Page 2 - Table 2 — Compression Exponent “N”; High Compression Ratio —; Table 4 — Actual Suction Gas Temperature
2 OPEN-DRIVE COMPRESSORS These compressors are designed to operate with Refriger- ants 12, 22, 134a, 502, or 507/404A. See Table 1. Operating Requirements — Satisfactory operation of a reciprocating compressor depends on 3 fundamentalrequirements: 1. Prevention of excess discharge temperature.2. Ade...
Page 4 - Extended periods of continuous, fully unloaded operation; Table 5 — Total Heat Rejection Factors; RPM
4 Compressor Capacity Notes 1. Compressor capacities are based on 1750 rpm and 15 F subcooling for all unit sizes and refrigerants. 2. Multiplying factors for other rpm: See Multiplying Factors chart on page 31. 3. Liquid subcooling greater than (less than) 15 F incorpo- rated in ratings increases (...
Page 5 - Table 6 — Rating Basis and Capacity Multipliers for R-12 and R-134a*; SST; SST —
5 Table 6 — Rating Basis and Capacity Multipliers for R-12 and R-134a* LEGEND *R-134a capacity multipliers start at 0° F SST and above. SST (F) SDT (F) RETURN GAS TEMPERATURE (F) –30 –20 –10 0 10 20 30 40 50 60 65 –30 90 0.963 0.966 0.970 0.973 0.977 0.981 0.985 0.989 0.993 0.998 1.000 100 0.951 0.9...
Page 17 - Table 12 — Compressor Ratings
17 Table 12 — Compressor Ratings; R-507/404A LEGEND NOTES: 1. Shaded ratings require water-cooled heads, if the dis- charge temperature exceeds 275 F. 2. An oil cooler is recommended for all long stroke compressors (5H46, 66, 86, 126). 3. Oil cooler required when SST is below –20 F.4. Refer to Table...
Page 19 - Table 15 — Weight Distribution, Compressor; Capacity Control —; SHORT-STROKE COMPRESSORS ONLY; Fig. 4 — Cylinder Unloading Sequence
19 Table 15 — Weight Distribution, Compressor Units (See drawing, Table 14) LEGEND NEMA — National Electrical Manufacturers Association *Oversize frame. Capacity Control — For all 5F,H compressors, a pressure-type cylinder unloader is used. On 5F20 and 5F30compressors, the capacity control valve is ...
Page 20 - Table 16 — Capacity Control Reduction Steps; Table 17 indicates control oil pressure at which controlled; Fig. 5 — Operating Sequence of Capacity Reduction Steps
20 Table 16 — Capacity Control Reduction Steps *Two controlled cylinders (to 33 1 / 3 %) available on request for 5F30. Principle of Operation of the System — An increase in suc-tion gas pressure, which requires increased compressorcapacity, causes the needle valve to close. Therefore, lubrica-tion ...
Page 21 - Table 17 — Initial and Final Unloading; Capacity Control Valve: Function is to raise or lower the
21 Table 17 — Initial and Final Unloading Oil Pressures — 5F20, 5F30 5F40 THROUGH 5H86 (Fig. 7)Major Elements of Capacity Control Systems: 1. Capacity Control Valve: Function is to raise or lower the control oil pressure to the hydraulic relay piston inresponse to refrigerant suction pressure. Incre...
Page 22 - Fig. 9 — Pneumatic Compensation
22 5H120, 5H126 CAPACITY CONTROL (Fig. 8) — This ca-pacity control system is slightly different from the system on5F40 through 5H86 compressors. Unloaded starting and capac-ity reduction is obtained by holding open the suction valves ofa number of cylinders. For capacity control purposes, asuction-p...
Page 23 - Capacity Control
23 Control Pressurestats — Dual pressurestats are furnished withall 5F,H compressors. They are often referred to as high- andlow-pressure cutouts. Their function is to cut the circuit to theholding coil of the compressor motor starter when pressuresetting limits are exceeded. The high pressurestat h...
Page 24 - Fig. 13 — Recommended Solenoid Valve Operation
24 2 2R* 1R 1 1L 3 2L 4 B D C E A * PUMP OIL PRESS. DUMP TOCRANKCASE OIL TO UNLOADERPOWER ELEMENTS *STEP 2R DOES NOT EXIST ON A 5F40 COMPRESSOR. NO HOLE IS REQUIRED AT POINT A FRONT VIEW BOTTOM VIEW HANDHOLE COVER (ALL PIPE PLUGS 1/8 NPT) FROM UNLOADERCONNECTIONS WHEN UNLOADING DESIRED,SOLENOID VALV...
