650 2745 530 1060 1590 2665 505 1015 1520 2535 410 825 1235 2055

2500 6170 5655 5450 5280 5025 4730 4575 4425 4230 3430

150 290 290 285 280 280 280 275 265 245 195

SPECIAL CLASS B16.34 - 2013 MAXIMUM NON-SHOCK WORKING PRESSURE, PSIG 300 600 900 1500 750 1500 2250 3750 750 1500 2250 3750 740 1480 2220 3700 735 1465 2200 3665 735 1465 2200 3665 735 1465 2200 3665 715 1430 2145 3575 690 1380 2075 3455 635 1270 1905 3170 515 1030 1545 2570

2500 6250 6250 6170 6105 6105 6105 5960 5760 5285 4285

NOTE: Upon prolonged exposure to temperatures above 800°F (426°C), the carbide phase of steel may be converted to graphite. Permissible, but not recommended for prolonged use above 800°F (426°C).

ASTM A352 GR LCB

°F -20 to 100 200 300 400 500 600 650

150 265 255 230 200 170 140 125

STANDARD CLASS B16.34 - 2013 MAXIMUM NON-SHOCK WORKING PRESSURE, PSIG 300 600 900 1500 695 1395 2090 3480 660 1320 1980 3300 640 1275 1915 3190 615 1230 1845 3075 585 1175 1760 2930 550 1105 1655 2755 535 1065 1600 2665

2500 5805 5505 5315 5125 4885 4595 4440

150 290 290 290 290 290 290 290

SPECIAL CLASS B16.34 - 2013 MAXIMUM NON-SHOCK WORKING PRESSURE, PSIG 300 600 900 1500 695 1395 2090 3480 695 1395 2090 3480 695 1395 2090 3480 695 1395 2090 3480 695 1395 2090 3480 695 1395 2090 3480 695 1390 2080 3470

2500 5805 5805 5805 5805 5805 5805 5780

150 290 290 290 290 290 290 290

2500 6250 6250 6250 6250 6250 6250 6250

NOTE: Not to be used over 650°F (343°C).

ASTM A352 GR LCC & LC3

°F -20 to 100 200 300 400 500 600 650

150 290 260 230 200 170 140 125

STANDARD CLASS B16.34 - 2013 MAXIMUM NON-SHOCK WORKING PRESSURE, PSIG 300 600 900 1500 750 1500 2250 3750 750 1500 2250 3750 730 1455 2185 3640 705 1405 2110 3520 665 1330 1995 3325 605 1210 1815 3025 590 1175 1765 2940

2500 6250 6250 6070 5865 5540 5040 4905

NOTE: Not to be used over 650°F (343°C).

* “Special Class” applies to weld-end valves only and requires NDE testing in accordance with ASME B16.34 - 2013. www.cranecpe.com

Crane ChemPharma & Energy

Pressure / Temperature Range ASTM A217 GR WC6

°F -20 to 100 200 300 400 500 600 650 700 750 800 850 900 950 1000 1050 1100

150 290 260 230 200 170 140 125 110 95 80 65 50 35 20 20(a) 20(a)

STANDARD CLASS B16.34 - 2013 MAXIMUM NON-SHOCK WORKING PRESSURE, PSIG 300 600 900 1500 750 1500 2250 3750 750 1500 2250 3750 720 1445 2165 3610 695 1385 2080 3465 665 1330 1995 3325 605 1210 1815 3025 590 1175 1765 2940 570 1135 1705 2840 530 1065 1595 2660 510 1015 1525 2540 485 975 1460 2435 450 900 1350 2245 320 640 955 1595 215 430 650 1080 145 290 430 720 95 190 290 480

2500 6250 6250 6015 5775 5540 5040 4905 4730 4430 4230 4060 3745 2655 1800 1200 800

150 290 290 290 290 290 290 290 280 280 275 260 225 155 105 70 45

SPECIAL CLASS B16.34 - 2013 MAXIMUM NON-SHOCK WORKING PRESSURE, PSIG 300 600 900 1500 750 1500 2250 3750 750 1500 2250 3750 750 1500 2250 3750 750 1500 2250 3750 750 1500 2250 3750 750 1500 2250 3750 750 1500 2250 3750 735 1465 2200 3665 730 1460 2185 3645 720 1440 2160 3600 680 1355 2030 3385 585 1175 1760 2935 400 795 1195 1995 270 540 810 1350 180 360 540 900 120 240 360 600

2500 6250 6250 6250 6250 6250 6250 6250 6110 6070 6000 5645 4895 3320 2250 1500 1000

NOTE: Use normalized and tempered material only. Not to be used over 1100°F (593°C). The deliberate addition of any element not listed in ASTM A217, Table 1 is prohibited, except that Ca and Mg may be added for deoxidation. (a) Flanged end valve ratings terminate at 1000°F (537°C).

ASTM A217 GR WC9

°F -20 to 100 200 300 400 500 600 650 700 750 800 850 900 950 1000 1050 1100

150 290 260 230 200 170 140 125 110 95 80 65 50 35 20 20(a) 20(a)

STANDARD CLASS B16.34 - 2013 MAXIMUM NON-SHOCK WORKING PRESSURE, PSIG 300 600 900 1500 750 1500 2250 3750 750 1500 2250 3750 730 1455 2185 3640 705 1410 2115 3530 665 1330 1995 3325 605 1210 1815 3025 590 1175 1765 2940 570 1135 1705 2840 530 1065 1595 2660 510 1015 1525 2540 485 975 1460 2435 450 900 1350 2245 385 755 1160 1930 265 535 800 1335 175 350 525 875 110 220 330 550

2500 6250 6250 6070 5880 5540 5040 4905 4730 4430 4230 4060 3745 3220 2230 14 55 915

150 290 290 285 280 280 275 275 270 270 270 260 230 180 130 85 55

SPECIAL CLASS B16.34 - 2013 MAXIMUM NON-SHOCK WORKING PRESSURE, PSIG 300 600 900 1500 750 1500 2250 3750 750 1500 2250 3750 740 1480 2220 3695 730 1455 2185 3640 725 1450 2175 3620 720 1440 2165 3605 715 1430 2145 3580 705 1415 2120 3535 705 1415 2120 3535 705 1415 2120 3535 680 1355 2030 3385 600 1200 1800 3000 470 945 1415 2360 335 670 1005 1670 220 435 655 1095 135 275 410 685

2500 6250 6250 6160 6065 6035 6010 5965 5895 5895 5895 5645 5000 3930 2785 1820 1145

Crane ChemPharma & Energy

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Pressure / Temperature Range ASTM A217 GR C5

°F -20 to 100 200 300 400 500 600 650 700 750 800 850 900 950 1000 1050 1100 1150 1200

150 290 260 230 200 170 140 125 110 95 80 65 50 35 20 20(a) 20(a) 20(a) 15(a)

STANDARD CLASS B16.34 - 2013 MAXIMUM NON-SHOCK WORKING PRESSURE, PSIG 300 600 900 1500 750 1500 2250 3750 750 1500 2250 3750 730 1445 2185 3640 705 1410 2115 3530 665 1330 1995 3325 605 1210 1815 3025 590 1175 1765 2940 570 1135 1705 2840 530 1065 1595 2660 510 1015 1525 2540 485 975 1460 2435 375 745 1120 1870 275 550 825 1370 200 400 595 995 145 290 430 720 100 200 300 495 60 125 185 310 35 70 105 170

2500 6250 6250 6070 5880 5540 5040 4905 4730 4430 4230 4060 3115 2285 1655 1200 830 515 285

150 290 290 290 290 290 290 290 280 280 275 260 230 170 125 90 60 40 20

SPECIAL CLASS B16.34 - 2013 MAXIMUM NON-SHOCK WORKING PRESSURE, PSIG 300 600 900 1500 750 1500 2250 3750 750 1500 2250 3750 750 1500 2250 3750 750 1500 2250 3750 750 1500 2250 3750 750 1500 2250 3750 750 1500 2250 3750 735 1465 2200 3665 730 1460 2185 3645 720 1440 2160 3600 615 1225 1840 3065 465 935 1400 2335 345 685 1030 1715 250 495 745 1245 180 360 540 900 125 250 375 620 75 155 230 385 45 85 130 215

2500 6250 6250 6250 6250 6250 6250 6250 6110 6070 6000 5105 3895 2855 2070 1500 1035 645 355

SPECIAL CLASS B16.34 - 2013 MAXIMUM NON-SHOCK WORKING PRESSURE, PSIG 300 600 900 1500 750 1500 2250 3750 750 1500 2250 3750 750 1500 2250 3750 750 1500 2250 3750 750 1500 2250 3750 750 1500 2250 3750 750 1500 2250 3750 735 1465 2200 3665 730 1460 2185 3645 720 1440 2160 3600 680 1355 2030 3385 600 1200 1800 3000 470 945 1415 2355 315 635 950 1585 215 430 645 1070 140 285 425 705 95 190 285 470 65 130 195 320

2500 6250 6250 6250 6250 6250 6250 6250 6110 6070 6000 5646 5000 3930 2645 1785 1180 785 535

NOTE: Use normalized and tempered material only. The deliberate addition of any element not listed in ASTM A217, Table 1 is prohibited, except that Ca and Mg may be added for deoxidation. (a) Flanged end valve ratings terminate at 1000°F (537°C).

ASTM A217 GR C12

°F -20 to 100 200 300 400 500 600 650 700 750 800 850 900 950 1000 1050 1100 1150 1200

150 290 260 230 200 170 140 125 110 95 80 65 50 35 20 20(a) 20(a) 20(a) 20(a)

STANDARD CLASS B16.34 - 2013 MAXIMUM NON-SHOCK WORKING PRESSURE, PSIG 300 600 900 1500 750 1500 2250 3750 750 1500 2250 3750 730 1455 2185 3640 705 1410 2115 3530 665 1330 1995 3325 605 1210 1815 3025 590 1175 1765 2940 570 1135 1705 2840 530 1065 1595 2660 510 1015 1525 2540 485 975 1460 2435 450 900 1350 2245 375 755 1130 1885 255 505 760 1270 170 345 515 855 115 225 340 565 75 150 225 375 50 105 155 255

2500 6250 6250 6070 5880 5540 5040 4905 4730 4430 4230 4060 3745 3145 2115 1430 945 630 430

150 290 290 290 290 290 290 290 280 280 275 260 230 180 120 80 55 35 25

* “Special Class” applies to weld-end valves only and requires NDE testing in accordance with ASME B16.34 - 2013. www.cranecpe.com

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Materials of Construction Cast steel bolted bonnet valves described in this catalog are typically manufactured of carbon steel. When specified, the valves are available in the alloys shown below which are suitable for steam, water, oil, oil vapor, gas and general services. Please contact factory or customer service for availability and material breakdowns.

Body and Bonnet or Cap Materials Part No. Suffix

ASTM Classification

Material Classification

A216 WCB

Carbon Steel

For service up to 800°F (426°C) where corrosion and oxidation are not a factor. (1) (4) (5)

A217 WC6

1 ¼ CR, ½ Mo

For service up to 1000°F (537°C). (2) (3) (4) (5)

A217 WC9

2 ¼ CR, 1 Mo

For service up to 1100°F (593°C) where good creep strength is required. (2) (3) (4) (5)

A217 C5

5% CR, ½ Mo

For service up to 1200°F (649°C). Better corrosion and oxidation resistance than other grades. (2)

A217 C12

9% CR, 1 Mo

For service up to 1200°F (649°C). Best corrosion and oxidation resistance than other grades. (2)

A352 LCB

Low Carbon Steel

A351 CF8M

Stainless Steel (316)

For services up to 1000°F (537°C), where corrosion and oxidation resistance are desired.

