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In 2000, EPG took the guide in gaining ISO14001 setting management certificate and thereafter handed the inspection of clean generation and recycling economic climate, profitable the title of “Zhejiang Eco-friendly Company”. We are seeking forward to developing profitable organization relationships with new customers around the entire world in the potential. It has established stable cooperation with a lot of effectively identified universities and institutes in china this sort of as, Zhejiang University, Jilin College, Technical committee of nationwide chain drive regular, Institute of national chain drive, Zhejiang software engineering material institute, Huhan material defense institute and it cooperated to located China Very first Auto chain institute with Nationwide chain travel institute.

Multi-effect evaporation, Crystallization amp Concentration, squander drinking water remedy, Environmental protecting gear

Organization Details

HangZhou EPTTA EPTRY CO., the greatest company of alcoholic beverages, gas ethanol and DDGS substantial protein feed full tools in EPT.

Our organization can design and manufacture Multi-impact evaporator amp MVR evaporator
Our company can design and style and manufactureclass-I, class-II, course-III strain vessel.

Our firm is able to design and style, manufacture, put in and alter 3000t-500000t alcohol full equipmentin the turnkey venture .

Item Description:

MVR Procedure Exposition

one Procedure liquids

The liquid to be handled, prior to EPTring the boiling chamber D01 (the place the EPT conditions of 70 kPa and 90 degC are preserved), is preheated in the heat exchanger E03 by the concentrate (if the optional method V is mounted) and in E02 by the discharging distillate. Pump G02 functions repeatedly recirculating the liquid to be handled in orEPTto hold cleanse the plate exchanger E02 and feeding the EPT by means of opening of valve VP01, controlled by the stage sensor LS01. The filtration system F02 (if the optional program IV is installed) makes it possible for to individual feasible coarse supplies current in the liquid EPTring the EPT (see par.10). The concentrate is recirculated by the pump G01 which pumps it by way of the principal heat exchanger E01 (tube side). Inside of E01 the liquid EPTs from the condensing vapour the heat essential to boil after heated, the concentrate is despatched once again to the boiling chamber D01. As a consequence of the EPT, a part of the liquid instantly boils (flash evaporation). The made vapour passes through the drops separator (H04) in orEPTto eradicate suspended liquid drops and improve the high quality of the output distillate.

The blower K01 compresses the vapour and sends it to the heat exchanger E01 (shell facet) in which it releases the latent heat to the procedure liquid. The condensed vapour is collected in the tank D02 and then it is discharged by the pump G03 following a heat exchange in E02. The sensor CE01 actions the conductivity of the distillate: high conductivity means substantial entrainment of liquid in the boiling chamber and the EPT demonstrates an alarm to the operator.

The temperature sensor TE02 steps the temperature of the distillate in D02. The movement sensor FT01 steps the quantity of distillate discharged. The exchanger E01 can be provided with quotfloating head quot in orEPTto enable an less complicated cleansing procedure, by signifies of elimination of the tube nest, if the EPT treats fouling vapours.

The concentrate is discharged routinely through the valve VP05. Movement sensor FT02 actions the quantity of focus discharged.

The density meter DT01 (if the optional method I is put in) makes it possible for to discharge the focus once it reaches a density benefit set by the consumer.

Answers amp Technologies

Throughout the startup of the EPT the liquid in the EPT and the distillate in D02 are heated by the resistors ER01- ER02- ER03-ER05-ER06. The incondensable gases are discharged through a devoted chimney (outlet five, see Determine 1). Dry cooler K03 (if the optional technique VI is put in) enables to condense possible residual vapours eXiHu (West Lake) Dis.ting by means of the vent.

two Mechanical vapour recompression

The produced vapour in the boiling chamber D01 is sucked into the positive displacement blower K01 that, by means of the compression, raises the temperature later on the vapour passes via the shell of the exchanger E01 the place it condenses and releases the latent heat to the recirculated liquid of the boiling chamber. Valve VP10, during startup phase, is open up in orEPTto enable a gradual startup of the blower K01.

Admirer K02 permits to keep managed the temperature of the oil in the blower in orEPTto lengthen its provider lifestyle in situation of operation in thermally tough conditions.

three Thermal recovery methods

Thermal restoration is realised via the exchangers E03 (if the optional method V is installed) and E02. The liquid to be taken care of crosses each of them and warms up before EPTring the boiling chamber. Temperature sensor TE08 actions the temperature of the liquid to be treated EPTring the EPT following the recovery exchangers.

The focus passes through the tube and shell heat exchanger E03 and cools down, ahead of its discharging, as a consequence of the heat exchange with the liquid to be treated. Valve VP03 (if the optional system V is set up) allows the stream of the liquid to be treated by way of exchanger E03. The distillate EPTrs the plate warmth exchanger E02 and cools down, before its discharging, as a consequence of the heat exchange with the liquid to be dealt with.

Temperature sensor TE07 actions the temperature of the distillate editing the EPT.

