Coke oven flue gas desulfurization technology and system

A desulfurization process and desulfurization system technology, applied in gas treatment, membrane technology, and dispersed particle separation, etc., can solve the problems of not really realizing SO2 emission reduction, failing to meet the desulfurization requirements of coke oven flue gas, and low flue gas outlet temperature , achieve the effect of short flue gas residence time, improved desulfurization effect, and small spraying amount

Inactive Publication Date: 2016-09-21
HUATIAN ENG & TECH CORP MCC +1
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  • Abstract
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  • Claims
  • Application Information

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Problems solved by technology

[0004] In response to these problems, CN103877856A proposes to use coke produced by coking enterprises to reduce SO in flue gas 2 Adsorption removal, this method can ensure the purification of coke oven flue gas under the condition of lower flue temperature drop, but because the coke produced by the coking plant has a small specific surface area and limited adsorption capacity, it needs to continuously replenish a large amount of fresh coke to Satisfy SO 2 emission requirements, and the SO adsorbed by the spent coke in the downstream utilization process 2 Will still be released, just implemented SO 2 The transfer of emissions does not really achieve SO 2 emission reduction
CN101874975 discloses a double-alkali semi-dry desulfurization process, but this method only mixes a certain proportion of sodium hydroxide in the absorbent of the conventional lime dry desulfurization process, which can improve the desulfurization efficiency to a certain extent, but because sodium-alkali cannot regeneration, also significantly increases operating costs
At the same time, this method still mainly uses calcium alkali as the absorbent, and it is difficult to achieve a lower flue gas temperature drop while satisfying the desulfurization efficiency.
At the same time, the existing mature double-alkali desulfurization process is a wet process, the flue gas outlet temperature is low, and calcium sulfate deposition and blockage are prone to occur during the slurry circulation process, which also cannot meet the desulfurization requirements of coke oven flue gas

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  • Coke oven flue gas desulfurization technology and system

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Embodiment 1

[0032] The coke oven flue gas desulfurization system in this embodiment includes a spray drying tower 1, a bag filter 2, a desulfurization dust buffer 3, a sodium-alkali regeneration tank 4, a vacuum belt dehydrator 5, a sodium-alkali mixing tank 6, and a slurry buffer tank 7.

[0033]The spray drying tower 1 and the bag filter 2 are connected by a flue. The spray drying tower 1 includes a spray drying tower body, a rotary sprayer 8 is arranged on the tower body, and a hopper is arranged at the lower end of the tower body. The bag filter 2 includes a flue gas dust removal part connected up and down and an ash bin for collecting the dust removed by the dust removal part. The ash bin of the bag filter 2 and the hopper of the spray drying tower 1 pass through the pneumatic ash conveying pipeline and the desulfurization dust buffer bin 3 respectively. connect. The desulfurization dust buffer bin 3 and the sodium-alkali regeneration tank 4 are connected by a pneumatic ash conveying...

Embodiment 2

[0039] The coke oven flue gas desulfurization process in this embodiment is realized by using the coke oven flue gas desulfurization system in Example 1.

[0040] The temperature is 180℃, SO 2 Concentration is 300mg / Nm 3 The coke oven flue gas from the flue gas enters the spray drying tower 1 from the flue gas distributor 9, and is in co-current contact with the droplets of the caustic soda solution sprayed by the rotary atomizer 8. The concentration of the caustic soda solution sprayed into the tower is 20wt%, the design value of the Na2 / S molar ratio is 1.05, the design value of the residence time of the flue gas in the tower is 5s, the average flow rate of the interface in the tower is 0.3m / s, the caustic soda solution The control range of the average particle size of the mist droplets is 60-80 μm. Most of the sodium hydroxide reacts with sulfur dioxide in the tower to form sodium sulfite and is dried into solid desulfurized ash. The desulfurized ash enters the bag filte...

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Abstract

The invention discloses a coke oven flue gas desulfurization technology and system and mainly aims to reduce temperature drop of flue gas in a desulfurization process so as to meet the hot standby requirement of a chimney. According to the coke oven flue gas desulfurization technology and system, a sodium-alkali solution is taken as a desulfurizing agent, the atomized sodium-alkali solution is subjected to a reaction with SO2 in flue gas, and sulfite is generated, dried with the flue gas and recovered by a dust collector; the recovered desulfurized dust is regenerated by the aid of a Ca(OH)2 solution, desulfurized gypsum and a sodium-alkali regenerated solution are obtained, and the sodium-alkali regenerated solution returns to a desulfurization system for circulating desulfurization. With the adoption of the coke oven flue gas desulfurization technology and system, investment and operation cost of coke oven flue gas desulfurization can be remarkably reduced, the outlet flue gas temperature of desulfurization equipment is increased, the hot standby requirement of the chimney can be met without reheating, and meanwhile, the problems of scaling, difficulty in sodium-alkali regeneration and the like of a wet double-alkali method are solved.

Description

technical field [0001] The invention relates to a coke oven flue gas desulfurization process and system. Background technique [0002] As one of the main air pollutants, sulfur dioxide has always been the focus of my country's emission reduction work. With the continuous improvement of environmental protection legislation and the increasingly stringent environmental protection standards, certain progress has been made in reducing sulfur dioxide emissions. appear. However, in the non-electrical industries such as coke oven smelting, iron and steel metallurgy, building materials and cement, where the emission reduction work started late, the emission reduction situation of air pollutants is still very serious. Especially for flue gas emissions from coke oven smelting, most companies have not taken any emission reduction measures. According to the requirements of "Coking Chemical Industry Pollutant Emission Standard" (GB16171-2012), the emission concentration of sulfur dioxi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/78B01D53/50B01D53/96
CPCB01D53/502B01D53/504B01D53/96B01D2251/304B01D2258/0283
Inventor 安忠义詹茂华冯博王浩
Owner HUATIAN ENG & TECH CORP MCC
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