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Second esterification reactor in continuous production device of poly (trimethylene terephthalate)

A technology of polyethylene terephthalate and propylene glycol, which is applied in the field of the second esterification reactor, can solve the problems of reducing production costs, complicated process flow, unfavorable production management, etc., and achieves the improvement of product quality, guaranteed reaction time, and guaranteed sequence flow effect

Inactive Publication Date: 2012-01-11
BC P INC CHINA NAT PETROLEUM CORP +1
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  • Claims
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AI Technical Summary

Problems solved by technology

In the existing continuous polymerization technology for producing poly(trimethylene terephthalate), the esterification reactor generally adopts a vertical reactor. Since various additives need to be added in different esterification stages during the production process, if a vertical reactor is used It is not easy to control the residence time of additives, the process flow is complicated, and it increases equipment investment and production energy consumption, which is not conducive to production management and reduction of production costs.

Method used

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  • Second esterification reactor in continuous production device of poly (trimethylene terephthalate)
  • Second esterification reactor in continuous production device of poly (trimethylene terephthalate)

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Embodiment Construction

[0019] Such as figure 1 As shown, the present invention provides a second esterification reactor in a continuous production device for poly(trimethylene terephthalate) 1,3-trimethylene, comprising a reactor tank body 1, and the reactor tank body is a horizontal tank body , which is provided with one or more partitions 4, the partition divides the inner space of the reactor body into at least two chambers, the upper edge of the partition and the upper part of the reactor body There is a space between the inner walls. The length of each of the chambers can be set to be equal or unequal according to specific process requirements and actual conditions. For example, the position of the partition can be set according to the difference in the required residence time of the esterified product in each of the chambers, so that the The chambers are set with different lengths to control the residence time of the materials in each chamber so as to provide greater controllability for addin...

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Abstract

The invention provides a second esterification reactor in a continuous production device of poly (trimethylene terephthalate) (PTT), comprising a reactor autoclave body, wherein, the reactor autoclave body is horizontal and provided with one or more separator plates inside, the separator plates separate the inner space of the reactor autoclave body into at least two cavities, each cavity has same or different length with other cavity, the bottom of the separator plate is provided with a through hole or a gap for the circulation of the materials, the upper edge of the separator plate is apart from the inner wall of the upper portion of the reactor autoclave body with a spacing, partial or all cavities are correspondingly provided with additive conduits and stirrers, and the reactor autoclave body is provided with a jacket and / or a heating coil. According to the invention, the retention time of the esters in different cavity is controllable, so that the esterification degree is controlled, and by adding various additives in the esters with different esterification degree in different cavity, the product quality is improved.

Description

technical field [0001] The invention relates to a device for producing polytrimethylene terephthalate, in particular to a second esterification reactor in a continuous production device for polytrimethylene terephthalate. Background technique [0002] Polytrimethylene terephthalate (PTT) is a new type of polyester material that was successfully developed industrially in the mid-1990s. In the existing continuous polymerization technology for producing poly(trimethylene terephthalate), the esterification reactor generally adopts a vertical reactor. Since various additives need to be added in different esterification stages during the production process, if a vertical reactor is used Then it is difficult to control the residence time of the additive, the technological process is complicated, and the equipment investment and production energy consumption are increased, which is not conducive to production management and reduction of production cost. Contents of the invention ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08G63/183C08G63/78
Inventor 许贤文顾爱军杨建川李盛兴
Owner BC P INC CHINA NAT PETROLEUM CORP
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