公开(公告)号：US20170037319A1

公开(公告)日：2017-02-09

申请号：US15149681

申请日：2016-05-09

Applicant: Cool Planet Energy Systems, Inc.

Inventor： Michael C. CHEIKY ,  Ronald A. SILLS

IPC: C10B47/12 ,  C10B53/02 ,  C10B57/02 ,  C10L5/44

CPC classification number: C10B47/12 ,  B01J6/008 ,  B02C21/00 ,  C10B53/02 ,  C10B57/02 ,  C10G1/02 ,  C10G2300/1011 ,  C10G2300/1014 ,  C10L1/02 ,  C10L1/04 ,  C10L5/447 ,  C10L2290/02 ,  C10L2290/06 ,  Y02E50/14 ,  Y02E50/30 ,  Y02E50/32 ,  Y02P20/145 ,  Y02P30/20

Abstract: A method is disclosed for generating useful Chemical intermediates from biomass using a novel pyrolysis reactor that utilizes the inherent thermal properties of carbon under compression as the biomass is subjected to sequential or concurrent temperature ramps. The ramps are sufficient to volatilize and selectively create different components, while the pressure application aids the selective decomposition of the biomass.

Abstract translation: 公开了一种使用新型热解反应器从生物质产生有用的化学中间体的方法，其利用在压缩下的碳的固有热性质，因为生物质经受顺序或同时的温度斜坡。 斜坡足以挥发和选择性地产生不同的组分，而压力施加有助于生物质的选择性分解。

公开(公告)号：US09550937B2

公开(公告)日：2017-01-24

申请号：US14448404

申请日：2014-07-31

Applicant: BAKER HUGHES INCORPORATED

Inventor： Koral B. Campbell ,  Jerry J. Weers

IPC: C09K8/584 ,  C10G29/20 ,  C10G21/06 ,  C09K8/58 ,  C10L1/02

CPC classification number: C09K8/58 ,  C09K8/584 ,  C10G29/20 ,  C10G2300/302 ,  C10L1/02 ,  C10L1/04 ,  C10L2230/00

Abstract: At least one biosurfactant may be added to a hydrocarbon-based fluid to decrease the viscosity of the hydrocarbon-based fluid. The biosurfactant(s) may be less toxic to the environment than other diluents typically used to decrease the viscosity of such fluids. The biosurfactant(s) may be or include, but are not limited to mycolic acids, glycolipids, lipopolysaccharides, lipoproteins-lipopeptides, phospholipids, and combinations thereof.

Abstract translation: 可以将至少一种生物表面活性剂加入到基于烃的流体中以降低烃基流体的粘度。 与通常用于降低这种流体粘度的其它稀释剂相比，生物表面活性剂对环境的毒性较小。 生物表面活性剂可以是或包括但不限于霉酚酸，糖脂，脂多糖，脂蛋白 - 脂肽，磷脂及其组合。

公开(公告)号：US20170009144A1

公开(公告)日：2017-01-12

申请号：US15270163

申请日：2016-09-20

Applicant: Neste Oyj

Inventor： Pekka AALTO ,  Kati SANDBERG ,  Tomi NYMAN ,  Maija HAKOLA

IPC: C10G3/00 ,  C09D7/00 ,  C10M105/04 ,  C10G65/04 ,  C10L1/04

CPC classification number: C10G3/50 ,  C07C1/22 ,  C07C9/14 ,  C09D7/20 ,  C10G3/42 ,  C10G45/58 ,  C10G65/043 ,  C10G2300/1011 ,  C10G2400/00 ,  C10L1/04 ,  C10L2200/0469 ,  C10L2270/08 ,  C10M105/00 ,  C10M105/04 ,  C10M177/00 ,  C10M2203/003 ,  C10M2203/022 ,  C10N2220/021 ,  C10N2220/025 ,  C10N2220/028 ,  C10N2220/031 ,  C10N2240/201 ,  C10N2240/40 ,  Y02P20/582 ,  Y02P30/20

Abstract: A composition, including 40-50 wt-% C14 paraffins, based on the total weight of the composition, and 35-45 wt-% C15 paraffins, based on the total weight of the composition, wherein the C14 and C15 paraffins are produced from a biological raw material.

