Mvr Machinery and Compression Evaporator Energy-Saving Evaporator

Mvr Machinery and Compression Evaporator Energy-Saving Evaporator

Multi-result evaporation, Crystallization & Focus, squander h2o remedy, CZPTal protective equipment 

Business Details

HangZhou XIHU (WEST LAKE) DIS. CZPT CO., the largest manufacturer of liquor, gas ethanol and DDGS higher protein feed complete equipment in China.

Our organization can layout and manufacture Multi-impact evaporator & MVR evaporator
Our firm can design and manufactureclass-I, class-II, course-III pressure vessel.

Our firm is able to style, manufacture, install and alter 3000t-500000t liquor complete equipmentin the turnkey venture .

Product Description:

   MVR Method Exposition

one Procedure liquids

The liquid to be dealt with, ahead of coming into the boiling chamber D01 (in which the vacuum situations of 70 kPa and 90°C are preserved), is preheated in the warmth exchanger E03 by the focus (if the optional program V is installed) and in E02 by the discharging distillate. Pump G02 functions continually recirculating the liquid to be dealt with in purchase to hold thoroughly clean the plate exchanger E02 and feeding the boiler by means of opening of valve VP01, controlled by the level sensor LS01. The filtration gadget F02 (if the optional system IV is set up) allows to separate possible coarse supplies current in the liquid entering the device (see par.ten). The focus is recirculated by the pump G01 which pumps it via the major warmth exchanger E01 (tube facet). Inside of E01 the liquid gets from the condensing vapour the heat essential to boil when heated, the concentrate is despatched again to the boiling chamber D01. As a outcome of the vacuum, a portion of the liquid immediately boils (flash evaporation). The produced vapour passes by means of the drops separator (H04) in get to get rid of suspended liquid drops and enhance the good 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 gathered in the tank D02 and then it is discharged by the pump G03 right after a heat trade in E02. The sensor CE01 measures the conductivity of the distillate: substantial conductivity implies substantial entrainment of liquid in the boiling chamber and the machine demonstrates an alarm to the operator.

The temperature sensor TE02 steps the temperature of the distillate in D02. The circulation sensor FT01 measures the volume of distillate discharged. The exchanger E01 can be supplied with “floating head” in purchase to allow an less complicated cleansing procedure, by indicates of removal of the tube nest, if the equipment treats fouling vapours.

The concentrate is discharged instantly by means of the valve VP05. Flow sensor FT02 steps the amount of concentrate discharged.

The density meter DT01 (if the optional technique I is put in) allows to discharge the concentrate when it reaches a density price established by the user.

Options & CZPT

Throughout the startup of the device the liquid in the boiler and the distillate in D02 are heated by the resistors ER01- ER02- ER03-ER05-ER06. The incondensable gases are discharged via a devoted chimney (outlet five, see Figure one). Dry cooler K03 (if the optional method VI is installed) permits to condense possible residual vapours exiting through the vent.

2 CZPT vapour recompression

The developed vapour in the boiling chamber D01 is sucked into the good displacement blower K01 that, by means of the compression, raises the temperature afterwards the vapour passes via the shell of the exchanger E01 in which it condenses and releases the latent warmth to the recirculated liquid of the boiling chamber. Valve VP10, throughout startup stage, is open in purchase to let a gradual startup of the blower K01.

Admirer K02 permits to keep managed the temperature of the oil in the blower in get to prolong its service lifestyle in case of operation in thermally challenging circumstances.

3 Thermal restoration programs

Thermal restoration is realised through the exchangers E03 (if the optional technique V is put in) and E02. The liquid to be taken care of crosses both of them and warms up just before getting into the boiling chamber. Temperature sensor TE08 measures the temperature of the liquid to be handled getting into the boiler after the recovery exchangers.

The concentrate passes via the tube and shell warmth exchanger E03 and cools down, ahead of its discharging, as a consequence of the heat trade with the liquid to be handled. Valve VP03 (if the optional system V is set up) allows the stream of the liquid to be dealt with by means of exchanger E03. The distillate enters the plate heat exchanger E02 and cools down, ahead of its discharging, as a consequence of the warmth exchange with the liquid to be handled.

