CN105833658A - Lead-removing purification system for non-ferrous metal smelting waste gas - Google Patents

Lead-removing purification system for non-ferrous metal smelting waste gas Download PDF

Info

Publication number
CN105833658A
CN105833658A CN201610384955.0A CN201610384955A CN105833658A CN 105833658 A CN105833658 A CN 105833658A CN 201610384955 A CN201610384955 A CN 201610384955A CN 105833658 A CN105833658 A CN 105833658A
Authority
CN
China
Prior art keywords
gas
lead
reactor
spin resonance
electron spin
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201610384955.0A
Other languages
Chinese (zh)
Inventor
杨俊锋
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN201610384955.0A priority Critical patent/CN105833658A/en
Publication of CN105833658A publication Critical patent/CN105833658A/en
Pending legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/007—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by irradiation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/02—Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
    • B01D46/023—Pockets filters, i.e. multiple bag filters mounted on a common frame
    • C—CHEMISTRY; METALLURGY
    • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B13/00—Obtaining lead
    • C—CHEMISTRY; METALLURGY
    • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B7/00—Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
    • C22B7/005—Separation by a physical processing technique only, e.g. by mechanical breaking
    • C—CHEMISTRY; METALLURGY
    • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B7/00—Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
    • C22B7/02—Working-up flue dust
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
    • F27D17/004—Systems for reclaiming waste heat
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
    • F27D17/008—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases cleaning gases
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/60—Heavy metals or heavy metal compounds
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
    • B01D2257/708—Volatile organic compounds V.O.C.'s
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2258/00—Sources of waste gases
    • B01D2258/02—Other waste gases
    • B01D2258/025—Other waste gases from metallurgy plants
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2259/00—Type of treatment
    • B01D2259/80—Employing electric, magnetic, electromagnetic or wave energy, or particle radiation
    • B01D2259/806—Microwaves
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00—Technologies related to metal processing
    • Y02P10/25—Process efficiency

Abstract

The invention discloses a lead-removing purification system for non-ferrous metal smelting waste gas. The lead-removing purification system comprises a waste heat exchanger, a gas overheat protecting device, a thermal type gas mass flowmeter, a mixed gas flow regulating valve, a microwave electron spin resonance reactor, a bag-type dust collector, a VOC (volatile organic compounds) combustion treatment device, a flue gas water-washing and cooling tower and an induced draft fan. The lead-removing purification system for the non-ferrous metal smelting waste gas has the advantages that on the basis of creative use of an electron spin resonance characteristic of a metal lead element, covalent electrons in lead dust (mainly referring to lead oxides in various valent states ) can be in a spin resonance state under direct action of microwave radiation with a specific frequency to weaken a covalent bond in a molecule; at the moment, if a magnetized metal exists around the molecule, the covalent bond thereof can be broken and bonds to the surface of the magnetized metal again to form an elemental lead particle, and the elemental lead particle is subjected to simple centrifugal separation, in other words, the lead particle can be separated and recovered, so that resource recycling is achieved.