Abstract translation: 基于组合物的总重量，包含40-50重量％C14链烷烃和基于组合物总重量的35-45重量％C 15链烷烃的组合物，其中C 14和C 15链烷烃由 生物原料。

公开(公告)号：US09534178B2

公开(公告)日：2017-01-03

申请号：US14764485

申请日：2013-08-01

Applicant: PETROCHINA COMPANY LIMITED

Inventor： Shoutao Ma ,  Ran Tian ,  Zhihua Zhang ,  Gang Wang ,  Famin Sun ,  Ruiqin Zhang ,  Chunmei Yu ,  Shengbo Sun ,  Xiufang Feng ,  Fengxuan Li ,  Jinling Zhu

IPC: B01J8/00 ,  B01J8/02 ,  B01J8/04 ,  C10G45/00 ,  C10G45/02 ,  C10G65/00 ,  C10G65/02 ,  C10G65/04 ,  C10G65/08 ,  C10L1/04 ,  C10G45/20 ,  C10L1/08 ,  C10G49/00 ,  C10L1/00

CPC classification number: C10G65/08 ,  B01J8/0453 ,  B01J8/0492 ,  B01J2208/00849 ,  B01J2208/00938 ,  C10G45/20 ,  C10G65/04 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10G2400/10 ,  C10L1/04 ,  C10L1/08 ,  C10L2270/026 ,  C10L2290/545

Abstract: A hydrogenation method and distillate two-phase hydrogenation reactor in which the size of an upper space of the reactor is greater than that of a lower catalyst bed part. The reactor comprises 2 to 4 catalyst beds. An inner component for gas replenishment and for stripping a liquid-phase stream containing impurities is arranged between at least one adjacent catalyst bed and comprises a separator plate and exhaust pipes. The separator plate is provided with multiple downcomer through holes. The separator plate is connected with a plurality of exhaust pipes. The exhaust pipes are vertically arranged above the separator plate. The top parts of the exhaust pipes are in contact with the lower part of the upper catalyst bed.

Abstract translation: 一种氢化方法和蒸馏二相氢化反应器，其中反应器的上部空间的大小大于下部催化剂床部分的尺寸。 反应器包含2至4个催化剂床。 用于补充气体和用于汽提含有杂质的液相物流的内部部件设置在至少一个相邻的催化剂床之间，并且包括隔板和排气管。 隔板设有多个降液管通孔。 分隔板与多个排气管连接。 排气管垂直布置在隔板的上方。 排气管的顶部与上部催化剂床的下部接触。

公开(公告)号：US09528060B2

公开(公告)日：2016-12-27

申请号：US14347423

申请日：2012-03-08

Applicant: Shigeki Takeshima ,  Naozumi Arimoto

Inventor： Shigeki Takeshima ,  Naozumi Arimoto

IPC: C10M171/00 ,  C10M171/02 ,  C10M101/00 ,  C10L1/26 ,  C10M169/04 ,  C10L1/04 ,  C10L1/16 ,  C10L10/00

CPC classification number: C10L1/265 ,  C10L1/04 ,  C10L1/1625 ,  C10L10/00 ,  C10M169/048 ,  C10M171/02 ,  C10M2203/1025 ,  C10M2205/024 ,  C10M2205/026 ,  C10M2205/028 ,  C10M2205/0285 ,  C10M2205/04 ,  C10M2205/06 ,  C10M2207/028 ,  C10M2207/262 ,  C10M2209/084 ,  C10M2223/045 ,  C10M2229/041 ,  C10N2220/022 ,  C10N2220/029 ,  C10N2220/033 ,  C10N2230/02 ,  C10N2230/06 ,  C10N2230/08 ,  C10N2230/54 ,  C10N2230/68 ,  C10N2240/102 ,  C10N2210/02

Abstract: The present invention relates to a system oil composition for crosshead diesel engines, the system oil composition having excellent heat resistance and being effective for improvement of fuel efficiency. More specifically, the present invention relates to a system oil composition for crosshead diesel engines in which the system oil composition includes a mineral oil and/or a synthetic oil as a base oil (A) and has a kinematic viscosity of at least 35 mm2/s at 50° C., a high-shear viscosity of at most 45 mPa·s at 50° C., and a high-shear viscosity of at least 15 mPa·s at 70° C.

