公开(公告)号：US20150203760A1

公开(公告)日：2015-07-23

申请号：US14593876

申请日：2015-01-09

Applicant: Proton Power, Inc.

Inventor： Samuel C. Weaver ,  Daniel L. Hensley ,  Samuel P. Weaver ,  Daniel C. Weaver ,  Lee S. Smith

IPC: C10B53/02 ,  C10L1/04 ,  C10B53/00

CPC classification number: C10G1/02 ,  B01D45/08 ,  B01D47/02 ,  B01D50/004 ,  B01D53/1412 ,  B01D53/1418 ,  B01D53/1425 ,  B01D53/1487 ,  B01D53/1493 ,  B01D2252/103 ,  C10B1/02 ,  C10B7/10 ,  C10B47/06 ,  C10B47/44 ,  C10B53/00 ,  C10B53/02 ,  C10G1/00 ,  C10G1/002 ,  C10G1/06 ,  C10G3/40 ,  C10G2300/1011 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10L1/04 ,  C10L1/06 ,  C10L1/08 ,  C10L2200/0469 ,  C10L2270/023 ,  C10L2270/026 ,  C10L2270/04 ,  C10L2290/02 ,  C10L2290/06 ,  C10L2290/08 ,  C10L2290/24 ,  C10L2290/543 ,  C10L2290/544 ,  C10L2290/547 ,  C10L2290/56 ,  Y02E50/14 ,  Y02P30/20 ,  Y02T50/678

Abstract: Methods, systems, and devices for liquid hydrocarbon fuel production, hydrocarbon chemical production, and aerosol capture are provided. For example, a carbon-oxygen-hydrogen (C—O—H) compound may be heated to a temperature of at least 800 degrees Celsius such that the C—O—H compound reacts through a non-oxidation reaction to generate at least a hydrocarbon compound that may be at least a component of a liquid hydrocarbon fuel or a hydrocarbon chemical. The liquid hydrocarbon fuel may be a liquid when at a temperature of 20 degrees Celsius. The C—O—H compound may include biomass. In some cases, the hydrocarbon compound produced through the non-oxidation reaction includes a hydrocarbon aerosol form as the hydrocarbon compound at least as it is produced or cools. Some embodiments include aerosol capture methods, systems, and devices, which may include passing a hydrocarbon aerosol form through a material in a liquid phase in order to gather the aerosol material.

Abstract translation: 提供了液体烃燃料生产，碳氢化合物生产和气溶胶捕集的方法，系统和装置。 例如，可以将碳 - 氢 - 氢（C-O-H）化合物加热到至少800摄氏度的温度，使得C-O-H化合物通过非氧化反应反应以产生至少一种 烃化合物，其可以是至少液体烃燃料或烃化学物质的组分。 当液体烃燃料在20摄氏度的温度下可以是液体。 C-O-H化合物可包括生物质。 在一些情况下，通过非氧化反应产生的烃化合物至少包括烃生成或冷却的烃类气溶胶形式。 一些实施例包括气溶胶捕获方法，系统和装置，其可以包括使烃气溶胶形式通过液相中的材料以收集气溶胶材料。

公开(公告)号：US20150184079A1

公开(公告)日：2015-07-02

申请号：US14423531

申请日：2013-07-12

Applicant: Frank RIEDEWALD

Inventor： Frank Riedewald

IPC: C10B53/07 ,  C10L1/08 ,  C10B49/14 ,  C10B27/06 ,  C10B11/00 ,  C10B31/06

CPC classification number: C10B53/07 ,  C10B11/00 ,  C10B27/06 ,  C10B31/06 ,  C10B49/14 ,  C10G1/10 ,  C10L1/08 ,  C10L2200/0469 ,  C10L2270/026 ,  C10L2290/02 ,  C10L2290/544 ,  Y02P20/143

Abstract: Disclosed is a process for treating waste plastic materials such as whole tyres, coarsely cut tyres, large plastic pieces, plastic composites such as hoses or combinations of above into gases, liquids and solids by direct heating in a pyrolysis liquid (1) such as molten salt or molten metal. The pyrolysis system is constructed such that the segregation of the light and heavy materials occurs within the pyrolysis chamber. The carbon black is segregated from the pyrolysis vapours via a cyclone and fractions of carbon black may be obtained by installing a number of cyclones in series so that different qualities of carbon black may be produced. Diesel or other oils, steel, carbon black, ZnO and synthesis gas are recovered; all of which can be feed streams to other processes. This process avoids the inefficient procedure of cutting the tyres or other plastic composites into small pieces before treatment by pyrolysis and also recovers valuable components.

