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Treatment of waste water in producing isophthalic acid dicarbomethoxy-5-sodium sulphonate and its resource utilization method

A technology for the production of dimethyl isophthalate and waste water, which is applied in chemical instruments and methods, heating water/sewage treatment, adsorption water/sewage treatment, etc., can solve the problem of undiscovered dimethyl isophthalate-5- Sodium sulfonate production waste water treatment and resource recycling report and other issues, to achieve the effect of realizing waste recycling

Inactive Publication Date: 2006-03-22
NANJING UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The result of literature search shows: before the present invention is completed, do not find the report that the dimethyl isophthalate-5-sodium sulfonate production waste water is carried out treatment and resource recycling

Method used

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  • Treatment of waste water in producing isophthalic acid dicarbomethoxy-5-sodium sulphonate and its resource utilization method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0019] Pack 20mL (about 15g, dry weight) of NDA150 resin into an adsorption column (Φ20×250mm) with a heat preservation jacket.

[0020] Take 55mL of yellow dimethyl isophthalate-5-sodium sulfonate production wastewater, distill 5mL and cool to room temperature. The CODcr of the upper column liquid is 116800mg / L, and the content of dimethyl isophthalate-5-sodium sulfonate is 31600mg / L. At room temperature (25°C), the flow rate of 10mL / h passes through the resin column, and the adsorbed water is colorless. The content of dimethyl isophthalate-5-sodium sulfonate and its intermediate products is reduced to 1260mg / L, and the CODcr is reduced to 26400mg / L. After neutralization and aerobic biochemical treatment, the water can reach the national first-class discharge standard .

[0021] The adsorbed NDA150 resin is desorbed and regenerated with 40mL of hot water at a temperature of 85±5°C, and the flow rate is 10mL / h. The resin regenerated by desorption is reused. The desorption r...

Embodiment 2

[0023] Pack 200mL (about 150g, dry weight) of NDA150 resin into an adsorption column (Φ35×500mm) with an insulated jacket.

[0024] Take 600mL of yellow production wastewater, distill 60mL and cool to room temperature. The CODcr of the upper column liquid is 123500mg / L, and at room temperature (25°C) passes through the resin column at a flow rate of 100mL / h, and the adsorbed water is colorless, dimethyl isophthalate-5-sodium sulfonate and its intermediate product The content is reduced to 2160mg / L, and the CODcr is reduced to 38200mg / L. After neutralization and aerobic biochemical treatment, the water can reach the national first-level discharge standard.

[0025] The adsorbed NDA150 resin is desorbed and regenerated with 400mL of hot water at a temperature of 80±1°C, and the flow rate is 100mL / h. The resin regenerated by desorption is reused. The desorption rate of dimethyl isophthalate-5-sodium sulfonate was 95%. After the desorption solution (400mL) is distilled, the 340...

Embodiment 3

[0027] 600mL (about 450g, dry weight) of NDA150 resin was evenly packed in three glass columns (Φ35×500mm) with insulation jacket.

[0028] Take 1700mL light yellow production waste water, distill 200mL and cool to room temperature. The CODcr of the upper column liquid is 139400mg / L. At room temperature (25°C) with a flow rate of 200mL / h, it passes through three series-connected resin columns successively. - The content of sodium 5-sulfonate and its intermediate products is reduced to 440mg / L, and the CODcr is reduced to 10660mg / L. After neutralization and aerobic biochemical treatment, the water can reach the national first-level discharge standard.

[0029] The adsorbed NDA150 resin is desorbed and regenerated with 400mL of hot water at a temperature of 80±1℃ per column, and the flow rate is 100mL / h. The resin regenerated by desorption is reused. The desorption rate of dimethyl isophthalate-5-sodium sulfonate was 95%. The desorption solution (400mL) of each column was dis...

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Abstract

A process for treating and reclaiming the sewage generated by production of dimethyl metanaphthalate-5-sodium sulfonate includes such steps as distilling, adsorbing the dimethyl metanaphthalate-5-sodium sulfonate and its intermediate product by cross-linking polystyrene resin bed, adding alkali for neutralizing, vacuum distillation to obtain clean water, returning the water back to production, cooling the distilled dregs to obtain decahydrated sodium sulfate crystal, desorbing said resin by hot water for regenerating it, and vacuum distilling the desorbed water for recovering dimethyl metanaphthalate-5-sodium sulfate and its intermediate product.

Description

1. Technical field [0001] The invention relates to the treatment of the production waste water discharged in the production process of the excellent anionic surfactant dimethyl isophthalate-5-sodium sulfonate used in polyester dyeing modification, specifically, dimethyl isophthalate Recycling of ester-5-sodium sulfonate and its intermediate products and recycling of sodium sulfate in wastewater. 2. Background technology [0002] Dimethyl isophthalate-5-sodium sulfonate (SIPM) is mainly used as an excellent anionic surfactant for polyester dyeing and modification. Its production generally adopts the "one-pot method", and the process is as follows: After direct sulfonation of isophthalic acid, it is esterified with methanol, and then reacted with alkali to obtain dimethyl isophthalate-5-sodium sulfonate. [0003] [0004] Using the above-mentioned production process, about 7 tons of strong acid wastewater will be produced per ton of product. The wastewater is light yellow,...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F9/04C02F9/02C02F1/04C02F1/28C02F1/66C02F101/34
Inventor 李爱民费正皓钱洪明龙超张根成刘福强高冠道刘伟蔡建国石鸿雁王穆君陈金龙张全兴
Owner NANJING UNIV