| MOQ: | 1 Sets |
| Price: | 10000 USD |
| Delivery Period: | 2 months |
| Payment Method: | L/C,T/T |
| Supply Capacity: | 200 sets / days |
What Is an Evaporation Reactor? Principles, Types & Applications
Answering the core question: What is an evaporation reactor, and how does it concentrate process streams through controlled solvent removal? An evaporation reactor is a heat-driven separation vessel that removes volatile solvents (typically water or organic solvents) from liquid process streams by applying thermal energy to vaporize the solvent while retaining concentrated non-volatile products. These reactors achieve overall heat transfer coefficients (U-values) of 500-2000 W/m2-K, concentration factors of 5-10x, and operate across temperatures from 50C (vacuum evaporation) to 180C (atmospheric). Common configurations include falling film, rising film, and wiped film evaporators, each optimized for viscosity ranges from 1 cP to over 100,000 cP in food, pharmaceutical, chemical, and wastewater treatment applications.
1. Core Operating Principles of Evaporation Reactors
Evaporation reactor performance is governed by three heat transfer and mass transfer principles:
2. Major Types of Evaporation Reactors
Industrial evaporation reactors are categorized by liquid flow pattern and mechanical design:
Evaporation Reactor Types Comparison Matrix
| Evaporator Type | Heat Transfer Mechanism | Operating Parameters | Best-Suited Application |
|---|---|---|---|
| Falling Film | Thin gravity film on tube wall | U: 1200-2000 W/m2-K, 50-150C, 0.01-0.1 MPa, viscosity <100 cP | Heat-sensitive products: fruit juice, dairy, pharma extracts |
| Wiped Film | Mechanical wiper creates turbulent film | U: 800-1500 W/m2-K, 50-200C, high vacuum 0.001 MPa, viscosity up to 100,000 cP | Viscous, fouling, or crystallizing: glycerol, polymer, spent oil |
| Forced Circulation | Pumped flow prevents tube boiling | U: 800-1200 W/m2-K, 80-150C, 0.1-0.5 MPa, velocity 1.5-3 m/s | Scaling/crystallizing: salt brine, wastewater ZLD, caustic |
Frequently Asked Questions (FAQ)
Q: What is the overall heat transfer coefficient in a falling film evaporation reactor?
A: Falling film evaporators typically achieve U-values of 1200-2000 W/m2-K, the highest among evaporation reactor types. This is because the thin liquid film (0.1-0.5 mm) on the tube wall creates minimal thermal resistance, and the high surface renewal rate from gravity-driven flow enhances convective heat transfer. For comparison, forced circulation evaporators achieve 800-1200 W/m2-K.
Q: How does multiple-effect evaporation improve energy efficiency?
A: In multiple-effect evaporation, vapor from the first effect serves as heating medium for the second effect at lower pressure, and so on through 3-7 effects. A triple-effect system achieves a steam economy of 3.5-4.0 (3.5-4.0 kg water evaporated per kg steam consumed), compared to 0.85-0.95 for single-effect. Each subsequent effect operates 20-40C lower, with the final effect typically under vacuum at 50-60C.
Q: What is the Duhring rule and why does it matter for evaporation reactor design?
A: The Duhring rule states that the boiling point of a solution at one pressure is a linear function of the boiling point of the pure solvent at another pressure. It is used to calculate boiling point elevation (BPE), which reduces the available temperature driving force. For example, a 50% NaOH solution has a BPE of 43C at atmospheric pressure, meaning the reactor must supply 43C of additional thermal energy beyond pure-water evaporation, directly impacting heating area sizing and energy consumption.
Q: Which evaporation reactor type is best for highly viscous or fouling products?
A: Wiped film (agitated thin film) evaporators are the preferred choice for viscosities of 100-100,000 cP and fouling-prone materials. The rotating wiper blades (tip speed 4-12 m/s) continuously renew the heated surface, prevent thermal degradation through short residence times (10-60 seconds), and handle materials that would block falling film distributors or scale forced circulation tubes.