CN102712856A - 用于生产具有低的芳族化合物含量的烃流体的方法 - Google Patents
用于生产具有低的芳族化合物含量的烃流体的方法 Download PDFInfo
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- CN102712856A CN102712856A CN2010800618288A CN201080061828A CN102712856A CN 102712856 A CN102712856 A CN 102712856A CN 2010800618288 A CN2010800618288 A CN 2010800618288A CN 201080061828 A CN201080061828 A CN 201080061828A CN 102712856 A CN102712856 A CN 102712856A
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- 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
- C10G45/44—Hydrogenation of the aromatic hydrocarbons
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- 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
- C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
- C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
- C10G65/04—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps
- C10G65/08—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps at least one step being a hydrogenation of the aromatic hydrocarbons
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- 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
- C10G2300/1051—Kerosene having a boiling range of about 180 - 230 °C
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- 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
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- 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
- C10G2300/1059—Gasoil having a boiling range of about 330 - 427 °C
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- 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
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- 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
- C10G2300/301—Boiling range
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- 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
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/4006—Temperature
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- 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
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/4012—Pressure
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- 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
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/4018—Spatial velocity, e.g. LHSV, WHSV
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- 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
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/4081—Recycling aspects
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- 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
- C10G2400/18—Solvents
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- 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)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Description
特性 | 单位 | 方法 | T1 | T2 | D1 | D2 | D3 |
在15℃的密度 | kg/m3 | ASTM D4052 | 842 | 847 | 823 | 823 | 822 |
赛波特色度 | ASTM D56 | 30 | 30 | >+30 | >+30 | ||
硫ppm | ppm | ASTM D5453 | <1 | <1 | <1 | ||
蒸馏IBP | ℃ | ASTM D86 | 237 | 305 | 231 | 243 | 278 |
蒸馏FBP | ℃ | ASTM D86 | 287 | 364 | 266 | 286 | 309 |
闪点 | ℃ | ASTM D93 | 100 | 154 | 100 | 109 | 138 |
苯胺点 | ℃ | ASTM D611 | 76 | 89 | 79 | 84 | 89 |
在40℃的粘度 | mm2/c | ASTM 445 | 3.0 | 5.2 | 2.4 | 3.0 | 4.0 |
倾点℃ | ℃ | ASTM D97 | -40 | -12 | -33 | -21 | -12 |
芳族化合物 | ppm | UV法 | 42 | 1840 | 12 | 24 | 48 |
环烷烃 | 重量% | GC | 78.9 | 71.7 | 55.8 | 52.1 | 44.3 |