Abstract translation: 本发明涉及十字头柴油发动机的系统油组合物，该系统油组合物具有优异的耐热性并且对提高燃料效率是有效的。 更具体地说，本发明涉及一种十字头柴油发动机的系统油组合物，其中系统油组合物包含矿物油和/或合成油作为基础油（A），其运动粘度至少为35mm 2 / 在50℃下的高剪切粘度在50℃下最高为45mPa·s，在70℃下的高剪切粘度为至少15mPa·s。

公开(公告)号：US09505986B2

公开(公告)日：2016-11-29

申请号：US14331775

申请日：2014-07-15

Applicant: JX NIPPON OIL & ENERGY CORPORATION

Inventor： Yasutoshi Iguchi ,  Hideki Ono ,  Akira Koyama

IPC: C10L1/00 ,  C10G3/00 ,  C10G45/58 ,  C10G65/04 ,  C10L1/04

CPC classification number: C10G3/50 ,  C10G3/46 ,  C10G3/49 ,  C10G45/58 ,  C10G65/043 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/202 ,  C10G2300/30 ,  C10G2300/301 ,  C10G2300/4018 ,  C10G2300/80 ,  C10G2400/08 ,  C10L1/04 ,  C10L2200/043 ,  C10L2200/0461 ,  C10L2270/04 ,  C10L2290/10 ,  Y02P30/10 ,  Y02P30/20

Abstract: The aviation fuel oil base of the present invention is obtained by hydrotreating an oil to be treated containing an oxygen-containing hydrocarbon compound derived from an animal or vegetable oils and fat and a sulfur-containing hydrocarbon compound and then hydroisomerizing the resultant hydrotreated oil, wherein a yield of a fraction having a boiling range of 140 to 300° C. is 70 mass % or more; an isoparaffin content is 80 mass % or more; a content of isoparaffin having 2 or more branches is 17 mass % or more; an aromatic content is less than 0.1 vol %; an olefin content is less than 0.1 vol %; a sulfur content is less than 1 mass ppm; and an oxygen content is less than 0.1 mass %.

Abstract translation: 本发明的航空燃料油基质是通过加氢处理含有来源于动植物油脂和含硫烃化合物的含氧烃化合物的待处理油，然后将得到的加氢处理油加氢异构化得到的，其中 沸点140〜300℃的馏分的产率为70质量％以上， 异链烷烃含量为80质量％以上; 具有2个以上分支的异链烷烃的含量为17质量％以上; 芳族含量小于0.1体积％; 烯烃含量小于0.1vol％; 硫含量小于1质量ppm; 氧含量小于0.1质量％。

公开(公告)号：US09504983B2

公开(公告)日：2016-11-29

申请号：US14509084

申请日：2014-10-08

Applicant: Karlton D. Krause

Inventor： Karlton D. Krause

IPC: B01J19/00 ,  B01J19/18 ,  B01J19/20 ,  C10G1/02 ,  C10L1/02 ,  C10L1/04 ,  C10G1/00 ,  C10L1/00 ,  A01C3/00

CPC classification number: B01J19/20 ,  C10G1/02 ,  C10G2300/1011 ,  C10L1/02 ,  C10L1/04 ,  Y02P30/20

Abstract: A system for converting animal waste into fuel, oil and other useful products is presented and includes a confinement building, a waste storage facility or lagoon for holding animal waste, a solids separating system for separating solids from liquids, a mixing and macerating unit for mixing the proper combination of fluids and solids and for managing the particle size, a pumping unit for pressurizing the system, a first heat exchanger unit, a reactor vessel, a second heat exchanger unit, an oil and water separating unit and an oil storage facility. The reactor vessel includes at least one auger blade that extend around a centrally positioned column that conducts heat into the reactor vessel. The animal waste is pumped through the reactor vessel as heated is applied. The heat and pressure converts the animal waste to oil and water which is later separated.

Abstract translation: 提出了将动物废物转化为燃料，油和其他有用产品的系统，其中包括一个封闭式建筑物，一个用于保存动物废物的废物储存设施或泻湖，用于从液体中分离固体的固体分离系统，用于混合的混合和浸渍装置 流体和固体的适当组合和用于管理颗粒尺寸的组合，用于对系统加压的泵送单元，第一热交换器单元，反应器容器，第二热交换器单元，油和水分离单元以及储油设备。 反应堆容器包括至少一个螺旋叶片，其绕中心定位的塔延伸，其将热量传导到反应器容器中。 当加热时，动物废物被泵送通过反应器容器。 热和压力将动物废物转化为稍后分离的油和水。

公开(公告)号：US20160333307A1

公开(公告)日：2016-11-17

申请号：US15111723

申请日：2015-01-16

Applicant: CALYSTA, INC.

