Robert Olmsted - Chapel Hill NC Paula Keith - Holly Springs NC Sergey Dryga - Chapel Hill NC Ian Caley - Durham NC Maureen Maughan - Durham NC Robert Johnston - Chapel Hill NC Nancy Davis - Chapel Hill NC Ronald Swanstrom - Chapel HIll NC
Assignee:
Alphavax, Inc. - Research Triangle Park NC University of North Carolina at Chapel Hill - Chapel Hill NC
The present invention provides methods and compositions comprising a population of alphavirus replicon particles comprising two or more isolated nucleic acids selected from 1) an isolated nucleic acid encoding an env gene product or an immunogenic fragment thereof of a human immunodeficiency virus, 2) an isolated nucleic acid encoding a gg gene product or an immunogenic fragment thereof of a human immunodeficiency virus, wherein the gg gene product or immunogenic fragment thereof is modified to inhibit formation of virus-like particles containing the gg gene product or the immunogenic fragment thereof and their release from a cell, and 3) an isolated nucleic acid encoding a pol gene product or an immunogenic fragment thereof of a human immunodeficiency virus, wherein the pol gene product or immunogenic fragment thereof is modified to inhibit protease, integrase, RNase H and/or reverse transcriptase activity, and wherein the nucleic acids are each contained within a separate alphavirus replicon particle.
Alphavirus Vectors And Virosomes With Modified Hiv Genes For Use As Vaccines
Robert Olmsted - Chapel Hills NC, US Paula Keith - Holly Springs NC, US Sergey Dryga - Chapel Hill NC, US Ian Caley - Durham NC, US Maureen Maughan - Durham NC, US Robert Johnston - Chapel Hill NC, US Nancy Davis - Chapel Hill NC, US Ronald Swanstrom - Chapel Hill NC, US
The present invention provides methods and compositions comprising a population of alphavirus replicon particles comprising two or more isolated nucleic acids selected from 1) an isolated nucleic acid encoding an env gene product or an immunogenic fragment thereof of a human immunodeficiency virus, 2) an isolated nucleic acid encoding a gag gene product or an immunogenic fragment thereof of a human immunodeficiency virus, wherein the gag gene product or immunogenic fragment thereof is modified to inhibit formation of virus-like particles containing the gag gene product or the immunogenic fragment thereof and their release from a cell, and 3) an isolated nucleic acid encoding a pol gene product or an immunogenic fragment thereof of a human immunodeficiency virus, wherein the pol gene product or immunogenic fragment thereof is modified to inhibit protease, integrase, RNase H and/or reverse transcriptase activity, and wherein the nucleic acids are each contained within a separate alphavirus replicon particle.
Paula M. Keith - Terre Haute IN Wendy Cain - Terre Haute IN
Assignee:
International Minerals & Chemical Corp. - Northbrook IL
International Classification:
C12P 2102 C07K 1300 C12N 121 C12N 1503 C12N 1518
US Classification:
435 694
Abstract:
A high titer fermentation process using transformed Escherichia coli cells carrying a plasmid containing DNA which codes for Somatomedin C is disclosed. Titers of about 900-1000 mg/L have been obtained using the method of the present invention; about two times the titer of prior art processes.
Fermemtation Process For The High Level Production Of Bovine Growth Hormone
Paula M. Keith - West Terre Haute IN Wendy J. Cain - Terre Haute IN
Assignee:
International Minerals & Chemical Corp. - IN
International Classification:
C12P 2102 C12N 1500
US Classification:
435 70
Abstract:
A high density fermentation process for high yield production of bovine growth hormone by transformant E. coli is described. The process employs transformant strains of E. coli containing an expression vector coding for bovine growth hormone under the control of a bacteriophage lambda promoter-operator and a plasmid containing the. lambda. cI857 gene which codes for the temperature-sensitive repressor protein. In the initial growth period, the level of dissolved oxygen in the fermentation medium is maintained at about 20% to 60% saturation and the temperature of the medium is kept at 26. degree. -30. degree. C. Production of bovine growth hormone is then induced by raising the temperature of the medium to at least about 42. degree. C. The temperature is then reduced to about 38. degree. C. to 41. degree. C. to optimize cell growth for the remainder of the induction period, during which the level of dissolved oxygen in the medium is maintained at about 10% to 40% saturation.