Carrier 30HR User Manual

Carrier

«>

30HR,HS040, 050,060

Hermetic Reciprocating Compressors 40 thru 160 Tons

зон R160

30HR,HS070thru 160

DESCRIPTION

These modern multiple-compressor liquid chilling pack ages offer all the conveniences and economy of packaged design, for use in chilled water air-conditioning systems and various types of process cooling applications. Every machine is completely factory engineered and assembled to ensure a perfectly balanced refrigeration system. All com ponents are matched to perform with high efficiency and

low power consumption. Only external water and electrical connections must be completed to make the water-cooled unit operational. Condenserless models require, in addition, only refrigerant line connections to the remote condenser.

The water-cooled model (30HR) is a complete onepackage system with two condensers having built-in sub coolers, and a direct expansion cooler with two refrigerant*, circuits, one for each condenser.

FEATURES

• Low Inrush and Running Current because of sequential

starting and stopping Multiple Compressors*.

• Easy to Service bolted-hermetic compressors.

• Wide Range of Distribution Voltages (208 v to 600 v)

allowed by Carrier Voltage Standards*.

• Protection against Single-Phasing of compressor motors, assured by manual reset, magnetic-trip circuit breakers.

• Internal Motor Protection against overheating, provided

by quick-sensing elements embedded in motor windings.

• Optimum Control of Chilled Water Temperature for closer Capacity Control provided by Multiple-Step

Controller.

Model 30HS is a condenserless 30HR, designed for use with remote water-cooled, air-cooled or evaporative type condensers Includes all features of the 30HR.

Multiple serviceable compressors are mounted on spring

vibration isolators to minimize sound and vibration trans

mission to the unit frame and the building structure. Hot-gas mufflers dampen compressor gas pulsations, giving smooth, quiet operation.

Each refrigerant circuit includes a thermal expansion

valve, a liquid line solenoid valve, a filter-drier and

combination liquid line sight glass and moisture indicator.

Compact construction allows passage thru 36-inch door

way. Little floor space required for installation.

• Balanced Wear on Compressors assured by manual

transfer switch, which changes the lead compressor in the

starting sequence.

• Increased System Capacity, without raising horsepower

requirements, afforded by refrigerant subcooling.

• Protection against Refrigerant Migration and Oil Dilution

provided by compressor crankcase heaters, which are on during compressor off cycle.

• Reduced Power Costs because of partial load operation at higher suction temperatures made possible by two

separate refrigerant circuits.

©Carrier Corporation 1969

^Single feature sheet available

Form 30HR,HS-5P

ACCESSORIES

• Oil Pressure Safety Switch Package available for water-cooled

units (standard on air-cooled units)

• Condenser Manifold Package, available for all 30HR units except

30HR160, provides common inlet and outlet water connections Package contains two steel manifolds, each in two sections Field welding required

• Control Circuit Transformer, field-installed, provides 115-volt

secondary ciicuit if separate source is not available

• Chilled Water Flow Switch prevents compressors from operating

unless water is flowing

• Unit Enclosure Panels, with fiber glass insulation, completely

enclose compressor and condenser section.

PHYSICAL DATA

UNIT PHYSICAL DATA

UNIT 30HR,HS APPROX OPER HR

WT (lb)* HS

REFRIG CHG HR

(R-22)t HS 44 55 64 78 88 98

COMPRESSOR 06Et

% Cap.^ Ckt 1

Ckt 2

No. Control Steps Total Cylinders Total Oil Chg (pt)

CONDENSER 09RP 30HR Units Only

Ckt 1 Ckt 2

REFRIG CONN, (in.) N

Liquid Discharge

040 050

2747 3186

1820 2210

79 94 5 99

55 60 50 57 45

022 027 022

2 % 2 Vs 2 y 2 ly» 2..iy

40 50

33 38 47 52 57

022 027 033 033

060 070 080 090 100 no

3313 2280

027

2 ly

4940 3470 3525 3585 4470

1 16 131 141 164 174

Reciprocating Semihermet

14 16

043

1 iy¡

5125

62 5 37 5

1. ly

054

iVs; 1

o. Size

5350

67 50 55 50 33 50

7 8 8 18

070 054 033

1 2y 1 ly

6400 6525 6655

1 13 122 132 148

c - 1750

20 22

66 71

054 054

2 ly

4530

rpm

45 50 50

070

2 ly

1 2 y 1 ly

120

7580

4590 5290

183 198

24 76 76

070 070 070

2 2 y

140

8000 5400

50 50

24 24

070

2. 2Vs

160

220

168

084 084

*lncludes refrigerant operating charge. tSOHR shipped with full oper charge, 30HS shipped with holding

charge (charge for remote condenser and interconnecting piping added in field).

