Resumen de: WO2025118046A1
The present invention refers to a phosphorous-based composition to be used in ethanol/alcohol production, specifically used in the fermentation step, more particularly, such composition is suitable for improving the yeast metabolism in a fermentation process, thereby, increasing the ethanol yield production, without resulting in increased costs or modifications in the production process. A method for applying said composition in an ethanol process and the use of the composition are also described.
Resumen de: WO2025122608A1
A fuel pellet is disclosed. The fuel pellet comprises a plant fiber and a lignin modifying enzyme exogenous to the plant fiber. In some embodiments, the plant fiber is a Tracheophytes plant fiber. In some embodiments, the plant fiber is a monocot plant fiber. In some embodiments, the plant fiber is a Poaceae plant fiber. In some embodiments, the plant fiber is a Saccharum plant fiber. In some embodiments, the plant fiber is sugarcane bagasse plant fiber. In some embodiments, the pellet does not contain a binding agent. In embodiments without a binding agent, the fuel pellet is held together by lignin, which is present in the plant fiber and modified to hold the plant fibers together. In some embodiments, the lignin modifying enzyme is a lignase. In some other embodiments the lignin modifying enzyme is a laccase. The disclosure further provides a method of making a fuel pellet.
Resumen de: WO2025122763A1
Disclosed herein are processes for separating liquefied grains prior to a fermentation. The described processes enable separation of insoluble biomass solids from soluble carbohydrates to yield at least one biomass solids fraction and at least one carbohydrates-rich fraction. The process involves an initial dilution step where liquefied grains are combined with either water or a recycled soluble matter stream, the latter comprising an aqueous solution of residual carbohydrates recovered from a first bioprocessing stage. The diluted liquid mash undergoes a first fractionation stage involving mechanical processing, yielding two distinct streams: a first retentate stream containing insoluble biomass solids and residual carbohydrates, and a permeate stream containing dissolved carbohydrates. The first retentate stream is then mechanically processed in a first bioprocessing stage, resulting in two outputs: a processed first retentate stream containing the insoluble biomass solids, and the recycled soluble matter stream containing residual carbohydrates. The process culminates in the collection of dissolved carbohydrates and insoluble biomass solids, which constitute the carbohydrates-rich fraction and biomass solids fraction, respectively. These processes provide efficient separation of grain components to yield extremely clean fermentation medium for ethanol and useful biomass solid products untainted by fermentation processes.
Resumen de: US20260308469A1
Improved dry grind systems and methods with front end germ separation for producing one or more sugar (or carbohydrate) streams for biochemical production, such as alcohol. Corn germ, for example, can contain high concentrations of oil and ash, and other impurities that can have negative impacts to unit operations in a dry grind plant. Front end germ separation from a corn flour slurry can provide desirable improvements to dry grind systems and methods. The separated germ/germ fragments can be further subjected to additional processing separate and apart from the further processing of the stream from which the germ was removed, which can produce a more desirable sugar (or carbohydrate) stream due to the reduced amount of undesirable, unfermentable components (e.g., reduced amount of germ) and which may be subjected to liquefaction and eventually fermentation (or other process(es)) such as for biochemical production.
Resumen de: US20260308558A1
Xylanase variants; polynucleotides encoding the variants; nucleic acid constructs, vectors, and host cells comprising the polynucleotides; compositions comprising the xylanase variants and methods of using the variants.
Resumen de: US20260308465A1
0000 Methods, apparatuses, and systems for the conversion of bioalcohol to renewable diesel fuel are disclosed. In an example embodiment, a method includes providing a first bio-alcohol feed stream comprising a first bio-alcohol to a first dehydration reactor and providing a second bio-alcohol feed stream comprising a second bio-alcohol to a second dehydration reactor; dehydrating, in parallel, at least a portion of the first bio-alcohol feed stream to a first alkene process stream in the first dehydration reactor and at least a portion of the second bio-alcohol feed stream to a second alkene process stream in the second dehydration reactor; providing the first alkene process stream to an oligomerization reactor and oligomerizing at least a portion of the first alkene process stream to produce a first olefin process stream; providing the second alkene process stream from the second dehydration reactor to a dimerization reactor and dimerizing at least a portion of the second alkene process stream to produce a second olefin process stream; providing the first and second olefin process streams to a distillation apparatus and separating, via distillation, lighter olefins from longer carbon chain olefins; and hydrogenating at least a portion of the longer carbon chain olefins.
