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418 results about "Growth phase" patented technology

Growth phase. A phase in the life cycle of an industry when companies move beyond the startup phase into a phase of increased competition for market share.

Ethanol production with dilute acid hydrolysis using partially dried lignocellulosics

In a process for converting lingnocellulosic biomass to ethanol, the improvement of obtaining higher fermentable soluble sugar yields by drying acid impregnated biomass particles, comprising: a) feeding moist lignocellulosic biomass into an acid impregnator to render it acid-soaked and draining the acid-soaked biomass to about 30% to 35% by weight solids; b) dewatering the acid-soaked biomass by drying or centrifugation to prevent compaction of the biomass and arrive at about 40% to 60% by weight solids; c) subjecting the acid-impregnated biomass to a first-stage hydrolysis reactor at a temperature of from 130° C. to 220° C. and discharging formed hydrolysate into a flash tank at about 120° C. to 140° C. to hydrolyze most of the remaining soluble oligosaccharides to monomeric sugars, and flashing remaining hydrolysate to a second flash tank at a lower temperature than the first flash tank-the second flash tank serving as a feed surge tank for a counter-current extractor; d) washing the hydrolysate, adjusting the pH of the sugar extract to about 5, and recovering more than 95% of the soluble sugars in the first-stage hydrolysate slurry by a counter-current extractor; e) subjecting remaining washed-first stage solids of pretreated biomass to a second-stage acid and metal salt impregnator and dewatering by drying or centrifugation to prevent compaction of biomass to arrive at 40% to 60% by weight solids; f) subjecting the acid and metal salt-impregnated biomass to a second-stage hydrolysis reactor at a temperature from 190° C. to 240° C. and discharging formed hydrolysate into a flash tank, at about 120° C. to 140° C. to hydrolyze most of the remaining soluble oligosaccharides to monomeric sugars and flashing remaining hydrolysate to a second flash tank at a lower temperature than the first flash tank, the second flash tank serving as a feed surge tank for second-stage fementors; g) cooling pH-adjusted extract from the counter-current extractor, feeding the extract to a first-stage fermentor and air sparging the first-stage fermentor at a rate sufficient to promote enough yeast growth to compensate for loss through second-stage fermentors; h) pH adjusting second-stage hydrolysate slurry to 4.5, cooling the slurry and adding it into the top of the first fermentor of a two-fermentor train in the second stage fermentors, pumping broth from the bottom of the first stage fermentors to the second stage fermentors while the yeast is in the growth phase for a period sufficient to consume over 95% of fermentable sugars; and i) recovering ethanol.
Owner:MIDWEST RES INST

Polypeptide production in animal cell culture

A method of producing a polypeptide in fed batch cell culture is provided which involves an initial cell growth phase and a distinct production phase. In the initial growth stage, animal cells having nucleic acid encoding the polypeptide are cultured at a starting osmolality of about 280-330 mOsm in the presence of a concentration of glucose controlled throughout the culturing to be within a range between about 0.01 and 1 g/L. This is followed by a production phase, where the cultured animal cells of the growth phase are inoculated at a cell seed density of at least 1.0×106 cells/mL and the cells are cultured at a starting osmolarity of about 400-600 mOsm in the presence of a concentration of glucose controlled throughout the culturing to be within a range between about 0.01 and 1 g/L. Preferably, the glutamine concentration in the cell culture medium is simultaneously controlled in order to curtail production of lactic acid and ammonia which result from unnecessarily high glutamine concentrations. During the growth phase, production of potentially detrimental metabolic waste products, such as lactic acid, is controlled thereby curtailing the increase of osmolality due to accumulation and neutralization of waste products. Thus, the cell growth can be improved. In the production phase, the cell culture conditions are modified in order to arrest or reduce cell growth and thereby direct nutrient utilization toward production, as opposed to cell growth. Overall, it is intended that the method results in an improvement in specific productivity, reduction in production run times and/or an increase in final product concentration.
Owner:GENENTECH INC

