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November 14, 2007

Piping Material Specification Terms

The following article lists some simple, informative tips that will help you have a better experience with Piping Material Specification Terms.

Compact Gate Valve

Compact gate valves are used for economic reasons. They are cheaper and weighs lesser. Lesser weight in a piping system means fewer supports and therefore, savings. It is used for small size gate valves up to 1-½” although the standards supports its use up to 2”. This is because most projects have socketwelds only up to 1- ½” NPS. The reference for these valves is API 602.

Full Port(Bore) vs. Reduced Port (Bore) vs. Standard Port(Bore)

The full port valve has an inlet and an outlet size equal to the ball opening size. In contrast, a reduced port has a bigger inlet tapering towards the smaller ball opening. The outlet tapers toward a bigger exit. Standard port is actually another name for reduced port.

Reducers

Reducers may either be concentric or eccentric. However, for small reducers, most often than not, they are concentric because they are made of forged material like A105. With Caltex specifications, small reducers are not distinguished (as to whether they are concentric or eccentric), which can be confusing.

 

Piston Lift

This type of check valve uses the piston in the form of a cylinder, with its lower end shaped to form a seating face. The cylindrical part fits into the shell. The piston must be long enough to ensure that it is well guided over the distance of its travel. Likewise, piston-type check valves shall have an integral or separate guide of sufficient length to ensure effective guidance over the full length of the piston travel.

Tanged Insert

A type of gasket used as a substitute for asbestos.

 

SC, BC

Check valves do not have bonnets, instead covers are used. SC stands for Screwed Cover while BC means Bolted Cover. Screwed Cover is usually used for low pressure service, instrument air and water. Bolted Covers can be used for higher pressure service.

Bonnet

Bonnet is a valve body closure component that contains an opening for the stem. Attachment of bonnet to the body shall be either of the following types:

Bolted bonnet (BB) - A valve construction in which the bonnet is bolted in the body. A mating flange between the body and bonnet shall be installed. This flange shall be of a suitable shape to provide adequate strength. The joint between the body and bonnet shall be of a type that confines the gasket.

Screwed bonnet (SB) - A valve construction in which the body and the bonnet are attached using by a threaded end. There are two types namely:

Threaded-in bonnet - a bonnet that is threaded into the body.

Threaded-over bonnet - a bonnet into which the body is threaded.

Screwed bonnet is mainly used for instrument air, potable water lines and very low pressure service such as CL125 and CL150. Some projects require seal welding for this type of valve construction.

Union bonnet (UB) - A valve bonnet that is fastened to the valve body by means of a union nut. Union bonnet valve construction may be used for very low pressure service.

Welded bonnet (WB) - A valve construction wherein the bonnet is welded to the body. This type of bonnet is rarely used but is applicable for very toxic fluid service (Type M). Maintenance or replacement of the unit is difficult for the welding is uneasy to remove.

Pressure seal bonnet (PSB) - A bonnet closure assembly in which internal fluid pressure force on the bonnet increases the compressive loading on the sealing gasket. This type of assembly is very expensive and usually used for very high pressure services (over 900 psi).

Gland
A part of a valve that provides compression on the packing to prevent leakage.

OS&Y (Outside Screw and Yoke)

A valve design where in the packing is between the stem threads and the valve body. Yoke is a part of a valve assembly used to position the stem nut to mount the valve actuator.

ISS (Inside Screw and Stem)

This assembly is of two types namely:

Inside screw non-rising stem - A type of gate valve design where in the disc rises on the threaded part of the stem instead of the stem rising through the bonnet. The stem does not rise or descend as the stem is turned.

Inside screw rising stem - A type of gate valve or globe valve design where in the stem has both rotary and axial motions and rises as the stem is turned. The stem threads are between the stem packing and closure member.

Stem - a valve component to which motion is impaired outside the valve assembly to move the closure member inside the valve.

Seats

There are two seats in a valve: the disc seat and the body seat. The disc seat is softer and removable. The body seat is usually harder than the disc. All disc seats can be removed unlike body seats.

There's a lot to understand about Piping Material Specification Terms. We were able to provide you with some of the facts above, but there is still plenty more to write about in subsequent articles.

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November 16, 2007

OVERVIEW OF PIPING LAYOUT


1 What is Piping Layout? (Purpose of Piping Layout)

To determine the following:

a. Equipment Layout
b. Construction & Structure (configuration & elevation)
c. Equipment (vessel) nozzle orientation, platform, lug & ladder (location & configuration)
d. Piping Arrangement (line routing, location of piping component & instrument)
e. Electrical/ Instrument cable layout, location local panel, junction boxer lighting, etc.
f. Location of buried piping & drip funnels.

