Rancang Bangun Pompa Kalor Pada Alat Pengering Hibrida Pompa Kalor dan Surya
Lampiran I
Refrigerant 22 (Chlorodifluoromethane) Properties of Saturated Liquid and Saturated Vapor
Temp,*
°C
−150.00
−140.00
−130.00
−120.00
−110.00
−100.00
−90.00
−80.00
−70.00
−60.00
−50.00
−48.00
−46.00
−44.00
−42.00
−40.80b
−40.00
−38.00
−36.00
−34.00
−32.00
−30.00
−28.00
−26.00
−24.00
−22.00
−20.00
−18.00
−16.00
−14.00
−12.00
−10.00
−8.00
−6.00
−4.00
−2.00
0
2
4
6
8
10
12
14
16
18
20
22
24
26
28
30
32
34
36
38
40
42
44
46
48
50
55
60
65
70
75
80
85
90
95
96.14c
Absolute
Pressure,
MPa
Density,
kg/m3
Liquid
Volume,
m3/kg
Vapor
—
—
0.00006
0.00023
0.00074
0.00200
0.00480
0.01035
0.02044
0.03747
0.06449
0.07140
0.07890
0.08700
0.09575
0.10132
0.10518
0.11533
0.12623
0.13793
0.15045
0.16384
0.17815
0.19340
0.20965
0.22693
0.24529
0.26477
0.28542
0.30728
0.33040
0.35482
0.38059
0.40775
0.43636
0.46646
0.49811
0.53134
0.56622
0.60279
0.64109
0.68119
0.72314
0.76698
0.81277
0.86056
0.91041
0.96236
1.01650
1.07280
1.13140
1.19240
1.25570
1.32150
1.38980
1.46060
1.53410
1.61030
1.68920
1.77090
1.85550
1.94310
2.17530
2.42740
2.70080
2.99670
3.31680
3.66270
4.03680
4.44160
4.88200
4.99000
1701.5
1675.3
1649.7
1624.0
1598.0
1571.7
1545.1
1518.3
1491.1
1463.6
1435.5
1429.8
1424.1
1418.4
1412.6
1409.1
1406.8
1401.0
1395.1
1389.2
1383.3
1377.3
1371.3
1365.2
1359.1
1352.9
1346.8
1340.5
1334.2
1327.9
1321.5
1315.0
1308.5
1301.9
1295.3
1288.6
1281.8
1275.0
1268.1
1261.1
1254.0
1246.9
1239.7
1232.4
1225.0
1217.6
1210.0
1202.4
1194.6
1186.8
1178.8
1170.7
1162.5
1154.2
1145.7
1137.1
1128.4
1119.5
1110.4
1101.2
1091.8
1082.1
1057.1
1030.5
1001.8
970.4
935.3
894.8
845.1
777.5
665.4
523.8
—
—
229.29
63.648
21.3110
8.2980
3.6548
1.7816
0.94476
0.53734
0.32405
0.29469
0.26849
0.24507
0.22410
0.21256
0.20526
0.18832
0.17306
0.15927
0.14680
0.13551
0.12525
0.11593
0.10744
0.09970
0.09262
0.08615
0.08023
0.07479
0.06979
0.06520
0.06096
0.05706
0.05345
0.05012
0.04703
0.04417
0.04152
0.03906
0.03676
0.03463
0.03265
0.03079
0.02906
0.02744
0.02593
0.02451
0.02319
0.02194
0.02077
0.01968
0.01864
0.01767
0.01675
0.01589
0.01507
0.01430
0.01357
0.01288
0.01223
0.01161
0.01020
0.00895
0.00784
0.00684
0.00594
0.00511
0.00433
0.00355
0.00264
0.00191
Enthalpy,
kJ/kg
Liquid
26.01
43.84
57.00
68.51
79.47
90.24
100.95
111.66
122.36
133.11
143.91
146.08
148.25
150.43
152.61
153.93
154.80
156.99
159.19
161.40
163.61
165.82
168.04
170.27
172.51
174.75
177.00
179.26
181.53
183.81
186.09
188.38
190.69
193.00
195.32
197.66
200.00
202.35
204.72
207.10
209.49
