HRP20211585T1 - Postupak pretvaranja velikog opterećenja pomoću jedinice za katalitički kreking i koraka za selektivnog hidrogeniranja benzina iz katalitičkog krekiranja - Google Patents
Postupak pretvaranja velikog opterećenja pomoću jedinice za katalitički kreking i koraka za selektivnog hidrogeniranja benzina iz katalitičkog krekiranja Download PDFInfo
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- 238000000034 method Methods 0.000 title claims 14
- 238000004523 catalytic cracking Methods 0.000 title claims 7
- 238000005984 hydrogenation reaction Methods 0.000 title claims 4
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 claims 8
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 claims 8
- 239000003054 catalyst Substances 0.000 claims 7
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims 5
- 239000010457 zeolite Substances 0.000 claims 5
- 238000004519 manufacturing process Methods 0.000 claims 4
- 238000006384 oligomerization reaction Methods 0.000 claims 4
- 239000004215 Carbon black (E152) Substances 0.000 claims 3
- 229910021536 Zeolite Inorganic materials 0.000 claims 3
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims 3
- 229930195733 hydrocarbon Natural products 0.000 claims 3
- 150000002430 hydrocarbons Chemical class 0.000 claims 3
- 238000000746 purification Methods 0.000 claims 3
- 238000000926 separation method Methods 0.000 claims 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims 2
- HHUIAYDQMNHELC-UHFFFAOYSA-N [O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O Chemical class [O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O HHUIAYDQMNHELC-UHFFFAOYSA-N 0.000 claims 2
- 239000003463 adsorbent Substances 0.000 claims 2
- 238000009835 boiling Methods 0.000 claims 2
- 238000004821 distillation Methods 0.000 claims 2
- 239000007788 liquid Substances 0.000 claims 2
- 239000002808 molecular sieve Substances 0.000 claims 2
- 239000002994 raw material Substances 0.000 claims 2
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims 2
- 150000003464 sulfur compounds Chemical class 0.000 claims 2
- -1 ZSM-5 Inorganic materials 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 claims 1
- 150000001875 compounds Chemical class 0.000 claims 1
- 150000001993 dienes Chemical class 0.000 claims 1
- 229910001657 ferrierite group Inorganic materials 0.000 claims 1
- 229910021472 group 8 element Inorganic materials 0.000 claims 1
- 239000011159 matrix material Substances 0.000 claims 1
- 229910052751 metal Inorganic materials 0.000 claims 1
- 239000002184 metal Substances 0.000 claims 1
- 239000000203 mixture Substances 0.000 claims 1
- 229910052680 mordenite Inorganic materials 0.000 claims 1
- 229910052757 nitrogen Inorganic materials 0.000 claims 1
- 229910000510 noble metal Inorganic materials 0.000 claims 1
- 239000000377 silicon dioxide Substances 0.000 claims 1
- 238000001179 sorption measurement Methods 0.000 claims 1
- 239000000758 substrate Substances 0.000 claims 1
- 238000011144 upstream manufacturing Methods 0.000 claims 1
- 238000005406 washing Methods 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 1
Classifications
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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
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
- C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
-
- 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
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/02—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
- C10G11/04—Oxides
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
- C07C2/02—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons
- C07C2/04—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation
- C07C2/06—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation of alkenes, i.e. acyclic hydrocarbons having only one carbon-to-carbon double bond
- C07C2/08—Catalytic processes
- C07C2/12—Catalytic processes with crystalline alumino-silicates or with catalysts comprising molecular sieves
-
- 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
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/02—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
- C10G11/04—Oxides
- C10G11/05—Crystalline alumino-silicates, e.g. molecular sieves
-
- 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
- C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
-
- 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
- C10G45/32—Selective hydrogenation of the diolefin or acetylene 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
- 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
- C10G65/12—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including cracking steps and other hydrotreatment steps