2 Related Work for Piping Layout

a. Plot Plan Preparation
b. Design Info Preparation
c. Piping Strength Analysis
d. Piping Material Take-off
e. Piping Drawing Preparation

3 Data Gathering & Verification

a. Collect necessary Documents
b. Verify Accuracy

4 Preparation of Basic Piping Layout Plan

a. Piping Conceptual Routing
b. Equipment Layout
c. Civil/Structure Formation
d. Valve & Instrument Assembly
e. Electrical/Instrument Cable Routing
f. Fire Escape Routes/ Maintenance Area

5 Preparation of Breakdown of Piping Layout

a. By Facilities
b. By Section of Facilities
c. By Structure
d. By Unit

6 Determination of Area of Priority

a. Tight Schedule for Design Info. Issuance
b. Some connection with other company (Hook-Up)
c. Plot Plan to Fix Early
d. Complete Set of Documents
e. Having Lines w/ High Temperature: High Pressure (material to be use is high Grade (special) material & Large Size)
f. Piping Material to be Ordered Early

7 Preparation of Piping Layout

7.1 Piping Design Input Data   (Before layout preparation)

a. Plot Plan
b. Process Flow Diagram, Piping & Instrument Diagram & Utility Flow Diagram
c. Line Index
d. Client Standard
e. Piping Material Specification (line classes)
f. Equipment Skeleton Drawing (Pressure vessel except H/E)   
g. Piping General Specifications
h. Standard Drawing (standard pipe support, max. supporting span, & typical detail
i. Existing Job Ref. Vendor Catalog (pump/comp.)
j. Instrument Data Sheet Dwg & Catalog
k. Data Sheet (H/E)
l. Vendor Catalog/ Existing Job Ref.
m. Layout Procedure

7.2 Piping Design Input Data   (During layout preparation)

7.2.1 Supplied from instrument department

a. Cable Routing (main/ pipe rack/sub pipe rack & sleeper)
b. Vendor Drawings
c. Tie-in Dimension List
d. Air Supply Tapping Point
e. Piping/Instrument Split of Work

7.2.2 Supplied from Electrical Department

> Cable Routing (main/ pipe rack/sub pipe rack & sleeper)

7.2.3 Supplied from Fire Fighting Section

a. P & ID
b. General Arrangement
c. Typical Detail (Hydrant; monitor)
d. Vendor Drawings

7.2.4 Supplied from Package Department

a. Package Equipment Vendor Drawing
b. Package P & ID

7.2.5 Supplied from Piping Department

a. Piping Special Component Vendor Drawing
b. LC/LG Arrangement

7.2.6 Supplied from Civil Department

> Site Grading Plan

7.3 Piping Design Output Data   (During layout preparation)

7.3.1 Supply to Equipment Department

a. Equipment Installation Height
b. Nozzle Orientation
c. Platform & Ladder
d. Support Lug
e. LG/LC Arrangement
f. Nozzle Force & Moment

7.3.2 Supply to Civil/ Structural Department

a. Equipment Installation Height
b. Pipe Rack
c. Structure
d. Table Top
e. Sleeper
f. Pump Foundation
g. Pipe Support
h. Drip Funnel Location
i. Operating Platform (Misc.)
j. Pipe Trench
k. Embedded Plate
l. U/G Pressure Piping Layout
m. Spill Wall
n. Pit Information
o. Pit Support Foundation Location

7.3.3 Supply to Instrument Department

a. LG/Visual Direction
b. LC Visual Direction
c. CV Direction

7.3.4 Supply to Furnace (Optional)

a. Platform & Stair or Ladder
b. Pipe Support
c. Burner Orientation

7.3.5 Supply to Package Equipment (Optional)

> Package Unit Orientation

7.3.6 Supply to Rotary

> Rotary Machine Orientation

7.4 Piping Design Output Data   (After layout preparation)

> Final Piping Layout

8 Checking of Piping Layout

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November 17, 2007

Chemical Engineering Software

Pressure Drop via the Karman Method
Mr. Daan Le Roux of SASOL shares his spreadsheet based on the Karman pressure drop method as featured in the June 2006 edition of CEP Magazine.
 
Chemical Plant Cost Estimation
Ever wonder what really goes into estimating the cost of a world scale chemical production facility?  Here is a sample of such a spreadsheet used for a project in India.  Build your own from this sample which includes virtually all of the economics that need to be considered.
 
2005 MS Excel Spreadsheet Competition
These are some of the best entries received during the 2005 spreadsheet competition:

Steam Tracing (Winner)
Vapor Pressure from Antoine Coefficients
Column Diameter and HETP Calculation
Packed Column Scrubber Design
Reactor Particle Size and Velocity Calculation
Condensate Line Sizing

 
Two Phase Flow in Pipes
Download this easy to use spreadsheet to estimate pressure losses in pipes with two-phase flow.
 
Various Chemical Engineering Calculation Spreadsheets
Zip file with Excel spreadsheets including calculations such as: unsteady state heat transfer, horizontal vessel calibration data, catenary equations, compressible flow calculations, cone and circle geometry, control valve sizing, dewpoints of acidic gases, duct calculations, orifice sizing, packed scrubber design, flat plate deflections, pump performances, and rectangular weir flow.  These spreadsheet provided by Mr. Neil Stone of Esco Engineering.
 
Filtration Spreadsheets from Dr. Richard Holdich
Calculations include specific surface area, compressible cake at constant pressure, compressible cake at constant flow, power law equation, pressure leaf clarification costing, and rotary vacuum filtration.  Complete with documentation.   Files are in Excel format, download as a zip file.
 
