23 - pccw hong kong test 0404

Upload: abdou-hussein

Post on 05-Apr-2018

221 views

Category:

Documents


0 download

TRANSCRIPT

  • 7/31/2019 23 - PCCW Hong Kong Test 0404

    1/17

    AN

    EVALUATION

    OF

    THE EFFECTS OF

    PERMAFROST TREATMENT

    FOR

    ON A

    CARRIER30GBWATERCHILLER

    AT THE

    PCCWEXCHANGE BUILDING

    TAI PO MARKET,HONGKONG,SAR

  • 7/31/2019 23 - PCCW Hong Kong Test 0404

    2/17

    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.

  • 7/31/2019 23 - PCCW Hong Kong Test 0404

    3/17

  • 7/31/2019 23 - PCCW Hong Kong Test 0404

    4/17

    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

  • 7/31/2019 23 - PCCW Hong Kong Test 0404

    5/17

    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.

  • 7/31/2019 23 - PCCW Hong Kong Test 0404

    6/17

    Copyright: enACon Limited, Hong Kong

    Polar Oil Company, Australia

    Pre Treatment Test

    February 23-24, 2004

    Appendix A

  • 7/31/2019 23 - PCCW Hong Kong Test 0404

    7/17

    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 ]

  • 7/31/2019 23 - PCCW Hong Kong Test 0404

    8/17

    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 ]

  • 7/31/2019 23 - PCCW Hong Kong Test 0404

    9/17

    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 ]

  • 7/31/2019 23 - PCCW Hong Kong Test 0404

    10/17

    Copyright: enACon Limited, Hong Kong

    Polar Oil Company, Australia

    Post Treatment Test

    April 18-19, 2004

    Appendix A

  • 7/31/2019 23 - PCCW Hong Kong Test 0404

    11/17

    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 ]

  • 7/31/2019 23 - PCCW Hong Kong Test 0404

    12/17

    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 ]

  • 7/31/2019 23 - PCCW Hong Kong Test 0404

    13/17

    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

  • 7/31/2019 23 - PCCW Hong Kong Test 0404

    14/17

    Copyright: enACon Limited, Hong Kong

    Polar Oil Company, Australia

    Performance

    Comparison

    Pre: February 23-24, 2004

    &

    Post: April 18-19, 2004Appendix B

  • 7/31/2019 23 - PCCW Hong Kong Test 0404

    15/17

    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)

  • 7/31/2019 23 - PCCW Hong Kong Test 0404

    16/17

    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

  • 7/31/2019 23 - PCCW Hong Kong Test 0404

    17/17

    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