This paper summarized the pressure control methods used in 16 large-scale production facilities in China for vaccines against foot-and-mouth disease virus and highly pathogenic avian influenza virus.We presented the p...This paper summarized the pressure control methods used in 16 large-scale production facilities in China for vaccines against foot-and-mouth disease virus and highly pathogenic avian influenza virus.We presented the pressure control modes,with their characteristics,of the"constant supply"mode-variable exhaust air volume system and the"constant supply"mode-constant exhaust air volume system.This paper analyzed the influence of common problems(e.g.,pressure reference zero drift,positive pressure reversal and failure to restore the original normal working conditions after working condition conversion)on system stability during pressure control in BSL-3 large-scale production facilities and their solutions,providing references for the design and implementation of similar construction projects under the new situation.展开更多
[Objective] The aim of this study was to develop a simple and effective method for the polysaccharide extraction from Spirulina. [Method] The polysaccha- rides were directly extracted from the fresh algae mat or dry p...[Objective] The aim of this study was to develop a simple and effective method for the polysaccharide extraction from Spirulina. [Method] The polysaccha- rides were directly extracted from the fresh algae mat or dry powder of Spirulina in boiling water. The contents and quality of the extracted polysaccharides were measured. [Result] On average, 236.06 g of polysaccharide was extracted from 25 kg of fresh Spirulina mat, with a yield rate of 0.94%, while 191.95 g of polysac- charide was extracted from 2.5 kg of dry powder of Spirulina with a yield rate of 0.77%. The polysaccharide content in the extract of fresh Spirulina mat was 12.56% （according to glucose content）, while that of the dry powder was 12.38% （according to glucose content）; the glucose was produced during the hydrolysis of Spirulina polysaccharide. [Conclusion] Extraction polysaccharide from Spirulina with boiling wa- ter greatly reduces the use of ethanol, and the possibility of pollution from the ex- ogenous non-food chemical reagents, so that the extracted polysaccharides can be used as food materials. This method makes it possible to establish the production line for Spirulina polysaccharide.展开更多
It was in flask optimization tests proved that 2% serum, pH 7.0, 5:10 000 inoculation concentration of infectious bursal disease virus (IBDV) and 108 hours cultivation for IBDV harvest after its inoculation were the o...It was in flask optimization tests proved that 2% serum, pH 7.0, 5:10 000 inoculation concentration of infectious bursal disease virus (IBDV) and 108 hours cultivation for IBDV harvest after its inoculation were the optimal conditions when IBDV was propagated on Vero cells. 250 ml self-made spinner bottle and 5 L stirring fermentor tests proved that IBDV could maintain higher liters for a long time and the highest liters of IBDV in a spinner bottle and a fermentor were 8.875 and 8.58 ( - lgTCID50/0.1 ml) respectively when IBDV was proliferated on Vero cells using 2 g/L microcarriers in a spinner bottle and a fermentor and was cultivated under the optimum conditions obtained from flask tests after Vero cells had developed a confluent monolayer on microcarriers, which were at least one titer higher than the highest titer in the traditional rolling bottle. All these results suggested that this technology could be applied to large scale production for IBDV.展开更多
基金supported and financially funded by the National Key R&D Program of China:Source identification,monitoring and integrated control of indoor microbial contamination(No.2017YFC0702800).
文摘This paper summarized the pressure control methods used in 16 large-scale production facilities in China for vaccines against foot-and-mouth disease virus and highly pathogenic avian influenza virus.We presented the pressure control modes,with their characteristics,of the"constant supply"mode-variable exhaust air volume system and the"constant supply"mode-constant exhaust air volume system.This paper analyzed the influence of common problems(e.g.,pressure reference zero drift,positive pressure reversal and failure to restore the original normal working conditions after working condition conversion)on system stability during pressure control in BSL-3 large-scale production facilities and their solutions,providing references for the design and implementation of similar construction projects under the new situation.
文摘[Objective] The aim of this study was to develop a simple and effective method for the polysaccharide extraction from Spirulina. [Method] The polysaccha- rides were directly extracted from the fresh algae mat or dry powder of Spirulina in boiling water. The contents and quality of the extracted polysaccharides were measured. [Result] On average, 236.06 g of polysaccharide was extracted from 25 kg of fresh Spirulina mat, with a yield rate of 0.94%, while 191.95 g of polysac- charide was extracted from 2.5 kg of dry powder of Spirulina with a yield rate of 0.77%. The polysaccharide content in the extract of fresh Spirulina mat was 12.56% （according to glucose content）, while that of the dry powder was 12.38% （according to glucose content）; the glucose was produced during the hydrolysis of Spirulina polysaccharide. [Conclusion] Extraction polysaccharide from Spirulina with boiling wa- ter greatly reduces the use of ethanol, and the possibility of pollution from the ex- ogenous non-food chemical reagents, so that the extracted polysaccharides can be used as food materials. This method makes it possible to establish the production line for Spirulina polysaccharide.
文摘It was in flask optimization tests proved that 2% serum, pH 7.0, 5:10 000 inoculation concentration of infectious bursal disease virus (IBDV) and 108 hours cultivation for IBDV harvest after its inoculation were the optimal conditions when IBDV was propagated on Vero cells. 250 ml self-made spinner bottle and 5 L stirring fermentor tests proved that IBDV could maintain higher liters for a long time and the highest liters of IBDV in a spinner bottle and a fermentor were 8.875 and 8.58 ( - lgTCID50/0.1 ml) respectively when IBDV was proliferated on Vero cells using 2 g/L microcarriers in a spinner bottle and a fermentor and was cultivated under the optimum conditions obtained from flask tests after Vero cells had developed a confluent monolayer on microcarriers, which were at least one titer higher than the highest titer in the traditional rolling bottle. All these results suggested that this technology could be applied to large scale production for IBDV.