Vessel Pressure via the SRK Equation of State
Use this Excel spreadsheet to find the pressure inside a vessel via the SRK equation of state (EOS).  Brought to you by the Direction of Software Corner, Somak Mukherjee
 
Fired Furnace Excess Air Calculation
Calculate the excess air volume required for a hydrocarbon furnace with the Orsat analysis.  Excel spreadsheet provided by the Direction of Software Corner, Somak Mukherjee
 
Financial Calculation Spreadsheet
You know what a chore it is to optimize a chemical process and get to the bottom line.  Then you make some changes and have to do it all over again.  Here a great spreadsheet that should ease you pain substantially!
 
Water Properties Program
Download this small helper program so that you have the properties of water at your fingertips.  The link above is a direct link to the executable file.  This program was graciously donated the Resource Page by Pablo Coronel at pcorone@unity.ncsu.edu
 
Physical Properties DataBank AddIn for Excel
This Excel AddIn contains a moderate databank of chemicals and a nice array of physical properties.  It also contains Excel functions that can be pasted into worksheets (be sure you have one open first).  You'll find the AddIn under the Tools menu.
 
Units Conversions
These handy little programs are just about everywhere.  There a good and bad side to this one.  The bad side is that is runs in DOS, the good side is that it shows many different conversions at once.
 
The Reactor Lab
A fantastic program designed to help students gain a better understanding of reactor simulations…and best of all….it's free!
 
Insulation Calculation Programs
Two programs included to help you with insulation calculations.  The "Economic Thickness Calculator" will recommend the appropriate insulation thickness based on energy savings.  The "Insulated Pipe Temperature Prediction Spreadsheet" will help you predict the temperature inside a pipe and linear heat loss.
 
Vapor Pressure of Binary Liquid Mixtures
Use this spreadsheet to find the vapor pressure of binary liquid mixtures.   Based on fugacity corrected values from Antoines Law, this spreadsheet give accurate results with minimal inputs.
 
Physical Property Data Spreadsheet
This spreadsheet for Excel 97 contains data such as boiling and freezing points, critical data, density, vapor and liquid heat capacities, liquid viscosity, vapor pressures, and more for 468 chemicals.
 
Cooling Tower Calculator
This handy little DOS program will calculate the tower characteristic or cold water temperature for a given cooling tower with just a few inputs.  (See Cooling Tower article here at the "Resource Page")
 
Pipe Size Optimization for Carbon and Stainless Steel Pipes
This simple spreadsheet will calculate the most economical pipe diameter for a system based on flowrate, fluid density, and fluid viscosity.  The sheet is to be used for turbulent flow in carbon or stainless steel pipes.  It is designed to run on Excel 97 or higher and utilizes the Solver function so it must be installed as well.
 
Validating Binary VLE Data
Check the thermodynamic consistency of your binary VLE data with this easy to follow analysis.  Complete with spreadsheet to save you time!
 
Costing Distillation Columns
Enter some basic data and this EXCEL ADD-IN will do the rest.  Check out the specifications of the program.

Source:http://www.cheresources.com/software.shtml

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March 9, 2008

Classification of Carbon and Low-Alloy Steels

Abstract: 
The American Iron and Steel Institute (AISI) defines carbon steel as follows:Steel is considered to be carbon steel when no minimum content is specified or required for chromium, cobalt, columbium [niobium], molybdenum, nickel, titanium, tungsten, vanadium or zirconium, or any other element to be added to obtain a desired alloying effect; when the specified minimum for copper does not exceed 0.40 per cent; or when the maximum content specified for any of the following elements does not exceed the percentages noted: manganese 1.65, silicon 0.60, copper 0.60.

Steels can be classified by a variety of different systems depending on:

  • The composition, such as carbon, low-alloy or stainless steel.
  • The manufacturing methods, such as open hearth, basic oxygen process, or electric furnace methods.
  • The finishing method, such as hot rolling or cold rolling
  • The product form, such as bar plate, sheet, strip, tubing or structural shape
  • The deoxidation practice, such as killed, semi-killed, capped or rimmed steel
  • The microstructure, such as ferritic, pearlitic and martensitic
  • The required strength level, as specified in ASTM standards
  • The heat treatment, such as annealing, quenching and tempering, and thermomechanical processing
  • Quality descriptors, such as forging quality and commercial quality.

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Carbon Steels

The American Iron and Steel Institute (AISI) defines carbon steel as follows:

Steel is considered to be carbon steel when no minimum content is specified or required for chromium, cobalt, columbium [niobium], molybdenum, nickel, titanium, tungsten, vanadium or zirconium, or any other element to be added to obtain a desired alloying effect; when the specified minimum for copper does not exceed 0.40 per cent; or when the maximum content specified for any of the following elements does not exceed the percentages noted: manganese 1.65, silicon 0.60, copper 0.60.

Carbon steel can be classified, according to various deoxidation practices, as rimmed, capped, semi-killed, or killed steel. Deoxidation practice and the steelmaking process will have an effect on the properties of the steel. However, variations in carbon have the greatest effect on mechanical properties, with increasing carbon content leading to increased hardness and strength. As such, carbon steels are generally categorized according to their carbon content. Generally speaking, carbon steels contain up to 2% total alloying elements and can be subdivided into low-carbon steels, medium-carbon steels, high-carbon steels, and ultrahigh-carbon steels; each of these designations is discussed below.

