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US4324696A Expired / Lapsed US ⏱️ 0.0 years remaining

Method of preparing crystalline zeolite catalyst of high activity

Assignee: Mobil Oil AS
•
Filing: 1980-03-10
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Granted: 1982-04-13
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Expires: 2000-03-10
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Abstract

Abstract Super active catalyst of high hydrocarbon conversion activity prepared by contacting crystalline zeolite materials of silica/alumina mole ratios greater than 7 and having a constraint index between 1/2 and 12 with steam followed by base exchange of the resultant steamed product with an ammonium salt.

Inventors

  • 👤 Joseph N. Miale

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-24 04:39
CPC Classifications
B; B01; B01J; B01J29/00; B01J29/04; B01J29/06; B01J29/70; B01J29/7019; B01J29/40; B01J29/7046; B01J37/00; B01J37/08; B01J37/10; B01J2229/00; B01J2229/30; B01J2229/36; Y; Y10; Y10S; Y10S423/00; Y10S423/22; Y10S423/29; Y10S423/33

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 66 words
A method for preparing a super active synthetic crystalline zeolite catalyst material of high hydrocarbon conversion activity having a constraint index between about 1/2 and 12 and a SiO 2 /Al 2 O 3 mole ratio greater than 7 which comprises contacting the hydrogen form of zeolite ZSM-12, ZSM-20 or ZSM-23 with steam followed by base exchange of the resultant steamed product with an ammonium salt.
Claim 2
Independent Claim 66 words
A method for preparing a super active synthetic crystalline zeolite catalyst material of high hydrocarbon conversion activity having a constraint index between about 1/2 and 12 and a SiO 2 /Al 2 O 3 mole ratio greater than 7 which comprises contacting the hydrogen form of zeolite ZSM-12, ZSM-20 or ZSM-23 with steam followed by base exchange of the resultant steamed product with an ammonium salt.
Claim 3
Dependent Claim 9 words
The product produced by the method of claim 1.
Claim 4
Dependent Claim 48 words
A method according to claim 1 wherein steaming is conducted at between about 50 to 100% H 2 O pressure for a period between about 10 minutes and 2 hours at about 1000° F. or for a period between about 4 and 24 hours at about 900° F.
Claim 5
Dependent Claim 18 words
A method according to claim 3 wherein said ammonium salt solution is between about 0.1 and 5 N.
Claim 6
Dependent Claim 11 words
The product produced by the method of claims 3 or 4.
Claim 7
Dependent Claim 16 words
A method according to claim 1 wherein said zeolite is the acid form of zeolite ZSM-12.
Claim 8
Dependent Claim 16 words
A method according to claim 1 wherein said zeolite is the acid form of zeolite ZSM-20.
Claim 9
Dependent Claim 16 words
A method according to claim 1 wherein said zeolite is the acid form of zeolite ZSM-23.

References Cited (Backward Citations)

US3140252A Cited
US3331882A Cited
US3293192A Cited
US3391075A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-04-12 1985-10-12 1986-04-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-04-12 1989-10-12 1990-04-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-04-12 1993-10-12 1994-04-13 $7700.00 Window Closed / Lapsed

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