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Publicaciones de los últimos 15 días/Last 15 days publications (excluidas pubs. CN y JP /CN and JP pubs. excluded)
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GENETICALLY MODIFIED YEAST FOR PRODUCTION OF NON-ALCOHOLIC BEVERAGES

Publication No.:  AU2024332297A1 12/03/2026
Applicant: 
BERKELEY FERMENTATION SCIENCE INC
BERKELEY FERMENTATION SCIENCE INC
AU_2024332297_PA

Absstract of: WO2025049654A2

Provided herein are genetically modified yeast cells that comprise genetic modifications to reduce sensory detection of one or more wort-associated off-flavors of a fermented beverage and the cell is not capable of converting maltose and/or maltotriose to ethanol. Also provided are methods of producing fermented products (e.g., non-alcoholic fermented beverages) using the genetically modified yeast cells described herein.

PROCESS FOR CONVERTING POMACE DERIVED FROM WINERIES INTO A FOOD INGREDIENT AND PRODUCT

Publication No.:  US20260068914A1 12/03/2026
Applicant: 
CRUSH DYNAMICS INC [CA]
CRUSH DYNAMICS INC
US_20260068914_PA

Absstract of: US20260068914A1

A process for converting pomace derived from the production of fruit wine into a nutrient-rich food product, and a product made by said process. The process comprises milling the pomace, carrying out an anaerobic ethanolic fermentation in an anaerobic fermenter by adding yeast and optionally sugars to produce ethanol; carrying out an aerobic acetic acid fermentation in an aerobic fermenter by adding acetic acid bacteria to produce acetic acid, shearing the acetic acid pomace to produce a raw puree; and further processing the raw puree into a puree or powder. The process can be used to produce a product that qualifies for Kosher certification. The nutrient-rich product can be used as an ingredient in foods as a flavour, texture and color enhancer, to mask bitter flavours or off-notes, as a preservative, to fortify processed foods.

METHOD FOR PRODUCING HIGH ENERGY DENSITY CO2-DEPLETED WOOD FUELS

Publication No.:  EP4707362A1 11/03/2026
Applicant: 
PROFAGUS GMBH [DE]
ProFagus GmbH
EP_4707362_A1

Absstract of: EP4707362A1

Die Erfindung betrifft die Herstellung von CO<sub>2</sub>-armen Holzbrennstoffen (z.B. Holzpellets oder Holzbriketts) mit hoher Energiedichte durch die Zugabe von Kohlestaub, wie z.B. Holz-, Stein- oder Braunkohlenstaub, während des Produktionsverfahrens.

BIOETHANOL PRODUCTION FROM WASTE USING ENZYMES

Publication No.:  EP4705496A2 11/03/2026
Applicant: 
HALL PHILIP [GB]
Hall, Philip
CN_121443746_A

Absstract of: AU2024267388A1

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..

Process for Producing Low-CO2 Wood Fuels With High Energy Density

Publication No.:  US20260062637A1 05/03/2026
Applicant: 
PROFAGUS GMBH [DE]
proFagus GmbH
US_20260062637_A1

Absstract of: US20260062637A1

The production of low-CO2 wood fuels (for example, wood pellets or wood briquettes) with high energy density by adding coal dust, such as wood, stone, or lignite dust, during the production process.

PROCESS OF ALCOHOLIC FERMENTATION OF STARCHY SUBSTRATES WITH ELIMINATION OF THE YEAST PROPAGATION STEP, AND WITHOUT THE USE OF SEPARATOR CENTRIFUGES

Publication No.:  US20260062653A1 05/03/2026
Applicant: 
GODOY ALEXANDRE [BR]
FERREIRA GUILHERME MARENGO [BR]
GODOY Alexandre,
FERREIRA Guilherme Marengo
US_20260062653_PA

Absstract of: US20260062653A1

An alcoholic fermentation process that eliminates the yeast propagation step and dispenses with the use of separator centrifuges. An objective is to remove the yeast propagation step in ethanol production processes based on starchy substrates, resulting in reduced fermentation time, improved fermentation yield, and significant reductions in operating costs, particularly regarding the daily acquisition of yeasts.

