A method for purifying organic amines
An organic amine and ion exchange technology, which is applied in chemical instruments and methods, separation methods, adsorption water/sewage treatment, etc., can solve the problems of difficult engineering, incomplete ion exchange purification, high energy consumption of distillation technology, etc., to achieve Strong pertinence, reduced operating costs, and strong flexibility
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[0023] According to a preferred embodiment of the present invention, the method for purifying organic amines further includes: when at least one of the filter adsorption medium, anion exchange medium and cation exchange medium in the bed reaches saturation, regenerate it and then use it again. The regeneration method can be a conventional choice in the art, for example, can be selected from at least one of thermal regeneration method, washing method and ion exchange method. Wherein, when the regeneration method is a thermal regeneration method, the regeneration conditions generally include: the regeneration temperature can be 50-600°C, preferably 150-300°C; the regeneration medium can be hot air, hot nitrogen, At least one of hot oxygen, hot acid gas and hot water vapor; the volumetric space velocity of the regeneration medium can be 0.05-15h -1 , preferably 0.1-5h -1 . When the regeneration method is washing and / or ion exchange, the regeneration conditions generally includ...
Embodiment 1
[0027] This example is used to illustrate the method for purifying organic amines provided by the present invention.
[0028] The composition of organic amine solution to be purified: N-methyldiethanolamine content 35% by weight, K + Content 0.37% by weight, Na + Content 0.59% by weight, Cl - Content 0.7 wt%, SO 4 2- Content 0.49% by weight, TEA + (tetraethylammonium cation) content 0.256% by weight, CH 3 COO - Content 0.26% by weight, HCOO - The content is 0.12% by weight, and the rest is water.
[0029] The steps of purifying the organic amine solution are as follows:
[0030] (1) Fill 300ml of styrene-based strongly basic anion-exchange resin (model 201×7, mass total exchange capacity of 3.6mol / kg) into a resin column whose height-to-diameter ratio is 3, called column 1;
[0031] (2) 500ml HY molecular sieve pellets (containing HY molecular sieve 60% by weight, containing kaolin 40% by weight, wherein, HY molecular sieve is a cation exchange medium, and kaolin is a...
Embodiment 2
[0037] This example is used to illustrate the method for purifying organic amines provided by the present invention.
[0038] The composition of the organic amine solution to be purified is as in Example 1.
[0039] The steps of purifying the organic amine solution are as follows:
[0040] (1) Fill 300ml of styrene-based strongly basic anion-exchange resin (model 201×7, mass total exchange capacity of 3.6mol / kg) into a resin column whose height-to-diameter ratio is 3, called column 1;
[0041] (2) Fill 500ml of styrene-based strongly acidic cation exchange resin (model 001×7, with a total mass exchange capacity of 4.6mol / kg) in a resin column with a height-to-diameter ratio of 3, called column 2;
[0042] (3) Take 700ml of the above-mentioned organic amine solution to be purified at a volume space velocity of 1.2h -1 The flow rate continuously flows through column 1 and column 2, and the temperature of both column 1 and column 2 is controlled at 40°C for processing.
[0043...
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