As a group, carbon steels are by far the most frequently used steels. More than 85% of the steel produced and shipped in the United States is carbon steel.

Low-carbon steels contain up to 0.30% C. The largest category of this class of steel is flat-rolled products (sheet or strip), usually in the cold-rolled and annealed condition. The carbon content for these high-formability steels is very low, less than 0.10% C, with up to 0.4% Mn. Typical uses are in automobile body panels, tin plate, and wire products.

For rolled steel structural plates and sections, the carbon content may be increased to approximately 0.30%, with higher manganese content up to 1.5%. These materials may be used for stampings, forgings, seamless tubes, and boiler plate.

Medium-carbon steels are similar to low-carbon steels except that the carbon ranges from 0.30 to 0.60% and the manganese from 0.60 to 1.65%. Increasing the carbon content to approximately 0.5% with an accompanying increase in manganese allows medium carbon steels to be used in the quenched and tempered condition. The uses of medium carbon-manganese steels include shafts, axles, gears, crankshafts, couplings and forgings. Steels in the 0.40 to 0.60% C range are also used for rails, railway wheels and rail axles.

High-carbon steels contain from 0.60 to 1.00% C with manganese contents ranging from 0.30 to 0.90%. High-carbon steels are used for spring materials and high-strength wires.

Ultrahigh-carbon steels are experimental alloys containing 1.25 to 2.0% C. These steels are thermomechanically processed to produce microstructures that consist of ultrafine, equiaxed grains of spherical, discontinuous proeutectoid carbide particles.

High-Strength Low-Alloy Steels

High-strength low-alloy (HSLA) steels, or microalloyed steels, are designed to provide better mechanical properties and/or greater resistance to atmospheric corrosion than conventional carbon steels in the normal sense because they are designed to meet specific mechanical properties rather than a chemical composition.

The HSLA steels have low carbon contents (0.05-0.25% C) in order to produce adequate formability and weldability, and they have manganese contents up to 2.0%. Small quantities of chromium, nickel, molybdenum, copper, nitrogen, vanadium, niobium, titanium and zirconium are used in various combinations.

HSLA Classification:

  • Weathering steels, designated to exhibit superior atmospheric corrosion resistance
  • Control-rolled steels, hot rolled according to a predetermined rolling schedule, designed to develop a highly deformed austenite structure that will transform to a very fine equiaxed ferrite structure on cooling
  • Pearlite-reduced steels, strengthened by very fine-grain ferrite and precipitation hardening but with low carbon content and therefore little or no pearlite in the microstructure
  • Microalloyed steels, with very small additions of such elements as niobium, vanadium, and/or titanium for refinement of grain size and/or precipitation hardening
  • Acicular ferrite steel, very low carbon steels with sufficient hardenability to transform on cooling to a very fine high-strength acicular ferrite structure rather than the usual polygonal ferrite structure
  • Dual-phase steels, processed to a micro-structure of ferrite containing small uniformly distributed regions of high-carbon martensite, resulting in a product with low yield strength and a high rate of work hardening, thus providing a high-strength steel of superior formability.

The various types of HSLA steels may also have small additions of calcium, rare earth elements, or zirconium for sulfide inclusion shape control.

Low-alloy Steels

Low-alloy steels constitute a category of ferrous materials that exhibit mechanical properties superior to plain carbon steels as the result of additions of alloying elements such as nickel, chromium, and molybdenum. Total alloy content can range from 2.07% up to levels just below that of stainless steels, which contain a minimum of 10% Cr.

For many low-alloy steels, the primary function of the alloying elements is to increase hardenability in order to optimize mechanical properties and toughness after heat treatment. In some cases, however, alloy additions are used to reduce environmental degradation under certain specified service conditions.

As with steels in general, low-alloy steels can be classified according to:

  • Chemical composition, such as nickel steels, nickel-chromium steels, molybdenum steels, chromium-molybdenum steels
  • Heat treatment, such as quenched and tempered, normalized and tempered, annealed.

Because of the wide variety of chemical compositions possible and the fact that some steels are used in more than one heat-treated, condition, some overlap exists among the alloy steel classifications. In this article, four major groups of alloy steels are addressed: (1) low-carbon quenched and tempered (QT) steels, (2) medium-carbon ultrahigh-strength steels, (3) bearing steels, and (4) heat-resistant chromium-molybdenum steels.

Low-carbon quenched and tempered steels combine high yield strength (from 350 to 1035 MPa) and high tensile strength with good notch toughness, ductility, corrosion resistance, or weldability. The various steels have different combinations of these characteristics based on their intended applications. However, a few steels, such as HY-80 and HY-100, are covered by military specifications. The steels listed are used primarily as plate. Some of these steels, as well as other, similar steels, are produced as forgings or castings.

Medium-carbon ultrahigh-strength steels are structural steels with yield strengths that can exceed 1380 MPa. Many of these steels are covered by SAE/AISI designations or are proprietary compositions. Product forms include billet, bar, rod, forgings, sheet, tubing, and welding wire.

Bearing steels used for ball and roller bearing applications are comprised of low carbon (0.10 to 0.20% C) case-hardened steels and high carbon (-1.0% C) through-hardened steels. Many of these steels are covered by SAE/AISI designations.