COOLER PHYSICAL DATA

UNIT 30HR.HS

SHELL, Net Vol

(gal.) OD (ft-in.) Length (ft-in.)

TUBES

Number Length (ft-in.) Outside Area

(sq ft)

REFRIG CIRCUITS REFRIG PASSES MAX DESIGN WKG

PRESS, (psig)

050,060

040

23 6 36 5

0-1 oy 0-12y 6- 0V4

7- 6

200 294

6-2V2 7-8 y

158 284

070,080,

Prime Surface

6-ll’/i6

Refrigerant Side - 235

Water Side - 250

100,110,

090

1-4 1-6 1-6

6-9 7-6

Copper

488

7-87.6

440 645 762

140,160

120

50 0 52 7

646 646

9-2%

2 2

WATER CONN. (In.)

Inlet and Outlet* Drain

*ASA flat-face flange

9-0

ifSee Electrical Data table for sizes and usage.

CONDENSER PHYSICAL DATA

(^DENSER 09RP

Length

TUBES

Number

• Length (ft-in.)

022 1 027 033 043 1 054

i-oy

3-1 oy0-1 oy

5-10 5-10 5-10 5-10 7-2

5-lOy.

0-1 oy

Integral Fi

56 64 84 84

5-1073 2

1-oy 1-oy

n, 19 Fins/in.

070 084

1-2

7-2 7-2

124

105

7-27«

Area

Inside (sq ft) Outside (sq ft)

44 8 51 2 66 8 82.8

145 166 217 268

117

103.5 121.5 336 394

SUBCOOLERTUBES

Number Length (ft-in.)

5 5 5 9

5-10732

7-2 y

Area

Inside (sq ft) Outside (sq ft)

6 1

WATER CONN. (in.F

Inlet

Outlet

4 C 4 0 4 9 8 8

4,0

13 0 13 0

13 0

272 3 3

272

2V2 272

272

15.9

3 4

28 5

2721

WATER PASSES

MAX DESIGN WKG

PRESS, (psig)

Refrigerant Side — 385

Water Side — 250

*ASA flat-face flanges (or weld neck flange). fTwo inlets on 30HR160.

DIMENSIONS

30HR,HS040,050,060

ACCESSORYMANIFOLD

2-7

1" FLARE CONNECTION

FOR WATER REGULATING VALVE, EACH CONDiSAMEON UNITS 30HR070-I60)

“I _!

CONTROL PANEL

D D

WATER

INLET

- i. COOLER

-9-0

3"_

0 0

0 ”[

MTG HOLE

! i-o|"diam

UNIT 30HR,HS DIMENSIONS (ft-in.)

DIAM

Height to chilled

Distance between

chi 1 led water outlets E

Distance from either

end of unit to water outlet F

Pull Space

Cooler Tubes G Condenser Tubes HI

Length A

Wiilth iuc? ^

" (HS) B

Height C

water outlets D

050,

040

060

7-6 9-0 */4 3-0

3-0

2-]%

2-1%

4-1%

4-1 %

0-6V s0-6 V4

6-2% 7-7

0-7%

0-8%

9-3%

7-0% 6-5%

6-5%

LEFT SIDE VIEW

WATER INLET AND OUTLET

NOTE: ALLOW 2-0 SERVICE SPACE AT REAR OF UNIT.

30HR,HS070thru 160

^SIZES 070-090 HAVE 3 COMPRESSORS; 100 THRU 160 HAVE 4.

DIMENSIONS (ft - in.)

UNIT 30HR,HS

070,080,090

100,110,120

140,160

*Overall length for 070 thru 120. Overall for 140,160 is 10-6-1/8, measured at cooler. t30HR140 only (manifold not used on 30HR160).

A* C

; 8-6 6-3% 4-2% 5- 9%

i 9-4 6-5%

9-4 6-5 % 4-4%

4-4% 5-11%

5-11%6

D E F G H

3- 8% 6-1

3-10% 6-8

3-10%6

8-1

2-0%

1 -9% 7- 3%

0-7%

6- 1%

8-10%

7-4% 1-4

6-1 6-1 l-4%4t

1-4%4

SELECTION PROCEDURE (With Example)

I Determine the unit size and operating conditions required to

meet the given capacity at the given conditions.

