by Mike Frankel, CPD
February 1, 2010
Some common considerations to think about when selecting service valves other than those needed for the plumbing industry.
This article is intended to help an engineer evaluate generic factors
when selecting appropriate valves for process piping. It is not intended to aid
engineers in the actual design and selection of valves for specific
services.
Also, for purposes of this article the definition of a valve is a mechanical
device designed to precisely control flow of any liquid being piped. Not
covered are check valves, pressure-relief valves and other special-duty valves.
Valves discussed in this article can be classified as on/off service,
throttling service (where it would be used for flow control and preventing
reverse flow) and pressure control. These valves can be operated manually,
remotely or automatically. Related variables include system pressure,
temperature, and chemical variations of the fluid in the systems in which they
are installed.
Codes that apply to these systems (whether operating separately or together)
exist from several bodies, including the American Petroleum Institute, American
Water Works Association, Manufacturers Standardization Society, American
Society of Mechanical Engineers and American Standards Association. Each of
these codes represent general industry, manufacturers, consumers and
engineering societies. There are several other codes that may also apply.
To begin, let’s discuss some of the materials more commonly used in the
manufacturing of valves.
The Bronzes
The bronzes, which are a copper base alloy family of metals, offer a fair to
excellent corrosion resistance in most general service applications such as
steam, water, refined oil and natural gas. They are easily shaped, cast or
forged, and machined.
Within their maximum temperature limitations they are widely used for valves
from 1/8 through 3 inches. Above the 3-inch size, except where required for
specific corrosion resistance, all-bronze valves are seldom used because of
their higher cost as compared to iron body valves. There are two main alloys
used: ASTM B61 and ASTM B62.
ASTM B61.
Commonly known as cast steam or valve bronze, this material is composed of
86-90% copper, 5.5-6.5% tin, 3-5% zinc and 1-2% lead, as well as other
miscellaneous materials. Its physical properties are as
follows:
Trim is the internal component of a valve that is exposed to great
stress, or subject to a combination of erosion and/or corrosion. These include:
A. Stainless steel with 13% chromium (types
4190, 416 and 420), which have high hardness and makes them resistant to
wear and erosion. Valves trimmed with this material, nickel-copper and stellite
are highly recommended for water, steam and gas up to a temperature of 850°F.
B. Stellite is a cobalt-chromium-tungsten
alloy deposited on facings by welding. It is highly recommended for severe
service, most commonly steam.
C. A wide variety of additional materials are
available. Consult manufacturers for severe conditions.
A. Butt weld end connections
are available for only cast steel valves. Appropriate ASA standards should be
specified for their use.
B. Flanged ends allow valves to be
bolted to a piping system. Flanged ends are available for bronze, iron, ductile
iron, cast and forged steels all in accordance with various ASA and ASME
specifications.
C. Hub ends allow attachment to a
piping system by caulking a joint with lead or a gasket material. Hub ends are
available on iron valves, gates and checks.
D. Mechanical ends allow valves to be
bolted to a piping system without leakage and are considered more positive than
hub ends. This joint incorporates a stuffing box principal using a triangular
gasket, held by a gland and bolted to the pipe ends. Mechanical ends use joints
that allow some deflection as well as longitudinal expansion and contraction,
and are best for underground water and gas.
E. Screwed end connections are
furnished with female threaded ends matching the male end of the pipe to which
it is to be joined. It is available in bronze, iron, ductile iron, cast and
forged steel, and limited to smaller valves up to four inches (DN 200) because
of the difficulty in making up the joint.
F. Socket weld ends are available on
small forged-steel valves, those up to two inches (DN100). The pipe to be
welded slips into a socket on the valve. The socket weld has some advantages
over the butt weld, such as not having to tack weld. It is supported and
aligned by the socket, and there is no danger of leaving any welding
obstruction inside the pipe.
G. Solder end is available for brass
or bronze valves used for water, oil and gas having copper tubing as the supply
pipe.
H. Union end for bronze valves
consists of a union nut and a companion nipple. It is particularly useful where
there is a reasonable expectation that the valve has to be replaced.
I. Grooved ends depend on grooves
machined into the body of the valve and the pipe to which it is to be
connected. A split ring with bolts in the perimeter is placed in the grooves
and used as the closure with a gasket added to prevent leakage.
Some of the general considerations that go into the selection of materials for a particular application are as follows:
Gate Valve
The gate valve is the most-popular style in the world for flow control. Gate
valves exist for a single primary purpose: to stop flow. They are sometimes
known as “stop” or “block” valves. The advantage of using gate valves is that,
in the fully open position, they offer almost no resistance to flow. This valve
should not be operated in a partially open position because of potential damage
to the seating surfaces.