Temperature sensor TE07 steps the temperature of the distillate enhancing the device.

four Auxiliary liquids

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

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

Tap h2o, for washing of factors within the boiling chamber D01, by way of timed valves VP07 (sensor LS01 washing)

and VP12 (foam sensor SS01 washing, if the optional technique III is installed).

Additive metering with pump G07 and pneumatic valve if the optional technique II is set up.

Bactericide metering in the delivery pipeline of distillate discharge pump, if the optional program AM BT D is set up.

Comparison Between MVR and four-impact Evaporator


four-effect Evaporator



CZPT-preserving, vaporizing 1 ton h2o consumes .three ton clean steam.

Far more energy-conserving,vaporizing one ton drinking water consumes 30kw*h electrical energy


Refreshing steam

CZPT electrical power





CZPT method period with even bigger temperature variance affects durability.

Shorter process duration with reduced temperature improves durability.

Output Type





one. it is a change important total established gear,easy products, less worker,considerably less area,much less cost.

2. can produce 1000L-1000000L 96%-99.9% liquor(ethanol) for every day.

three. can use Corn, wheat, cassava, molasses,rice,potato, day,beetroot ,sugar cane ect which contains starch or sugar material.

four. we can do the flip crucial method or section part.

five. Can improve and rebuild previous alcoholic beverages(ethanol) generation line .

You can select single distill tower to preserve money, also can decide on five distill column to get very good top quality liquor/ethanol.

Five-Column Three-Effect Distillation Approach
Our business styles and manufactures latestFive-Column 3-Impact Distillation products.This new procedure is promoted on the basis of standard 5-column differential-stress column and mostly utilized for tremendous-wonderful liquor manufacturing.
The key of this method is the heating methods,the steam heats one particular column right and transfers theheat to other four columnsto obtain 3-influence thermal coupling and power-conserving outcomes.
In terms of electricityefficiency, it can save fifty% electricity and avoid the restoring of circulating pumps and also increase the doing work life of there-boilers.

Double-Mash-Column 3-Effect Distillation Procedure
This method applies to the generation of general-grade liquor& gas ethanol, and it was awarded Chinese national patent, it is the onlysuccessfulapplicationof double mash column & 3-effect in the globe,which creates general-quality liquor.
This approach is composed by mash column, rectification column and composite column. The composite column functions as mash column and rectification column.
The important of this method is the heating methods: the steam heats one particular column directly and transfers the warmth to other two columns to accomplish a few-effect thermal coupling and vitality-preserving results.
The advantage of this procedure is power-savingit saves more than 40% steam.

Generation Ability

one,Our company was recognized in the nineteen fifties, developed and created the initial stainless steel distillation column in China.

two,Our firm can make six complete sets of gear (such as crushing segment, liquefying saccharification segment, fermentation segment, distillation section and DDGS segment) in a thirty day period.

3,Among sixteen creation workshops,3 workshops are for mechanic manufacture, five workshops arefor production process, 8 workshops are for assembling & welding.

4,We own innovative machining tools and merchandise tests gear.

Made capability

1). We personal Style License of Particular CZPT D1 & D2 Class CZPT License of Unique CZPT A2 Class Style License of Particular CZPT GC Course.

2).Our company achieves far more than 20 patent certificates on distillation, DDGS, and other fields.

three). Our business owns ASME certification, ISO 9001 CZPT Method Certification, ISO 14001 CZPTal Management Method Certification & GB/T28001 Occupational Health and Security Administration System Certification

Following-income Provider

1).Our firm can give a sophisticated product following-sale support and can guarantee the implementation, upkeep and commission of tasks.

two). We can get to the undertaking website right after getting the user’s notification.

Deal & Transportation

Our business can package the goods in accordance to business export CZPT, and use container or bulk transport.

Make contact with us

Title:  Vick Liang
Electronic mail:   [email protected]
Tel:       86~thirteen 0571 88828 13858117778953842508
Phone:  86-538-3393266
Fax:       86-538-3399066
Skype:   vicklwk
QQ:        496443614
Address: HangZhou High-tech CZPT Zone, HangZhou, ZheJiang , China

Mvr Machinery and Compression Evaporator Energy-Saving Evaporator

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