GIVEN;

Capacity ........................................................................................SOTons

Leaving Chilled Water Temp (LCWT)

Chilled Water Rise...............................................................................10 F

Entering Condenser Water Temp .....................................................85 F

Fouling Factor (Cooler and Condenser)

FOR 30HR (WATER-COOLED CONDENSER):

Enter the Ratings table marked 44 F Leaving Chilled Water Temperature. Read down the left column (CAP ) to 80 tons Note that either a 080 or 090 unit may be selected. Final unit selection should be based on present and future job requirements and the economics of the job. For this example, data from the table is shown below for a 080 unit.

..............................................

............................................

PERFORMANCE DATA

44 F

0005

II Determine from Ratings table operating data for selected unit.

Unit...............................................................................................30HR080

Saturated Discharge Temp (SDT) Compressor Motor Power input (KW)

Total Heat Rejection (THR) ....................................................101.5 Tons

Cooler Water Flow ..................................................................192.0 Gpm

Cooler Water Pressure Drop (PD) Condenser Water Flow

Leaving Condenser Water Temp (Lwt)...........................................95.6 F

Condenser Water Pressure Drop (PD)

For fouling factors other than .0005 refer to the Correction For

Fouling Factors table to: adjust the required capacity, correct the compressor power input, and correct the actual condenser water quantity required. ForA t (SDT — entering cond water temp) other than 30 F, refer to curve.

FOR 30HS (CONDENSERLESS):

Use the same method, with the exception that the condenser water data do not apply. For the remote condenser data, refer to appropriate Carrier condenser data publication.

...........................................................

.......................................................

..........................................

..................................................

...........................................

75.9 Kw

229.4 Gpm

107.0 F

10.7 Ft

12.0 Ft

CORRECTIONS FOR FOULING FACTORS

Ratings are based on .0005 fouling factor in the cooler and condenser. Correction factors for other fouling factors are given in the following table:

CORR FACTOR

FOULING

FOR CAPACITY

FACTOR AND COND WATER

Condenser

1 02

1.00

Clean

.0005

Cooler

1.01 1 00

.001 .98 .002

To correct capacity, adjust as follows:

a Adjusted required capacity (use to enter table)

_______ cooler factor x condenser factor

b. Actual compressor power input

= compressor kw (from table) x correction factor for

power input

c. Actual condenser water quantity

= gpm (from table) x cooler factor x condenser factor

required capacity

.94

________

CORR FACTOR

FOR

POWER INPUT

Condenser

1.00 1 03

1.10

Ratings based on: 10 F chilled water rise (suitable for 5 F to

15 F rise without adjustment), .0005 fouling factor in cooler (and

condenser on model 30HR), 15 F subcooling, and R-22.

Ratings in boldface type (44 F chilled water page) are in

accordance with the latest ARI Standard 590. Conditions:

30HR — 44 F leaving chilled water temperature with 10 F rise, 95 F leaving condenser water temp with 10 F rise and .0005 fouling factor in cooler and condenser.

30HS — 44 F leaving chilled water temperature with 10 F rise, .0005 fouling factor in cooler, 105 F condensing temperature for remote water-cooled or evaporative condenser, 120 F condensing temperature for air-cooled condenser.

Ratings based on 15 F subcooling. On 30HR units this occurs at 30 F A t (SDT — entering condenser water temperature.) When a 30HR (water-cooled condenser) unit is selected at conditions other than 30 F A t use the curve below to correct the ratings table capacity.

RATINGS

The following ratings tables are for both 30HR (water-cooled condenser) and 30HS (condenserless) models. Condenser water data apply to model 30HR only. Ratings beyond limits shown and/or brine ratings are available in Carrier Application Data publications.

Ratings shown for Saturated Discharge Temperature (SDT) over

120 F do not apply to model 30HR.

Correction = Ratings table capacity x percent capacity correction

(from above curve). Above 30 F At add the correction to rating table capacity. Below 30 F At subtract the correction from rating table capacity.