Resumen de: US20260308643A1
A method for producing second-generation bioethanol with a reduced production cost. The method for producing bioethanol, which is a method for producing bioethanol from cellulose, includes: in order, a saccharification step of adding an enzyme to the cellulose for saccharification to obtain a sugar liquid; a step of obtaining a concentrated sugar liquid by concentrating the obtained sugar liquid; a fermentation step of adding yeast to the concentrated sugar liquid for fermentation to obtain hydrous bioethanol; and a concentration step of concentrating the hydrous bioethanol to obtain bioethanol. The method further includes at least one of a step of collecting the enzyme using a ceramic membrane after the saccharification step and a step of collecting unreacted yeast using a ceramic membrane after the fermentation step, and/or in the step of obtaining the concentrated sugar liquid, the sugar liquid is concentrated using a protein-supported polyamide RO membrane.
Resumen de: US20260308644A1
The invention relates to a method for treating waste material. The method comprises the steps of: a. converting the waste material into a slurry, e.g., by adding water; b. adding enzymes to the slurry and allowing the enzymes to extract sugars from the slurry by enzyme saccharification; c. separating the liquid content of the slurry from the solid waste content to give a liquid; d. converting the liquid to an ethanol-water mixture; and e. concentrating or separating the ethanol-water mixture to give ethanol. An apparatus for treating waste material according to the method is also provided.
Resumen de: EP4818292A2
A method for producing lignin pellets is disclosed. The lignin pellets comprise lignin in an amount of 90 - 99.99 weight-% based on the total weight of the lignin pellets. The method comprises providing a lignin powder; mixing an additive with the lignin powder to provide a mixed lignin powder, subjecting the mixed lignin powder to a pelletizing treatment to provide lignin pellets, wherein the lignin pellets have a diameter of 2.5 - 8 mm. Further is disclosed a lignin pellet, a product, and the use of the lignin pellet.
Resumen de: AU2024433554A1
The present invention relates to a pyrolysis plant for batchwise production of biochar by pyrolysis of biomass. The invention further relates to a method of batchwise production of biochar by pyrolysis of biomass using the pyrolysis plant according to the invention. The pyrolysis plant serves for batchwise (discontinuous) production of biochar by pyrolysis of biomass, in particular of plant material, wherein the pyrolysis plant has: - at least one carrier insert for accommodating the biomass, - a drying device (2) for drying the biomass, - a pyrolysis device (3) for the pyrolysis of the biomass dried in the drying device (2) to obtain biochar with exclusion of oxygen or with a low level of oxygen supply, - a conveying device for supplying drying air to the drying device (2), - a heat exchanger (6) for heating the drying air conveyed by the conveying device by means of waste heat from the pyrolysis device (3).
Resumen de: WO2026202207A1
A mobile reactor (1) to convert a batch of biomass into biochar in a batch process. The mobile reactor (1) comprises a pyrolysis chamber (100) for receiving the biomass. A longitudinal axis of the pyrolysis chamber (110) extends from a first end of the pyrolysis chamber (101) to a second end of the pyrolysis chamber (102). In the intended use of the reactor (1), when placed on a ground, the pyrolysis chamber (100) is aligned in such a way that the longitudinal axis of the pyrolysis chamber (110) forms a target angle (a) of 20°-50° to the horizontal, wherein the first end of the pyrolysis chamber (101) is the lowerlying end of the pyrolysis chamber (100).
Resumen de: US20260297550A1
Described are a recombinant host cell, a composition comprising a glucoamylase and methods of saccharifying the starch substrate using the glucoamylase. Moreover, the disclosure also relates to a process of producing fermentation products and a method for increasing starch digestibility in an animal as well as a method of producing a fermented beverage.
Resumen de: US20260297503A1
0000 Disclosed herein are genetically engineered yeast cells capable of producing ethanol. The genetically engineered yeast cells comprise an exogenous polynucleotide sequence encoding a glyceraldehyde-3-phosphate dehydrogenase (gapN) enzyme at least 60%, at least 70%, at least 80%, at least 85%, at least 90%, at least 95%, at least 97%, at least 99%, or 100% identical to at least one of SEQ ID NOs: 28, 32, 48, 52, 64, 68, 80, 92, and 96.
Resumen de: US20260297632A1
Methods of and system for growing and maintaining an optimized/ideal active yeast solution in the yeast tank and fermenter tank during the fermentation filling cycle are provided. A new yeast stage tank is used between the yeast tank and the fermenter tank allowing yeast to rapidly produce a huge amount of active young yeast cells for a fermenter during the filling period. A measurable and useful controlling factor, %DT/%Yeast by weight ratio (or “food” to yeast ratio), is used (e.g., %DT=glucose), which offers information on the health status of the yeast. The controlling factor is used to control the status of the yeast throughout the entire process.
