PL134116B1 - Method of decarbonizing and demetalizing hydrocarbons - Google Patents
Method of decarbonizing and demetalizing hydrocarbons Download PDFInfo
- Publication number
- PL134116B1 PL134116B1 PL1981230887A PL23088781A PL134116B1 PL 134116 B1 PL134116 B1 PL 134116B1 PL 1981230887 A PL1981230887 A PL 1981230887A PL 23088781 A PL23088781 A PL 23088781A PL 134116 B1 PL134116 B1 PL 134116B1
- Authority
- PL
- Poland
- Prior art keywords
- temperature
- contact material
- hydrocarbon
- charge
- column
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims 15
- 229930195733 hydrocarbon Natural products 0.000 title claims 12
- 150000002430 hydrocarbons Chemical class 0.000 title claims 12
- 239000000463 material Substances 0.000 claims 14
- 239000004215 Carbon black (E152) Substances 0.000 claims 10
- 239000007787 solid Substances 0.000 claims 10
- 238000002485 combustion reaction Methods 0.000 claims 6
- 230000000630 rising effect Effects 0.000 claims 4
- 239000000446 fuel Substances 0.000 claims 2
- 238000004227 thermal cracking Methods 0.000 claims 2
- 239000005995 Aluminium silicate Substances 0.000 claims 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims 1
- 235000012211 aluminium silicate Nutrition 0.000 claims 1
- 229910052799 carbon Inorganic materials 0.000 claims 1
- 238000004523 catalytic cracking Methods 0.000 claims 1
- 239000004927 clay Substances 0.000 claims 1
- 239000010779 crude oil Substances 0.000 claims 1
- 238000001704 evaporation Methods 0.000 claims 1
- 230000008020 evaporation Effects 0.000 claims 1
- 239000007789 gas Substances 0.000 claims 1
- 229910052739 hydrogen Inorganic materials 0.000 claims 1
- 239000001257 hydrogen Substances 0.000 claims 1
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 claims 1
- 230000001590 oxidative effect Effects 0.000 claims 1
- 239000011148 porous material Substances 0.000 claims 1
- 238000000926 separation method Methods 0.000 claims 1
- 239000010802 sludge Substances 0.000 claims 1
- 239000011343 solid material Substances 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 1
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
- C10G25/00—Refining of hydrocarbon oils in the absence of hydrogen, with solid sorbents
- C10G25/06—Refining of hydrocarbon oils in the absence of hydrogen, with solid sorbents with moving sorbents or sorbents dispersed in the oil
- C10G25/09—Refining of hydrocarbon oils in the absence of hydrogen, with solid sorbents with moving sorbents or sorbents dispersed in the oil 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
- C10G51/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only
- C10G51/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only
- C10G51/04—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only including only thermal and catalytic cracking 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
- C10G55/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process
- C10G55/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process plural serial stages only
- C10G55/06—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process plural serial stages only including at least one catalytic cracking step
-
- 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
- C10G9/00—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G9/28—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid material
- C10G9/32—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid material according to the "fluidised-bed" technique
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S208/00—Mineral oils: processes and products
- Y10S208/01—Automatic control
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)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Dispersion Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Claims (11)
