Rapid screening method of industrial carbon dioxide trapping agent
A carbon dioxide and screening method technology, applied in chemical instruments and methods, separation methods, dispersed particle separation, etc., can solve the problems of not being able to judge the overall performance of carbon dioxide, consuming a lot of time and materials, and high cost, saving time and materials. consumption, reliable results and low operating costs
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Embodiment 1
[0029] The schematic diagram of the rapid screening experiment of this embodiment is as follows: figure 1 As shown, the specific screening system is monoethanolamine (MEA), diethylaminoethanol (DEEA), N-methyldiethanol (MDEA), 2-amino-2-methyl-1-propanol with a mass fraction of 30%. The five amine solutions of alcohol (AMP) and diethanolamine (DEA), the screening steps are:
[0030] (1) Solvent pretreatment: Load the newly configured 300ml amine solution into a 500ml reactor, and put the reactor in a constant temperature water bath to heat and stabilize to 40°C, keep the liquid phase stirring speed at 1400r / min, The flow rate of carbon dioxide gas is 0.2L / min. The absorption reaction is stopped when the amine solution is half-saturated, and the exhaust gas flow is basically constant at this time. Then put the reactor containing the above-mentioned treated solution into a constant temperature water bath heated and stabilized to 80°C. When the temperature of the solution rises to...
Embodiment 2
[0037] The screened system is MEA and DEEA aqueous solutions with a total concentration of 5mol / L, and the molar ratios are 4:1, 2:3, 2.5:2.5, 3:2, and 1:4, and other screening conditions and steps are as in the example 1. The solution loads after pretreatment were 0.300, 0.251,0.203, 0.161 and 0.087 (mol / mol), respectively.
[0038] The load and circulation capacity of the lean-rich liquid obtained by the absorption and desorption of the lean liquid are shown in Table 2. The circulation capacity values of the five solvents are shown in Table 2. The relative order of circulation capacity is 2.5:2.5> 3:2> 2:3> 1:4> 4:1. The MEA and DEEA mixed amine solution with a total concentration of 5mol / L and a molar ratio of 2.5:2.5 was screened to have the highest carbon capture efficiency.
[0039] Table 2 shows the load and circulation capacity of the rich and poor solution of MEA and DEEA mixed amine solutions with different molar ratios of 5 mol / L.
[0040] Table 2
[0041]
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