211.89
214.31
216.74
219.18
221.63
224.10
226.59
229.09
231.60
234.14
236.69
239.25
241.84
244.44
247.06
249.71
252.37
255.06
257.77
260.51
263.27
270.31
277.56
285.06
292.90
301.18
310.10
320.05
331.98
348.86
366.59
Vapor
335.85
340.24
344.75
349.38
354.11
358.93
363.82
368.75
373.68
378.58
383.39
384.35
385.29
386.23
387.17
387.72
388.09
389.01
389.93
390.84
391.74
392.63
393.52
394.39
395.26
396.12
396.97
397.81
398.64
399.46
400.27
401.07
401.85
402.63
403.39
404.14
404.87
405.59
406.30
406.99
407.67
408.33
408.97
409.60
410.21
410.80
411.38
411.93
412.46
412.98
413.46
413.93
414.37
414.79
415.18
415.54
415.87
416.17
416.44
416.68
416.87
417.03
417.24
417.14
416.65
415.69
414.09
411.60
407.72
401.33
387.46
366.59
Entropy,
kJ/(kg·K)
Liquid
0.0566
0.1961
0.2916
0.3694
0.4386
0.5027
0.5629
0.6197
0.6738
0.7253
0.7748
0.7844
0.7940
0.8035
0.8130
0.8186
0.8224
0.8317
0.8410
0.8502
0.8594
0.8685
0.8776
0.8866
0.8955
0.9044
0.9133
0.9222
0.9309
0.9397
0.9484
0.9571
0.9657
0.9743
0.9829
0.9915
1.0000
1.0085
1.0170
1.0254
1.0338
1.0422
1.0506
1.0590
1.0673
1.0756
1.0840
1.0923
1.1006
1.1088
1.1171
1.1254
1.1336
1.1419
1.1501
1.1584
1.1667
1.1749
1.1832
1.1915
1.1998
1.2081
1.2291
1.2503
1.2718
1.2940
1.3169
1.3413
1.3680
1.3998
1.4442
1.4918
Vapor
2.5752
2.4222
2.3017
2.2033
2.1220
2.0545
1.9982
1.9508
1.9109
1.8770
1.8480
1.8427
1.8376
1.8326
1.8277
1.8249
1.8230
1.8184
1.8140
1.8096
1.8054
1.8013
1.7973
1.7934
1.7896
1.7859
1.7822
1.7787
1.7752
1.7719
1.7686
1.7653
1.7621
1.7590
1.7560
1.7530
1.7500
1.7471
1.7443
1.7415
1.7387
1.7360
1.7333
1.7306
1.7280
1.7254
1.7228
1.7202
1.7177
1.7151
1.7126
1.7101
1.7075
1.7050
1.7024
1.6999
1.6973
1.6947
1.6921
1.6894
1.6867
1.6840
1.6768
1.6692
1.6610
1.6518
1.6413
1.6287
1.6128
1.5907
1.5491
1.4918
Specific Heat cp,
kJ/(kg·K)
Liquid
—
—
—
—
—
—
1.070
1.070
1.072
1.076
1.083
1.085
1.087
1.089
1.091
1.092
1.093
1.096
1.098
1.101
1.104
1.107
1.110
1.114
1.117
1.121
1.125
1.129
1.133
1.137
1.141
1.146
1.151
1.156
1.161
1.166
1.171
1.177
1.183
1.189
1.195
1.202
1.208
1.215
1.223
1.230
1.238
1.246
1.254
1.263
1.272
1.282
1.292
1.302
1.313
1.325
1.338
1.351
1.365
1.380
1.396
1.414
1.464
1.528
1.611
1.726
1.896
2.176
2.725
4.186
—
∞
Vapor
0.434
0.445
0.458
0.470
0.483
0.497
0.511
0.527
0.544
0.563
0.584
0.589
0.594
0.598
0.603
0.606
0.608
0.614
0.619
0.624
0.630
0.636
0.642
0.648
0.654
0.660
0.667
0.674
0.681
0.688
0.695
0.703
0.710
0.718
0.727
0.735
0.744
0.753
0.762
0.772
0.782
0.792
0.802
0.813
0.825
0.837
0.849
0.862
0.875
0.889
0.904
0.919
0.935
0.952
0.970
