Method for treating waste water generated in production of refined terephthalic acid
A technology for purified terephthalic acid and waste water production, which is applied in the fields of water/sewage multi-stage treatment, extraction water/sewage treatment, adsorption water/sewage treatment, etc., which can solve the problems of inability to meet the requirements for recycling and save money. and cost, wide application scope and low operating cost
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Embodiment 1
[0042] This example is used to illustrate the PTA production wastewater treatment and reuse method provided by the present invention.
[0043]Get 2000 grams of waste water (the composition of the waste water is shown in Table 2 below) of the TA refining stage that is filtered to remove solid impurities and join in the separatory funnel of 5000 milliliters, then will contain 100 grams of trioctylamine, 200 grams of n-octanol and 300 grams of kerosene Add the mixed complexing extractant into the separatory funnel, cover the bottle stopper, and shake it in the shaker for 30 minutes at room temperature, so that the two phases reach the extraction equilibrium, then let it stand, take out the water phase, and carry out COD Cr value determination. The measurement results are shown in Table 3 below.
[0044] Weigh 20 grams of dry macroporous adsorption resin (DM301) and fill it into a glass adsorption column with a diameter of 2.3 cm. The filling height is 11.0 cm. 1000 grams of eff...
Embodiment 2
[0047] This example is used to illustrate the PTA production wastewater treatment and reuse method provided by the present invention.
[0048] Get 2000 gram composition and join the waste water identical with embodiment 1 in the separatory funnel of 5000 milliliters, then will contain the complex extractant of 200 gram tributyl phosphate and 200 gram kerosene in the separatory funnel, cover the bottle stopper , at 40°C, shake in a shaker for 10 minutes to make the two phases reach extraction equilibrium, then stand still, take out the water phase, and carry out COD Cr value determination. The measurement results are shown in Table 3 below.
[0049] Weigh 10 grams of dry macroporous adsorption resin (NKA-2) and place it in a 1000 milliliter conical flask, add 2000 grams of the water sample after the above-mentioned complexation extraction, put the conical flask into a shaker and vibrate for 3 hours, separate Resin and water phase, COD of water samples Cr value determination....
Embodiment 3
[0052] This example is used to illustrate the PTA production wastewater treatment and reuse method provided by the present invention.
[0053] According to the method of embodiment 1, 2000 grams of PTA production wastewater are reused, and the difference is that the complexing extractant is 50 grams of trioctylamine, 50 grams of tri(dodecyl)amine, 300 grams of kerosene and 100 grams of iso Octanol, the amount of cation exchange resin is 4.0 grams. The experimental results are shown in Table 3 or Table 4.
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