Mvr Citric Acid Evaporator

Mvr Citric Acid Evaporator

Multi-impact evaporation, Crystallization & Focus, squander h2o therapy, CZPTal protective equipment 

Firm Data

HangZhou XIHU (WEST LAKE) DIS. CZPT CO., the greatest company of liquor, fuel ethanol and DDGS large protein feed complete equipment in China.

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

Our organization is able to style, manufacture, install and adjust 3000t-500000t liquor total equipmentin the turnkey project .

Merchandise Description:

   MVR Approach Exposition

one Approach liquids

The liquid to be treated, before entering the boiling chamber D01 (where the vacuum circumstances of 70 kPa and 90°C are maintained), is preheated in the warmth exchanger E03 by the focus (if the optional method V is installed) and in E02 by the discharging distillate. Pump G02 performs continually recirculating the liquid to be handled in order to preserve thoroughly clean the plate exchanger E02 and feeding the boiler by way of opening of valve VP01, controlled by the level sensor LS01. The filtration system F02 (if the optional method IV is set up) makes it possible for to separate attainable coarse resources present in the liquid entering the device (see par.ten). The focus is recirculated by the pump G01 which pumps it via the principal warmth exchanger E01 (tube facet). Inside of E01 the liquid gets from the condensing vapour the warmth essential to boil after heated, the focus is sent yet again to the boiling chamber D01. As a consequence of the vacuum, a part of the liquid immediately boils (flash evaporation). The created vapour passes by way of the drops separator (H04) in buy to remove suspended liquid drops and improve the top quality of the output distillate.

The blower K01 compresses the vapour and sends it to the warmth exchanger E01 (shell side) exactly where it releases the latent warmth to the procedure liquid. The condensed vapour is gathered in the tank D02 and then it is discharged by the pump G03 soon after a warmth trade in E02. The sensor CE01 measures the conductivity of the distillate: high conductivity indicates substantial entrainment of liquid in the boiling chamber and the machine exhibits an alarm to the operator.

The temperature sensor TE02 actions the temperature of the distillate in D02. The stream sensor FT01 actions the sum of distillate discharged. The exchanger E01 can be supplied with “floating head” in get to allow an less difficult cleaning method, by signifies of removal of the tube nest, if the machine treats fouling vapours.

The concentrate is discharged automatically through the valve VP05. Movement 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 once it reaches a density price established by the user.

Options & CZPT

Throughout the startup of the equipment 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 by means of a dedicated chimney (outlet five, see Determine one). Dry cooler K03 (if the optional technique VI is set up) permits to condense feasible residual vapours exiting by means of the vent.

2 CZPT vapour recompression

The made vapour in the boiling chamber D01 is sucked into the optimistic displacement blower K01 that, by indicates of the compression, raises the temperature afterwards the vapour passes via the shell of the exchanger E01 where it condenses and releases the latent heat to the recirculated liquid of the boiling chamber. Valve VP10, during startup phase, is open in purchase to allow a gradual startup of the blower K01.

Enthusiast K02 permits to maintain controlled the temperature of the oil in the blower in get to prolong its provider life in circumstance of operation in thermally difficult situations.

3 Thermal recovery systems

Thermal recovery is realised by means of the exchangers E03 (if the optional technique V is put in) and E02. The liquid to be dealt with crosses each of them and warms up before getting into the boiling chamber. Temperature sensor TE08 actions the temperature of the liquid to be dealt with moving into the boiler following the restoration exchangers.

The concentrate passes through the tube and shell warmth exchanger E03 and cools down, just before its discharging, as a consequence of the warmth exchange with the liquid to be dealt with. Valve VP03 (if the optional system V is put in) allows the flow of the liquid to be treated through exchanger E03. The distillate enters the plate heat exchanger E02 and cools down, just before its discharging, as a consequence of the heat exchange with the liquid to be handled.

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

4 Auxiliary liquids

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

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

Tap h2o, for washing of parts inside of the boiling chamber D01, via 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 installed.

Bactericide metering in the shipping pipeline of distillate discharge pump, if the optional method AM BT D is installed.

Comparison Among MVR and four-impact Evaporator


four-effect Evaporator



CZPT-conserving, vaporizing 1 ton water consumes .three ton refreshing steam.

A lot more energy-conserving,vaporizing one ton water consumes 30kw*h electricity


Clean steam

CZPT electric power





CZPT procedure period with even bigger temperature variance has an effect on toughness.

Shorter process period with low temperature increases durability.

Output Kind





one. it is a flip essential whole set products,straightforward tools, considerably less employee,less location,much less value.

two. can generate 1000L-1000000L 96%-99.nine% alcohol(ethanol) for each day.

3. can use Corn, wheat, cassava, molasses,rice,potato, day,beetroot ,sugar cane ect which is made up of starch or sugar substance.

four. we can do the switch essential method or area part.

five. Can boost and rebuild old alcohol(ethanol) generation line .

You can pick single distill tower to conserve cash, also can decide on five distill column to get great quality alcohol/ethanol.

5-Column Three-Result Distillation Method
Our firm types and manufactures latestFive-Column Three-Effect Distillation gear.This new procedure is promoted on the basis of traditional five-column differential-stress column and mainly used for super-fine alcoholic beverages production.
The crucial of this method is the heating strategies,the steam heats one particular column directly and transfers theheat to other 4 columnsto obtain a few-result thermal coupling and strength-conserving effects.
In conditions of electricityefficiency, it can save 50% electricity and keep away from the repairing of circulating pumps and also increase the doing work existence of there-boilers.

Double-Mash-Column Three-Influence Distillation Method
This process applies to the creation of standard-quality liquor& gas ethanol, and it was awarded Chinese national patent, it is the onlysuccessfulapplicationof double mash column & 3-effect in the globe,which generates basic-quality liquor.
This process is composed by mash column, rectification column and composite column. The composite column capabilities as mash column and rectification column.
The crucial of this process is the heating approaches: the steam heats a single column immediately and transfers the warmth to other 2 columns to achieve a few-result thermal coupling and strength-conserving consequences.
The edge of this approach is power-savingit saves above forty% steam.

Generation Ability

1,Our company was set up in the nineteen fifties, created and made the initial stainless metal distillation column in China.

two,Our company can generate 6 total sets of gear (like crushing part, liquefying saccharification section, fermentation segment, distillation area and DDGS area) in a month.

three,Amongst 16 production workshops,three workshops are for mechanic manufacture, 5 workshops arefor manufacturing process, 8 workshops are for assembling & welding.

four,We own innovative machining gear and item testing tools.

Developed capacity

1). We own Style License of Special CZPT D1 & D2 Class CZPT License of Particular CZPT A2 Course Design License of Specific CZPT GC Class.

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

three). Our organization owns ASME certification, ISO 9001 CZPT Technique Certification, ISO 14001 CZPTal Management Technique Certification & GB/T28001 Occupational Overall health and Security Management Technique Certification

Right after-revenue Support

one).Our organization can offer a sophisticated item after-sale support and can guarantee the implementation, servicing and fee of assignments.

two). We can get to the project site soon after receiving the user’s notification.

Deal & Transport

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

Contact us

Identify:  Vick Liang
Email:   [email protected]
Tel:       86~thirteen 0571 88828 13858117778953842508
Telephone:  86-538-3393266
Fax:       86-538-3399066
Skype:   vicklwk
QQ:        496443614
Handle: HangZhou Large-tech CZPT Zone, HangZhou, ZheJiang , China

Mvr Citric Acid Evaporator