
Heat Transfer
BrazedPlate Heat Exchangers
Installation, Operation and Maintenance Manual

Installation
FIGURE 1
FIGURE 2
T
Mb
Mv
Evaporators
Refrig. In: ......... F4
Refrig. Out: ...... F1
Liquid In:............ F2
Liquid Out: ......... F3
STEAM TO LIQUID
Condensers
Steam In: ......... F1
Condensate Out: F4
Liquid In:............ F3
Liquid Out: ......... F2
Condensers
REFRIGERATION:
Refrig. In: ......... F1
Refrig. Out: ...... F4
Liquid In:............ F3
Liquid Out: ......... F2
TABLE 4
of ITT Brazed Plate Heat Exchangers
Upon receipt of the exchanger, inspect for shipping    
1.
2.
3.
damage, especially to the connections. If damage is 
extensive, notify the carrier immediately. Finally, check the 
heat exchanger against proper drawings and spec sheets to 
make sure everything is as expected.
Before piping up, inspect all openings in the 
heat exchanger for foreign material. Remove all plugs 
and shipping covers immediately prior to installing.  
Make sure it is thoroughly cleaned to remove all preservation 
materials, if any were used, unless the material is soluble in 
the system fluid.
For single phase fluids, the heat exchanger can be 
mounted in any orientation that is convenient and  
should be piped in a counter current, parallel flow  
arrangement. For two phase fluids, the heat exchanger  
should be mounted vertically and piped as shown in  
Figure 1 and Table 1. Connections may be either on the front 
or back of the exchanger.
Provide air vent valves for the heat exchanger so that it 
4.
5.
6.
7.
can be purged to prevent or relieve vapor or gas binding.
Install proper relief valves and temperature alarms 
to make sure the heat exchanger is not subject to 
conditions beyond the intended design.
Do not weld or braze brackets or attachments 
directly to body of heat exchanger.
For soldering type connections, braze with minimum 
45% silver solder and at maximum 1200° F. For 
welded type connections use TIG or MIG welding. Avoid 
overheating. A wet cloth or rag should be placed around the 
base of the connection. A Nitrogen purge should be used to 
avoid internal oxidation. Braze or weld with exchanger in 
the vertical position.
CAUTION: 
Many Heat exchangers circulate fluids which are irritating or dangerous to the human system. 
These fluids could cause problems if bolted or threaded joints are not maintained in a leak tight 
condition at operating pressures, temperatures, and no flow, ambient conditions. 
Even if fluids are not irritating or dangerous, a leak could cause a slippery situation on the floor below.
Since one fluid in the heat exchanger is at a higher temperature, any leaks may cause burns.

Liquid Hot Liquid Cold
Gas Hot Liquid Cold
Condensing Gas  Hot  Liquid Cold
Liquid or Gas  Hot  Vaporizing Liquid  Cold
Start both fluids gradually 
at the same time.
Start cold fluid 
first then hot fluid.
Start hot fluid first then 
slowly start cold fluid. 
Avoid temperature shock.
Start hot fluid 
first then cold fluid.
Shut down both fluids 
gradually at the same time.
Shut down hot fluid 
gradually then cold fluid.
Shut down cold fluid 
first then hot fluid.
Shut down cold fluid 
first then hot fluid.
Type of Fluid  Relative  Type of Fluid  Relative  Start-Up  Shut-Down
Temperature   Temperature  Procedure  Procedure
TABLE 4
Condensers
REFRIGERATION: STEAM TO LIQUID
Refrig. In:  F1
Refrig. Out:  F4
Liquid In:  F3
Liquid Out:  F2
Evaporators
Refrig. In:  F4
Refrig. Out:  F1
Liquid In:  F2
Liquid Out:  F3
Evaporators
Refrig. In: ......... F4
Refrig. Out: ...... F1
Liquid In:............ F2
Liquid Out: ......... F3
Condensers
Steam In:  F1
Condensate Out:  F4
Liquid In:  F3
Liquid Out:  F2
STEAM TO LIQUID
Condensers
Steam In: ......... F1
Condensate Out:  F4
Liquid In:............ F3
Liquid Out: ......... F2
Model  T (lbs)  F (lbs)  Mb (in-lbs)  Mv (in-lbs)
400  3327  1798.4 (-1348.8)  327.5  1504.6 
410 
411  5552.6  1798.4 (-1348.8)  540  1504.6 
412
415  5552.6  2158.1 (-1663.5)  540  3407.5
422  24952.8  6069.6 (-4720.8)  6550  8912.7
433  Consult  Factory  Consult  Factory
Start both fluids gradually  
at the same time.
Start cold fluid 
first then hot fluid.
Start hot fluid first then  
slowly start cold fluid.  
Avoid temperature shock.
Start hot fluid 
first then cold fluid.
Shut down both fluids  
gradually at the same time.
Shut down hot fluid  
gradually then cold fluid.
Shut down cold fluid  
first then hot fluid.
Shut down cold fluid  
first then hot fluid.
Temperature    Temperature  Procedure  Procedure
Condensers
REFRIGERATION:
Refrig. In: ......... F1
Refrig. Out: ...... F4
Liquid In:............ F3
Liquid Out: ......... F2
TABLE 2
TABLE 4
435 psig Standard Design
Condensers
REFRIGERATION: STEAM TO LIQUID
Refrig. In:  F1
Refrig. Out:  F4
Liquid In:  F3
Liquid Out:  F2
Evaporators
Refrig. In:  F4
Refrig. Out:  F1
Liquid In:  F2
Liquid Out:  F3
Evaporators
Refrig. In: ......... F4
Refrig. Out: ...... F1
Liquid In:............ F2
Liquid Out: ......... F3
Condensers
Steam In:  F1
Condensate Out:  F4
Liquid In:  F3
Liquid Out:  F2
STEAM TO LIQUID
Condensers
Steam In: ......... F1
Condensate Out:  F4
Liquid In:............ F3
Liquid Out: ......... F2
Model  T (lbs)  F (lbs)  Mb (in-lbs)  Mv (in-lbs)
400  3327  1798.4 (-1348.8)  327.5  1504.6 
410 
411  5552.6  1798.4 (-1348.8)  540  1504.6 
412
415  5552.6  2158.1 (-1663.5)  540  3407.5
422  24952.8  6069.6 (-4720.8)  6550  8912.7
433  Consult  Factory  Consult  Factory
Model  T (lbs)  F (lbs)  Mb (in-lbs)  Mv (in-lbs)
400   200   100     20     200 
410 
411   280   130     27     300 
412
Start both fluids gradually  
at the same time.
Start cold fluid 
first then hot fluid.
Start hot fluid first then  
slowly start cold fluid.  
Avoid temperature shock.
Start hot fluid 
first then cold fluid.
Shut down both fluids  
gradually at the same time.
Shut down hot fluid  
gradually then cold fluid.
Shut down cold fluid  
first then hot fluid.
Shut down cold fluid  
first then hot fluid.
Temperature    Temperature  Procedure  Procedure
Condensers
REFRIGERATION:
Refrig. In: ......... F1
Refrig. Out: ...... F4
Liquid In:............ F3
Liquid Out: ......... F2
TABLE 2
TABLE 4
TABLE 3
The nozzle connections are designed 
8.
for normal torque force and damage 
may occur if over tightened. The use of pipe 
sealant materials compatible with the system 
fluids is recommended for threaded type 
connections. Connection load limits should be 
observed and are shown in Figure 2, Table 2, 
and Table 3.
150 psig Pressure Design
Operation
Be sure the entire system is clean 
1.
vent plugging of passages with debris. 
The use of strainers or settling tanks in 
pipelines leading to the heat exchanger 
is recommended. The recommended 
strainer size is 20-24 mesh.
before starting operation to pre-
2. 3.
Start operating gradually. See 
Table 4 for suggested start-up 
and shut-down procedures for most 
applications. If in doubt, consult the 
nearest ITT Heat Transfer representative 
for specific instructions.
CAUTION: 
A heat exchanger is a pressure vessel designed for operation at certain specific limits of pressure and temperature. The cooling or process system, 
which includes the heat exchanger, must be safeguarded with safety valves and controls so that these heat exchanger design conditions are not 
exceeded. All operating personnel should be made aware of these specific design pressures and temperatures.
conditions in excess of the specified 
design limits shown on the nameplate 
attached to the heat exchanger.
4.
       corroding.
Do not operate the heat exchanger 
under pressure and/or temperature 
Drain all fluids when shutting down 
to eliminate possible freezing and   

