Carrier 19EA User Manual

4 (2)

Carrier

ermetic Centrifugal Liquid Chillers

INTRODUCTION

persons concerned with the start-up and ope^ion of the 19EA machine should understand thteie instructions and all necessary job data before initial start-up. Instructions are in proper sequence for optimum machine performance.

Data and Equipment Required

PRINTS:

Machine assembly wiring, and

 

piping

 

Starter diagrams

 

Special controls and related

 

wiring (if any)

INSTRUCTIONS: 19EA Installation book 19EA Operating and Main­ tenance book

Starter Instructions

MATERIALS: Mechanics’ tools, electronic or halide leak detector, clamp-on ammeter, volt-ohmmeter

INITIAL PREPARATIONS

Machine Tightness — The 19EA is shipped with the refrigerant charge in the utility vessel and a holding charge (10 psig) in the unishell. Several levels of leak testing may be required depending on condition of machine on arrival and at start-up. Determine machine condition and follow pro­ cedure indicated in Table 1.

For transferring refrigerant and evacuating vessels, follow the pumpout instructions on pages 3 and 4.

Table 1 — Selection of Leak Test Procedures

MACHINE CONDITION

PROCEDURE

1. Unishell holding charge

4

and utility vessel refrig­

erant level unchanged.

 

 

 

2 Unishell holding charge

3 and 4 on unishell

decreased slightly.

 

 

 

3. Utility vessel refrigerant

Leak test with halide or

level decreased slightly.

electronic leak detector.

 

 

4. Unishell holding charge

 

completely gone Opened

1

valve or other open con­

 

nection suspected.

 

 

 

5 Unishell holding charge

 

completely gone Vessel

'2., 3, and 4 on unishell

leak assumed

 

 

 

6 Refrigerant charge in

1 - Use nitrogen with

utility vessel completely

R-12 tracer in pressur­

gone. Opened valve or

izing for leak test pro­

, \ other open connection

cedures 2 and 3

suspected.

 

7 Refrigerant charge in

2, 3/ and 4 on uti! ity

utility vessel completely

vessel. Use nitrogen with

gone. Vessel leak

R-12 tracer for pressuriz­

assumed

ing in 2 and 3

 

 

Nev«f charge Squid refr^erant into the unisheii if vessd isressarc is beiow 3S ps^.., or vtaife water pumps itoi op«ratirig. Cooler tube freeze-trp and. dam^e may rearlt,

PROCEDURE 1 — Standing Vacuum Test

1. Attach a mercury manometer (absolute pressure-type) to the refrigerant charging valve,

(6) Fig. 1. A dial-type gage cannot indicate the small amount of leakage acceptable during a short period of time.

2.Pull a vacuum on the vessel (see evacuating procedures on page 3) equal to 25 in. Hg, ref 30-in. bar. (2.5 psia), using the pumpout system pump.

3.Valve off pump to hold vacuum, and record manometer reading.

4.If the leakage rate is less than 0.05 in. Hg/24 hours, perform procedure 3, aU steps under Machine Dehydration and procedure 4.

5.If the leakage rate exceeds 0.05 in. Hg/24 hours, perform procedures 2, 3, all steps under Machine Dehydration, and procedure 4 in the order indicated.

6.Remove mercury manometer from refrigerant charging valve.

PROCEDURE 2 — Follow steps 1 thru 4 of Return Refrigerant to Normal Operating Conditions, page 3. Raise vessel pressure slowly to 5 psig by cracking open valve 4. Perform leak test with hahde or electronic detector and repair any leaks.

PROCEDURE 3 — Following steps 1 thru 5 of Return Refrigerant to Normal Operating Condi­ tions, page 3, raise vessel pressure to 35 psig. Perform leak test with halide or electronic detector and repair any leaks.

PROCEDURE 4 — Equalize pressure between utility vessel and unishell following steps 1 thru 5 of Return Refrigerant to Normal Operating Conditions, page 3. Vessel pressure will be approxi­ mately 70 psig. Perform leak test with halide or electronic detector and repair any leaks.

If refrigerant charge was lost and nitrogen has been used for pressurizing in procedures 2 and 3, evacuate vessel and then charge 400 lb of R-12 for procedure 4. If vessels are then leak tight, continue charging refrigerant to the level indicated in Charging Quantity Table below.

Table 2 — Charging Quantity

MACHINE SIZE

WEIGHT (lb R-12)

19EA 400, 430, 465

2000

19EA 500, 550

2200

19EA 590, 630

2400

Form 1PFA-1.S?;

COMPRESSOR MOTOR

COMPRESSOR

TERMINAL BOX

MOTOR DRIVE

 

e, add

CONDENSER

REAR VIEW

SECTION

COMPRESSOR

/ MOTOR DRIVE

CONDENSER

 

CONTROL BOX

 

 

 

 

 

FRONT VIEW

PUMPOUT UNIT

COMPRESSOR

COOLER

UNISHELL

LEGEND

1 Pumpout Service Valve 1

20. Sight Glass — Rotation

2 Pumpout Service Valve 2

21. Sight Glass — Seal Oil

3

Pumpout Service Valve 3

22

Sight Glass — Liquid Level

4. Pumpout Service Valve 4

23

Sight Glass — Liquid Level

5

Pumpout Service Valve 5

24. Sight Glass — Liquid Level

6

Pumpout Service Valve 6 and Refrigerant Charging Valve

25

Sight Glass — Liquid Level

7. Pumpout Service Valve 7

26

Refrigerant Drain Valve

8 Pumpout Service Valve 8

27.

