Thread Content
Industrial-grade practical composite material microchannel continuous reactors (as opposed to the expensive silicon carbide microchannels that become clogged and are thus unusable after that): Feature 1: Resistant to clogging: The reaction modules can be disassembled and reassembled. Powdered catalysts and slightly soluble reactants can be used. It has a wide range of adaptability, and blockages do not cause significant losses. It overcomes the drawback of being unable to use solid catalysts, as well as solid reactants and products, after bonding in silicon carbide reactors. 2: Economically durable with a long warranty period. (The warranty for silicon carbide microchannels is only one year, as their after-sales costs are high) Our warranty can last up to five years. It can be used with confidence. 3 composite modules: corresponding corrosion-resistant materials are used depending on the manufacturing process to ensure absolute corrosion resistance. (Silicon carbide-bonded microchannels cannot be used with hydrofluoric acid); for hydrofluoric acid, we use composite materials with excellent corrosion resistance and high thermal conductivity… So don’t rely too much on foreign products – domestic microchannels are inexpensive, practical, and durable. Jiangsu Caihu (15861244688) – feel free to ask for details. The first batch of hazardous processes includes: phosgene and phosgenation processes, electrolysis processes (chlor-alkali), chlorination processes, nitration processes, ammonia synthesis processes, cracking processes, fluorination processes, hydrogenation processes, diazotization processes, oxidation processes, peroxidation processes, amination processes, sulfonation processes, polymerization processes, and alkylation processes. Group 2 of hazardous processes: new coal chemical processes [coal-to-oil processes (methanol-to-gasoline, Fischer-Tropsch oil synthesis), coal-to-olefins via methanol, coal-to-dimethyl ether, coal-to-ethylene glycol (syngas-based ethylene glycol production), coal-to-methane gas (coal gas methanization), coal-to-methanol, methanol-to-acetic acid, etc.], calcium carbide production process, and azidation process. Note: The aforementioned process principles require the use of microchannel reactors to replace conventional reaction vessels. If microchannel reactors cannot be used (for example, due to excessively long reaction times or because they are not suitable for industrial production), a thermal reaction assessment and classification must be conducted as evidence.