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A method for depletion or removal of endotoxin from an endotoxin-containing source or potentially endotoxin-containing source

A technology of endotoxin, source, applied in the field of fractionation

Pending Publication Date: 2021-07-23
ビーアイエーセパレーションズディーオーオー
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The net effect is that an additional purification step is required

Method used

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  • A method for depletion or removal of endotoxin from an endotoxin-containing source or potentially endotoxin-containing source
  • A method for depletion or removal of endotoxin from an endotoxin-containing source or potentially endotoxin-containing source
  • A method for depletion or removal of endotoxin from an endotoxin-containing source or potentially endotoxin-containing source

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0112] Experimental controls were prepared to provide a baseline for recording the relative effectiveness of the invention.

[0113] 10 mL of a clarified harvest of E. coli cell culture containing phage T4 was partially purified by hydrophobic interaction chromatography (HIC). With 50mM Tris, 1mM CaCl 2 , 0.5mM MgCl 2 , 20mM NaCl, 10% glycerol, pH7.7, and the final conductivity was 7.42mS / cm to elute HIC to obtain the phage elution peak. 100 μL CIMmac Qa (strong anion exchange) monolith (BIA Separations) was washed with 50 mM Tris, 1 mM CaCl 2 , 0.5mM MgCl 2 , 20mM NaCl, 10% glycerol, pH7.7 balance. Load the diluted phage onto the QA monolithic column. Wash the monolithic column with 60 bed volumes of equilibration buffer, then elute with a 50 bed volume (5 mL) linear gradient to 50 mM Tris, 1 mM CaCl 2 , 0.5mM MgCl 2 , 2M NaCl, 10% glycerol, pH 7.7. The column was cleaned and disinfected with 1M sodium hydroxide and 2M sodium chloride. Fractions were collected throug...

Embodiment 2

[0114] Embodiment 2 (comparison)

[0115] Endotoxin reduction experiments were performed initially with hydrophobic interaction chromatography (HIC) followed by IDA-Fe, a negatively charged chelating ligand (CIM IDA, BIA Separations). HIC was performed on T4 phage harvest as described in Example 1, but on a larger scale, with 160 mL of lysate loaded onto an 8 mL HIC monolithic column. The endotoxin content of 31mL eluted fraction was 138,167EU / mL. The fraction was treated with 20nM KH 2 PO 4 , 10% glycerol, pH 7.0 diluted to a final conductivity of 6.7mS / cm. A 340 μL IDA monolithic column was prepared by washing with 20 Cv deionized water; then 20 CV 100 mM acetic acid, pH 3.0; 20 CV 200 mM ferric chloride, then 20 CV 50 mM acetic acid, 2.0 M sodium chloride, pH 4.5; 20 Cv deionized water. The column was then equilibrated to 20 mM potassium phosphate, 10% glycerol, pH 7.0. Dilute 2(2) mL of the fraction from HIC with 40 mL of mobile phase A to a conductivity of 6.7 mS / c...

Embodiment 3

[0117] Experiments show that the experimental monolithic column produced by BIASeparations immobilized ferric ions on the solid surface of tris(2-aminoethyl)amine (TREN) achieves a higher yield compared with strong anion exchangers (CIMmultus QA, BIA Separations). Good endotoxin reduction.

[0118] HIC was performed on T4 phage harvests as described in Example 2. Endotoxin detection showed that the endotoxin content of the phage fraction was 138167EU / ml. Dilute 2 mL of the fraction from HIC with 40 mL of mobile phase A to give a final conductivity of 9.3 mS / cm. A 1 ml TREN monolithic column was prepared as described in Example 2 by running reagents on it at a flow rate of 5 CV / min. The column was equilibrated with 20 mM potassium phosphate (pH 7.0). 40 mL of the diluted sample was loaded, and the column was washed with 15 CV of 20 mM potassium phosphate, pH 7.0. The column was eluted with a 20CV linear gradient with an endpoint of 500 mM potassium phosphate, pH 7.0. Fract...

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Abstract

A method for depletion or removal of endotoxins from a known or suspected endotoxin-containing source by virtue of a solid phase extraction material in an essentially aqueous system comprising the steps of providing a known or suspected endotoxin-containing source, contacting the known or suspected endotoxin-containing source with a positively charged solid phase material having a surface on which ferric iron is immobilised, wherein the solid phase extraction material has immobilised the ferric iron by (2-aminoethyl)amine (TREN) ligand incubating the known or suspected endotoxin-containing source for a period of time sufficient to bind endotoxin to the porous solid phase material, separating the solid phase material from the essentially aqueous system, optionally isolating the essentially aqueous system freed or depleted from endotoxin.

Description

[0001] The present invention relates to methods for the removal or removal of endotoxins from endotoxin-containing sources and various fields in which the methods of the invention can be applied, as well as fractions obtainable by the methods of the invention. Background technique [0002] Lipopolysaccharide (Lipopolysaccahrides, LPS) is a cell wall component of Gram-negative bacteria. When such bacteria die and degrade, LPS, also known as endotoxin, is shed into the surrounding environment. Endotoxin is stable and can persist for a long time even under harsh conditions. Endotoxins are a concern for the biopharmaceutical industry because of their high toxicity. Even amounts as low as a few parts per million can cause a febrile reaction. Larger doses can cause organ failure and death. [0003] Potential sources of endotoxins in bioprocessing include the following: [0004] -Some products grow in Gram-negative bacteria. Therefore, they are contaminated with large amounts of...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C12Q1/24C07K1/22C07K1/18C07K1/20C07K1/36C12N7/00C12N7/02
CPCC07K1/18C07K1/20C07K1/22C07K1/36C12N7/00C12N2795/10151C12Q1/24B01D15/327B01D15/34B01D15/363
Inventor P·S·加农L·雷布拉
Owner ビーアイエーセパレーションズディーオーオー