Document dQdVLO4eE149VGR24oG9a4gQR
KRACK WINTER CONTROL
Cootjuo Cofiootsea.
AIR COOLED CONDENSERS
Remold Type
Ball-bearing fan shafts. Alemite external
grease fittings for bearings and motor. Semi
automatic external belt adjustment (Pat. ap
plied for).
Bulletin AC-457
^Evaporator
"
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WC-IIE.I2
VX-ZK LUZ.
WC-31Zi.2>Zt
REFRIGERANT-12
REFRIGERANT-22
WINTER CONTROL MODEL
CAPACITY TENS
WINTER CONTROL NO.
CAPACITY TONS
WC-I12 WC-212 C-312
1 thro 7.*4 7.S thru 14.9
IS thru 35.
WC-122 WC-222 WC-322
1 thru 7.4 7.5 thru 14.9
IS thru 3S
* For lager caperidea oec cnhiple mater cootroia ia parallel
The need for a modulating device for use in conjunction with constant air flow air cooled condensers is gen erally recognized. Falling temperatures produce corre spondingly low operating pressure and eventually cause system problems, at the expansion valve. The Krack Winter Control, a completely automatic system; positively eliminates these conditions.
Krack winter control consists of three valves. The first, designated as Valve L in the accompanying diagram controls pressure in the condenser itself by filling or emptying same-in accordance with pressure variation.
*L* LIQUID FROM CONDENSER
7/8* I.D. Sw. 7/8* l.D. S*.
1-1/8* I.D. Sw.
CONNECTION DATA
*G* HOT GAS FROM COMPRESSOR DISCR.
7/8* l.D. Sw. 7/8* I.D. Sw. 1-1/8* I.D. Sw.
C LIQUID TO RECEIVQt
7/8*. I.D. Sw. 7/8* I.D. S*. 1-1/0* I.D. Sw.
The second or Valve G controls pressure in the receiver by using discharge line gas in accordance with pres
sure variation therein. The third, a check valve desig nated as C, prevents liquid escape from receiver to condenser under any condition. Settings for the valves indicated are approximately as follows:
. Valve L Valve G
"12" 105#
95#
"22" 180# 160#
i Conversion factors for various tempera. ture differences between entering air and condensing
temperature.
Conversion factors for suction ternperatures lower than 40 F. at various condensing temperatures.
I. Air-cooled condenser specification chart based on 90 F. ambient air and 110 F. con densing temperature.
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CONDENSING TEMPERATURE - - CORRECTION FACTOR
aosonsma tcbpkiatubb
4JS mi BULB
95 90 ' 95 100 10S
100
rn 116.0. r m. 9
1.34 2.1
ios 110 US
oiscenes pR&ssott
126. 2 136 146-1 137 1 21X6 23S.7 243.1 26X6
1 .00 3 .34 2.0
.60 t.oo
1.34 2.00
.61 .80
1.00 1.34 2.0
.57 .67 .80 1.00 1.34
125 _ 130
141.4 sa.3
50 57 67 80 1. 00
166. 2 M.6
,4S .50 .57 .47
.80
SUCTION TEMPERATURE -- CORRECTION FACTOR
awsasuto
AUCT10II TBIPEtATUAR
TBraxnu -40 -30 -20 -10 0 10 20 30 40
100" 110 120
130
1.25 1.22 1.31 1.26 1.37 132 1.43 1 37
1.17 1.13
1.21 i.n 1.23 140 1.30 1.2S
1.1 1.06 1.03 1.0 .98 1.13 1.09 1.06 1.03 1.0 1.1S l.U 1.(8 1.05 1.02 1.20 1,16 1 12 k.08 1.0S
MODO.
NOB. CAPACTTT
SVWTORAT0R 00 MBIBIT at0 some*
110 CDND. '
TONS BTO/HR.
