1. Max measured length is 200', max equivalent length is 250'
Liquid Lines
Velocity
This should be between 100 fpm and 400 fpm for either R-
410A or R-22.Exceeding 400 fpm is acceptable, but may lead
to refrigerant noise issues. 5 ton units using 3/8" lines will be
405 fpm for R-22 or 483 fpm for R-410A. While acceptable,
the possibility of noise must be understood and explained to
the owner Avoid placing lines inside walls or directly above
sleeping areas whenever possible
Pressure Drop
This can be no more than 35 psi for R-22 or 60 psi for R-
410A. Exceeding those parameters is NOT ALLOWED as it
would cause a loss of subcooling which leads to capacity loss
and/or failed components. If a HP system has both vertical
rise and vertical drop in the liquid line, enter the NET value
as a rise. In an A/C system enter the net rise OR net drop as
appropriate.
Suction Lines
Velocity
This should be between 1000 fpm and 3000 fpm for either R-
410A or R-22. Less than 1000 fpm on vertical risers may not
allow oil to be returned to the compressor and exceeding
3000 fpm will cause noise and vibration problems. Velocity
on horizontal runs is allowed to be as low as 800 fpm.
Pressure Drop
This should be no more than 3 psi for R-22 or 5 psi for R-
410A Exceeding these values is not recommended but is
allowed. However it results in capacity loss at a rate of 1%
for every psi on R-22 and .7% for every psi on R-410A
Long Line Sets
A long line set is defined as exceeding 75 Feet in length and
MUST include a:
1. crankcase heater if one is not factory installed.
2. normally closed solenoid valve installed in the liquid line
near the condensing unit.
3. Non Bleed TXV (standard requirement on most units at
13 SEER and higher).
4. hard start kit (single phase units only).
5. Install Schrader access valves at the indoor unit for both
the suction and liquid lines. These are optional, but
recommended to aid in troubleshooting pressure drops,
subcooling and TXV operation
Using Receivers to overcome loss of subcooling
When using a receiver it must be understood that subcooling
measurements cannot be attempted in the field as the receiver contents
are in a saturated state. No hydrolic or hydorstatic seal exists so
subcooling cannot be measured. A sight glass between the receiver and
TXV must be used to charge the system by adding refrigerant until
bubbles are gone, then adding 1/2 the pump down capacity of the
receiver. Use of receivers is not supported by the factory because the
application typically does not fall within their published guidelines.
NOTES:
1. If on a long line set the liquid line will be exposed to direct
sunlight, or very high ambient conditions, it should be
insulated
2. If the unit contains a rotary compressor the MAXIMUM
line length is 100'
3. If more than 5 feet of underground piping is installed on a
cooling only system, install an accumulator with volume
equal to 1/2 the system's refrigerant volume.
4. If a long line set application uses a two stage system,
meaning a single refrigerant circuit with either two
compressors or a single compressor that reduces capacity,
consider decreasing the vertical suction riser (if one exists)
by one line size.
5. Noise from lines running through basements and/or attics
can often be avoided by adhearing to the velocity
guidelines and taking care use non metalic hangers such as
mesh strap which insulates the refrigerant lines from the
joists. Overcharging will also contribute to noise.
Discharge or vapor line mufflers can eliminate harmonic
noises sometimes encountered in otherwise properly sized
and charged systems.
6. For addtional information consult the most recent
Application Guidlines for Refrigeration Piping as
published by UPG. If your application exceeds
theseparameters, you must contact Jack Bartell or the
factory for assistance
REMEMBER: With 2 stage units you must look at the suction line
velocity at reduced capacity to insure velocity remains above 1000fpm
on suction risers. If it does not, reducing the riser size by one size will
correct the problem
1. Slope horizontal suction lines on cooling only systems approximately
1 inch every 20 feet toward the outdoor unit to facilitate proper oil
return. Since the flow of refrigerant is bidirectional on heat pumps,
all horizontal vapor lines should be level. Pre-charged lines with
excess tubing should be coiled horizontally in an inconspicuous
location to avoid oil trapping. Never coil excess tubing vertically.
2. Use long radius elbows wherever possible
3. Use PVC piping as a conduit for all underground installations.See
Figure 2. Buried lines must be kept as short as possible to minimize
the build up of liquid refrigerant in the vapor line during long
periods of shutdown.
TRAPS
Traps are not required if the piping is properly sized.
Traps will only add pressure drop to the system, further
reducing capacity
INDOOR UNIT ABOVE OUTDOOR UNIT
a common problem with the cooling cycle (air conditioning or heat
pump) is that the amount of liquid sub-cooling varies as operating
conditions change (such as outdoor ambient). Under some conditions, it
is possible that flashing will actually occur in the liquid riser. As long as
only liquid is present in the liquid riser, the liquid static pressure loss
can be calculated at 1/2 psi per foot of rise. However, as soon as flashing
starts, the rate of pressure loss increases and continues to increase as
the amount of gas increases. For this reason, the restrictions on
elevation differences for this configuration must be based on
the entire range of operating conditions. When the indoor
unit is above the outdoor unit, the pressure loss in the liquid
line during the cooling cycle will limit the amount of elevation
difference allowed. Since both friction and static head
contribute to pressure loss, it can be stated that the elevation
difference allowed decreases as the total equivalent line
length (horizontal plus vertical) increases.
OUTDOOR UNIT ABOVE INDOOR UNIT
When the outdoor unit is above the indoor unit, the static pressure
gain in the liquid line vertical drop (1/2 psi per foot) may overcome the
frictional pressure loss resulting in a total pressure gain. A pressure
gain in the liquid line is not detrimental to the performance of the
system. On cooling only systems where the outdoor unit is located high
above the indoor coil, it may even be possible to reduce the size of the
liquid line. The static gain in the vertical drop will offset the increased
friction loss caused by smaller tubing. In addition, the reduction in the
total system charge due to the smaller liquid line will enhance the
reliability of the system. With this configuration, gas velocity in the
vapor riser must be kept above 1000 feet per minute for proper oil
return and below 3000 feet per minute to avoid noise and vibration
problems.