Crystalline MWW-type titanosilicate catalyst for producing oxidized compound, production process for the catalyst, and process for producing oxidized compound by using the catalyst
Abstract
A crystalline titanosilicate catalyst which is usable as a catalyst in the oxidation reaction of a compound having a carbon-carbon double bond and at least one other functional group, a process for producing the catalyst, and a process for producing an oxidized compound by an oxidation reaction using the catalyst. It has been found that a crystalline titanosilicate having a structural code of MWW effectively functions as a catalyst in an oxidation reaction of a compound having a carbon-carbon double bond and at least one other functional group wherein the carbon-carbon double bond of the compound is oxidized by using a peroxide as an oxidizing agent, thereby to highly selectively provide an intended oxidized compound.
Claims
exact text as granted — not AI-modified1 . A crystalline MWW-type titanosilicate catalyst for producing an oxidized compound, which is usable in producing an oxidized compound by an oxidation reaction of a compound having a carbon-carbon double bond and at least one other functional group wherein the carbon-carbon double bond of the compound is oxidized by using a peroxide as an oxidizing agent; the catalyst having an MWW structure and being represented by the following composition formula (1):
xTiO 2 .(1-x)SiO 2 Composition formula (1)
wherein x is a number of 0.0001 to 0.2:
2 . A crystalline MWW-type titanosilicate catalyst for providing an oxidized compound according to claim 1 , wherein x is a number of 0.005 to 0.2.
3 . A crystalline MWW-type titanosilicate catalyst for producing an oxidized compound, which is usable in producing an oxidized compound by an oxidation reaction of a compound having a carbon-carbon double bond and at least one other functional group wherein the carbon-carbon double bond of the compound is oxidized by using a peroxide as an oxidizing agent; the catalyst having an MWW structure and being represented by the following composition formula (2):
xTiO 2 .yM 2 O 3 .(1-x-2y)SiO 2 Composition formula (2)
wherein M represents at least one element selected from the group consisting of aluminum, boron, chromium, gallium and iron, x is a number of 0.0001 to 0.2 and y is a number of 0.0001 to 0.1.
4 . A crystalline MWW-type titanosilicate catalyst for providing an oxidized compound according to claim 3 , wherein M in the composition formula (2) is boron.
5 . A crystalline MWW-type titanosilicate catalyst for providing an oxidized compound according to claim 3 , wherein x is a number from 0.005 to 0.2.
6 . A crystalline MWW-type titanosilicate catalyst for providing an oxidized compound according to claim 3 , wherein y is a number from 0.0001 to 0.05.
7 . A process for producing a crystalline MWW-type titanosilicate catalyst for providing an oxidized compound according to claim 1 , said production process comprising:
a first step of heating a mixture comprising a template compound, a titanium-containing compound, a boron-containing compound, a silicon-containing compound and water, to thereby obtain a precursor; and a second step of calcining the precursor obtained in the first step, to thereby obtain a crystalline titanosilicate.
8 . A process for producing a crystalline MWW-type titanosilicate catalyst for providing an oxidized compound according to claim 7 , wherein the template compound is a nitrogen-containing compound.
9 . A process for producing a crystalline MWW-type titanosilicate catalyst for providing an oxidized compound according to claim 8 , wherein the nitrogen-containing compound is at least one compound selected from the group consisting of piperidine, hexamethyleneimine and a mixture thereof.
10 . A process for producing a crystalline MWW-type titanosilicate catalyst for providing an oxidized compound according to claim 7 , wherein the titanium-containing compound is at least one compound selected from the group consisting of titanium oxide, titanium halide and tetraalkyl orthotitanates.
11 . A process for producing a crystalline MWW-type titanosilicate catalyst for providing an oxidized compound according to claim 7 , wherein the boron-containing compound is at least one compound selected from the group consisting of boric acid, boric acid salt, boron oxide, boron halide and trialkylborons.
12 . A process for producing a crystalline MWW-type titanosilicate catalyst for providing an oxidized compound according to claim 7 , wherein the silicon-containing compound is at least one compound selected from the group consisting of silicic acid, silicic acid salt, silicon oxide, silicon halide, fumed silicas, tetraalkylorthosilicates and colloidal silica.
13 . A process for producing a crystalline MWW-type titanosilicate catalyst for providing an oxidized compound according to claim 7 , wherein the ratio between titanium and silicon in the mixture to be used in the first step is 0.001 to 0.3:1 (titanium:silicon) in terms of the molar ratio therebetween.
14 . A process for producing a crystalline MWW-type titanosilicate catalyst for providing an oxidized compound according to claim 7 , wherein the ratio between boron and silicon in the mixture to be used in the first step is 0.3 to 10:1 (boron:silicon) in terms of the molar ratio therebetween.
15 . A process for producing a crystalline MWW-type titanosilicate catalyst for providing an oxidized compound according to claim 7 , wherein the ratio between water and silicon in the mixture to be used in the first step is 5 to 200:1 (water:silicon) in terms of the molar ratio therebetween.
16 . A process for producing a crystalline MWW-type titanosilicate catalyst for providing an oxidized compound according to claim 7 , wherein the ratio between the template compound and silicon in the mixture to be used in the first step is 0.1 to 5:1 (template compound:silicon) in terms of the molar ratio therebetween.
17 . A process for producing a crystalline MWW-type titanosilicate catalyst for providing an oxidized compound according to claim 7 , wherein the heating temperature in the first step is in the range from 110 to 200° C.
18 . A process for producing a crystalline MWW-type titanosilicate catalyst for providing an oxidized compound according to claim 7 , wherein the calcining temperature in the second step is in the range from 200 to 700° C.
19 . A process for producing a crystalline MWW-type titanosilicate catalyst for providing an oxidized compound according to claim 7 , wherein the precursor obtained in the first step is contacted with an acid, and thereafter the second step is performed.Join the waitlist — get patent alerts
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