Description

A kind of non-ferrous metal metallurgy waste gas except lead cleaning system
Technical field
The present invention relates to a kind of non-ferrous metal metallurgy waste gas except lead cleaning system, belong to the exhaust-gas treatment field in environmental conservation.
Background technology
Lead is a kind of heavy metal element being widely present in human being's production life, uses from exploitation to finished product, and associated specialty reaches over one hundred kind.Lead contamination is more obvious in occupational environment, additionally, the aspect such as paint, the preservative of food processing industry and skin cosmetic the most all uses lead in building industry.
Meanwhile, lead is also the material that a kind of toxicity is the biggest, and many human organs can be brought harmful effect by lead, particularly to the lung of people, kidney, reproductive system, cardiovascular system.These impacts show as intelligence and decline (especially children for learning aspect being caused obvious problem), injury of kidney, sterile, miscarriage and hypertension, also can cause lead encephalopathy, angina abdominis, polyneuritis, hemolytic anemia etc..
But, owing to the generally existence of lead in environment, particularly environment and Lead in Air concentration in industrial development comparatively fast area increase, lead enters human body by food chain, causes human body and environment to suffer lead contamination.
Due to toxicity and the features of pollution of lead, requiring the highest to lead standard value in the environment, the use of lead is had and strictly limits by particularly western developed country.In the past few years, the annual production of China's lead reaches 1,350,000 tons, year consumption figure more than 80 ten thousand tons, be International Lead big producing country and consumption big country.But lead enterprise of China generally exists, and production technology falls behind, equipment modernization degree is low, lead resource waste and the present situation such as environmental pollution is serious.Although country takes some corresponding measures, but it is the most notable to produce effects.
In China, major part lead smelting enterprise mainly uses traditional little reverberatory furnace and blast furnace smelting process.Substantial amounts of lead dust, flue dust and sulfur dioxide is created in fusion process.Because it is not easily recycled, so major part is directly to discharge in atmosphere, the discharge of lead effusion thing causes the pollution to environment and air.
At present, what China used processes the method for lead in industrial waste gas mainly following three kinds:
(1) liquid absorption method: cardinal principle is to be imported to by lead dust in the dilute acetic acid solution of 1 ~ 3%, generates lead acetate by chemical reaction and precipitates.
(2) bag filter process: allow lead dust pass through porous body filtrate, completes to purify in the way of physics trapping.
(3) high-pressure electrostatic absorption method: by by charged for lead dust microgranule, and make it that directed movement to occur under the effect of electric field, thus reach the purpose of separation and collection.
The above-mentioned tradition universal existence initial investment of administering method is high with later stage O&M cost, lead dust treatment effeciency is unstable, trap filter equipment easily blocks, processes material consumption greatly and can produce the shortcomings such as leaded waste liquid in processing procedure.Therefore, it is necessary to break away from existing Treatment process route, innovated from the principle of purification treatment and changed, being developed the waste gas containing lead Treatment process of a kind of new type.
Summary of the invention
In order to solve problems present in prior art; this provide a kind of non-ferrous metal metallurgy waste gas except lead cleaning system, this system includes residual-heat exchanger, gas superheat protection device, thermal type gas quality flow meter, mixed gas flow regulation valve, microwave electron spin resonance reactor, fiber bag precipitator, VOC burning processing device, gas fume washing cooling tower, air-introduced machine etc.；nullWherein，Non-ferrous metal metallurgy waste gas enters residual-heat exchanger by gas piping，Overheated waste gas is made to be lowered the temperature and stablize at this through heat exchange action，And the after-heat obtained is available for utilizing，The outlet of residual-heat exchanger connects gas superheat protection device by gas piping，Its effect is when residual-heat exchanger fault or the EGT after heat exchange remain unchanged too high，Can temporarily disconnected gas circuit，Play the effect of protection back-end processing device，The outlet of gas superheat protection device connects thermal type gas quality flow meter by gas piping，Can be to exhaust gas flow、The information such as flow velocity carry out real-time monitoring record，The outlet of thermal type gas quality flow meter connects mixed gas flow regulation valve by gas piping，The actual concentrations of lead dust in waste gas is adjusted by the method importing air，And waste gas is diluted accurately cooling，The outlet of mixed gas flow regulation valve connects microwave electron spin resonance reactor by gas piping，The outlet of microwave electron spin resonance reactor connects fiber bag precipitator by gas piping，Other particulate pollutants in waste gas are removed further at this，The outlet of fiber bag precipitator connects VOC burning processing device by gas piping，The organic pollution in removing exhaust gas is removed by high-temp combustion process，The outlet of VOC burning processing device connects gas fume washing cooling tower by gas piping，At this, waste gas after processing is carried out further water washing cleaning and cooling，The outlet of gas fume washing cooling tower connects air-introduced machine by gas piping，The outlet of air-introduced machine connects atmospheric environment by gas piping；
