EVP - Steam Ejector System
EVP - Steam Ejector System EVP Vacuum System Vacuum Products Malaysia, Penang, Singapore, Indonesia Supplier, Suppliers, Supply, Supplies | Hexo Industries (M) Sdn Bhd
EVP - Steam Ejector System

Description: EVP steam ejector and air ejector with water-saving, steam conservation features, it’s widely used in edible oil,waste oil refining,fatty acid distillation, deodorization.


Product Info:


Steam ejector is type of vacuum obtain device with certain pressure. Motive steam passing through the jet nozzle£¬its pressure decreased and speed accelerated, the steam’s potential energy is turned into kinetic energy, ejected into suction (mixing) chamber and mixed with evacuated gas. Then the energy is exchanged. When mixed air entering the diffuser, its speed lowered and pressure increased, the kinetic energy is turned into pressure energy. Followed can be found the general working principle:

besides, it’s also good option to be worked together with liquid ring vacuum pump to create higher ultimate pressure.

The combination of ejector and condenser meets various needs of vacuum

Main Features:
The working vacuum range is very wide: 0.005-101.3KPa (A);
The pumping volume can theoretically be unlimited;
There are no strict restrictions on the pumping medium, no matter the humidity of the pumped medium is high or low, whether there is dust or corrosion, it can be used;
No rotating parts, long service life;
Safe and reliable work, simple operation, low cost and easy maintenance;
With an intermediate condenser, a 12m high position is required;
Simple structure; reliable technology;stable vacuum degree; low maintenance and long service life.
It can be used to suction some corrosive gas, flammable, explosive gas and particulate medium,etc. directly.
Multi-stage steam ejector vacuum system with leading technology, stable performance and the lowest operating cost features. The other products are incomparable.

Steam jet vacuum pump features and applications:
vacuum metallurgy, vacuum deaeration, vacuum impregnation, freeze drying, concentration, distillation, refrigeration,vacuum evaporation of petroleum, chemical, pharmaceutical, oil, sugar, salt, paper and other fields,such as concentration, drying, distillation, distillation, crystallization, dehydrated, filtering, vacuum conveying material, chemical absorption and degassing process. With different pumping speed and working vacuum, we have many types of model for customer selection.

Specifications:
 

Steam jet vacuum pump layout :

Single stage steam jet vacuum pump

Single stage steam jet vacuum pump

 

Two stage steam jet vacuum pump

Two stage steam jet vacuum pump

model Vacuum absolute pressure Pumping volume

 

Air + water vapor

kg/h

Working steam pressure

 

MPa

Working steam consumption

 

kg/h

Cooling water temperature

 

OC

Cooling water circulation

 

m3/h

Working vacuum

 

mmhg/KPa

Ultimate vacuum

 

mmhg/Pa

¢òZPL(5/10)-40 40/5.3 16/2 5+10 0.5 68 32 3
¢òZPL(5/18)-40 40/5.3 16/2 5+18 0.5 110 32 4
¢òZPL(10/25)-40 40/5.3 16/2 10+25 0.5 188 32 6
¢òZPL(10/35)-40 40/5.3 16/2 10+35 0.5 198 32 7.5
¢òZPL(15/50)-40 40/5.3 16/2 15+50 0.5 273 32 11
¢òZPL(15/80)-40 40/5.3 16/2 15+80 0.5 420 32 16
¢òZPL(25/45)-75 75 30/4 25+45 0.8 135 32 6.8
¢òZPL(35/55)-75 75 30/4 35+55 0.8 238 32 7

 

Three stage steam jet vacuum pump

Three stage steam jet vacuum pump

model Vacuum absolute pressure Pumping volume

 

Air + water vapor

kg/h

Working steam pressure

 

MPa

Working steam consumption

 

kg/h

Cooling water temperature

 

