A kind of preparation method of solid-phase mercury-free catalyst for vinyl chloride synthesis
A mercury catalyst and vinyl chloride technology, applied in the field of fine chemistry, can solve the problems of high loss rate, low catalytic activity, low selectivity of vinyl chloride, etc., and achieve the effect of low loss rate
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Embodiment 1
[0025] Example 1 A preparation method for a solid-phase mercury-free catalyst for the synthesis of vinyl chloride
[0026] Step 1, preparation of activated carbon
[0027] (1) Raw material pretreatment
[0028] The selected raw materials are fly ash recovered from dust removal in power plants. The fly ash contains 35.6% ash, 28.2% silicon dioxide, 3.6% calcium oxide, 1.4% magnesium oxide, 12.7% aluminum oxide, and 1.58% titanium dioxide. Manganese dioxide 5.3%.
[0029] The above-mentioned fly ash is ground to a particle size of 1.6-2.0 μm, and then mixed with wood vinegar and coal tar. The mixing mass ratio of fly ash, wood vinegar and coal tar is 1:1:1.2; the coal tar Bitumen content is 48-52%.
[0030] Heat the mixture of fly ash, wood vinegar, and coal tar to 87-89°C, add silicon dioxide, sodium thiocyanate, and tapioca flour, and stir evenly to obtain a mixture;
[0031] The addition amount of described silicon dioxide, sodium thiocyanate and cassava flour is respecti...
Embodiment 2
[0046] Embodiment 2 above-mentioned catalyst is used for synthetic reaction of vinyl chloride
[0047] (1) Loading catalyst
[0048] Before loading the catalyst, check that there are no leaks inside and outside the reactor, and that the inner wall of the tubes is clean, dry, and free of debris; after opening the package, the catalyst of the present invention is immediately loaded into the tubes of the reactor, and the catalyst should be loaded within 0.5h Done, beware of moisture.
[0049] (2) Pretreatment
[0050] Pass in dry HCl at 90-100°C, control the speed at 30-32m 3 / h, continuous 1h, release acid from the bottom of the reactor.
[0051] (3) Synthesis of vinyl chloride reaction
[0052]The molar ratio of acetylene and hydrogen chloride is controlled at 1:1.1~1:1.3 (100% purity), and the mixed gas with a preheated temperature above 90°C is passed into the reactor, and the reaction temperature is controlled between 120~125°C; Airspeed 80h -1 , continuous operation 2...
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