EP1793912A4 - Energy efficient method and apparatus for exothermic reactions - Google Patents

Energy efficient method and apparatus for exothermic reactions

Info

Publication number
EP1793912A4
EP1793912A4 EP05760346A EP05760346A EP1793912A4 EP 1793912 A4 EP1793912 A4 EP 1793912A4 EP 05760346 A EP05760346 A EP 05760346A EP 05760346 A EP05760346 A EP 05760346A EP 1793912 A4 EP1793912 A4 EP 1793912A4
Authority
EP
European Patent Office
Prior art keywords
energy efficient
efficient method
exothermic reactions
exothermic
reactions
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
Application number
EP05760346A
Other languages
German (de)
French (fr)
Other versions
EP1793912A2 (en
Inventor
Arvids Judzis Jr
Abraham P Gelbein
John R Adams
Christopher C Boyer
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.)
Catalytic Distillation Technologies
Original Assignee
Catalytic Distillation Technologies
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
Priority claimed from US11/038,755 external-priority patent/US7320745B2/en
Application filed by Catalytic Distillation Technologies filed Critical Catalytic Distillation Technologies
Publication of EP1793912A2 publication Critical patent/EP1793912A2/en
Publication of EP1793912A4 publication Critical patent/EP1793912A4/en
Ceased legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14—Fractional distillation or use of a fractionation or rectification column
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/007—Energy recuperation; Heat pumps
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/009—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping in combination with chemical reactions
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14—Fractional distillation or use of a fractionation or rectification column
    • B01D3/32—Other features of fractionating columns ; Constructional details of fractionating columns not provided for in groups B01D3/16 - B01D3/30
    • B01D3/322—Reboiler specifications
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/42—Regulation; Control
    • B01D3/4211—Regulation; Control of columns
    • B01D3/4261—Side stream
    • 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
    • C10G2400/30—Aromatics

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
EP05760346A 2004-08-10 2005-06-17 Energy efficient method and apparatus for exothermic reactions Ceased EP1793912A4 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US60023604P 2004-08-10 2004-08-10
US11/038,755 US7320745B2 (en) 2005-01-19 2005-01-19 Energy efficient method for exothermic reactions
PCT/US2005/021456 WO2006023022A2 (en) 2004-08-10 2005-06-17 Energy efficient method and apparatus for exothermic reactions

Publications (2)

Publication Number Publication Date
EP1793912A2 EP1793912A2 (en) 2007-06-13
EP1793912A4 true EP1793912A4 (en) 2010-04-07

Family

ID=35968007

Family Applications (1)

Application Number Title Priority Date Filing Date
EP05760346A Ceased EP1793912A4 (en) 2004-08-10 2005-06-17 Energy efficient method and apparatus for exothermic reactions

Country Status (5)

Country Link
EP (1) EP1793912A4 (en)
CN (1) CN101124026B (en)
AR (1) AR054209A1 (en)
TW (1) TWI333871B (en)
WO (1) WO2006023022A2 (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4450311A (en) * 1983-06-29 1984-05-22 Mobil Oil Corporation Heat exchange technique for olefin fractionation and catalytic conversion system
US4456781A (en) * 1983-04-26 1984-06-26 Mobil Oil Corporation Catalytic conversion system for oligomerizing olefinic feedstock to produce heavier hydrocarbons
US4898716A (en) * 1983-06-29 1990-02-06 Mobil Oil Corporation Olefin fractionation and catalytic conversion system
US5243102A (en) * 1992-10-01 1993-09-07 Uop Etherification of C5 -plus olefins by sequential catalytic distillation
EP0673352A1 (en) * 1992-12-10 1995-09-27 Neste Oy Process and reactor system for oligomerization of olefins

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4008290A (en) * 1975-03-10 1977-02-15 Uop Inc. Cumene production
US5336821A (en) * 1993-05-06 1994-08-09 Uop Alkylation process with reactor effluent heat recovery

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4456781A (en) * 1983-04-26 1984-06-26 Mobil Oil Corporation Catalytic conversion system for oligomerizing olefinic feedstock to produce heavier hydrocarbons
US4450311A (en) * 1983-06-29 1984-05-22 Mobil Oil Corporation Heat exchange technique for olefin fractionation and catalytic conversion system
US4898716A (en) * 1983-06-29 1990-02-06 Mobil Oil Corporation Olefin fractionation and catalytic conversion system
US5243102A (en) * 1992-10-01 1993-09-07 Uop Etherification of C5 -plus olefins by sequential catalytic distillation
EP0673352A1 (en) * 1992-12-10 1995-09-27 Neste Oy Process and reactor system for oligomerization of olefins

Also Published As

Publication number Publication date
WO2006023022A3 (en) 2007-08-02
WO2006023022A2 (en) 2006-03-02
TWI333871B (en) 2010-12-01
CN101124026B (en) 2010-06-16
AR054209A1 (en) 2007-06-13
CN101124026A (en) 2008-02-13
EP1793912A2 (en) 2007-06-13
TW200610570A (en) 2006-04-01

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