Tabel Konveksi

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Transcript of Tabel Konveksi

Page 1: Tabel Konveksi

Konveksi paksa

Kondisi

No.Flow Rate

X To qw qv G' Tw Tb H ho Tbo Nuo Re

A

1

90

0.005 36.80 525381.8210507636.3

6

1672.435495

36.71 28.32 62681.69

43.20 43.95 0.015429

37928622

2 0.01 38.40 262690.91 5253818.18 38.35 28.32 26194.04

3 0.02 39.80 131345.45 2626909.09 39.78 28.32 11469.11

4 0.03 40.60 87563.64 1751272.73 40.58 28.32 7142.26

5 0.05 41.00 52538.18 1050763.64 40.99 28.32 4147.91

6 0.1 43.90 26269.09 525381.82 43.90 28.32 1687.07

7 0.2 47.30 13134.55 262690.91 47.30 28.32 692.27

8 0.4 52.60 6567.27 131345.45 52.60 28.32 270.54

9 0.6 57.90 4378.18 87563.64 57.90 28.32 148.04

10 0.8 64.60 3283.64 65672.73 64.60 28.32 90.52

B

1

70

0.005 39.60 525381.8210507636.3

6

1300.783163

39.51 28.32 46985.68

48.60 49.5 0.017357

47553948.36

2 0.01 41.70 262690.91 5253818.18 41.65 28.32 19708.74

3 0.02 43.80 131345.45 2626909.09 43.78 28.32 8500.16

4 0.03 45.00 87563.64 1751272.73 44.98 28.32 5255.94

5 0.05 45.90 52538.18 1050763.64 45.89 28.32 2990.87

6 0.1 49.50 26269.09 525381.82 49.50 28.32 1240.81

7 0.2 54.00 13134.55 262690.91 54.00 28.32 511.60

8 0.4 61.30 6567.27 131345.45 61.30 28.32 199.16

9 0.6 68.60 4378.18 87563.64 68.60 28.32 108.71

10 0.8 77.50 3283.64 65672.73 77.50 28.32 66.77

Data konstan dari praktikum

Flow P mmHg

p mm H2o Cp Pa A V DW dw Ta K

90 750.0010196.31

3 1.0110197325

5 24 20.00

6 0.005 28.3 14

Page 2: Tabel Konveksi

C

1

50

0.005 41.10 525381.8210507636.3

6

929.1308306

41.01 28.32 41428.20

51.68 52.8 0.018455

33797197.63

2 0.01 43.60 262690.91 5253818.18 43.55 28.32 17249.78

3 0.02 46.10 131345.45 2626909.09 46.08 28.32 7398.87

4 0.03 47.60 87563.64 1751272.73 47.58 28.32 4546.42

5 0.05 48.80 52538.18 1050763.64 48.79 28.32 2567.07

6 0.1 52.30 26269.09 525381.82 52.30 28.32 1095.88

7 0.2 58.00 13134.55 262690.91 58.00 28.32 442.64

8 0.4 66.40 6567.27 131345.45 66.40 28.32 172.49

9 0.6 74.80 4378.18 87563.64 74.80 28.32 94.21

10 0.8 85.00 3283.64 65672.73 85.00 28.32 57.94

Page 3: Tabel Konveksi
Page 4: Tabel Konveksi

0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.90.00

10.00

20.00

30.00

40.00

50.00

60.00

70.00

Grafik Kondisi A Hubungan X-Tb

Panjang pipa yang dipanaskan (X)

Tem

pera

tur d

alam

Pip

a (T

w)

0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.90.00

10.00

20.00

30.00

40.00

50.00

60.00

70.00

80.00

90.00

Grafik Kondisi B Hubungan X-Tw

Panjang pipa yang dipanaskan (X)

Tem

pera

tur d

alam

pip

a (T

w)

0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.90.00

10.00

20.00

30.00

40.00

50.00

60.00

70.00

80.00

90.00

Grafik Kondisi C Hubungan X-Tw

Temperature dalam Pipa (Tw)