0.989
1.009
1.030
1.052
1.076
1.102
1.129
1.209
1.307
1.435
1.609
1.862
2.268
3.039
5.041
—
∞
cp/cv
Vapor
1.285
1.275
1.266
1.258
1.250
1.243
1.237
1.233
1.231
1.231
1.233
1.233
1.234
1.235
1.236
1.237
1.237
1.239
1.240
1.242
1.243
1.245
1.247
1.249
1.252
1.254
1.257
1.260
1.263
1.266
1.269
1.273
1.277
1.281
1.285
1.289
1.294
1.299
1.305
1.310
1.316
1.323
1.330
1.337
1.345
1.353
1.361
1.370
1.380
1.391
1.402
1.413
1.426
1.440
1.454
1.470
1.486
1.504
1.524
1.545
1.568
1.593
1.667
1.762
1.888
2.064
2.324
2.748
3.555
5.643
—
∞
Velocity of
Sound
m/s
Liquid
Vapor
—
123
—
128
—
132
—
136
—
140
—
144
1094
147
1037
150
986
153
937
156
890
158
881
159
871
159
862
160
853
160
847
160
844
160
834
161
825
161
816
161
807
161
797
162
788
162
779
162
770
162
760
163
751
163
742
163
733
163
723
163
714
163
705
163
696
163
686
163
677
163
668
163
658
163
649
163
640
163
630
163
621
163
611
163
602
162
592
162
583
162
573
162
564
161
554
161
544
160
535
160
525
160
515
159
506
159
496
158
486
158
476
157
466
156
456
156
446
155
436
154
426
153
415
153
389
150
362
148
335
145
306
142
276
138
244
134
209
129
170
124
—
—
0
0
Viscosity, µ
Pa·s
Liquid
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
260.1
254.7
249.4
244.2
239.1
234.1
229.1
224.2
219.4
214.7
210.1
205.6
201.2
196.9
192.6
188.5
184.4
180.5
176.6
172.8
169.1
165.4
161.9
158.4
155.0
151.7
148.5
145.4
142.3
139.3
136.3
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
Vapor
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
11.08
11.16
11.24
11.32
11.40
11.48
11.56
11.64
11.72
11.80
11.88
11.96
12.04
12.12
12.20
12.28
12.36
12.44
12.52
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
Thermal Cond,
mW/(m·K)
Liquid
—
—
—
—
—
—
—
—
128.0
123.1
118.4
117.5
116.5
115.6
114.7
114.1
113.8
112.9
112.0
111.1
110.1
109.2
108.4
107.5
106.6
105.7
104.8
103.9
103.1
102.2
101.3
100.4
99.6
98.7
97.9
97.0
96.2
95.3
94.5
93.6
92.8
92.0
91.1
90.3
89.5
88.7
87.8
87.0
86.2
85.4
84.6
83.8
83.0
82.2
81.4
80.6
79.8
79.0
78.2
77.4
76.6
—
—
—
—
—
—
—
—
—
—
∞
Vapor
—
—
—
—
—
—
—
—
—
5.61
6.31
6.44
6.58
6.71
6.85
6.93
6.98
7.11
7.24
7.37
7.50
7.63
7.76
7.89
8.02
8.14
8.27
8.40
8.52
8.64
8.77
8.89
9.02
9.14
9.26
9.38
9.50
9.63
9.75
9.87
9.99
10.11
10.23
10.35
10.47
10.59
10.71
10.82
10.94
11.06
11.18
11.30
11.42
11.54
11.66
11.78
11.90
12.02
12.14
12.26
12.38
—
—
—
—
—
—
—
—
—
—
∞
Surface
Tension
mN/m
Temp,*
°C
37.59
35.70
33.84
32.00
30.17
28.37
26.59
24.83
23.10
21.39
19.70
19.37
19.04
18.70
18.37
18.18
18.05
17.72
17.39
17.07
16.74
16.42
16.10
15.77
