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热解炭化系统

Resumen de: CN224313450U

本实用新型提供了一种热解炭化系统，包括：进料组件，具有物料进口和物料出口；热解炭化组件，包括热解炭化炉，热解炭化炉具有热解炭化腔和加热腔，热解炭化腔的一端具有热解炭化进口，热解炭化腔的另一端具有热解炭化出口和烟气出口，热解炭化进口高于热解炭化出口设置，热解炭化进口与物料出口连通，加热腔具有加热进口和加热出口；供热组件，包括燃烧器，燃烧器具有气体进口和气体出口；净化组件，包括干式脱酸塔、除尘器和湿式脱酸塔，干式脱酸塔具有净化进口，除尘器的进口与干式脱酸塔的出口连通。通过本申请提供的技术方案，能够解决现有技术中的热解炭化系统效率低、维修频繁以及会对环境造成严重污染的问题。

一种木质颗粒加工用的压实机

Resumen de: CN224310840U

本实用新型涉及木质颗粒压实技术领域，且公开了一种木质颗粒加工用的压实机，包括底板，所述底板的顶部固定安装有支撑杆，所述支撑杆的顶部固定安装有压实箱，所述压实箱的顶部固定安装有安装架。该木质颗粒加工用的压实机，通过设置挤压释放组件，挤压释放组件使用后在连接杆和活动杆的连接下，液压缸伸展，上压板下移，下压板上移，使得上压板和下压板相互靠拢对投入到压实箱中的木质颗粒压实成块状，待木质颗粒压实完成后，液压缸收缩，上压板上移，下压板下移，使得上压板和下压板相互远离，当下压板上的木质颗粒完全与压实箱脱离时，顺着下压板的上表面滑出，从而方便了对木质颗粒进行压实卸料工作。

一种具有可燃气回收系统的炭化炉

Resumen de: CN224313458U

本实用新型属于炭化炉技术领域，具体地，涉及一种具有可燃气回收系统的炭化炉，包括炉体、炉膛、焦油管和净化装置，炉体的前侧设有燃料口、炉体的后侧设有废气管，炉膛固定设置在炉体的上侧，炉膛的右侧设有投料口和炉门，焦油管的一端连接炉膛，且另一端连接炉体，净化装置设置在炉膛的左侧，且净化装置包括外壳、进气管、过滤箱、管道一、洗涤箱、管道二、吸附箱和出气管，本装置通过过滤箱、洗涤箱、和吸附箱对高温加热干馏过程中，木炭时会产生大量烟气进行处理，其中包含的一氧化碳、氧、氮、甲烷、丙烷等可燃气体，通过喷淋、吸附等净化后排入炉体，实现废气的回收利用，避免对环境和大气造成污染。

一种反应釜供氧结构

Resumen de: CN224293211U

本实用新型公开一种反应釜供氧结构，包括釜体、釜盖，釜体内设置有炉胆，釜体的底部设置有燃烧机构，燃烧机构位于炉胆外侧，燃烧机构包括燃烧器、环形供氧管、供氧盒和送气管，供氧盒固定于釜体底部，其顶部布置有燃烧器，底面设有第一进氧管，第一进氧管延伸至釜体外侧并与第一鼓风机连接，由第一鼓风机向供氧盒内输送空气，供氧盒顶部开设有多个出气孔；环形供氧管环绕供氧盒设置，环形供氧管上分布有若干个出气口，环形供氧管一端设置有第二进氧管，本装置通过双路供氧系统、可升降燃烧机构和弧形可燃气注入装置的协同设计，显著增强了供氧均匀性并优化了温度场控制，从而实现了高品质竹炭的高效、稳定生产。

一种高温燃烧室

Resumen de: CN224302106U

本实用新型提供一种高温燃烧室，燃烧室的出口端设置有防爆门和燃气出口；燃烧室的进口端设置有燃烧器接口，燃烧室通过燃烧器接口与燃烧器连通，燃烧室的进口端还设置有燃气进口、空气进口、有机玻璃观察口及火检口；燃烧室的顶部设置有第一热电偶、第二热电偶和压力表，第一热电偶用于检测燃烧室进口端的温度，第二热电偶用于检测燃烧室出口端的温度，压力表用于检测燃烧室出口端的压力；根据第一热电偶、第二热电偶和压力表的读数调整燃烧器的参数设置及燃气和空气进出的流量，保证燃烧室内的温度维持在900‑1200℃。本实用新型的高温燃烧室，能够将炭化炉燃烧产生的大部分废气物高温燃烧，剩余部分可燃废气物输送到其他设备二次利用。

