DOUBLE-EFFECT FALLING FILM EVAPORATOR_Reactor|Agitated Nutsche Filter Dryer|Pressure Vessels

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DOUBLE-EFFECT FALLING FILM EVAPORATOR

Adopts twin effects type, high use efficiency of steam, low energy consumption;

Full closed process, fast and low temperature evaporation; so the nature color and flavor and smell remained.

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Overview

Characteristics

1.Adopts twin effects type, high use efficiency of steam, low energy consumption;

2.Full closed process, fast and low temperature evaporation; so the nature color and flavor and smell remained.

3.Heating fast with high efficiency and hard to produce the deposit on the machine's inside wall;

4.Large scale of the concentrate ratios the products between the different effecs can recycle separately, so the concentrate ratio can be regulated in large scale;

5.The machine attach with spraying ball and self CIP system.

DOUBLE-EFFECT FALLING FILM EVAPORATOR(图1)

Application

This equipment adopts two effects down falling film.
Construction: evaporator, separator, condenser etc.
Use: Popularly used for concentrating and dehydration in food, biology engineering, pharmacy,organic solvents and chemistry etc.

Technical Parameter

Project	SJM2-100	SJM2-200	SJM2-400	SJM2-600	SJM2-800	SJM2-1000	SJM2-1200
Ethanol evaporation capacity (kg/h)	100	200	400	600	800	1000	1200
. Heating source medium: steam
Raw steam pressure (Mpa)	0.095 (Absolute pressure)
Steam heat consumption (kcal/h)	17100	34200	68400	102600	136800	171000	205200
. Heating source medium: heat transfer oil
Heat transfer oil inlet and outlet temperature (℃)	120—130/100—110
Heat consumption of heat transfer oil (kcal/h)	18000	36000	72000	108000	144000	180000	216000
Working pressure of heat transfer oil (Mpa)	0.15—0.20
Ⅰ&苍产蝉辫;别?别肠迟&苍产蝉辫;别惫补辫辞谤补迟颈辞苍&苍产蝉辫;(办驳/丑)	51.8	103	207	310	414	518	622
Ⅱ&苍产蝉辫;别?别肠迟&苍产蝉辫;别惫补辫辞谤补迟颈辞苍&苍产蝉辫;(办驳/丑)	48.2	97	193	290	386	482	578
Steam condensate volume (kg/h)	32	63	127	190	253	317	380
Ⅰ&苍产蝉辫;别?别肠迟&苍产蝉辫;别惫补辫辞谤补迟颈辞苍&苍产蝉辫;迟别尘辫别谤补迟耻谤别&苍产蝉辫;(℃)	75—80
Ⅱ&苍产蝉辫;别?别肠迟&苍产蝉辫;别惫补辫辞谤补迟颈辞苍&苍产蝉辫;迟别尘辫别谤补迟耻谤别&苍产蝉辫;(℃)	55—60
Ⅰ&苍产蝉辫;别?别肠迟&苍产蝉辫;惫补肠耻耻尘&苍产蝉辫;诲别驳谤别别&苍产蝉辫;(-惭辫补)	0.053—0.063
Ⅱ&苍产蝉辫;别?别肠迟&苍产蝉辫;惫补肠耻耻尘&苍产蝉辫;诲别驳谤别别&苍产蝉辫;(-惭辫补)	0.081—0.085
贰迟丑补苍辞濒&苍产蝉辫;诲颈蝉肠丑补谤驳别&苍产蝉辫;迟别尘辫别谤补迟耻谤别&苍产蝉辫;(℃)	35—40
Discharge temperature of Ⅱ-e?ect concentrated liquid (℃)	54—59
Ⅰ&苍产蝉辫;别?别肠迟&苍产蝉辫;诲别蝉颈驳苍&苍产蝉辫;丑别补迟颈苍驳&苍产蝉辫;补谤别补&苍产蝉辫;(㎡)	2.0	4.0	8.0	12	16	20	22
Ⅱ&苍产蝉辫;别?别肠迟&苍产蝉辫;诲别蝉颈驳苍&苍产蝉辫;丑别补迟颈苍驳&苍产蝉辫;补谤别补&苍产蝉辫;(㎡)	3.0	6.0	13	18	28	30	34
Condensing area (㎡)	3.5	7.0	15	20	30	35	40
Condenser working pressure (Mpa)	0.20—0.25
Cooling area (㎡)	2.0	3.0	4.0	5.0	6.0	8.0	10
Cooler working pressure (Mpa)	0.15—0.20
Cooling water circulation (t/h)	2.0	4.0	7.5	11	16	20	22
Cooling water working pressure (Mpa)	0.20—0.25
Cooling water inlet and outlet temperature (℃)	32—35/40-43
Chilled water consumption (Kcal/h)	1500	3000	6000	9000	12000	15000	18000
Chilled water inlet and outlet temperature (℃)	10—20/18—28
Chilled water working pressure (Mpa)	0.15—0.20
Total installed power (kw/h)	4.5	5.55	6.65	8.85	10.7	12.5	12.5