Purification of capsular polysaccharides
AssigneeVaxcyte, Inc.
InventorsPeter T. Davey, Marc Wong, Kathleen Ma, Brian Fennell
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Abstract
Described herein are methods of purifying various S. pneumoniae serotype capsular polysaccharides from cell lysates, which improve the yield of polysaccharides while minimizing the amount of Host Cell Protein (HCP) in the product.
Claims23
A process of purifying a capsular polysaccharide cell lysates to produce a purified polysaccharide, the process comprising the steps of:
- (a) flowing a crude capsular polysaccharide cell lysate through a carbon filter wherein the carbon filter is loaded at a load capacity of three times the specified load capacity for the carbon filter;
- and
- (b) flowing a resulting solution from step (a) through a ceramic hydroxyapatite column wherein the ceramic hydroxyapatite column is loaded at fifty percent load capacity.
The process of claim 8, wherein the first set of depth filters of step (a) having a pore size ranging from about 0.2 microns to about 0.45 microns.
A process of purifying a capsular polysaccharide cell lysate to produce a purified polysaccharide, the process comprising the steps of:
- a) passing the capsular polysaccharide cell lysates through at least one depth filter placed in series resulting in a depth filtered polysaccharide;
- b) introducing the depth filtered polysaccharide onto a first tangential flow filtration (TFF) resulting in a first TTF purified polysaccharide;
- c) precipitating the first TTF purified polysaccharide with a cationic surfactant resulting in a cationic surfactant purified polysaccharide;
- d) mixing the cationic surfactant purified polysaccharide with a solution of potassium iodide (KI) resulting in a KI purified polysaccharide that is in solution;
- e) flowing the KI purified polysaccharide through a carbon filter, wherein the KI purified polysaccharide is loaded at three times load capacity specified for the carbon filter resulting in a carbon filter purified polysaccharide;
- f) flowing the carbon filter purified polysaccharide through a ceramic hydroxyapatite column resulting in a ceramic hydroxyapatite purified polysaccharide, wherein the ceramic hydroxyapatite column is used at a fifty percent load capacity specified for the ceramic hydroxyapatite's column size;
- g) flowing the ceramic hydroxyapatite purified polysaccharide through a hydrophobic interaction (HI) chromatography column resulting in a HI purified polysaccharide;
- and
- h) flowing the HI purified polysaccharide through a second TFF process to obtain a resulting final purified polysaccharide with an overall yield of at least 30%.
Dependencies are inferred from the claim text.