一种低能耗燃料颗粒冷却风道

Resumen de: CN224302463U

本实用新型涉及颗粒燃料加工技术领域，且公开了一种低能耗燃料颗粒冷却风道，包括第一底座，第一底座的顶部固定连接有第一壳体。该低能耗燃料颗粒冷却风道，当使用者将第一集料盒进行更换时，使用者将第一夹块通过转轴转动，使第一夹块的一端脱出第一延伸块的内壁，使第一集料盒与第一底座的连接脱离，让使用者可以进行更换，原料在第二壳体内部的转动过程中，受到第一螺旋导流板的引导，不仅实现了原料的均匀混合，还促使原料中的废屑或过小的颗粒有效分离，这些废屑或颗粒通过第一筛孔顺利筛漏至第一卸料管，并最终落入第一集料盒中集中收集，极大提高了冷却风道的工作效率与原料的利用率，减少了废料的产生。

一种反应釜炉盖密封装置

Resumen de: CN224293240U

本实用新型公开一种反应釜炉盖密封装置，包括反应釜体和釜盖，所述反应釜体的顶端环设有若干个密封组件，当釜盖置于反应釜体上时，密封组件会对其施加向下压力，使釜盖与釜体紧密贴合，所述釜盖底端或反应釜体顶端上设置有密封圈；所述密封组件包括支座、转杆、固定座和压杆，所述支座固定于反应釜体上，所述转杆转动装配于支座上，且固定座安装于转杆的另一端，所述压杆升降装配于固定座上，所述压杆向下移动从而与釜盖接触施压，本实用新型通过机械施压结构替代人工敷泥操作，将釜盖密封流程从繁复的清理、填补、压实中解放；操作者仅需水平旋转定位与垂直锁紧两个动作，即可在极短时间内完成密封加载。

一种秸秆颗粒燃料加工用压缩装置

Resumen de: CN224293195U

本实用新型涉及秸秆颗粒燃料加工技术领域，且公开了一种秸秆颗粒燃料加工用压缩装置，包括有：底板，所述底板的顶部固定安装有螺钉；调节组件，所述调节组件设置在底板的顶部；其中，所述调节组件包括有模具部位、调节部位，所述模具部位、调节部位均设置在底板的顶部；加工组件，所述加工组件设置在底板的顶部；其中，所述加工组件包括有支撑部位、加工部位。本实用新型通过设置调节组件，顶板的内部固定安装有多种类型的模具，通过手柄转动顶板，圆台会跟着转动，当需要使用的模具处于下料台的上方时，将固定件依次穿过定位孔、通孔，使顶板与支板之间位置固定，模具完成调换，达到了模具更换便捷的效果。

一种生物质颗粒加工用防堵塞压粒机

Resumen de: CN224293194U

本实用新型公开了一种生物质颗粒加工用防堵塞压粒机，属于生物质颗粒加工技术领域，其技术方案要点包括压粒机本体，所述压粒机本体包括底座、驱动件、压粒腔室、进料斗和下料壳，所述进料斗的内腔设置有辅助送料组件，所述下料壳的顶部设置有辅助烘干组件，解决了现有生物质颗粒加工的压粒机通常缺乏辅助送料搅拌结构，当生物质原料进入进料斗后，原料容易在进料斗和压粒腔室的连接处堆积堵塞，使原料难以顺利进入压粒腔室进行压粒作业，而且部分湿度较大的生物质原料容易粘附在进料斗内壁，进一步加剧进料困难，并且现有压粒机在下料环节缺少辅助烘干结构，生物质颗粒压粒成型后，若颗粒湿度较大，难以保持稳定的形状的问题。

一种生物质燃料颗粒生产筛分装置

Resumen de: CN224293925U

本实用新型公开了一种生物质燃料颗粒生产筛分装置，涉及生物质燃料颗粒加工技术领域。一种生物质燃料颗粒生产筛分装置，包括：工作台、筛分仓、回收仓、立杆、摇杆、电机、转盘；回收仓固定在工作台上；回收仓的仓室底面呈倾斜设置；立杆包括两个，两个立杆间隔固定在回收仓的仓室底面；筛分仓的两侧与两个立杆分别转动连接；筛分仓的仓室底面为筛网结构；电机固定在工作台上；转盘固定在电机主轴上。本实用新型，设计了一种生物质燃料颗粒生产筛分装置，此筛分装置结构简单、且便于操作，借助此筛分装置可顺利进行杂质碎屑的筛除操作；同时，筛分仓底部的筛网结构为敞口式设置，筛网堵料后便于进行清理。