Resumen de: US20260297630A1
0000 The disclosure provides a process for the production of ethanol and one or more low boiling compound from a fermentable carbon source. The ethanol and the low boiling compound(s) are produced using an ethanol-producing yeast modified to further produce the one or more low boiling point compounds. In one embodiment, the low boiling compound(s) are acetone, 1-propanol, and/or 2-propanol. Additionally, the disclosure provides a process for the isolation ad purification of the one or more low boiling compounds from ethanol.
Resumen de: US20260297637A1
A process for enzymatic esterification of free fatty acids. In particular, the present invention relates to a pretreatment process for conversion of free fatty acids in oils and fats as feedstock for base-catalyzed transesterification to produce biodiesel.
Resumen de: US20260297446A1
0000 The invention relates to a device for the treatment of a feedstock, comprising a furnace (301) with an enclosure comprising an inlet (316) and an outlet (304) for the feedstock and an inlet (317) and an outlet (318) for a gas. The device comprises a feedstock recovery system (306) comprising a recovery line (305) connected to the enclosure at the feedstock outlet (304) and comprising a sampling and/or analysis means (319). It comprises two lines in parallel downstream of the sampling and/or analysis means (319), one of the lines being a line leading to a storage tank (308) and another line being a line leading to a port (303) for reintroducing the feedstock into the furnace (301). 0000 The invention also relates to a drying or torrefaction process and to an installation for producing hydrocarbons using the drying or torrefaction device.
Resumen de: US20260297429A1
0000 Described are technologies including processes and system for generation of renewable fuel from nutrient-laden organic waste. The processes described in this specification include processes to convert biomass into a gas using an anoxic gas production process. This output gas can be converted into renewable energy fuels via multiple chemical and/or biological processes.
Resumen de: WO2025109194A2
The present invention refers to an ultrasonic baffled hydrothermal (UBH) reactor for the pretreatment of lignocellulosic biomass, using rotating baffles (180) and blades (182) driven by a motor (73), surrounding heating coils (181) and ultrasonic probes (177, 123). The invention also refers to immobilized cellulase using metal-organic frameworks (MOF). This invention also refers to the counter-current saccharification process. The invention further refers to a thermosiphon which can be used couples with a falling film in a distillation. Additionally, it also refers to a process for producing bioethanol using said UBH reactor, the immobilized cellulase in a counter-current process and a falling film e coupled with the thermosiphon. A system for producing bioethanol comprising the UBH reactor, a saccharification counter-current process, falling films and a thermosiphon is also presented. The uses of the UBH reactor, the enzyme and the thermosiphon are also proposed.
Resumen de: WO2025109537A2
Process for depolymerizing lignocellulosic biomass comprising the following steps: (a) subjecting the lignocellulosic biomass to depolymerization in the presence of at least one alcohol having from 1 to 5 carbon atoms, preferably from 1 to 2 carbon atoms, operating at a weight/weight (w/w) lignocellulosic biomass/alcohol ratio comprised between 0.1 and 1, preferably comprised between 0.15 and 0.8, in supercritical conditions, at a temperature comprised between 200°C and 300°C, preferably comprised between 220°C and 295°C, at a pressure comprised between 40 bar and 170 bar, preferably comprised between 50 bar and 150 bar, for a time comprised between 5 minutes and 150 minutes, preferably comprised between 10 minutes and 130 minutes, obtaining: (i) a mixture comprising a liquid phase comprising depolymerized lignocellulosic biomass and at least one alcohol and a solid phase comprising carbon residues ("char"), depolymerized lignocellulosic biomass and, optionally, non-depolymerized lignocellulosic biomass; (ii) optionally, a gaseous phase; (b) separating the liquid phase comprising depolymerized lignocellulosic biomass and at least one alcohol from the mixture (i) obtained in step (a) obtaining: (iii) a liquid phase comprising depolymerized lignocellulosic biomass and at least one alcohol; (iv) a solid phase comprising carbon residues ("char"), depolymerized lignocellulosic biomass and, optionally, non-depolymerized lignocellulosic biomass; (c) subjecting the liquid phase c
