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Analogue mobile bed chromatic reactor

A technology for simulating moving beds and reactors, applied in the field of simulated moving bed chromatography reactors, can solve the problems of large amount of stationary phase and mobile phase in intermittent chromatography, difficult popularization and application of chromatography reactor technology, and low concentration of separated products, etc. Speed, improve separation efficiency, improve the effect of conversion rate

Inactive Publication Date: 2002-10-16
ZHEJIANG UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Due to the shortcomings of batch chromatography, such as the large amount of stationary phase and mobile phase, low utilization rate of adsorbent, low concentration of separated products, and high separation cost, it is difficult to popularize and apply the chromatographic reactor technology with the characteristics of batch chromatography in the industrial field.

Method used

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  • Analogue mobile bed chromatic reactor
  • Analogue mobile bed chromatic reactor
  • Analogue mobile bed chromatic reactor

Examples

Experimental program
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Embodiment Construction

[0018] like figure 1 The simulated moving bed chromatographic reactor of the closed-loop structure shown, it comprises four packed columns 1,2,3,4, is connected by the outlet end of the first packed column 1 and the inlet port of the second packed column 2, the first The outlet end of the two packed columns 2 is connected to the inlet end of the third packed column 3, the outlet end of the third packed column 3 is connected to the inlet end of the fourth packed column 4, and the outlet end of the fourth packed column 4 The inlet port of the first packed column 1 is connected through the circulating pump 10 and the connecting pipeline 7; the inlet port of each packed column 1, 2, 3, 4 passes through the respective on-off valves VA1, VA2, VA3, VA4 and They are respectively connected to the raw material liquid inlet pipeline 5 for inputting the reactant and the eluent inlet pipeline 6 for inputting the eluent through respective on-off valves VB1, VB2, VB3, VB4; each packed column...

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Abstract

The chromatographic reactor includes three or more packed columns cascaded successively. The inlet end of each packed column is connected via a separated switch-type valve to the inlet pipe for material liquid to enter and the inlet pipe for eluting liquid to enter; and the outlet end of each packed column is connected via a separated switch-type valve to the outlet pipe for residual liquid with enriched weak sorptive component from reacted product to drain and the outlet pipe for extracting liquid with enriched strong sorptive component from reacted product to drain. By means of controlling the switch state of the valves, the present invention performs, chromatographic separation and reaction simultaneously, so that the reactor can run continuously with high reaction converting rate and high produce separating efficiency. The present invention is especially suitable for chromatographic separation course of different products and of product and reactant.

Description

technical field [0001] The invention relates to a reaction separation coupling device containing a catalyst and an adsorbent for liquid treatment, in particular to a simulated moving bed chromatographic reactor. Background technique [0002] In the application fields of chemical industry, medicine, biology and fine chemical industry, there are generally a series of separation devices in the downstream of the chemical reactor or biochemical reactor to cooperate to form the whole process, and these separation devices mainly use physical methods to realize the reaction products and reactants. The separation, and the purification of the reaction product is realized, so as to obtain the product that meets the quality index. However, in the case of reversible reactions or reaction by-products that can poison the catalyst, this type of process has disadvantages such as low reaction conversion rate, low product yield, low separation efficiency, and low prod...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D15/08B01J8/02
Inventor 卢建刚
Owner ZHEJIANG UNIV
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