Stainless Steel (304)

For services up to 1000°F (537°C), where corrosion and oxidation resistance are desired, but lower costs then CF8M and slightly lower material strengths and corrosion resistance can be tolerated.

A351 CF8

Service Conditions

For service from –20°F to 650°F (-29°C to 345°C). This material must be quenched and tempered to obtain tensile and impact properties needed at subzero temperatures.

(1) Upon prolonged exposure to temperatures above 800°F (426°C), the carbide phase of carbon steel may be converted to graphite. Permissible, but not recommended for prolonged usage above 800°F (426°C). (2) Flanged end valves rated to 1000°F (537°C). (3) Considerations should be given to the possibility of excessive oxidation (scaling) when used above 1050°F (565°C). (4) Product used within the jurisdiction of Section 1 Power Boilers of the ASME Boiler and Pressure Vessel code is subject to the same temperature limitations as specified in that document. (5) Product used within the jurisdiction of Power Piping, ASME Code for Pressure Piping B31.1, is subject to the same maximum temperature limitations placed upon the material in paragraph 124.2.

Trim Material Code

API Trim No.

Nominal Trim

N/A 5 8 9 1 2 6

1 5 8* 9 11 12 16

HF / HF (2) F6 / HF (1) (2) Monel® / Monel® (4) Monel® / HF (4) (2) 316 / HF (3) (2) 316/HF / 316/HF (3) (2)

Stem Material Obsolete 13 Cr (410) 13 Cr (410) Monel Monel® 316 SS 316 SS

(1) 13% Chromium AISI Type 410 Stainless Steel. (2) Hard Facing is weld deposited Cobalt base alloy. (3) Austenitic Stainless Steel is a Ni-Cr-Mo stainless steel in the AISI Type 316 category. (4) Ni-Cu Alloy. * Standard offering

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End

Operator

Trim

Class

Type

Size

Material

ORDERING INFORMATION

® 12 A 1 A 8 H G PACIFIC API-600 CAST STEEL VALVES How To Order

SIZE 1

02 3 6 2H

CLASS

TYPE

A217 C5 A217 C12 A352 LCC A352 LCB 150# A351 CF8M A351 CF8 300# A351 CF3 600#

Material Classification Carbon Steel 1 ¼ CR, ½ Mo 2 ¼ CR, 1 Mo 5% CR, ½ Mo 9% CR, 1 Mo Low Carbon Steel Low Carbon Steel Stainless Steel (316) Stainless Steel (304) Stainless Steel (304L)

TRIM MATERIAL

MATERIAL API Trim No. No.

A B C D E F

Nominal Trim

GATE GLOBE CHECK GATE with CE/PED GLOBE with CE/PED CHECK with CE/PED

N/A (e.g. check valves) TRIM MATERIAL Handwheel

API Trim No. Bevel Gear

02 2H 03 04 … 18 20 24

1 3 6

VALVE ENDS

Nominal Trim

SIZE

CLASS

Seating Surfaces

OPERATOR No.

Stem Material

No. Material Classification N/A 1ASTM Obsolete (2) A216 Carbon Steel 5A 5 WCB HF / HF Alloy 6 13 Cr (410) (4) Monel® 9D 9 WC6 Monel® / 1Monel® Monel® A217 ¼ CR, ½ Mo (1) (2) 8E 8* WC9 F6 / HF 13 Cr (410) A217 2 ¼ CR, 1 Mo 13 Cr / Alloy 6 (4) (2) Monel® /5% HFCR, Monel® 1F 11 A217 C5 ½ Mo Monel® / Alloy 6 (3) (2) 2G 12 C12 316 / HF 316 SS A217 9% CR, 1 Mo 316SS / Alloy 6 (3) (2) 6? 16 LCC 316/HF /Low 316/HF 316SS / Alloy 6 (both) 316 SS A352 Carbon Steel EB 8 to A352 NACELCB MR0103 Low Carbon Steel N 12 to NACE MR0103 A351 CF8M Stainless Steel (316) H (1) 13% Chromium AISI Type 410 Stainless Steel. (3) Ni-Cr-Mo stainless steel in the AISI Type 316 category. A351 CF8 SteelAlloy. (304) K (2) Hard Facing is weld deposited Cobalt baseStainless alloy. (4) Ni-Cu * Standard Offering A351 CF3 Stainless Steel (304L) L

0 H G S P E

End

Operator

ORDERING INFORMATION

F W R

No.

Raised Face Butt Weld End Seating Surfaces Ring Type Joint

(4) Ni-Cu Alloy.

* Standard Offering H

A B C D E F

GATE GLO CHE GATE GLO CHE

150# 300# 600#

ASTM A216 WCB A217 WC6 A217 WC9 A217 C5 A217 C12 A352 LCC A352 LCB A351 CF8M A351 CF8 A351 CF3

API Trim No.

Material Classification Carbon Steel 1 ¼ CR, ½ Mo 2 ¼ CR, 1 Mo 5% CR, ½ Mo 9% CR, 1 Mo Low Carbon Steel Low Carbon Steel Stainless Steel (316) Stainless Steel (304) Stainless Steel (304L)

Nominal Trim

1 O (2) 5 HF / HF Monel® / Monel® (4) 9 (1) (2) 8* F6 / HF 1 (4) (2) Monel® / HF M 11 12 316 / HF (3) (2) 3 (3) (2) 16 316/HF / 316/HF 316S 8 to NACE MR0103 12 to NACE MR0103

N/A Bare Stem 1 Obsolete Pneumatic 5 Cylinder 5 HF / HF (2) Alloy 6 (4) Electric Motor Monel® / Monel® Monel® 9 9 8 8* F6 / HF (1) (2) 13 Cr / Alloy 6 (4) (2) Monel® / HF Monel® / Alloy 6 1 11 (1) SS 13% Chromium AISI Type 410 Stainless Steel. 2 12 316 / HF (3) (2) 316SS / Alloy 6 316 (2) Hard Facing is weld deposited Cobalt base alloy. (3) (2) 6 16 316/HF / 316/HF 316SS / Alloy 6 (both) 316 SS E 8 to NACE MR0103 N 12 to NACE MR0103 OPERATOR (1) 13% Chromium AISI Type 410 Stainless Steel. (3) Ni-Cr-Mo stainless steel in the AISI Type 316 category. & valves) Energy www.cranecpe.com 0 Crane ChemPharma N/A (e.g. check (2) Hard Facing is weld deposited Cobalt base alloy.

TYPE

18" 20" 24"

TRIM MATERIAL N/A 5 9 Stem Material 8 1 13 Cr (410) 2 Monel® 6 13 Cr (410) E Monel® N

2" 2.5" 3" 4"

MATERIAL No. A D E F G ? B H K L

Material

PACIFIC API-600 CAST

Class

150# 2" 300# 600# 2.5"

03 3" 04 4" MATERIAL … No. 18 18"ASTM A216 WCB A 20 20" A217 WC6 D 24 24" A217 WC9 E F G ? B H1 K3 L6

GATE GLOBE CHECK GATE with CE/PED GLOBE with CE/PED CHECK with CE/PED

Type

A B C D E F

Class

Type

Size

18" 20" 24"12

TYPE

Size

CLASS

2" 2.5" 3" 4"

Trim

ORDERING INFORMATION 02 2H 03 04 … 18 20 24

Material

SIZE

Handwheel Bevel Gear

(3) Ni-Cr-Mo stain (4) Ni-Cu Alloy.

Crane ChemPharma & Energy Crane Energy Headquarters 4526 Research Forest Drive, Suite 400 The Woodlands, Texas 77381 U.S.A Phone: +1 936-271-6500 Fax +1 936-271-6510 www.cranecpe.com

Pacific Valves Customer Service 3201 Walnut Avenue Signal Hill, CA 90755 U.S.A Phone: +1 562-426-2531 Fax +1 562-595-9717

Crane Cast Steel Customer Service 2129 3rd Avenue, S.E. Cullman, Alabama 35055 U.S.A Phone: +1 256-775-3800 Fax: +1 256-775-3860

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Crane Co., and its subsidiaries cannot accept responsibility for possible errors in catalogues, brochures, other printed materials, and website information. Crane Co. reserves the right to alter its products without notice, including products already on order provided that such alteration can be made without changes being necessary in specifications already agreed. All trademarks in this material are property of the Crane Co. or its subsidiaries. The Crane and Crane brands logotype, in alphabetical order, (ALOYCO®, CENTER LINE®, COMPAC-NOZ®, CRANE®, DEPA®, DUO-CHEK®, ELRO®, FLOWSEAL®, JENKINS®, KROMBACH®, NOZ-CHEK®, PACIFIC VALVES®, RESISTOFLEX®, REVO®, SAUNDERS®, STOCKHAM®, TRIANGLE®, UNI-CHEK®, WTA®, and XOMOX®) are registered trademarks of Crane Co. All rights reserved. © Crane ChemPharma & Energy

CPE-PACIFIC-GGC-TDS-EN-LT-2017_03_28

NEW! Pacific®CSV Cast Steel Valves

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For the heart of your plant, don’t settle for anything less than Crane's Pacific Valves®. The new Pacific®CSV valves have undergone Crane’s rigorous development and testing process. Each Pacific® valve is uniquely built and tested per the latest standards, delivering superior performance in the most challenging conditions. Designed in accordance with the industry’s latest fugitive emissions standards, each of the products in the new Pacific®CSV portfolio meets API 624 compliance standards, offering the highest level of quality and performance. Our world-class manufacturing and traceability processes from the pour to delivery of assembled valves, provide the highest quality assurance established to meet or exceed our customers' requirements. The Pacific® Cast Steel Valves have been type tested to the latest industry fugitive emissions standards.

Designed and tested in accordance with API 624, 600, 623, 622, and ASME B16.34. Available in special alloys and stainless steel.

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Pacific®CSV Cast Steel Valves

Globe Valve features include:

Gate Valve features include:

Swing Check features include:

Fully-guided wedge ensures smooth operation in both horizontal and vertical orientations to deliver improved resistance to sticking.

Uniquely designed line contact between disc and seat results in lower seating torque, permitting faster set up.

Disc fastener is restrained by the bonnet to eliminate the risk of a displaced disc and prevent damage to downstream equipment.

Modular stuffing box facilitates changeover for low fugitive emissions and monitoring port options.

The guided disc option facilitates seating during turbulent flow conditions.

Internal hung disc pin arrangement eliminates leak path from pressure boundary.

Live loading option extends fugitive emissions performance by eliminating the need for manual packing adjustment.

Integral ISO 5210 mounting is available in larger sizes for ease of actuation.

Modular design enables easy change to an optional external pin arrangement if counterweights are required.

Configurations & Sizes Valve Type

ANSI Pressure Class 150

Gate

300 600 150

Globe

300 600 150

Swing Check

300 600

IN.

