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Low-temperature multiple-effect evaporation crystallization and filtration process

A multi-effect evaporation and two-effect evaporation technology, applied in the low-temperature multi-effect evaporation crystallization filtration coupled with solute recovery process, waste heat utilization and waste liquid emission reduction, multi-effect evaporation crystallization granulation field, can solve the problem of intensified friction and collision of solute particles, easy to Blocking pipelines, discharge ports, pipelines, container corrosion and other problems, to achieve the effect of high production efficiency, not easy to block pipelines, and energy saving

Active Publication Date: 2013-07-10
DALIAN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

In order to obtain more crystals, the concentration of the solution is often raised to a high level, a large amount of solvent needs to be evaporated, and a large amount of heat source is consumed, resulting in high cost of crystallization and insufficient crystallization; and the corrosion of pipes and containers by high-concentration solutions is also very serious. It is easy to block the pipeline and the discharge port; at the same time, when the concentration is too high, the friction and collision between the solute particles will intensify, so that the resulting crystal particles will be smaller

Method used

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  • Low-temperature multiple-effect evaporation crystallization and filtration process

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Embodiment Construction

[0010] Below in conjunction with technical scheme and accompanying drawing, take ammonium sulfate crystallization as example to describe the specific embodiment of the present invention in detail.

[0011] Send the ammonium sulfate solution preheated to the boiling point with a concentration of 35% and a flow rate of 2000kg / h into the first-effect evaporator, and use dichloroethane vapor at a temperature of 83.4°C as a heat source to make the solution concentrated to 42%. Generate secondary steam at 75°C; the concentrated solution enters the second-effect evaporator to continue to evaporate; the heat required for this effect is 212.02kw, and the heat transfer coefficient is 2461.516W / (m 2 k), the heat transfer area is 25.18m 2 . In the two-effect evaporator, the secondary steam generated by the first effect is used to heat and evaporate and the solution is partially flashed to generate secondary steam at 64.6°C, and the solution is concentrated to 52.4%; the concentrated solu...

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Abstract

The invention relates to a low-temperature multiple-effect evaporation crystallization and filtration process belonging to the technical field of chemical engineering separation and energy conversation and emission reduction. The process is characterized in that processes of low-temperature multiple-effect evaporation, crystallization and filtration, granulation and the like are coupled to form aset of complete waste liquid emission free process for concentrating and extracting solute. The process comprises two loops, wherein a three-effect evaporator, a cooler, a crystallization filter and a heat exchanger form a loop; a four-effect evaporator and a crystallization filter form the other loop; low-temperature heat source or waste heat is utilized in one-effect evaporation, and secondary steam generated by the former one-effect is utilized in other effect evaporation; and heat required by the heat exchanger in a three-effect evaporation circulating loop is supplied by heat released bytemperature reduction of a heat source flowing from a one-effect evaporator. The invention has the advantages of reducing investment cost by adopting the low-temperature heat source or waste heat andthe secondary steam as heat sources, lightening corrosion because the concentration of a solution is not overhigh by adopting a reflux mode, being not easy to block a pipe, reducing operation cost, and being capable of completely separating out the solute without emitting waste liquid.

Description

technical field [0001] The invention belongs to the technical field of chemical separation and energy saving and emission reduction, and relates to a low-temperature multi-effect evaporation crystallization filtration coupling solute recovery process method, in particular to multi-effect evaporation crystallization granulation of substances whose solubility does not change much with temperature, waste heat utilization and Waste liquid reduction technology. Background technique [0002] The usual method of multi-effect evaporation crystallization is that the solution is concentrated through each effect evaporator in turn, and crystallized in the last effect. In order to obtain more crystals, the concentration of the solution is often raised to a high level, a large amount of solvent needs to be evaporated, and a large amount of heat source is consumed, resulting in high cost of crystallization and insufficient crystallization; and the corrosion of pipes and containers by high...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D9/02B01D1/26
Inventor 马学虎兰忠刘晓燕白涛彭本利朱霞
Owner DALIAN UNIV OF TECH
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