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换热设备

管式加热炉

作者:admin    访问量:3672    发布时间:2014-11-26


公称换热面积m2

通道间距mm

计算
换热面积
m2

 
1m/ces
处理量m3/h

接管公称直径

 

重量(kg)

I 6B

I 16B

1

6

1.0

3.89

40

I 6,I 16B1-0.2/300-6

44

50

2

6

2.1

3.89

40

I 6,I 16B2-0.2/400-6

78

85

4

6

4.4

8.2

50

I 6,I 16B4-0.4/400-6

131

135

10

4.5

17.3

80

I 6,I 16B4-0.5/450-10

129

133

10

4.8

13.7

70

I 6,I 16B4-0.4/500-10

161

205

8

6

7.3

8.21

50

I 6,I 16B8-0.4/500-6

212

215

10

7.85

17.3

80

I 6,I 16B8-0.5/550-10

235

273

10

7.3

20.90

80

I 6,I 16B8-0.6/500-10

237

275

10

6

11.1

8.21

50

I 6,I 16B10-0.4/600-6

295

355

10

11.5

17.3

80

I 6,I 16B10-0.5/650-10

315

405

10

11.2

20.90

80

I 6,I 16B10-0.6/600-10

305

395

15

6

16.9

12.54

70

I 6,I 16B15-0.6/600-6

415

490

10

14.72

17.3

80

I 6,I 16B15-0.5/760-10

405

575

10

15.0

28.1

80

I 6,I 16B15-0.8/600-10

400

570

14

15.6

39.3

100

I 6,I 16B15-0.8/700-14

505

680

20

6

21.7

8.21

50

I 6,I 16B20-0.4/800-6

540

710

10

21.0

20.90

80

I 6,I 16B20-0.6/800-10

555

735

14

20.9

39.30

100

I 6,I 16B20-0.8/800-14

660

830

25

10

26.6

29.90

80

I 6,I 16B25-0.6/900-10

610

950

14

26.9

39.20

100

I 6,I 16B25-0.8/900-14

720

1060

30

10

28.2

28.10

100

I 6,I 16B30-0.8/800-14

750

1180

14

32.2

39.20

100

I 6,I 16B30-0.8/1000-14

980

1370

40

10

45.4

35.30

100

I 6,I 16B40-1.0/900-10

1130

1515

14

40.2

19.4

125

I 6,I 16B40-1.0/1000-14

1200

1630

50

10

53.9

35.3

100

I 6,I 16B50-1.0/1000-14

1360

1755

60

10

61.05

35.3

100

I 6,I 16B60-1.0/1100-10

1920

2112

14

60.08

49.40

125

I 6,I 16B60-1.0/1200-14

2000

2200

80

10

81.83

35.3

100

I 6,I 16B80-1.0/1200-10

2560

2816

14

80.9

49.40

125

I 6,I 16B80-1.0/1400-14

2667

1934

100

10

101.9

35.3

100

I 6,I 16B100-1.0/1300-10

3200

3520

14

100.06

49.40

125

I 6,I 16B100-1.0/1500-14

3333

3666

120

10

115.5

35.3

100

I 6,I 16B120-1.0/1500-10

3870

4257

14

119.0

49.40

125

I 6,I 16B120-1.0/1700-14

4020

4422

130

14

128.80

49.4

125

I 6,I 16B130-1.0/1750-14

4241

4665

18

129.09

63.5

150

I 6,I 16B130-1.0/1967-18

4462

4908

150

14

148.1

49.4

125

I 6,I 16B150-1.0/1890-14

4702

5172

18

148.2

63.5

150

I 6,I 16B150-1.0/2010-18

4962

5458

公称换热面积m2

通道间距mm

计算换热面积   m2

 
1m/ces
处理量
m3/h

接管公称直径

 

重量(kg)

I 6T

I 16T

6

6

6.5

8.2

50

I 6, I 16T6-0.4/500-6

230

280

10

5.8

13.7

70

I 6, I 16T6-0.4/600-10

285

350

8

6

8.7

8.2

50

I 6, I 16T8-0.4/600-6

370

430

10

7.7

17.3

80

I 6, I 16T8-0.5/660-10

395

454

10

8.7

13.7

70

I 6, I 16T8-0.4/700-10

405

465

10

6

9.9

12.5

70

I 6, I 16T10-0.6/500-6

335

395

10

9.2

17.30

80

I 6, I 16T10-0.5/660-10

472

543

10

8.8

20.9

80

I 6, I 16T10-0.6/600-10

410

495

15

6

12.5

8.2

50

I 6, I 16T15-0.4/700-6

510

580

10

14.64

17.30

80

I 6, I 16T15-0.5/800-10

679

781

10

13.3

20.9

80

I 6, I 16T15-0.6/700-10

575

680

14

13.8

29.2

100

I 6, I 16T15-0.6/800-14

640

755

20

6

19.0

12.5

70

I 6, I 16T20-0.6/700-6

730

845

10

18.3

28.1

80

I 6, I 16T20-0.8/800-10

735

870

14

18.5

39.3

100

I 6, I 16T20-0.8-800-14

810

960

25

10

23.1

28.1

100

I 6, I 16T25-0.8/800-10

935

1120

14

23.3

49.4

125

I 6, I 16T25-1.0/800-14

1000

1165

30

10

29.0

35.3

100

I 6, I 16T30-1.0/800-10

1190

1470

14

28.1

59.4

125

I 6, I 16T30-1.2/800-14

1170

1425

40

10

40.9

20.9

80

I 6, I 16T40-0.6/1200-10

1725

1885

14

42.3

39.3

100

I 6, I 16T40-0.8/1200-14

1845

2110

18


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