10"

12"

14"

16"

18"

20"

24"

100

150

200

250

300

350

400

450

500

600

• • • • • • • • •

• • • • • • • •

• • •

Materials & Trims • Available in WCB, LCC, CF8M, CF8 and alloys • Available in all API trims

Standards • API-600, API 623, API 594 • ASME B16.34, B16.5, B16.10, B16.25 • ISO 5210 Top Mounting flange available • API 624, ISO 15848-1

For inquires contact your Crane representative or pvsales@cranecpe.com 3201 Walnut Ave. Signal Hill, CA 90755, U.S.A Tel.: 1 (562) 426-2531 Fax: 1 (562) 304-1650 www.cranecpe.com

Crane ChemPharma & Energy, PACIFIC® Crane Co., and its subsidiaries cannot accept responsibility for possible errors in catalogues, brochures, other printed materials, and website information. Crane Co. reserves the right to alter its products without notice, including products already on order provided that such alteration can be made without changes being necessary in specifications already agreed. All trademarks in this material are property of the Crane Co. or its subsidiaries. The Crane and Crane brands logotype, in alphabetical order, (ALOYCO®, CENTER LINE®, COMPAC-NOZ®, CRANE®, DEPA®, DUO-CHEK®, ELRO®, FLOWSEAL®, JENKINS®, KROMBACH®, NOZ-CHEK®, PACIFIC VALVES®, RESISTOFLEX®, REVO®, SAUNDERS®, STOCKHAM®, TRIANGLE®, UNI-CHEK®, WTA®, and XOMOX®) are registered trademarks of Crane Co. All rights reserved. [Myraid-Roman-6.84]

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Installation, Operation and Maintenance Manual PacificÂŽCSV Cast Steel Valves

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Table of Contents

Section A - Warnings and General Valve Operation & Maintenance........................................4 Section B - Bolted Bonnet Gate Valves.........................................................................................................12 Section C - Bolted Bonnet Globe/Stop Check Valves.........................................................................16 Section D - Bolted Bonnet Swing Check Valves.....................................................................................20 Section E - Bolting Torques..................................................................................................................................24 Section F - Long Term Storage..........................................................................................................................28 Section G - Valve Installation...............................................................................................................................30 Section H - Packing & Gasket Maintenance & Valve Lubrication.................................................34 Section I - Fitting Gate Valves.............................................................................................................................38 Section J - Gear and Motor Actuators...........................................................................................................40

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Warnings 1. All Pacific® Valves are designed and manufactured to be installed in applications where no more than 1g of force in excess of gravity is applied to the valve in any direction. This 1g force can be an effect of Traffic, Wind or Earthquake. Pacific® valves should not be used in applications that exceed 1g.

6. When operating any valve stand clear of any moving parts such as the stem and/or disc assembly.

2. All piping system components are subject to certain levels of erosion and corrosion. As the valve wall thickness is the governing variable in overall service life,care should be taken to ensure that all valves and related piping components are of a suitable wall thickness for the given application. Periodic inspections should also be made as valves/components may wear over time.As a minimum, annual inspection of the Body and Bonnet wall thickness should be performed with calibrated measuring devices such as micrometers and/or ultrasonic thickness gauges. Severe applications may require additional inspection types and/or frequency. Additionally, valves should be inspected for general signs of component wear and/ or damage caused by process media, i.e. steam cutting. This may include the removal of insulation and/or other coverings to ensure a proper inspection. All valves should also be cycled completely during these inspections to ensure proper operability. Care should be taken to ensure that this will not affect the operating system.

8. Motor operated valves should be left in their factory set condition, unless the system operating parameters dictate a change.If changes are necessary,they should be performed in small increments and then the valve operation inspected. When adjusting these settings, use only the lightest/lowest setting possible to achieve the desired performance. Excess torque and/or thrust in the motor settings, may damage or lockup the valve. Never remove a motor operator, gear operator or manual operating assembly from a valve while it is pressurized. The valve must be completely relieved of all pressure prior to this disassembly.

3. All Pacific® valves are designed for operation in clean media. This media should be free of all debris and particulate matter. Debris in the media may cause damage and/or reduced performance to the valve. 4. The style, size, pressure class and material selection of all valves are the responsibility of the piping system designer. Pacific® may offer suggestions in this area, however the selection process is solely the responsibility of plant designers. Plant designers should also take into account the specific effects that the process media will have on the valve wall thickness and corresponding service life and ensure that the selected material is compatible with the process media. It is the responsibility of the piping designer to ensure that valves are equipped with any necessary venting and/or draining capabilities. 5. Do not exceed 100% of the maximum pressure rating of the valve at any time during its operation. Pressure spikes beyond the valve’s pressure rating are solely the responsibility of the user.

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7. All manually operated Pacific® valves are designed to be tightened by hand only. Do not apply excessive input torque via pipe wrenches“cheater bars”or other devices.

9. Care should be taken to ensure that electrical motors are wired correctly to the power source. Incorrect phasing of 3-phase wiring may cause valve/motor damage. 10. The operator of any valve should have an understanding of the effects of opening/closing the valve with regards to its role in the overall piping system. Operators of valves under pressure should take caution to ensure that the valve is in good operating condition prior to operating it under pressure. 11. Certain valve applications take place at elevated temperatures. Care should be taken in these instances to ensure that an operator does not touch any portion of the valve other than the handwheel. In severe temperature applications (300°F and above), insulation may be required on the valves to protect operators from the heat. 12. Certain processes utilize flammable, caustic and/or otherwise unstable media. Care should be taken in these circumstances to ensure the operator is aware of the specific health and safety risks associated with that medium. 13. All Pacific® valves should be operated within the pressure and temperature ranges listed in Table 2 of ASME B16.34. Under no circumstances should the valves be operated at conditions outside these tables.All piping systems should contain independent support mechanisms and should not utilize the valve as a sole means of support.

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Warnings 14. The estimated total lifespan of a PacificÂŽ valve when installed within ideal boundary conditions is 20 years, however, this lifespan may vary widely dependent upon operating conditions. 15. All valve actuators shall be sized by referring to the specific relevant valve torque and thrust data published by PacificÂŽ. Generic or standard valve information shall not be used. 16. It is the ultimate responsibility of the piping designer to ensure that each valve is sized appropriately for the given system parameters of pressure, temperature, flow rate, velocity, pressure drop, etc. and that the proper trim is specified for the system design parameters. Additionally it is the responsibility of the piping designer to ensure that the corresponding actuator sizing data is correct for the given application. 17. Valves other than globes should not be used for throttling applications. Severe damage may occur to other valve styles. When using globe valves for throttling, do not operate the valve continuously at less than 10% open. 18. All valves shall only be used within their defined boundary conditions. All standard materials of construction, including bolting are suitable for operation within the boundary conditions listed in Section 8.0 of this document. Care should be taken to ensure that all valves are not operated at conditions that exceed or deviate from the defined boundary conditions. The boundary conditions must be adhered to regardless of the piping system status, including but not limited to: Start-up, hydro-testing, chemical cleaning, system flushing, etc.

22. It is the responsibility of the user/owner of a plant to ensure that all valve operators are ordered to meet all applicable requirements and specifications. 23. Only valves that have been certified as fire safe shall be used in piping systems that may be exposed to fire. 24. Low Emission Packing is suitable for 100 ppm. Standard graphite packing is available, but valve will be in accordance to API 600 12th edition. 25. When operating manual valves, gloves should be worn to minimize the risk of injury to the hands. 26. In situations where manual valves are difficult to operate due to substantial torque requirements, it is recommended that the valve be supplied with a gear or motor operator. 27. All valves should be mounted with the stem vertical and the pipeline horizontal. Check valves may be installed in vertical pipelines only when the normal flow is in the upward direction. For any other orientation, please contact the factory. 28. Depending upon the specific application, normal lubricants may not be sufficient for higher temperature applications. In this case, higher temperature lubricants should be used in place of the standard type. 29. All valve packing glands should be tightened in an even manner. Care should be taken to ensure that the packing gland and/or gland flange do not contact the valve stem or stuffing box during tightening.

19. Valves are not suitable to serve as block valves during system hydrostatic pressure tests that exceed 1.1 times the cold working pressure. 20. Care should be taken around all valves as injury or damage may occur from the leakage of hot, high pressure and/ or caustic materials from a gasket and/or packing joint. Additionally, packing and/or gasket leaks may cause external corrosion damage to the valve. 21. When possible, gate valves should be relieved of maximum seating force when left in the closed position. By relieving this force, it may help prevent damage caused by excessive thermal stem expansion. Care should be taken however to ensure that the valve is not opened, only that the torque/thrust has been removed from the stem. www.cranecpe.com

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General Valve Operation & Maintenance 1.0 THEORY OF OPERATION

GATE VALVES | Gate valves are designed to close off or open up the flow in a pipeline. The wedge is designed to completely stop flow and form a tight seal against pressure in either direction. In the open position, the wedge is completely out of the flow stream. Gate valves are not recommended for throttling use. GLOBE VALVES | Globe valves are designed to close off, open up or throttle the flow in a pipeline. The disc is designed to completely stop flow and form a tight seal with pressure under the disc. In the 10% open position to full open position, globe valves are effective in throttling line pressure. NOTE: Continuous throttling at less than 10% open may cause excessive vibration, noise, wear and damage to discs and seats. CHECK VALVES | Swing check valves are designed to open by the system pressure in a line. The normal direction of flow in the line will open the valve, and any attempt by the flow to reverse will close the valve completely. The check valve typically does not require any outside force or signal to operate properly. Check valves allow flow in one direction only.

2.0 DESCRIPTION

This manual covers all Pacific® bolted bonnet valves. These valves are designed within the limits of ASME B16.34, API 600, API 623, and API 594. For the Operator and Mounting Topworks of these valves, the user is referred to the applicable Section in this manual. See Section 5.0 for Operation of Valves. This manual is for reference purposes only. Disassembly and maintenance of valves should only be performed by qualified personnel. Consult Pacific® for specific technical support. For Specific information regarding a particular style of valve, please refer to the corresponding detailed Section.

3.0 INSTALLATION

When unpacking, care should be exercised in lifting and handling to avoid damage to valves or injury to personnel. Do not lift any valve by the handwheel or stem. Use lifting lugs or straps around the valve body. For specific Installation Information, please refer to Section G of this manual. When installing, ensure that all foreign material is removed from the interior of the valve, including desiccants. NOTE: Do not remove protective end coverings until immediately prior to valve installation. NOTE: Do not disassemble or modify a Pacific® valve in any way prior to installation. This will void the factory warranty if it occurs. When installing flanged or ring joint end flex wedge gate or globe valves into the line, it is advisable to have the valve slightly open to prevent the wedge from becoming “stuck” due to thermal expansion and to discourage damage to the seating surfaces. There is an exception to this with Butt-weld end valves, they should be installed in a lightly closed position. See Valve Installation Section G. A protective paint may have been applied to the weld ends on some valves, and it should be removed before welding, unless it is a deoxaluminite paint which acts as a welding flux and does not need to be removed. Use the smallest electrodes and the minimum amperage possible consistent with approved welding procedures. This will help to minimize warpage in the seat areas. Tack welds should be ground out before completing the root pass in that area. Valves of carbon steel should be allowed to cool slowly. The valve may be covered with a heat-insulating blanket to promote slow cooling and limit the heat-affected zone. Appropriate industry standards should be followed for all PWHT. Certain valve types are designed to function in a single direction (check valves, etc.) All markings should be noted on the valves. Arrows on the valves indicating flow direction should correspond with the system flow direction. NOTE: Ensure that all foreign material (dirt, weld slag, rocks, wood construction materials, weld rod, etc.) has been removed from the valve prior to and after installation. Foreign material is the primary cause of premature seat failures.

4.0 WARRANTY

All Pacific® valves are backed by a full manufacturer’s warranty against defects in materials or workmanship. It should be noted that any work or modification performed on a Pacific® valve must be authorized by Pacific® in order to retain the original factory warranty.

