bhe install
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Brazed Heat
Exchanger
Installation Manual
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I. Introduction
The Brazed Plate Heat Exchanger
Alfa Laval is credited with
inventing the original brazed plate heatexchanger. The brazed heat exchanger
is a compact variation of the traditionalplate heat exchanger. But, unlike the
traditional plate heat exchanger, the
BHE does not have a carbon steel frame,gaskets, tightening bolts or carrying bar.
It consists simply of AISI 316 stainless
steel corrugated channel plates, apressure plate and a frame plate with
connections that are brazed together in a
vacuum furnace.
How It Works
When the plate pack is
compressed, it creates a continuousseries of channels with portholes in each
of the four corners. The media enters
the inlet connections and is distributedinto the narrow channels between the
plates. The passages between the plates
and corner portholes are arranged so thatthe two heat-transfer media can travel in
alternate channels. A brazed seal around
the outer edge of the plates retains themedia within the channels. As the
warmer medium passes through the unit,
it releases heat energy to the thin plate
wall, which instantly transfers it to the
colder medium on the other side.The thin plates have a uniquely
designed herringbone geometry that
creates high turbulence and low pressure
loss. This optimal plate pattern gives theBHE and extremely high overall heat
transfer coefficient. This pattern has
been developed through theoreticalcalculations, checked by laboratory tests
and proven itself in the field.
II. The Alfa Laval Brazed
Heat Exchanger Series
The Copper-Brazed Heat Exchanger Line
Alfa Laval has developed astandard line of BHEs to encompass
different applications and heat loads.
These heat exchangers, from the smallestunit, the CB14, to the largest, the
CB300, are brazed with 99.9% pure
copper.
The Nickel Brazed Plate HeatExchanger is an alternative for
applications where copper is not
appropriate, such as de-ionized water orammonia.
Brazed Heat Exchangers aresuitable for liquid/liquid, steam/liquid,
and gas/liquid applications.
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Standard BHEs
Custom-designed BHEs can be
equipped with:
Multiple passes
Different connection positions Non-standard connections
Three-media configurations
Multi-pass BHEs
Multi-pass units are used to
increase the thermal length of the heat
exchanger. With this design, more heat
is transferred from the hot medium to thecold medium, at the expense of a higher
pressure drop. Figures 3A and 3B
illustrate the difference between the oneand two pass design.
III. BHE Specifications
Fluid Quality
To minimize risk of corrosion,the media pH values should be neutral.
The media must not contain chemicalscorrosive to stainless steel (AISI 316) or
the brazing material (copper or nickel).
Stainless steel is especially sensitive tolocalized spot and crevice corrosion due
to chloride, sulfite and sulfate ions.
Above a critical ion concentration thepassivity of the steel breaks down and
local spot corrosion occurs.
Materials Plates and connections AISI 316Brazing material
CB units Copper 99.9%NB units Nickel Alloy
ApprovalSweden Statens Anlaggningsprovning (SA)
Germany Technische Uberwachungsverein
USA Underwriters Laboratories (UL)American Society of Mechanical
Engineers (ASME) upon request
for some modelsCanada Canadian Standards Association
(CSA)
The data label shows:
1) Alfa Laval manufacturing number
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2) Connection position. S indicates
the front cover plate, T the backcover plate.
3) Unit description as follows:
a. Model
b. Plate number and typec. Connection configuration code
Example: CB26-70H S52
CB26 Model Type70 Number of Plates
H Type of Plate in Model
S52 Connection Code
BHE Connections
BHE connections are available inthe following:
Threaded and/or soldered
Flange (some models)
Rotolock
Victualic
For further details, please refer to theBrazed Plate Heat Exchanger Product
Catalog(Pub. No. ENSR00005EN 0207).
IV. Installation
General Information
For the highest heat transfer,
connect the unit so that a countercurrentflow is obtained.
Installation
Figure 5 shows the installation of
an evaporator. For evaporators connectthe refrigerant to the side with the
soldered connections (S3, S4) so that it
enters the unit at the bottom. Theexpansion device should be positioned
not less than 6-8 inches from the
connection (S3). Bent tubes and elbows
between the expansion device and theconnection should be avoided. Connect
the liquid to that side of the BHE that
best suits your installation (S1, S2) or(T1, T2).
NOTE: Units with the option of the
real double circuit have a single water
circuit with connections in a central
position and two independentrefrigerant circuits. The refrigerant
circuits, unless otherwise indicated,
have diagonal flow. The refrigerant
side connections follow the normal
rules with the additional note of being
diagonally opposite.