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
0.00
−150.00
−140.00
−130.00
−120.00
−110.00
−100.00
−90.00
−80.00
−70.00
−60.00
−50.00
−48.00
−46.00
−44.00
−42.00
−40.80
−40.00
−38.00
−36.00
−34.00
−32.00
−30.00
−28.00
−26.00
−24.00
−22.00
−20.00
−18.00
−16.00
−14.00
−12.00
−10.00
−8.00
−6.00
−4.00
−2.00
0.00
2.00
4.00
6.00
8.00
10.00
12.00
14.00
16.00
18.00
20.00
22.00
24.00
26.00
28.00
30.00
32.00
34.00
36.00
38.00
40.00
42.00
44.00
46.00
48.00
50.00
55.00
60.00
65.00
70.00
75.00
80.00
85.00
90.00
95.00
96.14
Universitas Sumatera Utara
*temperatures are on the ITS−90 scale b = normal boiling point c = critical poin
Sumber: 1997 ASHRAE Fundamentals Handbook (SI)
Universitas Sumatera Utara
Lampiran II
Jumlah biaya rancang bangun pompa kalor
No
Jumlah
Bahan
Ukuran
@
Harga (Rp)
10.000
110.000,00
1
1 gulung
Kertas aluminium foil
1 x 11 m
2
6 lembar
Rock woll
3 x 0,6 x 1 m
3
1 gulung
Plat seng (tebal 0.3m)
12 x 1,1 m
4
1 unit
Air conditioner LG 1 1/2 PK
4.000.000
5
1 unit
Control Panel(Jasa dan alat)
5.000.000
6
1 kotak
Paku rivet
7
3 kaleng
thiner
18.000
54.000
8
3 kaleng
Cat minyak silver
38.000
114.000
9
8 batang
besi siku
65.000
440.000
10
1 kg
busur las
30.000
11
4 buah
Corong saluran udara
150.000
350.000,00
35.000
Ø4 mm
420.000
60.000
40 x 40mm
Jumlah
10.728.000,00
Universitas Sumatera Utara
Refrigerant 22 (Chlorodifluoromethane) Properties of Saturated Liquid and Saturated Vapor
Temp,*
°C
−150.00
−140.00
−130.00
−120.00
−110.00
−100.00
−90.00
−80.00
−70.00
−60.00
−50.00
−48.00
−46.00
−44.00
−42.00
−40.80b
−40.00
−38.00
−36.00
−34.00
−32.00
−30.00
−28.00
−26.00
−24.00
−22.00
−20.00
−18.00
−16.00
−14.00
−12.00
−10.00
−8.00
−6.00
−4.00
−2.00
0
2
4
6
8
10
12
14
16
18
20
22
24
26
28
30
32
34
36
38
40
42
44
46
48
50
55
60
65
70
75
80
85
90
95
96.14c
Absolute
Pressure,
MPa
Density,
kg/m3
Liquid
Volume,
m3/kg
Vapor
—
—
0.00006
0.00023
0.00074
0.00200
0.00480
0.01035
0.02044
0.03747
0.06449
0.07140
0.07890
0.08700
0.09575
0.10132
0.10518
0.11533
0.12623
0.13793
0.15045
0.16384
0.17815
0.19340
0.20965
0.22693
0.24529
0.26477
0.28542
0.30728
0.33040
0.35482
0.38059
0.40775
0.43636
0.46646
0.49811
0.53134
0.56622
0.60279
0.64109
0.68119
0.72314
0.76698
0.81277
0.86056
0.91041
0.96236
1.01650
1.07280
1.13140
1.19240
1.25570
1.32150
1.38980
1.46060
1.53410
1.61030
1.68920
1.77090
1.85550
1.94310
2.17530
2.42740
2.70080
2.99670
3.31680
3.66270
4.03680
4.44160
4.88200
4.99000
1701.5
1675.3
1649.7
1624.0
1598.0
1571.7
1545.1
1518.3
1491.1
1463.6
1435.5
1429.8
1424.1
1418.4
1412.6
1409.1
1406.8
1401.0
1395.1
