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Multistage crystallization process for the production of p-xylene

A technology for paraxylene and crystallization, which is applied in the field of multi-stage crystallization for the production of paraxylene, can solve the problems of high energy consumption, serious scaling of the precooler, and difficulty in crystal washing, and saves refrigeration energy and reduces refrigeration energy. Consumption, the effect of good technical effect

Active Publication Date: 2015-12-09
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The technical problem to be solved by the present invention is the problems of high energy consumption, serious fouling of the precooler and difficult crystal washing in the existing crystallization method for producing p-xylene, and a new multi-stage crystallization method for producing p-xylene is provided method, which has the advantages of low energy consumption, light fouling of the precooler, and easy washing of crystals

Method used

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  • Multistage crystallization process for the production of p-xylene
  • Multistage crystallization process for the production of p-xylene

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Embodiment 1

[0025] The multistage crystallization method for separating p-xylene described in the present invention.

[0026] Such as figure 1Said, the mixed xylene raw material a enters the raw material tundish 1, the temperature is 30°C, the flow rate is 1075kg / h, the p-xylene content is 95wt%, a part of the raw material b is pre-cooled by the mother liquid heat exchanger 2 and the precooler 3 After returning to the raw material tundish 1, the flow rate is 5375kg / h, and a part of raw material c enters the crystal slurry tank 4 to heat up the crystal, the flow rate is 1075kg / h, and the temperature is 15°C. The operating temperature of the crystal slurry tank 4 is 11°C, the overflow mother liquor d flows out from the upper part and enters the primary crystallizer 8 for crystallization, the concentrated crystal slurry e is separated by the solid-liquid separator 5 to obtain the filtered mother liquor f and p-xylene crystals g, The filtered mother liquor f enters the primary crystallizer 8...

Embodiment 2

[0028] The multistage crystallization method for producing p-xylene described in the present invention.

[0029] According to the operating condition of embodiment 1, adopt as figure 1 In the multi-stage crystallization method for producing p-xylene, the flow rate of mixed xylene raw material b is 10750 kg / h.

Embodiment 3

[0031] The multistage crystallization method for producing p-xylene described in the present invention.

[0032] According to the operating condition of embodiment 1, adopt as figure 1 In the multi-stage crystallization method for producing p-xylene, the flow rate of mixed xylene raw material b is 16125kg / h.

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Abstract

The invention relates to a multi-stage crystallization method for producing p-xylene. The problems of high energy consumption, serious scaling of a precooler and difficulty in crystal washing in the prior art are mainly solved. According to the technical scheme, the method comprises the following steps: feeding mixed xylene raw materials into a raw material intermediate tank; causing overflow mother liquor in a crystal slurry tank to flow out of the upper part and enter a primary crystallizer for crystallization, causing concentrated crystal slurry to flow out of the lower part, performing separation to obtain filtered mother liquor and p-xylene crystals by using a solid-liquid separator, causing the filtered mother liquor to enter the primary crystallizer for crystallization, performing separation on the crystal slurry in the primary crystallizer to obtain p-xylene crystals and primary crystallized-filtered mother liquor by using the solid-liquid separator, and heating and melting the p-xylene crystals in a melting tank; dividing the primary crystallized-filtered mother liquor into two jets, performing separation on crystal slurry in a secondary crystallizer to obtain p-xylene crystals and secondary crystallized-filtered mother liquor, and returning the p-xylene crystals into the crystal slurry tank. According to the method, the problems are well solved; the method can be used for p-xylene crystallization production.

Description

technical field [0001] The present invention relates to a multistage crystallization method for producing p-xylene. Background technique [0002] Paraxylene is an important raw material for the polyester industry, mainly used to produce purified terephthalic acid (PTA) or purified dimethyl terephthalate (DMT), and then produce polyester (PET) from PTA and DMT, and separate Mixed xylene is the main production method of p-xylene. Mixed xylenes are mainly composed of p-xylene, m-xylene, o-xylene and ethylbenzene. The difference between the boiling points of each component is small, but the difference in melting point is large. The crystallization method can be used to separate p-xylene. [0003] Patent US5498822 discloses a crystallization method for separating p-xylene. In this method, the raw material of mixed xylene is pre-cooled by a precooler, and then a high-purity p-xylene product is obtained by separating through a single-stage crystallization process. In the actual c...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C15/08C07C7/14
Inventor 陈亮肖剑顾军民钟思青张鸿翔
Owner CHINA PETROLEUM & CHEM CORP
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