A kind of processing method of isatin wastewater

A treatment method and wastewater technology, which is applied in energy wastewater treatment, water/sewage multi-stage treatment, water/sludge/sewage treatment, etc., can solve the problems of ineffective effect, complicated operation, high technical cost, etc., and reduce the difficulty of treatment , The process is simple, the effect of reducing costs

Active Publication Date: 2016-08-24
ZHEJIANG QICAI ECO TECH CO LTD
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  • Application Information

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Problems solved by technology

[0011] The invention discloses an effective, stable and cost-effective treatment method for isatin wastewater, which combines chlorine dioxide oxidation treatment with conventional oxidation treatment, on the one hand solves the problem that the effect of conventional decolorization treatment is not obvious, and on the other hand On the one hand, it solves the problems of high cost and complicated operation of photocatalysis and other technologies, and at the same time achieves the purpose of removing COD, removing chroma, recovering high-quality ammonium salt, saving costs, and utilizing resources

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  • A kind of processing method of isatin wastewater
  • A kind of processing method of isatin wastewater

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Effect test

Embodiment 1

[0041] A certain isatin wastewater is black and red, the COD is about 18080mg / L, and the acidity (in terms of H 2 SO 4 Total) is 37%. Use liquid ammonia to adjust the pH of the wastewater to 5, add 1% ferrous sulfate and 2% hydrogen peroxide (based on the mass of isatin wastewater) in a mass percentage, keep warm at 55°C and stir for 1 hour, adjust the pH of the solution to 8 with ammonia water, and then add Activated carbon with a mass percentage of 0.1% was stirred and adsorbed for 0.5h, and the COD of the filtrate I was filtered to be about 9906mg / L; after the filtrate I was adsorbed by the macroporous resin of the model HYA106, the COD of the column liquid was about 4580mg / L; Pass ClO into the column solution 2 Oxidize for 0.5h, keep ClO in solution 2 The concentration is 1000mg / L (based on the volume of the column liquid), and the pH value is kept at about 8 during the oxidation process to obtain an orange solution. The COD of the solution is about 923mg / L; then add 0....

Embodiment 2

[0060] A certain isatin wastewater is dark red, COD is about 12000mg / L, acidity (in terms of H 2 SO 4 Total) is 32%. Use ammonia water to adjust the pH of the wastewater to 6, based on the mass of isatin wastewater, add 0.5% activated carbon by mass percentage, stir and adsorb for 0.5h, then filter to obtain wine red filtrate I; pass 1000mg / L ClO into filtrate I 2 After oxidizing for 0.5h, an orange solution was obtained, and the COD of the solution was about 4000mg / L; then 0.4% activated carbon was added to stir and adsorb for 0.5h, and filtered to obtain light yellow filtrate II. Distill this filtrate II under reduced pressure to obtain condensed water COD=114mg / L, NH 3 -N=43.2mg / L, the quality of the ammonium sulfate obtained by concentration reaches the GB535-1995 standard, and the dry nitrogen content is 20.61%.

Embodiment 3

[0062] A certain isatin wastewater is orange-red, with a COD of about 8000mg / L, which is strongly acidic. Adjust the pH of the solution to 5 with ammonia water, heat and control the temperature at 50°C, and add FeSO 4 with H 2 o 2 After stirring and reacting for 1 h, flocculate and filter; the resulting filtrate was passed through ClO 2 (ventilation rate is 1000mg / L), react for 30min, the COD of the solution obtained after the reaction is about 3000mg / L; add 0.1% diatomaceous earth to obtain light yellow solution after adsorption. Adjust the pH of the solution to about 5, and distill under reduced pressure to obtain condensed water COD=84mg / L, NH 3 -N=11.2mg / L, the quality of the ammonium sulfate obtained by concentration reaches the GB535-1995 standard, and the dry nitrogen content is 20.90%.

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Abstract

The invention discloses a method for treating isatin wastewater. The method comprises the following steps: adding alkali liquor into the isatin wastewater to regulate the pH value to 5-7, and pre-treating to obtain treating fluid; introducing ClO2 into the treating fluid to carry out an oxidation reaction; treating the treating fluid after the oxidation reaction via an MVR technology or multi-effect evaporation to obtain ammonium sulfate salt, recycling the condensate, and additionally treating the concentrated solution. According to the method for treating isatin wastewater, disclosed by the invention, chlorine dioxide oxidation is combined with conventional treatment to solve the problem of unobvious treatment of conventional decoloration on one hand and solve the problems of high cost and complicated operation of a photocatalysis technology and other technologies on the other hand, and meanwhile, the purposes of removing COD, removing chroma, recycling high-quality ammonium salt, saving the cost and realizing resource utilization are achieved.

Description

technical field [0001] The invention relates to the technical field of industrial wastewater, in particular to a treatment method for isatin wastewater. Background technique [0002] Isatin is an indole derivative, which is often used as a dyeing raw material for medicine, printing and dyeing, and can be used to make vat dyes and drugs. [0003] At present, isatin is mainly synthesized through the following steps: adding aqueous solution of hydroxylamine hydrochloride, aqueous solution of aniline hydrochloride and aqueous solution of chloral to the reaction bottle and mixing, then heating up to about 100°C for reaction to obtain α-oximinoacetanilide (2) The yield is about 80%. Slowly add oxime-acetanilide into concentrated sulfuric acid, react at 60-80°C, deamination and ring closure give isatin (3) with a yield of 75%, and the total yield of the two steps is 60%. [0004] [0005] In the existing process, oxime amine waste water and cyclization waste water are usually ...

Claims

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Application Information

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Patent Type & AuthorityPatents(China)
IPC IPC(8): C02F9/10C01C1/24
CPCY02W10/37
Inventor刘妍陈磊张静吕伏建田李嘉尚官郧
OwnerZHEJIANG QICAI ECO TECH CO LTD