Method and device for degassing solid polymer and recovering effluent gas

A solid polymer and exhaust gas technology, which is applied in the field of solvents and unreacted monomers in polyolefin resins, can solve the problems of low degassing efficiency and exhaust gas recovery efficiency, ineffective separation of hydrogen, and increased safety hazards. , to achieve significant economic benefits and environmental friendliness, strong practical significance and application value, and reduce system energy consumption

Inactive Publication Date: 2012-06-06
ZHEJIANG UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This method can effectively make the solid polymer degassing, and can also effectively utilize the solvent and / or unreacted polymerization feed that reclaims from the solid polymer, yet, there is weak point in this method: (1) through step ( i) The polymer powder after degassing contains a large amount of polymer feed, which is removed by inert gas in step (ii), and the resulting discharge contains inert gas, polymer feed and water The gas is not recovered, but discharged to the torch, which causes a serious waste of raw materials, increases production costs, and pollutes the environment; (2) the drying gas of step (i) contains hydrogen, and the polymer discharged from the reactor It also contains hydrogen, which cannot be effectively separated and gradually accumulates in the degassing container, which will affect the degassing effect of the polymer, increase potential safety hazards, and even affect the entire production system in severe cases until the shutdown
[0010] In summary, the existing solid polymer degassing and exhaust gas recovery methods have disadvantages such as low degassing efficiency and exhaust gas recovery efficiency, high energy consumption, large raw material consumption, and unfriendly environment. Therefore, a degassing method is invented. A solid polymer degassing method with high gas efficiency, effective recycling of raw materials, energy saving and environmental friendliness has high economic benefits and practical significance

Method used

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  • Method and device for degassing solid polymer and recovering effluent gas
  • Method and device for degassing solid polymer and recovering effluent gas
  • Method and device for degassing solid polymer and recovering effluent gas

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0047] like figure 2 As shown, a solid polymer degassing and exhaust gas recovery device includes a degassing container 4, a gas separation device and a recovery device.

[0048] The degassing container is a cylindrical structure, and two gas collection devices for separating the degassing area and collecting exhaust gas are arranged inside. The first gas collection device 61 is arranged in the middle of the degassing container 1, and the second gas collection device 61 The collection device 62 is arranged at the bottom of the degassing container 4 near the outlet, the top of the degassing container 4 is a primary degassing zone, the middle part of the degassing container 4 and the area where the second gas collecting device 62 is located is a secondary degassing zone, The lower part of the degassing container 4 below the second gas collection device 61 is a three-stage degassing zone.

[0049]The recovery device includes a first compressor 51 , a cooler 6 , a condenser 7 an...

Embodiment 2

[0055] The same device as in Example 1 was used to produce ethylene-hexene copolymerized linear low-density polyethylene (LLDPE) products by a gas-phase fluidized bed process, with a reaction temperature of 88° C. and a reaction pressure of 2.1 MPa, using non-condensing operation. The LLDPE product discharged from the reactor enters the top of the degassing vessel 4 driven by the conveying gas, and the flow rate of each component in the feed stream 40 is: LLDPE powder 40t / h, nitrogen 180kg / h, hydrogen 3kg / h, ethylene 2600kg / h, hexene 2000kg / h. Among them, ethylene and hexene are unreacted monomers without solvent. The temperature of the degassing container 4 is 81° C., the pressure is 20 kPa, the first degassing medium is ethylene, and the flow rate of the first degassing medium stream 10 is 400 kg / h. The first exhaust gas 11 is compressed and condensed, the outlet pressure of the first compressor 51 is 2.0 MPa, and the outlet temperature of the cooler 6 is 30°C. After more ...

Embodiment 3

[0060] like image 3 As shown, a solid polymer degassing and exhaust gas recovery device includes a degassing container 4, a gas separation device and a recovery device.

[0061] Shown degassing container and gas separation device are identical with the device in embodiment 1 and 2, and described recovery device is in figure 2 On the basis of the shown device, a non-porous composite membrane primary separation device 92 is added between the condenser 7 and the porous membrane separation device 8 .

[0062] The ethylene-butene copolymerized linear low density polyethylene (LLDPE) product is produced by the gas phase fluidized bed process, the reaction temperature is 88°C, the reaction pressure is 2.1MPa, and the condensation operation is adopted. The LLDPE product discharged from the reactor enters the top of the degassing vessel 4 driven by the transport gas, and the flow rate of each component in the feed stream 40 is: LLDPE powder 40t / h, nitrogen 160kg / h, hydrogen 3kg / h, e...

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Abstract

The invention discloses a method for degassing a solid polymer and recovering effluent gas. A solid polymer enters a degassing container for decompression and is subjected to three degassing processes: 1) the solid polymer fully contacts with a gaseous reacting substance to remove the most of a solvent and an unreacted monomer in the solid polymer; 2) the processed solid polymer fully contacts with inert gas to remove the gaseous reacting substance and further remove the solvent and the unreacted monomer; and 3) the processed solid polymer fully contacts with the inert gas containing a catalyst deactivator. The effluent gas discharged in the degassing steps 1) and 2) is separated and processed from gas after being recovered, and the solvent, the unreacted monomer and a degassing medium are all recovered and utilized. The invention also discloses a device for implementing the method. With the method disclosed by the invention, degassing time for a polymer is shortened, the use amount of the degassing medium is reduced, the solvent and the unreacted monomer can be effectively recovered, and the degassing medium is recycled, thereby preventing micromolecules from being accumulated, reducing emission amount and lowering energy consumption. The method has the advantages of strong realistic significance and application value.

Description

technical field [0001] The invention relates to the technical field of solid polymer treatment, in particular to a method for removing solid polymers, especially solvents and unreacted monomers in polyolefin resins, by using gas-phase reactive substances and inert gases, and recovering and recycling exhaust gas and device. Background technique [0002] In the polymerization reaction, depending on the process and physical properties, the polymerization product will be in different states, among which the polymer is typically discharged from the reactor in the form of solid powder, such as the gas phase polyolefin process. When the solid polymer is discharged from the reactor, there are often residual solvents and unreacted monomers in the polymer powder. Taking the gas-phase fluidized bed production process of linear low-density polyethylene (LLDPE) as an example, the LLDPE powder contains unreacted Monomers, comonomers and condensing agents such as ethylene (C 2 h 4 ), pr...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08F6/00C08F10/00C08J11/02
Inventor 蒋斌波楼佳明王靖岱阳永荣黄正梁
Owner ZHEJIANG UNIV
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