单环烷烃 | 重量% | GC | 25.3 | 22.9 | 20.8 | 20.3 | 18.4 |
多环烷烃 | 重量% | GC | 53.6 | 48.8 | 35.0 | 31.8 | 25.8 |
链烷烃 | 重量% | GC | 21.1 | 28.3 | 44.2 | 47.9 | 55.7 |
异链烷烃 | 重量% | GC | 15.1 | 20.9 | 30.2 | 32.0 | 38.2 |
正链烷烃 | 重量% | GC | 6.0 | 7.4 | 13.9 | 15.9 | 17.5 |
Claims (31)
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/IB2009/056017 WO2011061576A1 (en) | 2009-11-20 | 2009-11-20 | Process for the production of hydrocarbon fluids having a low aromatic content |
IBPCT/IB2009/056017 | 2009-11-20 | ||
PCT/IB2010/055313 WO2011061716A2 (en) | 2009-11-20 | 2010-11-19 | Process for the production of hydrocarbon fluids having a low aromatic content |
Publications (2)
Publication Number | Publication Date |
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CN102712856A true CN102712856A (zh) | 2012-10-03 |
CN102712856B CN102712856B (zh) | 2019-08-13 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201080061828.8A Active CN102712856B (zh) | 2009-11-20 | 2010-11-19 | 用于生产具有低的芳族化合物含量的烃流体的方法 |
Country Status (9)
Country | Link |
---|---|
US (1) | US9315742B2 (zh) |
EP (1) | EP2501784B1 (zh) |
KR (1) | KR101605787B1 (zh) |
CN (1) | CN102712856B (zh) |
BR (1) | BR112012012090B1 (zh) |
ES (1) | ES2669030T3 (zh) |
RU (1) | RU2566363C2 (zh) |
TW (1) | TWI507517B (zh) |
WO (2) | WO2011061576A1 (zh) |
Cited By (6)
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CN104910950A (zh) * | 2015-05-15 | 2015-09-16 | 东北石油大学 | 石油工业环保型钻井泥浆用油 |
CN104981534A (zh) * | 2012-12-10 | 2015-10-14 | 道达尔销售服务公司 | 用于获得具有高于300℃的沸腾温度和低于或等于-25℃的倾点的烃溶剂的方法 |
CN105793397A (zh) * | 2013-11-18 | 2016-07-20 | 道达尔销售服务公司 | 具有低芳族烃和硫含量的烃流体的生产方法 |
CN105992809A (zh) * | 2013-12-23 | 2016-10-05 | 道达尔销售服务公司 | 用于从石油馏分中除去芳族化合物的改善的方法 |
CN107690469A (zh) * | 2015-05-20 | 2018-02-13 | 总和营销服务 | 可生物降解的烃类流体的生产方法 |
CN110168064A (zh) * | 2016-10-27 | 2019-08-23 | 道达尔销售服务公司 | 生物可降解烃流体用作钻井液的用途 |
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WO2011061575A1 (en) * | 2009-11-20 | 2011-05-26 | Total Raffinage Marketing | Process for the production of hydrocarbon fluids having a low aromatic content |
WO2011061576A1 (en) * | 2009-11-20 | 2011-05-26 | Total Raffinage Marketing | Process for the production of hydrocarbon fluids having a low aromatic content |
KR101797771B1 (ko) | 2011-11-01 | 2017-12-13 | 에스케이이노베이션 주식회사 | 다환 방향족 화합물을 다량 포함하는 유분으로부터 방향족 탄화수소 및 올레핀을 제조하는 방법 |
KR101603061B1 (ko) * | 2015-03-30 | 2016-03-14 | 대흥특수화학(주) | 역유화 중합 방법에 의한 고 증점제 및 그 제조방법 |
EP3294841B1 (en) | 2015-05-12 | 2022-07-13 | Ergon, Inc. | Process for production of high performance process oil based on distilled aromatic extracts |
KR102608627B1 (ko) | 2015-05-12 | 2023-12-04 | 에르곤,인크 | 고성능 공정 오일 |
EP3095839A1 (en) * | 2015-05-20 | 2016-11-23 | Total Marketing Services | Biodegradable hydrocarbon fluids by hydrogenation |
FR3046176A1 (fr) * | 2015-12-23 | 2017-06-30 | Axens | Procede d'hydrotraitement ou d'hydroconversion avec striper et ballon separateur basse pression sur la section de fractionnement |
US10494579B2 (en) * | 2016-04-26 | 2019-12-03 | Exxonmobil Research And Engineering Company | Naphthene-containing distillate stream compositions and uses thereof |
CN107460005B (zh) * | 2017-07-26 | 2019-05-21 | 天津大学 | 利用生物油催化加氢耦合催化裂化制备芳香烃和烯烃的方法及装置 |
KR101971360B1 (ko) * | 2017-10-30 | 2019-04-22 | 한화토탈 주식회사 | 나프텐 함량이 풍부한 탈방향족 탄화수소 유체의 제조 방법 |
