RU2013120517A - METHODS FOR PRODUCING DIESEL FRACTION SUBSTANCES HAVING IMPROVED COLD FLUIDITY PROPERTIES - Google Patents

METHODS FOR PRODUCING DIESEL FRACTION SUBSTANCES HAVING IMPROVED COLD FLUIDITY PROPERTIES Download PDF

Info

Publication number
RU2013120517A
RU2013120517A RU2013120517/04A RU2013120517A RU2013120517A RU 2013120517 A RU2013120517 A RU 2013120517A RU 2013120517/04 A RU2013120517/04 A RU 2013120517/04A RU 2013120517 A RU2013120517 A RU 2013120517A RU 2013120517 A RU2013120517 A RU 2013120517A
Authority
RU
Russia
Prior art keywords
diesel fraction
oxygen
paraffin
product stream
intermediate product
Prior art date
Application number
RU2013120517/04A
Other languages
Russian (ru)
Inventor
Питер Кокаефф
Сухейл Ф. АБДО
Original Assignee
Юоп Ллк
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Юоп Ллк filed Critical Юоп Ллк
Publication of RU2013120517A publication Critical patent/RU2013120517A/en

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/58—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
    • C10G45/60—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins characterised by the catalyst used
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G3/00—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
    • C10G3/42—Catalytic treatment
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G3/00—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
    • C10G3/50—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids in the presence of hydrogen, hydrogen donors or hydrogen generating compounds
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/58—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/02—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
    • C10L1/026—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only for compression ignition
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
    • C10L1/08—Liquid carbonaceous fuels essentially based on blends of hydrocarbons for compression ignition
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1011—Biomass
    • C10G2300/1014—Biomass of vegetal origin
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1011—Biomass
    • C10G2300/1018—Biomass of animal origin
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1022—Fischer-Tropsch products
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1037—Hydrocarbon fractions
    • C10G2300/1048—Middle distillates
    • C10G2300/1055—Diesel having a boiling range of about 230 - 330 °C
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/20—Characteristics of the feedstock or the products
    • C10G2300/201—Impurities
    • C10G2300/202—Heteroatoms content, i.e. S, N, O, P
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/20—Characteristics of the feedstock or the products
    • C10G2300/30—Physical properties of feedstocks or products
    • C10G2300/304—Pour point, cloud point, cold flow properties
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/70—Catalyst aspects
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/04—Diesel oil
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P30/00—Technologies relating to oil refining and petrochemical industry
    • Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

1. Способ (10) получения вещества дизельной фракции (42), имеющего улучшенные свойства текучести на холоде, включающий стадии:обеспечения (12) парафинового сырья (15) дизельной фракции;получения (14) промежуточного потока (20) продукта, содержащего заранее определенное количество кислородсодержащих органосоединений из парафинового сырья дизельной фракции; иконтактирования (22) потока промежуточного продукта с катализатором депарафинизации в условиях процесса, при которых кислородсодержащие органосоединения химически взаимодействуют с катализатором депарафинизации для превращения части н-парафинов в потоке промежуточного продукта в изопарафины, одновременно понижая до минимума крекинг вещества дизельной фракции.2. Способ по п.1, где стадия обеспечения (12) парафинового сырья (15) дизельной фракции включает подачу парафинового сырья дизельной фракции, содержащего н-парафины и кислородсодержащие органосоединения, и где стадия получения (14) потока (20) промежуточного продукта включает удаление части кислородсодержащих органосоединений из парафинового сырья дизельной фракции, одновременно сохраняя в ней заранее определенное количество кислородсодержащих органосоединений.3. Способ по п.2, где заранее определенное количество кислородсодержащих органосоединений, сохраняющееся в парафиновом сырье (15) дизельной фракции, содержит от 200 до 2000 частей на миллион по массе кислорода.4. Способ по п.2, где стадия подачи парафинового сырья (15) дизельной фракции включает получение парафинового сырья дизельной фракции из биовозобновляемого источника.5. Способ по п.2, где стадия подачи парафинового сырья (15) дизельной фракции включ�1. Method (10) for producing a diesel fraction substance (42) having improved cold flow properties, including the stages of: providing (12) paraffin raw materials (15) of the diesel fraction; obtaining (14) an intermediate stream (20) of a product containing a predetermined the amount of oxygen-containing organocompounds from paraffin raw materials of the diesel fraction; and contacting (22) the intermediate product stream with a dewaxing catalyst under process conditions in which oxygen-containing organo compounds chemically react with the dewaxing catalyst to convert a portion of the n-paraffins in the intermediate product stream into isoparaffins, while simultaneously minimizing the cracking of the diesel fraction substance. The method according to claim 1, where the step of providing (12) paraffin feedstock (15) to the diesel fraction includes supplying paraffin feedstock to the diesel fraction containing n-paraffins and oxygen-containing organo compounds, and where the step of obtaining (14) the intermediate product stream (20) includes removing part of oxygen-containing organo-compounds from the paraffin raw material of the diesel fraction, while simultaneously maintaining a predetermined amount of oxygen-containing organo-compounds in it.3. The method according to claim 2, wherein the predetermined amount of oxygen-containing organo compounds stored in the paraffin feedstock (15) of the diesel fraction contains from 200 to 2000 ppm by weight of oxygen.4. The method according to claim 2, where the step of supplying the paraffin raw material (15) to the diesel fraction includes obtaining the paraffin raw material of the diesel fraction from a biorenewable source. The method according to claim 2, where the stage of supplying paraffin raw materials (15) to the diesel fraction includes