30HS units matched with remote condensers which have greater

than (less than) the 15 F subcooling in the ratings, increases

(decreases) system capacity. To adjust capacity, multiply capacity ratings by 0,94, then adjust this result upward by 0 4 percent for each degree F of available subcooling

PERFORMANCE DATA

30HR,HS RATINGS

Leaving Chilled

Water Temperature

42 F

COOLER

FLOW DATA

lOF RISE

(tons) (F)

34 0 j 131 4

36.G : ! 24 C 38 G

. ..“'V'.v,,

■ 40,7 Î 42 C i

44 C i 94 6 41 2

38 CÎ

40 0 j 127 4 52 6

4? C 1

.:.42.2. 0:12Q,0:: .50.2

46.0

46.4

46.9 1 5.05.0 .45.5. ...59.8

48 0

50 0

44.0

46 C

48.0

.:::49.7. i.:î2Û.O .l.S9:6T..66,.6.; .:U9.2

50.C 52 C

54,0

...55.3:

56.0

. ..56.3. Î ’.Q5.Q

58 C

60 0 96.8 62 0 92 2 50 4

54 0

56.C 58 C 126 2 74 0

60 0

.....6L2

62 C ^

64.0

66.0

68.0

68..5

. ,69.3.

70 C

72 0 100 2

60 C 62 C 132.3 86 8 86 6

64 0

66 C

68.0 121 8

, 69.0,

70. C 72 C

74.0

76.0

V 77.5

78.0

.78.,!,

80. G

82,0 65 0

70 0

75 C 122.2

: 76 .4, i: J2S.0 .90,5

80 0

85 C

S6.0

, ,:S6.3.

90.0 95 0

! .120.0 . 49..G .50.9Î .89.0. 7.4

I 1 16 7 48 0

109 4 45.7

040

107.0 44.9 53.4

- J05.0.. 102 1

134 2

120.8 Ì08 n

050

ÎÔ6.8 46.2 101 6 44 6 60 7 115.2 5 3

95 1

133 9 64 4 ^62 3 105 6 128 9 62 7 63.8

124 ]

i 1 19 4 59 4

1 14 8

060

.1..1.C..3..

U07..4 ..5.5.4. 1C5.S.

101 3

134 2 77 4 130 2 75 7

122,4

; 120.0

118 6 70 8 82 1 148 8

070 114 9

111.2 67 7 85 2 158 4 7 3

107.6

; 306.6 :

;..ÌQ5.0,:

103 9

136 0 128 7

125 2

! 123.0 80.9 92 C

i ¡8 4 80,1

080 115 0

111 7

108.5 75.5

.Ì06..1..

105.2

, 5.05.0

101 9 72 5 100 6

98,6 71.0

138 6 130 1

114 5

090

107.0

Ì05.5

,5.05.0.

99 5 91 8 75 9 1 16 5

(tons)

48 8

52 2 .50.2 .50.2 86 4

51 6 91.2 7 8

53.0

.53 ..8 .. 98-9 .. 9.2 78.5 91 4

44.3. 43 4

54.3

55.7 105.6

54 8 53 6 91 2 3 3

54 9 96 0

SO s

56 3 100.8

,55.4 ; 1GÎ.4 4, ;

46 F

42.7

61 0 65.3

57 8

-jr\ rv

..56...3,

. .«’.y V.

.7Î..C. .132.6 .,71.6.

..54.S.

.54.5 ..7.LS.

53 3 73 1

51 9

72,4

80..5

.7,1.3

.81.5.

69.2 83 7 153 6 6 9 1 15 5 92 4 2 6

66.2 86 8

6.5.8

.0,5.2.

64 8 63 3

88 6 85 0

83 4 89 7 81 7 91.2 163 2

78 5 77 C

.-74.4, 93.6

74.0 :..99.ü

.73.9

102.2 196.8 11.3 [202.1 87 1 9 5 329 2 87 4 23 7

100 2 93 5

95 6 91 4

,100.9 104 '8

87 3

83.4 ,108.7 204,0 1 ? 1 151.0 92 6 4 5

82.7 Î09.S

:82..4

l'D9.7 ,207.2 .32,5. 151.1

1 12 6

79.6

Gpm 81 61 6 3

100.8 9.6

1 10 4 4.9

5v.2

59.5 !!f.2 'll 2.6 5.0

62 1 120,0

1 10.4 4 9 1 15.2

120 0

66 9

124 8 6 2

68 4

: 79.6 6 7

,,!.3.4..4. ,135,2.

