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MVR Evaporation and Crystallization Unit

MVR蒸发结晶装置通过回收二次蒸汽潜热实现能量循环利用,相比传统多效蒸发节能50%以上,无需外供生蒸汽即可运行,是实现高盐废水零排放和资源回收的核心装备。


National Service Hotline:400-611-6861
Technical Advantage
Ultimate Energy Efficiency
The electricity consumption for ton water evaporation is 25-40 kWh, and the steam consumption is ≤ 150 kg/ton water, which saves more than 50% energy compared to three effect evaporation.
No waste heat emissions
The secondary steam is fully recovered and utilized, without the need for circulating cooling water, reducing the load on the cooling tower.
low-temperature evaporation
Evaporation temperature of 40-80 ℃, suitable for heat sensitive materials, not easily denatured.
High degree of automation
PLC fully automatic control, integrated remote monitoring and interlocking protection.
Process Selection

Material Properties  Process Impact  Mitigation Measures

High viscosity/Prone to scaling  

High flow resistance, susceptible to pipe blockage and wall buildup  

Select forced circulation evaporator, with a tube flow velocity of 1.5-3 m/s

Thermosensitive  

Prone to decomposition/degredation at high temperatures  

Opt for low-temperature evaporation (≤80°C) and short dwell time

High chloride (>500ppm) High corrosion resistance Flow components selected as TA2 titanium alloy/2205 duplex stainless steel

The boiling point elevation is significant. The compressor temperature rise must cover the required range. Sodium gluconate requires a temperature rise of 18-20°C


Equipment Selection

1. Selection of evaporator type


type


Applicable working conditions


characteristic


Forced circulation evaporator


Working conditions with high viscosity, easy scaling, and containing crystalline particles


High flow rate (1.5-3m/s), anti blocking and anti scaling, wide applicability


falling film evaporator


Low viscosity, heat sensitivity, and no crystallization conditions


High heat transfer coefficient, short residence time, suitable for thermosensitive materials


OSLO/DTB crystallizer


Operating conditions requiring control of crystal particle size


Crystal uniformity, high purity, suitable for crystallization needs


 


2. Material selection


Material Type


Applicable scenarios


core advantage


316L stainless steel


Low chlorine environment (<200ppm)


Corrosion resistance, moderate cost, suitable for conventional working conditions


Duplex stainless steel 2205/2507


Conventional high salt scenario, chloride ion<0.5g/L


Resistant to pitting corrosion, suitable for most industrial high salt wastewater


Titanium alloy TA2


Chloride ion>500ppm or high temperature acidic working conditions


Resistant to strong corrosion and suitable for extreme high chlorine environments


Hastelloy C-276


Extreme corrosive environments such as cyanide and strong acids


Resistant to strong corrosion and suitable for various extremely complex working conditions


3. Compressor selection


compressor type


Applicable temperature rise


characteristic


Roots compressor


8-15℃


Simple structure, suitable for materials with low boiling point rise, moderate cost


Centrifugal compressor


12-25℃


High efficiency, stable operation, suitable for most industrial wastewater scenarios


Multi stage series compressor


>25℃


Suitable for high boiling point materials, with high investment but stable operation


Material supplement


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The material of the compressor should match the working conditions, and carbon steel with nickel plating or duplex steel should be preferred


4. Auxiliary equipment


Circulating pump: high flow, low head axial flow pump, variable frequency regulation.


Solid liquid separation: Separation of crystalline salts using a centrifuge or vacuum belt filter.


Drying system: Airflow drying/disc dryer to ensure product moisture content<0.5%.


Automation system: PLC/DCS+online cleaning (CIP), fault interlock protection.