A device for continuously removing thermally stable salts in alkanolamine desulfurization solution using double-membrane stack-magnetoelectric dialysis
A technology of desulfurization solution and thermal stability, applied in electrodialysis, membrane technology, semi-permeable membrane separation, etc., can solve the problem of high energy consumption and material consumption pollutant treatment, high viscosity and particle size requirements, and membrane acid and alkali resistance. High requirements for problems, to achieve the effect of enhanced stability and reliability, high current efficiency, low maintenance and operating costs
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Embodiment 1
[0020] Such as figure 1 As shown in the figure, C is the positive membrane, A is the negative mold, B is the bipolar membrane, H is the magnetic field vector, I is the first membrane stack, and II is the second membrane stack. The first membrane stack and the second membrane stack in this embodiment are both one-stage and one-stage models. There are ten sets of membranes in each membrane stack. The magnetoelectric dialysis space is all non-loop type. The size of the membrane tank is 100mm×300mm, in which the effective ion The selective membrane area is 65mm×210mm. The anodes of the first and second membrane stacks are titanium mesh coated with ruthenium and iridium, and the cathodes are stainless steel. The membrane arrangement between the cathode and anode of the first membrane stack is an alternating arrangement of positive and negative membranes, that is, CCACA...CAC mode, and the adjacent cathode and anode are positive membranes; the second membrane stack is one-stage one...
Embodiment 2
[0022] In this embodiment, the current density of the DC electric field between the anode and the cathode of the first membrane stack and the second membrane stack is 100mA / cm 2 , the electromagnetic field strength is 1.3T, the flow rate of the alcohol amine desulfurization solution is 1.15cm / s, the water flow rate is 1.16cm / s, the HSS content in the alcohol amine desulfurization solution is 6.34w%, and the alcohol amine content is 18.54w%. The content of HSS in the desulfurization solution is 0.54w%, the removal rate of thermally stable salt is 91.48%, the content of alcohol amine is 23.18w%, the loss rate of alcohol amine is 0.37w%, and the current efficiency is 85%. Other implementations are the same as in Example 1.
Embodiment 3
[0024] In this embodiment, the current density of the DC electric field between the anode and the cathode of the first membrane stack and the second membrane stack is 120mA / cm 2 , the electromagnetic field strength is 1.5T, the flow rate of the alcohol amine desulfurization solution is 1.05cm / s, the water flow rate is 1.06cm / s, the HSS content in the alcohol amine desulfurization solution is 7.23w%, and the alcohol amine content is 16.76w%. The content of HSS in the desulfurization solution is 0.44w%, the removal rate of thermally stable salt is 93.91%, the content of alcohol amine is 23.06w%, the loss rate of alcohol amine is 0.46w%, and the current efficiency is 86%. Other implementations are the same as in Example 1.
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