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MVR evaporation system employing two-effect parallel flow method

An evaporation system and two-effect technology, applied in the field of energy-saving technology, can solve the problem of high cost of compressors

Inactive Publication Date: 2017-05-31
杜明生
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  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] Both MVR technology and multi-effect evaporation technology belong to the energy-saving technology in the field of evaporation. The former has more obvious energy-saving advantages, but the cost of the core equipment compressor is relatively expensive.

Method used

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  • MVR evaporation system employing two-effect parallel flow method
  • MVR evaporation system employing two-effect parallel flow method

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Embodiment Construction

[0007] The original liquid is heated and evaporated by the first-effect equipment to separate the first-effect steam into a first-effect concentrated liquid, then enters the second-effect equipment for further evaporation and concentration, and then discharges into the subsequent process flow. When necessary, part of the concentrated liquid is forced to circulate back to the first-effect equipment. Continue to evaporate. The first-effect steam (that is, the secondary steam separated from the first effect) is directly used as the heat source of the second-effect heating equipment, and the second-effect steam (that is, the secondary steam separated from the second effect) enters the first effect after being compressed by the compressor. The heating device is used as the sole heat source. After heat exchange, the steam loses latent heat and condenses into liquid to be discharged. When it is necessary to make up for the heat balance of the system, open the raw steam input port in...

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Abstract

An MVR technology and a multi-effect evaporation technology belong to energy-saving technologies in the field of evaporation. The MVR technology is more obvious in energy-saving advantage, but core equipment compressor is relatively high in cost; an MVR system appears in a single-effect form in general and the investment cost of the compressor is almost half of all cost. The MVR technology is reasonably combined with a traditional multi-effect evaporation process employing a parallel flow method, and is optimized and integrated to form an MVR evaporation system employing a two-effect parallel flow method. The equipment investment can be reduced, the improvement of the efficiency of the whole evaporation system is facilitated, and the MVR evaporation system has the meaning of further energy conservation and emission reduction. The main measures of the system are as follows: secondary steam which is evaporated and separated from the second effect is compressed through a lobed rotor compressor to improve enthalpy and then used as sole first effect heating steam, meanwhile, the secondary steam which is evaporated and from the first effect is taken as a heat source of second effect heating equipment, and a little of live steam can be adopted to assist as a second effect heat source.

Description

technical field [0001] The invention relates to a mechanical vapor recompression system (abbreviated as MVR), which is mainly used as an energy-saving technology in the evaporation industry. Background technique [0002] Both MVR technology and multi-effect evaporation technology belong to the energy-saving technology in the field of evaporation. The former has more obvious energy-saving advantages, but the cost of the core equipment compressor is relatively expensive. MVR systems usually come only as a single-effect form, where the investment cost of the compressor is almost half that. Compared with the MVR technology, the traditional multi-effect evaporation process has a large gap in energy saving advantages, and at the same time, the cost performance is getting lower and lower with the increase of the number of effects, usually in the form of three effects. The advantage of multi-effect evaporation technology is that the process is mature and has cost advantages. The p...

Claims

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Application Information

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IPC IPC(8): B01D1/26B01D1/28B01D1/30
CPCB01D1/26B01D1/28B01D1/30
Inventor 杜明生
Owner 杜明生
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