IT1156128B - Propylene prepn from 4-12c olefin(s) - Google Patents

Propylene prepn from 4-12c olefin(s)

Info

Publication number
IT1156128B
IT1156128B IT24550/82A IT2455082A IT1156128B IT 1156128 B IT1156128 B IT 1156128B IT 24550/82 A IT24550/82 A IT 24550/82A IT 2455082 A IT2455082 A IT 2455082A IT 1156128 B IT1156128 B IT 1156128B
Authority
IT
Italy
Prior art keywords
olefins
propylene
mixt
zeolite
condensn
Prior art date
Application number
IT24550/82A
Other languages
Italian (it)
Other versions
IT8224550A0 (en
Inventor
Fausto Colombo
Giuseppe Paparatto
Enrico Moretti
Original Assignee
Montedipe Spa
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 Montedipe Spa filed Critical Montedipe Spa
Priority to IT24550/82A priority Critical patent/IT1156128B/en
Publication of IT8224550A0 publication Critical patent/IT8224550A0/en
Priority to EP83111240A priority patent/EP0109059B1/en
Priority to DE8383111240T priority patent/DE3372474D1/en
Application granted granted Critical
Publication of IT1156128B publication Critical patent/IT1156128B/en

Links

Landscapes

  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)

Abstract

4-12 (5-8)C olefins are converted to propylene by contact with a crystalline zeolitic alumino-silicate having SiO2/Al2O3 ratio (Z) not more than 300, e.g. a ZSM 5 or ZSM 11 zeolite, at space velocity higher than 50 (pref. 60-250) kg/hr. olefins per kg. zeolite, at 400-600 deg. C. The zeolite is pref. used in acid form or modified with Mg, Ca, Sr, Ba, P, Cr, Cu or Zn has average crystallite size below 0.5 micro m., and Z=25-220; it may be admixed with SiO2 or Al2O3 as binder. Activation with air at 450-750 deg. C, and periodic regeneration with air at 400-600 deg. C is appropriate. A mixt. of 4C olefins and paraffins that is not readily separable may be treated by the following steps; by contact with a zeolitic catalyst at 320-380 deg. C the 4C olefins in the mixt. are oligomerised at 5-8C olefins. These are sepd. by condensn. from the 4C paraffins, and converted by the present process to a mixt. contg. propylene. Hydrocarbons contg. 4 or more C atoms are then sepd. by condensn. from the propylene and other hydrocarbons of less than 4C atoms.
IT24550/82A 1982-11-10 1982-12-02 Propylene prepn from 4-12c olefin(s) IT1156128B (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
IT24550/82A IT1156128B (en) 1982-12-02 1982-12-02 Propylene prepn from 4-12c olefin(s)
EP83111240A EP0109059B1 (en) 1982-11-10 1983-11-10 Process for converting olefins having 4 to 12 carbon atoms into propylene
DE8383111240T DE3372474D1 (en) 1982-11-10 1983-11-10 Process for converting olefins having 4 to 12 carbon atoms into propylene

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
IT24550/82A IT1156128B (en) 1982-12-02 1982-12-02 Propylene prepn from 4-12c olefin(s)

Publications (2)

Publication Number Publication Date
IT8224550A0 IT8224550A0 (en) 1982-12-02
IT1156128B true IT1156128B (en) 1987-01-28

Family

ID=11213940

Family Applications (1)

Application Number Title Priority Date Filing Date
IT24550/82A IT1156128B (en) 1982-11-10 1982-12-02 Propylene prepn from 4-12c olefin(s)

Country Status (1)

Country Link
IT (1) IT1156128B (en)

Also Published As

Publication number Publication date
IT8224550A0 (en) 1982-12-02

Similar Documents

Publication Publication Date Title
EP0050021B1 (en) Production of aromatics from ethane and/or ethylene
CA2211043C (en) Hydrocarbon treatment and catalyst therefor
CA2015209A1 (en) Production of olefins
EP0259954B1 (en) Process for converting c2 to c12 aliphatics to aromatics over a zinc activated zeolite
WO2002028987A8 (en) A process for cracking an olefin-rich hydrocarbon feedstock
JP3090370B2 (en) Method for converting a feedstock comprising linear olefins
US5243117A (en) Catalyst and process for the selective production of para-dialkyl substituted benzenes
US4354049A (en) Process for the production of aromatic hydrocarbons
EP0101291A3 (en) Improved catalytic cracking
EP0655277A1 (en) Amorphous aluminosilicate catalyst
CA1207300A (en) Catalyst, a process for its preparation and an isomerization process in the presence of this catalyst
JPH06509352A (en) Hydrocarbon conversion methods
CA1122619A (en) Disproportionation of toluene
EP0005315B1 (en) Production of xylene hydrocarbons
IT1156128B (en) Propylene prepn from 4-12c olefin(s)
IT1206114B (en) Propylene prepn from 4-12c olefin(s)
IT1161559B (en) Propylene prepn from 4-12c olefin(s)
EP0146525B1 (en) Process for preparing crystalline silicas
US5093294A (en) Zeolite catalysts suitable for hydrocarbon conversion
US6130363A (en) Catalyst with a base of modified MFI zeolite, and its use in the isomerization of a C8 aromatic cut
US5336648A (en) Zeolite catalysts suitable for hydrocarbon conversion
IT1154546B (en) PROCESS FOR THE JOINT PRODUCTION OF PROPYLENE AND ISOBUTENE FROM LINEAR BUTENS
JPH0324456B2 (en)
US4125483A (en) Dimerization process catalyst
JPS6263528A (en) Production of p-xylene

Legal Events

Date Code Title Description
TA Fee payment date (situation as of event date), data collected since 19931001

Effective date: 19961217