單效降膜蒸發(fā)器

?醇蒸發(fā)量(kg /h)
Ethanol evaporation capacity(kg/h)

100

200

400

600

800

1000

1200

A、加熱源介質(zhì)：蒸汽
A. Heating source medium:steam

?蒸汽壓?(Mpa)
Raw steam pressure (Mpa)

0.085 (絕對壓? Absolute pressure)

耗蒸汽熱量(kcal/h)
Steam heat consumption (kcal/h)

30000

60000

120000

180000

240000

300000

360000

B、加熱源介質(zhì)：導(dǎo)熱油
B. Heating source medium:heat transfer oil

導(dǎo)熱油進(jìn)出口溫度(℃)
Heat transfer oil inlet and outlet temperature (℃)

120—130/100—110

耗導(dǎo)熱油熱量(kcal/h)
Heat consumption of heat transfer oil (kcal/h)

31000

62000

124000

186000

248000

310000

372000

導(dǎo)熱油?作壓?(Mpa)
Working pressure of heat transfer oil (Mpa)

0.15—0.20

蒸發(fā)溫度(℃)
Evaporation temperature (℃)

65—75

?醇出料溫度(℃)
Ethanol discharge temperature (℃)

35—40

濃縮液出料溫度(℃)
Concentrate discharge temperature (℃)

63—73

真空度(-Mpa)
Vacuum (-Mpa)

0.065—0.077

加熱?積(㎡)
Heating area (㎡)

3.0

6.0

12

18

24

30

36

冷凝?積(㎡)
Condensing area (㎡)

6.0

12

24

36

48

60

72

冷凝器?作壓?(Mpa)
Condenser workingpressure (Mpa)

0.20—0.25

冷卻?積(㎡)
Cooling area (㎡)

2.0

3.0

4.0

5.0

6.0

8.0

10

冷卻器?作壓?(Mpa)
Cooler working pressure (Mpa)

0.15—0.20

冷卻水循環(huán)量(t/h)
Cooling water circulation (t/h)

3.8

7.6

17

24

32

39

47

冷卻水?作壓?(Mpa)
Cooling water workingpressure (Mpa)

0.20—0.25

冷卻水進(jìn)出口溫度(℃)
Cooling water inlet and outlet temperature (℃)

32—35/40-43

冷凍水消耗量(Kcal/h) Chilled water consumption (Kcal/h)

1500

3000

6000

9000

12000

15000

18000

冷凍水進(jìn)出口溫度(℃)
Chilled water inlet and outlet temperature (℃)

10—20/18—28

冷凍水?作壓?(Mpa)
Chilled water workingpressure (Mpa)

0.15—0.20

裝機(jī)總功率(kw/h)
Total installedpower (kw/h)

3.75

5.55

6.6

8.7

10.7

12.5

14.25