139 2 7 8 144 0 8 3

74 7

148 8

76 3

129 6 4 9

76 C

77 5

134 4 5 3

79 0 139 2 5 6

3 A_A r\

. i:47_o . .6-2 1 15.5 92 0 2 5 1 15 5

163.2 7.S

n64',5

.87.2

87.9; :.:166.5. 8.0 88,4 168.0

172 8 8 7

90.0 144 0 6 0

85 2

148 8 6 4

88.2 153 6

158.4 7 3

„:T65;6 .8.0.

Î 68.0 8 2

92 S 94 3 172 8

95.9 177 6

97.4

182 4

: TS5.9: lO.'.l

187 2

99 G

137.4 .10.2

192.0 10.7

156 0

97.2 168 0 8 2

180.0

:l.83..3i 9.7 151 0 91 5 4 5 151 0 96 5

Î02.0

192 0

2'D6.4

216 0 13 6

228.0 15 1

75 80

Gpm Lwt (F) PD

_ _

7 0

72 0

96 0

97.6 .9.0 73 3 92 5 2 2

:..7.0;.

....7,2.

72 0 92 2 2 1

8 7 72 0 92 7 2 1 78 4

90 4 89 4 3 2

10 5

174.3 82 7 11 1

3 7

4.1 78 0 78 0 93 1 2.1 90 6

5.0 78 2 83 4 92 1 2 3 1116

102 1

5.8

183 3

4 5

S 7

. S.7. , 84 0

5 8

84 0 94.1 84 0 94 6 2 1 84 0 84 0 95 0 2.1 87 1 94 6 2 3 1 15 6 94 7 95 9 92 9

7,3

101 2 131 8 88 3 5 4 201 3

200 1 84.0

8 9

6.0 6 4

115 5 92 1 2 6 115 5 97 1 2 6 1 15 5

1 15 5 93 1 2 6

7.9 1 15 5 93 2 2 6 142 2 94 8 120 1 92 6

8 2

127 2 163 6 88 2 5 0 256 3 88 5 11 5

6.9

7 8

127 5 92 3 4 0 127 5 92 5

8.7

127 5 92 8

9 2

127 5

9,7

127.5 93 4 127 5 93 6 4.0 158 8 94 9

iC 2

128 1

129.4 155 5

7 1 9 4

10.7

151 0 92 0

Î2.4

151 0 92,7

200 2 88.8

92.0 2.1 72 0 97.0

__ _

_ _ _ _ _

92.2 93 2

89 2

83.1 11,2

_ _

_ _ _

94 0 2.1

92 1 3 1

~ - - - - - - - - _ _ _

— _ _ — —

— _ —

—

92 8 2 6 1 15 5

91 7

_ _ _

— — —

— _ — _ _ —

— _

93.1 4.0

93 5 4 0 169 9 93 3

90.5

_ _ _

_ — — _ - — — —

92 7 4 5 185 5 94 4 6 7

2 4

2.1 78 0 2 1

3.6 151 2

_ _

2 1 84 0 99 1

2 8 I3I 6

12 6

2 7 3 : 175 7 92 1 5 7 288 1 92.4 14 4

—

4 0 127 5

4.0 4 0

4 0 172 8 93 8 7 0 5 8 227 5

4 5 4 5 178.1 95 0

7 7 316 7 88,8 17 9

CONJJENSER WATER

Entering Water Temperature (F)

85 90

Gpm

Lwt(F) PD

_ _ _

_ _

72.0

97 2 96 2

89 3 103 2 129 2

141 6

115 5

133.2 160 7

127.5 97 3 127 5 97 8 4.0

127 5

135.1 97.3 4.5

151 0 97.0 4.5 160 7

94 3 3,1 92 6 4 1 162 0 93 2 9 9

90 1

- - - - - - - -

_ _ _ __ __

97 2 2 1 95 6

97 3 94 6

92.8

89.6 7 7

- - - - - - -

__ _

—

84 0

99,0

95 1 97 7 2 8 131.2 97 8

99 6 2 1

93 1 92 3 6 3

88 7 _

_ _ _ _ _ _ _ _ _

— _ — — _ —

97 0

97 4

97 8 2,6

95.7 3.4

93 2 4 8 253 0 93 4 11 4

_ _ _

— _

97 5 4 0

98 1

94 0 6 8

90 6 11 8

— —

96 4 5.2 230.0 96.6 10.0

- -

Gpm

Lwt (F) PD

_ _ _ _

72 0

2.1

72.0

2.1

2.5 103.5 i:28.T

227 3

6 3

78 0

IT? 9

2.8

3 3

]42„3 .95.0 Ó.8.:

