Production method of polypropylene and device thereof

A production device and production method technology, which is applied in the field of polypropylene, can solve problems such as raw materials, steam, and heat energy not being recovered, waste gas, waste water, and waste heat not being treated, and environmental pollution, so as to improve heat energy utilization efficiency and eliminate safety hazards. Hidden dangers and the effect of reducing production costs

Active Publication Date: 2009-12-30
ZHEJIANG SHAOXING SANJIN PETROCHEM
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Problems solved by technology

[0002] At present, the production methods of polypropylene mainly include the following types: 1. The solvent polymerization process has the disadvantages of large investment, high energy consumption, and serious environmental pollution; 2. The combined method of still-type liquid-phase polymerization and fluidized-bed gas-phase polymerization Bulk polymerization method; 3. Gas phase method, using a plug flow gas phase reactor; 4. A combined bulk polymerization method using a liquid phase loop reactor and a dense phase fluidized reactor; 5. Batch liquid phase bulk polymerization method
Among the above several processes, the batch-type liquid-phas...

Method used

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  • Production method of polypropylene and device thereof
  • Production method of polypropylene and device thereof
  • Production method of polypropylene and device thereof

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Embodiment Construction

[0043] like figure 1 Shown, the production device of polypropylene of the present invention mainly comprises:

[0044] Polymerization reaction unit, the polymerization reaction unit is connected with feed tank 1, and is used for polymerizing propylene and ethylene monomers to obtain polymer slurry, including pre-contact tank 2, pre-polymerization reactor 3, and polymerization reactor 3 connected in sequence ; An additional heat exchanger is provided at the inlet pipeline of the precontact tank 2;

[0045] The flash degassing unit is used to separate the polymer slurry produced by the polymerization reaction unit from the propylene monomer, including a flash tank 4 connected to the polymerization reactor 3, a bag filter 5 connected to the flash tank 4, and high-pressure washing The tower 11 is connected with the flash tank 4 on the one hand, and connected with the feed tank 1 on the other hand, the low-pressure scrubber 12 is connected with the bag filter 5 on the one hand, an...

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Abstract

The invention discloses a production method of polypropylene with an English name of Polypropylene (short for PP) and a device thereof, belonging to the technical field of polymer synthesis. The production method comprises the steps of: prepolymerization, polymerization-flash vaporization, degasification-steaming, drying-extruding, granulating-product package and the like. By optimizing the technique steps and parameters of prepolymerization, polymerization, flash vaporization, degasification, steaming, drying, extruding, granulating and the like, the invention improves the utilization ratio of raw materials, simultaneously adds a waste gas and waste liquor recovery system creatively, adds a heat recovery system of a washing tower, uses recovered heat for heating grease, and improves heat utilization ratio; the setting of powder and condensate recovery device improves production efficiency and reduces production cost; a standby water tank is added for granulating and water supply, thus preventing machine stopping caused by fault of the water tank and improving production efficiency; and the improvement of gas-exiting pipelines and exhaust pipelines eliminates potential safety hazard, saves cost and has good environment protection.

Description

technical field [0001] The invention relates to a production method of Polypropylene (abbreviated as PP) and a device thereof, belonging to the technical field of polymer synthesis. Background technique [0002] At present, the production methods of polypropylene mainly include the following types: 1. The solvent polymerization process has the disadvantages of large investment, high energy consumption, and serious environmental pollution; 2. The combined method of still-type liquid-phase polymerization and fluidized-bed gas-phase polymerization Bulk polymerization method; 3. Gas phase method, using a plug flow gas phase reactor; 4. A combined bulk polymerization method using a liquid phase loop reactor and a dense phase fluidized reactor; 5. Batch liquid phase bulk polymerization method . Among the above several processes, the batch-type liquid-phase bulk polymerization method uses propylene monomer as raw material, adds trace hydrogen, triethylaluminum and auxiliary cataly...

Claims

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Application Information

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IPC IPC(8): C08F10/06C08F2/01B29B9/06
CPCY02P70/10
Inventor 钟建明朱伟刚劳一峰赵珏明舒建成
Owner ZHEJIANG SHAOXING SANJIN PETROCHEM
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