-
- 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
- C10G69/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process
- C10G69/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only
-
- 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
- C10G69/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process
- C10G69/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only
- C10G69/12—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one polymerisation or alkylation step
- C10G69/126—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one polymerisation or alkylation step polymerisation, e.g. oligomerisation
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
Claims (3)
1. Postupak pretvaranja sirovine teškog ugljikovodika koji se sastoji od spojeva čija su vrelišta veća od 340°C, pri čemu navedeni postupak daje visoku fleksibilnost za proizvodnju propilena, benzina i srednjeg destilata, primjenjujući sljedeće korake kada proces radi u načinu rada maksimalnog propilena ili maksimalnog destilata:
a) korak katalitičkog krekiranja (FCC) teškog reza, koji proizvodi najmanje propilenski rez i benzinski rez u reaktoru s uzlaznom strujom s izlaznom temperaturom iz reaktora između 450°C i 650°C i omjerom C/O od između 2 i 20, ili u reaktoru sa silaznom strujom s izlaznom temperaturom iz reaktora između 480°C i 650°C i omjerom C/O od između 10 i 50, te u prisutnosti katalizatora koji sadrži aluminijev oksid, silicijev dioksid ili matricu silicijev dioksid-aluminijev oksid, pri čemu:
- kada postupak radi u režimu maksimalnog propilena, navedeni benzinski rez koji je proizveden u navedenom koraku katalitičkog krekiranja je C5-benzinski rez s konačnom točkom između 150°C i 220°C, pri čemu katalitičko krekiranje radi na izlaznoj temperaturi većoj od 600°C, a katalizator sadrži određeni udio zeolita ZSM5,
- kada proces radi u režimu maksimalnog destilata, navedeni benzinski rez koji je proizveden u navedenom koraku katalitičkog krekiranja je C5-150°C benzinski rez,
b) korak selektivnog hidrogeniranja (SHU) navedenog benzinskog reza koji je proizveden navedenim korakom katalitičkog krekiranja (FCC), koji radi pod sljedećim uvjetima: tlak između 0,5 i 5 MPa, temperatura između 80°C i 220°C, s prostornom brzinom tekućine po satu (LHSV) od između 1 h-1 i 10 h-1, prostorna brzina tekućine po satu je izražena u litrama punjenja po litri katalizatora na sat (l/l.h), te u prisutnosti katalizatora koji sadrži najmanje jedan metal iz skupine VIb i najmanje jedan neplemeniti metal iz skupine VIII, nanesen na poroznu podlogu, te pri čemu je težinski sadržaj oksida elementa skupine VIb između 4 i 20 težinskih%, a težinski sadržaj oksida elementa skupine VIII je manji od 15 težinskih%, korak selektivne hidrogenizacije (SHU) koji omogućuje hidrogeniranje diolefina prisutnih u navedenom benzinskom rezu i pretvorbu lakih spojeva sumpora iz navedenog benzinskog reza u spojeve sumpora više točke vrelišta,
c) korak destilacijskog odvajanja (SPLIT) benzina dobivenog iz koraka b), omogućavajući odvajanje dva reza: laganog benzinskog reza C5-Pf, i teškog benzinskog reza Pf-220°C, pri čemu temperatura Pf koja tvori granicu između lakog benzina i teškog benzina iznosi između 50°C i 80°C,
d) korak pročišćavanja (PUR) laganog benzinskog reza C5-Pf dobivenog iz koraka c), s ciljem smanjenja dušika na manje od 1 ppm po težini, poželjno manje od 0,2 ppm, kontaktom s adsorbentom odabranim iz aluminijevih oksida, silicijevog dioksida-aluminijevih oksida i molekularnih sita,
e) korak oligomerizacije (OLG) laganog benzinskog reza C5-Pf dobivenog iz koraka pročišćavanja (PUR), pri čemu su radni uvjeti navedenog koraka oligomerizacije (OLG) sljedeći:
kada proces radi u načinu rada s maksimalnim propilenom:
- temperatura između 120°C i 250°C,
- tlak između 3 i 6 MPa,
- katalizatori na bazi silicijevog dioksida-aluminijevog oksida;
kada proces radi u načinu rada s maksimalnim destilatom:
- temperatura između 150°C i 350°C,
- tlak između 3 i 6 MPa,
- katalizator na bazi kristalnog zeolita,
navedeni radni uvjeti koji omogućuju usmjeravanje proizvodnje na benzin ili srednji destilat,
f) korak odvajanja oligomera dobivenih na kraju koraka e), omogućuje oslobađanje najmanje dva reza:
- lagani benzinski rez PI-150°C,
- teški benzinski rez 150°C-220°C, i
- rez na 220°C+,
proces dalje radi prema sljedećim značajkama:
- kada proces radi u načinu rada s maksimalnim propilenom, lagani benzinski rez PI-150°C, teški benzinski rez 150°C-220°C i rez na 220°C+ koji su dobiveni iz koraka odvajanja oligomera recikliraju se u FCC,
- kada proces radi u načinu rada s maksimalnim destilatom, lagani benzinski rez PI-150°C se reciklira u FCC.
