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What Is an Evaporation Reactor? Principles, Types & Applications

What Is an Evaporation Reactor? Principles, Types & Applications

MOQ: 1 Sets
Price: 10000 USD
Delivery Period: 2 months
Payment Method: L/C,T/T
Supply Capacity: 200 sets / days
Detail Information
Place of Origin
China
Brand Name
Center Enamel
Certification
ASME,ISO 9001,CE, NSF/ANSI 61, WRAS, ISO 28765, LFGB, BSCI, ISO 45001
Material:
Stainless Steel, Carbon Steel
Size:
Customized
Design Pressure:
0.1-10 Mpa
Applications:
Chemical, Food Processing, Beverage Processing, Brewing, Metallurgy, Oil Refining, Pharmaceuticals
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Product Description

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:

  • Temperature Driving Force and Heat Transfer The rate of evaporation is proportional to the product of the overall heat transfer coefficient (U), heat transfer area (A), and logarithmic mean temperature difference (LMTD) between heating medium and process fluid: Q = U x A x delta-T_lm. Falling film evaporators achieve U-values of 1200-2000 W/m2-K due to thin liquid film formation (0.1-0.5 mm), while forced circulation types achieve 800-1200 W/m2-K.
  • Vapor-Liquid Separation and Entrainment Control Vapor generated in the heating section enters a separation vessel where droplet entrainment is controlled by demister pads, centrifugal separators, or tangential inlet design. The Duhring rule correlates boiling point elevation with concentration: a 50% NaOH solution exhibits a boiling point rise of 43C above pure water at atmospheric pressure, directly affecting the available temperature driving force.
  • Multiple-Effect Energy Integration Vapor from the first effect (effect 1) serves as the heating medium for effect 2 at lower pressure, and so on through 3-7 effects. Each subsequent effect operates at a 20-40C lower temperature, achieving a steam economy of 0.85-0.95 for single-effect, 1.8-2.0 for double-effect, and 3.5-4.0 for triple-effect evaporation, dramatically reducing energy consumption per kilogram of water evaporated.

2. Major Types of Evaporation Reactors

Industrial evaporation reactors are categorized by liquid flow pattern and mechanical design:

  • Falling Film Evaporator Reactor Liquid is distributed as a thin film (0.1-0.5 mm) on the interior surface of vertical tubes (6-12 m length, 30-50 mm diameter) and flows downward by gravity. Residence time is extremely short (5-30 seconds), making it ideal for heat-sensitive products such as fruit juices, milk concentrates, and pharmaceutical extracts. Achieves U-values of 1200-2000 W/m2-K and handles viscosities up to 100 cP.
  • Wiped Film (Agitated Thin Film) Evaporator A rotating wiper blade system (tip speed 4-12 m/s) spreads liquid into a thin turbulent film on the heated wall, enabling processing of highly viscous (100-100,000 cP), fouling, or crystallizing materials. Typical U-values are 800-1500 W/m2-K, with residence times of 10-60 seconds. Standard in glycerol recovery, polymer devolatilization, and spent-oil re-refining.
  • Forced Circulation Evaporator A circulation pump (flow velocity 1.5-3.0 m/s through the heating tubes) prevents tube boiling and suppresses fouling by maintaining the process fluid above its boiling point under pressure, flashing in the separator. Suitable for scaling, crystallizing, and high-solids solutions such as salt brine concentration and wastewater ZLD systems, with U-values of 800-1200 W/m2-K.

Evaporation Reactor Types Comparison Matrix

Evaporator TypeHeat Transfer MechanismOperating ParametersBest-Suited Application
Falling FilmThin gravity film on tube wallU: 1200-2000 W/m2-K, 50-150C, 0.01-0.1 MPa, viscosity <100 cPHeat-sensitive products: fruit juice, dairy, pharma extracts
Wiped FilmMechanical wiper creates turbulent filmU: 800-1500 W/m2-K, 50-200C, high vacuum 0.001 MPa, viscosity up to 100,000 cPViscous, fouling, or crystallizing: glycerol, polymer, spent oil
Forced CirculationPumped flow prevents tube boilingU: 800-1200 W/m2-K, 80-150C, 0.1-0.5 MPa, velocity 1.5-3 m/sScaling/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.