JP5991562B2 - 原油全体を脱アスファルトおよび脱硫するための統合された方法 - Google Patents
原油全体を脱アスファルトおよび脱硫するための統合された方法 Download PDFInfo
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- JP5991562B2 JP5991562B2 JP2015516064A JP2015516064A JP5991562B2 JP 5991562 B2 JP5991562 B2 JP 5991562B2 JP 2015516064 A JP2015516064 A JP 2015516064A JP 2015516064 A JP2015516064 A JP 2015516064A JP 5991562 B2 JP5991562 B2 JP 5991562B2
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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
- C10G67/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only
- C10G67/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only
- C10G67/04—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only including solvent extraction as the refining step in the absence of hydrogen
- C10G67/0454—Solvent desasphalting
- C10G67/0463—The hydrotreatment being a hydrorefining
-
- 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
- C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
- C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
- C10G47/10—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
- C10G47/12—Inorganic carriers
- C10G47/16—Crystalline alumino-silicate carriers
- C10G47/20—Crystalline alumino-silicate carriers the catalyst containing other metals or compounds thereof
-
- 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
- C10G67/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only
- C10G67/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only
- C10G67/04—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only including solvent extraction as the refining step in the absence of hydrogen
- C10G67/0454—Solvent desasphalting
- C10G67/049—The hydrotreatment being a hydrocracking
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0913—Carbonaceous raw material
- C10J2300/0946—Waste, e.g. MSW, tires, glass, tar sand, peat, paper, lignite, oil shale
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
-
- 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
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
-
- 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
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
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- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Catalysts (AREA)
Description
11 反応室
12 アスファルト画分
13 脱アスファルト油(DAO)
14 水素化分解/水素化処理領域
15 ガス化室
16 酸素
17 水蒸気
18 水素
19 ガス
20 改質原油
21 ガス化生成物
Claims (13)
- 原油全体原料油中の不純物を削減する方法であって、
(i)第一反応室において、原料油を固体吸着剤と接触させて溶媒脱アスファルトして、アスファルト画分および脱アスファルト油(DAO)を生成する工程、
(ii)別個の第二反応室および第三反応室において、DAOおよびアスファルト画分を処理する工程、
(iii)第二反応室において、2〜40重量%の活性金属を含有し、0.33〜1.50cc/gmの細孔容積、250〜450m 2 /gの表面積および少なくとも50Åの平均細孔直径を有する触媒の存在下で、100〜200barの圧力、350℃〜500℃の温度、0.1〜4.0h −1 のLHSV、および500〜2500SLt/Ltの水素:DAO比で、DAOを水素化分解して、硫黄および窒素を除去し、DAOに含まれ、370℃を超える沸点を有する炭化水素を留分に転化させる工程であって、触媒の活性金属は、アルミナ、シリカまたはゼオライト担体上のNiまたはMoを含んでなる工程、
(iv)第三反応室において酸素および水蒸気とアスファルト画分とを混合して、アスファルト画分をガス化し、水素を生成する工程、および
(v)第三反応室において生成した水素を第二反応室に導入する工程
を含み、原油全体原料油の蒸留を伴わずに実施される、方法。 - 溶媒脱アスファルトする工程は、原油と3〜7個の炭素原子を有する溶媒とを、溶媒の臨界温度未満の温度および溶媒の臨界圧力未満の圧力で混合する工程を含む、請求項1に記載の方法。
- 溶媒はn−ブタンおよびイソブタンを含んでなる、請求項2に記載の方法。
- 原油と溶媒とを10:1〜200:1w/wの重量比で混合する、請求項2に記載の方法。
- 一連の複数の室でDAOを水素化分解する工程を含む、請求項1に記載の方法。
- 水素化分解室は固定床室、沸騰床室またはスラリー床室である、請求項1に記載の方法。
- 担体はゼオライトである、請求項1に記載の方法。
- ゼオライトは、水蒸気、アンモニアまたは酸の少なくとも1つによる処理によって改質されたものであり、少なくとも1種の遷移金属を含有する、請求項7に記載の方法。
- 少なくとも1種の遷移金属はZnまたはTiである、請求項8に記載の方法。
- 900℃〜1700℃の温度および20bar〜100barの圧力でアスファルト画分をガス化する工程を含む、請求項1に記載の方法。
- アスファルトを部分燃焼させる化学量論バランスをもたらすために、第三反応室で酸素および水蒸気の少なくとも1つ並びにアスファルトの量を調節する工程を更に含む、請求項1に記載の方法。
- 酸素:炭素比に基づく化学量論比は重量で0.2:1.0〜10:0.2である、請求項10に記載の方法。
- 原油中の炭素の重量に基づいて0.1:1.0〜10:0.1の比で第三反応室にアスファルトおよび水蒸気を導入する工程を含む、請求項10に記載の方法。
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201261655732P | 2012-06-05 | 2012-06-05 | |
US61/655,732 | 2012-06-05 | ||