1.Zastrzezenia patentowe 1. Sposób odweglania 1 demetalizacji wsadu weglowodorowego z ropy pelnozakresowej lub frakcji pozostalosci, przez kontaktowanie tego wsadu, w pionowej kolumnie wznosnej , z mialko rozdrobnionym stalym materialem kontaktowym stanowiacym zasadniczo obojetny ma¬ terial staly,o mikroaktywnosciprzy krakingu katalitycznym zasadniczo nie wiekszej niz 20 w stosunkowo lagodnych warunkach obejmujecych temperature co najmniej okolo 480°C, przez okre6 czasu ponizej 3 sekundy i mniej niz potrzeba dla wzbudzenia w tym wsadzie krakingu termicznego, oddzielenie pod koniec tego okresu selektywnie odparowanej wiek¬ szej czesci tego wsadu od materialu kontaktowego z osadzone na nim nieodparowane czescie wsadu, kontaktowanie tego materialu kontaktowego z osadzonym na nim osadem, w strefie spa¬ lania, z gazem utleniajecym i spalenie tego osadu z wytworzeniem ciepla dla podniesienia temperatury materialu kontaktowego, zawracanie tak ogrzanego materialu kontaktowego do ponownego kontaktu ze wsadem weglowodorowym, znamienny tym, ze mierzy sie temperature w kolumnie, reguluje sie szybkosc zawracania tak ogrzanego materialu kontak¬ towego w zaleznosci od zmierzonej temperatury dla utrzymania w kolumnie temperatury na us¬ talonym z góry poziomie i reguluje sie dynamicznie uklad w celu wykorzystania malowartos- ciowej czesci wsadu o niskiej zawartosci wodoru jako paliwa na potrzeby procesu, przy czym regulacja dynamiczna obejmuje nastawienie ustalonej z góry wartosci temperatury mierzonej w kolumnie w przyblizeniu na minimalnym poziomie, przy którym osadzony osad za¬ pewnia odpowiednie ilosc paliwa, które po spaleniu utrzyma strefe spalania na ustalonej z góry wartosci temperatury, z tym, ze wyzej wymienione nastawienie przeprowadza sie przez obnizenie tej temperatury w kolumnie wznosnej przy dazeniu ukladu do obnizania temperatury w strefie spalania lub przez zwiekszenie ustalonej z góry temperatury w kolumnie wznosnej przy dezenlu ukladu do podwyzszenia temperatury w strefie spalania.
2. Sposób wedlug zastrz. 1, znamienny tym, ze prowadzec regulacje dyny- miczne procesu mierzy sie temperature w strefie spalania i ponownie ustala i nastawia temperature w kolumnie wznosnej na poziomie wymaganym do osiagniecia wartosci minimalnej*
3. Sposób wedlug zastrz. 1. znamienny tym, ze glówne czesc wsadu weglowo¬ dorowego odparowuje sie w ilosci mniejszej od ilosci calego wsadu weglowodorowego, w % wa¬ gowych, o nie wiecej niz dwukrotny wskaznik zawartosci wegla wedlug Conradsona tego wsadu weglowodorowego•
4. Sposób wedlug zastrz. ly znamienny tym, ze obojetny staly material kon¬ taktowy wprowadza sie do strefy selektywnego odparowania w temperaturze zasadniczo wyzszej od temperatury wsadu weglowodorowego.
5. Sposób wedlug zastrz. 1» znamienny tym, ze jako obojetny staly material kontaktowy stosuje sie gline wypalone.
6. Sposób wedlug zastrz. 1, znarolennytym, ze ustala sie czas przebywania wsadu weglowodorowego w kolumnie na mniej niz 0,5 s.
7. Sposób wedlug zastrz. 1, znamienny tym, ze jako obojetny staly material 2 kontaktowy stosuje sie porowate cialo stale o malej powierzychni wlasciwej, nizszej niz 100 m /g •
8. Sposób wedlug zastrz. 1, znamienny tym, ze jako obojetny staly material kontaktowy stosuje sie porowate cialo stale o malej powierzchni wlasciwej w zakresie oko¬ lo 10-15 ra2/g
9. Sposób wedlug zastrz. 1, znamienny tym. ze jako obojetny staly material kontaktowy stosuje sie wypalony kaolin.
10. Sposób wedlug zastrz. 1, znamienny tym, ze jako obojetny staly material kontaktowy stosuje sie porowate cialo stale w którym wiekszosc porów ma srednice 1,5-6 mikro¬ metrów.