OC

Cooling water circulation

 

m3/h

Working vacuum

 

mmhg/KPa

Ultimate vacuum

 

mmhg/Pa

¢óZPL(8/20)-20 20/2.6 8/1 8+20 0.5 80 32 5
¢óZPL(8/30)-20 20/2.6 8/1 8+30 0.5 130 32 8
¢óZPL(10/40)-20 20/2.6 8/1 10+40 0.5 155 32 10
¢óZPL(10/50)-20 20/2.6 8/1 10+50 0.5 234 32 15
¢óZPL(10/60)-20 20/2.6 8/1 10+60 0.5 256 32 18
¢óZPL(10/80)-20 20/2.6 8/1 10+80 0.5 289 32 20
¢óZPL(10/100)-20 20/2.6 8/1 10+100 0.5 335 32 35
¢óZPL(20/150)-20 20/2.6 8/1 20+150 0.5 387 32 35
¢óZPL(20/200)-20 20/2.6 8/1 20+200 0.5 456 32 40
¢óZPL(30/250)-20 20/2.6 8/1 30+250 0.5 491 32 45
¢óZPL(30/300)-20 20/2.6 8/1 30+300 0.5 532 32 48
¢óZPL(30/350)-20 20/2.6 8/1 30+350 0.5 732 32 50
¢óZPL(40/400)-20 20/2.6 8/1 40+400 0.5 789 32 55
¢óZPL(40/450)-20 20/2.6 8/1 40+450 0.5 888 32 60

 

Four stage steam jet vacuum pump

Four stage steam jet vacuum pump

model Vacuum absolute pressure Pumping volume

 

Air + water vapor

kg/h

Working steam pressure

 

MPa

Working steam consumption

 

kg/h

Cooling water temperature

 

OC

Cooling water circulation

 

m3/h

Working vacuum

 

mmhg/KPa

Ultimate vacuum

 

mmhg/Pa

¢ôZPL(8/20)-1 1/133 0.2/27 8+20 0.5 362 32 50
¢ôZPL(8/30)-1 1/133 0.2/27 8+30 0.5 430 32 50
¢ôZPL(10/40)-1 1/133 0.2/27 10+40 0.5 680 32 70
¢ôZPL(10/60)-1 1/133 0.2/27 10+60 0.5 980 32 100
¢ôZPL(10/80)-1 1/133 0.2/27 10+80 0.5 1230 32 160
¢ôZPL(10/100)-1 1/133 0.2/27 10+100 0.5 1500 32 180
¢ôZPL(20/120)-1 1/133 0.2/27 20+120 0.5 1980 32 200
¢ôZPL(20/150)-1 1/133 0.2/27 20+150 0.5 2500 32 200
¢ôZPL(20/200)-1 1/133 0.2/27 20+200 0.5 3000 32 250
¢ôZPL(30/300)-1 1/133 0.2/27 30+300 0.5 4500 32 300
¢ôZPL(40/400)-1 1/133 0.2/27 40+400 0.5 6000 32 380
¢ôZPL(50/500)-1 1/133 0.2/27 50+500 0.5 7000 32 550
¢ôZPL(80/800)-1 1/133 0.2/27 80+800 0.5 10000 32 650
¢ôZPL(8/20)-2 2/267 0.3/40 8+20 0.5 256 32 50
¢ôZPL(8/30)-2 2/267 0.3/40 8+30 0.5 295 32 50
¢ôZPL(10/40)-2 2/267 0.3/40 10+40 0.5 490 32 60
¢ôZPL(10/60)-2 2/267 0.3/40 10+60 0.5 680 32 70
¢ôZPL(10/80)-2 2/267 0.3/40 10+80 0.5 930 32 100
¢ôZPL(10/100)-2 2/267 0.3/40 10+100 0.5 1000 32 120
¢ôZPL(20/120)-2 2/267 0.3/40 20+120 0.5 1100 32 150
¢ôZPL(20/150)-2 2/267 0.3/40 20+150 0.5 1234 32 180
¢ôZPL(20/200)-2 2/267 0.3/40 20+200 0.5 1600 32 200
¢ôZPL(30/300)-2 2/267 0.3/40 30+300 0.5 2332 32 250
¢ôZPL(40/400)-2 2/267 0.3/40 40+400 0.5 2567 32 300
¢ôZPL(50/500)-2 2/267 0.3/40 50+500 0.5 3200 32 350
¢ôZPL(80/800)-2 2/267 0.3/40 80+800 0.5 3819 32 400

 

Five stage steam jet vacuum pump

Five stage steam jet vacuum pump

Note:
1. The models listed in the table are not exhaustive, and can be designed according to the technical parameters provided by users.
2. The technical parameters change accordingly when the user’s process conditions change, so the technical parameters are subject to the technical parameters given at the time of signing the contract.

 

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