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General Valve Operation & Maintenance 5.0 OPERATING INSTRUCTIONS

Pacific® valves are designed for simplicity and ease of operation. To open a gate, globe, or stop check valve, turn the handwheel in a counterclockwise direction; continue turning until interference is felt; at this point, the valve will be fully open. To close the valve, turn the handwheel in a clockwise direction; continue turning until interference is felt; at this point, the valve will be fully closed. Swing, lift and tilting disc check valves are designed to be operated by line pressure only. When the upstream line is pressurized, flow will open the disc. When the pressure is reduced upstream, or if there is backpressure, the disc will close. With some larger valves under conditions of high pressure, a rim pull of more than 250 lbs. may be required to achieve proper seating.CAUTION! - These valves were designed to operate within the pressure and temperature limits of ASME B16.34. Do not exceed these limits.

6.0 MAINTENANCE Item to Inspect Check Stem threads for wear Check for Packing leaks Check body/bonnet joint for leaks If conditions permit, operate valve Inspect all external connections Ensure Stem and seal areas are free from debris Check all lubrication points Inspect condition of motor and/or gear operators (when used) Inspect valve for obvious damage

Gate Globe Check

• • • • • • • • •

• • •

6.1 PREVENTATIVE MAINTENANCE AND PERIODIC INSPECTION Pacific® recommends that periodic inspections be made of all valves. The frequency of these inspections will vary, depending upon the severity of service and frequency of operation of the valve. As a minimum, all valves should be checked quarterly to ensure proper operation and discourage the damage compounding effects of leakage. The following list details the specific valve types and areas requiring inspection and maintenance. Warning! Do not remove or loosen the packing gland or bonnet bolts while the valve is pressurized.

6.2 MAINTENANCE OF VALVE UNDER PRESSURE If the above listed inspections reveal any indications, the following procedures are recommended: NOTE: Extreme care should be taken when working on any pressurized system! 6.2.1 If the stem packing is leaking, the eyebolt nuts on the gland flange should be tightened uniformly until the leakage stops. If the leakage continues or there is no adjustment remaining, additional packing must be installed or the packing must be replaced. (See disassembly procedure for appropriate Valve or Packing and Gasket Maintenance Section H) It should also be noted that the valve should be able to operate freely at all times. If the valve cannot operate due to excessive packing force, the packing has become worn and must be replaced during a system shutdown. 6.2.2 The stem threads that are exposed to atmosphere should be periodically lubricated to reduce wear, operating torque, and to deter corrosion. Care should be taken to ensure that only the threaded portion of the stem is lubricated. Pacific® does not recommend the practice of lubricating the sealing area of the stem, in the absence of lantern rings or with the exception when lantern rings are installed. This practice tends to attract debris and foreign material, which can lead to stem or stuffing box damage. 6.2.3 The yoke sleeve should be lubricated periodically through the grease fitting to ensure smooth operation. Lubrication should be inspected and revised at each application. Each installation may have specific requirements/ specifications regarding lubrication. 6.2.4 If leakage develops at the body/bonnet joint of a bolted bonnet valve, the bonnet stud nuts should be tightened uniformly. This tightening should be done in accordance with the Bolting Torque Section E of this manual. CAUTION! Do not overstress the bolting. If leakage continues, the gasket should be replaced. (See the Bolting Torque Section E or the appropriate valve disassembly procedure.) 6.2.5 If normal inspection reveals a binding or galling action of valve operating parts, it is advisable to dismantle and inspect the valve parts during a system shutdown. Contact Pacific® prior to disassembling any valve. www.cranecpe.com

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General Valve Operation & Maintenance 7.0 IDENTIFICATION All Pacific® valves are identified with a metal Tag that is riveted to the valve. This tag is usually found on the body/ bonnet joint area, or on the top plate area near the handwheel.

Figure Number

Size

Nominal pipe size (NPS) of the valve.

ASME B16.34 Class

Pressure class rating of the valve as defined in ASME B16.34, Section 2.

PSI @100°F

Pressure in psig at which the valve is rated to operate when the temperature does not exceed 100°F.

PSI @ Max °F

Maximum pressure at which the valve may be operated at the maximum temperature allowed by ASME B16.34, Table 2.

Max °F

Maximum temperature at which the valve may be operated within the limits of pressure allowed by ASME B16.34, Table 2.

Body

Body ASTM material grade designation.

Disc

Disc or Wedge trim material.

Seat

Seat trim material.

10 Stem D

Explanation of Tag Markings Number identifying the valve’s main features including material, class, trim, end connections, and operator type. See the following Sections for classification of Figure Numbers.

Stem material.

XXXX

Country of Origin.

When performing any work, ordering spare parts, or requesting technical support, please refer to this tag. The Serial number is stamped on the valve flange ends. The Figure number (1) and Factory code (J###) cast on the side of the valve body are keys to proper valve identification.

9 10

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PACIFIC API-600 CAST STEEL VALVES

Operator

Material

ORDERING INFORMATION

End

1 A 8 H G PACIFIC API-600 CAST STEEL VALVES

SIZE 1

02 3 6 2H

CLASS

TYPE

A217 C5 A217 C12 A352 LCC A352 LCB 150# A351 CF8M A351 CF8 300# A351 CF3 600#

Material Classification Carbon Steel 1 ¼ CR, ½ Mo 2 ¼ CR, 1 Mo 5% CR, ½ Mo 9% CR, 1 Mo Low Carbon Steel Low Carbon Steel Stainless Steel (316) Stainless Steel (304) Stainless Steel (304L)

TRIM MATERIAL

MATERIAL API Trim No. No.

A B C D E F

Nominal Trim

GATE GLOBE CHECK GATE with CE/PED GLOBE with CE/PED CHECK with CE/PED

N/A (e.g. check valves) TRIM MATERIAL Handwheel

API Trim No. Bevel Gear

Stem Material

F W R

(2) Hard Facing is weld deposited Cobalt base alloy.

No. A D E F G ? B H K L

Raised Face Butt Weld End Seating Surfaces Ring Type Joint

N/A 5 9 Stem Material 8 1 13 Cr (410) 2 Monel® 6 13 Cr (410) E Monel® N

A B C D E F

GATE GLOB CHEC GATE GLOB CHEC

150# 300# 600#

ASTM A216 WCB A217 WC6 A217 WC9 A217 C5 A217 C12 A352 LCC A352 LCB A351 CF8M A351 CF8 A351 CF3

API Trim No.

Material Classification Carbon Steel 1 ¼ CR, ½ Mo 2 ¼ CR, 1 Mo 5% CR, ½ Mo 9% CR, 1 Mo Low Carbon Steel Low Carbon Steel Stainless Steel (316) Stainless Steel (304) Stainless Steel (304L)

Nominal Trim

1 Ob (2) 5 HF / HF (4) Monel® / Monel® 9 (1) (2) 8* F6 / HF 1 (4) (2) Monel® / HF Mo 11 12 316 / HF (3) (2) 31 (3) (2) 16 316/HF / 316/HF 316S 8 to NACE MR0103 12 to NACE MR0103

(1) SS 13% Chromium AISI Type 410 Stainless Steel. 316 (2) Hard Facing is weld deposited Cobalt base alloy. 316 SS

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OPERATOR

* Standard Offering H

TYPE

18" 20" 24"

TRIM MATERIAL

(3) Ni-Cr-Mo stainless steel in the AISI Type 316 category. 0

(4) Ni-Cu Alloy.

2" 2.5" 3" 4"

MATERIAL

No.

N/A Bare Stem 1 Obsolete Pneumatic 5 Cylinder 5 HF / HF (2) Alloy 6 (4) Electric Motor Monel® / Monel® Monel® 9 9 (1) (2) 8 8* F6 / HF 13 Cr / Alloy 6 Monel® / HF (4) (2) Monel® / Alloy 6 1 11 (3) (2) 2 12 316 / HF 316SS / Alloy 6 (3) (2) 6 16 316/HF / 316/HF 316SS / Alloy 6 (both) E 8 to NACE MR0103 www.cranecpe.com N 12 to NACE MR0103 (1) 13% Chromium AISI Type 410 Stainless Steel.

02 2H 03 04 … 18 20 24

1 3 6

VALVE ENDS

Nominal Trim

SIZE

CLASS

Seating Surfaces

OPERATOR No.

No. Material Classification N/A 1ASTM Obsolete (2) A216 Carbon Steel 5A 5 WCB HF / HF Alloy 6 13 Cr (410) (4) Monel® 9D 9 WC6 Monel® / 1Monel® Monel® A217 ¼ CR, ½ Mo (1) (2) 8E 8* F6 / HF 13 Cr / Alloy 6 13 Cr (410) A217 WC9 2 ¼ CR, 1 Mo (4) (2) Monel® /5% HFCR, Monel® 1F 11 A217 C5 ½ Mo Monel® / Alloy 6 (3) (2) 2G 12 C12 316 / HF 316 SS A217 9% CR, 1 Mo 316SS / Alloy 6 (3) (2) 6? 16 LCC 316/HF /Low 316/HF 316SS / Alloy 6 (both) 316 SS A352 Carbon Steel EB 8 to A352 NACELCB MR0103 Low Carbon Steel N 12 to NACE MR0103 A351 CF8M Stainless Steel (316) H (1) 13% Chromium AISI Type 410 Stainless Steel. (3) Ni-Cr-Mo stainless steel in the AISI Type 316 category. A351 CF8 SteelAlloy. (304) K (2) Hard Facing is weld deposited Cobalt baseStainless alloy. (4) Ni-Cu * Standard Offering A351 CF3 Stainless Steel (304L) L

0 H G S P E

End

Trim

Material

150# 2" 300# 600# 2.5"

03 3" 04 4" MATERIAL … No. 18 18"ASTM A216 WCB A 20 20" A217 WC6 D 24 24" A217 WC9 E F G ? B H1 K3 L6

ORDERING INFORMATION Type

CHECK GATE with CE/PED GLOBE with CE/PED CHECK with CE/PED

Class

Type

18" 20" 24"12

C D E F

PACIFIC® API-600 CAST S

Size

CLASS

3" 4"

Size

03 04 … 18 20 24

Operator

SIZE TYPE FOR GATE, GLOBE AND CHECK VALVES 7.1 FIGURE NUMBER DEFINITION 02 2" A GATE ORDERING INFORMATION 2H 2.5" B GLOBE

Material

Class

Trim

Type

Size 12

Class

General Valve Operation & Maintenance

N/A (e.g. check valves) Handwheel

(3) Ni-Cr-Mo stainle (4) Ni-Cu Alloy.

F W

General Valve Operation & Maintenance 7.2 APPROPRIATE MAINTENANCE MANUAL SECTION FOR A GIVEN VALVE FIGURE NUMBER/STYLE The following charts denotes the appropriate maintenance manual Section for a given valve figure number/style. Please note that the Sections listed are the specialized Sections only and pertinent general valve information is contained in other Sections of this manual. Please refer to table of contents for total listings.

API 600 BOLTED BONNET - GATE VALVE, OS&Y

Manual Section

Class 150, solid wedge gate valve B Class 150, flexible wedge gate valve B Class 300, solid wedge gate valve B Class 300, flexible wedge gate valve B Class 600, solid wedge gate valve B Class 600, flexible wedge gate valve B

API 623 - BOLTED BONNET - GLOBE VALVE, OS&Y Class 150, plug type disc globe valve C Class 300, plug type disc globe valve C Class 600, plug type disc globe valve C

API 594 - BOLTED BONNET - SWING CHECK VALVE Class 150, swing check valve D Class 150, swing check valve w/outside lever & weight D Class 150, severe service swing check valve D Class 300, swing check valve D Class 300, swing check valve w/outside lever & weight D Class 600, swing check valve D Class 600, swing check valve w/outside lever & weight D

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General Valve Operation & Maintenance 8.0 BOUNDARY CONDITIONS The following chart denote the defined boundary conditions for all Pacific® Valve products. Boundary Conditions for Bolted Bonnet Products Scope of Product Service fluid

2”-24” 150#-600# • Water, steam, gas, or hydrocarbon compounds. • Corrosive or toxic fluids when used within the parameters defined herein. • No suspended solid material greater than 100 microns.

