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Method for recycling organic waste in BDP wastewater

A technology for organic waste and wastewater, applied in water pollutants, chemical instruments and methods, water/sewage treatment, etc., can solve problems such as cost reduction and difficult BDP wastewater treatment, and achieve the effect of reducing treatment costs and treatment costs.

Active Publication Date: 2021-04-06
ZHEJIANG WANSHENG
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] For the difficult problem of existing BDP wastewater treatment, the object of the present invention is to provide a method for recycling organic waste in BDP wastewater, and the method of the present invention can reclaim wastewater 90% of the organic matter in the water, which reduces the cost of subsequent wastewater treatment

Method used

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  • Method for recycling organic waste in BDP wastewater
  • Method for recycling organic waste in BDP wastewater
  • Method for recycling organic waste in BDP wastewater

Examples

Experimental program
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Effect test

Embodiment 1

[0037] 1) Add 1200g of BDP wastewater into a four-necked flask with stirring, start stirring, add 240g of hydrochloric acid dropwise, adjust to pH≤1, stir for 30min, transfer to a separatory funnel for layering, and obtain 120g of oil phase and 1320g of water phase , the COD of the water phase is about 30,000 mg / L, and the COD of the oil phase is in the range of 1.5-1.9 million mg / L;

[0038] 2) Transfer 120 g of the oil phase obtained in step 1) to a four-necked flask, and raise the temperature to 110° C. to remove water and phenol under a vacuum degree of -0.98 MPa. The distillation time is 2 hours; after the distillation is completed, add 10 g of PCl 5 And insulate and react for 3 hours at a temperature of about 80°C;

[0039] 3) Step 2) After the heat preservation reaction is completed, add 0.11g of magnesium chloride, after heating up to 90°C, add 10g of bisphenol A, continue to heat up to 95°C, and keep warm for 2h;

[0040] 4) Step 3) After the heat preservation is com...

Embodiment 2

[0046] 1) Add 1200g of BDP wastewater into a four-neck flask with stirring, start stirring, add 240g of hydrochloric acid dropwise, adjust to pH≤1, stir for 30min, transfer to a separatory funnel for layering, and obtain 120g of oil phase and 1320g of water phase , the COD of the water phase is about 30,000 mg / L, and the COD of the oil phase is in the range of 1.5-1.9 million mg / L;

[0047] 2) Transfer 120 g of the oil phase obtained in step 1) to a four-necked flask, and raise the temperature to 110° C. to remove water and phenol under a vacuum degree of -0.98 MPa. The distillation time is 2 hours; after the distillation is completed, add 10 g of PCl 5 And insulate and react for 3 hours at a temperature of about 80°C;

[0048] 3) Step 2) After the heat preservation reaction is completed, add 0.11g of magnesium chloride, after heating up to 90°C, add 10g of bisphenol A, continue to heat up to 95°C, and keep warm for 4h;

[0049] 4) Step 3) After the heat preservation is compl...

Embodiment 3

[0051] The implementation method of embodiment 3 is the same as embodiment 2, except that "the quality of phenol added dropwise in step 4) in embodiment 3 is 23g", and all the other experimental conditions are identical with embodiment 2. After the final reaction in Example 3, 88g of the crude product was obtained, and 83g of the BDP product was obtained after washing. The BDP product was tested, and the TPP content in the product was measured to be 2.98%, monomer 86.6%, dimer 6.6%, trimer 0.948%, tetramer 0.114%, phenol 0.018%, and the rest were unknown impurities.

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Abstract

The invention discloses a method for recycling organic waste in BDP wastewater. The method comprises the following steps: 1) acidifying BDP wastewater, and layering to obtain an oil phase and a water phase; 2) after liquid separation, carrying out reduced pressure distillation on an oil phase to remove water and phenol; 3) removing water and an oil phase of phenol, and adding PCl5 for acylating chlorination reaction to generate phosphoryl chloride; 4) adding a catalyst and bisphenol A to react, so that POCl3 generated in the step 3) further reacts with bisphenol A; and 5) dropwise adding phenol to continue the reaction to obtain a BDP crude product after the reaction is finished. In the method provided by the invention, the COD value in the water phase after layering is greatly reduced, and then a conventional wastewater treatment method is adopted, so that the treatment cost is greatly reduced. In the layered oil phase, residual moisture and phenol are removed through reduced pressure distillation, the distilled phenol can be directly used as a raw material for producing BDP after being refined, and distillation residues react to synthesize a BDP product, so that the treatment cost of the wastewater is greatly reduced.

Description

technical field [0001] The invention relates to a method for recycling organic waste in BDP wastewater. Background technique [0002] Bisphenol A bis(diphenyl phosphate), referred to as BDP, is a new type of phosphorus flame retardant. BDP is usually synthesized by a two-step method. First, under the action of the catalyst magnesium chloride, phosphorus oxychloride and bisphenol A are polycondensed into an intermediate product bisphenol A tetrachlorobisphosphate, and then the intermediate product bisphenol A tetrachlorobisphosphate is combined with Phenol undergoes esterification reaction to obtain the crude product of bisphenol A bis(diphenyl phosphate), and finally add solvent toluene and methylcyclohexane of equal quality to the crude product, and obtain the final High purity product. During the production process, wastewater with high salinity (the main salts are NaOH, NaCl), high toxicity (the main components are phenol and bisphenol A) is produced, and it also contai...

Claims

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Application Information

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IPC IPC(8): C02F9/10C02F101/34
CPCC02F9/00C02F2101/34C02F1/66C02F2209/06C02F1/725C02F1/048
Inventor 李旭锋褚昭宁蒋正国李文武
Owner ZHEJIANG WANSHENG