23 - pccw hong kong test 0404
TRANSCRIPT
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AN
EVALUATION
OF
THE EFFECTS OF
PERMAFROST TREATMENT
FOR
ON A
CARRIER30GBWATERCHILLER
AT THE
PCCWEXCHANGE BUILDING
TAI PO MARKET,HONGKONG,SAR
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INTRODUCTION
The aim of this report is to examine the effects of a product known as PermaFrost
upon one of the refrigeration circuit of the air-cooled Carrier 30BG060012E water
chiller at the PCCW Building, Hong Kong.
PermaFrost has previously been claimed to enhance the performance of refrigeration
and air conditioning systems elsewhere. Literature from the Polar Oil Company
(which markets the product) states that PermaFrost a molecular technology that
relies on highly activated thermal conductive compounds - will improve heat transfer
on metal surfaces and increase lubricity of the refrigerant oil.
It further states: When PermaFrosts Thermo-Conductive compound is added to the
compressor, it blends with the oil and moves through the system. As each molecule
attaches itself to metal surfaces within the system, it displaces dirt, carbon deposits,
and stagnant oils, eventually forming a thin layer. As a result, the system can move
more heat for the same amount of compressor action. Energy demand and
consumption can be reduced.
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RESULTS OF TESTING
Detailed results of the operating conditions are provided in the following charts, all
found in Appendix A:
1. Pre-treatment Test (February 23 - 24, 2004)
Chart 1A: Cooling Capacity, Power Input & Coefficient of Performance
Chart 1B: Discharge, Condensing, & Evaporating Temperatures, Superheat and
Subcooling
Chart 1C: Evaporator & Condenser Pressures
2. Post-treatment Test (April 18 - 19, 2004)
Chart 2A: Cooling Capacity, Power Input & Coefficient of Performance
Chart 2B: Discharge, Condensing, & Evaporating Temperatures, Superheat and
Subcooling
Chart 2C: Evaporator & Condenser Pressures
Observations
A comparison of the mean operating conditions for each of the tests are summarised
in table below:
Test Results : Operating Mean Values
Pre-treatment Post-treatment % change
Cooling Capacity (kW) 88.66 102.41 15.5
Power Input (kW) 31.10 31.08 -0.06
Coefficient of Performance, COP 2.85 3.32 16.5
Discharge Temperature (C) 93.42 96.30 0.03
Evaporating Temperature (C) -1.04 -4.31 -314
Condensing Temperature (C) 46.39 46.40 0.02Liquid Subcooling (K) 18.96 12.85 -32.2
Suction Superheat (K) 5.80 10.02 72.8
Condensing Pressure (bar) 16.85 16.86 0.06
Evaporating Pressure (bar) 3.81 3.31 -13.1
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From this table, a number of observations can be made about the effects of
PermaFrost on the chiller:
Cooling capacity increased by 15.5 % in the post-treatment test. This indicates asignificant improvement in heat transfer in the evaporator.
The COP (a ratio of the cooling capacity and power input) increased by 16.5% inthe post-treatment test. This indicates a significant improvement in the overall
system performance.
The decrease in the evaporating temperature and pressure further indicatessignificant improvement in heat transfer in the evaporator.
The decrease in the liquid subcooling and increase suction superheat in the testsdo not appear to have impact on the system performance.
The changes in power input and compressor discharge temperatures wereinsignificant.
CONCLUSION
The tests carried out on the chiller indicated an improvement in the cooling capacity
of 15.5% and an overall increase in system performance of 16.5 % after treatment
with PermaFrost. The increase in cooling capacity and system performance will
result in the compressor using less energy to achieve the same cooling effect on
the chilled water as prior to treatment with Permafrost. The decrease in energy
usage by the compressor will correspond approximately to the increase in the system
performance. This is achieved by a reduction of the compressor run time to produce
the same cooling effect on the chiller.
The salient results are summarised in the bar graphs in Appendix B.
