Improved N-methyldiethanolamine decarbonizing solution
A methyldiethanolamine decarburization solution and methyldiethanolamine technology are applied in air quality improvement, dispersed particle separation, chemical instruments and methods, etc., can solve problems such as insufficient comprehensive decarburization capacity, and achieve low regeneration energy consumption, The effect of large absorption capacity and high purification degree
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Embodiment 1
[0025] The performance of the MDEA decarburization fluid with morpholine (MAL) and piperazine (PZ) or morpholine (MAL) and diethanolamine (DEA) as activators was comprehensively evaluated by using the laboratory simulation device and conditions described above. The evaluation results are shown in Table 3 and Table 4:
[0026] P
[0027] It can be seen from Table 3 that adding MAL to the PZ-activated MDEA solution can significantly improve the decarburization performance of the solution. For 0.2MPa: add MAL to W MAL / W MDEA+PZ is 0.15 (ie W MAL / W MDEA =0.165) are effective, and the optimum content is W MAL / W MDEA+PZ is 0.10 (ie W MAL / W MDEA =0.11); for 0.3MPa: add MAL to W MAL / W MDEA+PZ is 0.12 (ie W MAL / W MDEA =0.132) are all effective, and the optimum content is W MAL / W MDEA+PZ is 0.10 (ie W MAL / W MDEA = 0.11).
[0028] P
[0029] It can be seen from Table 4 that adding MAL to DEA-activated MDEA significantly improves the decarburiza...
Embodiment 2
[0031] A certain annual production of 40,000 tons of synthetic ammonia decarburization device selects the said MDEA decarburization solution of the present invention (the concentration of MDEA is 36% by weight; the activator is morpholine and diethanolamine; the weight ratio of morpholine and MDEA is 0.06; diethanolamine and The weight ratio of MDEA is 0.2) for decarburization. After being put into operation, the production system is stable, and the absorption capacity is large, and the solution absorbs 20-22Nm of carbon dioxide per cubic meter 3 ;Low consumption: MDEA consumes 0.097 kg / ton of ammonia; diethanolamine consumes 0.019 kg / ton of ammonia; morpholine consumes 0.013 kg / ton of ammonia; steam consumes less than 1.2 tons / ton of ammonia.
Embodiment 3
[0033]The existing MDEA decarburization solution was used in the syngas decarbonization process of a formic acid branch plant, but it could only reach 60% of the design load after the start-up, and there were many degradation products in the solution. After using the MDEA decarburization solution of the present invention (the concentration of MDEA is 30% by weight; the activator is morpholine and piperazine, and the weight ratio of morpholine, piperazine and MDEA is 0.1: 0.1: 1), the result of use shows : MDEA has no obvious degradation, the content of activator is stable, the content of carbon dioxide after purification of syngas is less than 0.1%, and the production load reaches the design capacity.
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