Isolation Valve

9. Service Valve 9 (hidden between unishell and utility vessel)

28

Isolation Valve (hidden)

10

Differential Pressure Gage (oil)

29.

Isolation Valve

11

Condenser Pressure Gage

30. Isolation Valve — ball valve between unishell

12

Cooler Pressure Gage

 

and utility vessel (hidden)

13. Dehydrator Water Valve

31 Chilled Water Control Element

14

Oil Level Sight Glass

32

Pumpout Vent Valve with Flare Cap

15

Oil Temperature Gage

33.

Bearing Return Oil Thermometer (hidden)

16

Oil Heater (with indicator light)

34

Dehydrator Pressure Gage

17. Oil Heater Thermostat

35 Dehydrator Discharge Hand Valve

18 Oil Pressure Regulating Valve

36.

Oil Cooler Plug Cock

19 Oil Reservoir Charging Valve

37 Chilled Water Lo-Temp Cutout

Fig. 1 — Machine Components

ISOLATION VALVE OPERATION

Opening Compressor must be off and vessel pressures equalized (see Return Refrigerant to Normal Operating Condition, steps 1 thru 6).

^.Loosen packing nut 1/2 to 1 turn so valve stem will rotate and slide smoothly in packing. Do not let refrigerant trapped in valve body escape.

2.Hold stem in against line pressure and rotate stem counterclockwise as far as possible.

3.Slide stem out of body.

4i Rotate stem clockwise in the out position, until snug.

5. Tighten packing nut. Closing

1. Loosen packing nut 1/2 to 1 turn so valve stem will rotate and slide smoothly in packing. Do not let refrigerant trapped in valve body escape.

2.Rotate valve stem counterclockwise as far as possible.

3.Slide stem into valve until it bottoms.

4.Rotate stem clockwise, holding assembly in, until it is tight (25 ft-lb).

5.Tighten packing nut.

TRANSFER REFRIGERANT FROM UTILITY VESSEL TO UNI SHELL* from normal operating condition.

1.Add manometer near charging valve 6.

2.Close isolation valves (27), (28), and (30).

3.Open valves 1, 3, 4, 6, 7 and 8.

4.Close valves 2, 5 and 9.

5.Ensure that pumpout condenser water is off.

6.Turn on pumpout compressor until liquid is out of utility vessel.

7.Turn off pumpout compressor.

8.Close isolation valve (29).

9.Close valves 3 and 4.

10.Open valves 1 , 2 , 5 and 6.

1 1 . Turn on pumpout condenser water.

12. Run pumpout compressor until utility vessel pressure reaches 25 in. Hg, ref 30-in. bar. (2.5 psia).

13.Turn off pumpout compressor.

14.Close valves 1, 2, 5 and 6.

15.Turn off pumpout condenser water.

TRANSFER REFRIGERANT FROM UNISHELL TO UTILITY VESSEL* from normal operating condition.

1.Open drain valve (26).

2.Wait one hour; close isolation valves (27), (28) and (30).

3.Open valves 1 , 2 , 5, 6, 7 and 8.

4.Close valves 3 and 4.

5.Ensure that pumpout condenser water is off.

6.Turn on pumpout compressor for 20 minutes.

7.Turn off pumpout compressor.

8.Close isolation valve (29). Close valves 2 and 5.

10.Open valves 1, 3, 4 and 6.

11. Turn on cooler and condenser pumps and pumpout condenser water.

Fig. 2 — Pumpout System Schematic (See Fig. 1 Legend for Item Ref)

12.Run pumpout compressor until unishell pres­ sure reaches 25 in. Hg, ref 30-in. bar. (2.5 psia). Use dehydrator gage (34) for pressure reading.

13.Turn off pumpout compressor.

14.Close valves 1, 3, 4 and 6.

15.Turn off pumpout condenser water.

UTILITY VESSEL EVACUATING PROCEDURE*

1.Close valves 1 , 2 , 3, 4 and 9.

2.Open valves 5 , 6 , 1 and 8.

3.Open vent valve (32) and remove flare cap.

4.Turn off pumpout condenser water.

5.Operate pumpout compressor until manometer reads 25 in. Hg, ref 30-in. bar. (2.5 psia).

6.Close valves 5, 6, 7 and 8.

7.Shut off pumpout compressor.

8.Close vent valve (32) and replace flare cap.

UNISHELL EVACUATING PROCEDURE*

1.Close valves 2, 4, 6 and 9.

2.Open valves 1, 3 and 5.

3.Open vent valve (32) and remove flare cap.

4.Turn off pumpout condenser water.

5.Operate pumpout compressor until manometer reads 25 in. Hg, ref 30-in. bar. (2.5 psia).

6.Close valves 1, 3 and 5.

7.Shut off pumpout compressor.

8.Close vent valve (32) and replace flare cap.

RETURN REFRIGERANT TO NORMAL OPER­ ATING CONDITION *

1.Ensure that opened vessel has been evacuated.

2.Close valves 3, 4 and 5.

3.Open valves 1 , 2 , 6, 7 and 8.

4.Run water pumps.

5a. If unishell has been evacuated — Crack open valve 4, gradually increasing pressure in uni­ shell to 35 psig. Feed refrigerant slowly to prevent tube freeze-up.

*See Fig 1 and 2 for all numbered references.

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