一种生物质颗粒燃料原料预处理设备

Resumen de: CN224293382U

本实用新型公开了一种生物质颗粒燃料原料预处理设备，包括安装底板，所述安装底板的顶部通过螺栓固定有安装支架，所述安装支架的顶部设置有粉碎机构，所述粉碎机构包括粉碎滚筒、入料斗、伺服电机、驱动轴、驱动辊、粉碎锤、齿板、过滤网和排料槽，所述排料槽的底部设置有磁选机构，所述磁选机构的一侧设置有清理机构，所述清理机构的底部设置有运输机构，所述运输机构的顶部设置有喷淋机构；通过粉碎机构原料进行粉碎操作，并对粉碎后的原料进行筛选，直到原料符合标准，保证对原料粉碎操作的质量，通过磁选机构对粉碎后的原料进行磁选操作，通过运输机构和喷淋机构配合对原料的湿度进行调节，方便后续对原料的进一步加工。

METHOD FOR SEPARATING AND RECOVERING LIGNIN AND MELTABLE FLOWABLE BIOLIGNIN POLYMERS

Resumen de: US20260146135A1

Lignin is recovered from biomass or byproducts from biomass processing through the use of organic solvents and water while modifying the form or composition of the lignin. During the separation and recovery process, the lignin can be modified or integrated into a form which is more suitable for its intended use. As the lignin is suspended or is soluble within the organic solvent, the integration of materials or reactants may be more easily blended or dispersed within the lignin to improve performance, quality and overall production efficiency.

QUANTITATIVE ANALYSIS OF BIOMASS SAMPLES

Resumen de: US20260146983A1

A method for quantifying a cellulosic component in a sample includes preparing a first suspension by mixing an amount of sample with first aqueous acid at a concentration of 40 wt-% or greater; incubating the first suspension in a first incubation stage at a first incubation temperature of less than 40° C.; adding water or aqueous sulfuric acid to the incubated first suspension to form a second suspension having a concentration 40 wt-% or less of sulfuric acid based on a total weight of the second suspension; incubating the second suspension in a second incubation stage at a second incubation temperature of 50° C. or greater for an incubation period, wherein the sample is not subjected to hydrolysis at temperatures above 98° C.; separating a supernatant from the incubated second suspension; analyzing the supernatant for total content of xylose, mannose, galactose, and arabinose; and calculating, based on the analysis, the amount of the hemicellulose.

YEAST STRAINS EXHIBITING PROLONGED PERSISTENCE DURING A PLURALITY OF FERMENTATION CYCLES

Resumen de: US20260146256A1

0000 The present disclosure provides yeasts, which can be recombinant yeast host cells, exhibiting prolonged persistence when submitted to a plurality of fermentation cycles. The yeasts exhibit at least one of the following phenotypic trait: a fast settling phenotype, a rugose phenotype, an improved invertase activity, triploidy, increased signaling in a RAS/cAMP/PKA pathway or combinations thereof.

CONTINUOUS BIOCHAR KILN SYSTEM

Resumen de: WO2026110016A1

The continuous biochar kiln makes biochar from biomass. The continuous biochar kiln is continuously operated by using an updraft fire through a vertical rotating fire tube. The rotary fire tube is attached to a blade that acts as a conveyor or mixer. The blade conveys the biomass from the inlet to the outlet of the cylinder shape and air-tight kiln. As the biomass is conveyed it receives the heat transfer from the vertical rotating fire tube wherein the biomass transforms into biochar at the outlet valve through the process of pyrolysis. The pyrolysis combustible gas may be generated during the process and that gas becomes the thermal energy to continue fueling the kiln.

MODULATION OF NADPH GENERATION BY RECOMBINANT YEAST HOST CELL DURING FERMENTATION

Resumen de: US20260146255A1

The present disclosure concerns recombinant yeast host cells having a first genetic modification for downregulating a first metabolic pathway that converts NADP+ to NADPH, as well as a second genetic modification for upregulating a second metabolic pathway that converts NADP+ to NADPH. The second genetic modification allows the expression of a glyceraldehyde-3-phosphate dehydrogenase lacking phosphorylating activity, which can, in some embodiments, be from enzyme commission 1.2.1.9 or 1.2.1.90. The second pathway is distinct from the first metabolic pathway. The present disclosure also concerns a process for making and improving the yield of a fermented product, such as ethanol, using the recombinant yeast host cell.

METHOD FOR MONITORING A PRODUCTION PROCESS

Resumen de: WO2026111958A2

A method for monitoring an ethanol fermentation process involves positioning an accelerometer at or above the liquid level of a process stream in a fermentation vessel. The method includes collecting vibration data from the accelerometer during fermentation, analyzing the frequency spectra of the vibration data, and determining the fermentation rate based on the analysis. The system can also incorporate temperature data to improve prediction accuracy. The method can identify amplitude ranges in the frequency spectra, correlate these to carbon dioxide bubble production, and determine parameters such as bubble size, depth of origin, and microorganism location. The system can provide alerts for deviations in fermentation rate and recommend interventions. Additionally, the system can monitor various stages of ethanol production, including liquefaction, oil separation, centrifugation, evaporation, and drying, using multiple accelerometers to determine process parameters such as viscosity, composition, and equipment performance.

