US2011028307A1PendingUtilityA1
Catalyst and process for producing liquefied petroleum gas
Est. expiryNov 7, 2025(expired)· nominal 20-yr term from priority
B01J 29/084B01J 35/40C10L 3/12Y02P20/582C07C 2529/12B01J 37/0201C07C 9/10C07C 1/20C07C 2523/42C07C 2523/44B01J 23/44B01J 37/0236B01J 23/42C07C 2529/08C07C 9/08C07C 2521/08B01J 35/19B01J 35/617
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Claims
Abstract
A catalyst for producing a liquefied petroleum gas according to the present invention comprises a Pd- and/or Pt-based catalyst component and a USY-type zeolite. By using the catalyst, a hydrocarbon containing propane or butane as a main component, i.e. a liquefied petroleum gas, can be produced with high activity, high selectivity and high yield from at least one of methanol and dimethyl ether.
Claims
exact text as granted — not AI-modified1 . A catalyst for producing a liquefied petroleum gas, which is used for producing a liquefied petroleum gas containing propane or butane as a main component by reacting at least one selected from the group consisting of methanol and dimethyl ether with hydrogen, comprising
a Pd- and/or Pt-based catalyst component in which Pd and/or Pt is supported on a support; and a USY-type zeolite.
2 . A catalyst according to claim 1 , wherein a ratio (by weight) of the Pd- and/or Pt-based catalyst component to the USY-type zeolite is 0.1 to 1.5 (Pd- and/or Pt-based catalyst component/USY-type zeolite).
3 . A catalyst according to claim 1 , wherein the amount of supported Pd and/or Pt in the Pd- and/or Pt-based catalyst component is 0.1 to 5% by weight.
4 . A catalyst according to claim 1 , wherein the support for the Pd- and/or Pt-based catalyst component is silica.
5 . A catalyst according to claim 4 , wherein a specific surface area of the silica support for the Pd- and/or Pt-based catalyst component is 450 m 2 /g or more.
6 . A catalyst according to claim 1 , wherein the USY-type zeolite has a SiO 2 /Al 2 O 3 ratio of 5 to 50.Join the waitlist — get patent alerts
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