Isomerization catalyst, method for producing straight-chain olefin, and method for producing compound
A technology for straight-chain olefins and a manufacturing method, which can be used in the fields of isomerization to produce hydrocarbons, carbon compound catalysts, catalysts for physical/chemical processes, etc., can solve the problems of insufficient yield, reduced product purity, and difficulty in use, and achieve good efficiency. , the effect of suppressing catalytic degradation
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[0104] (Example 1)
[0105] 0.3 cc of H-β zeolite catalyst (manufactured by Tosoh Corporation, Si / Al=250 (mol / mol)) was filled in a tubular reactor (tube made of SUS). The inner diameter of the tubular reactor is 14 mm and the total length is 60 cm. Fill the upper and lower parts of the catalyst with glass beads. The average particle size of the glass beads is 1 mm. After connecting this reactor to a circulating reactor, an electric furnace was used to raise the temperature in the reactor to 350°C. The raw material (raw material gas) containing olefin, oxygen / nitrogen mixed gas (oxygen concentration 10%), and water (steam) are supplied to the reactor after the temperature rises. The olefin isomerization reaction is carried out in the above steps.
[0106] In addition, the flow rates of the raw material gas, air, and water (steam) into the reactor are as follows, respectively. In addition, the oxygen concentration in the gas supplied to the reactor was 8.5% by volume, and the w...
Example Embodiment
[0113] (Example 2)
[0114] As the isomerization catalyst, an H-ZSM-5 zeolite catalyst (manufactured by Tosoh Corporation, Si / Al=940 (mol / mol)) was used, and olefin isomerization was performed in the same manner as in Example 1, except that 化反应。 Chemical reaction.
Example Embodiment
[0115] (Example 3)
[0116] As the isomerization catalyst, the SAPO-34 zeolite catalyst prepared in reference to Comparative Example 2 of JP 2012-91997 A was used, and the olefin isomerization reaction was performed in the same manner as in Example 1, except that the SAPO-34 zeolite catalyst was used.
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