Kiln gas semi-dry process defluorination desulphurization dedusting equipment
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A technology of desulfurization and dust removal equipment and semi-dry method, which is applied in the direction of gas treatment, separation methods, chemical instruments and methods, etc., can solve the problems of poor defluorination and desulfurization effects, waste of raw materials, inconvenient dust collection and transportation, etc., and delay the drying time , Improve desulfurization efficiency and save manpower
Active Publication Date: 2018-08-07
济南国器工程技术有限公司
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[0005] In order to solve the above technical problems, the present invention provides a semi-dry method of defluorination, desulfurization and dust removal equipment for kiln flue gas to solve the problem of poor defluorination and desulfurization effect and serious waste of raw materials And the problem of inconvenient transportation of dust collection
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[0039] as attached figure 1 to attach Figure 6 shown
[0040] The present invention provides semi-dry defluorination, desulfurization and dedusting equipment for flue gas in a kiln, which includes a process water tank 1, a process water pump 2, a primary process water flow meter 3, a Venturi section structure 4 of a defluorination tower, a leak-proof cap 5, and a waste Dust packing vehicle structure 6, defluorination tower structure 7, secondary process water flow meter 8, defluorination tower outlet flue 9, cyclone separator 10, cyclone separator outlet flue 11, discharge pipe 12, primary exhaust Smoke pipe 13, defluorination tower return chute 14, lime powder bin structure 15, primary connecting pipe 16, manual valve 17, desulfurization tower outlet flue 18, smoke outlet pipe 19, desulfurization tower Venturi section 20, desulfurization lower layer Nozzle 21, desulfurization upper nozzle 22, desulfurization tower 23, flue gas induced draft fan 24, bag filter structure 25,...
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Abstract
The invention provides kiln gas semi-dry process defluorination desulphurization dedusting equipment. The kiln gas semi-dry process defluorination desulphurization dedusting equipment comprises a technology water tank, a technology water pump, a first stage technology water flowmeter, a defluorination tower Venturi segment structure, a leakproof cap, a waste dust packaged conveying vehicle structure, a defluorination tower structure, a second stage technology water flowmeter, a defluorination tower outlet flue, a cyclone separator, a cyclone separator outlet flue, a discharge pipe, a first stage smoke discharge pipe, a defluorination tower material return inclined groove, a lime powder cabin structure, a first stage connecting pipe, a hand-operated valve, a desulphurization outlet flue, asmoke outlet pipe, a desulphurization Venturi segment, a desulphurization lower layer nozzle, a desulphurization upper layer nozzle, a desulphurization tower, a flue gas induced draught fan, a cloth bag dedusting cylinder structure, a desulphurization material return inclined groove, and a second stage smoke discharge pipe. According to the kiln gas semi-dry process defluorination desulphurizationdedusting equipment, the defluorination tower and the desulphurization tower are adopted, it is beneficial for defluorination and then desulphurization, interaction of defluorination and desulphurization is avoided, defluorination and desulphurization effect is improved; the mechanical valve, a flue gas inlet pipe, and a filter screen are adopted, so that it is beneficial for control of smoke introduction speed.
Description
technical field [0001] The invention belongs to the technical field of environmental protection dust removal equipment, and in particular relates to a kiln flue gas semi-dry defluorination, desulfurization and dust removal equipment. Background technique [0002] The existing coal-fired flue gas purification is mainly desulfurization. The desulfurization device generally includes a reactor nested in the shell. The reactor is equipped with an absorption liquid atomization spray device. The flue gas enters from the upper end of the reactor and is mixed with the fog. After the absorbed liquid (generally ammonia water) is reacted and absorbed, it enters the interlayer between the reactor and the shell through the dehydration demister at the lower end of the reactor, and then is output from the flue gas outlet provided on the shell. On the one hand, due to the short reaction process, the existing desulfurization devices cannot meet the treatment of a large amount of flue gas cont...
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