Tower Reactor

A tower reactor is a vertical cylindrical chemical reactor widely used in industries such as chemical manufacturing, petroleum refining, pharmaceuticals, and environmental engineering. It is designed for efficient multiphase reactions (gas-liquid, liquid-liquid, or gas-liquid-solid), and its internal components include packing, trays, distributors, and demisters to enhance mass transfer and reaction efficiency. Tower reactors include a variety of types, such as packed bed reactors, bubble column reactors, airlift reactors, tray reactors, and fluidized bed reactors, each of which is tailored for specific reactions and flow characteristics. Equipped with an integrated temperature control system and flexible operating modes (continuous or intermittent), tower reactors are highly adaptable and have efficient heat and mass transfer capabilities, making them ideal for large-scale or complex reaction systems. Its design requires careful consideration of reaction kinetics, mass and heat transfer, fluid dynamics, and material compatibility to ensure optimal performance, safety, and scalability in industrial applications.


Equipment type Classification method Features Application scenario
Gas-liquid reaction tower Classification by reaction type Mainly used for chemical reactions between gas and liquid phases. Usually packing or trays are set in the tower to increase the gas-liquid contact area and promote mass transfer and reaction. For example, in an absorption tower, some components in the gas are absorbed by the liquid and undergo chemical reactions; in the shift reaction of synthetic ammonia, carbon monoxide reacts with water vapor under the action of a catalyst to produce hydrogen and carbon dioxide.
Gas-solid reaction tower Classified by reaction type Mainly used for chemical reactions between gas and solid phases. Solid particles usually exist in the form of a fixed bed or a fluidized bed, and the gas reacts when passing through the solid particle layer. For example, in a synthetic tower for synthetic ammonia, hydrogen and nitrogen react under the action of a catalyst to produce ammonia; in some waste gas treatment processes, harmful components in the gas react with solid adsorbents or catalysts.
Liquid-liquid reaction tower Classification by reaction type Mainly used for chemical reactions between liquid and liquid phases. By setting up a dispersion device (such as a nozzle, filler, etc.) in the tower, the two immiscible liquids can fully contact and react. For example, in some organic synthesis processes, reactants in two organic solvents react with each other to generate the target product.
Packed tower Classification by tower structure The tower is filled with packing, which has a large specific surface area and high porosity, and can provide a large amount of gas-liquid contact area to promote mass transfer and reaction. There are various types of packing, such as Raschig rings, Pall rings, corrugated packing, etc. It is widely used in absorption, distillation, gas-liquid reaction and other processes. For example, in sulfuric acid production, sulfur dioxide is absorbed by water in the packed tower to generate sulfurous acid.
Plate tower Classification by tower structure The tower is equipped with a plate, on which a liquid back-mixing device (such as a downcomer, overflow weir, etc.) is provided, and mass transfer and reaction are achieved through gas-liquid contact on the plate. Types of plate towers include sieve plate towers, float valve towers, bubble cap towers, etc. Commonly used in distillation, absorption and other processes. For example, in the process of petroleum distillation, plate towers are used to separate different fractions in crude oil.
Spray tower Classification by tower structure The liquid is sprayed into the tower through the nozzle to form droplets or mist, which fully contacts the gas to achieve mass transfer and reaction. The spray tower has high mass transfer efficiency, but requires a higher liquid injection pressure. Applicable to gas-liquid reaction and absorption processes, such as in some waste gas treatment processes, liquid absorbent is sprayed into the tower through the nozzle to absorb harmful components in the waste gas.
Absorption tower Classification by reaction process Mainly used in the process where certain components in the gas are absorbed by the liquid. The gas-liquid contact area is increased by fillers or plates in the tower, so that the solute in the gas is dissolved in the liquid and a chemical reaction may occur. For example, in waste gas treatment, alkaline liquid is used to absorb acidic gases (such as sulfur dioxide, hydrogen chloride, etc.) in the waste gas; in the production of synthetic ammonia, methanol is used to absorb carbon dioxide.
Distillation tower Classification by reaction process It is mainly used to separate liquid mixtures into components of different purities. Through multiple vaporization and condensation, the separation is achieved by taking advantage of the different volatilities of each component. The distillation tower can be a packed tower or a plate tower. It is widely used to separate mixtures in the fields of petrochemicals, fine chemicals, etc. For example, crude oil is separated into different fractions such as gasoline, kerosene, and diesel.
Catalytic tower Classification by reaction process The tower is filled with catalysts to accelerate the chemical reaction. The catalyst can be in the form of a fixed bed or a fluidized bed. The catalytic tower usually needs to control the reaction conditions such as temperature and pressure. For example, in the synthetic ammonia synthesis tower, hydrogen and nitrogen react to generate ammonia under the action of the catalyst; in the gasoline hydrorefining process, the catalytic tower is used to remove impurities such as sulfides in gasoline.
Oxidation tower Classification by reaction process Mainly used for oxidation reaction, usually oxygen or air is introduced into the tower to make the reactants undergo oxidation reaction. The oxidation tower can be a packed tower or a plate tower. For example, in the process of producing ethylene oxide, ethylene is oxidized in the oxidation tower to produce ethylene oxide.
Reduction tower Classification by reaction process Mainly used for reduction reaction, usually a reducing agent (such as hydrogen, carbon monoxide, etc.) is introduced into the tower to make the reactants undergo reduction reaction. The structure of the reduction tower is similar to that of the oxidation tower. For example, in some metal smelting processes, hydrogen is used to reduce metal oxides.
Continuous operation tower Classification by operation mode The material enters the tower continuously, the reaction proceeds continuously, and the product is discharged continuously. The continuous operation tower has high production efficiency and is suitable for large-scale production. Such as petroleum distillation tower, synthetic ammonia synthesis tower, etc.
Intermittent operation tower Classified by operation method The materials enter the tower in batches, and the products are discharged in batches after the reaction is completed. Intermittent operation towers are highly flexible and suitable for small-scale production or processes with large changes in reaction conditions. Such as some fine chemical reaction towers, laboratory reaction towers, etc.

