CL2012001247A1 - Metodo para mejorar la transferencia de calor de un intercambiador de calor, que comprende; determinar un area de maximo flujo de calor; disponer un aparato de mejoramiento de flujo del fluido de proceso; metodo para instalar un aparato de mejoramiento de flujo; aparato de intercambio de calor; y proceso para producir olefinas. - Google Patents

Metodo para mejorar la transferencia de calor de un intercambiador de calor, que comprende; determinar un area de maximo flujo de calor; disponer un aparato de mejoramiento de flujo del fluido de proceso; metodo para instalar un aparato de mejoramiento de flujo; aparato de intercambio de calor; y proceso para producir olefinas.

Info

Publication number
CL2012001247A1
CL2012001247A1 CL2012001247A CL2012001247A CL2012001247A1 CL 2012001247 A1 CL2012001247 A1 CL 2012001247A1 CL 2012001247 A CL2012001247 A CL 2012001247A CL 2012001247 A CL2012001247 A CL 2012001247A CL 2012001247 A1 CL2012001247 A1 CL 2012001247A1
Authority
CL
Chile
Prior art keywords
flow
heat
heat exchanger
area
installing
Prior art date
Application number
CL2012001247A
Other languages
English (en)
Inventor
Frank D Mcccarthy
Haan Stephen De
Original Assignee
Lummus Technology Inc
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.)
Filing date
Publication date
Application filed by Lummus Technology Inc filed Critical Lummus Technology Inc
Publication of CL2012001247A1 publication Critical patent/CL2012001247A1/es

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/06—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
    • F28F13/12—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media by creating turbulence, e.g. by stirring, by increasing the force of circulation
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/02—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by influencing fluid boundary
    • 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
    • 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
    • C10G9/18—Apparatus
    • C10G9/20—Tube furnaces
    • 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
    • C10G9/18—Apparatus
    • C10G9/20—Tube furnaces
    • C10G9/206—Tube furnaces controlling or regulating the tube furnaces
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23D—BURNERS
    • F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
    • F23D14/02—Premix gas burners, i.e. in which gaseous fuel is mixed with combustion air upstream of the combustion zone
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00—Tubular elements; Assemblies of tubular elements
    • F28F1/02—Tubular elements of cross-section which is non-circular
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00—Tubular elements; Assemblies of tubular elements
    • F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00—Tubular elements; Assemblies of tubular elements
    • F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/40—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only inside the tubular element
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/40—Characteristics of the process deviating from typical ways of processing
    • C10G2300/4056—Retrofitting operations
    • 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
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/20—C2-C4 olefins
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0022—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for chemical reactors
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2210/00—Heat exchange conduits
    • F28F2210/02—Heat exchange conduits with particular branching, e.g. fractal conduit arrangements
    • 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
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T29/00—Metal working
    • Y10T29/49—Method of mechanical manufacture
    • Y10T29/4935—Heat exchanger or boiler making

Abstract

MÉTODO Y APARATO PARA FABRICAR UN APARATO INTERCAMBIADOR DE CALOR PARA LA DESCOMPOSICIÓN, PIROLISIS, DE HIDROCARBUROS EN UNA MAYOR SELECTIVIDAD Y PERÍODO DE EJECUCIÓN MÁS LARGOS, EL CUAL MEJORA LA TRANSFERENCIA DE CALOR, TENIENDO POR LO MENOS UN TUBO INTERCAMBIADOR DE CALOR, QUE COMPRENDE; A) DETERMINAR UN ÁREA DE MÁXIMO FLUJO DE CALOR DEL POR LO MENOS UN TUBO INTERCAMBIADOR DE CALOR; Y B) DISPONER EN EL POR LO MENOS UN TUBO INTERCAMBIADOR DE CALOR, UN APARATO DE MEJORAMIENTO DE FLUJO, TAL COMO UN DEFLECTOR CON UN ÁNGULO DE GIRO, PARA CREAR UN PATRÓN DE FLUJO DESEABLE EN UN FLUIDO DE PROCESO QUE FLUYE A TRAVÉS DEL POR LO MENOS UN TUBO INTERCAMBIADOR DE CALOR; C) DONDE EL APARATO DE MEJORAMIENTO DE FLUJO ES DISPUESTO EN EL POR LO MENOS UN TUBO INTERCAMBIADOR DE CALOR AGUAS ARRIBA DE O EN EL ÁREA DETERMINADA DE MÁXIMO FLUJO DE CALOR DEL POR LO MENOS UN TUBO INTERCAMBIADOR DE CALOR; MÉTODO PARA INSTALAR UN APARATO DE MEJORAMIENTO DE FLUJO; APARATO DE INTERCAMBIO DE CALOR; Y PROCESO PARA PRODUCIR OLEFINAS.
CL2012001247A 2010-02-08 2012-05-11 Metodo para mejorar la transferencia de calor de un intercambiador de calor, que comprende; determinar un area de maximo flujo de calor; disponer un aparato de mejoramiento de flujo del fluido de proceso; metodo para instalar un aparato de mejoramiento de flujo; aparato de intercambio de calor; y proceso para producir olefinas. CL2012001247A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US30230410P 2010-02-08 2010-02-08