SYSTEMS AND METHODS FOR CONVERSION OF A BIOMASS INTO BIOFUEL USING A GEOTHERMAL HEAT SOURCE

Publication No.:  US20260062656A1 05/03/2026
Applicant: 
BLUE EVOLUTION INC [US]
Blue Evolution Inc
US_20260062656_PA

Absstract of: US20260062656A1

A system for converting a biomass into a biofuel including a biomass processing station arranged to receive the biomass from a biomass harvester, output the biomass to a hydrothermal liquefaction (HTL) converter, and receive a processed biomass from the HTL converter. The system includes a conduit arranged to transport the biomass from the biomass processing station to the HTL converter and transport the processed biomass from the HTL converter to the biomass processing station. The HTL converter includes a heat exchanger arranged to transfer thermal energy from a geothermal heat source to the biomass to convert the biomass into the processed biomass. The system also includes a controller arranged to monitor conditions of the biomass at locations along the conduit and adjust operations of components along the conduit to, thereby, adjust the conditions of the biomass at one or more locations along the conduit.

Enhanced Distillate Oil Recovery from Thermal Processing and Catalytic Cracking of Biomass Slurry

Publication No.:  US20260062625A1 05/03/2026
Applicant: 
WASTE TO FUELS INC [CA]
Waste to Fuels Inc
US_20260062625_PA

Absstract of: US20260062625A1

A method for thermal processing and catalytic cracking of a biomass to effect distillate oil recovery can include particle size reduction, slurrying the biomass with a carrier fluid to create a reaction mixture, slurrying a catalyst with a carrier fluid to create a catalyst slurry, heating the reaction mixture and/or the catalyst slurry, and depolymerizing the reaction mixture with the catalyst. The reaction mixture can undergo distillation and fractionation to produce distillate fractions that include naphtha, kerosene, and diesel. In some embodiments, thermal processing and catalytic cracking includes vaporization of the biomass followed by distillation and fractionation. In some embodiments, a resulting distillate can be used as a carrier fluid. In some embodiments, the method can include desulfurization, dehydration, and/or decontamination.

PROCESSES FOR RECOVERING PRODUCTS FROM A SLURRY

Publication No.:  US20260062719A1 05/03/2026
Applicant: 
POET GRAIN OCTANE LLC [US]
POET Grain (Octane), LLC
US_20260062719_PA

Absstract of: US20260062719A1

Improved processes and systems for recovering products from a corn fermentation mash. In some examples, a process recovers an oil product, a protein meal product, and a fiber product from a slurry. A process includes the following steps: introducing the slurry into a device with a flexible screen and mechanical agitation to produce a filtrate and a fibrous solid stream; and introducing the filtrate into a three-phase centrifuge to produce an oil stream, a high protein solids stream, and a water with solubles stream. The flexible screen includes a washing nozzle. The slurry is whole stillage from an ethanol process. The three-phase centrifuge is a three-phase decanter. The filtrate is heated before introducing into the three-phase centrifuge. The filtrate is optionally evaporated before introducing into the three-phase centrifuge.

廃棄物から作られたブリケット

Publication No.:  JP3254965U 05/03/2026
Applicant: 
ベルネッガーゲゼルシャフトミットベシュレンクテルハフツング
EP_4471112_PA

Absstract of: ZA202212654B

The invention relates to a process for producing briquettes (1), to a briquette (1) made of a waste material (2) and to the use of a briquette (1) in the process according to the invention. The process provides for providing a waste material (2) comprising at least one metal (3) and at least one organic material (4). It comprises performing a single- or multistage mechanical workup of the waste material (2) and a separation of at least one first fraction (5) from the waste material (2). A briquette mixture (6) containing the at least one first fraction (5) is produced, wherein the at least one first fraction (5) has a heating value of 0 MJ/kg to 30 MJ/kg. A heating value of the briquette mixture (6) is adjusted by varying at least the first fraction (5). The briquette mixture (6) is introduced into a briquetting apparatus (7) and pressed into briquettes (1) therein. This affords briquettes (1) having a heating value of 5 MJ/kg to 30 MJ/kg and having a maximum copper proportion of 0.1% by weight to 20% by weight.

Verfahren zur Herstellung von CO2-armen Holzpellets mit hoher Energiedichte

Publication No.:  DE102024125512A1 05/03/2026
Applicant: 
PROFAGUS GMBH [DE]
proFagus GmbH
DE_102024125512_A1

Absstract of: DE102024125512A1

Die Erfindung betrifft die Herstellung von CO2-armen Holzpellets mit hoher Energiedichte durch die Zugabe von Kohlestaub, wie z.B. Holz-, Stein- oder Braunkohlenstaub, während des Produktionsverfahrens.

