Tscheliessnig A - Search Results

1

Two-dimensional difference fluorescence gel electrophoresis to verify the scale-up of a non-affinity-based downstream process for isolation of a therapeutic recombinant antibody.

Grzeskowiak JK, Tscheliessnig A, Wu MW, Toh PC, Chusainow J, Lee YY, Wong N, Jungbauer A. Grzeskowiak JK, et al. Among authors: tscheliessnig a. Electrophoresis. 2010 Jun;31(11):1862-72. doi: 10.1002/elps.200900781. Electrophoresis. 2010. PMID: 20506420

2

2-D DIGE to expedite downstream process development for human monoclonal antibody purification.

Grzeskowiak JK, Tscheliessnig A, Toh PC, Chusainow J, Lee YY, Wong N, Jungbauer A. Grzeskowiak JK, et al. Among authors: tscheliessnig a. Protein Expr Purif. 2009 Jul;66(1):58-65. doi: 10.1016/j.pep.2009.01.007. Protein Expr Purif. 2009. PMID: 19367714

3

Two-dimensional fluorescence difference gel electrophoresis for comparison of affinity and non-affinity based downstream processing of recombinant monoclonal antibody.

Grzeskowiak JK, Tscheliessnig A, Toh PC, Chusainow J, Lee YY, Wong N, Jungbauer A. Grzeskowiak JK, et al. Among authors: tscheliessnig a. J Chromatogr A. 2009 Jun 12;1216(24):4902-12. doi: 10.1016/j.chroma.2009.04.014. Epub 2009 Apr 9. J Chromatogr A. 2009. PMID: 19423113

4

Host cell protein analysis in therapeutic protein bioprocessing - methods and applications.

Tscheliessnig AL, Konrath J, Bates R, Jungbauer A. Tscheliessnig AL, et al. Biotechnol J. 2013 Jun;8(6):655-70. doi: 10.1002/biot.201200018. Epub 2013 Feb 22. Biotechnol J. 2013. PMID: 23436780 Review.

5

Economics of recombinant antibody production processes at various scales: Industry-standard compared to continuous precipitation.

Hammerschmidt N, Tscheliessnig A, Sommer R, Helk B, Jungbauer A. Hammerschmidt N, et al. Among authors: tscheliessnig a. Biotechnol J. 2014 Jun;9(6):766-75. doi: 10.1002/biot.201300480. Epub 2014 Apr 4. Biotechnol J. 2014. PMID: 24706569

6

Ethanol precipitation for purification of recombinant antibodies.

Tscheliessnig A, Satzer P, Hammerschmidt N, Schulz H, Helk B, Jungbauer A. Tscheliessnig A, et al. J Biotechnol. 2014 Oct 20;188:17-28. doi: 10.1016/j.jbiotec.2014.07.436. Epub 2014 Aug 1. J Biotechnol. 2014. PMID: 25087738 Free article.

7

Comparison of protein A affinity sorbents II. Mass transfer properties.

Hahn R, Bauerhansl P, Shimahara K, Wizniewski C, Tscheliessnig A, Jungbauer A. Hahn R, et al. Among authors: tscheliessnig a. J Chromatogr A. 2005 Nov 4;1093(1-2):98-110. doi: 10.1016/j.chroma.2005.07.050. Epub 2005 Oct 5. J Chromatogr A. 2005. PMID: 16233875

8

High-performance monolith affinity chromatography for fast quantitation of immunoglobulin G.

Tscheliessnig A, Jungbauer A. Tscheliessnig A, et al. J Chromatogr A. 2009 Mar 27;1216(13):2676-82. doi: 10.1016/j.chroma.2008.07.063. Epub 2008 Jul 26. J Chromatogr A. 2009. PMID: 18703200

9

Adaptation of hybridomas to protein-free media results in a simplified two-step immunoglobulin M purification process.

Lee J, Tscheliessnig A, Chen A, Lee YY, Adduci G, Choo A, Jungbauer A. Lee J, et al. Among authors: tscheliessnig a. J Chromatogr A. 2009 Mar 27;1216(13):2683-8. doi: 10.1016/j.chroma.2008.10.067. Epub 2008 Oct 21. J Chromatogr A. 2009. PMID: 18992891

10

Dispersion effects in preparative polymethacrylate monoliths operated in radial-flow columns.

Hahn R, Tscheliessnig A, Bauerhansl P, Jungbauer A. Hahn R, et al. Among authors: tscheliessnig a. J Biochem Biophys Methods. 2007 Feb 23;70(1):87-94. doi: 10.1016/j.jbbm.2006.09.005. Epub 2006 Sep 22. J Biochem Biophys Methods. 2007. PMID: 17070924

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