Integrated system and method for multi-stage white-smoke-removing and purification of flue gas and waste heat recycling

A waste heat recovery and flue gas technology, applied in the field of integrated systems, can solve the problems of high absorbent consumption, low COP value, pipeline clogging and scouring, etc.

Active Publication Date: 2018-11-02
HEIMDALLR SHANGHAI ENERGY SAVING TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The technical problem to be solved by the present invention is to overcome the unreasonable use of heat, low COP value and the limitation of absorbent in the flue gas dewhitening and purification system in the prior art. Due to the defects of large consumption, high investment cost, serious pipeline blockage and erosion, and unstable operation of the system, a new type of integrated system and method for multi-stage dewhitening and purification of flue gas and waste heat recovery is provided.

Method used

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  • Integrated system and method for multi-stage white-smoke-removing and purification of flue gas and waste heat recycling
  • Integrated system and method for multi-stage white-smoke-removing and purification of flue gas and waste heat recycling
  • Integrated system and method for multi-stage white-smoke-removing and purification of flue gas and waste heat recycling

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0080] 1. An integrated system for multi-stage dewhitening and purification of flue gas and waste heat recovery

[0081] Such as figure 1 The integrated system for multi-stage dewhitening and purification of flue gas and waste heat recovery is shown. The integrated system includes a multi-stage absorption tower 10, a primary absorption liquid storage tank 20, a primary solution heat exchanger 30, a secondary solution external Circulating heat exchanger 40, secondary solution self-circulating heat exchanger 60 and secondary solution regeneration device 50;

[0082] The number of stages of the multi-stage absorption tower 10 is more than two, and the multi-stage absorption tower 10 is divided into a primary absorption zone 11 and a secondary absorption zone 13 from bottom to top; the multi-stage absorption tower 10 is provided with a wet flue gas inlet 111, The wet flue gas inlet 111 is used to send the wet flue gas into the primary absorption zone 11; Bit stability;

[0083]...

Embodiment 2

[0109] 1. An integrated system for multi-stage dewhitening and purification of flue gas and waste heat recovery

[0110] Such as figure 2 In the integrated system shown, there is also a wet electrostatic precipitator 135 above the secondary absorption zone 13 in the multi-stage absorption tower 10, and the rest are the same as the integrated system of Embodiment 1.

[0111] 2. Methods of flue gas dewhitening and purification and waste heat recovery

[0112] A method of flue gas dewhitening purification and waste heat recovery using the above-mentioned integrated system, the steps of the method are the same as those in Example 1, and the process parameters are slightly different, as follows:

[0113] In step (1), the inlet temperature of wet flue gas is 80°C, and the inlet flow rate of wet flue gas is 125000Nm 3 / h; the primary solution is 5wt% NaCl aqueous solution, the inlet temperature of the primary solution is 40°C, and the circulation flow rate of the primary solution ...

Embodiment 3

[0117] 1. An integrated system for multi-stage dewhitening and purification of flue gas and waste heat recovery

[0118] Such as image 3 In the integrated system shown, the integrated system is also provided with a first dry flue gas outlet 136 pipe leading from the dry flue gas outlet 136, and a flue gas heater 90 is arranged on the first dry flue gas outlet 136 pipe, and the flue gas The heater 90 is used to heat the dry flue gas; the secondary solution generator is also provided with a secondary steam outlet 51, and the secondary steam outlet 51 communicates with the thermal fluid channel of the flue gas heater 90, and the rest are the same as the integrated system of embodiment 1 .

[0119] 2. Methods of flue gas dewhitening and purification and waste heat recovery

[0120] A method of flue gas dewhitening purification and waste heat recovery using the above-mentioned integrated system, the steps of the method are the same as those in Example 1, and the process paramete...

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Abstract

The invention discloses an integrated system and method for multi-stage white-smoke-removing and purification of flue gas and waste heat recycling. The integrated system comprises a multi-stage absorbing tower, a primary absorbing liquid storage tank provided with an overflowing tube, a primary solution heat exchanger, a secondary solution external cycle heat exchanger, a secondary solution self-cycle heat exchanger and a secondary solution regeneration device; the multi-stage absorbing tower has more than two stages, is divided into a primary absorbing region and a secondary absorbing regionfrom bottom to top, and is provided with a wet flue gas inlet and a dry flue gas outlet; and the integrated system is further provided with a primary solution cycle loop, a secondary solution externalcycle loop, a secondary solution self-cycle loop and a flow distributing device, and by the flow distributing device, the flow meter of fluid in the secondary solution self-cycle loop and fluid in the secondary solution external cycle loop is (3-5): 1. By the integrated system and method, heat is utilized reasonably, COP value is high, consumption of an absorber is low, the investment cost of thesystem is also low, the pipe blockage and washing problem is greatly relieved, and the system runs continuously and stably.

Description

technical field [0001] The invention relates to an integrated system and method for multi-stage dewhitening and purification of flue gas and waste heat recovery. Background technique [0002] The traditional flue gas dewhitening and purification system only adopts a single-stage tower. The disadvantage of this purification system is that the heat of the system cannot be used reasonably, so the COP value (COP value=system output energy / driving power, wherein: driving power refers to the additional supply provided by the outside world) The electric energy, steam energy or gas heat energy) is low, and the consumption of absorbent is large, and the equipment investment cost is high; the obtained absorption liquid must be recycled through the regeneration system to recover the moisture in the wet flue gas, increasing the consumption of additional heat sources; in the absorption liquid All the solid impurities will enter the follow-up system, such as the pipeline system, heat exch...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/18F25B15/06F25B27/02F28D21/00
CPCB01D53/18F25B15/06F25B27/02F28D21/0003B01D2258/0283B01D2252/10B01D2252/103Y02A30/274
Inventor 白亮徐敬玉马元黄文乐
Owner HEIMDALLR SHANGHAI ENERGY SAVING TECH
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