Product

Rising Membrane Evaporator

Overview

The rising membrane evaporator is structured such that liquid enters the heating tubes via the principle of a siphon pump for heating. After flowing into the separator, the liquid is separated from the vapor, then returns to the evaporator through a circulation pipe, forming a closed-loop cycle. Therefore, this type of evaporator is also known as an external circulation evaporator. The heating tubes are composed of heat exchange tubes. After the raw material liquid is preheated to its boiling point or near the boiling point, it is introduced from the bottom of the heating chamber. Driven by the high-speed rising secondary vapor, the liquid flows along the inner wall of the heat exchange tubes while evaporating. The required concentration is achieved at the top of the heating chamber, and the finished liquid is discharged from the bottom of the separation chamber. The generated secondary vapor passes through the separation plate group set at the upper part to remove bubbles, water droplets, and impurities, becoming the heat source for the next effect.

 

The rising membrane evaporator is suitable for processing solutions with large evaporation capacity, thermal sensitivity, low viscosity, and easy foaming. However, it is not suitable for solutions with high viscosity, crystal precipitation, or easy scaling. It is applicable to the evaporation of substances with large evaporation capacity, thermal sensitivity, viscosity, and foaming properties. Due to the extremely short residence time in single-pass operation, it can be used as a high-concentration evaporator.

Main Characteristics

  1. High-degree liquid turbulence – To overcome the influence of gravity and move upward, the rising membrane evaporator is thus suitable for high-viscosity products and those prone to scaling on heating surfaces.
  2. Stable and efficient operation – Enabled by product circulation under broad operational conditions.
  3. Material flow process – The material enters the heating tubes uniformly from the bottom of the evaporator through a preheater, and is heated by the steam outside the tubes. Inside the tank, the material boils and vaporizes rapidly, forming a steam column in the middle of the heating tubes. The steam density decreases sharply, causing the steam to rise at high speed within the tubes. The liquid material is driven by the ascending steam, forming a thin film along the tube wall and rising rapidly while continuing to evaporate. The gas-liquid two phases are separated in the gas-liquid separator, and the material is concentrated. If the material concentration is insufficient after one evaporation, the material outlet can be connected in parallel with the heater inlet for partial reflux until the finished material meets the required concentration. The operation can adopt atmospheric pressure or vacuum conditions.

Technical Parameters Table

Specification Model SMNS-8 SMNS-12 SMNS-16 SMNS30
Heating Area (㎡) 8 12 16 30
Preheating Area (㎡) 6 8 10 20
Evaporation Capacity (kg/h) 550 850 1100 2000
Steam Pressure (MPa) 0.25 – 0.30
Condensation Area (㎡) 15 20 25 50

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