Method for preparing low-mercury catalyst by employing high-iodine-value active carbon
A technology for preparing activated carbon and low mercury catalyst, applied in the field of fine chemistry, can solve the problems of short service life of catalyst, low catalytic activity, consumption of resources, etc., and achieve the effect of improving catalytic efficiency, high catalytic activity and long service life
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Embodiment 1
[0025] Embodiment 1 A kind of method adopting high iodine value activated carbon to prepare low mercury catalyst
[0026] Step 1 Preparation of Activated Carbon
[0027] (1) Selection of raw materials
[0028] The selected raw material is coconut shell, containing 0.61% ash, 36.51% lignin, 53.06% cellulose, and 20.54% pentosan in cellulose.
[0029] (2) Carbonization
[0030] Grind the coconut shell, pass through a 100-mesh sieve, and carry out carbonization under the protection of N2 flow rate of 20ml / mim. Hours, get carbonized material.
[0031] (3) Once activated
[0032] The coconut shell powder after carbonization is impregnated with acid, and described acid comprises: 60% phosphoric acid, citric acid, oxalic acid, and the mass ratio is 4:3:1, and the mass ratio of acid and coconut shell powder charring is 2:1 , soaked for 3 hours, washed with water, and dried.
[0033] (4) Secondary activation
[0034] The coconut shell powder after one activation is placed in...
Embodiment 2
[0055] Embodiment 2 above-mentioned catalyst is used for synthetic reaction of vinyl chloride
[0056] In the reaction that the catalyst of the present invention is used to prepare vinyl chloride by acetylene hydrochlorination, the molar ratio of the reaction feed gas is C 2 h 2 / HCl=1 / 1.18, acetylene space velocity is 69h -1 , the reaction temperature is 120°C, and the hydrogen chloride activation time is 30 minutes.
[0057] The reaction tail gas was analyzed by chromatography, and the conversion rate of acetylene was 99.95%, the yield of vinyl chloride was 96.3%, and the catalytic efficiency was improved by 4.8m 3 / h; the unit consumption of the catalyst is low, the unit consumption of the catalyst is 0.00080g / ml vinyl chloride, the catalyst of the present invention has a long service life, reaching 8800 hours, and the consumption of the catalyst is reduced by 10%.
[0058] Unless otherwise specified, the percentages used in the present invention are all weight percent...
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