Service life

20 years or when corrosion significantly affects the wall thickness as defined by API 600 and ASME B16.34. This excludes normal maintenance parts such as packing, seals, gaskets and parts that move relative to each other e.g. seats, stems and bushings.

Allowable pressure and temps.

Per Table 2 ASME B16.34.

Materials for pressurized parts

Only materials approved by relevant governing body may be used. Refer to the approved CE materials list. Appropriate material for service conditions to be based upon the following criteria: 1. The design pressure and temperature. 2. An acceptable service life consistent with the corrosion rate of the material at design conditions. 3. Expected operating conditions within the defined pressure cycles, thermal cycles and flow velocity limits.

Packing and gasket materials

To be compatible with expected operating conditions.

Method of operation

• Gate and Globe: Handwheel, Manual Gear, Motor Actuator, Air or Hydraulic cylinder Actuator. • Check: self-actuation.

Frequency of operation

• Gate and Globe valves: not to exceed once per week or 50 per year. • Check: N/A.

Installation orientation

• Gate and Globe: Stem vertical up in a horizontal pipe run. • Check: Flow horizontal in a horizontal pipe run or Vertical up in a vertical pipe run.

Flow velocity

• To keep noise and erosion at or below reasonable levels, valves are not to be used for throttling service, and velocity is not to exceed the values shown in table below. • Check valves should operate at or above the velocity indicated to stabilize the disc and avoid premature wear. Maximum flow velocity for gate, globe and check valves: Gate 300√ V T-globe 120√ V Std check 200√ V Minimum flow velocity for check valves is 55√ V Where V = Specific volume of flowing medium in ft3/lb

Hydrostatic test

1.5 times the 100°F rating pressure in ASME B16.34 for the body material.

Pressure cycles

Unlimited cycles < Design Pressure/3.

Thermal cycles

Unlimited cycles < 30°F.

Heat up/cool down rate

Not to exceed 100°F per hour for 2000 cycles.

Pipe & support reactions

All reaction loads transmitted through valve ends. Cross section and Moment of Inertia of valve ends to be greater than that of the connecting pipe.

External fire capability

Valve seats of standard product may be solid metal or may contain plastic inserts. Solid metal seats are not suitable for a sustained external heat source greater than 1500°F. Plastic inserted seats are not suitable for temperatures greater than 450°F.

Wind and earthquake rating

1 g load in any direction.

Vent or drain method

None.

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Bolted Bonnet Gate Valves

SECTION B Bolted Bonnet Gate Valves

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Bolted Bonnet Gate Valves 1.0 GENERAL INFORMATION

4.0 LUBRICATION

For General Operation & Maintenance Information regarding this or any other Pacific® valve please refer to Section A of this manual.

4.1 | Parts requiring lubrication are stem and stem Nut threads 5,7, entire gasket 14, and under all nuts 16 before torquing. Bonnet studs and nuts should be lubricated with an antisieze lubricant.

2.0 COMPLETE DISASSEMBLY CAUTION! Before disassembling any valve, ensure that all pressure has been removed from the line and from any cavities within the valve. Contact Pacific® before disassembling any valve. 2.1 HANDWHEEL OPERATED VALVES | Upon completion of the disassembly procedure listed below, the handwheel 12 may be separated from the stem nut 7, by removing the handwheel nut 13. 2.2 GEAR AND MOTOR OPERATED VALVES | Refer to Section J, Gear and Motor Information.

5.0 SPECIAL TOOLS AND INSTRUCTIONS 5.1 | Recommended Bolting Torques are shown in Section E of this manual 5.2 | No special tools are required for general valve maintenance.

6.0 PREVENTATIVE MAINTENANCE 6.1 | Refer to Section A of this manual for General Valve Maintenance Information.

2.3 | The following page contains a general disassembly and reassembly procedure. These procedures cover the bulk of the disassembly and reassembly process, for specific information regarding general valve information, actuators, packing and gaskets, etc., please refer to the appropriate Section.

3.0 MAINTENANCE OF DISASSEMBLED VALVES 3.1 | Following the disassembly procedures listed below, examine the body cavity 1 for deposits of foreign material. 3.2 | Examine seating surfaces of seat rings 4 and disc/wedge 3 for wear. 3.3 | Examine stem 5, seal area, and threads for excessive wear. If excessive wear is evident, worn parts, or if necessary, the entire valve should be reconditioned or replaced. 3.5 | Pacific® can offer complete replacement seal kits and spare parts for reconditioning. When ordering, always state the figure number, factory code, serial number and the valve body/ trim material. 3.6 | Pacific® also offers complete remanufacturing services to rework your valve. If you find this necessary, our nationwide network of Pacific® Valve Service Centers will remanufacture your valve to factory specifications.

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Bolted Bonnet Gate Valves Class 150, 300, 600 & 900 - All Sizes DISASSEMBLY • Read the warning notice in Section 2.0 of these instructions. • Loosen and remove the packing gland eyebolt nuts 18. • Loosen and remove the bonnet nuts 16 and studs 15. • Using a strap or similar device (when necessary) lift the bonnet assembly 2 up and away from the valve body 1. Note and mark the orientation of the disc/wedge to the valve body and seats. • Remove the disc/wedge 3 from the stem 5. • While holding the stem 5 , turn the handwheel 12 in a clockwise direction to draw out the stem. • Once the stem has been removed, the gland 10 and the gland flange 11 may be removed. • Remove the packing 9 using a packing hook or similar tool. Care should be taken to ensure that there is no damage to the stuffing box surface. • Remove the gasket 14 from the valve body. • If necessary, remove the handwheel nut 13 and the handwheel 12. • Remove the stem nut retainer 8. This may require the removal of set screws or the removal of tack welds, depending upon the valve configuration. • Remove the stem Nut 7 . • Unless there is significant damage, the Backseat bushing 6 should not be removed.

REASSEMBLY • Clean all parts thoroughly. Lubricate the seating surfaces with a light oil to discourage galling during reassembly. • Install a new gasket 14. • Install new packing 9 , if necessary. Also install gland 10 and gland flange 11. • Install stem 5 into bonnet assembly. • Reinstall the packing gland eyebolt nuts 18. • Replace disc/wedge 3 onto stem. • Install bonnet and wedge assembly into valve body 1, noting the previously made marks to indicate the wedge orientation in the body. • Reinstall bonnet studs 15 and nuts 16. • Tighten the bonnet studs to the values listed in Section E of this manual.

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Item

Description

Item

Description

Body

Handwheel

Bonnet

Handwheel Nut

Disc

Gasket

Seat Ring

Bonnet Stud Bolt

Stem

Bonnet Stud Nut

Backseat Bushing

Eye Bolt

Stem Nut

Eye Bolt Nut

Stem Nut Retainer

Eye Bolt Pin

Packing

Spacer Bushing

Gland

Grease Fitting

Gland Flange

ID Tag (Not Shown)

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Notes

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Bolted Bonnet Globe Valves

SECTION C Bolted Bonnet Globe/ Stop Check Valves

* For illustration purposes only, Globe design supplied may or may not include plug guide.

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Bolted Bonnet Globe Valves 1.0

GENERAL INFORMATION

For General Operation & Maintenance Information regarding this or any other Pacific® Valve please refer to Section A of this manual.

2.0

COMPLETE DISASSEMBLY

CAUTION! Before disassembling any valve, ensure that all pressure has been removed from the line and from any cavities within the valve. Contact Pacific® before disassembling any valve. 2.1 HANDWHEEL OPERATED VALVES | Upon completion of the disassembly procedure listed below, the handwheel 50 may be separated from the yoke sleeve 31, by removing the handwheel nut 54. 2.2 GEAR AND MOTOR OPERATED VALVES | Refer to Section J of this manual for specific Gear and Motor Information. 2.3 | The following page contains a general disassembly and reassembly procedure. These procedures cover the bulk of the disassembly and reassembly process, for specific information regarding general valve information, actuators, packing and gaskets, etc., please refer to the appropriate Section.

3.3 | Examine stem 70, seal area and threads for excessive wear. 3.4 | If excessive wear is evident, worn parts, or if necessary, the entire valve should be reconditioned or replaced. 3.5 | Pacific® offers complete replacement seal kits and spare parts for reconditioning. When ordering, always state the figure number (or stock number) and serial number of the valve and the body material. 3.6 | Pacific® also offers complete remanufacturing services to rework your valve. If you find this necessary, our nationwide network of Pacific® Valve Service Centers will remanufacture your valve to factory specifications.

4.0 LUBRICATION 4.1 | Parts requiring lubrication are stem and yoke sleeve threads 70, 31, entire gasket 55, and under all nuts 16 & 17 before torquing. Bonnet studs and nuts should be lubricated with an antisieze lubricant to promote ease of future disassembly.

5.0 SPECIAL TOOLS AND INSTRUCTIONS 5.1 | Recommended Bolting Torques are shown in Section E of this manual

3.0 MAINTENANCE OF DISASSEMBLED VALVES

5.2 | No special tools are required for general valve maintenance.

3.1 | Following the disassembly procedures listed below, examine the body cavity 10 for deposits of foreign material.

6.0 PREVENTATIVE MAINTENANCE

3.2 | Examine seating surfaces of seat ring 11 and disc 71 for wear.

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6.1 | Refer to Section A of this manual for General Valve Maintenance Information.

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Bolted Bonnet Globe Valves Class 150, 300, 600 & 900 - All Sizes DISASSEMBLY • Read the warning notice in Section 2.0 page of these instructions. • Loosen and remove the packing gland bolts 16. • Loosen and remove the bonnet nuts 17 and studs 98. • Using a strap or similar device (when necessary) lift the bonnet assembly 30 up and away from the valve body 10. • Remove the disc 71 from the stem 70 by grinding off the tack welds 48 on the lock nut 72 or by removing the disc pin 49. • Remove the wheel nut 54 and the handwheel 50. • Remove the stem 70 by turning it until it is free of the yoke sleeve 31. • Once the stem has been removed, the gland 35 and the gland flange 36 may be removed. • Remove the packing 46 using a packing hook or similar tool. Care should be taken to ensure that there is no damage to the stuffing box surface. • Remove the gasket 55 from the valve body. • If necessary, remove the yoke sleeve 31 by unscrewing it counterclockwise. Note it may be necessary to remove set screws, depending upon valve configuration. • The bonnet stem bushing 32 should not be removed unless damaged.

REASSEMBLY • Clean all parts thoroughly. Lubricate the seating surfaces with a light oil to discourage galling during reassembly. • Install a new gasket 55. • Install new packing 46 , if necessary. Also install gland 35 and gland flange 36. • Install stem 70 into bonnet assembly. • Reinstall the packing gland nuts 16. • Replace disc 71 and lock nut 72 on to stem. • Replace disc pin 49, if provided • Install bonnet and disc assembly into valve body 10. • Reinstall bonnet studs 98 and nuts 17. • Tighten the bonnet studs to the values listed in Section E of this manual.