2. Postupak za pretvaranje sirovine teškog ugljikovodika, koji predstavlja visoku fleksibilnost za proizvodnju srednjeg destilata, benzina i propilena, prema patentnom zahtjevu 1, naznačen time što, kada postupak radi u načinu maksimalnog destiliranja, katalizator jedinice za oligomerizaciju se bira iz skupine koju čine zeoliti ferierit, ZSM-5, mordenit i ZSM-22, sami ili u smjesi, te je vrlo poželjno da se koristi zeolit ZSM-5.
3. Postupak za pretvaranje sirovine teškog ugljikovodika, koji predstavlja visoku fleksibilnost za proizvodnju srednjeg destilata, benzina i propilena, prema patentnom zahtjevu 1, naznačen time što jedinica za pročišćavanje (PUR) smještena uzvodno od jedinice za oligomerizaciju (OLG) koristi prethodno pranje vodom, nakon čega slijedi adsorpcija na adsorbentima kao što su aluminijevi oksidi, silicijev dioksid-aluminijevi oksidi ili molekularna sita, potonji se po mogućnosti temelje na NaX ili NaY zeolitima.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR1200424A FR2986799B1 (fr) | 2012-02-15 | 2012-02-15 | Procede de conversion d'une charge lourde, mettant en oeuvre une unite de craquage catalytique et une etape d'hydrogenation selective de l'essence issue du craquage catalytique |
| EP13290006.9A EP2636661B1 (fr) | 2012-02-15 | 2013-01-14 | Procédé de conversion d'une charge lourde, mettant en oeuvre une unité de craquage catalytique et une étape d'hydrogénation sélective de l'essence issue du craquage catalytique |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| HRP20211585T1 true HRP20211585T1 (hr) | 2022-01-21 |
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| Application Number | Title | Priority Date | Filing Date |
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| HRP20211585TT HRP20211585T1 (hr) | 2012-02-15 | 2013-01-14 | Postupak pretvaranja velikog opterećenja pomoću jedinice za katalitički kreking i koraka za selektivnog hidrogeniranja benzina iz katalitičkog krekiranja |
Country Status (10)
| Country | Link |
|---|---|
| US (1) | US9249364B2 (hr) |
| EP (1) | EP2636661B1 (hr) |
| JP (1) | JP6111084B2 (hr) |
| FR (1) | FR2986799B1 (hr) |
| HR (1) | HRP20211585T1 (hr) |
| MY (1) | MY163508A (hr) |
| PH (1) | PH12013000053A1 (hr) |
| PL (1) | PL2636661T3 (hr) |
| RU (1) | RU2617688C2 (hr) |
| TW (1) | TWI482849B (hr) |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| US9982204B2 (en) * | 2013-06-13 | 2018-05-29 | Uop Llc | Process for producing a chemical feedstock and apparatus relating thereto |
| CN104549431B (zh) * | 2013-10-23 | 2018-06-19 | 中国石油化工股份有限公司 | 一种含酸改性分子筛加氢裂化催化剂的制备方法 |
| US9914884B2 (en) | 2013-12-17 | 2018-03-13 | Uop Llc | Process and apparatus for recovering oligomerate |
| US9387413B2 (en) | 2013-12-17 | 2016-07-12 | Uop Llc | Process and apparatus for recovering oligomerate |
| JP6234829B2 (ja) * | 2014-01-24 | 2017-11-22 | Ｊｘｔｇエネルギー株式会社 | 重質油の流動接触分解法 |
| JP7311831B2 (ja) | 2014-12-09 | 2023-07-20 | 秋吉 神村 | 情報表示ラベル |
| US11566182B2 (en) | 2020-03-30 | 2023-01-31 | Chevron U.S.A. Inc. | Circular economy for plastic waste to polyethylene via refinery FCC feed pretreater and FCC units |
| CN115477957A (zh) * | 2021-05-31 | 2022-12-16 | 北京化工大学 | 汽油中烯烃含量的降低方法 |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| FR1004585A (fr) | 1948-05-18 | 1952-03-31 | Coiffure et vêtement imperméables pour mauvais temps | |
| US2945906A (en) * | 1955-10-15 | 1960-07-19 | Basf Ag | Cracking of oligomers of isobutene in the presence of silica-magnesia catalysts |
| DE3914817C2 (de) * | 1989-05-05 | 1995-09-07 | Huels Chemische Werke Ag | Verfahren zur Oligomerisierung von Olefinen |
| US4973790A (en) * | 1989-11-16 | 1990-11-27 | Mobil Oil Corporation | Process for upgrading light olefinic streams |