1389.2
1383.3
1377.3
1371.3
1365.2
1359.1
1352.9
1346.8
1340.5
1334.2
1327.9
1321.5
1315.0
1308.5
1301.9
1295.3
1288.6
1281.8
1275.0
1268.1
1261.1
1254.0
1246.9
1239.7
1232.4
1225.0
1217.6
1210.0
1202.4
1194.6
1186.8
1178.8
1170.7
1162.5
1154.2
1145.7
1137.1
1128.4
1119.5
1110.4
1101.2
1091.8
1082.1
1057.1
1030.5
1001.8
970.4
935.3
894.8
845.1
777.5
665.4
523.8
—
—
229.29
63.648
21.3110
8.2980
3.6548
1.7816
0.94476
0.53734
0.32405
0.29469
0.26849
0.24507
0.22410
0.21256
0.20526
0.18832
0.17306
0.15927
0.14680
0.13551
0.12525
0.11593
0.10744
0.09970
0.09262
0.08615
0.08023
0.07479
0.06979
0.06520
0.06096
0.05706
0.05345
0.05012
0.04703
0.04417
0.04152
0.03906
0.03676
0.03463
0.03265
0.03079
0.02906
0.02744
0.02593
0.02451
0.02319
0.02194
0.02077
0.01968
0.01864
0.01767
0.01675
0.01589
0.01507
0.01430
0.01357
0.01288
0.01223
0.01161
0.01020
0.00895
0.00784
0.00684
0.00594
0.00511
0.00433
0.00355
0.00264
0.00191
Enthalpy,
kJ/kg
Liquid
26.01
43.84
57.00
68.51
79.47
90.24
100.95
111.66
122.36
133.11
143.91
146.08
148.25
150.43
152.61
153.93
154.80
156.99
159.19
161.40
163.61
165.82
168.04
170.27
172.51
174.75
177.00
179.26
181.53
183.81
186.09
188.38
190.69
193.00
195.32
197.66
200.00
202.35
204.72
207.10
209.49
211.89
214.31
216.74
219.18
221.63
224.10
226.59
229.09
231.60
234.14
236.69
239.25
241.84
244.44
247.06
249.71
252.37
255.06
257.77
260.51
263.27
270.31
277.56
285.06
292.90
301.18
310.10
320.05
331.98
348.86
366.59
Vapor
335.85
340.24
344.75
349.38
354.11
358.93
363.82
368.75
373.68
378.58
383.39
384.35
385.29
386.23
387.17
387.72
388.09
389.01
389.93
390.84
391.74
392.63
393.52
394.39
395.26
396.12
396.97
397.81
398.64
399.46
400.27
401.07
401.85
402.63
403.39
404.14
404.87
405.59
406.30
406.99
407.67
408.33
408.97
409.60
410.21
410.80
411.38
411.93
412.46
412.98
413.46
413.93
414.37
414.79
415.18
415.54
415.87
416.17
416.44
416.68
416.87
417.03
417.24
417.14
416.65
415.69
414.09
411.60
407.72
401.33
387.46
366.59
Entropy,
kJ/(kg·K)
Liquid
0.0566
0.1961
0.2916
0.3694
0.4386
0.5027
0.5629
0.6197
0.6738
0.7253
0.7748
0.7844
0.7940
0.8035
0.8130
0.8186
0.8224
0.8317
0.8410
0.8502
0.8594
0.8685
0.8776
0.8866
0.8955
0.9044
0.9133
0.9222
0.9309
0.9397
0.9484
0.9571
0.9657
0.9743
0.9829
0.9915
1.0000
1.0085
1.0170
1.0254
1.0338
1.0422
1.0506
1.0590
1.0673
1.0756
1.0840
1.0923
1.1006
1.1088
1.1171
1.1254
1.1336
1.1419
1.1501
1.1584
1.1667
1.1749
1.1832
1.1915
1.1998
1.2081
1.2291
1.2503
1.2718
1.2940
1.3169
1.3413
1.3680
1.3998
1.4442
1.4918
Vapor
2.5752
2.4222
2.3017
2.2033
2.1220
2.0545
1.9982