C101D
1 12.000
CjqHD C3CMD
2 24.000 3 36,000
CS0HD
5 60.000
COIL A 6.75 81.000
C7SBD
COIL 8
7.5
90,000'
CD1L C 8.65
an. 94)
CX00SD
COIL B
10'
COIL C 11.5
COIL A 13.4
106.000 106.000 12.000 138.000 161.000
CISOBO C30080
CDIL B
CDIL C
COIL A
CDIL
cdil c
CDIL
C290BD COIL aiiL
COIL B
CDIL
15 16.59 18
B 32.8 33.4 25 35.8 3) 33.1
1*0.000 198.000 216.000 240.000 ZT4.000 261.000 300.000 323.000 360.000 S91.500
C400BD
40 .480,000
CS00BD
SO 600,000
COOOBD
60 730.000
AIR VQLUKB
cm
OTOR DATA
RILL HP U)AD RPN
(UP.
PAH DATA
operating * CHARGE
TIP B CTA. DRIVE
* Wl
*12
*22*
1395 1/8 L 5
21GO 1/4 2.5 900 1/3 3.0
659 - 2-1/4 5.0
11100 1- 1/2 4. 4
1900 1-1/2 4.4
10700 1-1/2 4^4
16300 1-1/2 4.4 16000 1-1/2 4.4
1S800 172S0
1-1/2 4.4 1-1/2 4.4
167 SO 1-1/2 4.4 160SO 2 5.8
S100 - 2 8.3
3B000 3 8.1
2790 3 6.3
268 SO 2250
3 6.3 3 8.3
21350 3 8.3 31500 3 6.3 30SO0 5 13.0 56000 > 1/2 19.6 56000 7-V2 19.6 56000 7- 1/2 19.6
Direct 1140 16 I1C 15 X 2
Direct 1140 20 11 4.9
Direct 1140 22 It 7.7
Direct u 2-23 11 1X7
4. 4 6.7 11. 2
Belt 17 25 42 4SS 15.5 14. 3
Belt 1725 42 435 IS. 6 14. 3
17 25 42 1725 17 25 48
Belt 435 15.5 Belt 435 21.6 Belt . 425 2L 4
14.3 19.7 B.7
17 25 48 17 25 48
Belt 435 21.4 B.7 Belt 450 38.4 35.4
17 25 48 17 25 48
Belt ' 450 38.4 Belt 49 SS.4
35.4 35. 4
17 25 >48 17 25 >48
Belt 425 42.3
Belt 435 42.3
39. a 29. 2
Belt 1725 >48 435 42.3 9. 2
Belt 1725 >48 4 56.5 52.3
Belt n 23 > 4 56.5 52-3
17 25 >48 17 25 >48
Belt 4 66.5 SX 3 Belt 49 79.0 73.0
1725 >46 17 25 >54 17 25 >54 1726 >54
Belt 49 79.0 73.0
gelt SW 105 98
Bett 610
140
130
Belt 630
. 210
195
APPGDX. SUPPING VBGBTS
1 230 380 SB0 800 830 B60 690 950 1010 ISO 190 IttO 1470 1530' 1590 . 1730 18 1940 2350 .259 3400 , 3600 3750
- `When using Krnck Winter Control, the condenser operetta? should be doubled end the receiver sized According!!.
1. Select from Table 1, Correction Fac tor applicable to condensing tempera ture and ambient temperature to be encountered on subject installation. 2. Obtain from Table 2. Correction Fac-' tor corresponding to suction tempera ture and condensing temperature at wtuch the equipment is designed to' operate. 3. Multiply Correction Factors obtained from Tables 1 and 2 by the Evaporator Load. 4. Select a KRACK Air Cooled Con denser from Table 3 having a nominal rating equal to or greater wan the fig ure arrind at in step 3.
EXAMPLE
To select a KRACK Air Cooled Condenser for: *
120 Condensing Temperature - - ' 90s Ambient Temperature
10s Suction Temperature 240.000 BTU/Hr. EVAPORATOR LOAD 1. Correction factor from Tabfe 1 for 120 condensing temperature and 90 ambient is. .67. 2. Correction factor from Table 2 for 10 suction and 120 condensing tem perature is 1.11. 3. Multiply evaporator loadby correc tion factors selected: 24D.ODO x .67 r 1.11 = 178,488 BTU/Hr.
.4 From Table 3 -- Model C150BD with
Coil B is selected.
Available With All Steel Hoi-Dipped Galvanized "B" Coil Elements, Far Use in Auxiliary Services.
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