Method for recovery and comprehensive resource treatment of phenol and ammonia in semi-coke waste water

A technology for the recovery of semi-coke wastewater and phenolic ammonia, which is applied in the field of resource-based comprehensive treatment of semi-charcoal wastewater and phenolic ammonia recovery, can solve problems that affect system stability, cannot be classified to obtain various organic products, and blockage of stripping trays. Achieve the effects of realizing efficient recycling, improving anti-fouling performance, ensuring water intake and operation

Active Publication Date: 2017-12-05
INST OF PROCESS ENG CHINESE ACAD OF SCI +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] Although the traditional phenolic ammonia recovery and treatment technology can effectively treat and recover the phenol and ammonia pollutants in semi-coke wastewater, due to technological limitations, the traditional phenolic ammonia recovery and treatment process has high energy consumption, low purity of recovered phenol resources, and systemic problems. Problems such as poor running stability are manifested in the following points:
[0006] 1. In the traditional phenolic ammonia recovery technology, the waste water often goes directly into the subsequent stripping tower after gravity degreasing or air flotation degreasing. Due to the special water quality structure of the semi-coke waste water, only physical degreasing often cannot solve the coke suspended in the waste water. Powder, coal powder, tar micelles and other solid pollutants with a density close to water will cause these pollutants to enter the subsequent stripping tower, which will easily cause blockage of the stripping tray and affect system stability;
[0007] 2. The ether or ketone single-component extractant used in the

Method used

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  • Method for recovery and comprehensive resource treatment of phenol and ammonia in semi-coke waste water

Examples

Experimental program
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Effect test

Embodiment 1

[0033] The semi-coke wastewater to be treated is a semi-coke processing enterprise, which is the wastewater after deacidification, deamination and pre-oil removal. The main indicators are: COD: 10000mg / L; oil: 500mg / L; total phenols: 2000mg / L ; NH4-N: 1500mg / L; pH value: 7.5.

[0034] The actual waste water treatment process is as follows: the waste water is left to stand for 36 hours in the semi-coke waste water tank, and the standing waste water is sent to the pre-oil removal reactor after passing through the coke filter, and the extraction oil-water ratio in the pre-oil removal reactor is 1: 15. The waste water from the pre-oil removal reactor enters the stripping and deacidification tower, which is heated by low-pressure steam, the steam pressure is 0.2Mpa, and the temperature at the top of the deacidification tower is controlled at 55°C. The wastewater from the bottom of the deacidification tower enters the ammonia distillation tower, which is heated by low-pressure stea...

Embodiment 2

[0037] The semi-coke wastewater to be treated is a calcium carbide production enterprise, which is wastewater after deacidification, deamination and pre-oil removal. The main indicators are: COD: 40000mg / L; oil: 5000mg / L; total phenols: 15000mg / L; NH4-N: 3000mg / L; pH value: 9.

[0038] The actual process of wastewater treatment is as follows: the wastewater is allowed to stand for 72 hours in the semi-coke wastewater tank, and the wastewater is sent to the pre-degreasing reactor after being passed through the coke filter. The extraction oil-water ratio in the pre-oil removal reactor is 1:8. The waste water from the pre-oil removal reactor enters the stripping deacidification tower, which is heated by low-pressure steam, the steam pressure is 0.3Mpa, and the temperature at the top of the deacidification tower is controlled at 80°C. The wastewater from the bottom of the deacidification tower enters the ammonia distillation tower, which is heated by low-pressure steam with a ste...

Embodiment 3

[0041] The semi-coke wastewater to be treated is the wastewater after deacidification, deamination and pre-oil removal of a coal chemical enterprise. The main indicators are: COD: 25000mg / L; oil: 2500mg / L; total phenols: 10000mg / L; NH4-N: 4000mg / L; pH value: 8.7.

[0042] The actual process of wastewater treatment is as follows: the wastewater is allowed to stand for 72 hours in the semi-coke wastewater tank, and the wastewater is sent to the pre-degreasing reactor after being passed through the coke filter. The extraction oil-water ratio in the pre-oil removal reactor is 1:10. The waste water from the pre-oil removal reactor enters the stripping deacidification tower, which is heated by low-pressure steam, the steam pressure is 0.3Mpa, and the temperature at the top of the deacidification tower is controlled at 80°C. The wastewater from the bottom of the deacidification tower enters the ammonia distillation tower, which is heated by low-pressure steam with a steam pressure o...

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Abstract

The invention discloses a method for recovery and comprehensive resource treatment of phenol and ammonia in semi-coke waste water. The method comprises the following steps: performing standing on the semi-coke waste water to realize gravity oil removing and separating recovery, filtering an effluent through a coke filter to remove a solid suspension, and introducing the effluent in an extraction pre-oil removal reactor for deeply removing oil residue, coke powder and tar pollutants in the waste water; performing stripping depickling on the waste water after extraction and pre-oil removal, performing ammonia distilling and performing extraction processing to remove and recover the acidic gas, ammonia and phenol in the waste water, and introducing the processed waste water which reaches the standard in a biochemical treatment system; performing extraction processing to obtain a phenol-rich organic phase, and converting phenols in an extract phase to sodium phenolate through alkali washing processing to realize separation of an extractant and the phenols; and introducing a sodium phenolate solution to an acidifying workshop section for acidifying to prepare crude phenol and sodium salt. The method can realize separation and enrichment of phenols, heavy oil, light oil, ammonia and acidic gas in the semi-coke waste water, realizes resource recovery, at the same time, realizes regeneration and cycle utilization of the extractant and alkali lye, and has good application prospect.

Description

technical field [0001] The invention relates to the field of semi-coke wastewater treatment, in particular to a resource-based comprehensive treatment method for recovering phenol and ammonia from semi-coke wastewater. Background technique [0002] Semi-coke wastewater is wastewater produced during coal dry distillation (about 550~650°C), which contains refractory organic pollutants such as phenol, tar, and ammonia. It is difficult to treat and has great environmental hazards. [0003] For semi-coke wastewater, the current conventional treatment methods usually include two stages: phenolic ammonia recovery pretreatment and biochemical treatment, in which the phenolic ammonia recovery pretreatment unit is not only a security system for the subsequent biochemical treatment system, but also directly related to the operation of the biochemical treatment system. It is also related to the recovery of valuable resources in semi-coke wastewater, so it is the key to the success of se...

Claims

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Application Information

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IPC IPC(8): C02F9/14C01C1/02C02F101/16C02F101/34
CPCC01C1/022C02F1/00C02F1/20C02F1/26C02F1/40C02F9/00C02F2101/16C02F2101/345C02F2301/08
Inventor 盛宇星李海波刘亚丽李玉平李成成
Owner INST OF PROCESS ENG CHINESE ACAD OF SCI
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