Publications (1)

Publication Number Publication Date
CL2012001247A1 true CL2012001247A1 (es) 2012-08-10

Family

ID=44356110

Family Applications (1)

Application Number Title Priority Date Filing Date
CL2012001247A CL2012001247A1 (es) 2010-02-08 2012-05-11 Metodo para mejorar la transferencia de calor de un intercambiador de calor, que comprende; determinar un area de maximo flujo de calor; disponer un aparato de mejoramiento de flujo del fluido de proceso; metodo para instalar un aparato de mejoramiento de flujo; aparato de intercambio de calor; y proceso para producir olefinas.

Country Status (14)

Country Link
US (1) US20120203049A1 (es)
EP (1) EP2534436A2 (es)
JP (1) JP5619174B2 (es)
KR (3) KR20120101717A (es)
CN (1) CN102597685B (es)
AR (1) AR081445A1 (es)
BR (1) BR112012019837A2 (es)
CA (1) CA2774979C (es)
CL (1) CL2012001247A1 (es)
MX (1) MX2012004568A (es)
SG (1) SG182353A1 (es)
TW (1) TWI524048B (es)
WO (1) WO2011097610A2 (es)
ZA (1) ZA201203128B (es)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103791753B (zh) 2012-10-30 2016-09-21 中国石油化工股份有限公司 一种传热管
GB2529407B (en) * 2014-08-18 2020-01-08 Joan Philomena Jones Heater
EP3387333A4 (en) * 2015-12-09 2019-08-28 Fulton Group N.A., Inc. COMPACT LIQUID HEATING SYSTEM WITH HEAT FLOW HIGH VOLUME DENSITY USING INCREASED HEAT EXCHANGE DROP

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6140396A (ja) * 1984-08-01 1986-02-26 Toyo Eng Corp 炭化水素の熱分解装置
JP3001181B2 (ja) * 1994-07-11 2000-01-24 株式会社クボタ エチレン製造用反応管
US5656150A (en) * 1994-08-25 1997-08-12 Phillips Petroleum Company Method for treating the radiant tubes of a fired heater in a thermal cracking process
JPH09222083A (ja) * 1996-02-16 1997-08-26 Matsushita Electric Ind Co Ltd 冷凍サイクルと圧縮機
KR100525879B1 (ko) * 1997-06-10 2005-11-02 엑손모빌 케미칼 패턴츠 인코포레이티드 공정 유체 가열용 가열 장치 및 올레핀의 제조 방법
CN1133862C (zh) * 1998-09-16 2004-01-07 中国石油化工集团公司 一种热交换管及其制造方法和应用
JP2000146482A (ja) 1998-09-16 2000-05-26 China Petrochem Corp 熱交換器チュ―ブ、その製造方法、及びその熱交換器チュ―ブを用いるクラッキング炉又は他の管状加熱炉
US6685893B2 (en) * 2001-04-24 2004-02-03 Abb Lummus Global Inc. Pyrolysis heater
US6425757B1 (en) 2001-06-13 2002-07-30 Abb Lummus Global Inc. Pyrolysis heater with paired burner zoned firing system
CN2735285Y (zh) * 2004-04-24 2005-10-19 辽宁石油化工大学 分段扰流子
US8585890B2 (en) * 2007-03-28 2013-11-19 China Petroleum & Chemical Corporation Tubular cracking furnace
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CN101619949B (zh) * 2009-07-31 2011-11-09 惠生工程（中国）有限公司 一种强化传热管

Also Published As

Publication number Publication date
ZA201203128B (en) 2013-02-27
KR101599662B1 (ko) 2016-03-04
CA2774979A1 (en) 2011-08-11
JP2013510936A (ja) 2013-03-28
SG182353A1 (en) 2012-08-30
CN102597685B (zh) 2014-10-01
CA2774979C (en) 2015-02-03
CN102597685A (zh) 2012-07-18
AR081445A1 (es) 2012-09-05
EP2534436A2 (en) 2012-12-19
JP5619174B2 (ja) 2014-11-05
MX2012004568A (es) 2012-06-08
BR112012019837A2 (pt) 2016-05-17
KR20140132013A (ko) 2014-11-14
TWI524048B (zh) 2016-03-01
WO2011097610A3 (en) 2011-12-01
WO2011097610A2 (en) 2011-08-11
KR20120101717A (ko) 2012-09-14
TW201200837A (en) 2012-01-01
US20120203049A1 (en) 2012-08-09
KR20140132014A (ko) 2014-11-14

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Independentes et al. 3.4. 1-Variáveis independentes