Discharge Valve Springs — When 5H compressors are used for booster applications where discharge pressure is below 10 psig, the standard discharge valve springs furnished with the machine should be replaced with an equal number of lighter weight springs, Part Number
No change in discharge valve springs is recommended for
5F compressors.
Motor Selection Data — In staged refrigeration sys- tems, the high stage compressor starts first and runs until low stage pressure has been reduced to a predetermined level before the low stage machine starts. With direct staged arrange- ments, the high stage machine draws gas from the evaporator through low stage machine bypass during this initial period. Size of the selected motor must be related to the maximum condition at which booster compressor can operate.
Compressor may run under heavy loads during periods of high suction pressure, especially on starting when system is warm. To handle these situations the motor must be sized larger than the actual balanced operation brake horsepower indicates, or special attention must be paid to operation of the system when starting initially. Tables
If the system is to operate only at a fixed low temperature, it is possible to avoid oversizing of motors providing careful op- eration is followed when the system is first put in operation.
On applications requiring reduction from ambient condi- tions to some extremely low temperature, the compression system will be operated at high suction pressures for consider- able periods of time. General practice is to drive the high stage compressor with a motor that will operate compressor at the highest expected evaporator temperature. This is generally the “air conditioning” rating of unit. For intermediate or low stage compressors, it is generally sufficient to size motor to take care of double the balance load indicated horsepower plus friction horsepower.
Also consider compressor starting torque requirements when selecting motor for a booster compressor. Starting torque of a motor only large enough to provide required normal operating bhp for booster applications may not be large enough to start the compressor. Recommended minimum motor sizes shown in Table 28 have been selected to assure adequate starting torque. Actual motor size selected is usually larger, depending on the maximum bhp conditions under which the compressor will run during pulldown or other abnormal operat- ing periods.
It is good practice to select motors with allowance for 10% voltage reduction unless there is a certainty that this cannot occur.
Compressor Starting Torque — Required compres- sor starting torque is dependent on the discharge pressure as well as the pressure differential occuring during
Selection Procedure — Selection of a 5F,H booster compressor requires that the load, saturated suction tempera- ture, saturated discharge temperature, type of system and refrigerant are known.
After the saturated intermediate temperature is determined from Fig. 21, the booster rating (Tables
SELECTED EXAMPLE:
Given:
Refrigeration Load. . . . . . . . . . . . . . . . . . . . . . . . . . . . . .5.7 tons Saturated Suction Temperature . . . . . . . . . . . . . . . . . . . . .
Refrigerant 22
Find: Compressor size and motor size.
Solution:
1.Figure 21 indicates an optimum saturated intermediate temperature of –2 F. Allow a 1 degree or 2 degree drop from the booster compressor to intercooler and from the intercooler to the high stage compressor.
Booster Saturated Suction Temperature =
2.At
The safety factor at 1750 rpm:
( 6.85.7 ) x 100 – 100 = 19.3 or 20%
This is satisfactory from Fig. 19 and a 5H60 compressor is selected.
3.Indicated hp (ihp) = bhp – Friction hp (fhp)
Where bhp is given in Table 26 and fhp is given in Table 28.
Indicated hp (ihp) = 12.1 – 3.07 = 9.03 Recommended minimum hp
=(2 x ihp) + fhp
=(2 x 9.03) + 3.07 = 21.13
Tentatively select a
4.With
1.303 x 6.8 = 8.86 tons (actual load)
5.Allowing a 1 degree drop from the intercooler, the high stage saturation suction temperature is
Allowing a 2 degree drop between the compressor and condenser, the high stage saturated discharge temperature = 80 + 2 = 82 F.
6.Referring to the 5F,H Compressor Ratings table, 5F60 at 1450 rpm (using multiplier in compressor capacity notes) has a capacity of 9.21 tons at
7.Assume that maximum load during pulldown occurs at 50 F suction and 90 F discharge. For this condition, the rating tables (using the multiplier in Step 6) indicate 15.8 bhp, thus a
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