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A Confined Bed Adsorption Separation Method

A separation method and bed adsorption technology, applied in the new separation field, can solve the problems of high price, collapse of expanded bed, difficult cleaning, etc., and achieve the effect of low cost and convenient operation

Inactive Publication Date: 2016-03-23
ZHEJIANG NORMAL UNIVERSITY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

One is that the solid filler in the expanded bed should have a relatively large density and a certain particle size distribution, so that when the bed expands, the large and heavy particles are at the bottom of the bed, and the small and light particles are at the top of the bed, forming a stable The classification behavior of this kind of expanded bed adsorbent is mostly monopolized by large foreign companies, and the price is expensive; second, the expanded bed device must be conducive to the formation of plug flow, especially at the fluid inlet and outlet of the device. There is an obvious jet area, such as the fluid distributor system launched by Denmark’s UpFront company named FastLine; third, a special operation method must be adopted, and the fluid flow rate should be controlled between the minimum fluidization velocity and the terminal velocity, especially for adsorbent adsorption. The properties of the corresponding substances will change, and it is necessary to adjust the flow rate, otherwise the state of the expanded bed cannot be maintained, and even the collapse of the expanded bed may occur
[0005] Among them, the design of fluid distributor and adsorbent is the most critical. In recent years, scholars from various countries have conducted a lot of research on this. Although some scholars have reported the application examples of pilot scale and production scale, most of the development of EBA process still only stays in the laboratory scale
The main reason is the above requirements on the expanded bed device, adsorbent and operation mode, especially the bridging effect caused by cell debris, nucleic acid anion substances, etc. Adjusting the flow rate and other operating conditions will also cause the collapse of the expanded bed, and the state of the expanded bed cannot be maintained. The industrialization of EBA technology has encountered a "bottleneck", which greatly limits the wide application of EBA technology in the field of bioengineering

Method used

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  • A Confined Bed Adsorption Separation Method
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  • A Confined Bed Adsorption Separation Method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0056] The inner diameter of the confined bed column is 24 mm, the outer diameter is 30 mm, and the height is 1000 mm (the experimental device can adjust the column height from 200 to 900 mm); the superparamagnetic adsorbent (adsorbent) has a particle size of 600 to 700 microns, and the active base The group is a carboxyl group. According to the magnetic hard confinement scheme, the column of "constrained bed column" is constructed. The fluids are deionized water, 10% and 20% glycerin-deionized water solution. The results show that the axial mixing coefficient of fluids with different viscosities and flow rates in the column beds of different heights is between 1-9×10-6m2 / s, and the fluids are similar to plug flow. The result is similar with or without glass beads with a particle size of 4 mm in the lower distributor.

Embodiment 2

[0058] The inner diameter of the confined bed column is 50 mm, the outer diameter is 58 mm, and the height is 1000 mm (the experimental device can adjust the column height from 200 to 900 mm); the fluid is deionized water, 10% and 20% glycerin-deionized water, respectively. Ion aqueous solution; the structured adsorbent is a self-made agarose DEAE type ion exchanger (adsorbent). The "constrained bed column" column was constructed according to the hard confinement scheme of regular adsorbent. The results show that the axial mixing coefficient of fluids with different viscosities and flow rates in the column beds of different heights is between 1-9×10-6m2 / s, and the fluids are similar to plug flow. The result is similar with or without glass beads with a particle size of 4 mm in the lower distributor.

Embodiment 3

[0060] The inner diameter of the confined bed column is 50 mm, the outer diameter is 58 mm, and the height is 1000 mm (the experimental device can adjust the column height from 200 to 900 mm); the adsorbent is DK110 resin (adsorbent) with a particle size of 1500 to 2000 microns. The fluids are deionized water, 10% and 20% glycerin-deionized water solution. The "constrained bed column" column was constructed according to the hard confinement scheme of regular adsorbent. The results show that the axial mixing coefficient of fluids with different viscosities and flow rates in the column beds of different heights is between 1-9×10-6m2 / s, and the fluids are similar to plug flow. The result is similar with or without glass beads with a particle size of 4 mm in the lower distributor.

[0061] The beneficial effect of the present invention is that the constrained bed adsorption separation method can directly extract the target components from the particle-containing material like the ex...

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PUM

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Abstract

The invention discloses a constraint bed adsorption separation technology. The constraint bed adsorption separation technology is mainly characterized in that an adsorbent is constrained on a fixed framework by utilizing an external force, gaps among a column body, the fixed framework, the adsorbent or a 'constraint assembly' constrained by an 'aggregate' allow solid particles to pass through, and as long as the flow velocity of fluid does not exceed a 'constraint force', the adsorbent can keep an 'initial constraint state' and is regularly arranged in a column of a constraint bed respectively according to three modes, namely hard constraint, soft constraint and aggregate constraint. The constraint bed adsorption separation technology can be used for directly extracting target ingredients from particle materials just like expanded bed adsorption to obtain a separation effect similar to that of a fixed bed, and also avoids the special conditions such as the adsorbent with certain density and particle size distribution, a fluid distributor system and specific flow velocity of the fluid necessary for an expanded bed; an expansion process is very convenient, low in cost and convenient to operate, and the constraint bed adsorption separation technology can be used for a material separation process, and especially can be used for a reaction process.

Description

Technical field [0001] The invention relates to the technical field of novel separation, in particular to a constrained bed adsorption separation method. Background technique [0002] Expanded Bed Adsorption (EBA) technology was developed in the 1990s. [0003] A new type of separation and purification technology that can directly capture the target product from the fermentation broth or cell homogenate, and integrate solid-liquid separation, concentration and initial purification into one operation unit, reducing the number of operation units, shortening the operation time, and saving The production cost is known as the first new unit operation in recent decades. The expanded bed is also called a stable fluidized bed (StabilizedFluidizedBed). The filler in the bed is in a critical fluidized state. It is a special case of a fluidized bed, but it is based on the stability of solid fillers (such as adsorbents and catalysts) in the expanded bed. For classification behavior, the numb...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D15/20B01D15/24
Inventor 何卫中邓刚
Owner ZHEJIANG NORMAL UNIVERSITY