11. Sposób wedlug zastrz. 1,znamienny tym, ze do wsadu weglowodorowego do¬ daje sie weglowodory, pare wodne lub wode przy kontaktowaniu go z obojetnym materialem kon¬ taktowym w ilosci zasadniczo obnizajecej cisnienie czestkowe weglowodoru.16 134 11612. * Sposób wedlug zastrz. 1, znamienny tym, ze selektywnie odparowane glówne czesc wsadu weglowodorowego po oddzieleniu od materialu kontaktowego szybko chlo¬ dzi sie do temperatury nizszej od temperatury, przy której nastepuje kraking termiczny. inr^fr^ Pracownia Poligraficzna UP PRL. Naklad 100 egz. Cena 100 zl PL PL PL
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US06/144,477 US4311580A (en) | 1979-11-01 | 1980-04-28 | Selective vaporization process and dynamic control thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| PL230887A1 PL230887A1 (pl) | 1982-02-15 |
| PL134116B1 true PL134116B1 (en) | 1985-07-31 |
Family
ID=22508767
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PL1981230887A PL134116B1 (en) | 1980-04-28 | 1981-04-28 | Method of decarbonizing and demetalizing hydrocarbons |
Country Status (26)
| Country | Link |
|---|---|
| US (1) | US4311580A (pl) |
| JP (1) | JPS56167787A (pl) |
| AT (1) | AT379609B (pl) |
| AU (1) | AU545668B2 (pl) |
| BR (1) | BR8102552A (pl) |
| CA (1) | CA1169010A (pl) |
| CH (1) | CH650014A5 (pl) |
| DD (1) | DD158645A5 (pl) |
| DE (1) | DE3116598A1 (pl) |
| EG (1) | EG15374A (pl) |
| ES (1) | ES502300A0 (pl) |
| FR (1) | FR2481311B1 (pl) |
| GB (1) | GB2075048B (pl) |
| GR (1) | GR74886B (pl) |
| HU (1) | HU189505B (pl) |
| IT (1) | IT1139087B (pl) |
| LU (1) | LU83319A1 (pl) |
| MX (1) | MX157605A (pl) |
| NL (1) | NL8102095A (pl) |
| NO (1) | NO161325C (pl) |
| OA (1) | OA06800A (pl) |
| PL (1) | PL134116B1 (pl) |
| PT (1) | PT72931B (pl) |
| RO (1) | RO82099B (pl) |
| ZA (1) | ZA812797B (pl) |
| ZW (1) | ZW10081A1 (pl) |
Families Citing this family (46)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0063683B1 (en) * | 1981-03-30 | 1986-09-10 | Ashland Oil, Inc. | Immobilisation of vanadium deposited on sorbent materials during the treatment of oils containing heavy metals and coke precursors |
| EP0065626B1 (en) * | 1981-04-20 | 1986-07-23 | Ashland Oil, Inc. | Immobilization of vanadium deposited on sorbent materials during the treatment of oils containing heavy metals and coke precursors |
| US4405445A (en) * | 1981-08-24 | 1983-09-20 | Ashland Oil, Inc. | Homogenization of water and reduced crude for catalytic cracking |
| GB2117394B (en) * | 1982-03-22 | 1986-05-21 | Engelhard Corp | Decarbonizing and demetallizing petroleum stocks |
| DE3211570A1 (de) * | 1982-03-29 | 1983-10-06 | Engelhard Corp | Verfahren und anordnung zum selektiven verdampfen einer schweren rohoelfraktion |
| US5073251A (en) * | 1982-10-19 | 1991-12-17 | Daniels Ludlow S | Method of an apparatus for recovering oil from solid hydrocarbonaceous material |
| US4585544A (en) * | 1984-03-09 | 1986-04-29 | Stone & Webster Engineering Corporation | Hydrocarbon pretreatment process for catalytic cracking |
| US4569754A (en) * | 1984-12-14 | 1986-02-11 | Engelhard Corporation | Selective vaporization process |
| US4781818A (en) * | 1984-12-18 | 1988-11-01 | Engelhard Corporation | Non catalytic solid mullite/crystalline silica material and use thereof |