METHOD FOR A COMBINED INTEGRATED CHARCOAL PYROLYSIS METALLURGICAL PLANT PROCESS

Publication No.:  EP4702105A1 04/03/2026
Applicant: 
WURTH PAUL SA [LU]
Paul Wurth S.A
CN_121039253_PA

Absstract of: CN121039253A

A method for operating a combined integrated charcoal pyrolysis metallurgical plant comprising a pyrolysis reactor and a metallurgical plant, comprising: feeding a dry raw carbon-rich feedstock to the pyrolysis reactor; -pyrolyzing the dry raw carbon-rich feedstock to produce charcoal and a pyrolysis gas; operating the metallurgical plant, in which charcoal is introduced as fuel and/or reducing agent and/or carburizing agent and/or slag blowing agent into the metallurgical plant; and-treating at least part of the pyrolysis gas as a first stream in the reformer in the presence of an oxygen-containing component, preferably air, O2, CO2 and/or H2O, to form an enhanced pyrolysis gas enriched in H2 and CO; and wherein the enhanced pyrolysis gas is fed through a combined integrated charcoal pyrolysis metallurgical plant for value-added utilization, in particular further as a fuel gas, a reducing gas and/or a carburizing gas.

PROCESS FOR REMOVING CHLORIDE FROM LIPID FEEDSTOCKS USING REJUVENATED CATALYST

Publication No.:  EP4702107A1 04/03/2026
Applicant: 
CHEVRON USA INC [US]
Chevron U.S.A. Inc
CN_121569005_A

Absstract of: US2024360379A1

A process involves sequentially treating a plurality of lipid feedstocks comprising a set of lipid feedstocks each having a chloride content of at least about 2 ppm with a metal oxide catalyst on an oxide support under first treating conditions to produce respective treated streams of the set of lipid feedstocks having a chloride content less than 1 ppm until a given one of the respective treated streams has a chloride content greater than 1 ppm and the metal oxide catalyst is converted to a spent metal oxide catalyst, converting the spent metal oxide catalyst to a rejuvenated metal oxide catalyst, and treating one or more additional lipid feedstocks each having a chloride content of at least about 2 ppm with the rejuvenated metal oxide catalyst under second treating conditions to produce one or more respective treated streams each having a chloride content less than 1 ppm.

FATTY ACID ESTERIFICATION PRETREATMENT PROCESS

Publication No.:  EP4702155A1 04/03/2026
Applicant: 
NOVOZYMES AS [DK]
Novozymes A/S
CN_121532520_A

Absstract of: AU2024260609A1

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.

一种食醋生产用蒸料装置

Publication No.:  CN223950980U 27/02/2026
Applicant: 
山西柏洼古井农业科技有限公司
CN_223950980_U

Absstract of: CN223950980U

本实用新型涉及食醋生产技术领域,具体为一种食醋生产用蒸料装置,包括蒸锅和顶盖,所述顶盖设置在蒸锅的顶端,所述蒸锅内设置有用于清理残渣的清理机构,所述清理机构包括转动槽,所述转动槽开设在蒸锅的内壁上靠顶端位置,所述转动槽内转动连接有转环,所述转环的外壁上固定有环状齿轨,所述环状齿轨位于转动槽内,该食醋生产用蒸料装置,通过设置有清理机构,能够实现对蒸锅内壁与底部进行残渣剐蹭清理,进行蒸料时收起延展条,进行作业,需要清理时,将延展条转动接触蒸锅底端,转动支撑杆对延展条起到支撑作用,通过电机带动齿轮在啮合环状齿轨的作用下,使转环带动清理机构进行转动,实现对粘连在内壁上的残渣进行清理的效果。

一种木炭进料除杂装置

Publication No.:  CN223946121U 27/02/2026
Applicant: 
普洱蜀龙木炭有限责任公司
CN_223946121_U