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Copyright: enACon Limited, Hong Kong
Polar Oil Company, Australia
Pre Treatment Test
February 23-24, 2004
Appendix A
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Copyright: enACon Limited, Hong Kong
Polar Oil Company, Australia
Chart 1A - Carrier Chiller at PCCW: Operating Cooling Capacity, Power Input & COP ( Pre- treatment
)
0.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
80.00
90.00
100.00
21:00
21:14
21:28
21:42
21:56
22:10
22:24
22:38
22:52
23:06
23:20
23:34
23:48
0:02
0:16
0:30
0:44
0:58
1:12
1:26
1:40
1:54
2:08
2:22
2:36
2:50
3:04
3:18
3:32
3:46
4:00
4:14
4:28
4:42
4:56
5:10
5:24
5:38
5:52
Feb 23 - 24, 2004
V
alue
Cooling Capacity [ Mean value: 88.66 kW ]
Power Input [ Mean value: 31.10 kW ]
COP [ Mean value: 2.85 ]
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Copyright: enACon Limited, Hong Kong
Polar Oil Company, Australia
Chart 1B - Carrier Chiller at PCCW: Operating Temperatures ( Pre- treatment )
-5
5
15
25
35
45
55
65
75
85
95
21:00
21:14
21:28
21:42
21:56
22:10
22:24
22:38
22:52
23:06
23:20
23:34
23:48
0:02
0:16
0:30
0:44
0:58
1:12
1:26
1:40
1:54
2:08
2:22
2:36
2:50
3:04
3:18
3:32
3:46
4:00
4:14
4:28
4:42
4:56
5:10
5:24
5:38
5:52
Feb 23 - 24, 2004
Temperature[C]
Discharge Temp [ Mean value: 93.42C ]
Condensing Temp [ Mean value: 46.39C ]
Evaporating Temp [ Mean value: - 1.04C ]
Superheat [ Mean value: 5.80K ]
Subcooling [ Mean value: 18.96C ]
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Copyright: enACon Limited, Hong Kong
Polar Oil Company, Australia
Chart 1C- Carrier Chiller at PCCW: Operating Pressures ( Pre- treatment )
0
2
4
6
8
10
12
14
16
18
21:00
21:14
21:28
21:42
21:56
22:10
22:24
22:38
22:52
23:06
23:20
23:34
23:48
0:02
0:16
0:30
0:44
0:58
1:12
1:26
1:40
1:54
2:08
2:22
2:36
2:50
3:04
3:18
3:32
3:46
4:00
4:14
4:28
4:42
4:56
5:10
5:24
5:38
5:52
Feb 23 - 24, 2004
Pressure[Bar]
Evaporating Pressure [ Mean value: 3.81 Bar ]
Condensing Pressure [ Mean value: 16.85 Bar ]
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Copyright: enACon Limited, Hong Kong
Polar Oil Company, Australia
Post Treatment Test
April 18-19, 2004
Appendix A
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Copyright: enACon Limited, Hong Kong
Polar Oil Company, Australia
Chart 2A - Carrier Chiller at PCCW: Operating Cooling Capacity, Power Input & COP ( Post-
treatment )
0.00
20.00
40.00
60.00
80.00
100.00
4:43:01
5:01:01
5:19:16
5:37:21
5:55:16
6:13:16
6:31:16
6:50:11
7:08:46
7:27:26
7:46:11
8:05:01
8:22:06
8:40:45
8:59:26
9:17:25
9:35:45
9:53:41
10:11:31
10:29:46
10:48:06
11:05:46
11:24:11
11:41:51
11:58:51
12:16:10
12:33:56
12:51:56
13:09:36
13:26:16
13:43:51
14:01:31
14:18:51
14:36:31
14:53:36
15:10:51
15:28:16
15:45:56
April 18 - 19, 2004
Value
Cooling Capacity [ Mean value: 102.41 kW ]
Power Input [ Mean value: 31.08 kW ]
COP [ Mean value: 2.85 ]
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Copyright: enACon Limited, Hong Kong
Polar Oil Company, Australia
Chart 2B - Carrier Chiller at PCCW: Operating Temperatures ( Post- treatment )
-5
15
35
55
75
95
4:43:01
5:01:01
5:19:16
5:37:21
5:55:16
6:13:16
6:31:16
6:50:11
7:08:46
7:27:26
7:46:11
8:05:01
8:22:06
8:40:45
8:59:26
9:17:25
9:35:45
9:53:41
10:11:31
10:29:46
10:48:06
11:05:46
11:24:11
11:41:51
11:58:51
12:16:10
12:33:56
12:51:56
13:09:36
13:26:16
13:43:51
14:01:31
14:18:51
14:36:31
14:53:36
15:10:51
15:28:16
15:45:56
April18 - 19, 2004
Temperature[C]
Discharge Temp [ Mean value: 96.30C ]
Condensing Temp [ Mean value: 46.40C ]
Subcooling [ Mean value: 12.85C ]
Superheat [ Mean value: 10.02 K ]
Evaporating Temp [ Mean value: - 4.31C ]
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Copyright: enACon Limited, Hong Kong
Polar Oil Company, Australia
Chart 2C - Carrier Chiller at PCCW: Operating Pressures ( Post - treatment )
0
2
4
6
8
10
12
14
16
18
20
4:43
:01
5:01
:01
5:19
:16
5:37
:21
5:55
:16
6:13
:16
6:31
:16
6:50
:11
7:08
:46
7:27
:26
7:46
:11
8:05
:01
8:22
:06
8:40
:45
8:59
:26
9:17
:25
9:35
:45
9:53
:41
10:11:31
10:29:
46
10:48:06
11:05:
46
11:24:11
11:41:51
11:58:51
12:16:
10
12:33:56
12:51:56
13:09:36
13:26:
16
13:43:51
14:01:31
14:18:51
14:36:31
14:53:36
15:10:51
15:28:
16
15:45:56
April 18-19, 2004
Pressure[Bar]
Condensing Pressure [ Mean value: 16.86 Bar ]
Evaporating Pressure [ Mean value: 3.31 Bar
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Copyright: enACon Limited, Hong Kong
Polar Oil Company, Australia
Performance
Comparison
Pre: February 23-24, 2004
&
Post: April 18-19, 2004Appendix B
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Copyright: enACon Limited, Hong Kong
Polar Oil Company, Australia
Comparison of Cooling Capacity resulting from treatment with PermaFrost
80
85
90
95
100
105
Pre-treatment Post-treatment
CoolingCapacity(kW)
Cooling Capacity (kW)
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Copyright: enACon Limited, Hong Kong
Polar Oil Company, Australia
Comparison of COP resulting from treatment with PermaFrost
2.6
2.7
2.8
2.9
3
3.1
3.2
3.3
3.4
Pre-treatment Post-treatment
CoefficientofPerformance,
COP
Coefficient of Performance, COP
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Copyright: enACon Limited, Hong Kong
Polar Oil Company, Australia
Comparison of Performance of Chiller resulting from treatment with PermaFrost
0
20
40
60
80
100
120
Cooling Capacity (kW) Power Input (kW) Coefficient of Performance, COP
Valu
e
Pre-treatment
Post-treatment