References Authors Abstract DOI
Study on Heat Transfer Characteristics of Stirred Tower Reactor Sun Jianzhong, Wang Dechong, Pan Zuren The heat transfer characteristics of multi-stage cooling coil baffles in a stirred tower reactor (SCR) were analyzed and experimentally studied using steady-state and unsteady-state heat transfer methods. A correlation formula for the heat transfer film coefficient on the baffle surface of the SCR multi-stage cooling coil is proposed, which takes into account the influence of both the stirring Reynolds number and the axial liquid flow Reynolds number. The results show that the influence of the axial liquid Heinz coefficient on the heat transfer film coefficient on the baffle surface of the SCR cooling coil is as important as the influence of the stirring Reynolds number. 10.3321/j.issn:1003-9015.2000.01.016
Design and research of spiral upflow tower photocatalytic reactor Ji Fangying, Xu Xuan, Fan Zihong, He Li A spiral upflow tower photocatalytic reactor was designed by adopting the cyclone separation model of particle pollutants, which improved the recovery rate of photocatalyst in the suspended photocatalytic reaction system. The reactor adopts a tower structure, which can effectively improve the ratio of the illumination area to the reaction liquid volume (A/V value) of the reactor. Under experimental conditions, the A/V value can reach 12.95. The reactor was used to treat nitrobenzene simulated wastewater. When the initial concentration of nitrobenzene was 466 mg/L, the removal rate of nitrobenzene in the reactor was stabilized at around 60%, and the recovery rate of the photocatalyst was 92.80% after 12 h of operation. 110.3321/j.issn:1000-4602.2009.23.023
Study on the treatment of nitrite in surface water using tower reactor Wang Liucheng, Xu Haisheng, Song Chengying, Zhao Jianhong The process conditions of ozone oxidation of nitrite in surface water in a tower reactor were studied, and the optimal process conditions for treating surface water with a nitrite nitrogen content of 0.21 mg/L to meet the "Surface Water Environmental Quality Standard" I, II, and III water were obtained. The study shows that the process is not affected by water temperature, has good stability, simple equipment, and low treatment cost. CNKI:SUN:HJJZ.0.2003-09-024
Bipolar Trickle Tower Reactor: Concept, Development, and Applications Frank C. Walsh, Luis F. Arenas, Carlos Ponce de León This paper introduces the concept of a drip tower using ordered bipolar electrode elements stacked into (10 to 80) similar porous 3D electrode layers separated by insulating spacers, and reviews the main features of electrochemical reactors based on the bipolar trickle tower reactor (BTTR) geometry. Fluid flow, mass transfer, active area, and bypass currents are considered in detail as they affect the reaction environment. Reactor design has been improved during electrode selection and tower construction. This paper illustrates the performance of BTTRs, including electrosynthesis and environmental treatment, using laboratory and industrial examples. Experimental data are used to rationalize the reaction environment and simulate performance. Operating factors such as electrolyte flow, mass transfer rate, and volumetric electrode area are emphasized as important factors in achieving high efficiency; minimizing internal bypass currents is critical. Developments have led to improved reactor architecture and a wider range of electrode material choices. 10.1149/1945-7111/abdd7a

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