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公开(公告)号：US08344194B2
公开(公告)日：2013-01-01
申请号：US12917980
申请日：2010-11-02
Applicant: Robert Bartek , Steve Yanik
Inventor： Robert Bartek , Steve Yanik
CPC classification number: C10G11/18 , C10G1/002 , C10G1/06 , C10G1/08 , C10G3/42 , C10G3/50 , C10G3/56 , C10G3/57 , C10G3/62 , C10G45/02 , C10G47/00 , C10G47/02 , C10G47/30 , C10G47/34 , C10G49/007 , C10G2300/1011 , C10G2300/1014 , C10G2300/107 , C10G2300/1074 , C10G2300/1077 , Y02P30/20
Abstract: A process for producing bio-fuel from biomass is disclosed herein. The process includes processing the mean particle diameter of the biomass by mechanical processing to a size ranging from 1 μm to 1000 μm to form particulated biomass. The particulated biomass is mixed with a liquid hydrocarbon to form a suspension, wherein the suspension includes between 1 weight percent to 40 weight percent particulated biomass. The suspension is heated to a temperature between 50° C. and 550° C. The heated suspension is fed into a unit selected from the group consisting of a pyrolysis reactor, a fluid catalytic cracking unit, a delayed coker, a fluid coker, a hydroprocessing unit, and a hydrocracking unit; and then at least a portion of the particulated biomass of the heated suspension is converted into fuel.
Abstract translation: 本文公开了一种从生物质生产生物燃料的方法。 该方法包括通过机械加工将生物质的平均粒径加工至1μm至1000μm的尺寸以形成颗粒状生物质。 将颗粒生物质与液体烃混合以形成悬浮液，其中悬浮液包含1重量％至40重量％的颗粒生物质。 将悬浮液加热至50℃至550℃之间的温度。将加热的悬浮液加入到选自热解反应器，流化催化裂化装置，延迟焦化器，流体焦化器， 加氢处理装置和加氢裂化装置; 然后加热的悬浮液的至少一部分微粒生物质被转化为燃料。
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公开(公告)号：US20120291340A1
公开(公告)日：2012-11-22
申请号：US13453880
申请日：2012-04-23
Applicant: Andries Quirin Maria BOON , Johan Willem GOSSELINK , John William HARRIS , Andries Hendrik JANSSEN , Sander VAN PAASEN , Colin John SCHAVERIEN , Nicolaas Wilhelmus Joseph WAY
Inventor： Andries Quirin Maria BOON , Johan Willem GOSSELINK , John William HARRIS , Andries Hendrik JANSSEN , Sander VAN PAASEN , Colin John SCHAVERIEN , Nicolaas Wilhelmus Joseph WAY
CPC classification number: C10G3/57 , B01J8/0055 , B01J8/1827 , B01J8/1872 , B01J8/388 , C10B49/22 , C10B53/02 , C10B57/06 , C10G1/08 , C10G3/50 , C10G11/18 , C10G2300/1011 , C10G2300/104 , C10G2300/1044 , C10G2300/1051 , C10G2300/1055 , C10G2300/107 , C10G2300/1077 , C10G2300/4006 , C10G2300/807 , C10L1/04 , Y02E50/14 , Y02E50/32 , Y02P30/20
Abstract: A process or a system for converting a solid biomass material is provided, comprising contacting the solid biomass material with a catalytic cracking catalyst at a temperature of more than 400° C. in a riser reactor to produce one or more cracked products. The riser reactor contains: a riser reactor pipe, which riser reactor pipe has a diameter that increases in a downstream direction; and a bottom section connected to the riser reactor pipe, which bottom section has a larger diameter than the riser reactor pipe.
