Method for fixing carbon dioxide in water-gas shift process through real-time carbonization of silicate
A water-gas shift and carbon dioxide technology, which is applied in the preparation of carbonate/acid carbonate, chemical instruments and methods, inorganic chemistry, etc. The effect of simple process and wide source of raw materials
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Embodiment 1
[0024] Using natural anorthite as CO 2 CO during water-gas shift reaction with fixative 2 removal and H 2 Preparation, using the following steps:
[0025] 1) The natural anorthite fixative and catalyst are mixed and filled into the reactor with built-in fixed bed;
[0026] 2) Pour the mixed gas with a CO concentration of 34.7% and a water-to-gas ratio of 0.6 into the reactor, so that the mixed gas has a temperature of 538 °C, a pressure of 12.5 MPa, and a shift gas velocity of 2.6 m / s. react;
[0027] 3) After the reaction, the adsorbed anorthite and the catalyst are sieved and separated, and CO 2 The fixative is processed later, and the catalyst is reused.
[0028] CO treated by this method 2 Emission concentration ≤5%, the prepared H 2 The concentration reaches 96%.
Embodiment 2
[0030] Using natural olivine as CO 2 CO during water-gas shift reaction with fixative 2 removal and H 2 Preparation, using the following steps:
[0031] 1) The natural olivine fixative and catalyst are mixed and filled into the reactor with built-in fluidized bed;
[0032] 2) Pour the mixed gas with a CO concentration of 18.2% and a water-to-gas ratio of 0.4 into the reactor, so that the mixed gas has a temperature of 477 °C, a pressure of 8.90 MPa, and a shift gas velocity of 3.5 m / s. react;
[0033] 3) After the reaction, the saturated olivine and the catalyst are separated by gravity separation, CO 2 The fixative is processed later, and the catalyst is reused.
[0034] CO treated by this method 2 Emission concentration ≤4%, the prepared H 2 The concentration reaches 92%.
Embodiment 3
[0036] Using natural kaolinite as CO 2 CO during water-gas shift reaction with fixative 2 removal and H 2 Preparation, using the following steps:
[0037] 1) The natural kaolinite fixative and catalyst are mixed and filled into the reactor with built-in mixed bed;
[0038]2) Pour the mixed gas with a CO concentration of 37.3% and a water-to-gas ratio of 0.7 into the reactor, so that the mixed gas has a temperature of 590 °C, a pressure of 5.5 MPa, and a shift gas velocity of 4.1 m / s. react;
[0039] 3) After the reaction, the adsorbed saturated kaolinite and the catalyst are separated by magnetic separation, CO 2 The fixative is processed later, and the catalyst is reused.
[0040] CO treated by this method 2 Emission concentration ≤3%, the prepared H 2 The concentration reaches 95%.
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