Fill-finish process for peptide solutions

Abstract

The enclosed disclosure describes, among other things, a method including the steps of a first deaerating step in which a mixture comprising peptides is deaerated by lowering the pressure, filtering the mixture through a sterilizing filter; and a second deaerating step, in which the filtrate is deaerated by vibration and lowering the pressure.

1 . A method for deaerating and sterilizing a self-assembling peptide solution having at least 0.5% of a self-assembling peptide, the method comprising the steps of:
 a first deaerating step wherein the self-assembling peptide solution is deaerated by lowering a pressure on the self-assembling peptide solution;   filtering the self-assembling peptide solution through a sterilizing filter; and   a second deaerating step wherein the filtrate is deaerated by vibration at a vibration frequency between 20 and 360 revolutions per minute, and by lowering the pressure on the self-assembling peptide solution by at least 0.05 MPa.   
     
     
         2 . The method of  claim 1 , wherein the sterilizing filter has an average pore size of less than 0.22 μm. 
     
     
         3 . The method of  claim 1 , wherein the self-assembling peptide comprises one of RADA16-I (SEQ ID NO:1), IEIK13 (SEQ ID NO: 39); and KLDL12 (SEQ ID NO: 12). 
     
     
         4 . The method of  claim 1 , wherein the first deaerating step comprises lowering the pressure at a rate of less than 0.01 MPa/min. 
     
     
         5 . The method of  claim 1 , wherein the first deaerating step occurs in a deaeration chamber comprises lowering the pressure by at least 0.095 MPa. 
     
     
         6 . The method of  claim 5 , wherein the pressure is lowered by at least 0.095 MPa for at least 30 minutes. 
     
     
         7 . The method of  claim 1 , wherein an eccentric distance of the vibration is between −10 cm and 10 cm. 
     
     
         8 . The method of  claim 1 , wherein the second deaerating step comprises lowering the pressure by at least 0.095 MPa. 
     
     
         9 . The method of  claim 1 , wherein step of sterilizing is performed with one of ethylene oxide gas and a hydrogen peroxide gas. 
     
     
         10 . The method of  claim 1 , wherein the filtration is performed at a pressure of at least 0.5 MPa. 
     
     
         11 . The method of  claim 1 , wherein the filter is constructed from a material selected from the group consisting of the following: cellulose nitrate, cellulose acetate, vinyl polymers, fluorocarbons, polyethylene, ultrahigh molecular weight polyethylene, polypropylene, EVA copolymers and alpha olefins, metallocene olefinic polymers, PFA, MFA, PTFE, polycarbonates, vinyl copolymers, polyamides, nylon, polyesters, cellulose, cellulose acetate, regenerated cellulose, cellulose composites, polysulfone, polyethersulfone, polyarylsulfone, polyphenylsulfone, polyacrylonitrile, polyvinylidene fluoride (PVDF), and blends thereof. 
     
     
         12 . The method of  claim 1 , wherein the filter is constructed from polyethersulfone. 
     
     
         13 . The method of  claim 1 , wherein the filtering step comprises a step of filling the filter at a first pressure, then increasing the pressure to perform the filtration. 
     
     
         14 . The method of  claim 1 , wherein the filter is washed prior to an integrity test. 
     
     
         15 . The method of  claim 14 , wherein the filter is washed with water prior to an integrity test, and the water is one of above 70° C. and high-pressure, or both. 
     
     
         16 . The method of  claim 1 , wherein the filtration step is performed with two filters operating in parallel.