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Caprolactam production wastewater treatment method

A technology for producing wastewater and caprolactam, which is applied in biological water/sewage treatment, heating water/sewage treatment, water/sewage multi-stage treatment, etc. It can solve the problems of waste of resources, difficult operation, complicated process, etc., and reduce energy consumption , production cost reduction, simple operation effect

Active Publication Date: 2021-01-05
福建天辰耀隆新材料有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] 1. This method has complex process, difficult operation, large energy consumption, and high production and operation costs;
[0007] 2. Both caprolactam and ammonium sulfate in wastewater cannot be recycled, and are eventually incinerated, resulting in waste
[0008] In the patent with the authorization number CN103708646B, a method for treating caprolactam industrial wastewater is disclosed, which adopts an improved wet oxidation method and introduces H 2 o 2 As an oxidant, it has a high COD removal rate, but the organic matter and ammonium sulfate in the wastewater cannot be recovered, resulting in a waste of resources

Method used

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  • Caprolactam production wastewater treatment method
  • Caprolactam production wastewater treatment method
  • Caprolactam production wastewater treatment method

Examples

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Effect test

Embodiment 1

[0043] The processing method of caprolactam production waste water, it comprises the following steps carried out in sequence:

[0044] S1 Distillation treatment of production wastewater: The caprolactam production wastewater is subjected to continuous feed distillation at 100°C under normal pressure. During the distillation process, the distillation condensate and distillation raffinate are continuously obtained. The discharge speed is the same, distill until the distillation raffinate has crystals, and the distillation raffinate is concentrated 4 times compared to the original caprolactam production wastewater; the content of COD in the distillation process of caprolactam production wastewater is 1500mg / L, ammonia nitrogen is 200~600mg / L L, the pH of the distillate is 8.5-9.5.

[0045] S2 Distillation raffinate recovery: The obtained distillation raffinate is left to stand for stratification, divided into upper layer material, middle layer liquid and lower layer crystal, and ...

Embodiment 2

[0049] The difference is that the temperature of the atmospheric pressure feed distillation treatment is 90° C., the feed speed during the distillation process is greater than the distillation discharge speed, and the distillation raffinate is concentrated 5 times relative to the original caprolactam production wastewater. Others are the same as in Example 1.

[0050] In the upper liquid prepared in this embodiment, the content of organic matter was 16.62%.

Embodiment 3

[0052] The difference is that the temperature of the atmospheric pressure feed distillation treatment is 120° C., and the distillation raffinate is concentrated 6 times relative to the original caprolactam production wastewater, and the others are the same as in Example 1.

[0053] In the upper layer liquid prepared in this embodiment, the content of organic matter was 16.32%.

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Abstract

The invention relates to wastewater treatment, in particular to a caprolactam production wastewater treatment method which comprises the following steps of: S1, distillation treatment of production wastewater: performing normal-pressure feeding distillation treatment on caprolactam production wastewater, continuously obtaining distillation condensate and distillation raffinate respectively in thedistillation process, and distilling until crystals are separated out of the distillation raffinate; and S2, distillation raffinate recovery: standing the obtained distillation raffinate for layering,dividing the distillation raffinate into an upper-layer substance, a middle-layer liquid and a lower-layer crystal, recovering the upper-layer substance and the lower-layer crystal of the distillation raffinate, and continuing distillation treatment of the middle-layer liquid in the step S1. According to the method, organic matters and ammonium sulfate are effectively recycled at low cost, and resource utilization is achieved.

Description

technical field [0001] The invention relates to wastewater treatment, in particular to a method for treating wastewater produced by caprolactam. Background technique [0002] The molecular formula of caprolactam is C 6 h 11 NO, the appearance is white powder or crystal, with oily feel. Caprolactam is one of the important organic chemical raw materials. Its main purpose is to produce polyamide chips (usually called nylon-6 chips, or nylon-6 chips) through polymerization, which can be further processed into nylon fibers, engineering plastics, and plastic films. Nylon-6 slices have different application areas depending on the quality and index. [0003] Chemical oxygen demand, or COD, represents the amount of oxygen required for potassium dichromate to oxidize organic matter in one liter of sewage under strong acidic conditions, and can roughly represent the amount of organic matter in sewage. [0004] The COD of caprolactam production wastewater is about 40000mg / L, the amm...

Claims

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Application Information

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IPC IPC(8): C02F9/14C01C1/24C02F101/10C02F101/16C02F101/30
CPCC02F9/00C01C1/24C02F2001/007C02F1/04C02F3/302C02F1/38C02F1/50C02F2101/30C02F2101/16C02F2101/101
Inventor 陈云祥张朋利陈旭光王艳琦杨成砚
Owner 福建天辰耀隆新材料有限公司
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