200M Window Reactor

The reactor primarily consists of a vessel, agitator, heat transfer system, sealing mechanism, and control system, and is suitable for high‑temperature, high‑pressure chemical reactions. Its operating principle involves the polymerization of olefin monomers under the action of initiators and catalysts, with reaction temperature and efficiency controlled via agitation and heat transfer devices. Depending on the operating mode and polymerization process, reactors are classified into batch and continuous types, as well as gas‑phase, bulk liquid‑phase, and solution polymerization varieties. The equipment must meet requirements for efficient production, stable product quality, and operational safety.

Classification:

High‑pressure reactor

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Telephone:

400-920-1718

Product Description

Structure: It typically consists of a reactor vessel, a stirring device, a heat transfer system, a sealing mechanism, and a control system. The reactor vessel is the site of the reaction and is generally made from high‑strength stainless steel or other corrosion‑resistant materials to withstand the high temperatures, high pressures, and chemical corrosion encountered during the reaction process. The stirring device ensures thorough mixing of the reactants, enhances mass and heat transfer, and guarantees that the reaction proceeds uniformly. The heat transfer system is used to control the reaction temperature; common designs include jacketed systems and coil‑type systems, which regulate the temperature inside the reactor by circulating heating or cooling media. The sealing mechanism prevents leakage of reactants and ensures that the reaction takes place in a closed environment. The control system monitors and regulates various reaction parameters—such as temperature, pressure, and stirring speed—to ensure that the reaction proceeds safely and stably.
Working principle: In the olefin polymerization reactor, olefin monomers undergo a polymerization reaction under the influence of initiators, catalysts, and other agents. The initiator decomposes to generate free radicals or ionic active centers, which trigger chain‑growing polymerization reactions in the olefin monomers, causing the monomer molecules to continuously link together and form long-chain polymers. A large amount of heat is released during the reaction, which must be promptly removed via a heat transfer system to maintain the reaction temperature within an appropriate range. At the same time, the stirring device ensures thorough contact between the catalyst and the monomers, thereby enhancing reaction efficiency and improving the uniformity of the polymer.
Type
According to the operating method: They can be divided into batch reactors and continuous reactors. Batch reactors are suitable for small‑batch, multi‑variety production, offering flexible operation that can be adjusted according to different product requirements; however, their production efficiency is relatively low. Continuous reactors, on the other hand, are ideal for large‑scale production, boasting high production efficiency and stable product quality—but they require a substantial capital investment and impose higher demands on operational control.
According to the aggregation process: These can be categorized into gas-phase polymerization reactors, bulk liquid-phase polymerization reactors, and solution polymerization reactors. In gas-phase polymerization reactors, olefin monomers exist in the gaseous state, and the reaction takes place in the gas phase, offering advantages such as a simple process flow and convenient post‑processing of the product. In bulk liquid-phase polymerization reactors, monomers undergo polymerization in the liquid state without the addition of solvents to the reaction system, resulting in high product purity; however, removing the heat of reaction can be relatively challenging. Solution polymerization reactors, on the other hand, involve dissolving monomers and catalysts in an appropriate solvent for polymerization, with mild reaction conditions that are easy to control—but the resulting product requires post‑processing steps such as solvent recovery.

