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Device for desulfurizing flue gas by seawater through membrane absorption and its process

A desulfurization device and membrane absorption technology, applied in separation methods, chemical instruments and methods, and separation of dispersed particles, can solve the problems of uneven distribution of absorption liquid and flue gas, difficulty in engineering application, high operation and maintenance costs, and achieve High seawater utilization rate, stable desulfurization efficiency, strong resistance to flue gas SO2 concentration and flow impact

Inactive Publication Date: 2013-09-18
TIANJIN SEA WATER DESALINATION & COMPLEX UTILIZATION INST STATE OCEANOGRAPHI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Among them, the dry and semi-dry processes need to consume a large amount of absorbent, and produce solid by-products, which cause heavy equipment wear and high operation and maintenance costs.
Mature wet processes include seawater method and limestone-gypsum method. Compared with limestone-gypsum method, seawater method can save a lot of fresh water consumed for preparing absorption liquid, but due to the use of traditional gas absorption equipment (such as packed tower, liquid column tower and still cannot get rid of the common problem of wet flue gas desulfurization: due to the direct contact between the gas-liquid two-phase during the flue gas absorption process, the process is vulnerable to hydrodynamic conditions such as liquid flooding, channeling, and mist entrainment Limitation, resulting in uneven distribution of absorption liquid and flue gas, low mass transfer efficiency, and a large amount of water vapor in the discharged flue gas, coupled with residual SO 2 , so there is equipment corrosion problem
Due to the large air resistance caused by the capillary phenomenon of the hollow fiber membrane absorber, it is necessary to provide flue gas through a gas compressor, which consumes a lot of power
Therefore, the previous research on the removal of acid gas by membrane absorption method is in the laboratory stage, and it is difficult to realize engineering application.

Method used

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  • Device for desulfurizing flue gas by seawater through membrane absorption and its process
  • Device for desulfurizing flue gas by seawater through membrane absorption and its process
  • Device for desulfurizing flue gas by seawater through membrane absorption and its process

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Embodiment 1

[0100] use as figure 1 In the membrane absorption seawater flue gas desulfurization process shown, the desulfurization core part of the device consists of three stages such as Figure 11 The box-type gas-liquid contacting membrane absorbers shown are assembled in series and installed horizontally. The hollow fiber membrane filling area of ​​each stage membrane absorber is 500m 2 , the film packing density is about 9%; the original seawater is used as the absorption liquid, its conductivity is 47400μS / cm-51800μS / cm, the pH value is 7.45-8.22, and the temperature is normal temperature; the actual coal-fired flue gas is used, and its SO 2 Concentration 1000mg / Nm 3 ~1600mg / Nm 3 , soot concentration 100mg / Nm 3 , the temperature is 130°C to 150°C, and before entering the membrane absorber, the temperature is lowered to below 50°C through a heat exchanger. Control the total flow of seawater 5m 3 / h~25m 3 / h, using parallel connection to flow through the three-stage membrane ab...

Embodiment 2

[0102] Adopt the same process, device and absorption liquid as above-mentioned embodiment 1, flue gas is SO 2 The concentration is 2860mg / Nm 3 and 4290mg / Nm 3 The high concentration of actual coal-fired flue gas, the seawater flow rate is controlled to 15m 3 / h, the pH value is 8.20~8.51, and the flue gas treatment capacity is 500Nm 3 / h~1300Nm 3 In the range of / h, the corresponding concentration is 2860mg / Nm 3flue gas, the desulfurization rate is 97.7%-88.5%, and the pH value of seawater after desulfurization is 3.3-5.5; the corresponding concentration is 4290mg / m 3 flue gas, flue gas treatment capacity ≤ 1000Nm 3 In the case of / h, the desulfurization rate is 97.1%-90.6%, and the pH value of seawater after desulfurization is 2.7-5.0. flue gas SO 2 Concentration at 1000mg / Nm 3 ~4290mg / Nm 3 Fluctuation within the range, flue gas treatment capacity ≤ 1000Nm 3 / h, the desulfurization rate reached above 90%. Membrane fouling control in gas phase and liquid phase and p...

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Abstract

The invention discloses a device for desulfurizing flue gas by seawater through membrane absorption and its process, the flue gas is sent to a membrane absorber shell side by a supercharging blower fan, the pretreated seawater enters in a membrane absorber tube side through a sea water pump and is taken as absorption liquid, gas phase and liquid phase form a reaction interface at the micropore of a hollow fiber membrane, SO2 in flue gas is reacted with seawater to generate sulfite and timely is taken away for realizing the flue gas desulphurization. Desulfurized seawater is discharged through aeration sulfur fixation and pH value standard achieving. The device of the invention is composed of a one stage or multistage membrane absorber, the membrane absorber is composed of multi-group curtain type or column type hollow fiber film component group. The process has the characteristics of low air resistance of the device, small power consumption and high desulphurization efficiency. A design of an automatic on-line backwashing and cleaning technology is capable of controlling and mitigating membrane pollution, the device possesses small volume and light weight, and enables modularized integration; the flow velocity of the gas phase and the liquid phase can be independently controlled in a wide scope, and the problem of device corrosion caused by entrainment water vapor in flue gas in a traditional seawater method can be avoided.

Description

technical field [0001] The invention belongs to the intersecting field of air pollution control technology and application of membrane science and technology, and specifically relates to a system for removing sulfur dioxide in flue gas by using seawater as an absorption liquid and membrane absorption technology. Background technique [0002] Sulfur dioxide in the atmosphere mainly comes from the combustion of fossil fuels such as industrial waste gas and coal and oil. In our country at present and for a long period of time in the future, it is still the mainstream to provide heat and power resources through coal burning. In recent years, the rapid economic development in coastal areas has led to an increase in the economic burden caused by electricity shortages, resulting in the rapid development of coastal thermal power, which currently accounts for about one-third of the total installed capacity of thermal power. SO emissions from the power industry 2 About 50% of the co...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D53/78B01D53/50B01D53/18
Inventor 陈颖关毅鹏刘国昌郭春刚张召才李晓明李雪梅吕经烈
Owner TIANJIN SEA WATER DESALINATION & COMPLEX UTILIZATION INST STATE OCEANOGRAPHI
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