Resumen de: WO2025109515A1
Process for producing bio-oil from lignin comprising the following steps: (a) subjecting the lignin to extraction of the oligomers in the presence of at least one alcohol having from 1 to 5 carbon atoms, preferably from 1 to 2 carbon atoms, operating at the boiling temperature of said alcohol or, in the case of a mixture of alcohols at the temperature of the higher-boiling alcohol, for a time comprised between 30 minutes and 90 minutes, preferably comprised between 40 minutes and 70 minutes, obtaining a liquid phase comprising oligomers and at least one alcohol and a solid phase comprising lignin essentially free of said oligomers; (b) subjecting the solid phase comprising lignin essentially free of said oligomers obtained in step (a) to depolymerization in the presence of at least one alcohol having from 1 to 5 carbon atoms, preferably from 1 to 2 carbon atoms, in supercritical conditions, operating at a temperature comprised between 200°C and 300°C, preferably comprised between 220°C and 295°C, at a pressure comprised between 40 bar and 170 bar, preferably comprised between 50 bar and 150 bar, for a time comprised between 5 minutes and 150 minutes, preferably comprised between 10 minutes and 130 minutes, obtaining: - (i) a gas phase; - (ii) a mixture comprising an oily phase consisting of bio-oil, a liquid phase comprising at least one alcohol and a solid phase comprising carbon residues ("char"), an oily phase consisting of bio-oil and, optionally, unconverted lignin;
Resumen de: WO2025108769A1
The invention relates to a method for treating a lignocellulosic biomass, with a) an optional step of impregnating the biomass (1), b) a step of cooking (3) the biomass (1) in the presence of water vapor (2) in order to obtain a mixture comprising the biomass (5) and water vapor (4a), c) a separation step in order to obtain the pretreated biomass (5) and the water vapor (4a), d) a step of condensing (17) the water vapor (4a) from the cooking step b) to liquid effluent (4b), e) an enzymatic hydrolysis step (6) in order to obtain a hydrolyzed biomass (7), f) a step of fermenting (8) the hydrolyzed biomass (7) in order to obtain a mixture comprising a fermented biomass (9) and a solid residue, then at least one step of washing said mixture or said solid residue obtained in step f), using the liquid effluent resulting from the condensation step d).
Resumen de: WO2025107081A1
An apparatus for carbonizing biomass may have: at least one dehumidifying unit configured for receiving biomass, for exposing the biomass to drying gases to reduce a moisture content in the biomass and for outputting dehumidified biomass; at least one carbonization unit having an inlet configured for receiving the dehumidified biomass, an outlet configured for outletting biomass with an increase carbon content, at least one feed screw unit configured for displacing the biomass from the inlet to the outlet, and at least one chamber surrounding at least part of an exterior surface of the feed screw unit, the chamber being in heat exchange relation with the exterior surface and configured for heating the exterior surface of the feed screw unit, the feed screw unit being sealed from the inlet to the outlet; and a pneumatic drying circuit configured for directing biomass in the dehumidifying unit using a flow of drying gases, the pneumatic drying circuit including a drying gas source configured for producing the drying gases.
Resumen de: CN224807396U
0001 本实用新型公开了一种快速响应的碳化塔倒塔,两侧所述连通口的相对侧均设置有连通管,两侧所述连通管的顶部均连接有安装壳,所述安装壳的内部均安装有电机,两侧所述连通管的内部均连接有密封板,本快速响应的碳化塔倒塔碳化塔快速倒塔系统通过电机驱动实现自动化操作:启动时,电机带动蜗杆齿轮机构,将密封板从水平关闭状态旋转90°至垂直开启位置,使两侧碳化塔通过连通管形成通路,物料在压差作用下快速转移,完成倒塔后,电机自动反转使密封板复位关闭,整个过程完全机械自动化,无需人工干预,安装壳提供密封保护确保稳定运行,显著提升了倒塔效率和操作安全性。
Nº publicación: CN224812493U 29/09/2026
Solicitante:
河南北工机械制造有限公司
Resumen de: CN224812493U
本实用新型公开了一种用于生物炭制备炭化反应釜,包括反应釜本体和釜盖,所述反应釜本体的外侧下方左右两侧安装有锁块,所述釜盖旋转连接在反应釜本体的上方,且釜盖的上方右侧安装有提手一,所述锁块的外围安装有弧槽,且弧槽与锁块为滑动连接。该一种用于生物炭制备炭化反应釜,与现有的炭化反应釜相比,将原料倒入反应釜本体中,通过提手一旋转釜盖闭合反应釜,再旋动旋块使锁杆嵌入嵌块并下压固定釜盖;电机驱动伸缩杆带动搅拌杆旋转,同时伸缩杆往复伸缩使原料充分翻动;反应完成后,反向操作开启釜盖,通过提手二旋转反应釜本体在支架上倾倒,锁块沿弧槽滑动至顶端,插入插销固定开口向下的倾斜姿态,便于废渣排出及内壁清理。