Abstract translation: 公开了一种通过在热解液（1）中直接加热来将诸如整个轮胎，粗切轮胎，大塑料件，塑料复合材料如软管或上述组合的废塑料材料处理成气体，液体和固体的方法， 盐或熔融金属。 热解系统被构造成使得轻质和重物质的分离发生在热解室内。 炭黑通过旋风分离器与热解蒸汽分离，并且可以通过串联安装多个旋风分离器获得部分炭黑，从而可能产生不同质量的炭黑。 回收柴油或其他油，钢，炭黑，ZnO和合成气; 所有这些都可以为其他流程提供流。 该过程避免了在通过热解处理之前将轮胎或其它塑料复合材料切割成小块并且还恢复有价值的组分的低效程序。

公开(公告)号：US09051519B2

公开(公告)日：2015-06-09

申请号：US13827153

申请日：2013-03-14

Applicant: ELEVANCE RENEWABLE SCIENCES, INC.

Inventor： Linda A. Kunz ,  Tessa M. Pals ,  Steven A. Cohen ,  Melvin L. Luetkens, Jr. ,  Chander Balakrishnan ,  Robert B. Snyder

IPC: C07C1/00 ,  C07C6/02 ,  C07C5/05 ,  C10G3/00 ,  C11C3/12 ,  C10G29/20 ,  C10G45/00 ,  C10G45/58 ,  C10G50/00 ,  C10G65/04 ,  C10G69/12 ,  C11B3/00 ,  C10L1/02 ,  C10L1/08 ,  C11C3/00 ,  C11C3/10 ,  C07C6/04 ,  C07C1/213 ,  C07C5/03 ,  C07C7/13

CPC classification number: C11C3/126 ,  C07C1/213 ,  C07C5/03 ,  C07C5/05 ,  C07C6/04 ,  C07C7/13 ,  C07C2523/28 ,  C07C2523/42 ,  C07C2523/44 ,  C07C2523/46 ,  C07C2523/72 ,  C07C2523/745 ,  C07C2523/755 ,  C10G3/42 ,  C10G3/44 ,  C10G3/50 ,  C10G29/205 ,  C10G45/00 ,  C10G45/58 ,  C10G50/00 ,  C10G65/043 ,  C10G69/123 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/1088 ,  C10G2300/30 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10G2400/20 ,  C10G2400/22 ,  C10L1/00 ,  C10L1/026 ,  C10L1/08 ,  C10L2200/0469 ,  C10L2200/0476 ,  C11B3/00 ,  C11C3/003 ,  C11C3/10 ,  C11C3/12 ,  C11C3/123 ,  Y02P20/582 ,  Y02P30/20 ,  C07C11/02 ,  C07C11/12 ,  C07C9/14 ,  C07C9/22 ,  C07C11/21

Abstract: Methods are provided for refining natural oil feedstocks and partially hydrogenating polyunsaturated olefins and polyunsaturated esters. The methods comprise reacting the feedstock in the presence of a metathesis catalyst under conditions sufficient to form a metathesized product comprising olefins and esters. In certain embodiments, the methods further comprise separating the polyunsaturated olefins from the polyunsaturated esters in the metathesized product. In certain embodiments, the methods further comprise partially hydrogenating the polyunsaturated olefins in the presence of a hydrogenation catalyst, wherein at least a portion of the polyunsaturated olefins are converted to monounsaturated olefins. In other embodiments, the methods further comprise partially hydrogenating the polyunsaturated esters in the presence of a hydrogenation catalyst, wherein at least a portion of the polyunsaturated esters are converted to monounsaturated esters.

Abstract translation: 提供了用于澄清天然油原料和部分氢化多不饱和烯烃和多不饱和酯的方法。 所述方法包括在复分解催化剂存在下，在足以形成包含烯烃和酯的复分解产物的条件下使原料反应。 在某些实施方案中，所述方法还包括从所述多元不饱和酯中分离所述多不饱和烯烃。 在某些实施方案中，所述方法还包括在氢化催化剂存在下部分氢化多不饱和烯烃，其中至少一部分多不饱和烯烃转化为单不饱和烯烃。 在其它实施方案中，所述方法还包括在氢化催化剂存在下部分氢化多不饱和酯，其中至少一部分多不饱和酯转化为单不饱和酯。

