GB1307542A - Thermal cracking process - Google Patents
Thermal cracking processInfo
- Publication number
- GB1307542A GB1307542A GB2462870A GB1307542DA GB1307542A GB 1307542 A GB1307542 A GB 1307542A GB 2462870 A GB2462870 A GB 2462870A GB 1307542D A GB1307542D A GB 1307542DA GB 1307542 A GB1307542 A GB 1307542A
- Authority
- GB
- United Kingdom
- Prior art keywords
- cracking
- ethane
- thermal cracking
- coke formation
- added
- Prior art date
- Legal status (The legal status 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 status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C4/00—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
- C07C4/02—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by cracking a single hydrocarbon or a mixture of individually defined hydrocarbons or a normally gaseous hydrocarbon fraction
- C07C4/04—Thermal processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0006—Controlling or regulating processes
- B01J19/002—Avoiding undesirable reactions or side-effects, e.g. avoiding explosions, or improving the yield by suppressing side-reactions
- B01J19/0026—Avoiding carbon deposits
-
- 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
- C10G9/14—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils in pipes or coils with or without auxiliary means, e.g. digesters, soaking drums, expansion means
- C10G9/16—Preventing or removing incrustation
-
- 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
- Y10S585/00—Chemistry of hydrocarbon compounds
- Y10S585/949—Miscellaneous considerations
- Y10S585/95—Prevention or removal of corrosion or solid deposits
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
1307542 Reducing coke formation in tubular cracking ESSO RESEARCH & ENG CO 21 May 1970 24628/70 Heading C5E In the production of unsaturated hydrocarbons, e.g. ethylene and butadiene, by thermal cracking of a hydrocarbon feed in the presence of steam in a tubular furnace, coke formation is reduced by providing a phosphorus compound and/or a bismuth compound in the vapour phase in the cracking zone. Suitable compounds are listed, and may be added continuously or intermittently or even as a pretreatment of the tubes since they have been found to exhibit a lasting effect. Coke reduction is obtained even with highsulphur feeds. In examples the feed is ethane or high-sulphur ethane, and the P or Bi is added in the form of H 3 PO 4 , trimethyl phosphate, PH 3 or Bi 2 O 3 .
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US72426468A | 1968-04-25 | 1968-04-25 | |
GB2462870 | 1970-05-21 | ||
NLAANVRAGE7008717,A NL164893C (en) | 1968-04-25 | 1970-06-15 | METHOD FOR THERMAL CRACKING OF A NORMAL LITER GASEOUS PETROLEUM FRACTION. |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1307542A true GB1307542A (en) | 1973-02-21 |
Family
ID=27258356
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2462870A Expired GB1307542A (en) | 1968-04-25 | 1970-05-21 | Thermal cracking process |
Country Status (3)
Country | Link |
---|---|
US (1) | US3531394A (en) |
GB (1) | GB1307542A (en) |
NL (1) | NL164893C (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0618281A1 (en) * | 1993-03-29 | 1994-10-05 | Betz Europe, Inc. | High temperature corrosion inhibitor |
WO1999014290A1 (en) * | 1997-09-17 | 1999-03-25 | Nalco/Exxon Energy Chemicals, L.P. | Method of inhibiting coke deposition in pyrolysis furnaces |
Families Citing this family (54)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4024051A (en) * | 1975-01-07 | 1977-05-17 | Nalco Chemical Company | Using an antifoulant in a crude oil heating process |
US4404087A (en) * | 1982-02-12 | 1983-09-13 | Phillips Petroleum Company | Antifoulants for thermal cracking processes |
US4444649A (en) * | 1982-11-15 | 1984-04-24 | Union Oil Company Of California | Antifoulant for high temperature hydrocarbon processing |
US4724064A (en) * | 1983-11-17 | 1988-02-09 | Betz Laboratories, Inc. | Composition and method for coke retardant during hydrocarbon processing |
US4551227A (en) * | 1984-04-16 | 1985-11-05 | Phillips Petroleum Company | Antifoulants for thermal cracking processes |