| US4784748A (en) * | 1987-10-28 | 1988-11-15 | Mobil Oil Corporation | FCC unit combined with a circulating fluid bed combustor |
| US4980045A (en) * | 1988-08-02 | 1990-12-25 | Chevron Research Company | Heavy oil pretreatment process with reduced sulfur oxide emissions |
| US5269980A (en) * | 1991-08-05 | 1993-12-14 | Northeastern University | Production of polymer particles in powder form using an atomization technique |
| BR9805727A (pt) * | 1998-12-29 | 2000-07-04 | Petroleo Brasileiro Sa | Processo de craqueamento catalìtico fluido com carga de alimentação pré-vaporizada |
| US8105482B1 (en) | 1999-04-07 | 2012-01-31 | Ivanhoe Energy, Inc. | Rapid thermal processing of heavy hydrocarbon feedstocks |
| WO2000061705A1 (en) | 1999-04-07 | 2000-10-19 | Ensyn Group Inc. | Rapid thermal processing of heavy hydrocarbon feedstocks |
| DK1332199T3 (da) | 2000-09-18 | 2012-02-06 | Ivanhoe Htl Petroleum Ltd | Produkter fremstillet ved hurtig termisk behandling af tunge carbonhydridråmaterialer |
| US8062503B2 (en) | 2001-09-18 | 2011-11-22 | Ivanhoe Energy Inc. | Products produced from rapid thermal processing of heavy hydrocarbon feedstocks |
| US7097758B2 (en) * | 2002-07-03 | 2006-08-29 | Exxonmobil Chemical Patents Inc. | Converting mist flow to annular flow in thermal cracking application |
| US7138047B2 (en) * | 2002-07-03 | 2006-11-21 | Exxonmobil Chemical Patents Inc. | Process for steam cracking heavy hydrocarbon feedstocks |
| CA2489876C (en) * | 2002-07-03 | 2011-04-19 | Exxonmobil Chemical Patents Inc. | Converting mist flow to annular flow in thermal cracking application |
| US7090765B2 (en) * | 2002-07-03 | 2006-08-15 | Exxonmobil Chemical Patents Inc. | Process for cracking hydrocarbon feed with water substitution |
| US7572365B2 (en) * | 2002-10-11 | 2009-08-11 | Ivanhoe Energy, Inc. | Modified thermal processing of heavy hydrocarbon feedstocks |
| US7572362B2 (en) * | 2002-10-11 | 2009-08-11 | Ivanhoe Energy, Inc. | Modified thermal processing of heavy hydrocarbon feedstocks |
| WO2005095548A1 (en) * | 2004-03-22 | 2005-10-13 | Exxonmobil Chemical Patents Inc. | Process for steam cracking heavy hydrocarbon feedstocks |
| US7220887B2 (en) * | 2004-05-21 | 2007-05-22 | Exxonmobil Chemical Patents Inc. | Process and apparatus for cracking hydrocarbon feedstock containing resid |
| US7481871B2 (en) * | 2004-12-10 | 2009-01-27 | Exxonmobil Chemical Patents Inc. | Vapor/liquid separation apparatus |
| US7408093B2 (en) * | 2004-07-14 | 2008-08-05 | Exxonmobil Chemical Patents Inc. | Process for reducing fouling from flash/separation apparatus during cracking of hydrocarbon feedstocks |
| US7193123B2 (en) * | 2004-05-21 | 2007-03-20 | Exxonmobil Chemical Patents Inc. | Process and apparatus for cracking hydrocarbon feedstock containing resid to improve vapor yield from vapor/liquid separation |
| US7351872B2 (en) * | 2004-05-21 | 2008-04-01 | Exxonmobil Chemical Patents Inc. | Process and draft control system for use in cracking a heavy hydrocarbon feedstock in a pyrolysis furnace |
| US7312371B2 (en) * | 2004-05-21 | 2007-12-25 | Exxonmobil Chemical Patents Inc. | Steam cracking of hydrocarbon feedstocks containing non-volatile components and/or coke precursors |
| US7235705B2 (en) * | 2004-05-21 | 2007-06-26 | Exxonmobil Chemical Patents Inc. | Process for reducing vapor condensation in flash/separation apparatus overhead during steam cracking of hydrocarbon feedstocks |