公开(公告)号：US20150144528A1

公开(公告)日：2015-05-28

申请号：US14408585

申请日：2013-06-28

Applicant: SHELL OIL COMPANY

Inventor： Eduard Philip Kieffer ,  Duurt Renkema ,  Jelle Rudolf Anne Sietsma

IPC: C10G69/02 ,  C10M101/02 ,  C10L1/04

CPC classification number: C10G69/02 ,  C10G2/30 ,  C10G45/58 ,  C10G65/12 ,  C10G2300/1022 ,  C10G2300/301 ,  C10G2300/302 ,  C10G2300/304 ,  C10L1/04 ,  C10L1/08 ,  C10L2200/0492 ,  C10L2290/42 ,  C10L2290/543 ,  C10M101/02 ,  C10M107/02 ,  C10M2205/173 ,  C10N2220/022 ,  C10N2270/00

Abstract: The present invention provides a process to prepare a gas oil fraction, a heavy distillate fraction and a residual base oil fraction, which process at least comprises the following steps: (a) subjecting the feedstock to a hydroprocessing step to obtain an at least partially isomerised feedstock; (b) separating the isomerised feedstock by means of distillation into at least a gas oil fraction, a heavy distillate fraction and a residual fraction, wherein the residual fraction has a T10 wt % boiling point of between 200 and 450° C.; (c) recycling part of the residual fraction to step (a); and (d) catalytic dewaxing of remaining residual fraction to obtain a residual base oil.

Abstract translation: 本发明提供了制备粗柴油馏分，重馏分馏分和残余基油馏分的方法，该方法至少包括以下步骤：（a）使原料进行加氢处理步骤以获得至少部分异构化的 原料; （b）通过蒸馏将异构化原料分离成至少瓦斯油馏分，重馏分馏分和残余馏分，其中残余馏分的T10重量％沸点在200-450℃之间; （c）将剩余部分的一部分再循环到步骤（a）中; 和（d）剩余残余馏分的催化脱蜡以获得残留的基础油。

公开(公告)号：US09040766B2

公开(公告)日：2015-05-26

申请号：US12782498

申请日：2010-05-18

Applicant: Mika Kettunen ,  Vaino Sippola ,  Marja Tiitta

Inventor： Mika Kettunen ,  Vaino Sippola ,  Marja Tiitta

IPC: C07C5/13 ,  C07C5/22 ,  C07C5/03 ,  B01J29/00 ,  B01J29/064 ,  B01J29/068 ,  C07C5/27 ,  C07C9/22 ,  C10G45/62 ,  C10G45/64 ,  C10L1/08 ,  C10G3/00 ,  B01J29/03 ,  B01J29/70 ,  B01J29/85

CPC classification number: C07C5/03 ,  B01J29/005 ,  B01J29/0308 ,  B01J29/064 ,  B01J29/068 ,  B01J29/70 ,  B01J29/85 ,  B01J2229/20 ,  B01J2229/42 ,  B01J2229/62 ,  C07C5/2775 ,  C07C9/22 ,  C10G3/45 ,  C10G3/47 ,  C10G3/49 ,  C10G3/50 ,  C10G45/62 ,  C10G45/64 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2400/04 ,  C10G2400/08 ,  C10L1/08 ,  Y02P30/10 ,  Y02P30/20

Abstract: The invention relates to a method for the manufacture of branched saturated hydrocarbons, said method comprising the steps where a feed comprising olefins having at least 10 carbons is simultaneously hydrogenated and isomerized in the presence of hydrogen at a temperature of 100-400° C., under hydrogen partial pressure of 0.01-10 MPa, in the presence of a catalyst comprising a metal selected from the metals of Group VIIIb of the Periodic Table of Elements, a molecular sieve selected from ten member ring molecular sieves, twelve member ring molecular sieves and mesoporous molecular sieves embedded with zeolite, and a carrier, to yield branched saturated hydrocarbons.