Claims (10)

1. Способ (10) получения вещества дизельной фракции (42), имеющего улучшенные свойства текучести на холоде, включающий стадии:1. A method (10) for producing a diesel fraction substance (42) having improved cold flow properties, comprising the steps of: обеспечения (12) парафинового сырья (15) дизельной фракции;providing (12) paraffin feed (15) of the diesel fraction; получения (14) промежуточного потока (20) продукта, содержащего заранее определенное количество кислородсодержащих органосоединений из парафинового сырья дизельной фракции; иobtaining (14) an intermediate stream (20) of a product containing a predetermined amount of oxygen-containing organocompounds from paraffin feed of a diesel fraction; and контактирования (22) потока промежуточного продукта с катализатором депарафинизации в условиях процесса, при которых кислородсодержащие органосоединения химически взаимодействуют с катализатором депарафинизации для превращения части н-парафинов в потоке промежуточного продукта в изопарафины, одновременно понижая до минимума крекинг вещества дизельной фракции.contacting (22) the intermediate product stream with a dewaxing catalyst under process conditions in which oxygen-containing organocompounds chemically interact with the dewaxing catalyst to convert part of the n-paraffins in the intermediate product stream to isoparaffins, while minimizing cracking of the diesel fraction substance. 2. Способ по п.1, где стадия обеспечения (12) парафинового сырья (15) дизельной фракции включает подачу парафинового сырья дизельной фракции, содержащего н-парафины и кислородсодержащие органосоединения, и где стадия получения (14) потока (20) промежуточного продукта включает удаление части кислородсодержащих органосоединений из парафинового сырья дизельной фракции, одновременно сохраняя в ней заранее определенное количество кислородсодержащих органосоединений.2. The method according to claim 1, where the step of providing (12) the paraffin feed (15) of the diesel fraction comprises supplying the paraffin feed of the diesel fraction containing n-paraffins and oxygen-containing organocompounds, and where the step of obtaining (14) the intermediate product stream (20) comprises removing part of the oxygen-containing organo compounds from the paraffin feed of the diesel fraction, while simultaneously preserving in it a predetermined amount of oxygen-containing organo compounds. 3. Способ по п.2, где заранее определенное количество кислородсодержащих органосоединений, сохраняющееся в парафиновом сырье (15) дизельной фракции, содержит от 200 до 2000 частей на миллион по массе кислорода.3. The method according to claim 2, where a predetermined amount of oxygen-containing organocompounds stored in the paraffin feed (15) of the diesel fraction contains from 200 to 2000 parts per million by weight of oxygen. 4. Способ по п.2, где стадия подачи парафинового сырья (15) дизельной фракции включает получение парафинового сырья дизельной фракции из биовозобновляемого источника.4. The method according to claim 2, where the step of supplying the paraffin feed (15) of the diesel fraction comprises obtaining paraffin feed of the diesel fraction from a bio-renewable source. 5. Способ по п.2, где стадия подачи парафинового сырья (15) дизельной фракции включает получение парафинового сырья дизельной фракции из монооксида углерода и водорода с помощью синтеза Фишера-Тропша.5. The method according to claim 2, where the step of supplying the paraffin feed (15) of the diesel fraction comprises producing paraffin feed of the diesel fraction from carbon monoxide and hydrogen using Fischer-Tropsch synthesis. 6. Способ по п.2, где стадия контактирования (22) потока (20) промежуточного продукта с катализатором депарафинизации включает гидроизомеризацию потока промежуточного продукта при температурах между 550°F (288°С) и 600°F (316°С).6. The method according to claim 2, wherein the step of contacting (22) the intermediate product stream (20) with a dewaxing catalyst comprises hydroisomerizing the intermediate product stream at temperatures between 550 ° F (288 ° C) and 600 ° F (316 ° C). 7. Способ по п.2, где стадия контактирования (22) потока (20) промежуточного продукта с катализатором депарафинизации включает гидроизомеризацию потока промежуточного продукта при давлении между 500 фунтами на квадратный дюйм избыточного давления (3447 килопаскалей) и 800 фунтами на квадратный дюйм избыточного давления (5516 килопаскалей).7. The method according to claim 2, wherein the step of contacting (22) the intermediate product stream (20) with a dewaxing catalyst comprises hydroisomerizing the intermediate product stream at a pressure between 500 psi (3447 kilopascals) and 800 psi (5516 kilopascals). 8. Способ по п.2, где стадия контактирования (22) потока (20) промежуточного продукта с катализатором депарафинизации включает гидроизомеризацию потока промежуточного продукта при одновременном добавлении водорода со скоростью 2500-5000 стандартных кубических футов на баррель (или 421,3-842,6 нормальных кубических метров на кубический метр).8. The method according to claim 2, wherein the step of contacting (22) the intermediate product stream (20) with a dewaxing catalyst comprises hydroisomerizing the intermediate product stream while adding hydrogen at a rate of 2500-5000 standard cubic feet per barrel (or 421.3-842, 6 normal cubic meters per cubic meter). 9. Способ по п.1, где кислородсодержащие органосоединения включают карбоновую кислоту.9. The method according to claim 1, where the oxygen-containing organocompounds include carboxylic acid. 10. Способ по п.1, где стадия обеспечения (12) парафинового сырья (15) дизельной фракции включает получение парафинового сырья дизельной фракции из источника на нефтяной основе, и где стадия получения (14) потока промежуточного продукта включает:10. The method according to claim 1, where the stage of providing (12) paraffin raw materials (15) of the diesel fraction includes obtaining paraffin raw materials of the diesel fraction from an oil-based source, and where the stage of obtaining (14) the intermediate product stream includes: гидроочистку (14) парафинового сырья дизельной фракции; и после гидроочистки, добавление заранее определенного количества кислородсодержащих органосоединений (18) к парафиновому сырью дизельной фракции. hydrotreating (14) of a paraffin feed of a diesel fraction; and after hydrotreating, adding a predetermined amount of oxygen-containing organocompounds (18) to the paraffin feed of the diesel fraction.
RU2013120517/04A 2010-10-13 2011-10-11 METHODS FOR PRODUCING DIESEL FRACTION SUBSTANCES HAVING IMPROVED COLD FLUIDITY PROPERTIES RU2013120517A (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US12/903,874 US20120090223A1 (en) 2010-10-13 2010-10-13 Methods for producing diesel range materials having improved cold flow properties
US12/903,874 2010-10-13
PCT/US2011/055666 WO2012051130A2 (en) 2010-10-13 2011-10-11 Methods for producing diesel range materials having improved cold flow properties

