EP2048217A3 - Method for decarbonising cracking furnaces - Google Patents
Method for decarbonising cracking furnaces Download PDFInfo
- Publication number
- EP2048217A3 EP2048217A3 EP08017417A EP08017417A EP2048217A3 EP 2048217 A3 EP2048217 A3 EP 2048217A3 EP 08017417 A EP08017417 A EP 08017417A EP 08017417 A EP08017417 A EP 08017417A EP 2048217 A3 EP2048217 A3 EP 2048217A3
- Authority
- EP
- European Patent Office
- Prior art keywords
- decoking
- cracking
- cracking furnace
- entkokungsabgas
- exhaust gas
- 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.)
- Ceased
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B43/00—Preventing or removing incrustations
- C10B43/02—Removing incrustations
- C10B43/10—Removing incrustations by burning out
-
- 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
- C10G70/00—Working-up undefined normally gaseous mixtures obtained by processes covered by groups C10G9/00, C10G11/00, C10G15/00, C10G47/00, C10G51/00
-
- 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
Landscapes
- 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)
- Materials Engineering (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Die Erfindung beschreibt ein Verfahren zur Entkokung eines Spaltofens (1) zur Spaltung von Kohlenwasserstoffen. Während der Entkokung wird in die Spaltrohre (2) und die anschließenden Spaltgaskühler (3) ein Gemisch aus Luft und Wasserdampf geschickt. Während der Entkokung wird dabei die Strahlungszone (1a) des Spaltofens (1) über die Brenner (4) auf einer Temperatur von ca. 1100°C gehalten. Das dabei entstehende Entkokungsabgas (5) wird zu einem Zyklonabscheider (6) geleitet. Vor dem Zyklonabscheider (6) wird Wasser (7) in regelmäßigen Zeitabständen in das Entkokungsabgas (5) eingedüst. Im Zyklonabscheider (6) werden feste Partikel, wie beispielsweise Kokspartikel oder Staubpartikel, aus dem gasförmigen Entkokungsabgas herausgetrennt (8). Das von festen Bestandteilen befreite Entkokungsabgas (9) wird in den Feuerraum der Strahlungszone (1a) des Spaltofens (1) geführt. Bei den dort herrschenden Tempertauren wird das im Entkokungsabgas (9) noch vorhandene Kohlenmonoxid nahezu vollständig zu Kohlendioxid umgewandelt. Das, dem Spaltofen entweichende, Abgas (10) ist somit nunmehr befreit von Koks- bzw. Staubpartikeln und Kohlenmonoxid. The invention describes a process for decoking a cracking furnace (1) for the cracking of hydrocarbons. During decoking, a mixture of air and water vapor is sent into the cracking tubes (2) and the subsequent quenching gas coolers (3). During decoking, the radiation zone (1a) of the cracking furnace (1) is kept at a temperature of about 1100 ° C. via the burners (4). The resulting Entkokungsabgas (5) is passed to a cyclone separator (6). Before the cyclone separator (6) water (7) is injected into the Entkokungsabgas (5) at regular intervals. In the cyclone separator (6), solid particles, such as coke particles or dust particles, are separated from the gaseous decoke exhaust gas (8). The freed from solid components Entkokungsabgas (9) is fed into the combustion chamber of the radiation zone (1a) of the cracking furnace (1). In the tempertures prevailing there, the carbon monoxide still present in the decoking exhaust gas (9) is almost completely converted to carbon dioxide. The, the cracking furnace escaping, exhaust gas (10) is thus now exempt from coke or dust particles and carbon monoxide.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE200710048984 DE102007048984A1 (en) | 2007-10-12 | 2007-10-12 | Process for the decoking of cracking furnaces |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2048217A2 EP2048217A2 (en) | 2009-04-15 |
EP2048217A3 true EP2048217A3 (en) | 2012-06-06 |
Family
ID=40298632
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP08017417A Ceased EP2048217A3 (en) | 2007-10-12 | 2008-10-02 | Method for decarbonising cracking furnaces |
Country Status (2)
Country | Link |
---|---|
EP (1) | EP2048217A3 (en) |