Jara

k Ti

tik y

ang

ditin

jau

(X)

Page 5: Tabel Konveksi

]

0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.90.00

5.00

10.00

15.00

20.00

25.00

30.00

Grafik Kondisi A-C Hubungan X-Tb

Panjang Pipa yang ditinjau (X)

Tem

pera

tur d

alam

pip

a (T

w)

0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.90.00

10000.00

20000.00

30000.00

40000.00

50000.00

60000.00

70000.00

Grafik Kondisi A Hubungan X-H

Koefisien Perpindahan Kalor (Tw)

Jara

k Ti

tik y

ang

ditin

jau

(X)

0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.90.00

5000.0010000.0015000.0020000.0025000.0030000.0035000.0040000.0045000.0050000.00

Grafik Kondisi B Hubungan X-H

Koefisien Perpindahan Kalor (Tw)

Jara

k Ti

tik y

ang

ditin

jau

(X)

Page 6: Tabel Konveksi

0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.90.00

5000.00

10000.00

15000.00

20000.00

25000.00

30000.00

35000.00

40000.00

45000.00

Grafik Kondisi C Hubungan X-H

Koefisien Perpindahan Kalor (Tw)

Jara

k Ti

tik y

ang

ditin

jau

(X)

0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.90.00

5000.00

10000.00

15000.00

20000.00

25000.00

30000.00

35000.00

40000.00

45000.00

Grafik Kondisi C Hubungan X-H

Koefisien Perpindahan Kalor (Tw)

Jara

k Ti

tik y

ang

ditin

jau

(X)

Page 7: Tabel Konveksi

Radiasi

Pengujian

Pembacaan Termocouple (mv)

Radiation Shield (mm)

Konversi ke Suhu Suhu Mutlak

t1 t2 output r L to tr To Tr

1 1.62 1.22 0.01 40.00 280.00 35.31 0.26 308.31 273.26

2 1.66 1.23 0.01 40.00 280.00 35.92 0.26 308.92 273.26

3 1.73 1.23 0.01 40.00 280.00 36.78 0.26 309.78 273.26

4 1.90 1.23 0.01 40.00 280.00 38.88 0.26 311.88 273.26

5 2.28 1.24 0.01 40.00 280.00 43.62 0.26 316.62 273.26

6 3.02 1.24 0.02 40.00 280.00 52.60 0.51 325.60 273.51

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PengujianPembacaan

Termocouple (mv)Radiation

Shield (mm)Konversi ke

Suhu Suhu MutlakFro Emc

t1 t2 output r L to tr To Tr

1 1.62 1.22 0.01 40.00 280.00 35.31 0.26 308.31 273.26 0.02 0.204

2 1.66 1.23 0.01 40.00 280.00 35.92 0.26 308.92 273.26 0.02 0.200

3 1.73 1.23 0.01 40.00 280.00 36.78 0.26 309.78 273.26 0.02 0.194

4 1.90 1.23 0.01 40.00 280.00 38.88 0.26 311.88 273.26 0.02 0.182

5 2.28 1.24 0.01 40.00 280.00 43.62 0.26 316.62 273.26 0.02 0.158

6 3.02 1.24 0.02 40.00 280.00 52.60 0.51 325.60 273.51 0.02 0.250

305.00 310.00 315.00 320.00 325.00 330.000.000

0.050

0.100

0.150

0.200

0.250

0.300

Grafik Temperatur (To) - Emisivitas (Emc)

Emisivitas

Tem

pera

tur (

To)

273.20 273.25 273.30 273.35 273.40 273.45 273.50 273.550.000

0.050

0.100

0.150

0.200

0.250

0.300

Grafik temperatur (Tr) - Emisivitas (E mc)

Emisivitas (Tr)

Tem

pera

tur (

Tr)

Page 9: Tabel Konveksi

70 80 90 100 110 120 130 140 150-1

1

3

5

7

9

11

13

15

Kurva Temp-λ

Set Temp

λ

Page 10: Tabel Konveksi

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