Publications (1)

Publication Number Publication Date
RU2013120517A true RU2013120517A (en) 2014-11-20

Family

ID=45932848

Family Applications (1)

Application Number Title Priority Date Filing Date
RU2013120517/04A RU2013120517A (en) 2010-10-13 2011-10-11 METHODS FOR PRODUCING DIESEL FRACTION SUBSTANCES HAVING IMPROVED COLD FLUIDITY PROPERTIES

Country Status (5)

Country Link
US (1) US20120090223A1 (en)
CN (1) CN103140572A (en)
RU (1) RU2013120517A (en)
WO (1) WO2012051130A2 (en)
ZA (1) ZA201303268B (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8624070B2 (en) 2010-12-13 2014-01-07 Exxonmobil Research And Engineering Company Phosphorus recovery from hydrothermal treatment of biomass
US8431756B2 (en) 2010-12-13 2013-04-30 Exxonmobil Research And Engineering Company Conversion catalysts and processes having oxygenate and water stability
US8487148B2 (en) 2010-12-13 2013-07-16 Exxonmobil Research And Engineering Company Hydrothermal treatment of biomass with heterogeneous catalyst
US8704019B2 (en) 2010-12-13 2014-04-22 Exxonmobil Research And Engineering Company Catalyst recovery in hydrothermal treatment of biomass
US8704020B2 (en) 2010-12-13 2014-04-22 Exxonmobil Research And Engineering Company Catalytic hydrothermal treatment of biomass
US9453169B2 (en) 2013-09-13 2016-09-27 Uop Llc Process for converting fischer-tropsch liquids and waxes into lubricant base stock and/or transportation fuels
US10988421B2 (en) 2013-12-06 2021-04-27 Exxonmobil Chemical Patents Inc. Removal of bromine index-reactive compounds
US10829697B2 (en) * 2015-07-27 2020-11-10 Uop Llc Processes for producing a fuel from a renewable feedstock
FI127307B (en) 2017-01-27 2018-03-15 Neste Oyj Refined fuel compositions and methods for their preparation

