CN211800052U - Desulfurization, denitrification and dust removal integrated flue gas treatment device for cement kiln - Google Patents
Desulfurization, denitrification and dust removal integrated flue gas treatment device for cement kiln Download PDFInfo
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- CN211800052U CN211800052U CN202020143769.XU CN202020143769U CN211800052U CN 211800052 U CN211800052 U CN 211800052U CN 202020143769 U CN202020143769 U CN 202020143769U CN 211800052 U CN211800052 U CN 211800052U
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Abstract
The utility model discloses a SOx/NOx control dust removal integration flue gas treatment device for cement kiln, including connecting in orderThe kiln tail preheater, the inlet flue and the comprehensive reactor are characterized in that a reducing agent jet orifice, a heavy metal/dioxin jet orifice and a deacidification agent jet orifice are arranged on the inlet flue, the comprehensive reactor comprises a reaction tank and a double-layer filtering sleeve arranged in the reaction tank, and the double-layer filtering sleeve comprises an outer-layer high-temperature-resistant filtering pipe and an inner-layer high-temperature-resistant filtering pipe soaked with a catalyst. The utility model discloses can remove SOx and NOx and take off dioxin and dust simultaneously, dust, NOx, SO in the flue gas after synthesizing the reactor2The pollutants are greatly reduced, the emission concentration meets the requirement of ultralow emission, the technological process of desulfurization, denitrification and dust removal of the cement kiln is simplified, the running resistance of the system is reduced, and the purposes of saving investment and running cost are achieved.
Description
Technical Field
The utility model relates to a field is administered to cement kiln tail flue gas, specifically is a desulfurization denitration dust removal integration flue gas is administered device for cement kiln.
Background
The temperature of the flue gas at the outlet of the preheater at the kiln tail of the cement kiln is as high as 300-330 ℃, and the flue gas has large quantity and high dust content (as high as 80-120 g/Nm)3) The content of alkaline earth metal and alkali metal is high (the content of CaO is more than 40 percent), the ash viscosity is high, particularly, the flue gas of solid waste is treated cooperatively, the pollutant components are very complex, and the like, and the flue gas contains harmful components such as chlorine, sulfur, nitrogen oxide, dust, heavy metal, dioxin, and the like. The high-temperature SCR denitration device is built at the outlet of the kiln tail preheater, the large catalyst volume brings large occupied area of the reactor, the high-dust environment easily causes the catalyst to be worn, blocked and poisoned, the ash removal device has high operation cost and high failure rate, and the risk of kiln shutdown treatment is easily brought; when the dust removal device is additionally arranged to solve the high-dust problem, the defects that the traditional bag-type dust remover is difficult to bear high temperature, the electric dust remover is low in operation efficiency, large in occupied area and the like are faced, and the problem that high-concentration carbon monoxide in solid waste flue gas brings about safe use of the electric dust remover is cooperatively treated; limestone/gypsum method flue gas wet desulphurization system installed at rear endSO as to effectively remove SO in the flue gas2The removal efficiency can reach 97 percent, but the defects of large water consumption, high investment and operation cost and the like exist.
Particularly, at present, when a lot of domestic wastes are treated cooperatively by using a cement kiln, pollutants such as dioxin, dust, heavy metal pollution and the like are easily generated by burning, and the method is also a new problem faced by cooperative treatment in the cement industry at present.
If different removing devices are additionally arranged aiming at different pollutants, the problem of multi-pollution treatment is solved by connecting different removing devices in series, and the defects of high investment cost, large floor area, complex flue gas system, excessively complex operation and maintenance and the like exist.
SUMMERY OF THE UTILITY MODEL
The to-be-solved technical problem of the utility model is to provide a SOx/NOx control dust removal integration flue gas treatment device for cement kiln realizes that sulfur dioxide, dust, nitrogen oxide, dioxin integration desorption are administered under the high temperature condition, and process flow is short, need not reheat, and the system energy consumption is low.
The technical scheme of the utility model is that:
a desulfurization denitration dust removal integration flue gas treatment device for cement kiln, including kiln tail preheater, import flue and the comprehensive reactor of connecting in order from the past backward, the import flue on be provided with reductant injection, heavy metal/dioxin injection and deacidification agent injection, the comprehensive reactor include retort and set up the double-deck filter tube in the retort, double-deck filter tube including outer high temperature resistant filter tube and the inlayer soaks the high temperature resistant filter tube that has the catalyst.