Abstract translation: 提供了一种用于转化固体生物质材料的方法或系统，包括在立管反应器中使固体生物质材料与催化裂化催化剂在大于400℃的温度下接触以产生一种或多种裂化产物。 提升管反应器包括：提升管反应器管，其提升管反应器管的直径在下游方向上增加; 以及连接到提升管反应器管的底部，该底部具有比提升管反应器管更大的直径。
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公开(公告)号：US20120284811A1
公开(公告)日：2012-11-08
申请号：US13101427
申请日：2011-05-05
Applicant: Teresa Huskowska
Inventor： Teresa Huskowska
Abstract: In an embodiment, the invention relates to the seeds, plants, and plant parts of canola line SCV372145 and to methods for producing a canola plant produced by crossing canola line SCV372145 with itself or with another canola line. The invention also relates to methods for producing a canola plant containing in its genetic material one or more transgenes and to the transgenic canola plants and plant parts produced by those methods. This invention also relates to canola lines or breeding lines and plant parts derived from canola line SCV372145, to methods for producing other canola lines, lines or plant parts derived from canola line SCV372145 and to the canola plants, varieties, and their parts derived from use of those methods. The invention further relates to hybrid canola seeds, plants and plant parts produced by crossing the line SCV372145 with another canola line.
Abstract translation: 在一个实施方案中，本发明涉及油菜系SCV372145的种子，植物和植物部分以及通过将卡诺拉油菜SCV372145自身或与另一种油菜线交叉产生的油菜植物的方法。 本发明还涉及在其遗传物质中含有一种或多种转基因和通过这些方法生产的转基因卡诺拉植物和植物部分产生卡诺拉植物的方法。 本发明还涉及从卡诺拉油菜SCV372145得到的卡诺拉线或育种系和植物部分，以及用于生产其它卡诺拉油菜系，来自油菜籽系SCV372145的品系或植物成分的方法以及来自使用的卡诺拉植物，品种及其部分 的这些方法。 本发明还涉及通过将SCV372145与另一个卡诺拉线交叉产生的杂种油菜籽，植物和植物部分。
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公开(公告)号：US20120279118A1
公开(公告)日：2012-11-08
申请号：US13286479
申请日：2011-11-01
Applicant: Tien-Te Lee
Inventor： Tien-Te Lee
IPC: C10L1/00
CPC classification number: B01F3/0811 , B01F3/088 , B01F2003/0849
Abstract: A fuel emulsification system includes a first emulsification device and a second emulsification device. The first emulsification device includes a first outlet end, and a first inlet end in fluid communication with an outlet pipe unit of a tank that receives a mixture of combustible fuel and water. The first emulsification device is configured to emulsify the mixture from the tank into a first emulsion, and to output the first emulsion through the first outlet end. The second emulsification device includes a second outlet end, and a second inlet end in fluid communication with the first outlet end for receiving the first emulsion therefrom. The second emulsification device is configured to emulsify the first emulsion into a second emulsion, and to output the second emulsion through the second outlet end.
Abstract translation: 燃料乳化系统包括第一乳化装置和第二乳化装置。 第一乳化装置包括第一出口端和与容纳可燃燃料和水的混合物的罐的出口管单元流体连通的第一入口端。 第一乳化装置构造成将混合物从罐中乳化成第一乳液，并通过第一出口端输出第一乳液。 第二乳化装置包括第二出口端和与第一出口端流体连通以从其接收第一乳液的第二入口端。 第二乳化装置被配置为将第一乳液乳化成第二乳液，并且通过第二出口端输出第二乳液。
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公开(公告)号：US20120272565A1
公开(公告)日：2012-11-01
申请号：US13546271
申请日：2012-07-11
Applicant: Robert Bartek , Michael Brady , Dennis Stamires
Inventor： Robert Bartek , Michael Brady , Dennis Stamires
CPC classification number: C10B53/02 , C10B49/16 , C10B57/08 , C10C5/00 , C10G1/02 , C10G1/08 , C10G2300/1011 , C10L1/02 , Y02E50/14 , Y02E50/30 , Y02P30/20
Abstract: Aspects of the present invention relate to methods, systems, and compositions for preparing a solid biomass for fast pyrolysis. The method includes contacting the solid biomass with an inorganic material present in an effective amount for increasing fast pyrolysis yield of an organic liquid product (e.g., bio-oil). In various embodiments, the inorganic material is selected from the group consisting of aluminum sulfate, aluminum nitrate, aluminum chloride, aluminum hydroxide, ammonium hydroxide, magnesium hydroxide, potassium hydroxide, and combinations thereof.