Abstract translation: 本发明涉及一种制备支链饱和烃的方法，所述方法包括以下步骤：其中包含具有至少10个碳原子的烯烃的进料在氢气存在下在100-400℃的温度下同时氢化和异构化， 在氢分压为0.01-10MPa的条件下，在包含选自元素周期表第Ⅷb族金属的金属催化剂存在下，选自十个成员环分子筛，十二个成员环分子筛和 嵌入沸石的介孔分子筛和载体，得到支链饱和烃。

公开(公告)号：US09028675B2

公开(公告)日：2015-05-12

申请号：US13535436

申请日：2012-06-28

Applicant: Sebastien Bergeron ,  Ashok Uppal ,  Robert J. Falkiner ,  Marc-André Poirier

Inventor： Sebastien Bergeron ,  Ashok Uppal ,  Robert J. Falkiner ,  Marc-André Poirier

IPC: C10G17/00 ,  C10G17/095 ,  C10G53/10 ,  C10L1/08 ,  C10G61/02 ,  C10G27/04 ,  C10G29/04 ,  C10G53/14

CPC classification number: C10G17/095 ,  C10G27/04 ,  C10G29/04 ,  C10G53/10 ,  C10G53/12 ,  C10G53/14 ,  C10G61/02 ,  C10G2300/1051 ,  C10G2300/202 ,  C10G2300/301 ,  C10G2300/4018 ,  C10G2400/08 ,  C10L1/08

Abstract: This invention relates to a method for increasing thermal stability of fuel, as well as in reducing nitrogen content and/or enhancing color quality of the fuel. According to the method, a fuel feedstock can be treated with a solid phosphoric acid catalyst under appropriate catalyst conditions, e.g., to increase the thermal stability of the fuel feedstock. Preferably, the fuel feedstock can be treated with the solid phosphoric acid catalyst at a ratio of catalyst mass within a contact zone to a mass flow rate of feedstock through the zone of at least about 18 minutes to increase the thermal stability of the fuel feedstock, along with reducing nitrogen content and/or enhancing color quality.

Abstract translation: 本发明涉及提高燃料的热稳定性以及减少氮含量和/或提高燃料颜色质量的方法。 根据该方法，燃料原料可以在合适的催化剂条件下用固体磷酸催化剂处理，例如提高燃料原料的热稳定性。 优选地，燃料原料可以用固体磷酸催化剂以接触区域内的催化剂质量与原料通过该区域的至少约18分钟的质量流量比进行处理，以增加燃料原料的热稳定性， 以及减少氮含量和/或增强颜色质量。

公开(公告)号：US20150111723A1

公开(公告)日：2015-04-23

申请号：US14560421

申请日：2014-12-04

Applicant: KiOR, Inc.

Inventor： Robert Bartek ,  Michael Brady ,  Dennis Stamires

IPC: B01J21/16 ,  B01J23/10 ,  B01J23/26 ,  B01J23/06 ,  B01J23/78 ,  B01J23/08 ,  B01J23/02 ,  B01J23/00 ,  B01J27/18 ,  B01J23/34

CPC classification number: B01J21/16 ,  B01J21/005 ,  B01J23/005 ,  B01J23/007 ,  B01J23/02 ,  B01J23/06 ,  B01J23/08 ,  B01J23/10 ,  B01J23/26 ,  B01J23/34 ,  B01J23/78 ,  B01J27/1806 ,  C10B53/02 ,  C10B57/06 ,  C10G1/00 ,  C10G1/06 ,  C10G1/08 ,  C10G3/44 ,  C10G3/45 ,  C10G3/50 ,  C10G2300/1011 ,  C10G2300/1014 ,  C10L1/08 ,  Y02E50/13 ,  Y02E50/14 ,  Y02E50/15 ,  Y02E50/32 ,  Y02P30/20 ,  Y02T50/678

Abstract: A process for biomass catalytic cracking is disclosed herein. More specifically, the process is in presence of is a mixed metal oxide catalyst represented by the formula (X1O).(X2O)a.(X3YbO4) wherein X1, X2 and X3 are alkaline earth elements selected from the group of Mg, Ca, Be, Ba, and mixture thereof, and Y is a metal selected from the group of Al, Mn, Fe, Co, Ni, Cr, Ga, B, La, P and mixture thereof, wherein the catalyst is formed by calcining at least one compound comprising at least one alkaline earth element and a metal element.