DE (1) | DE102007048984A1 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103965947B (en) * | 2013-02-06 | 2015-10-28 | 中国石油化工集团公司 | A kind of pyrolyzer furnace binding |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2929316A1 (en) * | 1978-08-04 | 1980-02-28 | Schroeder Wilburn C | CONTINUOUS METHOD FOR HYDROGENATING COAL |
EP0021167A1 (en) * | 1979-06-08 | 1981-01-07 | 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 |
EP0036151A1 (en) * | 1980-03-15 | 1981-09-23 | BASF Aktiengesellschaft | Process for thermally decoking coolers for cracked gases |
WO1990012851A1 (en) * | 1989-04-14 | 1990-11-01 | Procedes Petroliers Et Petrochimiques | Process and apparatus for decoking a steam-craking installation |
US5183642A (en) * | 1989-10-06 | 1993-02-02 | Procedes Petroliers Et Petrochimiques | Installation for steam cracking hydrocarbons, with solid erosive particles being recycled |
EP0573001A1 (en) * | 1992-06-03 | 1993-12-08 | Praxair Technology, Inc. | Waste recycle system |
EP1087007A2 (en) * | 1999-09-22 | 2001-03-28 | Technip Italy S.p.A. | Process and apparatus for reducing the coke dust in the effluents during the decoking of cracking ovens |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2830824A1 (en) | 1978-07-13 | 1980-01-24 | Linde Ag | Steam-cracking of heavy hydrocarbon(s) - using the waste heat to pre-heat the oil before and after previous hydrogenation |
DE2854061A1 (en) | 1978-12-14 | 1980-07-03 | Linde Ag | METHOD FOR PREHEATING HYDROCARBONS BEFORE THERMAL CLEAVING |
DE4102862A1 (en) | 1991-01-31 | 1992-08-06 | Linde Ag | METHOD FOR THE DECOKING OF SPLIT OVENS |
-
2007
- 2007-10-12 DE DE200710048984 patent/DE102007048984A1/en not_active Withdrawn
-
2008
- 2008-10-02 EP EP08017417A patent/EP2048217A3/en not_active Ceased
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2929316A1 (en) * | 1978-08-04 | 1980-02-28 | Schroeder Wilburn C | CONTINUOUS METHOD FOR HYDROGENATING COAL |
EP0021167A1 (en) * | 1979-06-08 | 1981-01-07 | 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 |
EP0036151A1 (en) * | 1980-03-15 | 1981-09-23 | BASF Aktiengesellschaft | Process for thermally decoking coolers for cracked gases |
WO1990012851A1 (en) * | 1989-04-14 | 1990-11-01 | Procedes Petroliers Et Petrochimiques | Process and apparatus for decoking a steam-craking installation |
US5183642A (en) * | 1989-10-06 | 1993-02-02 | Procedes Petroliers Et Petrochimiques | Installation for steam cracking hydrocarbons, with solid erosive particles being recycled |
EP0573001A1 (en) * | 1992-06-03 | 1993-12-08 | Praxair Technology, Inc. | Waste recycle system |
EP1087007A2 (en) * | 1999-09-22 | 2001-03-28 | Technip Italy S.p.A. | Process and apparatus for reducing the coke dust in the effluents during the decoking of cracking ovens |
Also Published As
Publication number | Publication date |
---|---|
DE102007048984A1 (en) | 2009-04-16 |
EP2048217A2 (en) | 2009-04-15 |
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Legal Events
Date | Code | Title | Description |
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PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
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Extension state: AL BA MK RS |
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RAP1 | Party data changed (applicant data changed or rights of an application transferred) |
Owner name: LINDE AG |
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RIC1 | Information provided on ipc code assigned before grant |
Ipc: C10B 43/02 20060101AFI20120427BHEP Ipc: B01J 8/08 20060101ALI20120427BHEP Ipc: C10G 9/16 20060101ALI20120427BHEP |
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17P | Request for examination filed |
Effective date: 20121115 |
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AKX | Designation fees paid |
Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MT NL NO PL PT RO SE SI SK TR |
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17Q | First examination report despatched |
Effective date: 20130410 |
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STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION HAS BEEN REFUSED |
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18R | Application refused |
Effective date: 20161213 |