Method for preparing o-chlorotoluene
A technology for o-chlorotoluene and dichlorotoluene, applied in the field of catalytic reduction to prepare o-chlorotoluene, can solve problems such as product waste, and achieve the effects of long service life and high conversion rate
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Embodiment 1
[0021] 1. The specific surface area of 25g is greater than 100m 2 / g, silicon carbide cylindrical particles with a diameter of 2-4mm, impregnated and adsorbed with 10ml of aqueous solution containing 5% tetraammonium palladium chloride, dried naturally at 110°C for 5 hours before use.
[0022] 2. Fill 25g of hydrogenation catalyst in a cylindrical reactor with a diameter of 20mm, raise the temperature to 200°C, and keep the hydrogen atmosphere after passing hydrogen for one hour; keep the reaction pressure at 0.05MPa, and continuously add 2,3-dihydrogen at 0.3ml / h The mixture of chlorotoluene, 2,4-dichlorotoluene and 2,5-dichlorotoluene was sampled after reacting for 1 hour and analyzed by gas chromatography.
[0023] The result is as follows:
[0024]
Embodiment 2
[0026] The mixture of 2,3-dichlorotoluene, 2,4-dichlorotoluene and 2,5-dichlorotoluene in Example 1 was replaced by 2,5-dichlorotoluene, and the others were the same as in Example 1.
[0027] The result is as follows:
[0028]
Embodiment 3
[0030] The silicon carbide-supported palladium catalyst in Example 1 was replaced by an activated carbon-supported palladium catalyst, and the others were the same as in Example 1.
[0031] The result is as follows:
[0032]
[0033] It can be seen that the activated carbon-supported palladium catalyst has a catalytic selectivity effect inferior to that of the silicon carbide-supported palladium catalyst, and industrial production preferably selects the activated carbon-supported palladium catalyst provided by the invention.
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