The outlet of the comprehensive reactor is connected with the inlet of the kiln tail waste heat boiler through an outlet flue, the outlet of the kiln tail waste heat boiler is connected with the high-temperature fan, a connecting flue is connected between the inlet flue and the outlet flue, a first switch valve is arranged on the inlet flue, a second switch valve is arranged on the outlet flue, and a third switch valve is arranged on the connecting flue.
And the inlet flue and the outlet flue are respectively provided with a temperature measuring element, a pressure measuring element and a CEMS monitoring instrument.
The reducing agent injection port is connected with an outlet of the reducing agent injection device, and an inlet of the reducing agent injection device is connected with the reducing agent storage tank; the heavy metal/dioxin adsorbent injection port is connected with an outlet of the adsorbent injection device, and an inlet of the adsorbent injection device is connected with the adsorbent storage tank; the deacidification agent jet orifice is connected with the outlet of the deacidification agent jet device, and the inlet of the deacidification agent jet device is connected with the deacidification agent storage tank.
The reducing agent storage tank is connected with an inlet of the reducing agent injection device through a reducing agent delivery pump, an outlet of the compressed air storage tank is connected with an inlet of the reducing agent injection device through a compressed air supply regulating valve, and a reducing agent metering and discharging device is arranged on a connecting pipeline between the reducing agent delivery pump and the inlet of the reducing agent injection device; the outlet of the adsorbent storage tank is connected with the inlet of the adsorbent injection device through a first Roots blower, and the outlet of the adsorbent storage tank is provided with an adsorbent metering and discharging device; the outlet of the deacidification agent storage tank is connected with the inlet of the deacidification agent spraying device through a second Roots blower, and the outlet of the deacidification agent storage tank is provided with a deacidification agent metering and discharging device.
The bottom of the reaction tank of the comprehensive reactor is of an ash bucket structure, the reaction tank of the comprehensive reactor is also internally provided with an ash removal device, and an ash outlet of the ash bucket is connected with an ash storage device through an ash conveying Roots blower.
The utility model has the advantages that:
(1) the double-layer filtering sleeve of the comprehensive reactor comprises an outer-layer high-temperature-resistant filtering pipe and an inner-layer high-temperature-resistant filtering pipe impregnated with the catalyst, flue gas firstly removes dust through the outer layer, the problems of dust blockage and poison inactivation caused by arrangement of the traditional catalyst in the reactor are avoided, and the service life is prolonged;
(2) the utility model is arranged at the high-temperature flue gas section at the tail of the cement kiln, fully utilizes the heat of the flue gas at the tail of the kiln and considers the optimal use temperature range of the catalyst, thereby avoiding the problem of flue gas temperature rise and saving energy consumption;
(3) the utility model is suitable for the treatment and removal of pollutants such as dioxin, heavy metal pollution and the like easily generated by burning when solid wastes such as household garbage, sludge and the like and dangerous wastes are cooperatively treated by the cement kiln;
(4) the utility model discloses a desulfurization denitration dust remover that cement kiln multiple pollutants was administered removes dioxin integration desorption, has simplified process flow, has reduced the running resistance, has hanged down operation and maintenance cost.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Referring to fig. 1, the desulfurization, denitrification and dust removal integrated flue gas treatment device for the cement kiln comprises a kiln tail preheater 1, an inlet flue 2 and a comprehensive reactor 3 which are sequentially connected from front to back, wherein a reducing agent injection port, a heavy metal/dioxin injection port and a deacidification agent injection port are arranged on the inlet flue 2, an outlet of the comprehensive reactor 3 is connected with an inlet of a kiln tail waste heat boiler 5 through an outlet flue 4, an outlet of the kiln tail waste heat boiler 5 is connected with a high-temperature fan 6, a connecting flue 7 is connected between the inlet flue 2 and the outlet flue 4, a first switch valve 8 is arranged on the inlet flue 2, a second switch valve 9 is arranged on the outlet flue 4, a third switch valve 10 is arranged on the connecting flue 7, temperature measuring elements 11, pressure measuring elements 12 and a CEMS monitoring instrument 13 are respectively arranged on the inlet flue 2 and the outlet flue 4, the comprehensive reactor 3 comprises a reaction tank and a double-layer filter sleeve arranged in the, the double-layer filtering sleeve comprises an outer-layer high-temperature-resistant filtering pipe and an inner-layer high-temperature-resistant filtering pipe which is impregnated with a catalyst, the bottom of the reaction tank of the comprehensive reactor is of an ash bucket structure, an ash cleaning device is further arranged in the reaction tank of the comprehensive reactor 3, and an ash outlet of the ash bucket is connected with an ash storage device 15 through an ash conveying roots fan 14.