US4545893A (en) * | 1984-07-20 | 1985-10-08 | Phillips Petroleum Company | Antifoulants for thermal cracking processes |
US4613372A (en) * | 1985-01-22 | 1986-09-23 | Phillips Petroleum | Antifoulants for thermal cracking processes |
US4663018A (en) * | 1985-06-27 | 1987-05-05 | Betz Laboratories, Inc. | Method for coke retardant during hydrocarbon processing |
US4756820A (en) * | 1985-09-06 | 1988-07-12 | Betz Laboratories, Inc. | Method for retarding corrosion and coke formation and deposition during pyrolytic hydrocarbon processing |
US4687567A (en) * | 1986-04-09 | 1987-08-18 | Phillips Petroleum Company | Antifoulants for thermal cracking processes |
US4804487A (en) * | 1986-04-09 | 1989-02-14 | Phillips Petroleum Company | Antifoulants for thermal cracking processes |
US4692234A (en) * | 1986-04-09 | 1987-09-08 | Phillips Petroleum Company | Antifoulants for thermal cracking processes |
US4666583A (en) * | 1986-04-09 | 1987-05-19 | Phillips Petroleum Company | Antifoulants for thermal cracking processes |
US4752374A (en) * | 1987-04-20 | 1988-06-21 | Betz Laboratories, Inc. | Process for minimizing fouling of processing equipment |
US4835332A (en) * | 1988-08-31 | 1989-05-30 | Nalco Chemical Company | Use of triphenylphosphine as an ethylene furnace antifoulant |
US4900426A (en) * | 1989-04-03 | 1990-02-13 | Nalco Chemical Company | Triphenylphosphine oxide as an ethylene furnace antifoulant |
US5000836A (en) * | 1989-09-26 | 1991-03-19 | Betz Laboratories, Inc. | Method and composition for retarding coke formation during pyrolytic hydrocarbon processing |
US4962264A (en) * | 1989-10-23 | 1990-10-09 | Betz Laboratories, Inc. | Methods for retarding coke formation during pyrolytic hydrocarbon processing |
US5039391A (en) * | 1991-01-03 | 1991-08-13 | Betz Laboratories, Inc. | Use of boron containing compounds and dihydroxybenzenes to reduce coking in coker furnaces |
US5093032A (en) * | 1991-01-03 | 1992-03-03 | Betz Laboratories, Inc. | Use of boron containing compounds and dihydroxybenzenes to reduce coking in coker furnaces |
US5258113A (en) * | 1991-02-04 | 1993-11-02 | Mobil Oil Corporation | Process for reducing FCC transfer line coking |
SA05260056B1 (en) * | 1991-03-08 | 2008-03-26 | شيفرون فيليبس كيميكال كمبني ال بي | Hydrocarbon processing device |
US5221462A (en) * | 1991-03-27 | 1993-06-22 | Betz Laboratories, Inc. | Methods for retarding coke formation during pyrolytic hydrocarbon processing |
US5128023A (en) * | 1991-03-27 | 1992-07-07 | Betz Laboratories, Inc. | Method for inhibiting coke formation and deposiiton during pyrolytic hydrocarbon processing |
US5360531A (en) * | 1992-12-10 | 1994-11-01 | Nalco Chemical Company | Phosphoric triamide coking inhibitors |
US5413700A (en) * | 1993-01-04 | 1995-05-09 | Chevron Research And Technology Company | Treating oxidized steels in low-sulfur reforming processes |
US5405525A (en) * | 1993-01-04 | 1995-04-11 | Chevron Research And Technology Company | Treating and desulfiding sulfided steels in low-sulfur reforming processes |
SA94150056B1 (en) * | 1993-01-04 | 2005-10-15 | شيفرون ريسيرتش أند تكنولوجي كمبني | hydrodealkylation |
DE69417879T2 (en) * | 1993-01-04 | 1999-08-12 | Chevron Chem Co | DEHYDROGENATION METHOD AND DEVICE HERE |
USRE38532E1 (en) | 1993-01-04 | 2004-06-08 | Chevron Phillips Chemical Company Lp | Hydrodealkylation processes |
US5354450A (en) * | 1993-04-07 | 1994-10-11 | Nalco Chemical Company | Phosphorothioate coking inhibitors |
US6274113B1 (en) | 1994-01-04 | 2001-08-14 | Chevron Phillips Chemical Company Lp | Increasing production in hydrocarbon conversion processes |
US6258256B1 (en) | 1994-01-04 | 2001-07-10 | Chevron Phillips Chemical Company Lp | Cracking processes |
US5575902A (en) * | 1994-01-04 | 1996-11-19 | Chevron Chemical Company | Cracking processes |
US5779881A (en) * | 1994-02-03 | 1998-07-14 | Nalco/Exxon Energy Chemicals, L.P. | Phosphonate/thiophosphonate coking inhibitors |
DE4405883C1 (en) * | 1994-02-21 | 1995-08-10 | Gerhard Prof Dr Zimmermann | Process for the preparation of thermally cracked products and application of the process for reducing the coking of heat exchange surfaces |