| US7488459B2 (en) * | 2004-05-21 | 2009-02-10 | Exxonmobil Chemical Patents Inc. | Apparatus and process for controlling temperature of heated feed directed to a flash drum whose overhead provides feed for cracking |
| US7311746B2 (en) * | 2004-05-21 | 2007-12-25 | Exxonmobil Chemical Patents Inc. | Vapor/liquid separation apparatus for use in cracking hydrocarbon feedstock containing resid |
| US7247765B2 (en) * | 2004-05-21 | 2007-07-24 | Exxonmobil Chemical Patents Inc. | Cracking hydrocarbon feedstock containing resid utilizing partial condensation of vapor phase from vapor/liquid separation to mitigate fouling in a flash/separation vessel |
| US7244871B2 (en) * | 2004-05-21 | 2007-07-17 | Exxonmobil Chemical Patents, Inc. | Process and apparatus for removing coke formed during steam cracking of hydrocarbon feedstocks containing resids |
| US7358413B2 (en) * | 2004-07-14 | 2008-04-15 | Exxonmobil Chemical Patents Inc. | Process for reducing fouling from flash/separation apparatus during cracking of hydrocarbon feedstocks |
| US7297833B2 (en) * | 2004-05-21 | 2007-11-20 | Exxonmobil Chemical Patents Inc. | Steam cracking of light hydrocarbon feedstocks containing non-volatile components and/or coke precursors |
| US7285697B2 (en) * | 2004-07-16 | 2007-10-23 | Exxonmobil Chemical Patents Inc. | Reduction of total sulfur in crude and condensate cracking |
| US7402237B2 (en) * | 2004-10-28 | 2008-07-22 | Exxonmobil Chemical Patents Inc. | Steam cracking of hydrocarbon feedstocks containing salt and/or particulate matter |
| US8173854B2 (en) * | 2005-06-30 | 2012-05-08 | Exxonmobil Chemical Patents Inc. | Steam cracking of partially desalted hydrocarbon feedstocks |
| JP6262749B2 (ja) * | 2012-10-19 | 2018-01-17 | サウジ アラビアン オイル カンパニー | 原油の高過酷度接触分解方法 |
| US9707532B1 (en) | 2013-03-04 | 2017-07-18 | Ivanhoe Htl Petroleum Ltd. | HTL reactor geometry |
| IN2013MU03604A (pl) | 2013-11-18 | 2015-07-31 | Indian Oil Corp Ltd | |
| CN109311794B (zh) * | 2016-06-16 | 2022-05-13 | 托普索公司 | 糖的热解碎裂 |
| WO2024209116A1 (es) * | 2023-04-05 | 2024-10-10 | Saudi Arabian Oil Company | Métodos y sistemas de conversión de petróleo crudo en productos petroquímicos |
| WO2024209117A1 (es) * | 2023-04-05 | 2024-10-10 | Saudi Arabian Oil Company | Métodos y sistemas de conversión de petróleo crudo en productos petroquímicos |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2608526A (en) * | 1946-12-14 | 1952-08-26 | Standard Oil Dev Co | Coking of carbonaceous fuels |
| US2874092A (en) * | 1955-05-26 | 1959-02-17 | Gulf Research Development Co | High-temperature, low-contact time coking process |
| US3074878A (en) * | 1957-10-18 | 1963-01-22 | Exxon Research Engineering Co | Short contact time system |
| US3324030A (en) * | 1964-11-10 | 1967-06-06 | Mobil Oil Corp | Tcc control by reactor effluent temperature |
| FR1446809A (fr) * | 1965-09-13 | 1966-07-22 | Universal Oil Prod Co | Procédé continu pour la préparation d'hydrocarbures de l'essence |
| US3513087A (en) * | 1968-08-30 | 1970-05-19 | Continental Oil Co | Control system for fluid cat cracker |
| FR2075950A2 (en) * | 1969-01-30 | 1971-10-15 | Continental Oil Co | Continuous hydrocarbon cracking |
| US3629097A (en) * | 1970-01-06 | 1971-12-21 | Continental Oil Co | Control system for fluid catalytic cracking process |
