公开(公告)号：WO2014135968A1

公开(公告)日：2014-09-12

申请号：PCT/IB2014/000465

申请日：2014-01-30

Applicant: VEROLUBE, INC.

Inventor： MACDONALD, Martin, R.

IPC: C10M175/00 ,  C10G45/58 ,  C10G67/02 ,  C10G7/00 ,  C10G7/06 ,  C10G71/00

CPC classification number: C10G53/04 ,  C07C5/02 ,  C07C7/005 ,  C10G7/00 ,  C10G7/003 ,  C10G7/006 ,  C10G21/006 ,  C10G21/02 ,  C10G21/16 ,  C10G21/18 ,  C10G21/20 ,  C10G21/24 ,  C10G45/04 ,  C10G53/06 ,  C10G53/08 ,  C10G67/04 ,  C10G67/14 ,  C10G2300/1007 ,  C10G2300/44 ,  C10G2400/22 ,  C10G2400/30 ,  C11B3/006

Abstract: A method for producing ILSAC GF5 or higher compatible oils from used oil, comprising separating material having a boiling point less than about 350°F from recovered oil to produce de- volatized oil fraction and light oil fraction. Separating material with a boiling point greater than about 350°F and less than about 650°F from the de-volatized oil fraction to produce fuel oil fraction and heavy oil fraction. Separating material with a boiling point greater than about 1200°F from the heavy oil fraction to produce partially purified oil fraction and residual fraction. Treating the partially purified oil fraction to separate it into purified oil fraction and contaminant fraction. Hydrogenating the contaminant fraction to remove predetermined compounds, further saturating the fraction and thereby creating a saturated oil fraction. Fractionating the saturated oil stream to produce one or more of naphtha fraction, diesel oil fraction and base oil fraction.

Abstract translation: 一种用于从废油中生产ILSAC GF5或更高相容的油的方法，包括从回收的油中分离沸点低于约350°F的材料以产生脱挥发油的油馏分和轻油馏分。 从脱挥发油的油馏分中分离沸点大于约350°F且小于约650°F的材料，以产生燃料油馏分和重油馏分。 从重油馏分中分离沸点大于约1200°F的材料，以产生部分纯化的油馏分和残余馏分。 处理部分纯化的油馏分将其分离成纯化的油馏分和污染物馏分。 将污染物馏分氢化以除去预定的化合物，进一步饱和馏分，从而产生饱和油馏分。 分馏饱和油流以产生一种或多种石脑油馏分，柴油馏分和基础油馏分。

公开(公告)号：WO2011143728A1

公开(公告)日：2011-11-24

申请号：PCT/BR2011/000095

申请日：2011-04-07

Applicant: PETRÓLEO BRASILEIRO S.A. - PETROBRAS ,  VIDAL VIEIRA, Jose Antonio ,  IURK ROCHA, Mauro ,  LOPES CARVALHO, Roberto ,  VIEIRA ALVES, Marcelo

Inventor： VIDAL VIEIRA, Jose Antonio ,  IURK ROCHA, Mauro ,  LOPES CARVALHO, Roberto ,  VIEIRA ALVES, Marcelo

IPC: C07C67/03 ,  C10G7/06 ,  C11C1/02 ,  C11C1/10 ,  C10L1/02 ,  C10L1/19 ,  C10L1/16 ,  C10G3/00

CPC classification number: C11B3/12 ,  C07C67/03 ,  C10G2300/1014 ,  C10G2300/1051 ,  C10G2300/30 ,  C10G2400/08 ,  C10L1/02 ,  C10L1/026 ,  C10L1/04 ,  C10L1/19 ,  C10L2200/043 ,  C10L2200/0476 ,  C10L2270/04 ,  C11C3/003 ,  Y02E50/13 ,  Y02P30/20 ,  Y02T50/678 ,  C07C69/24 ,  C07C69/52

Abstract: A presente invenção diz respeito a um processo de obtenção de bioquerosene de aviação e a uma composição de querosene de aviação contendo o bioquerosene de aviação assim produzido. O processo consiste em simultaneamente combinar três condições básicas: seleção de matéria-prima; condições de processamento; e controle de determinadas características do produto. A composição se classifica como uma composição semi-sintética de querosene de aviação podendo conter até 20% em peso do bioquerosene de aviação, atendendo os limites preconizados nas especificações internacionais para querosene de aviação.

