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Wastewater evaporating process and device system

A waste water, evaporation-drying technology, applied in water/sewage multi-stage treatment, water/sludge/sewage treatment, solution crystallization, etc., can solve the problem of affecting the operation and service life of equipment, complicated systems, and increasing the difficulty and cost of sewage treatment and other issues to achieve the effect of ensuring long-term stable operation

Active Publication Date: 2012-06-06
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 evaporating process and device system
  • Wastewater evaporating process and device system
  • Wastewater evaporating process and device system

Examples

Experimental program
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Effect test

Embodiment 1

[0132] Embodiment 1 of the present invention: waste water evaporation process (referring to figure 1): The waste water to be treated first enters the pretreatment softening system, and is softened by Glauber's salt-lime-flue gas method (see the following table 11 for specific chemical consumption parameters), removes easily scaled cations, and then stores them in the regulating tank. Pump into the buffer tank, add scale inhibitor and defoamer to the buffer tank, the amount of scale inhibitor added is 25g / t, and the amount of defoamer added is 3g / t; the waste water comes out of the buffer tank and is fed by the feed pump Enter the preheater 1 of the MVR system (preferably a plate heat exchanger), and exchange 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, first The fresh steam pre-evaporates the wastewater for about 100-200 minutes, reaching an ev...

Embodiment 2

[0153] Embodiment 2 of the present invention: waste water evaporation process (referring to figure 1 ): The wastewater to be treated first enters the pretreatment softening system, and then softens it with Glauber's salt-lime-flue gas method to remove the cations that are easy to scale, and then adds scale inhibitor at 25g / t, and then adds defoamer at 4g / t , into the preheater 1 of the MVR system for preheating, and then into the evaporator 2, into the fresh steam to pre-evaporate the wastewater, the resulting concentrated liquid and secondary steam enter the separator 3 for vapor-liquid separation, and the separated The secondary steam is compressed by the steam compressor 4 and sent to the evaporator 2 for recycling; the separated concentrated liquid enters the three-effect forced circulation evaporation and crystallization system for evaporation and crystallization in the mixed-flow evaporation method, and the concentrated liquid passes through the second effect and the firs...

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Abstract

The invention discloses a wastewater evaporating process and device system. The wastewater evaporating process comprises the following steps: the wastewater to be treated firstly enters a pretreatment softening system for softening treatment and secondly enters a mechanical vapor recompression (MVR) system for evaporation concentration; the generated secondary steam is compressed and enters an evaporator for recycling; the concentrated solution enters a triple effect flow-mixing forced circulation evaporation and crystallization system for evaporation and crystallization; the generated secondary steam is reused by the evaporation and crystallization system; the concentrated solution and crystalline grains obtained through crystallization are subject to solid-liquid centrifugal separation;the separated mother solution is sent back to a raw liquor tank or evaporated continuously for crystallization; and the separated crystals enter a centrifugal drying and packaging system for weighting and packaging. After the process disclosed by the invention is adopted to soften, evaporate and crystallize wastewater and dry and package the obtained crystals, wastewater is not discharged to the water bodies of the surface of earth and the aim of zero wastewater discharge can be realized; the process system is low-carbon and environmentally friendly; the material can be recycled, the thermal efficiency is high, the energy consumption is low, the energy can be saved, the operating cost can be greatly reduced, the range of temperature is small, the corrosion is low and the service life of the equipment is long, and the scaling has small possibility of occurrence.

Description

technical field [0001] The invention relates to a waste water evaporation process and a device system, in particular to a high-concentration industrial waste water and / or desulfurization waste water evaporation process and a device system, and belongs 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 ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D9/02C02F9/10
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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