Chromium-molybdenum heat-resistant steels contain 0.5 to 9% Cr and 0.5 to 1.0% Mo. The carbon content is usually below 0.2%. The chromium provides improved oxidation and corrosion resistance, and the molybdenum increases strength at elevated temperatures. They are generally supplied in the normalized and tempered, quenched and tempered or annealed condition. Chromium-molybdenum steels are widely used in the oil and gas industries and in fossil fuel and nuclear power plants.

Via: http://www.key-to-steel.com/ViewArticle.asp?ID=62#top

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March 28, 2008

ABBREVIATIONS FOR PIPING DRAWINGS and INDUSTRIAL CHEMICALS


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April 15, 2008

Choosing the Right Valve

If you are an engineering, you my like this article.You will learn:
Choosing the Right Valve
°Basic Gate Valve Design
°Basic Globe & Angle Valve Design
°Gate Valve Seating Designs
°Seating Materials
°Globe Valve Seating Designs
°Disc-Stem Connections
°Variations in Stem Operations
°Bonnet & Bonnet Joint Characteristics
°Basic Check Valve Designs
°Basic Ball Valve Designs
°Basic Butterfly Valve Designs
°The Common Materials of Which Valves Are Made
°How to Read Service Rating Marks

Let's start

What's So Important About Choosing the Right Valve?

Valves have long been more than just a simple device for turning on and shutting off flow.  Valve design has kept in step with industrial progress - the development of piping techniques, and the ever-growing list of fluids for processing, power, and finished product.

Progress in valve design puts at the piping engineer's elbow a great variety of valve types, each with some special qualification for service.  From these he may choose the right one to provide dependable and economical performance in each particular need.

It's a case of carefully matching up the valve's service characteristics with the service requirements.  It's a matter of knowing every detail of the job to be done - working pressure, temperature, fluid, volume of flow, corrosive elements, valve operating cycle, etc.  Other equally vital considerations are the original valve cost, installation cost, and, of course, the cost of maintenance.

Crane Co., as the world's leading valve manufacturer and supplier, helps customers with the problems of valve selection every day.  With this vast background of experience, Crane presents here as a helpful refresher for specifiers and buyers, the more important elements involved in choosing the right valve for the right job.
 
 
 

Principal Valve Types

Gate Valve

Commonly used in industrial piping, this type of valve, as a rule, should be used as a stop valve…to turn on and shut off the flow, as opposed to regulating flow.  It gets its name from the gate-like disc which operates at a right angle to the path of flow.
 
 

Globe and Angle Valves

The flow through globe valves follow a changing course, thereby causing increased resistance to flow and considerable pressure drop.  Because of the seating arrangements, globe valves are the most suitable for throttling flow.  The valve is named after its globular body.

Angle valves, similar in principle and a companion line to the globe, are designed to permit a 90 degree turn in piping and are less resistant to flow.
 
 

Check Valve

Sometimes referred to as the non-return valve, the check valve stops backflow in the piping.  Unlike the gate and globe valves, this simplest of types operates automatically.
 
 

Ball Valve

Unique in design, this valve controls the flow of a wide variety of fluids.  It can be opened or closed in a quarter-turn of the operating handle.  The name "ball" is derived from the ball-shaped disc located within the body.  A hole through the center of this disc provides the straight-through flow which is characteristic of ball valves. Light and durable, these are the valves that are playing increasingly important roles in our nation's missile projects, as well as in industry and commercial buildings.
 
 

Butterfly Valve

Here's a valve that is extremely durable, efficient and reliable.  The butterfly valve derives its name from the wing-like action of the disc which operates at right angles to the flow.  Its chief advantage is a seating surface which is not criticalThe reason for this being the disc impinges against a resilient liner to provide bubble tightness with low operating torque.

 

 

Basic Gate Valve Design
…how it should be used

 

Gate valves are by far the most widely used in industrial piping.  That's because most valves are needed as stop valves - to fully shut off or fully turn on flow - the only job for which gate valves are recommended.

Gate valves are inherently suited for wide-open service.  Flow moves in a straight line, and practically without resistance when disc is fully raised.

Seating is perpendicular or at right angle to the line of flow - meets it head on.  That's one reason why gate valves are impractical for throttling service and for too frequent operation.

For instance, a 6-inch gate valve holding fluid at 300 psi, puts a load of over 4 tons on one side of the disc, if there is only atmospheric pressure on the other.  While seated tight, there's no wear or undue strain on disc or seats.  But each time the valve is "cracked open," there's a threat of wire drawing and erosion of seating surfaces by the high-velocity flow.

Repeated movement of disc near point of closure under high-velocity flow, may create a drag on seating surfaces and cause galling or scoring on downstream side.  A slightly opened disc may cause turbulent flow with vibration and chattering of disc.

A gate valve usually requires more turns - more work - to open it fully.  Also, unlike many globe valves, the volume of flow through the valve is not in direct relation to number of turns of handwheel.

Since most gate valves used have wedge disc with matching tapered seats, refacing or repairing of the seating surfaces is not a simple operation.

CONCLUSION:  Gate valves, while not designed for throttling or too frequent operation are generally ideal for services requiring full flow or no flow.
 
