Chloride absorbent
A technology of adsorbent and hydrogen chloride, which is applied in other chemical processes, chemical instruments and methods, and separation of dispersed particles, etc., can solve the problems of limited application fields and poor water vapor resistance, and achieve good purification, good water resistance, and mechanical high intensity effect
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Embodiment 1
[0034] The adsorbent of the present embodiment uses kaolin 27% (weight, the same below), sodium bicarbonate 10%, calcium hydroxide 35%, diatomaceous earth 10%, zinc oxide 3%, manganese oxide 3%, titanium oxide 3%, 7% white clay and 2% carboxymethyl cellulose are used as raw materials, which are formed by kneading, mixing, extruding, and roasting at a temperature not exceeding 700°C.
[0035] Adsorption (dechlorination) conditions are: gas inlet hydrogen chloride concentration 1000-1500ppm, reaction space velocity 1500-2000hr -1 , Dechlorination temperature 100 ℃. The dechlorination agent can reduce the hydrogen chloride content of the outlet gas to below 0.5ppm, and the penetration chlorine capacity is 10%.
[0036] The concentration of hydrogen chloride in the import and export gas is detected by the silver nitrate volumetric method, and the chlorine capacity of the solid dechlorination agent is analyzed according to the determination method of chlorine in coal.
Embodiment 2
[0038] The raw materials for preparing the adsorbent in this example are: 20% of sepiolite, 10% of alkalized diatomite, 5% of clay, 5% of sodium bicarbonate, 30% of calcium carbonate, 10% of magnesium oxide, and 5% of manganese oxide , iron oxide 3%, chromium oxide 5%, ammonium bicarbonate 3%, carboxymethyl fiber 4%. After being ground and extruded, it is baked at a temperature lower than 700°C.
[0039] The adsorption (dechlorination) conditions are: the hydrogen chloride content of the gas inlet is 1500-1800ppm, and the reaction space velocity is 1500-2000hr -1 , The dechlorination temperature is 200°C. The concentration of hydrogen chloride at the gas outlet is less than 0.5ppm, and the breakthrough chlorine capacity is 15.3%.
[0040] The analysis detection method of hydrogen chloride concentration and chlorine volume is the same as embodiment 1.
Embodiment 3
[0042] The composition of raw materials in this example: 20% of alkalized kaolin, 15% of diatomite, 20% of calcium carbonate, 20% of calcium hydroxide, 5% of sodium bicarbonate, 5% of iron oxide, 3% of copper oxide, and 5% of magnesium oxide. %, carboxymethyl cellulose 4% and ammonium bicarbonate 3%. The calcining temperature after extruding is lower than 700°C.
[0043] The adsorption (dechlorination) conditions are: the hydrogen chloride content of the gas inlet is 2000-2300ppm, and the reaction space velocity is 2500hr -1 The dechlorination temperature is 300°C, the concentration of hydrogen chloride at the gas outlet is less than 0.5ppm, and the breakthrough chlorine capacity is 28.4%.
[0044] The analysis detection method of hydrogen chloride concentration and chlorine volume is the same as embodiment 1.
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