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Item

Description

Item

Description

Body

Disc Pin

Seat Ring

Handwheel

Nut

Eye Bolt

Nut

Wheel Nut

Bonnet

Gasket

Yoke Sleeve

Stem

Bonnet Stem Bushing

Disc/Plug

Packing Gland

Lock Nut

Gland Flange

Thrust Washer

Packing

Bonnet Studs

Eye Bolt Pin

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Notes

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Bolted Bonnet Swing Check Valves

SECTION D Bolted Bonnet Swing Check Valves

For illustration purposes only. Design supplied may be internal hung or have hinge with external plug access.

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Bolted Bonnet Swing Check Valves 1.0 GENERAL INFORMATION

4.0 LUBRICATION

For general information regarding this or any other valve please refer to Section A of this manual.

4.1 | Parts requiring lubrication are; entire gasket 55, and under all nuts 16 before torquing. Bonnet studs and nuts should be lubricated with an antisieze lubricant to promote ease of future disassembly.

2.0 COMPLETE DISASSEMBLY CAUTION! Before disassembling any valve, ensure all pressure has been removed from the line and from any cavities within the valve. Contact Pacific速 before disassembling any valve.

5.0 SPECIAL TOOLS AND INSTRUCTIONS

2.1 HANDWHEEL OPERATED VALVES (IF APPLICABLE) | Upon completion of the disassembly procedure listed below, the handwheel may be separated from the yoke sleeve, by removing the handwheel nut.

5.2 | No special tools are required for general valve maintenance.

2.2 GEAR AND MOTOR OPERATED VALVES | Refer to Section J of this manual for specific Gear and Motor Information.

6.1 | Refer to Section A of this manual for General Valve Maintenance Information.

5.1 | Recommended Bolting Torques are shown in Section E of this manual

6.0 PREVENTATIVE MAINTENANCE

3.0 MAINTENANCE OF DISASSEMBLED VALVES 3.1 | Following the disassembly procedures listed below, examine the body cavity 10 for deposits of foreign material. 3.2 | Examine seating surfaces of seat ring 11 and disc 71 for wear. 3.3 | Examine hinge 40 and hinge pin 41 for wear. 3.4 | If excessive wear is evident, worn parts, or if necessary the entire valve should be reconditioned or replaced. 3.5 | Pacific速 offers complete replacement seal kits and spare parts for reconditioning. When ordering, always state the figure number (or stock number) of the valve and the body material. 3.6 | Pacific速 also offers complete remanufacturing services to rework your valve. If you find this necessary, our nationwide network of Pacific速 Valve Service Centers will remanufacture your valve to factory specifications.

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Bolted Bonnet Swing Check Valves Class 150, 300, 600 & 900 - All Sizes DISASSEMBLY • Read the warning notice in Section 2.0 of these instructions. • Loosen and remove the bonnet nuts 16 and studs 98. • Remove and discard the gasket 55. • Remove the disc nut retention system 49. This may include the disc nut pin and or a tack weld. • Remove the disc nut 72 disc washer 85 and disc 71. Care should be taken to ensure that the disc is not damaged upon removal. • Remove the hinge mount • Remove the hinge and disc assembly from the valve. Note the position and quantity of any shims or spacers (when used). • If necessary, remove the hinge pin 41 from the hinge 40.

REASSEMBLY • Clean all parts thoroughly. • Reinstall hinge/disc assembly in reverse order • Care should be taken to reinstall/apply any lock devices on the disc to disc nut connection. • Install a new gasket 55. • Tighten bonnet fasteners to the values listed in Section E of this manual.

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Item

Description

Item

Description

Body

Disc Nut Pin

Seat Ring

Gasket

Nut

Disc

Cover/Bonnet

Disc Nut

Hinge

Disc Washer

Hinge Pin

Stud

Hinge Mount

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Notes

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Bolting Torque Data

SECTION E Bolting Torque Valves

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Bolting Torque Data 1.0 GENERAL INFORMATION For General Valve Operation & Maintenance Information please refer to Section A of this manual. This Section details the specific torque values recommended by Pacific® for bolting used in all Pacific® products.

2.0 STANDARD PROCEDURES CAUTION! The torque values in this section only apply to the body bonnet joints and flange joints. Please reference section H for packing torques. 2.1 | Always use new bolting materials. 2.2 | Verify that the materials are compatible with the process system as well as any temperature or pressure requirements. Note that bolting materials can have minor identification changes which may have a substantial impact on performance, ie. B7M vs. B7. 2.3 | Whenever allowed by system and process parameters, use appropriate lubrication to ensure even tightening of the bolting materials. For higher temperature applica-tions, the use of an “Antisieze” compound may be necessary to promote future disassembly.

3.0 ASSEMBLY AND MAINTENANCE OF FLANGED JOINTS When a flanged joint is assembled, each of the component parts in subject to tensile or compressive stresses of varying magnitude. In the great majority of cases, it is adequate to tighten the bolts sufficiently to withstand the test pres-sure without leakage. The maximum allowable stress values for bolting given in the various codes such as ASME Boiler and Pressure Vessel Code and the ASME Code for Pres-sure Piping are design values to be used in determining the minimum amount of bolting required.

greater than the design value therefore must be provided. If it is not, further bolt strain develops during the test which tends to part the joint and thereby, to decompress the gasket enough to al-low leakage. It is evident that an initial bolt stress higher that the design value may, and in some cases must, be developed in the tightening operation. This practice is permissible, as pointed out in Appendix S, Section VIII, Division 1 of the ASME Boiler and Pressure Vessel Code, provided it includes necessary and appropriate provision to insure against excessive flange distortion and gross crushing of the gasket. Investigation of field-erected flange joints has indicated that the probable bolt stress developed manually, when using standard wrenches on alloy steel bolts is:

Where S is the bolt stress and d is the nominal diameter of the bolt. Experience indicates that these stresses are satisfactory for ASME B16.5 flanges and will comply with the requirements as set forth in the preceding paragraphs. It can be seen that smaller bolts will have excessive stress unless judgement is used in pulling up on them. On the other hand, it will be impossible to develop the desired stress in very large bolts by ordinary hand wrenching. Impact wrenches may prove serviceable, but if not, resort may be had to such methods as preheating the bolt or using hydraulically-powered bolt tensioners. With some of these methods, control of the bolt stress is possible by means inherent in the procedure, especially if effective thread lubricants are employed, but in all cases, the bolt stress can be regulated within reasonable tolerances by measuring the bolt elongation with suitable extensometer equipment. Generally, simple wrenching without verification of the actual bolt stress meets all practical needs, and measured control of stress is employed only when there is some special or important reason for doing so.

A distinction must be recognized between the design value and the bolt stress that might actually exist or that might be needed for conditions other than the design pressure. The initial tightening of the bolts is a pre-stressing operation, and the amount of bolt stress developed must be within proper limits to insure, on the one hand, that it is adequate to provide against all conditions that tend to produce a leaking joint and, on the other hand, that it is not so excessive that yielding of the bolts and/or flanges can produce relaxation that also can result in leakage.

It is possible for the bolt stress to decrease after initial tightening, because of slow creep or relaxation of the gasket, particularly in the case of the “softer” gasket materials. This may be the cause of leakage in the hydrostatic test, in which case it may suffice merely to retighten the bolts. A decrease in bolt stress can also occur in service at elevated temperatures as a result of creep in the bolt and/or flange gasket material, with consequent relaxation. When this results in leakage under service conditions, it is common practice to retighten the bolts, and sometimes a single such operation, or perhaps several repeated at long intervals, is sufficient to correct the condition.

The first important consideration is the need for a joint to be tight in the hydrostat-ic test. An initial bolt stress of some magnitude

(Abstracted in part from Appendix S, Section VIII, Division 1 of the ASME Boiler and Pressure Vessel Code.)

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Bolting Torque Data 4.0 TORQUE VALUES All values are listed in foot/pounds (ft/lbs.) A range is supplied. All bolting torques are based upon use of well lubricated bolting. ASTM A193, Gr B7, B8, B8m and K-500 Bolting

30,000 psi

45,000 psi

60,000 psi

Bolt Diameter (inches)

No. of Threads (per inch)

Minor Diameter (inches)

Area Tensile Stress (sq. inches)

Torque (ft/lbs)

Tension (lbs)

Torque (ft/lbs)

Tension (lbs)

Torque (ft/lbs)

Tension (lbs)

1/4

.1887

.0318

654

1431

1908

5/16

.2443

.0524

1572

2439

3144

3/8

.2983

.0775

2325

3488

4650

7/16

.3499

.1063

3189

4784

6378

1/2

.4056

.1419

4257

6386

8514

9/16

.4603

.182

5460

8190

10920

5/8

.5135

.226

6780

10170

120

13560

3/4

.6273

.334

110

10020

165

15030

220

20040

7/8

.7387

.462

170

13860

255

20790

340

27720

.8466

.606

260

18180

390

27270

520

36360

1 1/8

.9716

.790

375

23700

565

35550

750

47400

1 1/4

1.0966

1.000

525

30000

790

45000

1050

60000

1 3/8

1.2216

1.233

715

36990

1,075

55485

1425

73980

1 1/2

1.3466

1.492

925

44760

1,395

67140

1850

89520

1 5/8

1.4716

1.78

1,200

53400

1,800

80100

2400

106800

1 3/4

1.5966

2.08

1,500

62400

2,250

93600

3000

124800

1 7/8

1.7216

2.41

1,850

72300

2,775

108450

3700

144600

1.8466

2.77

2,260

83100

3,390

124650

4525

166200

2 1/4

2.0966

3.56

3,260

106800

4,890

160200

6525

213600

2 1/2

2.3466

4.44

4,500

133200

6,750

199800

9000

266400

2 3/4

2.5966

5.43

6,025

162900

9,040

244350

12050

325800

2.8466

6.51

7,875

195300

11,815

292950

15750

390600

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Bolting Torque Data 4.0 BOLTING SEQUENCE

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Long Term Storage of Valves

SECTION F Long Term Storage of Valves

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Long Term Storage of Valves 1.0 GENERAL INFORMATION For General Operation & Maintenance Information regarding for valves, please refer to Section A of this manual.

2.0 STORAGE The following recommendations are for preparing valves and their accessories for Long Term Storage. They are necessary to maintain the valves in proper condition prior to installation into the pipeline. By following these procedures, abrasive and corrosive substances can be prevented from affecting valve performance. It is the purchaserâ&#x20AC;&#x2122;s responsibility to take the necessary precautions for the protection of valves in storage. 2.1 AS SHIPPED CONDITION | Valves are packaged with a moisture resistant closure on the valve ends. Where size permits, plastic plugs or caps are used. On larger size valves, wood covers are sealed with tape and securely attached with metal bands. On valves with pipe flanges the wooden covers are secured with bolts. All other openings are covered with plastic caps or plugs. Parts packaged separately are secured in packaging from the factory to prevent damage during handling and storage. These parts are to be stored off the ground in an area protected from the weather.

Slight external rusting may occur on valves stored outside. This will have little or no effect on their performance. If units are stored for more than 6 months we recommend that gate and globe valves be cycled open to close every 6 months to keep the packing from adhering to the stem and to help lubricate the stem and yoke. Heavy internal rust however, may be harmful and must be corrected. 2.4 PREPARATION FOR INSTALLATION INTO THE PIPELINE | Inspect valves as per the above instructions and remove any contamination, assuring that the valve is clean and dry. Re-torque all bolting to factory specifications to compensate for possible bolt relaxation, which may occur during long storage. Ensure that all foreign material has been removed from the valve.