4.2 174 2

__ _ _ _

84 0

2 1

84 0 104 1

2 1

94.2

4 1

5.7£),:6 .9.T

5 4 203 0

224 6

12 7

_ _ _ _

_ — _ — _ _ — _

2 5 115 5

115 5 115 5

2 6

140 3 99 6

190.3 ^6 0

3 8 SiÓ.2

_ — _ — —

_ _ _

_ — —

4.0 127 5

127 5

127.5

145.5

4.0

1.88

6.0 Ì236.3 . : .95:,C.:. 260 7 94.1 IS 3

267.3 93.9

4.5 151 C 101 5

151 0

6.2 '263.:7

286.0

102 0 102 2 2 ;

97.3

;95.;,Q’

90 7 18 0

_ _ _ _

102 2 2 1 80,7 106.7 2 2

96.1 5.6

93 2 10 2

—

_ _ _

— _ __ _

104 0 2.1

102 4 2.7 130 6 102 6

9 3 .5 92 8 16 2

102 0 2 5 1 15 8 102 1 102 4

. 95 0

- - - - - -

_ _ _

_ _ — — —

102.3 102 5 102 8

100.8 5 1 211 2

97.4

—

- - - - -

—

— —

— — -

102 0

T::'95.1QV: T3;3.

94.5 15.C

Gpm

Lwt(F)

_ _ _ _

74 2 106 5

2 1

87 2 104.3

4,1

164.4 97 8 9 9

; 6.'2

215 7

— — —

_ _

_ _ _ _ _

96 6 15 5 _

_ _

90 6

2 1 93.0 107 3

204 6 98 2 13.2

5,3

13,0

2 6 2 6

208 1 99 9

3 7

6.6 328 9

7.9

_ _

4 0

4.0 128 2

4.0 158 2

305.0 97 7 20 6

8 3

:52.7,

16.0 _

4.5 4 5 177 3 104.3

— -

107 7

—

— — _

—

_ _

—

_ — _

—

106.9 1 17 0 106 9 148 5 103.6

96 4

— __

—

_ _

— —

- -

—

107 3 104 3 100 9

- -

- —

- -

— —

- — —

106 5 4 5

- _

- —

127 5 107 3

151.0

2 2 3,0

_ _

2 4 2 6 5 3

_ _ _

2 5 2 6

4.1 7 8

18 4

_ —

— _

4.0 4 0 6 0

10.3

—

6.2 —

CAP. — Capacity KW — Compressor Motor Power Input at Rated Voltage

r ~1 Shaded areas show ratings for 105 F and 1 20 F condensing temp and ratings with 95 F leaving condenser water temp with 10 F rise

* Ratings for SDT above 120 F do not apply to 30H R

Lwt — Leaving Water Temp (F) PD — Pressure Drop (ft)

SDT - Saturated Discharge Temp (F) THR — Total Fleat Rejection (tons)

^2 P Leaving Chilled

Water Temperature

CAP.

SIZE

SDT*

(tons)

75.0 80 0

85.C

87.6 ' 90 0

95.0

98.7

99.5

100 .0

105.0 85 C 1

90 0 1

95.0

.95,5:

100 0

105.0

107:71 iOS,2.

1 10 c 1 15.0

90.0

95.0

100 .0

■f03;3

105 0 1 10 C 1 15.0

116.6 )57.0 Ì20.C 125 0

102 .0 Ì34.5 106 0

1 10. 0 1 14.0

1)5.7

1 18.0

122. 0

126.0

129.0

.13G..5,

134 0

1 17.0

121.0

125.0

129.0

.;3U

135 0

139.0 ;45;0

546,4

1 50 0 154 0

(F)

137.4 112 4

130.3 108.0 1 10.7 1 23.6

;t2o;q' 501.8: .Ì5Ó.6

117 0 100 1

inn

1 10.7 96.4 l'Oó.Oi

:5.Q5.,0.