Abstract translation: 本文公开了一种生物质催化裂化方法。 更具体地说，该方法是存在由式（X1O）表示的混合金属氧化物催化剂（X 2 O）a。（X 3 Y b O 4）其中X 1，X 2和X 3是选自Mg，Ca， Be，Ba及其混合物，Y是选自Al，Mn，Fe，Co，Ni，Cr，Ga，B，La，P及其混合物的金属，其中催化剂通过至少煅烧形成 一种化合物，其包含至少一种碱土金属元素和金属元素。

公开(公告)号：US08999011B2

公开(公告)日：2015-04-07

申请号：US13975828

申请日：2013-08-26

Applicant: David Lawrence Stern ,  Salvatore R. Di Mauro ,  Aldo Roccaro ,  Paul William Bessonette

Inventor： David Lawrence Stern ,  Salvatore R. Di Mauro ,  Aldo Roccaro ,  Paul William Bessonette

IPC: C10L1/16 ,  C10G45/02 ,  C10L1/08

CPC classification number: C10L1/1616 ,  C10G45/02 ,  C10G2300/1059 ,  C10G2300/202 ,  C10G2300/203 ,  C10G2300/207 ,  C10G2300/208 ,  C10G2300/302 ,  C10G2300/304 ,  C10G2300/308 ,  C10L1/08

Abstract: This invention relates to low sulfur marine/bunker fuel compositions and methods of making same. Contrary to conventional marine/bunker fuel compositions/methods, the inventive lower sulfur compositions/methods focus on use of mostly uncracked components, such as (cat feed) hydrotreated gasoils, and/or can also have reduced contents of residual components.

Abstract translation: 本发明涉及低硫海洋/燃料燃料组合物及其制造方法。 与传统的海洋/燃料燃料组合物/方法相反，本发明的低硫组合物/方法集中在使用大部分未裂化的组分，例如（猫饲料）加氢处理的油油，和/或还可以具有减少的残余组分含量。

公开(公告)号：US20150057476A1

公开(公告)日：2015-02-26

申请号：US14477758

申请日：2014-09-04

Applicant: NESTE OIL OYJ

Inventor： Jukka MYLLYOJA ,  Pekka AALTO ,  Pekka SAVOLAINEN ,  Veli-Matti PUROLA ,  Ville ALOPAEUS ,  Johan GRONQVIST

IPC: C07C1/24 ,  C07C5/03 ,  C07C7/12 ,  C07C7/13 ,  C07C5/27 ,  C07C7/10

CPC classification number: C10G3/50 ,  C07C1/24 ,  C07C5/03 ,  C07C5/2775 ,  C07C7/10 ,  C07C7/12 ,  C07C7/13 ,  C07C2529/076 ,  C10G3/46 ,  C10G3/47 ,  C10G45/02 ,  C10G45/58 ,  C10G45/62 ,  C10G45/64 ,  C10G65/043 ,  C10G2300/1011 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/202 ,  C10G2300/205 ,  C10G2300/207 ,  C10G2300/4006 ,  C10G2300/4081 ,  C10G2300/802 ,  C10G2400/04 ,  C10L1/08 ,  Y02E50/13 ,  Y02P30/20

Abstract: The invention relates to a process for the manufacture of diesel range hydrocarbons wherein a feed is hydrotreated in a hydrotreating step and isomerised in an isomerisation step, and a feed comprising fresh feed containing more than 5 wt % of free fatty acids and at least one diluting agent is hydrotreated at a reaction temperature of 200-400° C., in a hydrotreating reactor in the presence of catalyst, and the ratio of the diluting agent/fresh feed is 5-30:1.

Abstract translation: 本发明涉及一种用于制造柴油范围烃的方法，其中进料在加氢处理步骤中加氢处理并在异构化步骤中异构化，并且包含含有大于5重量％游离脂肪酸和至少一个稀释的新鲜原料的进料 在催化剂存在下，在加氢处理反应器中，在200-400℃的反应温度下加氢处理试剂，稀释剂/新鲜进料的比例为5-30:1。

公开(公告)号：US20150031927A1

公开(公告)日：2015-01-29

申请号：US13676541

申请日：2012-11-14

Applicant: The Government of the United States of America as represented by the Secretary of the Navy

Inventor： Benjamin G. Harvey ,  Heather A. Meylemans

IPC: C07C5/13 ,  C07C5/25 ,  C07C7/00 ,  C10G1/00 ,  C10L1/04

CPC classification number: C07C5/13 ,  C07C5/2506 ,  C07C7/00 ,  C10G1/00 ,  C10G3/42 ,  C10G3/44 ,  C10G3/45 ,  C10G3/50 ,  C10G2300/1014 ,  C10G2400/04 ,  C10G2400/08 ,  C10L1/04 ,  C10L1/08 ,  Y02E50/13 ,  Y02P30/20 ,  Y02T50/678

Abstract: A fuel and method for conversion of sesquiterpenes to high density fuels. The sesquiterpenes can be either extracted from plants or specifically produced by bioengineered organisms from waste biomass. This approach allows for the synthesis of high performance renewable fuels.