Visual gas hydrate dynamic experimental device

The invention provides a visual gas hydrate dynamic experimental device. The visual gas hydrate dynamic experimental device comprises a visual electromagnetic stirring reaction still, a voltage stabilizing pre-cooling gas supplying unit, an gas exhaust unit, a liquid charging / discharging unit, a temperature control unit and a data collecting and processing unit, wherein the visual electromagnetic stirring reaction still is used for mixing experimental gas and experimental liquid in the reaction still for reaction to form and decompose hydrate; the voltage stabilizing pre-cooling gas supplying unit and the gas exhaust unit are used for supplying pre-cooling experimental gas for the visual electromagnetic stirring reaction still and discharging gas; the liquid charging / discharging unit is used for injecting the experimental liquid to the visual electromagnetic stirring reaction still or discharging the experimental liquid; the temperature control unit is used for controlling the temperature change of the visual electromagnetic stirring reaction still; the data collecting and processing unit is used for collecting, processing, saving and analyzing kinetic parameters during a hydrate formation and decomposition process. According to the visual gas hydrate dynamic experimental device, numerous defects of a common hydrate dynamic experimental device are overcome, the kinetic properties in a nucleation phase and a growth phase of gas hydrate can be accurately determined, and the experimental device is simple, economical and convenient to operate.
Owner:GUANGZHOU INST OF ENERGY CONVERSION - CHINESE ACAD OF SCI

Large-scale cultivation method and quality detection method of cordyceps militaris fruit bodies

The invention discloses a large-scale cultivation method and a quality detection method of cordyceps militaris fruit bodies, comprising the steps of: (1) screening spawn; (2) preparing a rice solid culture medium (40-55 parts of rice and 45-60 parts of nutrient solution in every 100 parts by weight) and killing bacteria; (3) preparing liquid spawn: activating the spawn, inoculating the spawn into a liquid culture medium, conducting static culture for 24 hours and performing suspension culture on a shaking table; (4) culturing fruit bodies: inoculating the liquid spawn on the solid culture medium for dark culture for 6 days at the temperature of 20 DEG C until the surface of the medium is covered by mycelium; placing the well grown mycelium under incandescence with light intensity of 100 to 300 lux, wherein during a primordium growth phase, illumination is performed for 20-24 hours per day at the temperature of 20-24 DEG C; and during a fruit bodies growth phase, illumination is performed for 8-12 hours per day at the temperature of 18-20 DEG C and the fruit bodies are harvested 5 to 8 days after mature. The cordyceps militaris fruit bodies cultured by the method have the advantages of high yield and high content of active ingredients. Batches of cordyceps militaris fruit bodies have fingerprints with a similarity value greater than 0.950, indicating stable and controllable quality.
Owner:珠海市先康生物科技有限公司

Remote sensing extraction method of agricultural disaster information based on vegetation index time-space statistical characteristics

The invention provides a remote sensing extraction method of agricultural disaster information based on vegetation index time-space statistical characteristics and belongs to the technical field of agricultural disaster information acquisition, aiming at solving the problems that existing agricultural disaster remote sensing monitoring cannot be used for monitoring and evaluating a large-scale region or a long time sequence in the region and a monitoring method has no universality. On the basis of considering that vegetation indexes of different phonological regions, crops and growth phases have difference, an NDVI (Normalized Difference Vegetation Index) of each pixel in the phonological regions with known diseases and an average value NDVIm of the NDVI and a standard difference STD of the same crops are extracted; a relation between the parameters is analyzed by utilizing the statistical characteristics according to NDVI gradation histogram characteristics before and after the disasters and a disaster monitoring model is established; the agricultural disasters are extracted. According to the method provided by the invention, interference factors caused by the growth regions, different crops and growth phases are considered and the precision of a monitoring result is improved. The remote sensing extraction method provided by the invention is used for monitoring the agricultural disasters.
Owner:NORTHEAST INST OF GEOGRAPHY & AGRIECOLOGY C A S

Fermentation method for accelerating ganoderic acids and ganoderma lucidum polysaccharide biological synthesis

The invention discloses a fermentation method for promoting mythic fungus acid or mythic fungus polysaccharide biology to synthesize. The invention investigates the condition which is needed in the growth phase of mythic fungus cell and product synthesis phase, which respectively investigates the influence of control strategies of pH two phases and oxygen dissolution two phases to mythic fungus acid or mythic fungus polysaccharide biology according to unconsistency of environmental conditions which are needed in the phases of mythic fungus cell growth and production synthesis, and the invention respectively investigates the influence to mythic fungus acid or mythic fungus polysaccharide biology synthesis after control strategies of pH two phases and oxygen dissolution two phases or the fed strategy are mutually coordinated together on the basis of combining with an intermediate fed strategy. The test result shows that mythic fungus cells are obviously prompted to grow no matter respectively adopting a pH value two phases control strategy, an oxygen dissolution concentration two phases control strategy, or coordinating the pH value two phases control strategy and the oxygen dissolution concentration two phases control strategy with the fed strategy together, and the content or yield of mythic fungus acid or mythic fungus polysaccharide are greatly improved.
Owner:HUBEI UNIV OF TECH
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