GB1117562A

GB1117562A – Thermal cracking process
– Google Patents

GB1117562A – Thermal cracking process
– Google Patents
Thermal cracking process

Info

Publication number
GB1117562A

GB1117562A
GB38710/66A
GB3871066A
GB1117562A
GB 1117562 A
GB1117562 A
GB 1117562A
GB 38710/66 A
GB38710/66 A
GB 38710/66A
GB 3871066 A
GB3871066 A
GB 3871066A
GB 1117562 A
GB1117562 A
GB 1117562A
Authority
GB
United Kingdom
Prior art keywords
tubes
tube
steam
temperature
onstream
Prior art date
1966-04-29
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

Application number
GB38710/66A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)

ExxonMobil Technology and Engineering Co

Original Assignee
Exxon Research and Engineering Co
Esso Research and Engineering Co
Priority date (The priority date 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 date listed.)
1966-04-29
Filing date
1966-08-30
Publication date
1968-06-19

1966-08-30
Application filed by Exxon Research and Engineering Co, Esso Research and Engineering Co
filed
Critical
Exxon Research and Engineering Co

1968-06-19
Publication of GB1117562A
publication
Critical
patent/GB1117562A/en

Status
Expired
legal-status
Critical
Current

Links

Espacenet

Global Dossier

Discuss

238000000034
method
Methods

0.000
title
abstract
2

238000004227
thermal cracking
Methods

0.000
title
1

238000005336
cracking
Methods

0.000
abstract
2

229930195733
hydrocarbon
Natural products

0.000
abstract
2

150000002430
hydrocarbons
Chemical class

0.000
abstract
2

239000004215
Carbon black (E152)
Substances

0.000
abstract
1

239000000571
coke
Substances

0.000
abstract
1

239000000376
reactant
Substances

0.000
abstract
1

XLYOFNOQVPJJNP-UHFFFAOYSA-N
water
Substances

O
XLYOFNOQVPJJNP-UHFFFAOYSA-N
0.000
abstract
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

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

H—ELECTRICITY

H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER

H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY

H02J2300/00—Systems for supplying or distributing electric power characterised by decentralized, dispersed, or local generation

H02J2300/20—The dispersed energy generation being of renewable origin

H02J2300/28—The renewable source being wind energy

Abstract

In a process for thermally cracking hydrocarbons by passing them in admixture with steam through a multiplicity of tubes arranged in parallel in a cracking furnace, the tubes being subjected to radiant heat sufficient to cause the reactants within the tube to have a temperature of 1200-1600 DEG F., a minor proportion of the tubes are taken offstream by cutting off hydrocarbon feed and passing steam and/or water through said tubes in amount sufficient to maintain the tube temperature at essentially the same level as in the onstream tubes and to effect removal of coke deposit on the interior of the tubes, and thereafter returning said tubes to normal onstream operation. The tubes may pass through a convection-heated section prior to the radiant section, in which case the steam temperature at the cross-over point is at least 700 DEG F. One tube at a time may be decoked in this way, or more than one in which case the change-over may proceed successively.

GB38710/66A
1966-04-29
1966-08-30
Thermal cracking process

Expired

GB1117562A
(en)

Applications Claiming Priority (1)

Application Number
Priority Date
Filing Date
Title

US546277A

US3365387A
(en)

1966-04-29
1966-04-29
Off-stream decoking of a minor portion of on-stream thermal cracking tubes

Publications (1)

Publication Number
Publication Date

GB1117562A
true

GB1117562A
(en)

1968-06-19

Family
ID=24179666
Family Applications (1)

Application Number
Title
Priority Date
Filing Date

GB38710/66A
Expired

GB1117562A
(en)

1966-04-29
1966-08-30
Thermal cracking process

Country Status (12)

Country
Link

US
(1)

US3365387A
(en)

AT
(1)

AT276600B
(en)

BE
(1)

BE687073A
(en)

DE
(1)

DE1568469C3
(en)

DK
(1)

DK116434B
(en)

ES
(1)

ES331979A1
(en)

FR
(1)

FR1501836A
(en)

GB
(1)

GB1117562A
(en)

IL
(1)

IL26518A
(en)

NL
(1)

NL146871B
(en)

NO
(1)

NO138287C
(en)

SE
(1)

SE353077B
(en)

Cited By (1)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

GB2231057A
(en)

*

1989-01-12
1990-11-07
Inst Francais Du Petrole
Process and apparatus for steam cracking hydrocarbons

Families Citing this family (38)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

US3433731A
(en)

*

1967-03-01
1969-03-18
Monsanto Co
Coil decoking in steam cracking by intermittent switch to ethane feed

CA933535A
(en)

*

1969-07-28
1973-09-11
Esso Research And Engineering Company
Process of thermally cracking hydrocarbons with rapid decoking cycling

DE2026319B2
(en)

*

1970-05-29
1979-02-01
Exxon Research And Engineering Co., Linden, N.J. (V.St.A.)

