This instruction manual includes installation, maintenance, and operation information for the DFA variable orifice
desuperheater. Refer to separate instruction manuals for information on the actuator and accessories.
Do not install, operate, or maintain a DFA desuperheater without being fully trained and qualified in valve, actuator,
and accessory installation, operation, and maintenance. To avoid personal injury or property damage, it is important
to carefully read, understand, and follow all the contents of this manual, including all safety cautions and warnings. If
you have any questions about these instructions, contact your Emerson Process Management sales office before
proceeding.
Description
The Fisher DFA desuperheater flexible architecture (figure 1) incorporates both a water control element and a
variablegeometry mechanically atomized, selfcontained desuperheater for moderate to high flow variation. It is
installed through a flanged connection on the side of an NPS 8 or larger pipeline.
The desuperheater design incorporates an integral thermal liner inside the desuperheater body pipe. This minimizes
the potential for thermal shock when cool water is introduced to the unit which has been heated to the operating
steam temperature.
ThenozzlemountfortheDFAisengineeredtominimizethepotential for excitation due to vortex shedding and flow
induced vibration. The DFA desuperheater is installed through a flanged connection on a DN 200 (NPS 8) or larger
pipeline. Maximum unit C
www.Fisher.com
is 15.0.
V
DFA Desuperheater
August 2013
Table 1. Specifications
Available Configurations
(1)
and Valve Sizes
J DFA valve body style: Angle
Common Characteristics: Designed according to ASME
B16.34 Valve-Flanges, Threaded and Welding End
End Connections Styles
(1)
See tables 2 and 3
Maximum Inlet Pressure and Temperature
(1,2)
Flanged, Socketwelding, or Buttwelding: Consistent
with CL150, 300, 600, 900, 1500, and 2500 according
to ASME B16.34, unless limited by maximum pressure
drop or material temperature capabilities
Maximum Pressure Drop
(1)
Valve with Cavitrol™ III Cage: 149 bar (2160 psi) for
two-stage and 207 bar (3000 psi) for three-stage cage.
Consult Fisher Bulletin 80.2:030, Cavitrol III One-,Two-,
and Three-Stage trims, for more information
Anti-cavitation MicroFlat: <51.7 bard (<750 psid)
Inherent Rangeability
Up to 50:1. The ratio of maximum to minimum
controllable C
is dependent upon the available water
v
pressure differential
Instruction Manual
D103643X012
Shutoff Classifications per ANSI/FCI 70-2 and IEC
60534-4
Standard Cage (Micro-Flat):Flowdown
Cavitrol III Cage: Flow down
Bonnet Style and Mounting
Standard Bonnet
Yoke Temperature Limit: Standard bonnet with cast iron
yoke is limited to 537_C (1000_F)
Packing Arrangements
J Single, J Double, and J Leakoff standard graphite
packing, or optional J ENVIRO-SEAL™ and
J HIGH-SEAL packing systems. See bulletin 59.1:061,
ENVIRO-SEAL and HIGH-SEAL Packing System for
Sliding-Stem Valves
(1)
(5)
(1)
Spray Water Pressure Required
6.9 bar (100 psi) or larger is acceptable
1. Do not exceed thepressure or temperature limits in this bulletin, nor any applicable code or standard limitations.
2. EN (or other valvebody material) ratings and end connections can usually be supplied; consult your Emerson Process Management sales office.
3. A function of requiredturndown and equipment selection.
4. Special characterized cages are available. Contact your Emerson Process Management sales office.
5. Modified equal percentage characteristic is equal percentage for the first 75%of travel, then opens quickly for additional capacity.
(3)
Approximate Weight
See table 12
The DF A features:
1. Fine atomization over a wide range of operating conditions helping to assure rapid and complete vaporization of
injected water.
2. Available with a wide range of standard and anti-cavitation trim styles.
3. Designminimizesaffectsofthermalcycling.
4. High turndown capability.
5. Flexible architecture with multiple valve trim combinations and face-to-face dimensions available.
2
Instruction Manual
D103643X012
DFA Desuperheater
August 2013
Educational Services
For information on available courses for the Fisher DFA Desuperheater, as well as a variety of other products, contact:
Emerson Process Management
Educational Services, Registration
P.O. Box 190; 301 S. 1
st
Ave.
Marshalltown, IA 50158-2823
Phone: 800-338-8158 or
Phone: 641-754-3771
FAX: 641-754-3431
e-mail: education@emerson.com
Principle of Operation
The DFA desuperheater reduces steam temperatures through the introduction of cooling water directly into the hot
steam flow stream. By regulating the quantity of water that is injected, accurate downstream steam temperature can
be both controlled and maintained.
The rate of vaporization, and/or cooling, is a function of droplet size, distribution, mass flow, and temperature. Steam
velocity is critical and should be maintained at 6.1 to 9.1 meters per second (20 to 30 feet per second) as the
minimum. Actual minimum steam velocity requirements will vary by application. As steam velocity increases, a longer
distance is required to achieve homogeneous mixing and to complete vaporization.
In DFA desuperheater nozzle styles, the spraywater quantity is controlled by internal control valve which responds to
signals received from the temperature control system. The water enters the main tube of the desuperheater, passes
through the spray nozzle, and discharges into the steam line as a fine, atomized spray (see figure 4).
Each particular nozzle, or set of nozzles, in the sprayhead is tailored to meet a specific set of operatingconditions. The
nozzle design optimizes the spraywater droplet size promoting rapid atomization and complete vaporization of water
in the steam flow stream to obtain precise temperature control. The DFA desuperheaterusesavariablegeometryAF
nozzle. In the AF nozzle design (see figure 4), water enters the swirl chamber via compound angled orifices, thus
creating a rotational flow stream. This flow stream is further accelerated as it is forced up and out through the spray
annulus. The cone-shaped plug varies the geometry of the spray annulus using a force balance principle between
water pressure and the preload exerted by a helical spring. This variable geometry design sprays a thin hollow cone
over a wide range of flow rates, resulting in excellent temperature control over a wide range of operating conditions.
Figure 2. AF Nozzle Cross Section
STEM
BODY
SPRING
PLUG
A7191
NUT
PIN
WATER INJECTION HOLES
3
DFA Desuperheater
August 2013
Instruction Manual
D103643X012
Installation
WARNING
Always wear protective gloves, clothing, and eyewear when performing any installation operations to avoid personal
injury.
Personal injury or equipment damage caused by sudden release of pressure may result if the desuperheater is installed
where service conditions could exceed the limits of the pressure class noted on the nameplate. To avoid such injury or
damage, provide a relief valve for over pressure protection as required by government or accepted industry codes and
good engineering practices.
Check with your process or safety engineer for any additional measures that must be taken to protect against process
media.
If installing into an existing application, also refer to the WARNING at the beginning of the Maintenance section in this
instruction manual.
Table 2. Desuperheater Connection Size
DesignSteam Line Size, NPS
DFA8-603or4CL150-2500
1. Other standard flanges and connections are also available.