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Method for preparing porcine circovirus through basket reactor fermentation

A porcine circovirus and reactor technology, applied in biochemical equipment and methods, viruses/bacteriophages, microorganisms, etc., can solve the problems of uneven inoculation of cell species, expensive microcarriers, and only one-time use. Small area, high degree of automation, and the effect of improving quality

Active Publication Date: 2013-10-16
WENS FOODSTUFF GRP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although compared with the traditional spinner bottle culture process, it has the advantages of less land occupation, less energy consumption, less labor, easier expansion of production scale, higher virus toxicity, and stable product quality, but its production process has the following problems: ① There are problems of contact probability and compatibility between cells and microcarriers, and it is not easy to inoculate cells uniformly; ② The cell growth medium needs to be emptied during virus inoculation, and microcarriers will be lost when the medium is changed; Impurities such as cell debris in the microcarrier are cleaned, so they cannot be recycled and can only be used once, and the microcarrier is expensive, resulting in high production costs; ④ The growth state of the cells on the microcarrier is an extended form, close to a planar structure, and the virus is inoculated Finally, the cell death process is synchronous, that is, most of the cell death time is close, and in order to improve the efficiency of virus infection, an incubator whose main component is glucosamine needs to be added to the cell culture medium to promote the virus's infection of cells , so the virus can only be harvested once
Although the NBS basket bioreactor has been used in cell culture, however, different cells and viruses have different requirements on the culture environment and culture process conditions. Only when the conditions are suitable, the number of cultured cells or viruses Many, good activity, and high virus toxicity

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0044] Reactor: NBS Celligen plus basket bioreactor in the United States, the reactor tank is 5L, the effective volume is 3.5L, and 100g of Fibra Disk carrier is added.

[0045] Cell growth medium: RPMI-1640 medium 93% bovine serum 7%.

[0046] Cell maintenance solution: the volume fraction of RPMI-1640 culture medium is 98%, and the volume fraction of bovine serum is 2%.

[0047] Specific operation:

[0048] (1) Preparation of host cell species

[0049] Take the PK-15 cell line as the host cell, take out the cell species from the liquid nitrogen tank, resuscitate the cell, then place it in a culture bottle, add cell growth solution and culture it in an incubator at 37°C until the cell grows into a dense cell single layer, and then cultivated by the spinner bottle culture method, that is, the cells are divided into several culture flasks for cultivation, and after the cells are full of the culture flasks, they are digested with 0.25% trypsin solution, and then divided into s...

Embodiment 2

[0060] The difference from Example 1 is:

[0061] Reactor: American NBS BIOFLO 310 basket bioreactor, the reactor tank is 14L, the effective volume is 10L, and 300g Fibra Disk carrier is added.

[0062] Cell growth medium: RPMI-1640 medium 94% bovine serum 6%.

[0063] Cell maintenance solution: the volume fraction of RPMI-1640 culture medium is 99%, and the volume fraction of bovine serum is 1%.

[0064] Expansion of host cells in basket reactors

[0065] Load 300 g of Fibra Disk carriers into the carrier basket of the basket reactor, add PBS solution until the carriers are completely soaked in the PBS solution, and sterilize at 121° C. for 45 minutes. After emptying the PBS solution, add sterile cell growth solution until it covers the paddle of the basket stirring paddle. Set the parameters of the reactor before inoculation, including temperature 37°C, dissolved oxygen 50%, pH 7.0, stirring paddle speed 60 rpm, ventilation rate 0.3L / min, etc. After the parameters are sta...

Embodiment 3

[0072] The difference from Example 1 is:

[0073] Reactor: American NBS BIOFLO 510 basket bioreactor, the reactor tank is 40L, the effective volume is 30L, and 1200g Fibra Disk carrier is installed.

[0074] Cell growth medium: RPMI-1640 culture medium 96% bovine serum 4%.

[0075] Cell maintenance solution: the volume fraction of RPMI-1640 culture medium is 99.5%, and the volume fraction of bovine serum is 0.5%.

[0076] Expansion of host cells in basket reactors

[0077] Load 1200 g of Fibra Disk carriers into the carrier basket of the basket reactor, add PBS solution until the carriers are completely soaked in the PBS solution, and sterilize at 121° C. for 45 minutes. After emptying the PBS solution, add sterile cell growth solution until it covers the paddle of the basket stirring paddle. Set the parameters of the reactor before inoculation, including temperature 37°C, dissolved oxygen 60%, pH 7.3, stirring paddle speed 70 rpm, ventilation rate 1.0L / min, etc. After the ...

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PUM

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Abstract

The invention discloses a method for preparing porcine circovirus through basket reactor fermentation. The method for preparing the porcine circovirus through the basket reactor fermentation is characterized by comprising the following steps: (1), preparing the host cell species; (2), preparing a basket reactor before inoculation; (3), performing host cell propagating culture; and (4), performing virus proliferating culture: emptying cell growing liquid in the reactor, supplementing cell maintaining liquid with the volume equal to that of the emptied cell growing liquid, inoculating the porcine circovirus, 36-48h after inoculation, harvesting a virus solution for the first time, after harvesting the virus solution, adding the cell maintaining liquid with the volume equal to that of the harvested virus solution into the reactor, propagating, reproducing, and harvesting the virus again, circularly repeating for multiple times until the sugar consumption of cells in the virus solution to be harvested is detected to be reduced down to 0.5g / L / day, and harvesting the last porcine circovirus solution in the batch. The method is simple and feasible; and by the method, the production cost can be greatly reduced, the unit titer of a porcine circovirus antigen is significantly improved, and the harvest of the virus solution antigen in each fermentation batch is increased.

Description

technical field [0001] The invention relates to a production method for large-scale amplification of porcine circovirus, in particular to a method for preparing porcine circovirus by fermenting in a basket reactor. Background technique [0002] Porcine circovirus (PCV) can be divided into two types according to serotype: porcine circovirus type I (abbreviated as PCV1) and porcine circovirus type II (abbreviated as PCV2). PCV1 is not pathogenic but can produce Serum antibodies, PCV2 can have a strong susceptibility to pigs, and it is the cause of weaned piglet multisystem wasting syndrome (PMWS), porcine respiratory disease syndrome (PRDC), porcine skin and nephrotic syndrome (PDNS), etc. The main pathogen of the disease, PCV has 7 open reading frames (ORFs), among which ORF2 encodes the Cap protein of the virus, which constitutes the nucleocapsid of the virus. There is a common antigenic determinant on the Cap protein of PCV1 and PCV2, but there is no antigenic cross-reacti...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C12N7/00C12N7/02C12N5/07
Inventor 赵立民周庆丰宋延华蒋天华罗乃杰
Owner WENS FOODSTUFF GRP CO LTD
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