The reducing agent injection port is connected with an outlet of the reducing agent injection device 16, the reducing agent storage tank 17 is connected with an inlet of the reducing agent injection device 16 through a reducing agent delivery pump 18, an outlet of a compressed air storage tank 20 is connected with an inlet of the reducing agent injection device 16 through a compressed air supply adjusting valve 21, and a reducing agent metering and discharging device 19 is arranged on a connecting pipeline between the reducing agent delivery pump 18 and the inlet of the reducing agent injection device 16; the heavy metal/dioxin adsorbent injection port is connected with an outlet of the adsorbent injection device 22, an outlet of the adsorbent storage tank 23 is connected with an inlet of the adsorbent injection device 22 through a first roots blower 24, and an adsorbent metering and discharging device 25 is arranged at the outlet of the adsorbent storage tank 23; the deacidification agent jet orifice is connected with the outlet of the deacidification agent jet device 26, the outlet of the deacidification agent storage tank 27 is connected with the inlet of the deacidification agent jet device 26 through a second Roots blower 28, and the outlet of the deacidification agent storage tank 27 is provided with a deacidification agent metering and discharging device 29.
The desulfurization, denitrification and dust removal integrated flue gas treatment method for the cement kiln specifically comprises the following steps:
(1) firstly, opening a first switch valve 8 and a second switch valve 9, closing a third switch valve 10, and discharging high-temperature high-dust flue gas from a kiln tail preheater 1 and then entering a comprehensive reactor 3 through an inlet flue 2;
(2) spraying a denitration reducing agent (ammonia water with the concentration of 20-25% or urea solution with the concentration of 20%) atomized by compressed air into the inlet flue 2 through a reducing agent injection port to be mixed with flue gas, fully gasifying the denitration reducing agent by utilizing the heat of high-temperature flue gas, fully mixing the gasified denitration reducing agent with the flue gas, then feeding the gasified denitration reducing agent with the flue gas into the comprehensive reactor 3, spraying a heavy metal/dioxin adsorbent (active carbon powder) into the inlet flue 2 through a heavy metal/dioxin injection port to be mixed with the flue gas, then feeding the mixed flue gas into the comprehensive reactor 3, and spraying a deacidification agent (sodium bicarbonate powder with the granularity of more than 800 meshes) into the inlet flue 2 through a deacidification agent injection port to be mixed;
(3) the denitration reducing agent enters the integrated reactor 3The high-temperature resistant filter pipe which passes through the outer layer of the double-layer filter sleeve pipe and a catalyst layer on the high-temperature resistant filter pipe of the inner layer perform catalytic reduction reaction to reduce NOx in the flue gas into N2And H2O, reducing NOx emission concentration; after entering the comprehensive reactor 3, the heavy metal/dioxin adsorbent and the deacidification agent are covered on the high-temperature-resistant filter pipe on the outer layer of the double-layer filter sleeve, the specific surface area of the flue gas filter pipe provides a secondary adsorption reaction of the heavy metal/dioxin adsorbent and heavy metal and dioxin in flue gas, and provides a secondary neutralization reaction of the deacidification agent and acid gas in the flue gas, so that the emission concentration of the acid gas in the flue gas is reduced;
(4) the purified flue gas is discharged from an outlet of the comprehensive reactor 3, enters a kiln tail waste heat boiler 5 through an outlet flue 4, and is discharged into a rear-stage process through a high-temperature fan 6;
(5) and on the premise of obtaining the optimal absorption reaction efficiency and dust removal efficiency, the comprehensive reactor 3 starts the ash cleaning device to blow the final reaction product and dust on the double-layer filtering sleeve of the comprehensive reactor into the ash hopper and store the final reaction product and dust in the ash hopper through the ash conveying roots blower 14 and the ash storage device 15.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (6)
1. A SOx/NOx control dust removal integration flue gas treatment device for cement kiln, its characterized in that: the device comprises a kiln tail preheater, an inlet flue and a comprehensive reactor which are sequentially connected from front to back, wherein the inlet flue is provided with a reducing agent jet orifice, a heavy metal/dioxin jet orifice and a deacidification agent jet orifice, the comprehensive reactor comprises a reaction tank and a double-layer filtering sleeve arranged in the reaction tank, and the double-layer filtering sleeve comprises an outer-layer high-temperature-resistant filtering pipe and an inner-layer high-temperature-resistant filtering pipe impregnated with a catalyst.