Although gate valves are manufactured with virtually every metal, the most
common are bronze, steel and iron. Bronze (or brass) is the easiest to machine
and has the lowest manufacturing cost. It is mostly used for water and utility
service at pressures of 300 psi or lower. Steel is the material choice for
industrial valves. Two types of iron are used for valves: gray or cast iron and
malleable.
The gate valve’s closure element is a member (disk) that slides into a slot in
the body, which closes off the flow. There are three types of disks available:
solid, one-piece flexible and two-piece split.
Butterfly Valve
Butterfly valves are regarded as the oldest valve type used in the
process-control industry and are available in larger sizes — eight inches (DN
200) and up. They control flow using a one-quarter turn disk that rotates 90
degrees. In the closed position, the disk blocks flow. All butterfly valves are
not similar. Quality is important in the manufacturer of these valves because
closure depends on a precise fit. High-performance valves can be used for
bubbletight shutoff and precise throttling. Primarily used for water and
chemical systems, butterfly valves are not considered suitable for slurry or
systems containing particulates.
Globe Valve
The globe valve is manufactured of the same materials as gate valves. The globe
valve’s operation involves a linear rising stem with a multi-turn handwheel.
The globe valve’s complex flow path makes it excellent for throttling purposes.
It is well suited for automatic and remote operation. Typical applications are
for steam, chemical processing and gas service.
Plug Valve
The plug valve was developed several thousand years ago and used by the Romans
to control water into homes supplied by an aqueduct. The valve is manufactured
of the same materials as gate valves. It uses a one-quarter turn valve with an
oblong plug containing a hole for liquids to flow through. This valve could be
either lubricated (which helps operation) or non-lubricated. It could be either
sleeved or fully lined. For general use, the non-lubricated type is preferred.
Plug valves are well suited for many corrosive chemical applications and water.
Their one negative is the high turning torque necessary for operation.
Ball Valve
Ball valves are the most-used valve in the chemical industry. They are a
one-quarter-turn type that uses a ball with a drilled-out center, which allows
fluids to pass. Turning the ball 90 degrees in either direction cuts off or
allows flow. Ball valves range in size from 1/2 to 12 inches, and come in
flanged, socket weld, butt weld and threaded ends with a maximum of 600 psi.
The valves are manufactured in ductile iron through high alloys and a variety
of seating materials in three configurations: two-piece, three-piece and top entry.
The three-piece allows the body of the valve to be removed, keeping the end
connections intact. The two-piece is less expensive and must be removed
entirely. Top entry valves allow the ball to be easily removed for maintenance.
The ball valve is recommended for normal and severe chemical service
applications, water and gas. It is not recommended for slurry or liquids
containing particulates.
Diaphragm Valve
Also known as pinch valves (see Figure 1), diaphragm valves are manufactured from basic
ferrous alloys and high-performance thermoplastics. The valve consists of an
elastomeric sleevelike material that limits the maximum pressure and
temperature. It is available in two configurations: weir and straight-through patterns.
It operates by using a closure member outside the sleeve and a multi-turn hand
wheel that closes the sleeve to shut off flow. This type of valve is
characterized by streamlined flow and chemical resistance of the sleeve.
Shut-off is not bubbletight. It is generally used for chemical and high-purity
operations.
Regulator Valve
A regulator valve is a low-cost, standalone, self-actuating, proportional
controller whose controlling action is proportional to any deviation from a set
point. It does not require any auxiliary piping system. A typical regulator
valve is shown in Figure 2.
Limitations of regulators include a maximum size of typically six inches and
fixed failure modes, plus they are not generally applicable for severe service.
Control Valve
Control valves are not standalone valves that can only control the flow
rate. Rather, they are the final control element in a system and need to be
evaluated in that context. In principal, any continuously variable system
parameter that can be measured and compared to a set point can be controlled.
This parameter requires the addition of a proportional and integral control
mode that will return the measured variable to the approximate set point
following a load change.
When deciding between a control valve and a regulator valve, the following
questions should be considered:

Process piping installation. Source: www.iklimnet.com
Mike Frankel, CPD
Mike Frankel, CPD, is president of Utility Systems Consultants in Boynton Beach, FL, and has more than 45 years experience in the design and engineering for a variety of facilities, including healthcare, nuclear, pharmaceutical, housing, commercial and chemical facilities. He is an ASSE member, and is past president of the New Jersey ASPE chapter. He is the author of Utility Piping Systems Handbook, published by McGraw-Hill. He can be reached at mfrankl@aol.com.
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