Absstract of: CN223946121U

本实用新型公开了一种木炭进料除杂装置,包括底板,所述底板上侧设置除杂框,除杂框内中部安装分隔板,除杂框内部设置网格输送带一,网格输送带一内部设置斜板一,且斜板一固定在除杂框和分隔板之间,分隔板内部开设排出孔一,且排出孔一对应斜板一的位置,除杂框内部设置网格输送带二。本实用新型通过网格输送带一对木炭进行筛分,使大于木炭的杂质被截留在网格输送带一上被输送出去,通过网格输送带二使小于木炭的杂质被筛出滑落到收集框二内储存,除杂效果好,同时,除杂框产生震动,提高木炭的筛分除杂效率,同时,通过磁石板产生磁力,将筛分出木炭内的铁屑吸走,提高木炭的品质。

一种生物颗粒上料装置

Publication No.:  CN223950157U 27/02/2026
Applicant: 
淮南技嘉科技有限公司
CN_223950157_U

Absstract of: CN223950157U

本实用新型公开了一种生物颗粒上料装置,包括进料箱,所述进料箱上贯穿设有导料管,所述导料管内部转动设有螺杆,所述螺杆顶端向外延伸贯穿所述导料管,所述螺杆外侧端连接设有旋转电机,所述导料管底端贯穿设有排料管,所述排料管底端可拆卸设有排料漏斗,所述排料漏斗设置有多个,多个所述排料漏斗左右两端均设有安装板,两个所述安装板上端均设有安装杆,所述排料管左右两端均对应所述安装杆设有安装座,两个所述安装杆上均设有安装环,所述安装杆和安装环螺纹连接,通过排料漏斗的设计,方便对应不同外界装置导料,避免加料过程中意外掉落。

一种醋生产用储料装置

Publication No.:  CN223949915U 27/02/2026
Applicant: 
山东料百年食品科技有限公司
CN_223949915_U

Absstract of: CN223949915U

本实用新型公开了一种醋生产用储料装置,储料罐下端连接有出料管,出料管远离储料罐一端连接有定量罐,定量罐一侧竖直方向设置有透明观察窗,透明观察窗外侧设置有刻度线,定量罐内壁活动连接有密封活塞,本实用新型具有以下优点:通过转动调节杆可连带密封活塞运动,此时通过观察密封活塞位于透明观察窗处的刻度线位置,进而可精确调节定量罐内部的有效的容积,储料罐内部醋排放至定量罐中时,为避免储料罐内部产生负压影响排放,可打开进气管上的阀门开关,且醋进入定量罐中排挤定量罐中的气体,使得气体从通气孔排出即可排出,当定量罐中的液体充满时,会使得浮球漂浮堵塞通气孔,以此可避免定量罐中的从通气孔处溢出。

一种用于玉米发酵酒精的玉米渣过滤装置

Publication No.:  CN223945104U 27/02/2026
Applicant: 
河南汉永酒精有限公司
CN_223945104_U

Absstract of: CN223945104U

本实用新型涉及玉米加工技术领域,且公开了一种用于玉米发酵酒精的玉米渣过滤装置,包括架体,架体的顶部设有过滤桶,过滤桶的顶部连通有进料管,过滤桶的内部设有倾斜放置的第一筛板,第一筛板的较高一侧与过滤桶的内壁通过铰链相连,第一筛板的较低一侧设有排渣管,排渣管与过滤桶相连通,第一筛板的较低一侧下方设有振动组件;过滤桶的下方设有过滤箱,过滤桶与过滤箱通过连通管相连,过滤箱的内部设有第二筛板,第二筛板滑动设置在过滤箱内,第二筛板上设有牵引组件,过滤箱的底部连通有排液管。本实用新型极大的提升了固液分离效率,能充分满足大规模生产时的快速处理需求,保证滤液纯净度,满足了对液体质量的要求标准。

一种大型秸秆圆包与枝丫柴锅炉的推送装置

Publication No.:  CN223954188U 27/02/2026
Applicant: 
田玉祥王霞
CN_223954188_U

Absstract of: CN223954188U

本实用新型公开了一种大型秸秆圆包与枝丫柴锅炉的推送装置,包括炉体,所述炉体侧壁面安装有进料仓,所述进料仓侧壁面安装有推送结构,所述进料仓内为空腔结构,所述炉体侧壁面与进料仓贴合处开设有进料口,所述推送结构自身的支撑架下壁面开设有矩形通孔,所述矩形通孔内设有支撑梁,所述支撑梁上铺设有条形承载板,本实用新型涉及秸秆圆包锅炉推动撕裂技术领域。本装置便于秸秆圆包与枝丫柴燃烧,枝丫柴和秸秆圆包分开、分别推送,让枝丫柴和秸秆圆包燃烧充分,不会导致在炉体内秸秆圆包与枝丫柴燃烧程度不同导致资源浪费。

