Reaction method suitable for being catalyzed by solid catalyst

A solid-phase catalyst and reaction technology, applied in the field of reaction, can solve the problems of limited application range, fragmentation and wear, shortened service life, etc., and achieve the effect of wide application range, avoiding fragmentation and wear, and avoiding the decline of vitality

Active Publication Date: 2011-06-08
BIORIGHT WORLDWIDE
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] As far as the reaction method using a packed bed reactor is concerned, the existing problems are: [1] The exchange efficiency between the substrate and the solid-phase catalyst is low; [2] The reaction process is not easy to feed and gas, and it is not easy to adjust pH value and temperature, etc.; [3] Not suitable for viscous or insoluble substrates; [4] When using a solid-phase catalyst with small particles, the bed pressure drop is large, which leads to easy clogging
[0007] As far as the reaction method using a stirred reactor is concerned, although it can adjust various reaction conditions as required, in the process of stirring the stirring paddle, since the solid-phase catalyst is suspended in the substrate solution in the reaction tank, Strong collisions will occur between the solid phase catalyst particles, between the solid phase catalyst particles and the stirring paddle, and between the solid phase catalyst particles and the reaction tank wall (Enzymology, edited by Chen Shigen and Zhou Runqi, Fudan University Press, Shanghai , 2001; Biological Reaction Engineering, edited by Qi Yizheng and Xia Jie, Chemical Industry Press, Beijing, 2004), which leads to the fragmentation and wear of solid-phase catalyst particles due to collisions, thereby reducing the activity of solid-phase catalysts and reducing the use of The life is shortened, and the solid phase catalyst will produce fragments or slag due to fragmentation and wear, and these fragments or slag will be lost with the progress of the reaction, which will hinder the subsequent treatment of the reaction liquid, such as filtration and purification of the product, etc.
Moreover, it is well known that the greater the density and the faster the movement (rotational speed) of the solid-phase catalyst particles suspended in the solution, the higher the efficiency of the reaction; The more easily the catalyst fragments, the faster its activity declines
Therefore, the scope of application of the reaction method using a stirred reactor is limited, especially not suitable for solid-phase catalyst particles that are inherently fragile

Method used

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  • Reaction method suitable for being catalyzed by solid catalyst
  • Reaction method suitable for being catalyzed by solid catalyst
  • Reaction method suitable for being catalyzed by solid catalyst

Examples

Experimental program
Comparison scheme
Effect test

example 1

[0060] Example 1. Suspension agitation damages the immobilized enzyme carrier

[0061] use Figure 4 In the shown reactor, the currently widely used granular immobilized enzyme resin carrier Sepabeads EC-EP (Grazu V, Abian O, Mateo C, Batista-Viera F, Fernandez-Lafuente R, Guisan JM.Biotechnol Bioeng.2005, 90:597-605; Grazu V, Abian O, Mateo C, Batista-Viera F, Fernandez-Lafuente R, Guisan JM.Biomacromolecules.2003, 4:1495-1501) and granular immobilized glucose isomerase, respectively. Disc stirring (that is, as mentioned above, the granular immobilized enzyme resin carrier and the immobilized glucose isomerase are respectively loaded into the container 53, and the container 53 follows the rotating shaft 21 for centrifugal rotation to obtain the stirring effect) and suspension stirring test, compared The degree of damage to the resin carrier. Sepabeads EC-EP was purchased from Italy Resindion S.R.L company. Granular immobilized glucose isomerase was purchased from Sigma, St...

example 2

[0068] Example 2. The whole piece of open-pore immobilized cells is used as a stirring paddle for continuous stirring reaction to prepare high fructose syrup [1]

[0069] Glucose isomerase catalyzes the reaction that converts glucose into fructose. The preparation of the vector pRSET-lac-MGI4-35-kan expressing glucose isomerase is as follows. According to the sequence design of pGEMT-Easy (Promega), PCR primers are specifically: upstream primer RBS-NdeI: 5'-CATATGTATATCTCCTTCTTGTGTGAAATTG-3'; downstream primer RBS-AlwNI:

[0070] 5'-CAGTGGCTGCTGCCAGTGGCGATAAGTC-3'. Using pGEMT-Easy (Promega) as a template, PCR was performed with the above primers, and a 755bp product was amplified. The PCR conditions were: 50ng pGEMT-Easy (Promega), 0.4 μM RBS-NdeI, 0.4 μM RBS-AlwNI, 50 μM dATP, 50 μM dTTP, 50 μM dCTP, 50 μM dGTP, 20 mM Tris-HCl (pH 8.8), 10 mM KCl, 10 mM ( NH 4 ) 2 SO 4 , 2mM MgSO 4 , 0.1% Triton X-100, 2.5U Pfu DNA polymerase (Promega), the reaction volume was adjuste...

example 3

[0077] Example 3. The whole piece of open-pore immobilized cells is used as a stirring paddle for continuous stirring reaction in series to prepare high fructose syrup

[0078] The preparation of the glucose isomerase-immobilized cell sheet, the determination of its activity, its installation on the reaction tank, the operation of the isomerization reaction and the reaction tank, etc. basically refer to Example 2. In this example, 50 grams of glucose isomerase-immobilized cell sheets were prepared, and the enzyme activity was 5,298 units / gram. Using 2 such as Figure 4 In the shown reaction tanks, reaction tank I and reaction tank II, 23.5 grams of immobilized cell sheet belts with a specific activity of 5,298 units / g were filled in the grid tray 20 respectively, and reacted separately, and the operation was the same as that of Example 2. When the flow rate of the reaction tank I was recorded at 7.1 g / min, the optical rotation (22°C) was -8.68 (equivalent to 48.68% fructose c...

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Abstract

The invention discloses a reaction method applying to catalyze solid phase catalyst, the method uses the reactor including at least one reaction tank, the reaction tank includes tank body and rotate axle fixed in the tank body, the reaction tank also includes a container fixed on said axis which contains solid phase catalyst, the whole outer wall of the container is equipped with holes which can penetrate reaction liquid and gas but not solid phase catalyst. The solid phase catalyst also can be uses as an anticentripetal stirrer device, it rotates with the rotate axle to generating centrifugal force in reaction fluid while generates negative pressure in solid phase catalyst, the centrifugal force enforces the reacting fluid pass the solid phase catalyst along the anticentripetal directionand is kicked off, then the kicked off reaction fluid passes the solid phase catalyst again along negative pressure flow, so it produces circulating reflux to make said reaction fluid and / or gas passsaid solid phase catalyst and make them contact fully and effectively. The reaction method can prevent the vitality of catalyst decline, prolong the life tine of catalyst and had wide application range.

Description

technical field [0001] The invention relates to a reaction method, in particular to a reaction method in which the reaction medium is liquid. Background technique [0002] In the fields of pharmaceutical industry, food industry, environmental protection, agriculture, light textile industry, chemical industry and other fields, the reaction methods for various reactions are often realized by means of reactors, and most of the various reactions described therein require catalysts to react. For reactions carried out in liquid media, in order to improve the reaction efficiency, the reactants and catalyst must be in effective contact. This is especially true when the catalyst is a solid. [0003] In the fields of biology, pharmaceutical industry, food industry, environmental protection, agriculture, etc., enzymes or enzyme-containing cells are a more attractive type of catalyst among many catalysts. Moreover, at present, enzymes or enzyme-containing cells are mostly used in immo...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J8/10
Inventor 王骏金彩科
Owner BIORIGHT WORLDWIDE
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