Process for the thermal cracking of a petroleum fraction

US4046869A
(en)

*

1976-02-11
1977-09-06
Texaco Inc.
Steam reforming process

EP0021167B1
(en)

*

1979-06-08
1982-03-03
Linde Aktiengesellschaft
Process and apparatus for the thermal decoking of an apparatus for the thermal cracking of hydrocarbons such apparatus comprising a cracking zone followed by a cooler for the product gas

CA1232856A
(en)

*

1983-10-31
1988-02-16
Akinobu Fukuhara
Method for on-line decoking of flame cracking reactors

US4917787A
(en)

*

1983-10-31
1990-04-17
Union Carbide Chemicals And Plastics Company Inc.
Method for on-line decoking of flame cracking reactors

US4828681A
(en)

*

1984-12-24
1989-05-09
Exxon Research & Engineering Company
Process of thermally cracking hydrocarbons using particulate solids as heat carrier

US5078857A
(en)

*

1988-09-13
1992-01-07
Melton M Shannon
Delayed coking and heater therefor

US5190634A
(en)

*

1988-12-02
1993-03-02
Lummus Crest Inc.
Inhibition of coke formation during vaporization of heavy hydrocarbons

ATE114705T1
(en)

*

1989-04-14
1994-12-15
Procedes Petroliers Petrochim

METHOD AND APPARATUS FOR DECOKING STEAM CRACKERS.

ES2165039T3
(en)

1996-02-23
2002-03-01
Exxonmobil Chem Patents Inc

PROCEDURE FOR OBTAINING OLEFINS FROM RESIDUAL RAW MATERIALS AND OTHER HEAVY RAW MATERIALS.

FR2748273B1
(en)

*

1996-05-06
1998-06-26
Inst Francais Du Petrole

METHOD AND DEVICE FOR THE THERMAL CONVERSION OF HYDROCARBONS INTO ALIPHATIC HYDROCARBONS MORE UNSATURATED THAN THE STARTING PRODUCTS, COMBINING A STAGE OF STEAM CRACKING AND A STAGE OF PYROLYSIS

US5906728A
(en)

*

1996-08-23
1999-05-25
Exxon Chemical Patents Inc.
Process for increased olefin yields from heavy feedstocks

AU7727498A
(en)

1997-06-05
1998-12-21
Atf Resources, Inc.
Method and apparatus for removing and suppressing coke formation during py rolysis

US6406613B1
(en)

1999-11-12
2002-06-18
Exxonmobil Research And Engineering Co.
Mitigation of coke deposits in refinery reactor units

US6585883B1
(en)

1999-11-12
2003-07-01
Exxonmobil Research And Engineering Company
Mitigation and gasification of coke deposits

US6852294B2
(en)

*

2001-06-01
2005-02-08
Conocophillips Company
Alternate coke furnace tube arrangement

FR2837273B1
(en)

*

2002-03-15
2004-10-22
Inst Francais Du Petrole

METHOD FOR AT LEAST PARTIAL REMOVAL OF CARBON DEPOSITS IN A HEAT EXCHANGER

US20050038304A1
(en)

*

2003-08-15
2005-02-17
Van Egmond Cor F.
Integrating a methanol to olefin reaction system with a steam cracking system

US20060188417A1
(en)

*

2005-02-23
2006-08-24
Roth James R
Radiant tubes arrangement in low NOx furnace

US7513260B2
(en)

*

2006-05-10
2009-04-07
United Technologies Corporation
In-situ continuous coke deposit removal by catalytic steam gasification

US8864977B2
(en)

*

2008-07-11
2014-10-21
Exxonmobil Chemical Patents Inc.
Process for the on-stream decoking of a furnace for cracking a hydrocarbon feed

US8684384B2
(en)

*

2009-01-05
2014-04-01
Exxonmobil Chemical Patents Inc.
Process for cracking a heavy hydrocarbon feedstream

US8815080B2
(en)

*

2009-01-26
2014-08-26
Lummus Technology Inc.
Adiabatic reactor to produce olefins

US8137476B2
(en)

2009-04-06
2012-03-20
Synfuels International, Inc.
Secondary reaction quench device and method of use

US9127211B2
(en)

*

2011-09-13
2015-09-08
Sbt Technology, Inc.
Ethylene furnace decoking method

MX354848B
(en)

*

2011-12-21
2018-03-16
Hyl Tech S A De C V
Method and apparatus for production of direct reduced iron (dri) utilizing coke oven gas.