Details

Technical parameters

Product Description
Technical parameters
Product Details Chart

Details

Structure: It typically consists of a reactor vessel, a stirring device, a heat transfer system, a sealing mechanism, and a control system. The reactor vessel is the site of the reaction and is generally made from high‑strength stainless steel or other corrosion‑resistant materials to withstand the high temperatures, high pressures, and chemical corrosion encountered during the reaction process. The stirring device ensures thorough mixing of the reactants, enhances mass and heat transfer, and guarantees that the reaction proceeds uniformly. The heat transfer system is used to control the reaction temperature; common designs include jacketed systems and coil‑type systems, which regulate the temperature inside the reactor by circulating heating or cooling media. The sealing mechanism prevents leakage of reactants and ensures that the reaction takes place in a closed environment. The control system monitors and regulates various reaction parameters—such as temperature, pressure, and stirring speed—to ensure that the reaction proceeds safely and stably.
Working principle: In the olefin polymerization reactor, olefin monomers undergo a polymerization reaction under the influence of initiators, catalysts, and other agents. The initiator decomposes to generate free radicals or ionic active centers, which trigger chain‑growing polymerization reactions in the olefin monomers, causing the monomer molecules to continuously link together and form long-chain polymers. A large amount of heat is released during the reaction, which must be promptly removed via a heat transfer system to maintain the reaction temperature within an appropriate range. At the same time, the stirring device ensures thorough contact between the catalyst and the monomers, thereby enhancing reaction efficiency and improving the uniformity of the polymer.
Type
According to the operating method: They can be divided into batch reactors and continuous reactors. Batch reactors are suitable for small‑batch, multi‑variety production, offering flexible operation that can be adjusted according to different product requirements; however, their production efficiency is relatively low. Continuous reactors, on the other hand, are ideal for large‑scale production, boasting high production efficiency and stable product quality—but they require a substantial capital investment and impose higher demands on operational control.
According to the aggregation process: These can be categorized into gas-phase polymerization reactors, bulk liquid-phase polymerization reactors, and solution polymerization reactors. In gas-phase polymerization reactors, olefin monomers exist in the gaseous state, and the reaction takes place in the gas phase, offering advantages such as a simple process flow and convenient post‑processing of the product. In bulk liquid-phase polymerization reactors, monomers undergo polymerization in the liquid state without the addition of solvents to the reaction system, resulting in high product purity; however, removing the heat of reaction can be relatively challenging. Solution polymerization reactors, on the other hand, involve dissolving monomers and catalysts in an appropriate solvent for polymerization, with mild reaction conditions that are easy to control—but the resulting product requires post‑processing steps such as solvent recovery.

Product Description
Technical parameters
Product Details Chart

Structure: It typically consists of a reactor vessel, a stirring device, a heat transfer system, a sealing mechanism, and a control system. The reactor vessel is the site of the reaction and is generally made from high‑strength stainless steel or other corrosion‑resistant materials to withstand the high temperatures, high pressures, and chemical corrosion encountered during the reaction process. The stirring device ensures thorough mixing of the reactants, enhances mass and heat transfer, and guarantees that the reaction proceeds uniformly. The heat transfer system is used to control the reaction temperature; common designs include jacketed systems and coil‑type systems, which regulate the temperature inside the reactor by circulating heating or cooling media. The sealing mechanism prevents leakage of reactants and ensures that the reaction takes place in a closed environment. The control system monitors and regulates various reaction parameters—such as temperature, pressure, and stirring speed—to ensure that the reaction proceeds safely and stably.
Working principle: In the olefin polymerization reactor, olefin monomers undergo a polymerization reaction under the influence of initiators, catalysts, and other agents. The initiator decomposes to generate free radicals or ionic active centers, which trigger chain‑growing polymerization reactions in the olefin monomers, causing the monomer molecules to continuously link together and form long-chain polymers. A large amount of heat is released during the reaction, which must be promptly removed via a heat transfer system to maintain the reaction temperature within an appropriate range. At the same time, the stirring device ensures thorough contact between the catalyst and the monomers, thereby enhancing reaction efficiency and improving the uniformity of the polymer.
Type
According to the operating method: They can be divided into batch reactors and continuous reactors. Batch reactors are suitable for small‑batch, multi‑variety production, offering flexible operation that can be adjusted according to different product requirements; however, their production efficiency is relatively low. Continuous reactors, on the other hand, are ideal for large‑scale production, boasting high production efficiency and stable product quality—but they require a substantial capital investment and impose higher demands on operational control.
According to the aggregation process: These can be categorized into gas-phase polymerization reactors, bulk liquid-phase polymerization reactors, and solution polymerization reactors. In gas-phase polymerization reactors, olefin monomers exist in the gaseous state, and the reaction takes place in the gas phase, offering advantages such as a simple process flow and convenient post‑processing of the product. In bulk liquid-phase polymerization reactors, monomers undergo polymerization in the liquid state without the addition of solvents to the reaction system, resulting in high product purity; however, removing the heat of reaction can be relatively challenging. Solution polymerization reactors, on the other hand, involve dissolving monomers and catalysts in an appropriate solvent for polymerization, with mild reaction conditions that are easy to control—but the resulting product requires post‑processing steps such as solvent recovery.
技术参数
技术参数