PCT/US2013/043055 WO2013184462A1 (en) | 2012-06-05 | 2013-05-29 | Integrated process for deasphalting and desulfurizing whole crude oil |
Publications (2)
Publication Number | Publication Date |
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JP2015520271A JP2015520271A (ja) | 2015-07-16 |
JP5991562B2 true JP5991562B2 (ja) | 2016-09-14 |
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Application Number | Title | Priority Date | Filing Date |
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JP2015516064A Active JP5991562B2 (ja) | 2012-06-05 | 2013-05-29 | 原油全体を脱アスファルトおよび脱硫するための統合された方法 |
Country Status (7)
Country | Link |
---|---|
US (1) | US20130319910A1 (ja) |
EP (1) | EP2855639A1 (ja) |
JP (1) | JP5991562B2 (ja) |
KR (1) | KR101716986B1 (ja) |
CN (1) | CN104540926A (ja) |
SG (1) | SG11201408000XA (ja) |
WO (1) | WO2013184462A1 (ja) |
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KR102444109B1 (ko) * | 2013-12-24 | 2022-09-15 | 쉘 인터내셔날 리써취 마트샤피지 비.브이. | 중간 증류유의 제조 방법 |
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US9909068B2 (en) * | 2015-08-04 | 2018-03-06 | Saudi Arabian Oil Company | Integrated process for producing anode grade coke |
KR20180087437A (ko) | 2015-12-15 | 2018-08-01 | 사우디 아라비안 오일 컴퍼니 | 석유의 업그레이드를 위한 초임계 반응기 시스템 및 방법 |
US10066172B2 (en) | 2015-12-15 | 2018-09-04 | Saudi Arabian Oil Company | Supercritical water upgrading process to produce paraffinic stream from heavy oil |
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US10011790B2 (en) | 2015-12-15 | 2018-07-03 | Saudi Arabian Oil Company | Supercritical water processes for upgrading a petroleum-based composition while decreasing plugging |
US10233394B2 (en) | 2016-04-26 | 2019-03-19 | Saudi Arabian Oil Company | Integrated multi-stage solvent deasphalting and delayed coking process to produce high quality coke |
US10125318B2 (en) | 2016-04-26 | 2018-11-13 | Saudi Arabian Oil Company | Process for producing high quality coke in delayed coker utilizing mixed solvent deasphalting |
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US10815434B2 (en) | 2017-01-04 | 2020-10-27 | Saudi Arabian Oil Company | Systems and processes for power generation |
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US10604709B2 (en) | 2017-02-12 | 2020-03-31 | Magēmā Technology LLC | Multi-stage device and process for production of a low sulfur heavy marine fuel oil from distressed heavy fuel oil materials |
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US10941354B1 (en) | 2019-10-01 | 2021-03-09 | Saudi Arabian Oil Company | Hydrocracking catalyst comprising a beta zeolite (*BEA) framework substituted with Ti and Zr and methods for its preparation and use |
US11384298B2 (en) | 2020-04-04 | 2022-07-12 | Saudi Arabian Oil Company | Integrated process and system for treatment of hydrocarbon feedstocks using deasphalting solvent |
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- 2013-05-29 KR KR1020157000070A patent/KR101716986B1/ko active IP Right Grant
- 2013-05-29 SG SG11201408000XA patent/SG11201408000XA/en unknown
- 2013-05-29 US US13/904,545 patent/US20130319910A1/en not_active Abandoned
- 2013-05-29 JP JP2015516064A patent/JP5991562B2/ja active Active
- 2013-05-29 CN CN201380029767.0A patent/CN104540926A/zh active Pending
- 2013-05-29 EP EP13730395.4A patent/EP2855639A1/en not_active Ceased
- 2013-05-29 WO PCT/US2013/043055 patent/WO2013184462A1/en active Application Filing
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WO2013184462A1 (en) | 2013-12-12 |
US20130319910A1 (en) | 2013-12-05 |
JP2015520271A (ja) | 2015-07-16 |
KR20150021559A (ko) | 2015-03-02 |
SG11201408000XA (en) | 2015-01-29 |
KR101716986B1 (ko) | 2017-03-15 |
CN104540926A (zh) | 2015-04-22 |
EP2855639A1 (en) | 2015-04-08 |
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