1.9508
1.9109
1.8770
1.8480
1.8427
1.8376
1.8326
1.8277
1.8249
1.8230
1.8184
1.8140
1.8096
1.8054
1.8013
1.7973
1.7934
1.7896
1.7859
1.7822
1.7787
1.7752
1.7719
1.7686
1.7653
1.7621
1.7590
1.7560
1.7530
1.7500
1.7471
1.7443
1.7415
1.7387
1.7360
1.7333
1.7306
1.7280
1.7254
1.7228
1.7202
1.7177
1.7151
1.7126
1.7101
1.7075
1.7050
1.7024
1.6999
1.6973
1.6947
1.6921
1.6894
1.6867
1.6840
1.6768
1.6692
1.6610
1.6518
1.6413
1.6287
1.6128
1.5907
1.5491
1.4918
Specific Heat cp,
kJ/(kg·K)
Liquid
—
—
—
—
—
—
1.070
1.070
1.072
1.076
1.083
1.085
1.087
1.089
1.091
1.092
1.093
1.096
1.098
1.101
1.104
1.107
1.110
1.114
1.117
1.121
1.125
1.129
1.133
1.137
1.141
1.146
1.151
1.156
1.161
1.166
1.171
1.177
1.183
1.189
1.195
1.202
1.208
1.215
1.223
1.230
1.238
1.246
1.254
1.263
1.272
1.282
1.292
1.302
1.313
1.325
1.338
1.351
1.365
1.380
1.396
1.414
1.464
1.528
1.611
1.726
1.896
2.176
2.725
4.186
—
∞
Vapor
0.434
0.445
0.458
0.470
0.483
0.497
0.511
0.527
0.544
0.563
0.584
0.589
0.594
0.598
0.603
0.606
0.608
0.614
0.619
0.624
0.630
0.636
0.642
0.648
0.654
0.660
0.667
0.674
0.681
0.688
0.695
0.703
0.710
0.718
0.727
0.735
0.744
0.753
0.762
0.772
0.782
0.792
0.802
0.813
0.825
0.837
0.849
0.862
0.875
0.889
0.904
0.919
0.935
0.952
0.970
0.989
1.009
1.030
1.052
1.076
1.102
1.129
1.209
1.307
1.435
1.609
1.862
2.268
3.039
5.041
—
∞
cp/cv
Vapor
1.285
1.275
1.266
1.258
1.250
1.243
1.237
1.233
1.231
1.231
1.233
1.233
1.234
1.235
1.236
1.237
1.237
1.239
1.240
1.242
1.243
1.245
1.247
1.249
1.252
1.254
1.257
1.260
1.263
1.266
1.269
1.273
1.277
1.281
1.285
1.289
1.294
1.299
1.305
1.310
1.316
1.323
1.330
1.337
1.345
1.353
1.361
1.370
1.380
1.391
1.402
1.413
1.426
1.440
1.454
1.470
1.486
1.504
1.524
1.545
1.568
1.593
1.667
1.762
1.888
2.064
2.324
2.748
3.555
5.643
—
∞
Velocity of
Sound
m/s
Liquid
Vapor
—
123
—
128
—
132
—
136
—
140
—
144
1094
147
1037
150
986
153
937
156
890
158
881
159
871
159
862
160
853
160
847
160
844
160
834
161
825
161
816
161
807
161
797
162
788
162
779
162
770
162
760
163
751
163
742
163
733
163
723
163
714
163
705
163
696
163
686
163
677
163
668
163
658
163
649
163
640
163
630
163
621
163
611
163
602
162
592
162
583
162
573
162
564
161
554
161
544
160
535
160
525
160
515
159
506
159
496
158
486
158
476
157
466
156
456
156
446
155
436
154
426
153
415
153
389
150
362
148
335
145
306
142
276
138
244
134
209
129
170
124
—
—
0
0
Viscosity, µ
Pa·s
Liquid
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
260.1
254.7
249.4
244.2
239.1
234.1
229.1
224.2
219.4
214.7
210.1
205.6
201.2
196.9
192.6
188.5
184.4
180.5
