JOHNSON CONTROLS
38
FORM 150.73-NM1
ISSUE DATE: 09/04/2020
SECTION 4 – INSTALLATION
Refrigerant Line Sizing
Refrigerant piping systems must be designed to pro-
vide practical line sizes without excessive pressure
drops, prevent compressor oil from being “trapped” in
the refrigerant piping, and ensure proper flow of liquid
refrigerant to the thermal expansion valve. Consider-
ations should be given to:
1.
Suction line pressure drop due to refrigerant flow.
2. Suction line refrigerant velocity for oil return.
3.
Liquid line pressure drop due to refrigerant flow.
4. Liquid line pressure drop (or gain) due to vertical
rise of the liquid line.
provides the pressure drops for
given pipe sizes for both liquid and suction lines. The
pressure drops given are per 100 ft. (30.5 m) of refrig-
erant piping. These friction losses do not include any
allowances for strainer, filter drier, solenoid valve, iso-
lation valve, or fittings.
Nominal pressure drop for solenoids, sight glass, and
includes approximate equivalent
lengths for copper fittings.
To ensure a solid column of liquid refrigerant to the ex-
pansion valve, the total liquid line pressure drop should
never exceed 40 psi (276 kPa). Refrigerant vapor in the
liquid line will measurably reduce valve capacity and
poor system performance can be expected.
To allow adequate oil return to the compressor, suc-
tion risers should be sized for a minimum of 1000 fpm
(5.08 m/s) while the system is operating at minimum
capacity to ensure oil return up the suction riser. See
under column labeled “Nomi-
nal Tons (kW) Unloaded. For more details, refer to
ASHRAE Refrigeration Handbook, Chapter 2
.
Evaporator Below Condensing Unit
On a system where the evaporator is located below the
condensing unit, the suction line must be sized for both
pressure drop and oil return. In many cases a double
suction riser must be installed to ensure reliable oil re-
turn at reduced loads.
indicates
when a double suction riser should be used for listed
pipe sizes to provide adequate oil return at reduced
loads. The calculated information was based on main-
taining a minimum of 1000 fpm (5.08 m/s) refrigerant
vapor velocity at full load.
Condenser Below Evaporator
When the condensing unit is located below the evapo-
rator, the liquid line must be designed for both friction
loss and static head loss due the vertical rise. The value
of static head loss of 0.5 psi/ft.(3.4 kPa/30 cm) must be
added to the friction loss pressure drop in addition to
all pressure drops due to driers, valves, etc.
OIL TRAPS
All horizontal suction lines should be pitched at least
1/4 in./ft (2 cm/m) in the direction of the refrigerant
flow to aid in the return of oil to the compressor. All
suction lines with a vertical rise exceeding 3 ft (0.91 m)
should have a “P” trap at the bottom and top of the riser
to facilitate oil return. Suction lines with a vertical rise
exceeding 25 ft (7.6 m) should be trapped every 15 ft
(4.6 m).
For more details, refer to
ASHRAE Refrigeration Hand-
book. System Practices for Halocarbon Refrigerants
.
On systems where oil return is a problem,
oil separators may be required. How-
ever, if piping design is poor, even with a
separator, oil may be lost into the system
over time, which may cause compressor
failure.
REFRIGERANT CHARGE
The condensing unit is charged with nitrogen a hold-
ing charge. The operating charge for the condensing
unit, evaporator coil, and refrigerant piping must be
“weighed-in” after all refrigerant piping is installed,
leak checked, and evacuated.
70% of the calculated charge must be
added prior to starting a system. Fail-
ure to add 70% of the charge may cause
compressor overheating when the system
is first started.
Final adjustment of refrigerant charge should be veri-
fied by subcooling values (refer to section on Pre-Start-
up for checking subcooling). See
for Refrigerant Line Charges.
FILTER DRIERS/ SIGHT GLASSES/TXV’S
Liquid line filter driers, sight glass, and TXV’s are
field supplied for each refrigerant circuit.
Summary of Contents for YLUA0078
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