| CPC B01D 53/75 (2013.01) [B01D 53/0423 (2013.01); B01D 53/48 (2013.01); B01D 53/685 (2013.01); B01D 53/82 (2013.01); B01D 2251/404 (2013.01); B01D 2251/602 (2013.01); B01D 2253/102 (2013.01); B01D 2253/104 (2013.01); B01D 2253/3425 (2013.01); B01D 2257/2025 (2013.01); B01D 2257/30 (2013.01); B01D 2257/408 (2013.01); B01D 2258/025 (2013.01)] | 19 Claims |

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1. A hydrolysis reaction device for dechlorination and decyanation of blast furnace gas, wherein the hydrolysis reaction device comprises a cylinder body, wherein a top of the cylinder body is provided with an air inlet channel, and a bottom of the cylinder body is provided with an air outlet channel, and functional zones are arranged in the cylinder body; the functional zones are sequentially an air inlet zone, a first protective agent zone, a first transition zone, a second protective agent zone, a second transition zone, a hydrolysis zone and an air outlet zone along a gas flow direction, and adjacent functional zones are communicated; and feed holes and discharge holes are uniformly arranged on an outer side surface of the cylinder body;
wherein the first protective agent zone is filled with a dechlorination agent; the dechlorination agent is a composite metal oxide dechlorination agent; the composite metal oxide dechlorination agent is a calcium oxide-zinc oxide composite dechlorination agent or an aluminum oxide-copper oxide composite dechlorination agent; and the dechlorination agent is any one or a combination of two or more of spherical, cylindrical or honeycomb;
wherein the second protective agent zone is filled with adsorbent; the adsorbent is any one or a combination of two of activated carbon and alumina; and the adsorbent is any one or a combination of two or more of spherical, cylindrical or honeycomb;
wherein the hydrolysis zone is filled with a hydrolyzing agent; the hydrolyzing agent is any one or a combination of two of alumina and zinc oxide; and the hydrolyzing agent is any one or a combination of two or more of spherical, cylindrical or honeycomb; and
wherein a diameter ratio of the first protective agent zone, the second protective agent zone and the hydrolysis zone is (0.65-0.85):1:1, a height ratio of the first protective agent zone, the second protective agent zone and the hydrolysis zone is (0.55-0.75):(0.65-1):1, a volume space velocity of the first protective agent zone is 1200-3600 h−1, a volume space velocity of the second protective agent zone is 870-3000 h−1, and a volume space velocity of the hydrolysis zone is 550-2500 h−1.
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