2.2 RECOMMENDED STORAGE FACILITIES | The following are a list of storage types in order of most preferred to least preferred: 1. Enclosed weather tight building with a concrete floor. Enclosed building with a dirt floor. Valves must be on pallets. 2. Open air, valves on pallets on a concrete floor covered with a tarpaulin (this is not recommended for more than six months) 3. Open air, valves on pallets on a dirt floor and covered with a tarpaulin (this is not recommended for more than six months) 2.3 INSPECTION | Periodic inspections should be performed on all stored valves and parts. The frequency of these inspections should be determined by the type of storage facilities and weather conditions. At a minimum, all parts and valves should be inspected every 4-6 months. Inspect for dirt, moisture or any other type of contamination. If any is found the valve is to be thoroughly cleaned and dried. Repeat the above listed packaging procedure to ensure the valve is weather tight. www.cranecpe.com

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Valve Installation

SECTION G Valve Installation

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Valve Installation GENERAL INFORMATION For general valve information, please refer to Section A of this manual.

1.0 INTRODUCTION By exercising proper care in the installation of Pacific® valves, the probability of trouble-free service will be enhanced. It is important to recognize that in the transport, handling and storage of a valve between the time of manufacture and the time of installation, there are numerous possibilities for accident or error, which may affect valve performance. All valves should be handled/installed in such a manner as to comply with all applicable state, local and federal safety regulations including, but not limited to OSHA regulations. Personal Protective Equipment (PPE) should also be used in compliance with all regulations.

2.0 INSPECTION AND HANDLING Before installation of the valve, it is important to determine that the valve is in satisfactory condition. It may be helpful to observe the following points, in order to avoid subsequent valve problems: 2.1 | Carefully unpack valve and note any special warning tags or identification plates attached to the valve; take appropriate action. 2.2 | Check the valve for any markings indicating flow direction. If flow direction is indicated, appropriate care should be exercised to install the valve in the proper flow orientation. Check valves and non-return valves are uni-directional and must be installed in the proper orientation. 2.3 | Inspect the valve interior through the end ports to determine that it is clean and free from foreign matter and/ or harmful corrosion. Remove any special packing materials (blocks to prevent disc movement) or packages of desiccant. The wedge/discs of weld end gate/globe valves should be lightly closed during welding of the valves into the pipeline. 2.4 | Check the pipeline to ensure that it is properly aligned and supported. Expansion joints or bends should be in stalled in the pipeline to compensate for expansion and contraction. 2.5 | Only qualified riggers should handle the valves. The pick

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up point for all Pacific® valves is by the use of a strap or chain around the neck area of the valve body. Do not pick up Pacific® valves by use of straps or chains on or around the handwheels, yoke, bevel gear, motor or cylinder operator, or any override attachment. Do not pick up a valve by the packing bolting or other interior connections. After the weight of the valve is supported by a strap or chain around the neck of the valve body, other lines may be attached for steadying the valve in place during installation. 2.6 | Immediately prior to valve installation the interior of the piping (to which the valve is to be attached) should be checked for cleanliness and freedom from foreign materials.

3.0 INSTALLATION All valves should be installed in such a manner as to prevent exposure to excessive vibration and process flow turbulence. Check valves specifically are subject to increased turbulence and wear due to their position in a piping system. At a minimum, bolted bonnet check valves should have 10 pipe diameters of straight pipe immediately upstream of the valve and they should not be placed close to pumps, valves or other fittings. When Pacific® valves with bevel gear, motor or air cylinder operators are mounted in a position other than with the valve stem in a vertical position, contact Pacific® for specific instructions. 3.0.1 PREPARATION FOR INSTALLATION INTO THE PIPELINE | Inspect valves as per the above instructions and remove any contamination, assuring that the valve is clean and dry. Re-torque all bolting to factory specifications to compensate for possible bolt relaxation, which may occur during long storage. Ensure that all foreign material has been removed from the valve. 3.1 WELD END VALVES | Welded joints when properly made, provide a structural and metallurgical continuity between the pipe and the valve body. For socket weld joints it is usually required that the weld fillet have more cross sectional area that the pipe. Butt welds usually require full penetration and thickness at least equal to that of the pipe. If a pipe of a high strength alloy is welded to a valve with body material of lower mechanical strength, the weld usually must taper to a compensating greater thickness at the valve end, or the valve must have a matching high strength welded-on extension or "pup".

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Valve Installation CAUTION! All welding should be in accordance with any Code or jurisdictional regulations applicable to the piping system construction and with complete and approved welding procedures, and inspected as required by applicable specification. The following items are a general overview of sound welding practice: 3.1.1 | Check material markings on pipe and valve to confirm they are as specified.

tight sealing and compressive deformation of gasket material between facing flange surfaces. The bolting must provide the mechanical force necessary to maintain the necessary compressive stresses on the gasket, as well as resist the normal pressure forces tending to separate the joint. It should be recognized that bolting force used for "brute force" alignment of misaligned flanges will not be available to sustain gasket loading and pressure force loading, and the result may be a joint leakage problem.

3.1.2 | Inspect welding end surfaces, dimensions, and cleanliness. Correct any condition that might interfere with assembly and satisfactory welding.

3.2.1 | Check mating flange facings. If a condition is found which might cause leakage, (e.g. a deep radial groove or cut), do not attempt to assemble until the condition is corrected.

A protective paint may have been applied to the weld ends on some valves, and it should be removed before welding, unless it is a deoxaluminite paint which acts as a welding flux and does not need to be removed.

3.2.2 | Check bolting for proper size, length and material.

3.1.3 | If backing rings are to be used, check to confirm that ring material is compatible with pipe and valve materials, check individual rings for fit and cleanliness. 3.1.4 | Determine that the prescribed welding parameters including preheating and post weld heat treating if required, are in accordance with the approved welding procedure. 3.1.5 INSPECT VALVE-PIPE END ALIGNMENT; ADJUST IF AND AS REQUIRED. | Valves should be in a slightly closed position when welding in-line. This is opposite the normal recommended installation for flanged or threaded valves, which is to leave the valves in a slightly open to fully open position. The reasoning behind slightly closing the valve has to do with the welding installation. When welding valves in-line an electrode is connected to the valve body and the opposite electrode feeds the weld metal across the gap between the valve and the pipeline. If the electrode connected to the valve body is connected on the opposite side of the valve from where the welding is being performed than if the valve is left in an open position the current from the valve electrode to the welding electrode can arc across the gap between the valve disc/wedge and potentially damage or tack weld across the seating surfaces. 3.1.6 | Securely tack weld. 3.1.7 | Complete weld, using approved welding procedure. 3.2 FLANGED VALVES | Pipe flanged joints depend on

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3.2.3 | For flange bolting for steel flanges ASME Class 400 or higher, high strength material (usually B - 7) is required. The proper matching of flanges, bolting and gaskets is important. 3.2.4 | Check gaskets for obvious defects or damage. 3.2.5 | Use care to provide good alignment of flanges being assembled. Use suitable lubricants on bolt threads. When assembling, sequence the bolt tightening (in a star pattern) to make initial contact of flanges and gaskets as flat and parallel as possible. Tighten gradually and uniformly to avoid tendency to twist one flange relative to the other. Use of torque wrench is important to assure correct and uniform final tightening of flange bolting. 3.2.6 | Parallel alignment of flanges is especially important in the case of assembly of a valve into an existing system. It should be recognized that if the flanges are not parallel, in such instances, it would be necessary to bend something to make the flange joint tight. Simply forcing the flanges together with the bolting may bend the pipe, or it may bend the valve. In large diameter piping particularly, such conditions should always be brought to the attention of someone capable of evaluating the bending conditions, and corrective measures taken as needed. 3.2.7 | CAUTION! As indicated above, torque wrenches should be used for flange bolting. If, in the tightening process, the torque on a given bolt has been increasing with each part turn, and then is observed to remain unchanged or increase a much lesser amount with an additional part turn, that bolt is yielding. Such bolt should

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Valve Installation be replaced and scrapped. See Section E for Torque Values. 3.2.8 | Repeat the process at second valve end. Again apply wrench at end of valve to which pipe is being assembled.

4.0 TESTING AND ADJUSTMENT 4.1 | When a valve has been properly inspected and installed, it is reasonable to assume it will be in good condition and ready to operate. Nevertheless, it is at this time that the valve is at the end point of its more vulnerable phase. Operability can be proven only by test. 4.2 | At this point valves having adjustable stem seals should be checked to determine that packing has been properly installed and gland bolting has its initial adjustment. Additional adjustment should be determined according to need as valve operability is checked and as system pressure is introduced. 4.3 | A first observation can be made by actuating the valve through an open-close, or close-open cycle. If no obvious problems are observed, an actual test at pressure may be applied while tightness and operability are checked. 4.4 | It is a fairly common practice after the installation of piping systems to clean the systems by blowing with gas or steam or flushing with a liquid to remove debris and/or internal protective films and coatings. It should be recognized that valve cavities may form a natural trap in a piping system and material not dissolved in or carried out by the flushing fluid may settle in such cavities and adversely affect valve operation. Also, abrasive material carried by a high velocity fluid stream may cause serious damage to seating surfaces. Again, great care should be taken to ensure that the valve is free of all debris prior to operation. 4.5 | Upon installation, new valve lubrication should be applied to all lubrication points.

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Packing and Gasket Maintenance and Valve Lubrication

SECTION H Packing and Gasket Maintenance and Valve Lubrication

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Packing and Gasket Maintenance and Valve Lubrication 1.0 GENERAL INFORMATION

4.0 GASKET MAINTENANCE

For General Valve Operation & Maintenance Information please refer to Section A of this manual.

NOTE: The following information refers primarily to valves that have been repaired/reconditioned previously. It is always a sound practice to inspect and maintain all sealing areas. Inspection of the valve body/bonnet joint should be a part of routine maintenance inspection after installation and startup. Flanged valves should have the flange ends inspected at the same time. In addition to improper gasket installation procedure, thermal changes, pressure changes, vibrations etc also may cause leakage. If re-torquing of the bolting does not stop the leakage, the flanged joint should be unbolted and the gasket carefully examined.

2.0 PACKING MAINTENANCE 2.1 | Inspection of the valve stem/bonnet seal should be an essential part of routine monthly valve maintenance inspections. 2.2 | If inspection indicates the seal is leaking, the bolts holding the gland flange should be tightened uniformly (one- quarter of a turn at a time) until leakage stops. CAUTION!! Extreme care should be taken when working on or around any pressurized equipment. Tightening of bolting beyond this point results in over- compression of the packing against the stem, thereby producing excessive wear and loss of packing material. If difficulty is experienced in achieving satisfactory sealing without producing excessive stem friction, it may be desirable to increase or to replace the packing material. 2.3 | If gland travel is fully taken up and leakage does not stop, a careful examination of the stem should be undertaken. Operation of a valve on a regular basis will minimize corrosion between the stem and packing material. Any deterioration of the stem surface which is in contact with the stem seal or packing (such as dents, scratches, pitting or general corrosion) must be recognized as a probable cause of leakage problems. The valve stem should be examined to determine if it has become bent or misaligned. If any of the above conditions exist, the stem must be refinished or replaced. If the stem is undamaged and the valve continues to leak, addition to or replacement of the packing is necessary. 2.4 | Consult factory for any further packing related concerns.

Observation

Possible Remedies

Gasket corroded

Select replacement material with improved corrosion resistance.

Gasket extruded excessively

Select replacement material with better cold flow properties, select replacement material with better load carrying capacity - i.e., more dense.

Gasket grossly crushed

Select replacement material with better load carrying capacity, provide means to prevent crushing the gasket by use of a stop ring or redesign of flanges.

Gasket mechanically damaged due to overhang of raised face or flange bore

Review gasket dimensions to insure gaskets are proper size. Make sure certain gaskets are properly centered in joint.

