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Institution

Mobil

About: Mobil is a based out in . It is known for research contribution in the topics: Catalysis & Zeolite. The organization has 7085 authors who have published 10642 publications receiving 237497 citations. The organization is also known as: Socony-Vacuum Oil Company & Standard Oil Company of New York.


Papers
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Journal ArticleDOI
TL;DR: In this paper, benzene was alkylated with propylene over HZSM-5 zeolite catalysts to produce cumene with 88-94% selectivity.

83 citations

Patent
Bobbie J. Patton1, Vasel R. Slover1
07 Jul 1975
TL;DR: In this article, a transducers are mounted with a cavity formed between the drill collar and drill bit when they are in slidable engagement to measure axial and rotational motions of the drill bit.
Abstract: Apparatus is provided for measuring weight and torque on the drill bit in a logging-while-drilling system. The upper end of the drill bit is adapted for slidable engagement with the lower end of the drill collar. Transducers are mounted with a cavity formed between the drill collar and drill bit when they are in slidable engagement. The transducers measure axial and rotational motions of the drill bit which represent weight and torque on the drill bit, respectively.

83 citations

Patent
Paul G. Rodewald1
31 Mar 1976
TL;DR: In this article, a catalyst for selective production of C 2 -C 3 olefins is provided, which is especially applicable for the selective production and use of the specified catalyst in selectively converting lower monohydric alcohols and their ethers, especially methanol and dimethyl ether, to a hydrocarbon mixture rich in ethylene and propylene.
Abstract: A catalyst is provided, which is especially applicable for the selective production of C 2 -C 3 olefins, comprising a crystalline aluminosilicate zeolite having a silica to alumina ratio of at least about 12, a constraint index, as hereinafter defined, within the approximate range of 1 to 12 and having contained within the interior crystalline structure thereof added amorphous silica in an amount of at least about 0.3 and preferably between about 0.5 and about 30 weight percent. The resultant catalyst is characterized by n-hexane sorption capacity at a temperature of 90° C and a n-hexane partial pressure of 83 mm. of mercury which is at least 1 percent less than corresponding sorption capacity under identical conditions for the unmodified zeolite. Generally, the n-hexane sorption capacity for the described silica-modified zeolite, at the above specified conditions, is 5 to 60 percent less than that for the zeolite which has not undergone treatment to incorporate amorphous silica therein. The invention described herein also encompasses synthesis of the specified catalyst and use of the same in selectively converting lower monohydric alcohols and their ethers, especially methanol and dimethyl ether, to a hydrocarbon mixture rich in ethylene and propylene.

83 citations

Patent
Lewis B. Young1
08 Oct 1980
TL;DR: In this article, a method for decreasing catalyst coking and extending the usable catalyst life by pre-treatment of the catalyst with steam and/or a phosphorus-containing compound was proposed.
Abstract: There is disclosed a method for decreasing catalyst coking and extending the usable catalyst life by pre-treatment of the catalyst with steam and/or a phosphorus-containing compound. Catalysts benefiting from such pre-treatment comprise crystalline zeolites characterized by a silica to alumina mole ratio of at least 12 and a constraint index, as herein defined, within the approximate range of 1 to 12.

83 citations

Patent
Rudolph M. Lago1
12 May 1976
TL;DR: In this article, a catalytic process is provided for converting lower monohydric alcohols and their ethers, especially methanol and dimethyl ether, to a hydrocarbon mixture rich in C 2 -C 3 olefins and mononuclear aromatics with high selectivity for para-xylene production by contact, under conversion conditions.
Abstract: A catalytic process is provided for converting lower monohydric alcohols and their ethers, especially methanol and dimethyl ether, to a hydrocarbon mixture rich in C 2 -C 3 olefins and mononuclear aromatics with high selectivity for para-xylene production by contact, under conversion conditions, with a catalyst bed comprising a major proportion of particle-form inert solid diluent having intermixed therewith a crystalline aluminosilicate zeolite characterized by (1) a crystallite size not greater than 0.5 micron, (2) a particle size less than 2 millimeters in its smallest cross-sectional dimension, (3) a silica to alumina ratio of at least about 12 and (4) a constraint index, as hereinafter defined, within the approximate range of 1 to 12.

83 citations


Authors

Showing all 7085 results

NameH-indexPapersCitations
Galen D. Stucky144958101796
James A. Russell124102487929
Thomas Bein10967742800
George J. Hirasaki6527814164
Kai-Kit Wong6160514680
James Paul5925213394
Sankaran Sundaresan5824110083
Fabio Rocca5732519186
Roland Winston5547313911
Kyger C. Lohmann5414410112
Maurice A. Biot5015437311
Kenneth E. Peters4817113920
Paul L. Stoffa472609323
Clarence D. Chang472399047
Bruce H. Wilkinson451186483
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Performance
Metrics
No. of papers from the Institution in previous years
YearPapers
202112
202011
201910
201818
201712
201610