 

 

Gate valves are not designed for throttling

In a slightly opened position high-velocity flow will cause wire drawing and erosion of seating surfaces in gate valves.

Repeated movement of disc near point of closure under high-pressure flow may gall or score seating surfaces on downstream side.

Slightly opened disc in turbulent flow may cause troublesome vibration and chattering.

 

 

Basic Globe and Angle Valve Design
…highly essential to piping

 

Unlike the perpendicular seating in gate valves, globe valve seating is parallel to the line of flow.  All contact between seat and disc ends when flow begins.  These are advantages for more efficient throttling of flow, with minimum wire drawing and seat erosion.

The directly proportionate relation of size of seat opening to number of turns of handwheel, a distinctive feature of plug-type globe valves, permits close flow regulation.  An operator can gauge the rate of flow by the number of turns of the wheel.

Shorter disc travel - with fewer turns required to operate globe valves - saves considerable time and work - also wear on valve parts.

Whatever wear occurs as the result of frequent or severe operation presents less of a maintenance problem than in gate valves.  Seat and disc in most globe valves can be repaired without removing the valve from the pipe line.

CONCLUSION:  Globe valves, while not recommended where resistance to flow and pressure drop would be objectionable, are generally ideal for throttling, and preferable for frequent operation.
 

 

 

Basic Angle Valve Design

The angle valve effectively utilizes globe valve seating principle while providing for a 90 degree turn in piping.  It is less resisting to flow than the globe valve it displaces.  Requires fewer joints;  saves makeup time and labor.

 

 

Gate Valve Seating Designs…

 

 Solid Wedge Disc

The most widely used disc in gate valves - the solid wedge-shaped disc - with matching tapered body seating surfaces.  Favored for its strong, simple design and single part.

Can be installed in any position without danger of jamming due to misalignment of parts.

Ideal for steam service, and well suited for water, air, oil, gas, and many other fluids.

Most practical for turbulent flow because there's nothing inside to vibrate and chatter.

Refacing of the tapered disc surfaces isn't easy, but there's little need for it is valve is used fully opened or fully closed.

Might be subject to some sticking when subjected to extreme temperature changes where body contracts more than disc.  For such conditions, Crane flexible wedge disc is recommended.
 
 

Double Disc

This parallel-faced double disc makes closure by descending between matching seats in valve body.  As the valve is being closed, a lower spreader (or in some cases, a disc wedge) strikes a stop in the bottom of the body.  Further closure brings the upper spreader into contact with the lower spreader so that the discs are forced outward against the seats.

First opening movement releases discs, and continued operation raises them clear of seat openings.

Widely used on water service, in waterworks and sewage disposal plants;  also on oil and gas, in cross-country pipe lines.

Generally unsuited for steam.  Rapid expansion and high velocity of steam flow tend to vibrate loose internal parts in disc assembly, hastening wear.

Exposure of closed valve to rise in external temperature may cause dangerous increase in internal pressure, if non-compressible liquid is trapped between discs.

Because discs and body seats are perpendicular and parallel, repairing or refacing to compensate for wear is easier than on a tapered wedge disc.

Should be installed with stem above horizontal for best results.  Many spreader mechanisms are subject to jamming when installed with stem below horizontal line.

 

 

Their Service Characteristics

Flexible Wedge Disc

Developed especially to overcome sticking in high-temperature service with extreme temperature changes.  The shape of the flexible disc can be likened to two wheels on a very short axle.  The "axle" or spud at the center of the disc is amply strong to carry the two halves of the disc together at all times…and yet, it permits a degree of action between them.  It is this "flexibility" that makes the disc tight on both faces over a wide range of pressures…prevents sticking during temperature changes, and assures minimum operating torque.

Although each disc face can move independently of the other…up to two full degrees…the construction is one-piece.  There are no loose parts to cause harmful vibration.
 
 

Split Wedge Disc

A 2-piece, wedge disc that seats between matching tapered seats in body.

Spreader device is simple, and integral with disc halves.

When closing, last turn of handwheel forces discs against the seats.  When opening, the first turn releases the discs from the seats.
 

 

 

Seating Materials…
Key to valve performance
 
 The seat and disc constitute the "heart" of a valve;  do most of its work.  The material from which these parts are made, therefore, becomes important.  The tougher the service, the more severe the demand on seating.  Valve manufacturers recognize this fact by providing a wider choice of seating materials as valves go up the pressure-temperature scale or are offered for more rigorous service.

For relatively low pressure and temperatures and for ordinary fluids, seating materials are not a particularly difficult problem.  Bronze and iron valves usually have bronze or bronze-faced seating surfaces, or iron valves may be all iron.  Nonmetallic "composition" discs are available for tight seating on hard-to-hold fluids such as air or gasoline.

As pressures and temperatures increase or as the service becomes severe, careful consideration must be given to many factors, no one which can be overemphasized to the detriment of others.  Long, trouble-free life requires the proper combination of hardness, wear-resistance, resistance to corrosion, erosion, galling, seizing, and temperature.  Nor does it follow that a satisfactory combination in one instance will serve equally well in all others.  Type of valve is a limiting factor, too.

