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A collaborative flue gas waste heat utilization system and carbon-based loaded ionic liquid desulfurization method

A flue gas waste heat and flue gas technology, applied in separation methods, chemical instruments and methods, gas treatment, etc., can solve the problems of high-viscosity ionic liquid absorbent regeneration, high energy consumption, etc., achieve stability, economical benefits, and reduce emissions. , to enhance the effect of heat transfer

Active Publication Date: 2020-06-26
SHANDONG UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The purpose of the present invention is to overcome the deficiencies of the prior art, and provide a method and system for high-efficiency desulfurization of carbon-based loaded ionic liquids using flue gas waste heat using heat exchangers and flue gas waste heat to regenerate absorbents to solve the problem of high-viscosity ionic liquids. Problems in application and high energy consumption of absorbent regeneration

Method used

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  • A collaborative flue gas waste heat utilization system and carbon-based loaded ionic liquid desulfurization method
  • A collaborative flue gas waste heat utilization system and carbon-based loaded ionic liquid desulfurization method
  • A collaborative flue gas waste heat utilization system and carbon-based loaded ionic liquid desulfurization method

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example 1

[0050] Example 1: The ionic liquid used was synthesized under the action of microwaves. The ratio of triethanolamine and acetic acid was 1.2:1. After synthesis, activated carbon or silica gel was used for loading by impregnation. The loading ratio was 0.75:1, and then the ionic liquid was realized by evaporation and drying. load;

example 2

[0051] Example 2: The ionic liquid used was synthesized under the action of microwaves, the ratio of triethanolamine and acetic acid was 1.2:1, and after synthesis, 80-120 mesh activated carbon was used for loading by impregnation. The load ratio is 0.75:1, accurately weigh 7.5g of ionic liquid and dissolve it in 30ml of absolute ethanol, put 10g of 80-100 mesh activated carbon into it, keep stirring and gradually raise the temperature to 90°C, when most of the solvent is evaporated , put the loaded activated carbon into a drying oven at 50°C and dry until particles appear.

[0052] Take 2g of loaded activated carbon and place it in the reactor, pass through the simulated flue gas, and carry out the adsorption experiment at 40°C, and the loaded activated carbon is penetrated for about 7 hours.

example 3

[0053] Example 3: The ionic liquid used was synthesized under the action of microwaves, the ratio of triethanolamine and acetic acid was 1.2:1, and after synthesis, 60-80 mesh was used for loading by impregnation. The loading ratio is 0.75:1. Accurately weigh 7.5g of ionic liquid and dissolve it in 30ml of absolute ethanol. Put 10g of activated carbon into it, stir continuously and gradually raise the temperature to 90°C. When most of the solvent is evaporated, put the loaded The silica gel was dried in a drying oven at 50°C until particles appeared.

[0054] Take 2g of loaded activated carbon and place it in the reactor, pass through the simulated flue gas, and conduct the adsorption experiment at 40°C. The adsorption is complete in about 1.5h.

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Abstract

The invention provides a coordinated flue gas waste heat utilization system and a carbon-based supported ionic liquid flue gas desulfurization method, comprising an air preheater, a first heat exchanger, a second heat exchanger, a first absorption / analysis tower, a second Absorption / analyzing tower, gas-solid separator, fan, gas storage and acid making device, compressor and chimney, the air preheater is connected to the heat exchanger, and the flue gas cooled by the air preheater enters the first heat exchanger Carry out secondary heat exchange with the air in the heat exchanger, and the heated air is returned to the air preheater for secondary reheating and utilization; the first heat exchanger is also used as a heater for starting nitrogen in the analysis system. Nitrogen is connected to the absorption / analysis tower through a pipeline; the flue gas side of the second heat exchanger is connected to the absorption / analysis tower, the upper part of the absorption / analysis tower is connected to the chimney through a pipeline, and the bottom of the absorption / analysis tower is connected to the gas-solid through a pipeline The separator, after the gas-solid separator, is connected to the fan and the compressor in sequence, and the compressor is respectively connected to the gas storage acid making device and the second heat exchanger through the pipeline. The invention can not only make full use of the residual heat of the flue gas to realize the effective utilization of the low-temperature flue gas at the tail, but also solve the problems of high resistance and high energy consumption of the absorbent regeneration in the application of the high viscosity ionic liquid as the absorbent.

Description

technical field [0001] The invention belongs to the technical fields of heat exchange technology and flue gas desulfurization, and in particular relates to a flue gas waste heat utilization system and a method for flue gas desulfurization of carbon-based loaded ionic liquid. Background technique [0002] my country is the world's largest coal producer and consumer. Coal-fired power plants consume a lot of coal to provide steam and electricity, but also emit a lot of waste heat. Flue gas waste heat recovery generally adopts shell-and-tube heat exchangers, so the enhanced heat transfer technology of heat exchangers is of great significance to energy saving and consumption reduction. Among them, passive enhanced heat transfer technology has become an important research direction because it does not require external high-quality energy input to achieve the purpose of enhanced heat transfer. [0003] The use of fluid-induced vibration of heat transfer elements to achieve enhance...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): F23J15/06F23J15/04F23J15/02B01D53/14
CPCB01D53/1425B01D53/1481B01D53/1493B01D2252/30B01D2258/0283F23J15/022F23J15/04F23J15/06Y02E20/30
Inventor 崔琳唐立淑张立强马春元
Owner SHANDONG UNIV