Abstract translation: 本发明涉及生产航空生物猩猩的方法和航空煤油组合物，其包含如此生产的航空生物猩猩。 该方法包括三个基本条件的同时组合：原料的选择; 加工条件; 并控制定义的产品特性。 该组合物分级为半合成航空煤油组合物，其可以含有高达20重量％的航空生物蛋白，符合与航空煤油相关的国际标准中规定的限度。

公开(公告)号：WO2008027130A1

公开(公告)日：2008-03-06

申请号：PCT/US2007/016707

申请日：2007-07-25

Applicant: EXXONMOBIL CHEMICAL PATENTS INC. ,  MCCOY, James, N. ,  KEUSENKOTHEN, Paul, F. ,  SRIVASTAVA, Alok ,  GRAHAM, James, E.

Inventor： MCCOY, James, N. ,  KEUSENKOTHEN, Paul, F. ,  SRIVASTAVA, Alok ,  GRAHAM, James, E.

IPC: C10G7/06

CPC classification number: C10G7/06

Abstract: A process is described for producing deasphalted steam cracker tar comprising feeding steam cracker tar to a vacuum pipestill (VPS) including a flash zone separated from a zone comprising trays by at least one annular entrainment ring and obtaining as an overheads a deasphalted tar product and as a bottoms an asphaltenic heavy tar product. Also according to the invention, there is a system for the upgrading of tar comprising said VPS with at least one annular entrainment ring.

Abstract translation: 描述了一种用于生产脱沥青蒸汽裂化器焦油的方法，其包括将蒸气裂解焦油加入到真空管道（VPS）中，所述真空管道（VPS）包括通过至少一个环形夹带环从包含塔板的区域分离的闪蒸区域，并获得脱沥青焦油产物和作为塔顶馏出物， 一种沥青质焦油产品的底部。 同样根据本发明，存在一种用于使包含所述VPS的焦油升级至少一个环形夹带环的系统。

公开(公告)号：WO2002036712A3

公开(公告)日：2002-05-10

申请号：PCT/US2001/045530

申请日：2001-11-02

Applicant: HUCKER, Kenneth ,  BRASS, Sanford, P.

Inventor： HUCKER, Kenneth ,  BRASS, Sanford, P.

IPC: C10G7/06

Abstract: A process and apparatus are disclosed that relate generally to a process for reducing harmful or unwanted emissions during the production of asphalt, such as blue smoke. The process includes the introduction of a pump around of the wax oil fraction for re-introduction into the vacuum tower. Additional desirable features includes stripping trays below the wax oil collection tray and the feed zone. The results is to produce an asphalt product that creates less blue smoke in the hot mix plant. Another desirable feature is that a product can be created that meets Performance Grade specification with the addition of polymers or other additives.

公开(公告)号：WO0236712A2

公开(公告)日：2002-05-10

申请号：PCT/US0145530

申请日：2001-11-02

Applicant: HUCKER KENNETH ,  BRASS SANFORD P

Inventor： HUCKER KENNETH ,  BRASS SANFORD P

IPC: C10C3/06 ,  C10C3/00 ,  C10G7/06

CPC classification number: C10C3/00 ,  C10G7/06

Abstract: A process and apparatus are disclosed that relate generally to a process for reducing harmful or unwanted emissions during the production of asphalt, such as blue smoke. The process includes the introduction of a pump around of the wax oil fraction for re-introduction into the vacuum tower. Additional desirable features includes stripping trays below the wax oil collection tray and the feed zone. The results is to produce an asphalt product that creates less blue smoke in the hot mix plant. Another desirable feature is that a product can be created that meets Performance Grade specification with the addition of polymers or other additives.

Abstract translation: 公开了一种方法和装置，其通常涉及在生产沥青（例如蓝色烟雾）期间减少有害或不需要的排放物的方法。 该方法包括在蜡油馏分周围引入泵以重新引入真空塔。 另外期望的特征包括在蜡油收集托盘和进料区下方的剥离托盘。 结果是生产在热混合设备中产生较少蓝色烟雾的沥青产品。 另一个期望的特征是可以通过添加聚合物或其它添加剂来创建满足性能等级规格的产品。

公开(公告)号：WO99040988A1

公开(公告)日：1999-08-19

申请号：PCT/RU1998/000034

申请日：1998-02-13

IPC: B01D3/10 ,  C10G7/06

CPC classification number: C10G7/06 ,  B01D3/10 ,  Y10S203/16

Abstract: The present invention pertains to the field of petro-chemistry and to the petroleum-conversion industry. This invention essentially relates to a system which comprises a vacuum rectifying column as well as a vacuum generating device on the basis of a liquid-gas jet apparatus. The system of the present invention further comprises a jet pump, wherein the nozzle of said pump is connected to a duct for discharging the liquid fraction in the column, while its inlet for the medium to be pumped is connected to the outlet of the liquid-gas jet apparatus. The outlet of said pump is further connected to a separator. The system of the present invention has an increased efficiency when compared with analogous systems or its prototype.