Selection of seating materials for corrosive fluids, regardless of pressure-temperature, is almost endless.  Included are many types of alloys, as well as linings or coatings of many kinds.
 
 

 

Valve Catalog your best guide

Safest policy in specifying seating materials is in close adherence to valve manufacturer's recommendations, usually found in catalogs, otherwise supplied on request.

 

 

Globe Valve Seating Designs..

Plug Type Disc

Long taper with corresponding seat, giving a wide area of seating contact, makes the plug-type disc superior to all others for severe throttling service, such as blow-off, soot-blower, boiler feed.

Because of wide seat bearing, most cuts and nicks by dirt, scale, and other foreign matter in flow are seldom big enough to cause leakage.

Plug disc shape, in proper combination of metals for service, is most effective in resisting erosive effects of close throttling.

Construction permits replacement of seat if necessary.
 
 

 

Conventional (ordinary) Disc

A good seating design for many not-too-severe services, but not for close throttling.

Disc has relatively narrow contact with body seat - virtually a line bearing.  This narrow metal area, in closely throttled high-velocity flow, is subject to erosion and wire-drawing.

Deposit of particles of foreign matter on seat makes tight closure virtually impossible.

Yet uniform deposit on seat, such as coking action in oil refineries, is more easily broken down by the narrow bearing.  It makes a tight metal-to-metal contact easier than a wide seat.

Seat and disc can be conveniently serviced.

 

 

Needle Point Disc and Seat

Needle point valves are designed to give fine control of flow in small-diameter piping.  Their name is derived from their sharp-pointed conical disc and matching seat.  They come in globe and angle patterns, in bronze and steel, and find usage on steam, air, water, oil, gas, light liquid, fuel oil, and similar services.

Stem threads are finer than usual so that considerable movement of stem is required to increase or decrease opening through seat.

Usually, these valves have reduced seat diameter in relation to pipe size.
 

 

 

Their Service Characteristic

 Composition Disc

A useful design in bronze and iron valves for adaptability to many services and for quick repairs.

Discs available in compositions suitable for steam, hot water, cold water, oil, air, gas, gasoline, and many other fluids.  Disc change is quickly made with slip-on disc holder.

Highly regarded for dependable, tight seating on hard-to-hold fluids such as compressed air.  Flat face relatively "soft" disc seats against a raised crown in body.

Small particles of foreign matter are imbedded in disc, preventing seat damage and leakage.

Suited for all moderate pressure services except close regulating and throttling, which can rapidly cut out the disc.

 

 

Angle Valve Seating

It is well to note and remember the angle valve when looking for globe valves.  If there's a right angle turn in the line near where you need a valve, an angle pattern gives you important advantages.

It's available with the same seating variations as shown here for globe valves:  plug-type disc, conventional, and composition disc.

Has considerably reduced turbulence, restriction of flow, and pressure drop because flow makes one less change of direction than in globe valve.

Angle valve cuts down on piping installation time, labor, and materials, also reduces number of joints or potential leaks by serving as a valve and a 90 degree elbow.

 

 

Disc-Stem Connections…
important factor in valve selection

 

In Gate Valves

In a gate valve, the sole function of the stem is to raise and lower the disc.  In doing its job, the stem should not be subject to corollary stresses and strains of service conditions on the disc.

Thus, with gate valves, especially those used for higher pressure installations, a relatively loose disc-stem connection is desired.

If the connection were rigid, any side thrust on the disc caused by pressure and flow, would readily be transmitted to the stem, and tend to strain and possibly bend it.

A properly fitted loose connection relieves strain on the stem due to any lateral movement of the disc.
 
 

In Globe Valves

The stem in a globe valve not only raises and lowers the disc, but also must help guide it squarely to its seat.

Thus, unlike a gate valve, the globe valve disc-stem connection must be relatively close fitting to prevent any extreme lateral motion of the disc that would cause it to cock and seat improperly.

But, once the disc and seat are joined, the disc must stop turning while seating is completed by the stem.  This will avoid metal-to-metal friction between disc and seat that would be destructive to seating surfaces.

The solution to this need is a swivel action in globe valve disc-stem connections, which permits true and tight seating without damage to seating surfaces.

 

 

Variations in Stem Operations

 

Although in many valve applications the type of stem operation makes little or no difference, in other cases it can be important.  A simple example of the latter is the need for a self-indicator to show open or closed position, as in the case of rising stem valve, or, conversely, the need for a non-rising stem valve because of lack of head room.  This shows how stem operating designs are adapted to service needs.
 
 

Rising Stem with Outside Screw

On both valves shown here, whether opened or closed, the stem threads always remain outside the valve body.  They are not subjected to corrosion, erosion, sediment, or any elements in the line fluid that might damage stem threads inside the valve body.  Being outside, they can be lubricated easily when necessary.
 
 

Rising Stem with Inside Screw

This is the simplest and most common stem construction for gate, globe, and angle valves in the smaller sizes.  Stem turns and rises on threads inside the valve.  Position of handwheel indicates position of disc - opened or closed.
 
 

Non-rising Stem with Inside Screw

Generally used on gate valves only, this stem does not rise, but merely turns with handwheel.  In turning, the stem threads raise or lower the disc.  Since stem only rotates, packing wear is less.  Ideal where head room is limited.
 
