Hydrolysis technology for protease of heparin sodium
A technology of protease hydrolysis and heparin sodium, which is applied in the field of protease hydrolysis of heparin sodium, can solve the problems of slow speed and low extraction rate of heparin sodium, and achieve the effects of large waste of raw materials, high yield and improved production efficiency
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Embodiment 1
[0009] Select 500g of porcine small intestinal mucosal fluid with a salinity of 4 degrees, add NAOH, adjust its pH to 9, stir and heat up to 55°C, keep warm for 30 minutes, add alkali according to the small intestinal mucosa:alkaline protease weight ratio of 500:0.1 Protease, keep warm for 2 hours, after adding alkaline protease, intervene in ultrasound, specifically: the wavelength of ultrasound is 25Hz, and the power density is 0.5-0.7 W / cm 2 The supersonic wave was intervened once at the beginning and end of the enzymatic hydrolysis, and each treatment was 0.5h. After enzymolysis, conventional resin adsorption, elution, alcohol lake, and drying are used to obtain heparin sodium with a yield of 90% and a potency of 105U / mg. In this production, due to the reduction of the amount of NaCl, the amount of wastewater The reduction of 200 g per 1T of small intestine is achieved, which achieves the production goals of high efficiency, high yield and environmental protection.
Embodiment 2
[0011] Pump 200 pieces of pig small intestine mucosa and water with a salinity of 3.5 degrees in a 1000-liter reactor. The weight ratio of pig small intestine and water is 3:1. Add NAOH to adjust its pH to 9, stir and heat up to 55°C , after 30 minutes of heat preservation, according to the small intestinal mucosa: alkaline protease weight ratio of 500g: 0.1, add alkaline protease and keep warm for 2 hours. W / cm 2 The supersonic wave was intervened once at the beginning and end of the enzymatic hydrolysis, and each treatment was 0.5h. After enzymolysis, conventional resin adsorption, elution, alcohol lake, and drying are used to obtain heparin sodium with a yield of 91% and a potency of 106U / mg. In this production, due to the reduction of the amount of NaCl, the amount of wastewater The reduction of 300g per 1T small intestine is achieved, achieving the production goals of high efficiency, high yield and environmental protection.
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