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Expanded bed chromatographic separation column used for biochemical separation process and process flow

A chromatographic separation and separation process technology, applied in the field of chromatographic separation devices, can solve the problems of no commercial products, clogging, affecting the use effect/efficiency of the expanded bed, etc.

Inactive Publication Date: 2013-01-02
顾雄毅
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In order to achieve the goal of uniform pressure distribution, the volume of the cavity of the expanded bed must be large, but the increase in the volume of the cavity will lead to serious back-mixing and affect the use effect / efficiency of the expanded bed;
[0026] 2) In the middle and late stages of the "sample loading" process, as the solid content in the circulating sample solution increases, the solid particles coalesce. At this time, the circulating sample solution with high viscosity and high solid content is difficult to clean the porous screen. The role of the support plate, the clogging phenomenon will still occur, and it is difficult to avoid
[0027] Therefore, until now, this technical solution has not been practically applied in actual industrial production, nor has there been a corresponding commercial product.

Method used

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  • Expanded bed chromatographic separation column used for biochemical separation process and process flow
  • Expanded bed chromatographic separation column used for biochemical separation process and process flow
  • Expanded bed chromatographic separation column used for biochemical separation process and process flow

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0252] Example 1: Application of Expanded Bed in Monoclonal Antibody Production

[0253] The protein is expressed by CHO animal cells and analyzed outside the cells. The size of CHO cells is about 10-15um. They are cultured in 1,500L-10,000L cell tanks, and the final cell density is 1X10 7 cells / ml, titer 500mg / ml.

[0254] The traditional process requires high-speed continuous flow centrifugation plus depth filtration followed by protein A affinity chromatography, followed by ion exchange, hydrophobic, or high-resolution gel chromatography for further purification.

[0255]The above process usually takes 2 to 3 days to complete the three steps of continuous flow centrifugation, depth filtration, and protein A affinity coloring. Affinity chromatography runs at 180cm / hr (fixed bed ~ 120-180cm / hr), linear velocity (bed height 30cm, residence time 10 minutes), and the load is about 20g / L.

[0256] The chromatographic column has a volume of 37.5L and a diameter of about 40cm. T...

Embodiment 2

[0276] Embodiment 2: the application of expanded bed in the production of recombinant human albumin (rHSA)

[0277] The protein was expressed by Pichia Pastoris yeast cells, analyzed extracellularly, cultured in a 5,000L fermenter, and the final titer was ~1.0g / l.

[0278] The traditional process requires high-speed continuous flow centrifugation and deep-layer filtration, plus ion-exchange chromatography, and then further purification with hydrophobic and ion-exchange. The traditional process usually takes 2-3 days to complete the three steps of continuous flow centrifugation, depth filtration, and ion exchange capture chromatography. The ion exchange operates at a linear speed of 120cm / hr (fixed bed ~ 120-180cm / hr) (bed height 30cm, residence time 15 minutes), and the load capacity is about 10g / L. The chromatographic column has a volume of 500L and a diameter of about 140cm (145cm). The operating flow rate of the chromatographic system is about 1900L / hr, and the 5000L samp...

Embodiment 3

[0296] Embodiment 3: the application of expanded bed in antibiotic production

[0297] Antibiotic production, which is large in scale and high in flow rate, is another good field for expanding bed technology.

[0298] As the pharmaceutical industry has higher and higher requirements for the purity of antibiotics, ion exchange chromatography has gradually become a necessary means in the downstream separation process, especially when the fermentation broth contains flocculent solids that cannot be removed by filtration once. Expanded bed technology The application can have significant economic benefits.

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Abstract

The invention relates to an expanded bed chromatographic separation column used for a biochemical separation process and a process flow, belonging to the field of biochemistry. In the invention, a liquid pressure equalizing distributor with self-cleaning function is arranged below a porous blocking sieve plate at the bottom of an expanded bed, and an upper nozzle assembly with back-flushing cleaning function is arranged at the top of the expanded bed so that the expanded bed chromatographic separation column is suitable for treating a raw material liquid containing solid particle impurities, meanwhile, the raw material sample liquid entering the expanded bed can be better distributed uniformly, therefore, the problem of uniform distribution of feed liquid pressure of lower-bed pressure drop feed liquid along a radius direction in the industrial amplification production process is solved, fluid passing through a bed layer of the expanded bed is better ensured to be in a plug flow state, the separation theoretical plate number and the chromatographic separation efficiency of the expanded bed can be greatly enhanced, the using effect and the using efficiency of the expanded bed are improved and the adsorption capacity and the desorption resolution of the expanded bed are enhanced.

Description

technical field [0001] The invention belongs to the technical field of biochemistry, and in particular relates to a chromatographic separation device used for extraction / separation / purification in industrial scale production and a production process thereof. Background technique [0002] Chromatographic separation is one of the most commonly used methods in biochemical separation processes. [0003] The traditional chromatographic separation column (referred to as chromatographic column) adopts the form of fixed bed, that is, the adsorption resin is pressed and fixed in the chromatographic column with upper and lower porous sieve plates, so that it cannot flow, commonly known as "fixed bed". [0004] The characteristics of the traditional fixed bed are that due to the small porosity of the bed, the resistance of the fluid passing through the bed is relatively large, the fluid flows through the bed in a "plug flow", and the fluid velocity in the radial direction is well distr...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D15/08B01D15/18
Inventor 顾雄毅
Owner 顾雄毅
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