Patent classifications
C12Y302/01074
Detecting Xanthan Gum
Detecting xanthan gum in a sampling location includes delivering a tagged polypeptide to the sampling location. The tagged polypeptide includes a polypeptide and a fluorescent probe bound to the polypeptide, such that the fluorescent probe is released from the polypeptide to yield an unbound fluorescent probe when the polypeptide interacts with xanthan gum. Light that excites the unbound fluorescent probe is directed toward the sampling location, and an intensity of fluorescence emitted from the unbound fluorescent probe is assessed, wherein a non-zero intensity is indicative of the presence of xanthan gum in the sampling location. A device for the detection of xanthan gum has a sensing region including the tagged polypeptide, a light source adapted to direct light to the sensing region, the light source adapted to provide one or more wavelengths of light to excite the fluorescent probe, and a detector for detecting fluorescence emitted from the fluorescent probe.
Enzymes Manufactured in Transgenic Soybean for Plant Biomass Engineering and Organopollutant Bioremediation
A strategy for eliminating or greatly reducing the need for physical/chemical treatments or the use of whole microbes for lignocellulosic biomass and organopollutant degradation is disclosed. The soybean is a practical, cost-efficient and sustainable bioreactor for the production of lignin-degrading and cellulose-degrading enzymes. The use of soybean as a transgenic overexpression platform provides advantages that no other industrial scale enzyme expression system can match. Availability of a battery of related plant biomass degrading enzymes in separate transgenic soybean lines provides unprecedented flexibility in industrial and bioremediation processes. Depending upon the particular application, selected soybean-derived powdered enzyme formulations can be used, and their sequential addition can be orchestrated. Manufacturing enzymes using transgenic soybeans wherein these enzymes are capable of lignocellulose and organopollutant degradation into useful or nontoxic products will dramatically change biomass engineering schemes and environmental remediation practices. This technology has a sum of advantages that other protein expression system cannot duplicate, including the manufacturing of individual enzymes in a cost-effective manner that allows flexibility in cocktail composition, ease of application, and long term storage in the absence of a cold chain.
BETA-GLUCOSIDASE EXPRESSING YEAST FOR ENHANCED FLAVOR AND AROMA IN BEVERAGE PRODUCTION
The present disclosure concerns recombinant yeast host cells expressing heterologous enzymes for hydrolyzing flavor compounds glycosidically bound to a sugar molecule. The recombinant yeast host cells can be used in a subsequent production process to make alcoholic beverage products such as wines and beers.
Beta-glucosidase expressing yeast for enhanced flavor and aroma in beverage production
The present disclosure concerns recombinant yeast host cells expressing heterologous enzymes for hydrolyzing flavor compounds glycosidically bound to a sugar molecule. The recombinant yeast host cells can be used in a subsequent production process to make alcoholic beverage products such as wines and beers.
HEMICELLULASE ENRICHED COMPOSITIONS FOR ENHANCING HYDROLYSIS OF BIOMASS
Described are compositions and methods relating to cellulase/hemicellulase enzyme blends for improving the enzymatic hydrolysis of cellulosic and hemicellulosic materials, as commonly found in biomass.
Process for the production of an enzymatic cocktail using solid residues from a process for the biochemical coversion of lignocellulosic materials
The present invention concerns a process for the production of an enzymatic cocktail by submerged culture with a cellulolytic microorganism, comprising two phases: a phase a) for growth of said microorganism in the presence of at least one carbonaceous growth substrate in a closed reactor, said growth phase being carried out with a concentration of carbonaceous growth substrate in the range 10 to 90 g/L; a phase b) for the production of the enzymatic cocktail, in which at least one carbonaceous inducer substrate is supplied, said carbonaceous inducer substrate being at least one solid residue obtained from the step for enzymatic hydrolysis of lignocellulosic materials which have undergone a pre-treatment step, said production phase being carried out with a concentration of carbonaceous production substrate in the range 150 to 400 g/L.
Stable, functional chimeric cellobiohydrolase class I enzymes
The present disclosure relates to CBH I chimera fusion polypeptides, nucleic acids encoding the polypeptides, and host cells for producing the polypeptides.
Oleaginous bacterial cells and methods for producing lipids
This invention relates to cells and methods for producing lipids using cellulosic carbon source. More specifically the invention relates to oleaginous bacterial cells, wherein genes encoding at least one cellulolytic activity has been introduced. This invention also relates to methods for lipid production by cultivating an oleaginous bacterial strain or strains capable of expressing one or more cellulolytic activity.
STABLE, FUNCTIONAL CHIMERIC CELLOBIOHYDROLASE CLASS I ENZYMES
The present disclosure relates to CBH I chimera fusion polypeptides, nucleic acids encoding the polypeptides, and host cells for producing the polypeptides.
PREPARATION METHOD OF PECTIC POLYSACCHARIDE WITH EFFECT OF REGULATING AND CONTROLLING ICE CRYSTAL GROWTH
The present disclosure provides a preparation method of a pectic polysaccharide with an effect of regulating and controlling ice crystal growth, comprising step 1, extracting a pectin crude extract from fruit and vegetable powder; step 2, carrying out branched chain enzymolysis on pectin crude extract to obtain pectin enzymatic hydrolysate; step 3, adding pectin methylesterase and pectin acetylesterase into pectin enzymatic hydrolysate for precise de-esterification enzymolysis; step 4, adding 0.5-2 U/mL of polygalacturonase into pectin enzymatic hydrolysate obtained in step 3, and hydrolyzing for 1.5-2.5 hours; and step 5, collecting precipitate in pectin enzymatic hydrolysate obtained in step 4 to obtain modified pectin. The modified pectin has a purity higher than 90%, a methyl esterification degree of 45-55%, an acetylation degree less than 2%, a neutral sugar content less than 5%, and an average molecular weight of 1.4-7.5 kDa, and obviously reduces an ice crystal size in a freezing process.