Inventor： Howard Lam Ho Fong ,  John H Grate ,  Luan Nguyen ,  Joshua A. Silverman ,  Lisa Marie Newman ,  Lorraine Joan Giver ,  Drew D. Regitsky

IPC: C12N1/20 ,  A23N17/00 ,  C12R1/01 ,  C10L1/08 ,  C10G3/00 ,  C10L1/04 ,  C10L1/06 ,  A23K10/10 ,  C12N15/74

CPC classification number: C12N1/20 ,  A23K10/10 ,  A23N17/00 ,  B01D53/85 ,  B01D2251/95 ,  B01D2256/24 ,  B01D2256/245 ,  B01D2257/304 ,  B01D2258/05 ,  C10G3/00 ,  C10G2300/1025 ,  C10G2300/202 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10L1/04 ,  C10L1/06 ,  C10L1/08 ,  C10L3/102 ,  C10L2290/544 ,  C12N9/0051 ,  C12N9/0069 ,  C12N15/74 ,  C12P7/6463 ,  C12R1/01 ,  Y02A50/2359 ,  Y02P30/20

Abstract: The present disclosure provides compositions and methods for using recombinant C1 metabolizing microorganisms capable of metabolizing sulfur containing compounds and other contaminants to biologically convert sour or acidic natural gas into high-value molecules, and to allow recovery of stranded oil.

Abstract translation: 本公开提供使用能够代谢含硫化合物和其它污染物的重组C1代谢微生物的组合物和方法，以将酸性或酸性天然气生物转化为高价值分子，并允许回收绞股油。

公开(公告)号：US20160319201A1

公开(公告)日：2016-11-03

申请号：US15144222

申请日：2016-05-02

Applicant: Cool Planet Energy Systems, Inc.

Inventor： Michael C. CHEIKY ,  Rajashekharam MALYALA

IPC: C10G1/00 ,  C10B53/02 ,  C10L1/04 ,  C10G3/00 ,  C10G50/00

CPC classification number: C10G1/002 ,  C10B53/02 ,  C10G3/42 ,  C10G50/00 ,  C10L1/04 ,  C10L3/08 ,  C10L2200/0469 ,  C10L2290/06 ,  Y02E50/13 ,  Y02E50/14 ,  Y02E50/32 ,  Y02P30/20

Abstract: Multiple catalytic processing stations enable a method for producing volatile gas streams from biomass decomposition at discrete increasing temperatures. These catalytic processing stations can be programmed to maximize conversion of biomass to useful renewable fuel components based on input feedstock and desired outputs.

Abstract translation: 多个催化加工站实现了在不断增加的温度下从生物量分解产生挥发性气体流的方法。 这些催化加工站可以被编程为基于输入原料和期望的输出使生物质转化成有用的可再生燃料组分。

公开(公告)号：US09469827B2

公开(公告)日：2016-10-18

申请号：US14590737

申请日：2015-01-06

Applicant: Elevance Renewable Sciences, Inc.

Inventor： Steven A. Cohen ,  Melvin L. Luetkens, Jr. ,  Chander Balakrishnan ,  Robert Snyder

IPC: C07C1/00 ,  C07C5/03 ,  C07C1/24 ,  C11C1/08 ,  C10G45/00 ,  C10G45/58 ,  C10G50/00 ,  C10G65/04 ,  C11B3/00 ,  C10L1/02 ,  C10L1/08 ,  C11C3/00 ,  C10G3/00 ,  C07C67/03 ,  C07C67/54 ,  C07C6/04 ,  C07C51/09 ,  C07C2/86

CPC classification number: C10G3/42 ,  C07C2/862 ,  C07C6/04 ,  C07C51/09 ,  C07C67/03 ,  C07C67/54 ,  C07C2531/14 ,  C07C2531/24 ,  C10G45/00 ,  C10G45/58 ,  C10G50/00 ,  C10G65/043 ,  C10G69/02 ,  C10G2300/1011 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/1092 ,  C10G2300/1096 ,  C10G2300/202 ,  C10G2300/30 ,  C10G2300/301 ,  C10G2300/307 ,  C10G2300/308 ,  C10G2300/44 ,  C10G2400/00 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10G2400/20 ,  C10G2400/22 ,  C10L1/026 ,  C10L1/04 ,  C10L1/08 ,  C10L2200/0469 ,  C11B3/00 ,  C11C1/08 ,  C11C3/003 ,  Y02E50/13 ,  Y02P30/20 ,  Y02T50/678 ,  C07C69/533 ,  C07C57/03 ,  C07C57/12 ,  C07C11/02

Abstract: Methods are provided for refining natural oil feedstocks. 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 olefins from the esters in the metathesized product. In certain embodiments, the methods further comprise hydrogenating the olefins under conditions sufficient to form a fuel composition. In certain embodiments, the methods further comprise transesterifying the esters in the presence of an alcohol to form a transesterified product.