Patent classifications
C12N2500/05
Chemically defined albumin-free conditions for cardiomyocyte differentiation of human pluripotent stem cells
Methods for generating high-yield, high-purity cardiomyocyte progenitors or cardiomyocytes from pluripotent cells are described. Wnt/β-catenin signaling is first activated in pluripotent cells, by, for example, inhibiting Gsk-3 to obtain a first population of cells. Wnt/β-catenin signaling is then inhibited in the first cell population to induce cardiogenesis. One or more of these steps is performed under defined, albumin-free culture conditions.
Compositions and methods for differentiating stem cells into cell populations comprising beta-like cells
Methods, kits, compositions, and systems are provided for culturing pluripotent stem cells to produce populations of cells comprising beta-like cells (e.g., pancreatic lineage, glucose-responsive, and/or insulin-producing). In particular, culture conditions are provided that result in the generation of beta-like cells from a starting culture of human pluripotent stem cells.
Oligopeptide-free cell culture media
The present invention relates to oligopeptide-free cell culture media comprising at least 0.5 mg/L of a polyamine and to methods for cultivating cells in said oligopeptide-free cell culture media comprising at least 0.5 mg/L of a polyamine. The invention also relates to methods for expressing at least one protein in a medium comprising at least 0.5 mg/L of a polyamine and to methods for producing at least one virus in a medium comprising at least 0.5 mg/L of a polyamine.
METHOD OF USING NANO-SIZED MATERIALS FOR ENHANCING PRODUCTION OF SECONDARY METABOLITES IN PLANTS
One aspect of the disclosure is directed to a method for activation/enhancement of cell growth of a plant. The method also stimulates the production of pharmaceutically active metabolites, including alkaloids, in plant cell cultures. The method includes providing a nano-sized material contained agent, and treating the plant with the nano-sized material contained agent to allow sufficient interaction of cells of the plant with the nano-sized material so as to activate/enhance the cell growth of the plant or to stimulate the production of pharmaceutically active metabolites.
Cell culture medium
The present application describes an optimized medium for growth of mammalian cells as well as polypeptide production. The cell culture medium is characterized by a Sow ratio of sodium to potassium ions, it further relates to the method of producing polypeptides using such cell culture media. Sn another aspect, the method of polypeptide production can also comprise a temperature shift and/or a pH-shift to further optimize growth and product yield.
Method of producing oil containing polyunsaturated fatty acids by using <i>Schizochytrium </i>sp
Provided is a method of producing an oil containing polyunsaturated fatty acids by using Schizochytrium sp. The method comprises: performing fermentation using Schizochytrium sp.; resuspending the resultant cells after fermentation in water, adding cellulase and neutral protease for enzymolysis; mixing the enzymatic hydrolyzate with n-hexane, shaking, extracting, centrifuging, and collecting the n-hexane phase; concentrating the n-hexane phase under reduced pressure to remove the n-hexane, and drying to obtain an oil; performing a first crystallization and a second crystallization, and then performing cold filtration to obtain a liquid oil after the second crystallization; and subjecting the liquid oil to deacidification and decolorization. By regulating fermentation conditions and conducting concentration processing on polyunsaturated fatty acids, the content of eicosapentaenoic acid in the Schizochytrium sp. is increased to more than 12%, and the obtained oil is rich in docosahexaenoic acid, docosapentaenoic acid and eicosapentaenoic acid.
METHODS AND SYSTEMS FOR STABILIZATION AND PRESERVATION OF MICROBES
The present disclosure relates to methods of stabilization of microbial compositions comprising combining a population of pre-served microbial cells with at least one water activity scavenger (WAS) to a desired homogeneity level; and packaging and sealing the mixture of preserved microbial cells and the WAS. The present disclosure further relates to the stabilized microbial compositions and uses thereof.
METHODS FOR CULTURING IMMUNE CELLS
The preset disclosure provides methods of culturing TILs in a medium comprising at least about 30 mM to at least about 100 mM potassium ion. In some aspects, the methods disclosed herein enhance expansion of CD8.sup.+ TILs, relative to CD4.sup.+ TILs. In some aspects, the methods further increase the number of less-differentiated cells, e.g., less-differentiated TILs, in the population of cells. In some aspects, the methods disclosed herein enrich for tumor-reactive, e.g., tumor specific, TILs such that clonal diversity is preserved. In some aspects, the cells, e.g., the TILs, are administered to a subject in need thereof.
PROCESS AND COMPOSITION FOR CONTROLLING ETHANOL PRODUCTION
The present invention provides a process for controlling the production of ethanol by microbial fermentation of gaseous substrates. More specifically, a process is provided for controlling ethanol productivity through addition of vitamins. In accordance with the process, vitamins B1, B5 and B7 are added in amounts that increase specific ethanol productivity.
L-isoleucine-producing corynebacterium glutamicum fermentation medium and culture method
Disclosed is a L-isoleucine-producing Corynebacterium glutamicum fermentation medium, comprising a basal medium and a growth factor, wherein the growth factor consists of choline, betaine and vitamin B6, and the contents of each ingredient in the fermentation medium are: 0.2-1 g/L choline, 0.25-0.5 mg/L betaine, and 0.05-0.3 mg/L vitamin B6. Also disclosed is a method for cultivating the L-isoleucine-producing Corynebacterium glutamicum, comprising: inoculating the L-isoleucine-producing Corynebacterium glutamicum onto the fermentation medium, wherein the volume of the bacteria liquid accounts for 5-20% of the volume of the fermentation medium, adjusting the pH to 6.5-7 with aqueous ammonia, controlling the dissolved oxygen to 30-50%, and fermenting for 25-30 h; then decreasing the dissolved oxygen to 15-25%, and feeding a 50-80% glucose solution into the fermentation broth to control the residual sugar at 3-4%, continuing the fermentation until 60-70 hours, then terminating the fermentation, and controlling the temperature of the overall fermentation process at 29-33° C.