104.4 92.8 126.3 240.0 11 3 166.1 98 :

133 ;

126.8 115 8 120 6

!.12a.O:' i 11.415:27.5::

114 7

1 in

' ' 108.8 n04 2

105.7 ¡102.3

505.0

103 0 10 0 6

97 1

135 6 132.1 127.5 129 6

123.8 123 6 135 1 240.0 11.3

1 T20.0?120.'9.

1 1 18 2 119 7 139.0 252 0

520

1 12 7 1 15 8 142.9 264 0 13 6 158 0

' 107.2 11 2. 1 146.8

105.5

505.0 101 8 108 4 150.8

96 3

130 1 151 4 149 0 254 0 7.0

125.8 148 5 152 1 121 7

1120 .0

140

Ì ‘¡7.5

113 5

' 109.4

106.4 5,05.0

101.4 127 3 134 : 179 6 feo 0 28Î.C 8 4

130 1 126 C 172.8 174 1 300.0 122 Q 169.0 177.C 310 .0

; 120.0,

160

1 16 1 162.91181 3

1 12 2

106.3 1,52.3

1Q5..0

101.4

97.51143 1 194.6 370.0 13 7

PERFORMANCE DATA

-‘■"T ' " j COOL

,ER

THR

(tons)j Gpm

106 9 180 0 1 14 5

104.0 1 18.4

] 90 4

935/

T2S.3 236.9

93.5:1.125.9 238.S

89.2 130.3

119.1 204 0

120 .0

122.9 216.0 9.1

111.8

126.8 228.0 10. 2

108.0 130.7 240.0 Ì Ì 3 145.0

134.6 5 3c. 7

,505.8 137.2

138 6 264.0 13 6 194 2 92 2 5.1

97 C 142 5 276 0 14.9 312 5 86 0

127 8

131.3 ,137.6

14S:T

no. 9

148.4

5 50.6

104.8 154.8

154.6 145 9 245.0

144.7

155 1

'¡43:3'

156.3

Ì 4 2

158.1 283'C ‘

137 7 161 1 293.0

164.1

134. 2

566.4

5.3 5.6

167.5 353-0 ;0.2

130.3 170 2

DATA LISE

Gpm

Lwt(F)

_ _ _ _ _

6 3

192.0 7 2

204.0 8.1 ,8.6. 126 0 97.2

210,4.

216.0

228.0 10. 2 126 0 98.3

n.G 151.1 94 9 n.i. 160.1 93.9

252.0 12.4

— _ _ _ _

9.1

126.0

268.6 86 .6 10.7 - - - ~

8.1

_ _ _ _ _

229.2. .50:3..

252.0

258.5 53.1

259.6

216.0 9 1

228 0 10 .2

:24S„0.:

2.76.0

279:.B 55 3 177.2

280.6

288.0 16 2 222 8

300 0

264 0

274.0

278.0 8 .2

302.0

3I0V0

322.0 10.7

145 0 96 1 2 9

145.0

12 4

164.9 171 3 94 3 4 0

13.1

— — _ _ —

158.0

12.0

12 4 158 0 96 1 2 7 14 9

162 3

15.4 181 5 94 6 17 6 355.5 85 4 12 6

■‘8.5 160 0 99.0 2.9

10.0

6 5

_ —

7 5

8.0

160 C

9.0 160.0 99.0 2 9 169 0

9.6 197 0 95 0

215 0 94 0 275 0 90.0

_ _ _ _

176 4 171 1 290.0 8 9

10.G

.566.9 578,5.1 3.15.0. T0.3 158 71184.1

150,8 189.3 147 1

324 0 334 0

188-3 34S.0 12.3

351.,0:

191 8

360.0 13 1 308 0 90 0 6 7

10 8 180 0 99 0 11 4

12.5

_ — — _ _ _

9.4

180 0 99 0 180 0

225 C 95 0

100 0

244. C

429 0

30HR,HS RATINGS

ENSER WA

COND

8 0

102 .2 102 6

94 9 93 9 93 2

101. 1

98.3

95.0

94.3

92.1

100.9

101.7

96.9

95 1

104.0

98.0

95.0 94 0

104 0

104.0

95.0 90 0

ater Temper

PD ; Gpm

2 6 126 0

132 9

2.6

197.8

3.5

6.2 300.9-

335.2

7 2

358 5

7.9 _

145.0

2.9

162 5

2 9

245.1 98 2

4.3 6 4

33.1.0 ,:9S.O. . 7 Ì ¡356 4 9 8

158.0

2.7

158.0

2 7

2 7 194 9 4 6 298,5. 5 8 I35.5-.6

372 9 94 6

6.2

10 6

- - - - - - -

_ _

_ _ — —

160.0

2.9

2.9 174 0

219.0

3 3

4.9

298 0 98.0

7 21400.0

8.9 474 0 94.0

16 3

181.0 109.0

2 3

215.0

2 3

274,0

3 1

6.4

447 .0

517 C 94 0

7 9

14.6

itering W

7 5

97.6 2 6

93 3 4 3 _

Gpm

2.6

126.0 126 0

2.6

148.1 99 8

3 6

201.7

4.C

218.1 229 2

Lwt(F)

