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Wastewater evaporation concentration process and device system

An evaporative concentration and evaporation system technology, which is applied in water/sewage multi-stage treatment, water/sludge/sewage treatment, inorganic chemistry, etc. It can solve the problems that affect the operation and service life of equipment, difficult to clean, and the quality of recycled water is not as good as crystal seeds. Laws and other issues to achieve the effect of ensuring long-term stable operation

Inactive Publication Date: 2011-05-25
华电水务工程有限公司 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The seed crystal method has a good effect on wastewater treatment with a relatively low content of calcium ions and sulfate ions or one of the two in an industry or conventional water system, and the cleaning cycle is acceptable, but for already supersaturated systems When the desulfurization wastewater enters the preheater, scaling will occur soon due to the temperature rise and phase change. Once scaling is formed, it will be very difficult to clean, which will affect the operation and service life of the equipment.
[0004] The reverse osmosis concentration method requires pretreatment of RO influent, including turbidity, scaling substances, COD, etc., and the system is relatively complicated; the water quality of the recovered water is not as good as that of the seed crystal method, and the wastewater cannot be completely recovered, so it needs to be recycled to the surrounding environment or sewage collection system If a large amount of sewage is discharged into the existing sewage collection system, it will increase the difficulty and cost of subsequent sewage treatment

Method used

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  • Wastewater evaporation concentration process and device system
  • Wastewater evaporation concentration process and device system
  • Wastewater evaporation concentration process and device system

Examples

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Effect test

Embodiment 1

[0087] Embodiment 1 of the present invention: wastewater evaporation concentration process (see figure 1 ): The waste water to be treated is softened and stored in the adjustment tank, pumped into the buffer tank, and the scale inhibitor and defoamer are added to the buffer tank. The amount of scale inhibitor added is 25g / t, and the amount of defoamer added is 3g / t; waste water comes out of the buffer tank, and is pumped into the preheater 1 (preferably plate heat exchanger) of the MVR system by the feed pump, and exchanges heat with the steam condensate from the evaporator 2 and the forced circulation evaporation crystallization system; After the waste water is preheated, it enters the evaporator 2, and first injects fresh steam to pre-evaporate the waste water for about 100 to 200 minutes, reaching an evaporation temperature of 90°C (reducing the evaporation temperature can greatly inhibit the possibility of fouling, and reduce the evaporator due to fouling. Possibility of sca...

Embodiment 2

[0104] Embodiment 2 of the present invention: wastewater evaporation concentration process (see figure 1 ): After the wastewater to be treated is softened, first add scale inhibitor at 25g / t, add defoamer at 4g / t, put it into the preheater 1 of the MVR system for preheating, then enter the evaporator 2, inject fresh steam to The waste water is pre-evaporated, and the concentrated liquid and secondary steam produced enter the separator 3 for vapor-liquid separation, and the separated secondary steam is compressed by the steam compressor 4 and sent to the evaporator 2 for recycling; the separated concentrated liquid enters the third The high-efficiency forced circulation evaporation crystallization system conducts evaporation and crystallization in the mixed-flow evaporation method, and the concentrated solution passes through the second effect, first effect, and third-effect forced circulation evaporation crystallization system in turn, and the crystallized concentrated solution...

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Abstract

The invention discloses a wastewater evaporation concentration process and a wastewater evaporation concentration device system. The process comprises the following steps of: delivering softened wastewater to be treated to a mechanical vapor recompression (MVR) system to perform evaporation and concentration, compressing the generated secondary steam and then delivering the compressed steam to an evaporator to recycle, delivering the concentrate to a triple-effect mixed flow forced circulating evaporation crystallization system to perform evaporation and crystallization, performing solid-liquid centrifugal separation on the crystallized concentrate and crystal grains, returning the separated mother solution to a stock solution tank or continuously performing evaporation and crystallization, and reclaiming the separated crystal, wherein the secondary steam generated by evaporation and crystallization is recycled for the evaporation crystallization system. After the wastewater is evaporated and concentrated by adopting the process of mechanical vapor recompression circulating evaporation and triple-effect mixed flow forced circulating evaporation crystallization, the wastewater does not need to be discharged to the ground water area, and the wastewater is discharged in a form of steam or closed and embedded in a form of sludge or the like, so the purpose of zero discharge of the wastewater can be fulfilled; and the process system has high heat efficiency, low energy consumption, energy conservation, great reduction in running cost, low temperature difference, low corrosion, difficult scale formation and long equipment service life.

Description

technical field [0001] The invention relates to a waste water evaporation concentration process and a device system, belonging to the technical field of sewage treatment. Background technique [0002] At present, the commonly used follow-up advanced treatment methods for high-concentration industrial wastewater and / or desulfurization wastewater are: (1) seed crystal method: this process is to add crystal nucleus slurry to establish and maintain calcium sulfate crystallization during the brine circulation process of the evaporator, The evaporation of most of the water is completed in the brine concentrator, and the brine concentrator discharges brine with about 20% TDS, which is further concentrated and evaporated in the crystallizer, and the brine is concentrated into a rather thick crystal slurry and mother liquor (about solids). The crystallization slurry and mother liquor enter the drying spray chamber for drying, and are finally collected in the form of dry powder and s...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/10C01D5/00C01D3/04
Inventor 韩买良沈明忠张雪杰陈欣
Owner 华电水务工程有限公司
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