Mounting
Always mount the unit vertically
in two-phase applications. For single-phase applications the BHE can be
mounted horizontally or verticallywithout affecting the function.
Units smaller than CB26-30 can
be mounted directly on the pipes. Mountlarger units on anti-vibration plates or
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fasten with steel clamps (Figure 6 or 7)
or stud bolts, when included. If there is
risk of vibrations, use an anti-vibrationdevice as in Figure 8. Models with HX,
MX, LX plate configurations or model
AC must not be installed upside down.
The tightening torque for the 5/16 studbolts is 90-105 in-lb; for the 3/8, it is
195-221 in-lb. For larger sizes of units,removable feet and lifting lugs can be
provided as an option.
Threaded Connections
Connect the pipe using adynamometric wrench respecting the
indicated limits. The limits are
measured on the largest diameters. Incase of smaller connections, the torque islower. In the AC units, the Victualic
type connection can be supplied.
To avoid damaging the threadedconnections, it is important to mount the
BHE on the pipes within the
recommended design limits. (See table
below.) (See Figure 9.)
Table: Design Limits
BHE size T(lb) F(lb) MB(ft-lb) Mv(ft-lb)
CB14 3330 1800(-1350) 27 125
CB26,CB52
5550 2160(-1660) 45 285
CB76,AC120,
AC13024950 6070(-4720) 545 740
AC250 30800 7420(-5620) 675 2140
Soldered and Welded Connections
The temperature must not exceedthe melting point of the brazing material.
Use a wet towel around the connection
and the plate pack to reduce the heattransferred to the BHE plate pack during
installation.
Filling material: 30-55% silver alloy
Flux material: Black Flux for silversoldering
1. Clean the soldering assembly surface
at the copper tubes and BHEconnections.
a. Remove oil or other buildup with
degreasing solventb. Polish the surfaces to remove
oxides.
2. Apply the flux to the surface with abrush to remove and prevent
oxidation.3. For refrigeration installations, use a
dry Nitrogen gas on the refrigerantside to prevent oxidation.
4. Heat the soldering area to the
soldering temperature of about
1200F. (Higher temperatures will
melt the brazing material.) Use a
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wet cloth to minimize the heating
zone. WARNING: Unnecessary heating
(above 1200 F) can melt the brazing
material!
5. Keep the tube in a fixed position and
add the filler material.
V. Regulation
The efficient design of plate heat
exchangers allows the total hold-up
volume of the system (pumps, valves,piping and controls) to be much smaller
than that of systems using conventional
heat exchangers. This high efficiency
results in a quick response time. Thevalve and regulation equipment should
be designed accordingly.
The valve with the shortestresponse time should be placed close to
the outlet. This will give a faster
response when there is a small load.Follow the instructions from the valve
manufacturer and, if possible, use a PI
regulator with a logarithmic response.This is especially recommended in steam
applications.
Welding
1. Prepare the edge of the tube for
welding with a 30bevel.2. Place the piping into the connection.
Excessive cycling amplitude of
pressure and temperature can lead to
leakage after some time as a result offatigue phenomena. Thermal dynamicstresses are caused by large fast
temperature changes (more than 50F)and can damage the BHE. An ON/OFF
valve that causes pressure pulsation in
the BHE must be avoided. To minimizethermal fatigue, it is especially important
to avoid pressure and temperature
pulsations in steam applications orchanges in the condensate level inside
the steam condenser.
3. TIG-weld or MIG-weld the tube to
the connection, filling the groove
formed by the two edges. Thismethod minimizes the heating zone.
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Shut Down
VI. Operation Consult system instructions todetermine which pump should bestopped first.A liquid in motion in a pipe
system generates a high level of energy.
When a valve is closed or opened,causing the fluid to stop or continue, it
must be done slowly to avoid shockingthe system.
SLOWLY, close the valve
controlling the flow rate of the pumpbeing stopped.
When the valve is closed, stop the
pump.
Repeat for the other side.
WARNING: Do not use fast-closing
valves unless the pipes of the system
are very short!
If for any reason the heat exchanger
is shut down for a long period, itshould be drained. If the media
processed is corrosive, contains
particles, or has a tendency tocoagulate, it is recommended that the
heat exchanger be rinsed with waterand dried to avoid damage.
Start Up
Note: Consult equipmentmanufacturers start-up procedures forrefrigeration applications.