US5552085A (en) * | 1994-08-31 | 1996-09-03 | Nalco Chemical Company | Phosphorus thioacid ester inhibitor for naphthenic acid corrosion |
US5853565A (en) * | 1996-04-01 | 1998-12-29 | Amoco Corporation | Controlling thermal coking |
US5863416A (en) * | 1996-10-18 | 1999-01-26 | Nalco/Exxon Energy Chemicals, L.P. | Method to vapor-phase deliver heater antifoulants |
US6419986B1 (en) | 1997-01-10 | 2002-07-16 | Chevron Phillips Chemical Company Ip | Method for removing reactive metal from a reactor system |
US5944981A (en) * | 1997-10-28 | 1999-08-31 | The M. W. Kellogg Company | Pyrolysis furnace tubes |
US6482311B1 (en) * | 2000-08-01 | 2002-11-19 | Tda Research, Inc. | Methods for suppression of filamentous coke formation |
US6706669B2 (en) * | 2001-07-13 | 2004-03-16 | Exxonmobil Research And Engineering Company | Method for inhibiting corrosion using phosphorous acid |
GB0130145D0 (en) * | 2001-12-17 | 2002-02-06 | Ici Plc | Metal passivation |
WO2005033253A1 (en) * | 2003-10-07 | 2005-04-14 | Swiss E-Technic Ag | Low-sulfur oil and method for lowering the aggressiveness thereof |
WO2006125177A2 (en) * | 2005-05-19 | 2006-11-23 | Massachusetts Institute Of Technology | Electrode and catalytic materials |
GB0521534D0 (en) * | 2005-10-24 | 2005-11-30 | Johnson Matthey Catalysts | Metal passivation |
JP5713669B2 (en) * | 2007-03-30 | 2015-05-07 | ドルフ ケタール ケミカルズ (インディア)プライヴェート リミテッド | Prevention of high temperature naphthenic acid corrosion using organophosphorus sulfur compounds and combinations thereof |
MY157688A (en) | 2007-04-04 | 2016-07-15 | Dorf Ketal Chemicals I Private Ltd | Naphthenic acid corrosion inhibition using new synergetic combination of phosphorus compounds |
ES2614763T3 (en) | 2007-09-14 | 2017-06-01 | Dorf Ketal Chemicals (I) Private Limited | Novel additive to inhibit corrosion by naphthenic acid and its use procedure |
CA2734384C (en) | 2008-08-26 | 2015-03-10 | Dorf Ketal Chemicals (I) Pvt. Ltd. | An effective novel polymeric additive for inhibiting napthenic acid corrosion and method of using the same |
BRPI0913173B1 (en) * | 2008-08-26 | 2017-12-05 | Dorf Ketal Chemicals I | "ADDITIVE FOR INHIBITION OF CORROSION CAUSED BY ACID AND METHOD OF PRODUCTION AND USE OF THE SAME" |
EP2419491B1 (en) | 2009-04-15 | 2019-10-09 | Dorf Ketal Chemicals (I) Private Limited | Method of using an effective non - polymeric and non - fouling additive for inhibiting high - temperature naphthenic acid corrosion |
US20110014372A1 (en) * | 2009-07-15 | 2011-01-20 | Webber Kenneth M | Passivation of thermal cracking furnace conduit |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1847095A (en) * | 1927-03-11 | 1932-03-01 | Ig Farbenindustrie Ag | Prevention of the formation of carbon in operations carried out with hydrocarbons at an elevated temperature |
DE1143600B (en) * | 1961-01-07 | 1963-02-14 | Basf Ag | Process for preventing the heating surfaces from becoming dirty when heating raw benzenes or other light oils rich in aromatic and / or olefin |
US3405054A (en) * | 1965-06-23 | 1968-10-08 | Standard Oil Co | Refinery process stream anti-foulant |
US3261774A (en) * | 1965-09-01 | 1966-07-19 | Nalco Chemical Co | Reducing fouling in refining of petroleum products |
-
1968
- 1968-04-25 US US724264A patent/US3531394A/en not_active Expired - Lifetime
-
1970
- 1970-05-21 GB GB2462870A patent/GB1307542A/en not_active Expired
- 1970-06-15 NL NLAANVRAGE7008717,A patent/NL164893C/en not_active IP Right Cessation
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0618281A1 (en) * | 1993-03-29 | 1994-10-05 | Betz Europe, Inc. | High temperature corrosion inhibitor |
WO1999014290A1 (en) * | 1997-09-17 | 1999-03-25 | Nalco/Exxon Energy Chemicals, L.P. | Method of inhibiting coke deposition in pyrolysis furnaces |
Also Published As
Publication number | Publication date |
---|---|
NL164893C (en) | 1984-12-17 |
US3531394A (en) | 1970-09-29 |
NL7008717A (en) | 1971-12-17 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed [section 19, patents act 1949] | ||
PE20 | Patent expired after termination of 20 years |