| ZA764947B (en) * | 1975-08-27 | 1978-03-29 | Mobil Oil Corp | Fcc catalyst section control |
| US4263128A (en) * | 1978-02-06 | 1981-04-21 | Engelhard Minerals & Chemicals Corporation | Upgrading petroleum and residual fractions thereof |
| CA1127581A (en) * | 1978-02-06 | 1982-07-13 | David B. Bartholic | Preparation of fcc charge from residual fractions |
-
1980
- 1980-04-28 US US06/144,477 patent/US4311580A/en not_active Expired - Lifetime
-
1981
- 1981-04-22 GR GR64789A patent/GR74886B/el unknown
- 1981-04-25 EG EG81233A patent/EG15374A/xx active
- 1981-04-27 BR BR8102552A patent/BR8102552A/pt not_active IP Right Cessation
- 1981-04-27 PT PT72931A patent/PT72931B/pt unknown
- 1981-04-27 CH CH2736/81A patent/CH650014A5/de not_active IP Right Cessation
- 1981-04-27 DE DE19813116598 patent/DE3116598A1/de not_active Withdrawn
- 1981-04-27 NO NO811411A patent/NO161325C/no unknown
- 1981-04-27 AU AU69885/81A patent/AU545668B2/en not_active Ceased
- 1981-04-27 HU HU811090A patent/HU189505B/hu not_active IP Right Cessation
- 1981-04-27 AT AT0188881A patent/AT379609B/de not_active IP Right Cessation
- 1981-04-27 LU LU83319A patent/LU83319A1/fr unknown
- 1981-04-28 MX MX187039A patent/MX157605A/es unknown
- 1981-04-28 IT IT21424/81A patent/IT1139087B/it active
- 1981-04-28 ES ES502300A patent/ES502300A0/es active Granted
- 1981-04-28 NL NL8102095A patent/NL8102095A/nl not_active Application Discontinuation
- 1981-04-28 RO RO104137A patent/RO82099B/ro unknown
- 1981-04-28 PL PL1981230887A patent/PL134116B1/pl unknown
- 1981-04-28 ZW ZW100/81A patent/ZW10081A1/xx unknown
- 1981-04-28 ZA ZA00812797A patent/ZA812797B/xx unknown
- 1981-04-28 GB GB8113041A patent/GB2075048B/en not_active Expired
- 1981-04-28 DD DDAPC10G/2295600A patent/DD158645A5/de not_active IP Right Cessation
- 1981-04-28 FR FR8108463A patent/FR2481311B1/fr not_active Expired
- 1981-04-28 CA CA000376433A patent/CA1169010A/en not_active Expired
- 1981-04-28 OA OA57391A patent/OA06800A/xx unknown
- 1981-04-28 JP JP6350381A patent/JPS56167787A/ja active Pending
Also Published As
| Publication number | Publication date |
|---|---|
| DE3116598A1 (de) | 1982-03-25 |
| ES8203412A1 (es) | 1982-04-01 |
| IT1139087B (it) | 1986-09-17 |
| GB2075048B (en) | 1985-01-09 |
| AU545668B2 (en) | 1985-07-25 |
| JPS56167787A (en) | 1981-12-23 |
| LU83319A1 (fr) | 1981-12-01 |
| RO82099A (ro) | 1985-03-15 |
| MX157605A (es) | 1988-12-05 |
| BR8102552A (pt) | 1982-01-05 |
| NO161325B (no) | 1989-04-24 |
| CH650014A5 (de) | 1985-06-28 |
| PL230887A1 (pl) | 1982-02-15 |
| NO161325C (no) | 1989-08-02 |
| FR2481311A1 (fr) | 1981-10-30 |
| PT72931B (en) | 1982-04-12 |
| EG15374A (en) | 1986-06-30 |
| ZW10081A1 (en) | 1981-07-22 |
| NL8102095A (nl) | 1981-11-16 |
| FR2481311B1 (fr) | 1986-07-18 |
| AU6988581A (en) | 1981-11-05 |
| IT8121424A0 (it) | 1981-04-28 |
| ATA188881A (de) | 1985-06-15 |
| AT379609B (de) | 1986-02-10 |
| ES502300A0 (es) | 1982-04-01 |
| HU189505B (en) | 1986-07-28 |
| OA06800A (fr) | 1982-12-31 |
| US4311580A (en) | 1982-01-19 |
| GR74886B (pl) | 1984-07-12 |
| RO82099B (ro) | 1985-03-30 |
| CA1169010A (en) | 1984-06-12 |
| NO811411L (no) | 1981-10-29 |
| DD158645A5 (de) | 1983-01-26 |
| ZA812797B (en) | 1982-04-28 |
| GB2075048A (en) | 1981-11-11 |
| PT72931A (en) | 1981-05-01 |
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