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US10876055B2 (en) * | 2018-12-11 | 2020-12-29 | Phillips 66 Company | Hydrocracking process for producing distillate or naptha |
US11046899B2 (en) | 2019-10-03 | 2021-06-29 | Saudi Arabian Oil Company | Two stage hydrodearylation systems and processes to convert heavy aromatics into gasoline blending components and chemical grade aromatics |
US11142706B2 (en) | 2020-02-11 | 2021-10-12 | Saudi Arabian Oil Company | Processes and systems for petrochemical production integrating fluid catalytic cracking and deep hydrogenation of fluid catalytic cracking reaction products |
US11142711B2 (en) | 2020-02-11 | 2021-10-12 | Saudi Arabian Oil Company | Processes and systems for petrochemical production integrating deep hydrogenation of middle distillates |
US11124716B2 (en) | 2020-02-11 | 2021-09-21 | Saudi Arabian Oil Company | Processes and systems for petrochemical production integrating coking and deep hydrogenation of coking reaction products |
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FR3112076B1 (fr) | 2020-07-01 | 2022-12-16 | Oreal | Composition biphasée comprenant un tensioactif alkylpolyglycoside, un diol particulier et un composé alcane, ester ou éther comprenant de 15 à 30 atomes de carbone |
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2009
- 2009-11-20 WO PCT/IB2009/056017 patent/WO2011061576A1/en active Application Filing
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2010
- 2010-11-19 KR KR1020127015954A patent/KR101605787B1/ko active IP Right Grant
- 2010-11-19 ES ES10793320.2T patent/ES2669030T3/es active Active
- 2010-11-19 US US13/510,252 patent/US9315742B2/en active Active
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Cited By (10)
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CN104981534A (zh) * | 2012-12-10 | 2015-10-14 | 道达尔销售服务公司 | 用于获得具有高于300℃的沸腾温度和低于或等于-25℃的倾点的烃溶剂的方法 |
CN104981534B (zh) * | 2012-12-10 | 2017-12-08 | 道达尔销售服务公司 | 用于获得具有高于300℃的沸腾温度和低于或等于‑25℃的倾点的烃溶剂的方法 |
CN105793397A (zh) * | 2013-11-18 | 2016-07-20 | 道达尔销售服务公司 | 具有低芳族烃和硫含量的烃流体的生产方法 |
CN105793397B (zh) * | 2013-11-18 | 2020-07-21 | 道达尔销售服务公司 | 具有低芳族烃和硫含量的烃流体的生产方法 |
CN105992809A (zh) * | 2013-12-23 | 2016-10-05 | 道达尔销售服务公司 | 用于从石油馏分中除去芳族化合物的改善的方法 |
CN104910950A (zh) * | 2015-05-15 | 2015-09-16 | 东北石油大学 | 石油工业环保型钻井泥浆用油 |
CN107690469A (zh) * | 2015-05-20 | 2018-02-13 | 总和营销服务 | 可生物降解的烃类流体的生产方法 |
CN107690469B (zh) * | 2015-05-20 | 2021-06-29 | 总和营销服务 | 可生物降解的烃类流体的生产方法 |
CN110168064A (zh) * | 2016-10-27 | 2019-08-23 | 道达尔销售服务公司 | 生物可降解烃流体用作钻井液的用途 |
CN110168064B (zh) * | 2016-10-27 | 2023-05-09 | 道达尔销售服务公司 | 生物可降解烃流体用作钻井液的用途 |
Also Published As
Publication number | Publication date |
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WO2011061716A3 (en) | 2012-03-08 |
TW201139647A (en) | 2011-11-16 |
WO2011061576A1 (en) | 2011-05-26 |
EP2501784A2 (en) | 2012-09-26 |
BR112012012090A2 (pt) | 2018-03-20 |
TWI507517B (zh) | 2015-11-11 |
BR112012012090B1 (pt) | 2019-02-05 |
RU2012120281A (ru) | 2013-12-27 |
US9315742B2 (en) | 2016-04-19 |
EP2501784B1 (en) | 2018-04-18 |
US20130001127A1 (en) | 2013-01-03 |
ES2669030T3 (es) | 2018-05-23 |
RU2566363C2 (ru) | 2015-10-27 |
CN102712856B (zh) | 2019-08-13 |
KR20120117786A (ko) | 2012-10-24 |
KR101605787B1 (ko) | 2016-03-23 |
WO2011061716A2 (en) | 2011-05-26 |
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