一种竹木家具碳化装置

Publication No.:  CN223948113U 27/02/2026
Applicant: 
江西未家竹文化科技有限公司
CN_223948113_U

Absstract of: CN223948113U

本实用新型涉及家具碳化技术领域,提供了一种竹木家具碳化装置,包括碳化罐,所述碳化罐的内表面底部固定连接有多个定位套,所述定位套的内表面活动嵌设有定位杆,多个所述定位杆的顶部固定连接有承压板,所述承压板的内部转动连接有转杆,所述转杆的顶部固定连接有转盘,所述转杆的底部固定连接有蜗轮,所述蜗轮的外表面啮合连接有蜗杆,所述蜗杆的外表面转动连接有两个轴板并延伸出一端。本实用新型,装置设置有旋转受热碳化结构,确保竹木家具的各个表面和内部都能在合适的温度下进行碳化,避免局部过热导致木材表面烧焦或者内部碳化程度不一致,避免一侧受热膨胀产生的应力导致桌面弯曲变形,导致应力分布不均匀。

一种基于大豆渣制备生物炭的高温裂解装置

Publication No.:  CN223950957U 27/02/2026
Applicant: 
广东海洋大学
CN_223950957_U

Absstract of: CN223950957U

本实用新型公开了一种基于大豆渣制备生物炭的高温裂解装置,涉及生物炭制备技术领域,包括底板,底板的上表面固定连接有支撑框,支撑框的内壁转动连接有炭化筒,炭化筒的内壁安装有封闭门和加热丝,炭化筒的内壁转动连接有第一转杆,第一转杆的外表面连通有若干个用于提高豆渣受热均匀度的搅拌杆,第一转杆的外表面安装有电磁阀门。本实用新型能够在使用大豆渣制备生物炭时,利用反向转动的炭化筒和搅拌杆对大豆渣进行搅拌混合,从而使得大豆渣受热均匀,进而实现大豆渣同步加热炭化,同时可在生物炭制备完成后,利用冷却水与生物炭中的热量进行热交换,从而提高生物炭冷却降温效率,进而提高生物炭的制备效率,并降低生物炭制备成本。

一种生物柴油副产物甘油回收装置

Publication No.:  CN223945000U 27/02/2026
Applicant: 
府谷县仙灵脾技术开发有限公司
CN_223945000_U

Absstract of: CN223945000U

本实用新型涉及生物柴油生产技术领域,特别公开了一种生物柴油副产物甘油回收装置,所述回收分离桶的内部固定安装有用于产生高频交变磁场的电磁线圈,所述回收分离桶的内部均匀的固定安装有用于加热混合液的加热棒,所述冷凝箱的内部固定安装有用于冷却高温气体的废液冷凝锥;电磁线圈通电后将会在回收分离桶的内部形成一个产生变化的磁场,此时多个加热棒在磁场中将会产生涡流,由于加热棒具有一定的电阻,因此加热棒将会在涡流的作用下快速的发热,发热的加热棒将会对位于四周的混合液进行加热,均匀分布的加热棒直接在混合液的内部发热,不仅提高了加热速度,而且加热更加的均匀,达到了能够提高回收效率的效果。

COKE PRODUCTION METHOD

Publication No.:  WO2026042323A1 26/02/2026
Applicant: 
JFE STEEL CORP [JP]
\uFF2A\uFF26\uFF25\u30B9\u30C1\u30FC\u30EB\u682A\u5F0F\u4F1A\u793E
WO_2026042323_PA

Absstract of: WO2026042323A1

A coke production method comprising mixing carbonized biomass obtained through heat treatment of biomass, to a portion of blended coal for coke production and performing dry distillation thereon, wherein the volatile matter of the carbonized biomass on dry ash-free basis is 7.0-35 mass%.

COKE PRODUCTION METHOD

Nº publicación: WO2026042326A1 26/02/2026

Applicant:

JFE STEEL CORP [JP]
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WO_2026042326_PA

Absstract of: WO2026042326A1

A coke production method comprising mixing carbonized biomass obtained through heat treatment of biomass, to a portion of blended coal for coke production and performing dry distillation thereon, wherein O/C representing the ratio of the numbers of O atoms with respect to C atoms contained in the carbonized biomass is 0.040-0.200.

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