Abstract translation: 本发明的方面涉及用于制备用于快速热解的固体生物质的方法，系统和组合物。 该方法包括使固体生物质与有效量存在的无机材料接触，以提高有机液体产物（例如生物油）的快速热解产率。 在各种实施方案中，无机材料选自硫酸铝，硝酸铝，氯化铝，氢氧化铝，氢氧化铵，氢氧化镁，氢氧化钾及其组合。
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Patent Agency Ranking
公开(公告)号：US20120266525A1
公开(公告)日：2012-10-25
申请号：US13453801
申请日：2012-04-23
Applicant: Johan Willem GOSSELINK , John William HARRIS , Andries Hendrik JANSSEN , Sander VAN PAASEN , Colin John SCHAVERIEN , Nicolaas Wilhelmus Joseph WAY
Inventor： Johan Willem GOSSELINK , John William HARRIS , Andries Hendrik JANSSEN , Sander VAN PAASEN , Colin John SCHAVERIEN , Nicolaas Wilhelmus Joseph WAY
IPC: C10L1/00
CPC classification number: C10G1/08 , B01J8/18 , C10B49/22 , C10B53/02 , C10B57/06 , C10G3/50 , C10G3/57 , C10G11/18 , C10G2300/1011 , C10G2300/4006 , C10G2300/807 , C10L1/02 , C10L1/04 , Y02E50/14 , Y02P20/145 , Y02P30/20
Abstract: A process for converting a solid biomass material is provided. The solid biomass material is contacted with a catalytic cracking catalyst at a temperature of more than 400° C. in a riser reactor to produce one or more cracked products. The riser reactor is an external riser reactor with a curve and/or low velocity zone at its termination and wherein a part of the catalytic cracking catalyst has deposited in the curve and/or low velocity zone.
Abstract translation: 提供了一种转化固体生物质材料的方法。 固体生物质材料在提升管反应器中在超过400℃的温度下与催化裂化催化剂接触以产生一种或多种裂化产物。 提升管反应器是在其端接处具有曲线和/或低速区的外部提升管反应器，并且其中一部分催化裂化催化剂沉积在曲线和/或低速区中。
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公开(公告)号：US08268164B2
公开(公告)日：2012-09-18
申请号：US12119230
申请日：2008-05-12
Applicant: Scott Lee Wellington , Stanley Nemec Milam
Inventor： Scott Lee Wellington , Stanley Nemec Milam
IPC: C10M101/02 , C10L1/00
CPC classification number: C10G45/00 , C10G65/04 , C10L1/04 , Y02P20/142
Abstract: The present invention is directed to a crude product composition. The crude product has, per gram of crude product: at least 0.001 grams of naphtha, the naphtha having an octane number of at least 70, and the naphtha having at most 0.15 grams of olefins per gram of naphtha; at least 0.001 grams of kerosene, the kerosene having at least 0.2 grams of aromatics per gram of kerosene and a freezing point at a temperature of at most −30° C.; and at most 0.05 grams of residue.
Abstract translation: 本发明涉及粗产物组合物。 粗产物每克粗产物：至少0.001克石脑油，石脑油的辛烷值至少为70，石脑油每克石脑油中至多0.15克烯烃; 至少0.001克煤油，煤油每克煤油具有至少0.2克芳族化合物和在至多-30℃的温度下的凝固点; 至多0.05克残留物。
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公开(公告)号：US20120201947A1
公开(公告)日：2012-08-09
申请号：US13368813
申请日：2012-02-08
Applicant: Earnest Stuart
Inventor： Earnest Stuart
IPC: A23K1/00 , C07K14/00 , C07C67/48 , C07C69/003 , C07K1/14 , C07C29/74 , C07C31/12 , C10L1/00 , C07C31/08
Abstract: The present invention is a method for refining native biomass to extremely fine and highly disrupted particles using high shear and/or cavitation in combination with high temperature and high or low pH conditions which dissolve biomass to a high percentage. The method of the present invention results in a high percentage of hydrolysis, in many cases near theoretical levels, in short residence times while minimizing inputs over other methods, using low chemical inputs, and optionally with no chemical inputs in certain stages compared to existing processes. The method of the present invention also uses minimal electrical energy inputs and conserves heat energy within the process and reduces equipment requirements while producing concentrated products.
