A method for simultaneously preparing crude human urinary kininogenase and crude human urinary trypsin inhibitor
A technology of urinary kallikrein and urinary trypsin, which is applied in the directions of biochemical equipment and methods, peptidase, enzyme, etc., can solve the problems of unfavorable industrial production, low KN yield, etc., and achieves convenient purification treatment and reduced production cost. , the effect of improving the purification rate
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Embodiment 1
[0032] S1 Place 100 kg of strong base anion exchange resin as an adsorbent in a urine tank or urinal, and collect the strong base anion exchange resin that has absorbed urine protein;
[0033] S2 elutes the strong base anion exchange resin obtained in step S1 with a NaCl solution whose concentration is 0.72mol / L, and collects the eluent;
[0034] S3 Concentrate the eluate obtained in step S2 by ultrafiltration, adjust the pH value of the ultrafiltration concentrate to 3.9, and the conductivity to 2.3Ms / cm;
[0035] S4 load the concentrated solution obtained in step S3 onto the strong-acid cation exchange resin that has been balanced with the balance solution, wash it with 0.1mol / L acetic acid-sodium acetate buffer solution, the conductivity is 3Ms / cm, and the pH value is 3.9. The equilibrium solution of the strong acid type cation exchange resin is 0.1mol / L acetic acid-sodium acetate buffer solution, the conductance is 2.3Ms / cm, and the pH value is 3.9;
[0036] S5 was eluted...
Embodiment 2
[0039] S1 Place 100 kg of strong base anion exchange resin as an adsorbent in a urine tank or urinal, and collect the strong base anion exchange resin that has absorbed urine protein;
[0040] S2 elutes the strong base anion exchange resin obtained in step S1 with a NaCl solution whose concentration is 0.6mol / L, and collects the eluate;
[0041] S3 Concentrate the eluate obtained in step S2 by ultrafiltration, adjust the pH value of the ultrafiltration concentrate to 3.2, and conductance to 4.3Ms / cm;
[0042]S4 Load the concentrated solution obtained in step S3 onto the strong-acid cation exchange resin that has been balanced with the balance solution, and wash it with 0.3mol / L acetic acid-sodium acetate buffer solution, the conductivity is 4.1Ms / cm, and the pH value is 3.2. , the equilibrium solution of the strong acid type cation exchange resin is 0.3mol / L acetic acid-sodium acetate buffer solution, the conductance is 4.1Ms / cm, and the pH value is 3.2;
[0043] S5 was elute...
Embodiment 3
[0046] S1 Place 100 kg of strong base anion exchange resin as an adsorbent in a urine tank or urinal, and collect the strong base anion exchange resin that has absorbed urine protein;
[0047] S2 elutes the strong base anion exchange resin obtained in step S1 with a NaCl solution whose concentration is 0.8mol / L, and collects the eluate;
[0048] S3 Concentrate the eluate obtained in step S2 by ultrafiltration, adjust the pH value of the ultrafiltration concentrate to 4.2, and conductance to 1.3Ms / cm;
[0049] S4 Apply the concentrated solution obtained in step S3 to the strong-acid cation exchange resin that has been balanced with the balance solution, and wash it with 0.02mol / L acetic acid-sodium acetate buffer solution, the conductivity is 1.2Ms / cm, and the pH value is 4.2. , the equilibrium solution of the strong acid type cation exchange resin is 0.02mol / L acetic acid-sodium acetate buffer solution, the conductance is 1.2Ms / cm, and the pH value is 4.2;
[0050] S5 was elu...
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