__ _ _

145.0

96.8 97 4 2 9 95 0 3 8

_ _

— 95 9 2 7

96 7 2 7 96 7

95.1 3 4 91 2

—

_ _ _

98 0

98.0

— _

__ _ _

94.0 86 0 12 ^

2.9

12.4

2.9

3.5 5 2

_ _

2 9

3.3

4.3

5.C 7 7

2 3

2.3 2 3

3.6

4.2

145 0 101 8

177.3

220 .0

231.8

275 7

158 0

158 0 1 01 .1 158 0

208.2 235 7

243 8 94 6

325.1 91 1

160.0 103 0

160 0

172 0 103 0

214.0 264 0

298.0 419 0 90 0

180.0 180 0 209 0 101 0

301 c

335 0 94 0

458.0

TER

ature (F'

"^Ts

Lwt (?) pd" Gpm

_ _

107 2

106.4 2.9

99.8

:, 951.0 . , M3.2

94.1

93.5 18 3

_ _

106.1 104 3 3 7

94.3 15.9

— — — _ _

_ _

2 6 142 9

172.0

6.0 296.3 99.9 12 .8

16 2

2.9 154.0 109 8

218.7

7.9

389,8

1:3.,8

- -

— — _ _ _

— _ _ _

105 9

106.1 102 .6 4.1 274.2 102 5 7 7

.. 96.8,.

.55.0 12 .6

_ - _

—

_ —

108.0 2.9

107.0

103.0

,..95.0. :15*Q.

164 8

2 7

182 2

2.7 503 1

..9.0, 13 7

_ _ __ _ _ _

194.0 109.0 4 1

3.4

225 0 107 0 5 4

312.0 102.0 9 7

5.2

8.9

480 0 98 0 20 7

20 3

90^ -

Lwt (F)'

_ _

109 6

106.5 4 6 _

_ _

104 4

98 4 18.8

— _ _

— _

- -

_ _

110. 1

108.3 3.6

24 1

97 0

_ _ _

_ _

—

_ _ —

- - - - - -

...95.0

— —

105.0 3 3

101.0 5.3

— — _

_ _ _ _ _

_ _ _

223.0 109.0

2.3

286.0 396 0 101.0 11.0

13.9 18 7

_ — —

_ _ _

105.0 5.8

—

_ —

- - - -

3.2

3 3 6 4

2 9

3.5

_ _

_ _ _

_ _

„

_ —

44 F

CAP. ¡SIZE (tons)

36 0 :

38.0 i

40.C

040

42.0

42.6

44.0

46.0

Leaving Chilled

Water Temperature

SDT’

(F)

128 9

121.7!

Î2C*Q.^

114.6:

107.Sr

105.0;

100 3

92.9

THR

(tons)

52.4 50.9

50.2 52.3

49.6; 52.61

48.01 53 6 I

45.7; 55.0 [

44.9; 55.41

43.4' 56 3 !

41.21 57.71

COOLER

FLOW DATA

lOF RISE

G pm

86.4

7 0

91 2

7.8

92^3 ) 7.9

96.0 I 8.7

Î00.3 1 9,6 Ì02.4 i 9.8

105 6 no.5

110.4J11.5 Ì218.0

Gpm

72.0

72.0 73 7

81.6

107.0

Lwt (F)| po’

92.5

92.9 92 9

91.3

87.6 ¡16 7

81 4

Gpm

2 C : 72.0 2 1 i 72.0 2 2 90 3

2.6

108.3

4 4

165.4 I

CONDENSER WATER

Entering Water Temperature (F)

80 _

2.0 2 1

3 2 4 5

10 0

Gpm85Lwt(F)

72 0

102.5 2 0

79 3

m.7i

171 4

95.0 6.2

93.0 I 10.8

Lwt [F)

97.5 97 9 94 6 92 4

88 2

2 5

Gpm

77 6

105.3

217.0

Lwt(F)

106 3

102 3

96 1

2.4

4.3

16.7

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