| DE69012295T2 (de) * | 1989-11-16 | 1995-01-05 | Mobil Oil Corp | Verfahren zur Qualitätserhöhung von Leichtolefinströmen. |
| US5202015A (en) * | 1991-01-22 | 1993-04-13 | Mobil Oil Corporation | Process for distillate dewaxing coincident with light olefin oligomerization |
| CA2182994A1 (en) * | 1994-02-22 | 1995-08-24 | Exxonmobil Chemical Patents, Inc. | Oligomerization and catalysts therefor |
| US6803494B1 (en) * | 1998-05-05 | 2004-10-12 | Exxonmobil Chemical Patents Inc. | Process for selectively producing propylene in a fluid catalytic cracking process |
| US6024865A (en) * | 1998-09-09 | 2000-02-15 | Bp Amoco Corporation | Sulfur removal process |
| FR2797639B1 (fr) | 1999-08-19 | 2001-09-21 | Inst Francais Du Petrole | Procede de production d'essences a faible teneur en soufre |
| FR2837213B1 (fr) * | 2002-03-15 | 2004-08-20 | Inst Francais Du Petrole | Procede de production conjointe de propylene et d'essence a partir d'une charge relativement lourde |
| FR2879620B1 (fr) * | 2004-12-21 | 2007-02-23 | Inst Francais Du Petrole | Procede de conversion directe d'une charge comprenant des olefines a quatre et/ou cinq atomes de carbone, pour la production de propylene avec une co-production d'essence |
| FR2895416B1 (fr) | 2005-12-22 | 2011-08-26 | Inst Francais Du Petrole | Procede d'hydrogenation selective mettant en oeuvre un catalyseur sulfure |
| FR2935377B1 (fr) | 2008-08-29 | 2013-02-15 | Inst Francais Du Petrole | Procede de conversion d'une charge lourde en essence et en propylene presentant une structure de rendement modulable |
| FR2935389B1 (fr) | 2008-09-04 | 2012-05-11 | Inst Francais Du Petrole | Procede d'hydrogenation selective mettant en oeuvre un catalyseur sulfure de composition specifique |
| FR2959748B1 (fr) * | 2010-05-06 | 2012-05-18 | Inst Francais Du Petrole | Procede de craquage catalytique avec recycle d'une coupe olefinique prelevee en amont de la section de separation des gaz afin de maximiser la production de propylene. |
| FR2964389A1 (fr) * | 2010-09-07 | 2012-03-09 | IFP Energies Nouvelles | Procede de production de carburants kerosene et diesel a partir de coupes insaturees legeres et de coupes aromatiques riches en btx |
| FR2968010B1 (fr) * | 2010-11-25 | 2014-03-14 | Ifp Energies Now | Procede de conversion d'une charge lourde en distillat moyen |
-
2012
- 2012-02-15 FR FR1200424A patent/FR2986799B1/fr active Active
-
2013
- 2013-01-14 EP EP13290006.9A patent/EP2636661B1/fr active Active
- 2013-01-14 HR HRP20211585TT patent/HRP20211585T1/hr unknown
- 2013-01-14 PL PL13290006T patent/PL2636661T3/pl unknown
- 2013-02-04 TW TW102104249A patent/TWI482849B/zh active
- 2013-02-11 PH PH12013000053A patent/PH12013000053A1/en unknown
- 2013-02-13 JP JP2013025051A patent/JP6111084B2/ja active Active
- 2013-02-14 US US13/767,072 patent/US9249364B2/en active Active
- 2013-02-14 MY MYPI2013000463A patent/MY163508A/en unknown
- 2013-02-14 RU RU2013106524A patent/RU2617688C2/ru active
Also Published As
| Publication number | Publication date |
|---|---|
| PH12013000053B1 (en) | 2014-08-27 |
| JP2013166935A (ja) | 2013-08-29 |
| MY163508A (en) | 2017-09-15 |
| EP2636661A1 (fr) | 2013-09-11 |
| TW201335354A (zh) | 2013-09-01 |
| RU2013106524A (ru) | 2014-08-20 |
| PL2636661T3 (pl) | 2021-12-20 |
| US9249364B2 (en) | 2016-02-02 |
| PH12013000053A1 (en) | 2014-08-27 |
| JP6111084B2 (ja) | 2017-04-05 |
| EP2636661B1 (fr) | 2021-07-14 |
| FR2986799B1 (fr) | 2015-02-06 |
| RU2617688C2 (ru) | 2017-04-26 |
| TWI482849B (zh) | 2015-05-01 |
| FR2986799A1 (fr) | 2013-08-16 |
| US20130211161A1 (en) | 2013-08-15 |
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