 

Sliding Stem is Often Useful

The sliding stem valve is useful where quick opening and closing are wanted.  A lever takes the place of the handwheel, and stem threads are eliminated.  Available in both gate and globe valves.
 
 

Stuffing Box Designs Featured on CRANE Valves

Stuffing box must effect a tight seal around the stem to retain pressure inside piping system.  Stem must be tight without binding.  Packing is subject to wear and must be periodically compressed and eventually replaced.
 

  1. Packing Nut without Gland

    Used on low-pressure and small-size valves.  With wheel and packing nut removed, this type is easier to repack than ordinary gland type on valves with small diameter stem.
     
     
     

  2. Packing Nut with Gland

    Conventional type packing nut with loose gland.  Gland has small lip at top edge so that it can be pried out with screwdriver tip if jammed all the way down.
     
     
     

  3. Bolted Gland

    Deep stuffing box with two-piece ball-type gland and flange with swing-type eye bolts.  Construction maintains an even load on the packing and prevents binding on the stem even when the gland bolt nuts are pulled up unevenly.
     
     
     

  4. Injection Type

    Add new packing with the twist of a wrench, even under full rated line pressure, and with the disc in any position!  No need to backseat the disc.  The specially designed ball check valve eliminates possibility of packing extrusion.  When the packing reservoir is empty, simply back out the adjustment screw and insert a new pack stick.
     
     
     

  5. Lantern Type

    Superior construction for larger-size high pressure-temperature valves.  Cooling chamber with lantern spacer and three rings of packing below to wipe stem clean before it passes into the sealing rings above.  Two-piece ball-type gland and flange with swing-type eye bolts.

 

 

Bonnet and Bonnet Joint Characteristics
…of gate, globe, and angle valves

 

Which is best?

In choosing valves, the service characteristics of the bonnet joint should not be overlooked.  Bonnets and bonnet joints must provide a leakproof closure for the body.  There are many modifications, but the three most common types are screwed-in bonnet, screwed union ring bonnet, and bolted bonnet.
 

Screwed-in Bonnet

The simplest and least expensive construction, frequently used on bronze gate, globe, and angle valves, and recommended where frequent dismantling is not needed.

When properly designed with running threads, and carefully assembled, the screwed-in bonnet makes a durable pressure-tight seal, suited for many services.  On modified steel valve designs such as the lip-seal valve with a weld around the periphery of the body-bonnet juncture, the screwed-in bonnet withstands even high pressures and temperatures.
 
 

Screwed Union Ring Bonnet

A good choice for quick dismantling and reassembly - yet a strong, well-reinforced joint.

Convenient where valves need frequent inspection or cleaning - also for quick renewal or changeover of disc in composition disc valves.

Separate union ring applies direct load on bonnet to hold a pressure-tight joint with body.  Turning motion used to tighten ring is spent between shoulders of the ring and bonnet.  Hence, the point of seal contact between bonnet and body is less subject to wear from frequent opening of the joint.  Contact faces are less likely to be injured in handling.  Union ring gives the body added strength and rigidity against internal pressure and distortion.  While ideal on smaller-size valves, it is impractical on large sizes.
 
 

Bolted Bonnet Joint

A practical and commonly used joint for larger-size valves or for higher pressure applications.

Adaptable to all types of gasketing.

Multiple bolting, with small diameter bolts, permits equalized sealing pressure without the excessive torque needed to make large threaded joints.  Only small wrenches are needed.

Has practically no limitation for size.  Only the highest pressures and temperatures tax its capacity to permanently hold tight.
 
 

Lip-Seal Bonnet Joint

Crane's lip seal design features simplicity.  The body and bonnet are screwed together until a firm metal-to-metal contact is made between the smoothly machined, flat surfaces on the shoulder of the bonnet and the top of the body.  The shoulder of the bonnet is smaller in diameter than the mating area of the body, thus permitting the use of a fillet form of seal weld around the periphery of the connection.  Dismantling is accomplished by grinding off the fillet weld and unscrewing the bonnet.  The design makes possible compact, relatively lightweight valves ideal for high pressure-temperature services.  Absolute tightness, full seating area, and freedom from bonnet joint maintenance are other advantages.
 
 

CRANE Pressure-Seal Bonnet Joint

Newest and most effective bonnet joint, developed by Crane, for sealing the highest pressures and temperatures, especially in steam service.

Tightness of seal does not depend on nuts, bolts, and threads as in conventional bonnet joints.  Instead, Crane Pressure-Seal bonnet joint utilizes line fluid pressure to seal the joint.  The greater the pressure, the tighter the seal.

The actual joint is inside the valve, and is sealed with a wedge-shaped seal ring.  Internal fluid pressure acting on the entire underside area of the bonnet, is concentrated at the smaller contacting area of the wedge-shaped ring to make a pressure-tight metal-to-metal joint.

Available in gate, globe, angle, check and stop-check valves.

 

 

Basic Check Valve Design
 
 

The Swing Check…companion for gate valves

Swing checks work automatically as shown here.  But whether used in a horizontal line or vertical line for upward flow, they will not function properly unless installed with pressure under the disc.

Flow through swing checks is in a