Page 25 - Pump End Cover Assembly
25 CAPACITY CONTROL MODIFICATIONS FOR HEATPUMP APPLICATION — Where 5F40, 5F60, and 5H com-pressors are used in refrigerant cycle reversing heat pumpapplications, it is usually necessary to modify the standardcapacity control arrangement to satisfy unloading require-ments. On summer cycle, the compre...
Page 26 - The cylinders set up for unloading may be loaded or unload-; Table 18 — Capacity Control Steps and; Hot Gas Bypass —; Hot gas bypass may be required on
26 Application Requiring 50% Capacity Reductions — This isthe usual specification for heat pump applications and shouldcover majority of cases. The necessary modifications to com-pressor capacity control can be accomplished by ordering thecompressor with factory modifications and then completingmodi...
Page 27 - Table 19 — Compressor Starting Torques
27 The variety of systems using 5F,H compressors make it impractical to cover all aspects of hot gas bypass operation.The following guidelines will aid in determining the properapplication. The hot gas bypass valve is basically a pressure regulating valve installed to hold a constant compressor suct...
Page 28 - Table 20 — Belt Drive Packages
28 Table 20 — Belt Drive Packages LEGEND NOTE: Compressor shaft diameter before taper begins:5F20, 30 = 1.0 in.5F40, 60 = 1.5 in.All 5H = 2.0 DRIVE PACKAGE PART NUMBER COMPR SIZE HP FRAME SHAFT DIAM (in.) COMPR RPM CENTER TO CENTER (in.) FLYWHEEL PULLEY BELTS Pkg No. OD Pkg No. PD Pkg No. No. of Bel...
Page 30 - Fig. 18 — Flow Diagrams for Common Multistage Systems
30 When a capacity safety factor is used, the compressor is selected at its maximum speed to handle design load plus safe-ty factor. Multiplying factors for non-standard speeds areshown in Fig. 20. Whether or not added capacity offered by the safety factor is incorporated at once is a matter of judg...
Page 31 - Table 23 — Booster “R” Factors; Determining Intermediate Pressure —; Existence of a second appreciable load, at some higher; Gas Desuperheating —; Operation of a direct staged; Liquid Cooling —; It is also necessary to employ liquid; Oil Separators and Lubrication —; For booster application, factory oil charge should be drained; Fig. 19 — Booster Compressor Selection; Fig. 20 — Multiplying Factors —
31 Table 23 — Booster “R” Factors Air-cooled (R-12 and R-22) Water-cooled (R-22 only) Determining Intermediate Pressure — In applica- tion of commercial compressors to staged systems, the lowesttotal bhp per ton and most economical equipment selectionresults when using approximately equal compressio...
Page 32 - The standard dual pressure switch furnished with the; Table 24 — Control Pressurestats for; Fig. 21 — Optimum Intermediate Temperature for 2-Stage Compression
32 Control Pressurestat for Booster Applica-tion — The standard dual pressure switch furnished with the 5F,H compressor cannot be used for booster application.Replace it with an appropriate low temperature dualpressurestat that can operate at values shown in Table 24. Anycommercial pressure switch i...
Page 37 - Table 28 — Booster Compressor Starting Data
37 Table 28 — Booster Compressor Starting Data *Based on 1750 rpm with 5F,H compressors. Will vary directly with rpm at other speeds. CONDENSERS Condenser Physical Data — Refer to Table 29. Re- fer to 5F,H Product Data for information on the currentP701 water-cooled condensers used with the 5F,H wat...
Page 39 - Table 32 — Condenser Water Circuiting
39 Water Circuiting Arrangements — The water cir- cuiting arrangement selected for 5F and 09RH condensersdepends on available condenser water pressure, temperature,quantity and source. Refer to Table 32. Refer to the Carrier System Design Manual for specific information and recommendations for refri...
Page 40 - With the increase in brine flow rate, the rise will now be:; WATER TO GLYCOL FLOW; Fig. 22 — Water to Glycol Flow Rate Correction
Manufacturer reserves the right to discontinue, or change at any time, specifications or designs without notice and without incurring obligations. New PC 802 Catalog No. 510-509 Printed in U.S.A. Form 5F,H/09RH-2XA Pg 40 8-02 Replaces: 5F,H/09RH-1XA Copyright 2002 Carrier Cor poration Book 3 Tab DE1...