System and method for reducing gas purification and tail gas treatment of gas base shaft furnace system
A technology for tail gas treatment and gas-based shaft furnace, which is applied in chemical instruments and methods, separation methods, granular/powder fuel gasification, etc., to achieve the effects of ensuring continuity, reducing consumption and avoiding costs
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Embodiment 1
[0033] In this embodiment, the pulverized coal pyrolysis method is used to use oxygen, pulverized coal and water vapor as raw materials. The specific process steps as shown in the figure include:
[0034] (1) Preparation of crude reducing gas
[0035] Raw materials are prepared in crude reducing gas preparation unit 1, the temperature is 1000°C, the reaction pressure is 0.8MPa, and the carbon-hydrogen ratio of the product gas is adjusted by adjusting the amount of water vapor at 200°C. The main components of the raw reducing gas produced by the unit include CO 2 , CO, H 2 O, H 2 and H 2 S, where CO 2 The content is 3%, the hydrogen sulfide content is 5g / m 3 .
[0036] (2) Purification of crude reducing gas
[0037] The crude reducing gas from the crude reducing gas preparation unit 1 enters the crude reducing gas desulfurization and decarburization unit 2 . Firstly, it enters the rough reducing gas water washing tower 6, and the gas is in countercurrent contact with th...
Embodiment 2
[0050] Adopt the method of partial oxidation of natural gas, natural gas (hydrogen sulfide content is 20g / m 3 ), steam and oxygen prepare crude reducing gas in crude reducing gas preparation unit 1, wherein the hydrogen sulfide content in natural gas is 20g / m 3 , the reaction temperature is 900°C, the reaction pressure is 0.8MPa, and the carbon-hydrogen ratio of the product gas is adjusted by adjusting the amount of water vapor at 200°C. The main components of the raw reducing gas produced by the unit include CO 2 , CO, H 2 O, H 2 、H 2 S and SO 2 , where CO 2 5%, hydrogen sulfide content is 8g / m 3 , sulfur dioxide is 100ppm, and its operation condition is identical with embodiment 1, and the tail gas composition after tail gas treatment and catalyst regeneration unit 4 processing is: CO 2 Content 99.9%, SO 2 Not detected, H 2 S was not detected.
[0051] Compared with the prior art, the present invention has the following advantages and progress:
[0052] (1) The sy...
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