VII. Freeze Protection Before starting any pump, consultthe system instructions to determinewhich pump should be started first. For freeze protection use
thermostats and/or temperature controlsin the connections opposite to the liquid
inlet/outlet, if any, or in a temperature
pocket close to the outlet.
Make sure the control valve betweenthe pump and the unit is closed.
If there is a valve at the exit, make
sure it is completely open.
Open the vent.Connect the water side pipes toensure that the whole unit runs filled
with water.
Open the valve SLOWLY.
Close the vent after all of the air is
let out. To minimize freezing risk: Repeat the procedure for the other
side of the heat exchanger.1) Use a filter
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Insulation
Airtight insulation isrecommended. It is necessary when theunit is working as an evaporator at low
temperatures. This can be made, among
other solutions, using insulation sheets(Armaflex or similar) cut into
appropriate sizes and glued together as
shown. (See Figure 11.)
VIII. Maintenance
Heat Transfer
The purpose of the BHE is totransfer heat from one medium to
another. Heat passes very easily through
the thin walls separating the two media.
The pattern pressed into the plates makesthe plates strong and rigid and increases
the rate of heat transfer. This high rate
of heat transfer can be inhibited by the
formation of deposits on the platesurfaces. The corrugated pattern on Alfa
Laval plates induces turbulent flow.Turbulence provides strong resistance to
deposit buildup, but it cannot always
eliminate fouling. The deposits mayincrease the total wall thickness, and
consist of materials of a much lower
thermal conductivity than of the metal
plate. Thus, a layer of deposits canseverely reduce the overall heat transfer
rate. Corrosion can also occur under the
deposits. For corrective action, please
see Cleaning below.
Pressure Drop
Pressure drops are wasted
energy. All pipe systems, andequipment included in them, offer
resistance to the media flowing through
them. Some pressure drop is inevitable,
but it should be kept as close as possibleto the designed value for the BHE. The
formation of deposits on the heat transfersurfaces reduces the free space betweenthe plates. This means that more energy
is required to achieve the desired flow in
the BHE. Large particles and fibers mayalso clog the heat exchanger if it is not
equipped with a strainer. A reduced
ability to maintain the desired
temperatures along with an increasedpressure drop on either media, are
symptoms of fouling or clogging. For
corrective action, please see Cleaningbelow.
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Cleaning
Clean with detergents for fatty
deposits. For heavier fouling usechemicals such as formic acid, citric
acid, vinegar, or other organics in
concentrations compatible with copper.Alfa Laval BHEs can be cleaned
in place with the Cleaning-in-Place
(CIP) system, which chemically removescalcium deposits and other forms of
scaling from plate surfaces (See Figure
12.) Different solutions can be used,depending on the type of deposits. Every
application has to be considered
separately. The Cleaning-in-Place
procedure is generally the same,
regardless of the solution used.
CIP Procedure
1. Drain the unit.
2. Rinse with fresh water.3. Drain water.
4. Fill with fresh water.
5. Add cleaning agent (solution andconcentration depending on type of
fouling).
6. Circulate the cleaning solution (iffeasible).
7. Drain the cleaning solution.8. Add and circulate the passivating
liquid for corrosion inhibition of
plate surfaces.9. Rinse with fresh water.
10. Drain.
CAUTION: Do not use liquids that
are corrosive to stainless steel or the
brazing material (copper or nickel)!Do not leave the unit on standby after
cleaning! Contact the Alfa Laval
Service Center (1-866-Alfa Laval) for
more information about cleaning-in-
place equipment, detergents or
service.
IX. Assistance and Field
Service
TroubleshootingTo assure correct performance of
the unit, please check that:-it is correctly connected according
to page 4 of this leaflet.
-it is absolutely clean and free fromdeposits. Increased pressure drops
can reveal fouling.
-the control equipment is correctly
set up and that freezing does notoccur.
Alfa Laval maintains a largehighly specialized engineering staff tohandle your questions and problems.
Your nearest Alfa Laval representative
will be happy to provide you with quotesor answer to your questions. To assist
your representative in finding the best
solution, please provide the following
sizing information along with yourinquiry:
Hot Side Cold Side
FluidMass flow
Temperature InTemperature Out
Maximum Pressure Drop
Design Pressure
For Refrigeration Applications
Condensing TemperatureEvaporator Temperature
TX Valve Superheat
Total Heat of Rejection
Total Evaporator Tons
GPM
F
F
psig
psig
F
F
F
kBTU/H
TR
GPM
F
F
psig
psig
F
F
F
kBTU/H
TR
If you do not have this
information, it may be sufficient todescribe the existing heat exchanger.