Maintenance
Clean exchangers subject to 
1.
fouling (scale, sludge deposits, 
etc.) periodically, depending on specific 
conditions. A sludge or scale coating 
on the plates can reduce effectiveness.  
A marked increase in pressure drop 
and/or reduction in performance usually 
indicates cleaning is necessary.
Some suggested methods of 
3.
cleaning either side of the heat 
exchanger are listed below:
n Back flush with a high pressure stream 
of hot water to remove loose deposits.
n Circulating hot wash oil or light 
distillate will usually effectively remove 
sludge or similar soft deposits.
n  A 5% solution of Phosphoric Acid or 
Ox al ic  Acid may be  effective in 
removing more stubborn deposits. 
For optimum results, the solution 
should be in a back flush type flow 
pattern. Rinse heat exchanger with 
cl ean fresh water  after  use . It is 
recommended that the refrigerant 
circuit not be chemically cleaned. 
A s  s u g g e s t e d  u n de r 
2.
strainer is recommended if the fluid 
quality is poor (extensive dirt, debris, 
and contaminants). If the fluids are 
relatively clean, there should be little 
problem with fouling so periodic 
cleaning is adequate.
4.
be cleaned by commercial cleaning 
methods, then replacement of the unit 
is suggested.
“Operation”, the use of a 
If the h ea t e xc hange r i s 
excessively fouled and it cannot 
NO TE : Use in accordance with 
the manufacturer’s instructions and 
check that cleaning compounds are 
compatible with the materials of the 
heat exchanger. Since there are a 
wide variety of cleaning compounds 
av ai la bl e w hi ch  are c ompatible  
with certain metals and alloys,  it  
is recommended that you contact a  
representative of the above  
commercial cleaning products  
to determine which particular 
cleaning fluid they would 
suggest for your type of 
scaling problem.
CAUTION: 
When the heat exchanger is cleaned, it is 
important that full characteristics of the fouling 
material and the cleaning agent be known and 
care exercised in handling them according to 
instructions. Use eye protection to prevent 
damage to your eyes. Wear a respirator when 
required.
CAUTION: 
Do not exceed design conditions of heat 
exchanger during operation or maintenance.
CAUTION: 
Brazed plate heat exchangers have exposed 
sharp metal surfaces. Protective gloves are 
recommended during handling.
Warranty
Seller warrants only that it will furnish by freight a replacement for, or at its option 
repair, any product of its manufacture or part or portion thereof, proved to its 
satisfaction to be defective in material or workmanship under normal use and service 
within one (1) year from the date all other equipment or part thereof is first placed 
in use, or two (2) years from the date of shipment, whichever shall be less. See ITT 
terms and conditions of sale for details.
For m or e in fo rm at io n, pl ea se c on ta ct :
175 Standard Parkway • Cheektowaga, NY 14227
800/447-7700  Fax: 716/897-1777 
www.itt.com
Lit# 104-65 (4/07) 
© 2007 ITT
Heat Transfer