CN104520256A
(en)

2012-07-05
2015-04-15
国际壳牌研究有限公司
Integrated process for the preparation of olefins

EP3040325A1
(en)

2014-12-31
2016-07-06
Shell Internationale Research Maatschappij B.V.
Process for preparing ethylene, propylene and isoprene

EP3807381A1
(en)

*

2018-06-12
2021-04-21
SABIC Global Technologies B.V.
Naphtha splitter integration with hncc technology

WO2020159719A1
(en)

2019-01-30
2020-08-06
Exxonmobil Chemical Patents Inc.
Process and system for processing asphaltenes-rich feed

CN113574138B
(en)

2019-03-20
2023-09-22
埃克森美孚化学专利公司
Method for in-service decoking

US11072749B2
(en)

2019-03-25
2021-07-27
Exxonmobil Chemical Patents Inc.
Process and system for processing petroleum feed

WO2021230917A2
(en)

2019-12-30
2021-11-18
Exxonmobil Chemical Patents Inc.
Hydrocarbon pyrolysis with less exhaust emission

EP4277966A1
(en)

2021-01-18
2023-11-22
ExxonMobil Chemical Patents Inc.
Methods and systems for cracking hydrocarbons

WO2023114623A1
(en)

2021-12-16
2023-06-22
Exxonmobil Chemical Patents Inc.
Duty recovery system and process for steam cracking furnace

WO2023114633A1
(en)

2021-12-16
2023-06-22
Exxonmobil Chemical Patents Inc.
Steam cracking furnace and process

Family Cites Families (8)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

DE537895C
(en)

*

1923-06-26
1931-11-07
I G Farbenindustrie Akt Ges

Process for the production of gases rich in ethylene

US2076847A
(en)

*

1934-07-10
1937-04-13
Universal Oil Prod Co
Cleaning furnace tube

US2289351A
(en)

*

1939-04-06
1942-07-14
Texas Co
Method of cleaning heater tubes

US2372186A
(en)

*

1941-07-05
1945-03-27
United Gas Improvement Co
Pyrolyzing method and apparatus

FR984365A
(en)

*

1948-04-12
1951-07-05
Petrocarbon Ltd

Improvements in processes and devices for the thermal treatment of hydrocarbons

CH294686A
(en)

*

1949-07-26
1953-11-30
Limited Petrocarbon

Process for converting liquid hydrocarbons into olefin-containing gases and aromatic hydrocarbons.

BE617949A
(en)

*

1961-05-30
1962-09-17
Csf

Electronic key generator

US3268435A
(en)

*

1963-09-30
1966-08-23
Sellin Jan
Process and apparatus for admission to tubes in tube heaters

1966

1966-04-29
US
US546277A
patent/US3365387A/en
not_active
Expired – Lifetime

1966-08-30
GB
GB38710/66A
patent/GB1117562A/en
not_active
Expired

1966-09-15
NO
NO164749A
patent/NO138287C/en
unknown

1966-09-18
IL
IL26518A
patent/IL26518A/en
unknown

1966-09-19
BE
BE687073D
patent/BE687073A/xx
not_active
IP Right Cessation

1966-09-21
NL
NL666613309A
patent/NL146871B/en
not_active
IP Right Cessation

1966-09-23
FR
FR77382A
patent/FR1501836A/en
not_active
Expired

1966-09-28
DE
DE1568469A
patent/DE1568469C3/en
not_active
Expired

1966-09-30
AT
AT918066A
patent/AT276600B/en
active

1966-10-05
DK
DK515466AA
patent/DK116434B/en
unknown

1966-10-06
ES
ES0331979A
patent/ES331979A1/en
not_active
Expired

1966-10-10
SE
SE13692/66A
patent/SE353077B/xx
unknown

Cited By (2)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

GB2231057A
(en)

*

1989-01-12
1990-11-07
Inst Francais Du Petrole
Process and apparatus for steam cracking hydrocarbons

GB2231057B
(en)

*

1989-01-12
1993-03-17
Inst Francais Du Petrole
Process and apparatus for steam cracking hydrocarbons

Also Published As

Publication number
Publication date

NL146871B
(en)

1975-08-15

DE1568469B2
(en)

1977-03-10

DE1568469C3
(en)

1982-09-16

NL6613309A
(en)

1967-10-30

DK116434B
(en)

1970-01-12

US3365387A
(en)

1968-01-23

IL26518A
(en)

1970-03-22

BE687073A
(en)

1967-03-20

AT276600B
(en)

1969-11-25

NO138287B
(en)

1978-05-02

NO138287C
(en)

1978-08-09

SE353077B
(en)

1973-01-22

ES331979A1
(en)

1967-07-16

DE1568469A1
(en)

1972-02-24

FR1501836A
(en)

1967-11-18

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