Bound phosphorus-modified zeolite catalyst, method of preparing and method of using thereof
Abstract
Disclosed is a bound phosphorus-modified zeolite catalyst. Zeolite is treated with a phosphorus compound to form the phosphorus-treated zeolite. Binder material is treated with a mineral acid prior to being bound with the phosphorus-modified zeolite. The binder material includes inorganic oxide materials, such as alumina, clay, aluminum phosphate and silica-alumina, in particular, a binder of alumina or clay or their combinations. The mineral acid includes hydrochloric acid, nitric acid, phosphoric acid or sulfuric acid. The phosphorus-treated zeolite is combined with the acid-treated inorganic oxide binder material to form a zeolite-binder mixture. Water is added to form an extrudable paste which maybe shaped and is heated to a temperature of about 400° C. or higher to form a bound phosphorus-modified zeolite catalyst. For aromatic alkylation, the bound phosphorus-modified zeolite catalyst is contacted with an aromatic alkylation feed of an aromatic compound and an alkylating agent under reaction conditions suitable for aromatic alkylation.
Claims
exact text as granted — not AI-modified1 - 43 . (canceled)
44 . A method of preparing an alkyl aromatic product comprising:
a) treating a zeolite containing 10-oxygen ring pores with a phosphorus compound to form a phosphorus-treated zeolite; b) treating an inorganic oxide binder material with a mineral acid; c) combining the phosphorus-treated zeolite with an inorganic oxide binder material to form a zeolite-binder mixture; d) heating the zeolite-binder mixture at temperature of about 400° C. or higher to form a bound zeolite catalyst; and e) contacting the bound zeolite catalyst with an aromatic alkylation feed of an aromatic compound and an alkylating agent under reaction conditions suitable for aromatic alkylation.
45 . The method of claim 44 wherein the binder material includes at least one of alumina, clay, aluminum phosphate and silica-alumina.
46 . The method of claim 44 wherein the binder material is an alumina-containing material.
47 . The method of claim 44 wherein the binder material is present in an amount of from about 1% to about 99% by weight of the bound zeolite catalyst.
48 . The method of claim 44 wherein the binder material contains from about 1% to 99% by weight alumina or clay or their combinations.
49 . The method of claim 44 wherein the zeolite is a ZSM-5 zeolite.
50 . The method of claim 44 wherein the phosphorus-treated zeolite is heated to a temperature of about 300° C. or higher.
51 . The method of claim 44 wherein the zeolite-binder mixture is heated to a temperature of from 400° C. to about 700° C.
52 . The method of claim 44 further comprising adding water to the zeolite-binder mixture and shaping the zeolite-binder mixture
53 . The method of claim 44 wherein the aromatic compound is toluene.
54 . The method of claim 44 wherein the aromatic compound is toluene and the alkylating agent is methanol.
55 . The method of claim 44 further comprising steaming the bound zeolite at a temperature of 300° C. or less prior to contacting with the aromatic alkylation feed.
56 . The method of claim 44 wherein the zeolite is treated with a phosphorus compound to form a phosphorus-treated zeolite having a phosphorus content of from 0.01 to about 0.15 gram of phosphorus per gram of zeolite.
57 . The method of claim 56 wherein the zeolite is a ZSM-5 zeolite.
58 . The method of claim 57 wherein the binder material includes at least one of alumina, clay, aluminum phosphate and silica-alumina.
59 . The method of claim 57 wherein the binder material is an alumina-containing material.
60 . The method of claim 57 wherein the binder material is present in an amount of from about 1% to about 99% by weight of the bound ZSM-5 zeolite catalyst.
61 . The method of claim 57 wherein the binder material contains from about 1% to 99% by weight alumina.
62 . The method of claim 57 wherein the phosphorus-treated ZSM-5 zeolite is heated to a temperature of about 300° C. or higher.
63 . The method of claim 56 wherein the zeolite-binder mixture is heated to a temperature of from 400° C. to about 700° C.
64 . The method of claim 54 further comprising steaming the bound ZSM-5 zeolite at a temperature of 300° C. or less prior to contacting with the feed of toluene.
65 . The method of claim 44 wherein the mineral acid is hydrochloric acid, nitric acid, phosphoric acid or sulfuric acid
66 . The method of claim 65 wherein the mineral acid is nitric acid.Cited by (0)
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