Desulfurization ammonia nitrogen wastewater processing method

A technology for ammonia nitrogen wastewater and wastewater, applied in the direction of degassed water/sewage treatment, gaseous effluent wastewater treatment, multi-stage water treatment, etc., can solve the problems of large steam consumption, difficult treatment, high equipment cost, etc., to reduce steam consumption amount, prevent secondary pollution, and reduce energy consumption

Inactive Publication Date: 2020-05-08
中轻建设(安徽)设计工程有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the steam consumption of the existing ammonia distillation process is large (130-150kg / ton water), and the steam pressure requirement is also high (≥0.4MPa)
[0003] In addition, in actual use, there is often not only one source of ammonia nitrogen sewage, especially in the process of ammonia-acid flue gas desulfurization treatment, in addition to sintered limestone-gypsum wet desulfurization wastewater, there are also waste water from the acid system and ammonia station System wastewater, if it is treated separately, multiple sets of wastewater treatment systems are required, the equipment cost is high, and the floor area is large
Moreover, these waste waters have high water hardness, heavy metals, and a lot of suspended matter. If the ammonia is directly stripped and steamed, the deammonization effect will not be good, and the trays will easily scale. Heavy metals are also mixed with lime residue, making subsequent treatment difficult.

Method used

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  • Desulfurization ammonia nitrogen wastewater processing method
  • Desulfurization ammonia nitrogen wastewater processing method
  • Desulfurization ammonia nitrogen wastewater processing method

Examples

Experimental program
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Effect test

Embodiment 1

[0032] refer to figure 1 and image 3 , a desulfurization ammonia nitrogen wastewater treatment system device, including a raw water primary sedimentation tank 1 for wastewater precipitation, a coagulation reaction precipitation device 3 for precipitation and recovery of heavy metals, a calcium and magnesium removal device 4 for removing calcium and magnesium ions, Negative pressure deamination system for deamination, electrocoagulation device 9 for flocculation and removal of remaining heavy metals, and ammonia washing purifier 21 for tail gas treatment, ammonia washing purifier 21 is selected but not limited to WDJHT-2000 type, the washing A water distributor 22 is arranged inside the ammonia purifier 21, and a water seal structure 26 is arranged below the water distributor 22 of the ammonia washing purifier 21, and the water sealing structure 26 includes separating the ammonia washing purifier 21 into upper and lower parts. The baffle 23, the air intake pipe 24 penetrating...

Embodiment 2

[0046] In this embodiment, the ammonia nitrogen in the 125t / d total wastewater of a certain company is treated and recovered as an example. There are three streams of wastewater, one of which is sintered limestone-gypsum wet desulfurization wastewater, with a water volume of 5t / h, containing a large amount of calcium ions and Suspended solids; the other stream is dry desulfurization wastewater, that is, acidic raw water, with a water volume of 1.5t / h, containing a large amount of sulfuric acid and suspended solids; the third stream of wastewater is wastewater from the ammonia station system, with a water volume of 5t / d and an ammonia content of about 5%; The relevant parameters of the wastewater are shown in Table 1.

[0047] Table 1 Relevant parameters of ammonia nitrogen wastewater, treated water volume: 125t / d, calculated on the basis of 5.5t / h

[0048] Item (mg / L) Wet desulfurization wastewater Dry desulfurization wastewater Ammonia station system wastewate...

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Abstract

The invention discloses a desulfurization ammonia nitrogen wastewater processing method. A desulfurization ammonia nitrogen wastewater processing system device used in the method comprises a raw waterprimary settling pond for wastewater sedimentation, a coagulation reaction precipitation device for precipitating and recovering heavy metals, a calcium and magnesium removal device for removing calcium and magnesium ions, a negative pressure deamination system for deamination, an electric flocculation device for flocculating and removing residual heavy metals, and an ammonia washing purifier fortail gas processing, a water distributor is arranged in the ammonia washing purifier, and a water seal structure is arranged below the water distributor of the ammonia washing purifier. Through the arrangement of the negative pressure deamination system, the deamination temperature in the whole deamination process is reduced by utilizing the principle that the boiling point of a liquid phase is greatly reduced in a negative pressure state, so that the whole system can perform efficient deamination in a relatively low temperature state, the energy consumption can be greatly reduced, and the steam consumption is reduced; ammonia water and heavy metals can be recycled while ammonia nitrogen and heavy metals are removed, waste is turned into wealth, and secondary pollution is prevented.

Description

technical field [0001] The invention belongs to the technical field of desulfurization wastewater treatment and relates to a treatment method for desulfurization ammonia nitrogen wastewater. Background technique [0002] Ammonia nitrogen sewage produced in the process of industrial production will cause serious water pollution, affecting surface water, groundwater, soil and crop pollution. Therefore, ammonia nitrogen sewage needs to be treated before being discharged, and ammonia water can be recycled as an energy source. In the prior art, the conventional solution is the ammonia distillation process, using the high temperature in the tower to boil the ammonia-containing nitrogen water to remove ammonia, condensing the ammonia vapor with a condenser, recovering dilute ammonia water, and controlling the reflux ratio to achieve the required ammonia water concentration. However, the steam consumption of the existing ammonia distillation process is large (130-150kg / ton water), ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/10C02F101/16C02F101/20C02F103/18
CPCC02F9/00C02F2001/007C02F1/5281C02F1/001C02F1/66C02F1/04C02F1/20C02F2301/08C02F2103/18C02F2101/16C02F2101/20C02F2303/14
Inventor 孙士杰倪崑张颖秦玮石婧英
Owner 中轻建设(安徽)设计工程有限公司
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