Organic amine compound absorbent for removal of carbon dioxide in fire coal flue gas
A coal-fired flue gas and carbon dioxide technology, which is applied in the field of flue gas pollution control, can solve problems such as high costs, which are difficult for enterprises and society to bear
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Embodiment 1
[0039] Take two parts of 15wt% organic amine composite absorbent with monoethanolamine MEA as the main body, wherein the content of monoethanolamine MEA is 8%, AEEA is 1%, PZ is 1%, DETA is 1.5%, AMP is 1.5%, sulfolane 1%, DEA 1%, corrosion inhibitor potassium chromate 0.1%, antioxidant potassium sodium tartrate 0.5%, and the balance is water. The preparation method of the organic amine composite absorbent for removing carbon dioxide in coal-fired flue gas is obtained by mixing the components in the formula ratio. Composite absorbent temperature is 40°C, gas phase CO 2 The partial pressures are 15kPa (Experiment 1 in Table 3), 45kPa (Experiment 2 in Table 3), and will contain CO 2 and N 2 The mixed gas of the mixed gas is passed into two parts of the above-mentioned composite absorbent respectively, and after the gas-liquid two-phase reaches equilibrium, the CO in the composite absorbent 2 The ratio of the moles of organic amines to the sum of the moles of organic amines in...
Embodiment 2
[0043] Take two parts of 15wt% organic amine composite absorbent with monoethanolamine MEA as the main body, wherein the content of monoethanolamine MEA is 8%, AEEA is 1%, PZ is 1%, DETA is 1.5%, AMP is 1.5%, sulfolane 1%, DEA 1%, corrosion inhibitor potassium chromate 0.1%, antioxidant potassium sodium tartrate 0.5%, and the balance is water. The preparation method of the organic amine composite absorbent for removing carbon dioxide in coal-fired flue gas is obtained by mixing the components in the formula ratio. At atmospheric pressure, gaseous CO 2 Partial pressure 15kPa (Experiment 1 in Table 4), 45kPa (Experiment 2 in Table 4), containing CO 2 and N 2 The mixed gas of the mixed gas is input into two parts of the composite absorbent respectively, and reaches saturation at a temperature of 40°C. After the absorption is saturated, the composite absorbent is heated to 112°C to control the CO in the regeneration gas. 2 The partial pressures are 15kPa and 45kPa respectively....
Embodiment 3
[0047] Take two parts of 20wt% organic amine composite absorbent with monoethanolamine (MEA) as the main body, wherein the content of monoethanolamine (MEA) is 8%, AEEA is 1%, MMEA is 1%, AMP is 1%, and PZ is 1%, DETA 1%, sulfolane 2%, DEA 2%, DETA 1%, TETA 1%, TBEE 1%, corrosion inhibitor potassium chromate 0.1%, antioxidant potassium sodium tartrate 0.5%, The balance is water. The preparation method of the organic amine composite absorbent for removing carbon dioxide in coal-fired flue gas is obtained by mixing the components in the formula ratio. The temperature of the composite absorbent is 45°C, under normal pressure, the gas phase CO 2 The partial pressure is 60kPa (Experiment 1 in Table 5), 85kPa (Experiment 2 in Table 5), will contain CO 2 and N 2 The mixed gas of the mixture is passed into two parts of the above-mentioned composite absorbent respectively, and after the gas-liquid two-phase reaches equilibrium, the CO in the solvent is absorbed 2 and the molar rati...
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