2. The desulfurization, denitrification and dedusting integrated flue gas treatment device as claimed in claim 1, which is characterized in that: the outlet of the comprehensive reactor is connected with the inlet of the kiln tail waste heat boiler through an outlet flue, the outlet of the kiln tail waste heat boiler is connected with the high-temperature fan, a connecting flue is connected between the inlet flue and the outlet flue, a first switch valve is arranged on the inlet flue, a second switch valve is arranged on the outlet flue, and a third switch valve is arranged on the connecting flue.
3. The desulfurization, denitrification and dedusting integrated flue gas treatment device as claimed in claim 2, which is characterized in that: and the inlet flue and the outlet flue are respectively provided with a temperature measuring element, a pressure measuring element and a CEMS monitoring instrument.
4. The desulfurization, denitrification and dedusting integrated flue gas treatment device as claimed in claim 1, which is characterized in that: the reducing agent injection port is connected with an outlet of the reducing agent injection device, and an inlet of the reducing agent injection device is connected with the reducing agent storage tank; the heavy metal/dioxin adsorbent injection port is connected with an outlet of the adsorbent injection device, and an inlet of the adsorbent injection device is connected with the adsorbent storage tank; the deacidification agent jet orifice is connected with the outlet of the deacidification agent jet device, and the inlet of the deacidification agent jet device is connected with the deacidification agent storage tank.
5. The desulfurization, denitrification and dedusting integrated flue gas treatment device as claimed in claim 4, which is characterized in that: the reducing agent storage tank is connected with an inlet of the reducing agent injection device through a reducing agent delivery pump, an outlet of the compressed air storage tank is connected with an inlet of the reducing agent injection device through a compressed air supply regulating valve, and a reducing agent metering and discharging device is arranged on a connecting pipeline between the reducing agent delivery pump and the inlet of the reducing agent injection device; the outlet of the adsorbent storage tank is connected with the inlet of the adsorbent injection device through a first Roots blower, and the outlet of the adsorbent storage tank is provided with an adsorbent metering and discharging device; the outlet of the deacidification agent storage tank is connected with the inlet of the deacidification agent spraying device through a second Roots blower, and the outlet of the deacidification agent storage tank is provided with a deacidification agent metering and discharging device.
6. The desulfurization, denitrification and dedusting integrated flue gas treatment device as claimed in claim 1, which is characterized in that: the bottom of the reaction tank of the comprehensive reactor is of an ash bucket structure, the reaction tank of the comprehensive reactor is also internally provided with an ash removal device, and an ash outlet of the ash bucket is connected with an ash storage device through an ash conveying Roots blower.
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| Application Number | Priority Date | Filing Date | Title |
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| CN202020143769.XU CN211800052U (en) | 2020-01-22 | 2020-01-22 | Desulfurization, denitrification and dust removal integrated flue gas treatment device for cement kiln |
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| CN202020143769.XU CN211800052U (en) | 2020-01-22 | 2020-01-22 | Desulfurization, denitrification and dust removal integrated flue gas treatment device for cement kiln |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111167308A (en) * | 2020-01-22 | 2020-05-19 | 合肥中亚环保科技有限公司 | Desulfurization, denitrification and dust removal integrated flue gas treatment device and method for cement kiln |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111167308A (en) * | 2020-01-22 | 2020-05-19 | 合肥中亚环保科技有限公司 | Desulfurization, denitrification and dust removal integrated flue gas treatment device and method for cement kiln |
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