MY138901A - A reactive distillation alkylation process including in situ catalyst regeneration - Google Patents

A reactive distillation alkylation process including in situ catalyst regeneration

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Publication number
MY138901A
MY138901A MYPI20043492A MY138901A MY 138901 A MY138901 A MY 138901A MY PI20043492 A MYPI20043492 A MY PI20043492A MY 138901 A MY138901 A MY 138901A
Authority
MY
Malaysia
Prior art keywords
catalyst
aromatic
column
paraffin
zone
Prior art date
Application number
Inventor
Winder J Barry
Donald L Wharry
John R Schell
Mary J Brown
Joy L Murray
Richard C Howe
Wayne L Sorenson
Daniel P Szura
Gates Frank
Original Assignee
Sasol North America 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 Sasol North America Inc filed Critical Sasol North America Inc
Priority to MYPI20043492 priority Critical patent/MY138901A/en
Publication of MY138901A publication Critical patent/MY138901A/en

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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

A UNIFIED PROCESS WHICH COUPLES A UNIQUE IN-SITU CATALYST REGENERATION PROCESS WITH A CONTINUOUS REACTIVE DISTILLATION UNDER PRESSURE FOR THE ALKYLATION OF LIGHT AROMATIC HYDROCARBONS SUCH AS BENZENE WITH C2-C30 OLEFINS USING A SOLID ACID ALKYLATION CATALYST SUPPORTED IN THE REFLUX ZONE (21) OF A DISTILLATION COLUMN (SECTION A). PERIODIC REGENERATION OF THE CATALYST (SECTION E, F AND G) IS CARRIED OUT WITH A COUNTERCURRENT INJECTION OF A C4-C16 PARAFFIN (35) BELOW THE BENZENE RECTIFICATION ZONE AT THE TOP OF THE COLUMN, BUT ABOVE THE CATALYST ZONE WHILE THE AROMATIC HYDROCARBON REACTION FEEDSTOCK (17) IS INJECTED CONTINUOUSLY AT A POINT ABOVE A RECTIFICATION ZONE AT THE BASE OF THE COLUMN WHERE THE AROMATIC COMPOUND IS SEPARATED FROM THE PARAFFIN AND BY-PRODUCTS WASHED FROM THE CATALYST. THE USE OF THE C4-C16 PARAFFIN WITH THE AROMATIC AT A MOLE FRACTION IN THE RANGE OF 40 TO 90% ENABLES A REGENERATION TEMPERATURE OF ABOUT 175 - 2500C TO BE ACHIEVED AND MAINTAINED BY ADJUSTING THE COLUMN PRESSURE AND AROMATIC REFLUX RATE. SIGNIFICANTLY LOWER PRESSURES, ON THE ORDER OF 125 TO 370 PSIG, ARE REQUIRED TO ACHIEVE REGENERATION TEMPERATURE THAN WOULD BE OTHERWISE REQUIRED WITH THE USE ONLY OF THE AROMATIC HYDROCARBON TO DILUTE AND WASH THE BY-PRODUCTS FROM THE CATALYST SURFACES.
MYPI20043492 2004-08-26 2004-08-26 A reactive distillation alkylation process including in situ catalyst regeneration MY138901A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
MYPI20043492 MY138901A (en) 2004-08-26 2004-08-26 A reactive distillation alkylation process including in situ catalyst regeneration

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
MYPI20043492 MY138901A (en) 2004-08-26 2004-08-26 A reactive distillation alkylation process including in situ catalyst regeneration

Publications (1)

Publication Number Publication Date
MY138901A true MY138901A (en) 2009-08-28

Family

ID=45699537

Family Applications (1)

Application Number Title Priority Date Filing Date
MYPI20043492 MY138901A (en) 2004-08-26 2004-08-26 A reactive distillation alkylation process including in situ catalyst regeneration

Country Status (1)

Country Link
MY (1) MY138901A (en)

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