Static Plate Type Microreactor 
Static Plate Type Microreactor 

Static Plate Type Microreactor 

Internal heart-shaped flow channels enable efficient laminar diffusion through multiple segmentation and recombination, making it particularly suitable for reactions such as nitration, sulfonation, and polymerization;
Ideal for rapid liquid-liquid and gas-liquid reactions with low liquid hold-up, ensuring inherent safety;
Micron-scale flow channels combined with temperature and pressure control achieve high-efficiency mass and heat transfer.

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A plate-type microchannel reactor is a continuous reaction device that achieves efficient mass and heat transfer and is intrinsically safe through its narrow flow channel design. Plate-type reactors are commonly used for liquid-phase or gas-liquid-phase reactions. Their distinctive feature lies in the design of their internal flow channels: heart-shaped channels enable multiple divisions and reorganizations of the material, facilitating efficient laminar diffusion and making them particularly suitable for fast reactions such as nitration, sulfonation, and polymerization; diamond-shaped channels enhance turbulence intensity, making them suitable for high-viscosity materials; and T/Y-shaped channels are suitable for reactions such as the preparation of nanoparticles that form precipitates.

Material States Accommodated Gas-Liquid Two-Phase
Main Material Stainless Steel 316L (Other options: Silicon Carbide, Hastelloy, C4, PTFE, etc.)
Channel Liquid Hold-Up (ml) 20
Annual Processing Capacity (t/year) (24-hour operation) 100
Working Temperature (℃) -70~200℃ (Customizable up to 300℃)
Working Pressure (MPa) 2 MPa (Adjustable per customer process requirements)
Sealing Type Static Seal
Heat Exchange Method Internal and External Jackets

 

Reaction Type Examples of Reactions Advantages of Microcanal Reactors
Bromination Methyl Bromination Excellent control over the monobromination ratio
Addition to Double Bonds Virtually quantitative reaction
Hydroxyl Bromination Excellent control over isomerization impurities
Chlorination Alkane Chlorination Higher selectivity than conventional reactors
Benzyl Chlorination Higher selectivity than conventional reactors
Heterocyclic Chlorination Higher selectivity than conventional reactors
Nitration Nitration of Alcohols and Amines Significant reduction in oxidation impurities
Nitration of Benzene Rings and Heterocycles Excellent control over dinitration and oxidation impurities
Low-temperature reaction Low-Temperature Halogenation and Addition No cryogenic cooling required; significantly improved yield
Low-Temperature Dechlorination and Addition No cryogenic cooling required; very rapid reaction with high yield
Hydrogenation Hydrogenation of Double Bonds Effectively reduces over-reduction and polymerization impurities
Deprotection The reaction is fast, selectively deprotecting without reducing other easily reducible groups
Reduction of Alkynes Can selectively reduce to alkenes
Reduction of Carbonyl Groups Reduced catalyst consumption and increased number of reuses
Oxidation Oxidation of Hydroxyl Groups High selectivity with reduced other impurities
Oxidation of Methylene Groups to Ketones Selective oxidation of the α-methylene group in alkenes, offering higher selectivity and safety
Oxidation of Alkenes to Diols Significant increase in selectivity
Oxidative Elimination Reactions Allows the use of low-boiling-point, easily recoverable solvents with nearly quantitative conversion
Other Michael Addition Reactions Increased selectivity and reduced polymerization
Proton-Catalyzed Cyclization Reduced dimerization and isomerization, with a significant increase in yield
Suzuki Coupling Increased yield
Coupling of Azo Compounds Reduced azo decomposition, with yields potentially reaching 100%

 

Industry Reaction Type Reaction Materials Involved in Continuous Applications
Pharmaceuticals and Intermediates Nitration Solvents: nitric acid, acetic acid, dichloromethane, dichloroethane, acetic acid, acetic anhydride
Dichloroethane, etc.
Nitrating agents: fuming nitric acid, sulfuric acid, dinitrogen pentoxide
Pesticides and Intermediates Diazonation Phenylhydrazine, sodium nitrite, hydrochloric acid, sulfuric acid, methylpyridine, solid-liquid reactions
New Materials Oxidation Phosphotungstic acid, hydrogen peroxide, sodium hypochlorite, oxidation of hydroxyl groups, oxidation of methylene groups to ketones
Oxidation of alkenes to diols, oxidative elimination reactions
New Energy Bromination Methyl bromination, addition to double bonds, hydroxyl bromination
Dyes and Pigments Chlorination Alkanes, benzyl groups, chlorine gas, chlorination of heterocycles
Flavors and Fragrances Hydrogenation Hydrogenation of double bonds, deprotection, reduction of alkenes, reduction of carbon groups
Defense Industry Alkylation Methanol, ethanol, propanol, butanol, acetic acid, propionic acid, halides
Fine Chemicals Halogenation Chlorobenzene, bromoacrylonitrile, iodoethanol
Nanomaterials Fluorination Fluoroethylene, fluoroacetone, fluoroaniline, fluoroacetic acid
Cosmetics Industry Esterification Esterification reactions of fatty acids and polyols such as pentaerythritol; ethyl acetate, butyl propionate
Sulfonation Benzene, ethanol, n-butane, concentrated sulfuric acid, or fuming nitric acid
Grignard reaction Reaction of bromoethane with magnesium to produce ethyl Grignard reagent
Solid-liquid reaction Nitromethane, iron phosphate production, IVD microsphere preparation, pharmaceutical microsphere preparation
Gas-liquid reaction Oxidation reactions, hydrogenation reactions, etc.
Technical Advantages User Benefits
High mass and heat transfer efficiency; excellent mixing performance High product yield and high production efficiency
Precise process control, online monitoring, modular design, and automation Short production cycles and rapid scale-up
Minimized side reactions; micron-scale channel design High product purity and high selectivity
Small reaction volume; low liquid holding capacity Compact footprint and intrinsically safe
Maximum pressure resistance of 40 MPa; corrosion resistance (silicon carbide/Hastelloy) Suitable for hazardous processes such as nitration and chlorination
Low energy consumption; minimal catalyst usage Low total investment and low operating costs
Minimal waste (solid, liquid, and gas); low liquid holding capacity Compliant with environmental regulations and low safety risks
Minimal scaling-up effects; rapid process validation Rapid commercialization and reduced R&D costs
High-temperature resistance, diverse material options (316L, Hastelloy, etc.) Covers fields such as pharmaceuticals and electronic chemicals
Long catalyst lifespan, high system stability Optimized long-term operating costs

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