4 AuXiHu (West Lake) Dis.liary liquids

Antifoam, equipped by the opening of the timed valve VP06. If optional III is present, antifoam is metered instantly.

The foam sensor SS01 detects the existence of foam in D01 and instructions the opening of valve VP06.

EPTp drinking water, for washing of factors inside the boiling chamber D01, through timed valves VP07 (sensor LS01 washing)

and VP12 (foam sensor SS01 washing, if the optional system III is set up).

Additive metering with pump G07 and pneumatic valve if the optional system II is mounted.

EPTactericide metering in the delivery pipeline of distillate discharge pump, if the optional method AM EPTT D is put in.

Comparison EPTetween MVR and 4-result Evaporator


four-result Evaporator



Vitality-conserving, vaporizing one ton water consumes .three ton fresh steam.

Much more power-conserving,vaporizing 1 ton water consumes 30kw*h electric power


Refreshing steam

EPT electric power





EPTer method duration with greater temperature variance impacts sturdiness.

Shorter method length with lower temperature improves toughness.

Output Kind




1. it is a flip crucial EPT set equipment,basic tools, much less employee,considerably less spot,much less expense.

2. can create 1000L-1000000L 96%-ninety nine.nine% alcoholic beverages(ethanol) for every day.

3. can use Corn, wheat, cassava, molasses,rice,potato, date,beetroot ,suXiHu (West Lake) Dis.Hu (West Lake) Dis. cane ect which is made up of starch or suXiHu (West Lake) Dis.Hu (West Lake) Dis. substance.

4. we can do the flip key program or EPT portion.

5. Can increase and rebuild previous alcoholic beverages(ethanol) generation line .

You can decide on one distill tower to save income, also can decide on five distill column to get good top quality alcoholic beverages/ethanol.

Five-Column 3-Effect Distillation Approach
Our business styles and manufactures latestFive-Column Three-Effect Distillation gear.This new approach is promoted on the foundation of traditional five-column differential-pressure column and mainly utilized for tremendous-fantastic alcohol manufacturing.
The important of this process is the heating approaches,the steam heats one particular column immediately and transfers theheat to other 4 columnsto attain a few-result thermal coupling and strength-preserving results.
In terms of electricityefficiency, it can help save 50% electric power and stay away from the repairing of circulating pumps and also lengthen the working existence of there-EPTs.

Double-Mash-Column 3-Impact Distillation Process
This approach applies to the production of EPT-quality alcoholic beverages amp gasoline ethanol, and it was awarded EPT nationwide patent, it is the onlysuccessfulapplicationof double mash column amp three-result in the world,which makes EPT-quality liquor.
This procedure is composed by mash column, rectification column and composite column. The composite column features as mash column and rectification column.
The crucial of this method is the heating approaches: the steam heats 1 column directly and transfers the heat to other 2 columns to achieve 3-result thermal coupling and power-saving outcomes.
The advantage of this method is energy-savingit saves over 40% steam.

Generation Capacity

one,Our firm was estabEPTd in the fifties, created and made the initial stainless steel distillation column in EPT.

two,Our company can produce six complete sets of equipment (incXiHu (West Lake) Dis.Hu (West Lake) Dis. crushing EPT, liquefying saccharification EPT, fermentation EPT, distillation EPT and DDGS EPT) in a month.

three,Between 16 generation workshops,3 workshops are for mechanic manufacture, five workshops arefor producing procedure, 8 workshops are for assembling amp welding.

4,We very own innovative machining products and product screening gear.

Created capability

one). We personal Design and style License of Particular Products D1 amp D2 Course Manufacture License of Unique Equipment A2 Course Style License of Special Gear GC Class.

two).Our business achieves much more than twenty patent certificates on distillation, DDGS, and other fields.

three). Our organization owns ASME certification, ISO 9001 EPT Program Certification, ISO 14001 Environmental Management Program Certification amp GEPT/T28001 Occupational Overall health and Security Management Method Certification

Following-income Service

one).Our company can give a refined solution soon after-sale support and can ensure the implementation, servicing and fee of projects.

two). We can get to the venture website after receiving the user’s notification.

Package deal amp Transport

Our company can bundle the items in accordance to EPTrprise export stXiHu (West Lake) Dis.Hu (West Lake) Dis.rd, and use container or bulk transportation.

Make contact with us

Name: Vick Liang
Electronic mail: [email protected]
Tel: 86 13953842508
Mobile phone: 86-538-3393266
Fax: 86-538-3399066
Skype: vicklwk
QQ: 496443614
Handle: HangZhou High-tech EPT Zone, EPTi’an, ZheJiang , EPT
World wide web:

  in Sydney Australia  sales   price   shop   near me   near me shop   factory   supplier Mvr-Falling Film Evaporator manufacturer   best   Cost   Custom   Cheap   wholesaler

  in Sydney Australia  sales   price   shop   near me   near me shop   factory   supplier Mvr-Falling Film Evaporator manufacturer   best   Cost   Custom   Cheap   wholesaler