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Compartment turbulent bed desulfurization, denitrification and dust removal device and process thereof

A desulfurization, denitrification and dust removal device technology, applied in the field of desulfurization and denitrification, can solve problems such as many fault points, equipment jamming, desulfurization efficiency decline, etc., and achieve the effects of saving operating costs, increasing concentration, and improving utilization efficiency

Active Publication Date: 2021-04-20
山东祥桓环境科技有限公司 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0011] (1) The desulfurization efficiency is greatly affected by the fluctuating flue gas volume. When the actual flue gas volume is greater or less than the designed flue gas volume, the desulfurization efficiency will decrease. Especially when the boiler load is lower than 50% of the BMCR working condition, it will cause the bed of the desulfurization tower to collapse and cause the system to fail to operate normally
[0012](2) The desulfurization efficiency is low, even if the system is running normally, it barely meets the ultra-low requirements of the current national environmental protection standards
[0013] (3) The process route is long, the subsystems are complicated, there are many operating equipment, and there are many fault points, especially the desulfurization ash circulation system is unstable, ash leakage, equipment Jamming occurs frequently, and operation and maintenance costs are high
High initial investment and large floor area

Method used

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  • Compartment turbulent bed desulfurization, denitrification and dust removal device and process thereof
  • Compartment turbulent bed desulfurization, denitrification and dust removal device and process thereof
  • Compartment turbulent bed desulfurization, denitrification and dust removal device and process thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0036] This embodiment provides a sub-compartment turbulent bed desulfurization, denitrification and dust removal device. The sub-compartments are two rows of sub-compartments arranged vertically. The middle of the two rows of sub-compartments is a public flue. There is a compartment entrance baffle door 2, and a compartment exit baffle door 10 is arranged above;

[0037] The two columns of chambers are symmetrical and identical in structure, including the ash collection area, turbulent overflow area, ammonia injection area and dust removal area from bottom to top; the entrance baffle door 2 of the public flue chamber has air flow on the flue gas side Evenly distributed plates and baffles allow the flue gas to enter the turbulent overflow area.

[0038] as attached figure 1As shown, in some embodiments, the warehouses are eight warehouses, and the eight warehouses are arranged in two rows, with four on one side, and the middle of the two rows of warehouses is a public flue di...

Embodiment 2

[0051] This embodiment provides a process for desulfurization, denitrification and dust removal with a turbulent bed in separate chambers. The process is carried out in the device for desulfurization, denitrification and dust removal in a turbulent bed with separate chambers described in Embodiment 1.

[0052] It includes the following steps: the original flue gas containing a large amount of SOx, NOx and dust enters the chamber through the baffle door 2 at the entrance of the chamber, then passes through the air distribution plate and the baffle plate, and then passes through the turbulent overflow area and the ammonia injection area in sequence And the dust removal area, after purification, it is discharged.

[0053] Such as figure 1 As shown, it specifically passes through the lower turbulent bed of powdered activated coke 4, the upper turbulent bed of powdered activated coke 6 to the lower part of the ammonia injection grid layer. This process lasts 22 seconds. The powder...

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Abstract

The invention relates to the field of desulfurization and denitrification, and particularly provides a compartment turbulent bed desulfurization, denitrification and dust removal device and a process thereof. Compartments are two columns of compartments which are vertically arranged, a public flue is arranged between the two columns of compartments, a compartment inlet baffle door is arranged below the public flue, and a compartment outlet baffle door is arranged above the public flue; two rows of compartments are of a same symmetrical structure, and each compartment sequentially comprises an ash collecting area, a turbulence overflow area, an ammonia spraying area and a dust removing area from bottom to top; and an airflow uniform distribution plate and a baffle plate are arranged on the flue gas outlet side of the compartment inlet baffle door of the public flue, so that flue gas enters the turbulence overflow area. In order to overcome various defects of a flue gas treatment technology in the prior art, the invention provides a dry-type flue gas treatment device and process which integrate desulfurization, denitration and dust removal functions and can adapt to large-range fluctuation of boiler loads.

Description

technical field [0001] The present disclosure relates to the field of desulfurization and denitrification, and specifically provides a desulfurization, denitrification and dedusting device and a process thereof with a compartmental turbulent bed. Background technique [0002] The statements herein merely provide background information related to the present disclosure and may not necessarily constitute prior art. [0003] Coal-fired power generation boilers, steelmaking and sintering machines, and cement kilns all produce flue gas containing a large amount of pollutants, the main pollutant of which is generally SO x , NOx and dust, etc. If the flue gas is directly discharged into the atmosphere without treatment, it will cause serious pollution to the environment. Therefore, the treatment of the above-mentioned flue gas pollutants has become an extremely important link in the production process of industries such as electric power, steel and building materials. x There are...

Claims

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Application Information

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IPC IPC(8): B01D53/86B01D53/56B01D53/83B01D53/06B01D46/02B01D46/48
CPCY02A50/20
Inventor 张广海宋健豪秦雪莉孙鹏贺文腾宋德升马春元张立强
Owner 山东祥桓环境科技有限公司
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