Abstract translation: 本发明涉及石油化学和石油转化工业领域。 本发明基本上涉及一种基于液体气体喷射装置的真空精馏塔以及真空发生装置的系统。 本发明的系统还包括喷射泵，其中所述泵的喷嘴连接到用于排出塔中的液体部分的管道，而用于待泵送的介质的入口连接到液 - 喷气装置 所述泵的出口进一步连接到分离器。 与类似系统或其原型相比，本发明的系统具有更高的效率。

公开(公告)号：WO2021224949A1

公开(公告)日：2021-11-11

申请号：PCT/IT2021/050122

申请日：2021-04-21

Applicant: PATRON, Luigi

Inventor： PATRON, Luigi

IPC: C10G7/06 ,  C10G47/26 ,  C10G47/36 ,  C10G49/12 ,  C10G49/22 ,  C10G49/26 ,  B01J8/00 ,  B01J8/18 ,  B01J8/22 ,  B01J8/44

Abstract: The hydrogenation capacity of an upflow hydrocarbon hydrotreatment reactor is increased by expanding the gas-liquid contact surface.

公开(公告)号：WO2019053323A1

公开(公告)日：2019-03-21

申请号：PCT/FI2018/050640

申请日：2018-09-11

Applicant: NESTE OYJ

Inventor： MARKKANEN, Varpu

IPC: C10G67/04 ,  C10G21/00 ,  C10G47/00 ,  C10G7/06 ,  C10L1/02

Abstract: The present disclosure relates to marine fuel compositions having low sulfur content and processes for making such compositions.

公开(公告)号：WO2018187112A1

公开(公告)日：2018-10-11

申请号：PCT/US2018/024719

申请日：2018-03-28

Applicant: EXXONMOBIL RESEARCH AND ENGINEERING COMPANY

Inventor： BROWN, Stephen, H. ,  CUNNINGHAM, Brian, A. ,  SMILEY, Randolph, J. ,  ILIAS, Samia ,  RAICH, Brenda, A. ,  LE, Tien, V.

IPC: C10G55/06 ,  C10G55/08 ,  C10G67/04 ,  C10G7/06 ,  C10G11/05 ,  C10G21/00

Abstract: Systems and methods are provided for improving operation of a fluid catalytic cracker as part of an integrated processing environment including a deasphalting unit and a hydroprocessor. Optionally, a coker can be included in the integrated system to allow for further improvements. The improved processing can be facilitated based on a process configuration where a combination of deasphalting and hydroprocessing are used to perform conversion on more refractory compounds, so that the fluid catalytic cracker can be operated at lower severity conditions. This can allow for improved production of desirable olefins and reduced production of light paraffins and coke. Additionally or alternately, the processing configuration can allow the bottoms fraction from fluid catalytic cracking to be incorporated into a higher value use than the typical regular sulfur fuel oil disposition.

公开(公告)号：WO2018094353A1

公开(公告)日：2018-05-24

申请号：PCT/US2017/062614

申请日：2017-11-20

Applicant: SAUDI ARABIAN OIL COMPANY ,  ARAMCO SERVICES COMPANY ,  AL-GHAMDI, Mohammed Saeed ,  BAHAMMAN, Bader ,  AL OSAIMI, Naif ,  BARNAWI, Sami

Inventor： AL-GHAMDI, Mohammed Saeed ,  BAHAMMAN, Bader ,  AL OSAIMI, Naif ,  BARNAWI, Sami

IPC: C10G35/04 ,  C10G47/00 ,  C10G69/08 ,  C10G7/06 ,  C10G9/36 ,  C10G21/00

Abstract: Process scheme configurations are disclosed that enable conversion of crude oil feeds with several processing units in an integrated manner into petrochemicals. The designs utilize minimum capital expenditures to prepare suitable feedstocks for the steam cracker complex. The integrated process for converting crude oil to petrochemical products including olefins and aromatics, and fuel products, includes mixed feed steam cracking, fluid catalytic cracking and conversion of naphtha to chemical rich reformate. Feeds to the mixed feed steam cracker include light products from hydroprocessing zones within the battery limits, recycle streams from the C3 and C4 olefins recovery steps, and raffinate from a pyrolysis gasoline and FCC naphtha aromatics extraction zone within the battery limits. Chemical reformate from straight run naphtha streams is used as an additional feed to the aromatics extraction zone and or the mixed feed steam cracker.