Abstract translation: 本发明是一种利用高剪切和/或空化以及将生物质溶解成高百分比的高温和高pH或低pH条件结合使用，将天然生物质精制成极细和高度破碎的颗粒的方法。 本发明的方法导致在很短的停留时间内在许多情况下接近理论水平的百分比很高，同时使用低的化学输入，并且与现有方法相比，在某些阶段中可选择地没有化学输入 。 本发明的方法还使用最小的电能输入并节省了该过程中的热能并且在产生浓缩产品的同时降低了设备需求。
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公开(公告)号：US20120174471A1
公开(公告)日：2012-07-12
申请号：US13331065
申请日：2011-12-20
Applicant: Joseph Broun Powell , Juben Nemchand Chheda
Inventor： Joseph Broun Powell , Juben Nemchand Chheda
CPC classification number: C10G3/00 , C10G3/42 , C10G2300/1014 , C10G2300/202 , C10G2300/4081 , C10G2300/44 , C10L1/04 , Y02P30/20
Abstract: Biomass is contacted with an aqueous media to form an extracted biomass. An aqueous liquor separated from the extracted biomass is treated with a purification substrate to form a treated carbohydrate stream having less than 35% of the sulfur content and less than 35% of the nitrogen content, based on the untreated aqueous liquor stream, prior to contact with an aqueous phase reforming catalyst to form oxygenated intermediates that can be further processed to form a liquid fuel. An extracted biomass solids stream is also separated from the extracted biomass which is contacted with a first digestive solvent and then a second digestive solvent to form a solubilized pulp. This solublilized pulp may be combined with the aqueous liquor stream or combined to an aqueous reforming reaction system or recycled to the aqueous media to be processed further for an effective process to produce the liquid fuel.
Abstract translation: 生物质与水性介质接触以形成提取的生物质。 用提取的生物质分离的含水液体用净化底物处理，以在接触之前基于未处理的含水液体流形成具有少于35％的硫含量和小于氮含量的35％的经处理的碳水化合物流 与水相重整催化剂形成氧化中间体，其可进一步加工以形成液体燃料。 提取的生物质固体物流也与提取的生物质分离，其与第一消化溶剂接触，然后与第二消化溶剂接触以形成溶解的纸浆。 这种溶解的纸浆可以与含水液体流合并或与水性重整反应体系结合或再循环到水性介质中以进一步进行处理以产生液体燃料。
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公开(公告)号：US20120151826A1
公开(公告)日：2012-06-21
申请号：US13330775
申请日：2011-12-20
Applicant: Joseph Broun POWELL , Juben Nemchand CHHEDA
Inventor： Joseph Broun POWELL , Juben Nemchand CHHEDA
CPC classification number: C10G1/00 , C10G2300/1011 , C10G2300/1014 , C10G2300/202 , C10G2300/4081 , C10G2300/44 , Y02E50/343 , Y02P30/20 , Y02T50/678
Abstract: Processes to produce biofuels from biomass is provided where the biomass is contacted with an aqueous media to form a extracted biomass and at least a portion of an aqueous liquor separated from the extracted biomass containing soluble carbohydrate is treated with a purification substrate to form a treated carbohydrate stream having less than 35% of the sulfur content and less than 35% of the nitrogen content, based on the untreated aqueous liquor stream prior to contact with a hydrogenolysis catalyst to form a plurality of oxygenated intermediates that can be further processed to form a liquid fuel. An extracted biomass solids stream is also separated from the extracted biomass which is contacted with a first digestive solvent to form a pretreated biomass and then a second digestive solvent to form a solubilized pulp comprising soluble carbohydrates.
Abstract translation: 提供从生物质生产生物燃料的方法，其中生物质与水性介质接触以形成提取的生物质，并且用提取的含有可溶性碳水化合物的提取的生物质分离的至少一部分含水液体用纯化底物处理以形成经处理的碳水化合物 在与氢解催化剂接触之前，基于未处理的含水液体流，具有小于35％的硫含量和小于氮含量的35％的物流，以形成可以进一步处理以形成液体的多个含氧中间体 汽油。 提取的生物质固体物流也与提取的生物质分离，其与第一消化溶剂接触以形成预处理的生物质，然后是第二消化溶剂以形成包含可溶性碳水化合物的溶解纸浆。
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