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5689031A (en) * 1995-10-17 1997-11-18 Exxon Research & Engineering Company Synthetic diesel fuel and process for its production
CN1233796C (en) * 2003-09-15 2005-12-28 中国石油化工股份有限公司 Technology for hydrogenating treatment of synthetizing diesel oil
WO2008035155A2 (en) * 2006-09-19 2008-03-27 Ben-Gurion University Of The Negev Research & Development Authority Reaction system for production of diesel fuel from vegetable and animal oils
JP5732398B2 (en) * 2008-11-06 2015-06-10 エクソンモービル リサーチ アンド エンジニアリング カンパニーＥｘｘｏｎ Ｒｅｓｅａｒｃｈ Ａｎｄ Ｅｎｇｉｎｅｅｒｉｎｇ Ｃｏｍｐａｎｙ Hydrotreatment of biodiesel fuels and blends

Also Published As

Publication number Publication date
CN103140572A (en) 2013-06-05
US20120090223A1 (en) 2012-04-19
WO2012051130A2 (en) 2012-04-19
ZA201303268B (en) 2014-07-30
WO2012051130A3 (en) 2012-07-19

Similar Documents

Publication Publication Date Title
RU2013120517A (en) METHODS FOR PRODUCING DIESEL FRACTION SUBSTANCES HAVING IMPROVED COLD FLUIDITY PROPERTIES
Zhang et al. Insights into the mechanism of ethanol formation from syngas on Cu and an expanded prediction of improved Cu-based catalyst
Unruh et al. Fischer− Tropsch synfuels from biomass: maximizing carbon efficiency and hydrocarbon yield
EA201071143A1 (en) METHOD FOR PRODUCING LIQUID HYDROCARBONS FROM NATURAL GAS
ECSP13012389A (en) METHOD FOR BIOMASS METHANE PRODUCTION
NZ592785A (en) Integrated process for the production of vinyl acetate from acetic acid via ethylene
WO2012087504A3 (en) Integrated biorefinery for production of liquid fuels
FI20105583L (en) Process and apparatus for producing hydrocarbons
WO2010006386A3 (en) Catalytic co2 methanation process
US20130090393A1 (en) Process for producing hydrocarbons from syngas
MY184088A (en) Catalyst
Gaikwad et al. Effect of cyclooctane and l-tryptophan on hydrate formation from an equimolar CO2–CH4 gas mixture employing a horizontal-tray packed bed reactor
RU2015142611A (en) METHOD FOR CARBONILATION OF DIMETHYL ETHER
MY166161A (en) Hydrocarbon compound synthesis reaction unit and operating method thereof
RU2015102090A (en) METHOD FOR PRODUCING A LIQUID HYDROCARBON PRODUCT FROM SYNTHESIS GAS PRODUCED FROM BIOMASS
WO2012087503A3 (en) Integrated biorefinery for production of liquid fuels
CN103459565B (en) The manufacture method of hydrocarbon feed
KR101362950B1 (en) Hydrorefining process
PL408081A1 (en) Method for obtaining biofuel using ethanol or alcohol mixtures and the biofuel or biocomponent for obtaining engine fuels
CN101397266B (en) Synthetic method of 3-aminopropionitrile and reaction-rectification coupling apparatus used therefor
Zang et al. Experimental study on hydrate formation with synthesized CH4/CO2/N2 ternary mixtures
CN105585484B (en) A kind of method for improving dimethoxym ethane carbonylation reaction catalyst performance
CA2835766C (en) Injection of an additive from a synthesis gas into a synthesis unit for hydrocarbons enabling a homogenous concentration of a catalyst to be monitored and maintained
CN103289769A (en) Method without circulation loop for producing synthetic natural gas by complete methanation of synthesis gas
US9815692B2 (en) Configurations and method of integrating a gas to liquids (GTL) plant in a refinery

Legal Events

Date Code Title Description
FA92 Acknowledgement of application withdrawn (lack of supplementary materials submitted)

Effective date: 20150312