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62
results.
Updated on
01/09/2024 [06:46:00]
Results 50 to 62 of 62
Absstract of: US2024263199A1
The present disclosure discloses a method for improving production of L-lactic acid (L-LA) by Saccharomyces cerevisiae based on regulation and control of ethanol metabolic flux, and belongs to the technical field of microorganisms. According to the present disclosure, acid-resistant Saccharomyces cerevisiae TJG16 is used as a production strain, an ethanol dehydrogenase gene adhA derived from Bacillus subtilis is introduced to promote conversion of ethanol into acetaldehyde, and a lactate aldolase gene BAL derived from Brucella sp. is introduced to promote synthesis of lactic acid from the acetaldehyde. Moreover, an acetaldehyde dehydrogenase gene ALD6 is knocked out to prevent synthesis of acetic acid from the acetaldehyde, a transcriptional regulatory factor encoding gene GAL80 for regulating and controlling galactose is knocked out, and lactate dehydrogenase LDH is integrated, so that the L-LA is finally increased.
Absstract of: US2024263092A1
A biomass waste processor combining torrefaction and pyrolysis of biomass waste products operating at fixed temperatures via electric heating elements.
Absstract of: US2024263182A1
Genetically modified microorganisms that have the ability to convert carbon substrates into chemical products such as 2,3-BDO are disclosed. For example, genetically modified methanotrophs that are capable of generating 2,3-BDO at high titers from a methane source are disclosed. Methods of making these genetically modified microorganisms and methods of using them are also disclosed.
Absstract of: US2024263110A1
Systems and methods for fractionating whole stillage from an ethanol production facility are provided. Whole stillage undergoes a separation of its liquid portion (thin stillage) from the solid portion (fiber cake). In some embodiments, the solids and liquids in whole stillage may be separated utilizing a screening centrifuge. The fiber cake may be dried to generate a high fiber animal feed. The thin stillage may be provided to a three-phase separator for separation into an oil emulsion, an aqueous clarified stillage, and a protein paste. The protein paste may be dried to generate a high protein animal feed with greater than about 45% protein content. The clarified thin stillage is condensed to yield a syrup with greater than around 60% solids. The oil emulsion is subjected to a pH adjustment to liberate the oil from the emulsion, which is then separated.
Absstract of: AU2022354093A1
The present invention relates to an aqueous fermentation medium comprising sulphur in the form of at least one thiocarboxylate, wherein the thiocarboxylate has a chemical structure of Formula I and R= H, alkyl, COOH, COSH, and wherein the alkyl groups may also contain OH, COSH and/or COOH and wherein the concentration of the thiocarboxylate is 2 to 20 mg/L in the fermentation medium.
Absstract of: EP4410973A1
Provided are a recombinant yeast for producing lacto-N-triose, and an application thereof, belonging to the bioengineering field. The recombinant yeast comprises an amino acid sequence of a β-N-acetylglucosaminyl transferase and a coding nucleic acid sequence thereof, and/or a disruption of a marker gene. The technical solution of the present invention has the advantages of easy availability of raw materials, simple and feasible method, suitable for industrial production, and excellent application prospects.
Absstract of: AU2022349006A1
A thermochemical energy conversion unit includes a heat expansion assembly including a reactor configured to receive a biomass and convert the biomass into a burnable gas having undesirable materials therein and a biochar. The heat expansion assembly also includes a heat expansion discharge pipe configured to discharge the burnable gas from the heat expansion assembly. The thermochemical energy conversion unit also includes a gas scrubber assembly operatively connected to the heat expansion assembly and configured to receive the burnable gas therefrom and to remove the undesirable materials from the burnable gas. The gas scrubber assembly includes a scrubber discharge pipe configured to discharge the burnable gas from the gas scrubber assembly. The heat expansion assembly and the gas scrubber assembly are configured to be continuously fluidly connected from the heat expansion discharge pipe to the scrubber discharge pipe for generating a continuous flow of the burnable gas therealong.
Absstract of: CN221472046U
本实用新型公开了一种生物燃料颗粒成型机，包括底部支撑架、防护箱、加工筛筒、粉碎组件、吸尘箱和输料筒，所述防护箱设于底部支撑架上，所述加工筛筒设于防护箱内中部，所述粉碎组件设于加工筛筒内，所述吸尘箱对称设于防护箱两侧，所述吸尘箱上设有吸尘管，所述吸尘管延伸至防护箱内，所述吸尘管上设有吸尘头，所述输料筒设于底部支撑架上且位于防护箱下方，所述加工筛筒与输料筒上顶部之间设有导料筒，所述加工筛筒下底部设有出料网板。本实用新型涉及生物燃料颗粒加工设备技术领域，具体为一种具有粉碎和除尘效果的生物燃料颗粒成型机。
Absstract of: CN221484079U
本实用新型涉及生物质能原料处理技术领域，且公开了一种生物质能原料处理装置，包括主体机构、搅拌机构和烘干机构，所述搅拌机构位于主体机构的前方，所述烘干机构位于主体机构的下方，所述主体机构包括装置本体、驱动电机、旋转搅碎刀、活动块、所述驱动电机固定安装在装置本体左端的前后两端，所述旋转搅碎刀固定安装在驱动电机右端的传动端，所述旋转搅碎刀位于装置本体的内部，所述活动块固定安装在装置本体内端的右端。该生物质能原料处理装置，通过对主体机构的安装，使得本实用新型的搅碎能力有所提升，在实际使用过程中，可以快速有效地将原料进行搅碎，便于后续加工作业，提高了该生物质能原料处理装置的实用性。
Absstract of: WO2024158616A1
A method for treating grains having starch and non-starch carbohydrates, wherein the starch is present in an amount of at least 10 wt.% based on the dry weight of the grain. The grain is contacted with a solution containing at least one α-hydroxysulfonic acid; and to react under acid hydrolysis conditions to produce a product that is suitable for producing chemicals and/or fuel.
Absstract of: WO2024156936A1
The application relates to a biochar reactor (100) for producing biochar (BC). The biochar reactor comprises a horizontal reactor chamber (102), a receiver (104) for receiving (472) biomass (BM) to the biochar reactor, a pyrolyser (108) for pyrolysing (480) the received biomass to produce the biochar, a cooler (114) for cooling (488) the produced biochar, and a controller (346) for controlling the biochar reactor. The pyrolyser comprises at least one pyrolyser section (110) so that each pyrolyser section (110) is configured to pyrolyse the biomass by using a unique section-typical temperature range. The biochar reactor is configured to cause heat gas (HG) to flow through each pyrolyser section (110) to pyrolyse the biomass in a process temperature (T1, T2) within the section-typical temperature range in said pyrolyser section (110).
Nº publicación: CN221460298U 02/08/2024
Applicant:
沈阳禾林生物科技有限公司
Absstract of: CN221460298U
本实用新型提供一种碳化稻壳收集装置，涉及一种收集装置技术领域。该实用新型包括底座和碳化箱体，其中，碳化箱体上设置有加热结构，加热结构包括第一加热结构和第二加热结构，收集箱通过连通箱与碳化箱体连通，连通箱上设置有振动器。本实用新型通过设置有两组加热结构，通过六组热风机从两端对碳化箱体进行加热，同时与相应的四组电加热棒相配合，从而实现了将堆积的稻壳搅拌使其碳化的更加全面碳化的更加彻底，提高了工作效率。
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