176.6
172.8
169.1
165.4
161.9
158.4
155.0
151.7
148.5
145.4
142.3
139.3
136.3
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
Vapor
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
11.08
11.16
11.24
11.32
11.40
11.48
11.56
11.64
11.72
11.80
11.88
11.96
12.04
12.12
12.20
12.28
12.36
12.44
12.52
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
Thermal Cond,
mW/(m·K)
Liquid
—
—
—
—
—
—
—
—
128.0
123.1
118.4
117.5
116.5
115.6
114.7
114.1
113.8
112.9
112.0
111.1
110.1
109.2
108.4
107.5
106.6
105.7
104.8
103.9
103.1
102.2
101.3
100.4
99.6
98.7
97.9
97.0
96.2
95.3
94.5
93.6
92.8
92.0
91.1
90.3
89.5
88.7
87.8
87.0
86.2
85.4
84.6
83.8
83.0
82.2
81.4
80.6
79.8
79.0
78.2
77.4
76.6
—
—
—
—
—
—
—
—
—
—
∞
Vapor
—
—
—
—
—
—
—
—
—
5.61
6.31
6.44
6.58
6.71
6.85
6.93
6.98
7.11
7.24
7.37
7.50
7.63
7.76
7.89
8.02
8.14
8.27
8.40
8.52
8.64
8.77
8.89
9.02
9.14
9.26
9.38
9.50
9.63
9.75
9.87
9.99
10.11
10.23
10.35
10.47
10.59
10.71
10.82
10.94
11.06
11.18
11.30
11.42
11.54
11.66
11.78
11.90
12.02
12.14
12.26
12.38
—
—
—
—
—
—
—
—
—
—
∞
Surface
Tension
mN/m
Temp,*
°C
37.59
35.70
33.84
32.00
30.17
28.37
26.59
24.83
23.10
21.39
19.70
19.37
19.04
18.70
18.37
18.18
18.05
17.72
17.39
17.07
16.74
16.42
16.10
15.77
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
0.00
−150.00
−140.00
−130.00
−120.00
−110.00
−100.00
−90.00
−80.00
−70.00
−60.00
−50.00
−48.00
−46.00
−44.00
−42.00
−40.80
−40.00
−38.00
−36.00
−34.00
−32.00
−30.00
−28.00
−26.00
−24.00
−22.00
−20.00
−18.00
−16.00
−14.00
−12.00
−10.00
−8.00
−6.00
−4.00
−2.00
0.00
2.00
4.00
6.00
8.00
10.00
12.00
14.00
16.00
18.00
20.00
22.00
24.00
26.00
28.00
30.00
32.00
34.00
36.00
38.00
40.00
42.00
44.00
46.00
48.00
50.00
55.00
60.00
65.00
70.00
75.00
80.00
85.00
90.00
95.00
96.14
Universitas Sumatera Utara
*temperatures are on the ITS−90 scale b = normal boiling point c = critical poin
Sumber: 1997 ASHRAE Fundamentals Handbook (SI)
Universitas Sumatera Utara
Lampiran II
Jumlah biaya rancang bangun pompa kalor
No
Jumlah
Bahan
Ukuran
@
Harga (Rp)
10.000
110.000,00
1
1 gulung
Kertas aluminium foil
1 x 11 m
2
6 lembar
Rock woll
3 x 0,6 x 1 m
3
1 gulung
Plat seng (tebal 0.3m)
12 x 1,1 m
4
1 unit
Air conditioner LG 1 1/2 PK
4.000.000
5
1 unit
Control Panel(Jasa dan alat)
5.000.000
6
1 kotak
Paku rivet
7
3 kaleng
thiner
18.000
54.000
8
3 kaleng
Cat minyak silver
38.000
114.000
9
8 batang
besi siku
65.000
440.000
10
1 kg
busur las
30.000
11
4 buah
Corong saluran udara
150.000
350.000,00
35.000
Ø4 mm
420.000
60.000
40 x 40mm
Jumlah
10.728.000,00
Universitas Sumatera Utara