Dynamic Disk Microreactor
Features:
• Internal high-shear structure with high-speed impeller ensures uniform mixing of materials and high product stability;
• Suitable for viscous liquids and reactions involving or generating solid phases, capable of handling suspensions with highly efficient mixing, enabling formation of micro- and nano-particles to enhance reaction efficiency and prevent clogging.
Description:
Disc-type microreactors utilize high-speed rotation to generate a stable and easily controllable centrifugal force field, overcoming the limitations imposed by conventional gravitational fields on mass transfer rates and simulating a hypergravity environment. They are used to enhance molecular diffusion and interphase mass transfer between molecules of different sizes. The gap between the stationary outer shell and the high-speed rotating disc is only 0.5–2 mm. Under a gravitational field 100 times stronger than Earth’s and under the influence of immense shear forces, gas-liquid, liquid-liquid, and liquid-solid mixtures are torn into nanoscale films, filaments, and droplets. This rapidly renews the interfacial surfaces, enabling highly efficient mass transfer at the microscopic level.

Product Details:
| Material States Accommodated | Gas-Liquid-Solid Three-Phase |
| Main Material | Stainless Steel 316L (Other options: Silicon Carbide, Hastelloy, C4, PTFE, etc.) |
| Channel Liquid Hold-Up (ml) | 600 |
| Process Throughput (ml/min) | 1600-16000 |
| Solid Content Compatibility (%) | 0-40% |
| Annual Processing Capacity (t/year) (24-hour operation) |
8000 |
| Working Temperature (℃) | -70~200℃ (Customizable up to 300℃) |
| Working Pressure (MPa) | 2 MPa (Adjustable per customer process requirements) |
| Sealing Type | Magnetic Seal |
| Heat Exchange Method | Internal and External Jackets |
Application:
| 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. |
Advantages:

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