No apparent gasket compression visible

Select softer gasket material. Select thicker gasket material. Reduce gasket area to allow higher unit sealing load. Inspect flange dimensions.

Gasket Substantially on O.D. than I.D.

Indicative of excessive “flange rotation” or bending. Alter gasket thinner dimensions to move gasket reaction closer to bolts to minimize bending movement. Provide stiffness to flange by means of back-up rings. Select softer gasket material to lower required seating stresses. Reduce gasket area to lower seating stresses

Gasket unevenly compressed around circumference.

Improper bolt up procedure followed. Make certain proper sequential bolt up procedures are followed.

Gasket thickness varies periodically

Indicative of “flange bridging” between bolts or warped flanges. Provide reinforcing rings for flanges to better distribute bolt load. Select gasket material with lower seating stress. Provide additional bolts if possible to obtain better load distribution. If flanges are warped, re-machine or use softer gasket material.

3.0 PACKING INSTALLATION & INSTRUCTIONS 3.1 | Manually open and close valve several times to ensure all parts are working smoothly under pressure and to help “set” the packing. 3.2 | After several days, inspect valve for leakage. Slight adjustment may be required. 3.3 | The following suggestions apply if Chevron type Teflon packing is used: 3.3.1 | Ensure that sections of the lips of the rings are not turned over. 3.3.2 | Ensure that the packing rings are facing in the direction of the medium being sealed - whether it is liquid or gas. www.cranecpe.com

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Globe and Gate Valve LE Torque Torques for Teadit 2236 Packing Standard Configuration Valve Size (Inches)

Bolt Torque (ft-lbs) #150

#300

#600

2.5

128

110

227

191

325

104

225

346

110

273

180

317

196

401

Torques for Teadit 2236 Packing Standard Configuration Valve Size (Inches)

Bolt Torque (ft-lbs) #150

#300

#600

2.5

108

114

128

104

162

112

243

106

117

265

110

148

265

137

191

287

180

243

462

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Packing and Gasket Maintenance and Valve Lubrication 5.0 GASKET INSTALLATION PROCEDURES Regardless of the type of gasket being used or the materials of construction, certain basic procedures must be followed during assembly to ensure proper operation. While these comments may seem elementary, they are extremely important in achieving a satisfactory seal and minimizing the time required to successfully make up joints. The procedures should be followed whether bolt stresses will be achieved with ordinary stud wrenches, preheating studs, using tensioning devices, using torque wrenches, or using hydraulic wrenches. 5.1 | Inspect the gasket seating surfaces. Look for tool marks, cracks, scratches or pitting by corrosion and make sure that the gasket seating surface is proper for the type of gasket being used. Radial tool marks on a gasket seating surface are virtually impossible to seal regardless of the type gasket being used, therefore every attempt must be made to minimize them. 5.2 | Inspect the gasket. Make sure the material is as specified, look for any possible defects or damage in the gasket. 5.3 | Inspect and clean each stud or bolt, each nut, each washer, and the facing on the flanges against which the nuts will rotate. Look for severe galling, pitting, etc. If any of the above mentioned items are damaged beyond repair, replace the damaged item.

5.7 | Torque the bolts up to a maximum of thirty percent of the final torque value required following the sequence recommended. See Section E for bolting sequence and torques. Number bolts so that torquing requirements can be followed. With any gasket material, it is extremely important to follow a proper bolting sequence. If this sequence is not followed, the flanges can be cocked. Then, regardless of the amount of subsequent torquing, they cannot be brought back parallel. This problem, of course, is maximized on metallic gaskets more so than on non-metallic. 5.8 | Repeat step 5.7, increasing the torque to approximately 50 to 60 percent of the final torque required. 5.9 | Continue with a star pattern of re-torquing all studs or bolts to the desired amount until no further rotation of the nuts can be achieved. This may require several re-torquings since as one stud is torqued it will relieve the stress on the adjacent stud until such time as equilibrium is achieved. 5.10 | On high-pressure, high-temperature applications, it is recommended that the flanges be re-torqued to the required stress after 24 hours at operating pressures and temperatures to compensate for any relaxation or creep that may have occurred.

5.4 | Lubricate all thread contact areas and nut facings. The importance of proper lubrication cannot be over-stressed. No joint should be made up without the proper lubricant being applied to the threaded surfaces and to the nut facings. When flanges will be subjected to high temperatures, the use of an anti-seize compound should be considered to facilitate subsequent disassembly. 5.5 | With raised face and flat face installation, loosely install the stud bolts on the lower half of the flange. Insert the gasket between the flange facing to allow the bolts to center the gasket on the assembly. Install the balance of the bolts and nuts and bring all to a hand-tight or snug condition. 5.6 | If the gasket is being installed in a recess or a groove, center the gasket midway into the recess or the groove. If the joint is vertical it may be necessary to use some cup grease or a few dabs of gasket cement or some other adhesive compatible with the process fluids, to keep the gasket in position until the flanges are tightened.

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Proper Fitting of Wedge Gate Valves

SECTION I Proper Fitting of Wedge Gate Valves

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Proper Fitting of Wedge Gate Valves GENERAL INFORMATION For general information regarding this or any other valve please refer to Section A of this manual.

2.0 INTRODUCTION Fitting of gate valve wedges has a direct effect on the overall performance and longevity of the valve. Occasionally, wear or damage may facilitate the need to refit a gate valve. It is recommended that this operation be entrusted only to an experienced valve mechanic. Although it is recommended that this operation be performed in the shop, with correct equipment and proper care, it can be done with the valve in place. The following are suggested procedures and inspection points:

2.0 PROCEDURE 2.1 | New gate valve wedges are furnished with material left on each side to allow for custom fitting. The amount varies with valve sizes from .025” to .050” per side. Insert the wedge into the body after body seats have been finished and check the following points. 2.1.1 | Adequate finish for fitting. Wedge rides high in body seats. If this is not convenient, use inside calipers to check minimum distance between seats in the body and outside calipers to measure minimum distance across seats of wedge at the toe (bottom). Wedges should be polished/lapped to a minimum of 32 rms. Preferred finish is approximately 12 rms. 2.1.2 | Adequate guide clearance to permit seat face contact. Some valves are designed to allow the wedge to be inserted one way only (wide and narrow guides). Otherwise, select the most advantageous orientation of the wedge in the body. Match mark the body and wedge to ensure proper orientation.

2.1.6 | To check the fit, hang the wedge on a dummy stem (or appropriate fixture), insert it into the body, noting any lean of the wedge relative to the body guides and the guide clearance. Hit the end of the dummy stem with a hammer to seat the wedge and mark the body seat on the wedge. A sharp blow on the bottom of the body will free the wedge from the body seats. To emphasize the position of the seal, a thin film of Prussian Blue can be put on the wedge seat face prior to inserting into the body. 2.1.7 | When the wedge is finally fitted to the body and is resting between the seats (not hammered into place), there should be a small clearance at the toe (bottom), depending on the size and pressure class of the valve (body flexibility). Suggested Toe Clearance

150

Valve Size 300 & 400

600 & up

.0005 - .001

up to 4"

up to 6"

1 1/2" - 2"

.0015 - .003

5" - 12"

8" - 16"

All

.003 - .005

14" - 16"

18" up

.005 - .007

18" up

The ideal fit is with the wedge seal uniform and narrow (approx. 1/8”) all around. The seal on the wedge should be below the center of the wedge face (wedge riding high). See Figure 1 below. There should be sufficient guide clearance so that the wedge can seat on both sides. Also, there should be adequate T-head clearance to permit the wedge and stem to be self-aligning.

2.1.3 | Check that the center line of the wedge and body seats are oriented such that the stem T-head has proper clearance to align itself at assembly. 2.1.4 | Mount the wedge in a machine (grinder, boring mill or lathe), on a 10° angle face plate (adjustable or not). Center line of the seat face must be parallel to the guides. 2.1.5 | By trial and error, plus minute adjustments of the wedge angle and the orientation of its center line, fit the wedge to the body seats, by removing small amounts of surface material from the wedge. www.cranecpe.com

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Gear and Motor Actuated Valves

SECTION J Gear and Motor Actuated Valves

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Gear and Motor Actuated Valves 1.0 THEORY OF OPERATION

3.0 MAINTENANCE

Most valves, which are located in an accessible environment, are actuated by a manual handwheel mounted directly on top of the valve. When the valve size or differential pressure is so great that the handwheel size cannot keep the operating handwheel pull within customer reasonable limits, then a bevel gear should be mounted on the top-works. In addition, many customers require remote operation or operating times that are not possible with manual handwheels, in this case Electric Motor Actuators (EMO’s) can be used.

The gear or electric actuator itself should never require disassembly and it is recommended that this be done only by the Actuator manufacturer. If it becomes necessary to disassemble the valve, the actuator assembly must be removed first.

NOTE: Actuator limit and torque settings are factory set during valve testing for ASME cold working pressure tests. Additional adjustment may be required in the field. Contact Pacific® with any questions. WARNING! Do not use excessive air wrench torque or snipes on handwheels as the gearing or valve stem could be damaged!

2.0 INSTALLATION

The preferred orientation for Pacific® gear and motor actuated valves is in horizontal pipelines with the stem in a vertical position. When installed in any other position, motor actuated valves should be supported by means of a support clamp around the motor mounting plate. Please contact Pacific® when specifying an actuated valve with an orientation different than that listed above.

3.1 Preventive Maintenance

3.1.1 | With the actuator removed from the valve, examine the stem and actuator drive nut for thread wear, galling or binding. 3.1.2 | If excessive wear is evident, worn parts should be replaced.

Warning! Ensure that the electric motor actuator is wired correctly and phased properly prior to operation. Do not allow the valve to travel in the wrong direction (when phased is reversed). This can result in damage to the valve and void all valve warranties.

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Gear and Motor Actuated Valves DISASSEMBLY • Remove operator mounting bolts or stud/nuts 16A and 98A from mounting plate or mounting adapter 120. • Attach a support sling around operator 200 and prevent rotation. • Turn handwheel closed to turn operator off from stem and then lift gear operator off. In the case of an Electric Motor Operator it may be necessary to disengage or “declutch” the motor before using the manual handwheel. The Electric Motor Operator manufacturer’s manual should detail this procedure. • Remove spacer and coupling if used. (Not shown) • NOTE: Prior to the disassembly of any valve equipped with an Electric Motor Operator, ensure that all electrical sources have been disconnected and the appropriate lockout/ tagout procedures have been used. • Proceed with disassembly instructions given in the appropriate valve maintenance instructions.

ASSEMBLY • Install spacer and coupling if used. (Not shown) • Lift gear operator carefully over valve stem and while preventing operator from rotating, turn handwheel open until operator aligns over mounting holes. • Loosely install mounting bolts or stud/nuts 16A and 98A on mounting plate or mounting adapter 120 and then check that stem 70 operation does not bind. • Torque mounting bolts or stud/nuts 16A and 98A while valve is in open position. • Set torque and limit switches in accordance with the instruction manual for the applicable operator. • For all gate and globe style valves upon valve closing, the torque switch should be set to trip first.

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Notes

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Crane ChemPharma & Energy Crane Energy Headquarters 4526 Research Forest Drive, Suite 400 The Woodlands, Texas 77381 U.S.A Phone: +1 936-271-6500 Fax +1 936-271-6510 www.cranecpe.com

Pacific Valves Customer Service 3201 Walnut Avenue Signal Hill, CA 90755 U.S.A Phone: +1 562-426-2531 Fax +1 562-595-9717

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