BIOMASS PYROLYSIS-GASIFICATION DEVICE

Resumen de: WO2026109082A1

The present invention relates to the technical field of pyrolysis devices, and in particular to a biomass pyrolysis-gasification device, comprising a microwave heating reactor, a pretreatment mechanism and a driving mechanism, wherein the pretreatment mechanism comprises cutting mincer blades, which can push materials to gather towards the center during cutting; and the driving mechanism is configured to drive a cylinder to rotate about the horizontal axis and vertical center line thereof, such that the materials in the cylinder are in sufficient contact with the cutting mincer blades, whilst the materials gathered towards the center are dispersed outwards, thereby enabling the materials in the cylinder to repeatedly disperse and gather. In the present invention, the materials entering the cylinder are conveyed to the center part of the cylinder by means of the angled cutting mincer blades, whilst the driving mechanism drives the cylinder to rotate horizontally such that the materials entering the cylinder can be thrown away towards two ends of the interior of the cylinder under the action of centrifugal force. Thus, the materials can be repeatedly dispersed and gathered in the pretreatment mechanism, thereby achieving a more sufficient and comprehensive crushing processing effect.

YEAST STRAIN FOR LOW-ALCOHOLIC BEER

Resumen de: EP4748917A1

0001 The invention relates to a yeast cell that is capable of fermenting an aqueous fermentation medium comprising, per 100 mL, at least 0.8 g of a total of maltose and maltotriose, thereby producing alcohol in a concentration of 0.5 vol.% or less, based on the volume of the aqueous fermentation medium, , and that has an ability to decrease the pH of the aqueous fermentation medium by 0.7 pH units or more and/or that is capable of fermenting an aqueous fermentation medium comprising, per 100 mL, at least 0.8 g of a total of maltose and maltotriose and a total of glucose, fructose and sucrose of at most 0.8 g, thereby producing alcohol in a concentration of 0.5 vol.% or less, based on the volume of the aqueous fermentation mediumand that has an ability to convert at least 15 wt.% of said total of glucose, fructose and sucrose in a time of 6 h or less and/or that has an ability to convert at least 80 wt.% of said total of glucose, fructose and sucrose in a time of 16 h or less.

A REACTOR, A PLANT AND A PROCESS FOR THERMOCHEMICAL CONVERSION OF SOLID BIOMASS TO BIOCHAR

Resumen de: EP4748906A1

The present invention relates to a reactor for thermochemical conversion of solid biomass to biochar, in particular pyrolysis, consisting of a reactor chamber with a reactor chamber wall, a reactor chamber bottom, an inlet opening and an outlet opening, an outer retort arranged within the reactor chamber with an outer retort wall, an outer retort bottom, an outer retort lid and an outer retort opening, and an inner retort removably arranged in the outer retort with an inner retort wall, an inner retort bottom, an inner retort lid and an inner retort opening, wherein at least the partial, preferably complete outer surface of the inner retort wall and/or at least the partial, preferably complete outer surface of the inner retort bottom and at least the partial, preferably complete inner surface of the outer retort wall and/or at least the partial, preferably complete inner surface of the outer retort bottom form an interspace, wherein at least the partial, preferably complete outer surface of the outer retort wall and/or at least the partial, preferably complete outer surface of the outer retort bottom and at least the partial, preferably complete inner surface of the reaction chamber wall and/or at least the partial, preferably complete inner surface of the reaction chamber bottom form a flow channel for guiding a gaseous heating medium from the inlet opening to the outlet opening, wherein the flow channel comprises at least one flow element suitable for causing pressure loss

ETHANOL

Nº publicación: EP4748865A2 27/05/2026

Solicitante:

SEKISUI CHEMICAL CO LTD [JP]
Sekisui Chemical Co., Ltd.

Resumen de: EP4748865A2

0001 Problem To provide a practical and novel alcohol and derivatives thereof which have more industrial value than existing petrochemical raw materials. 0002 Solution Ethanol comprising an inorganic component and/or an organic component, wherein the inorganic component comprises at least one component selected from the group consisting of: silicon having a content of 10 mg/L or more and 100 mg/L or less; chromium having a content of 0.6 mg/L or less; iron having a content of 2.0 mg/L or less ; sodium having a content of 150 mg/L or more and 1000 mg/L or less; and potassium having a content of 1.0mg/L or more and 10 mg/L or less; and the organic component comprises at least one component selected from the group consisting of: aliphatic hydrocarbon having a content of 0.16 mg/L or more and 10 mg/L or less; aromatic hydrocarbon having a content of 0.4 mg/L or more and 10 mg/L or less; and dialkyl ether having a content of 0.1 mg/L or more and 100 mg/L or less.