Wherein, the shell of microwave electron spin resonance reactor is made up of carbon steel, its internal layer is coated with rubber flat plate and inhales ripple overcoat, reactor lower left quarter is provided with air intake valve, upper right quarter is provided with drain tap, the reactor upper left corner and position, the upper right corner are separately installed with 1 multicavity magnetron microwave generator, in the middle part of reactor, both sides are respectively provided with 1 rotary electric machine, it is connected with the magnetization ferrite stainless steel mesh being positioned at inside reactor via 2 driving connecting rods, reactor bottom is provided with 1 group of deslagging conveyer belt, deslagging conveyer belt is connected to waste residue row's mouth of reactor right lower quadrant；nullWaste gas containing lead dust enters inside reactor through the air intake valve of microwave electron spin resonance reactor lower left quarter，2 the multicavity magnetron microwave generators being positioned at the reactor upper left corner and the upper right corner are started working，The microwave radiation that frequency is 172.60MHz can be produced，It is fully radiated to whole inside reactor，In waste gas, the shared eletron of lead dust (mainly each oxides of lead) is by the radiation effects of this frequency microwave，Electron spin resonance phenomenon can occur，So that the covalent bond strength reduction in molecule，Simultaneously，Driven by the rotary electric machine being positioned at reactor both sides，Start to rotate at inside reactor through the magnetization ferrite stainless steel mesh of 2 driving connecting rod transmissions，With the lead dust molecule contacts that electron spin resonance occurs，Owing to occurring the lead dust surrounding molecules of electron spin resonance to also exist through magnetized metal object，Its covalent bond can be broken，And recombine as lead metal simple substance microgranule at magnetization ferritic stainless steel net surface，Drop on the deslagging conveyer belt of reactor bottom due to the dynamic produced centrifugal action of the not stall of magnetization ferrite stainless steel mesh，Waste residue row's mouth discharge reactor through deslagging tape transport to reactor right lower quadrant，And carry out recycling.
The dischargeable capacity of its microwave electron spin resonance reactor is 275m3, working pressure range is 0.10 ~ 0.95MPa, and operating temperature range is 105 ~ 300 DEG C.
Its microwave electron spin resonance reactor, the output of multicavity magnetron microwave generator is 1.32kW, and anode voltage is 4.25kV, and anode current is 300mA, and can produce microwave frequency is 172.60MHz, is about 9000 hours service life.
Its microwave electron spin resonance reactor, the running voltage of rotary electric machine is 380V, and output is 25kW, and rotation period is 5.0s.
Waste gas after being processed by native system, the removal efficiency of its lead dust is up to 97.5%.
It is an advantage of the current invention that:
(1) the electron spin resonance characteristic that make use of metallic lead element that native system is creative, when the shared eletron in lead dust is under the directly effect of a certain characteristic frequency microwave radiation, spin resonance phenomenon can occur, so that the covalent bond strength reduction in molecule, when it is with when coexisting through magnetized metal object, and its covalent bond can be broken, and recombine as lead metal simple substance microgranule on the surface of magnetizable metal thing, so that the lead dust in waste gas is removed, its removal efficiency is up to 99.5%.
(2) by the leaded granule generated after microwave electron spin resonance reactor for treatment, its density, much larger than the average density of waste gas, can be separated and recovered by the operation of easy inertial separation, onestep extraction metallic lead of going forward side by side, it is achieved that the cyclic utilization of waste.
(3) native system uses pure physical means that the lead dust in waste gas is carried out purified treatment, does not use any chemical substance, thus eliminates the risk introducing the pollutant new, harm is bigger.
(4) native system technology path is advanced, and occupation area of equipment is less, and treatment effect is good, and operation expense is the lowest, is conducive to popularization and application on a large scale.
Accompanying drawing explanation
Fig. 1 is the equipment schematic diagram of the present invention.
In figure: 1-residual-heat exchanger, 2-gas superheat protection device, 3-thermal type gas quality flow meter, 4-mixed gas flow regulation valve, 5-microwave electron spin resonance reactor, 6-fiber bag precipitator, 7-VOC burning processing device, 8-gas fume washing cooling tower, 9-air-introduced machine
Fig. 2 is the schematic diagram of microwave electron spin resonance reactor.
51-air intake valve, 52-multicavity magnetron microwave generator, 53-magnetization ferrite stainless steel mesh, 54-rotary electric machine, 55-driving connecting rod, 56-deslagging conveyer belt, 57-rubber flat plate inhale ripple overcoat, 58-drain tap, 59-waste residue row's mouth.
Detailed description of the invention
Non-ferrous metal metallurgy waste gas as shown in Figure 1 except lead cleaning system, this system includes residual-heat exchanger 1, gas superheat protection device 2, thermal type gas quality flow meter 3, mixed gas flow regulation valve 4, microwave electron spin resonance reactor 5, fiber bag precipitator 6, VOC burning processing device 7, gas fume washing cooling tower 8, air-introduced machine 9 etc.；nullWherein，Non-ferrous metal metallurgy waste gas enters residual-heat exchanger 1 by gas piping，Overheated waste gas is made to be lowered the temperature and stablize at this through heat exchange action，And the after-heat obtained is available for utilizing，The outlet of residual-heat exchanger 1 connects gas superheat protection device 2 by gas piping，Its effect is when residual-heat exchanger 1 fault or the EGT after heat exchange remain unchanged too high，Can temporarily disconnected gas circuit，Play the effect of protection back-end processing device，The outlet of gas superheat protection device 2 connects thermal type gas quality flow meter 3 by gas piping，Can be to exhaust gas flow、The information such as flow velocity carry out real-time monitoring record，The outlet of thermal type gas quality flow meter 3 connects mixed gas flow regulation valve 4 by gas piping，The actual concentrations of lead dust in waste gas is adjusted by the method importing air，And waste gas is diluted accurately cooling，The outlet of mixed gas flow regulation valve 4 connects microwave electron spin resonance reactor 5 by gas piping，The outlet of microwave electron spin resonance reactor 5 connects fiber bag precipitator 6 by gas piping，Other particulate pollutants in waste gas are removed further at this，The outlet of fiber bag precipitator 6 connects VOC burning processing device 7 by gas piping，The organic pollution in removing exhaust gas is removed by high-temp combustion process，The outlet of VOC burning processing device 7 connects gas fume washing cooling tower 8 by gas piping，At this, waste gas after processing is carried out further water washing cleaning and cooling，The outlet of gas fume washing cooling tower 8 connects air-introduced machine 9 by gas piping，The outlet of air-introduced machine 9 connects atmospheric environment by gas piping；Wherein, the shell of microwave electron spin resonance reactor 5 is made up of carbon steel, its internal layer is coated with rubber flat plate and inhales ripple overcoat 57, reactor lower left quarter is provided with air intake valve 51, upper right quarter is provided with drain tap 58, the reactor upper left corner and position, the upper right corner are separately installed with 1 multicavity magnetron microwave generator 52, in the middle part of reactor, both sides are respectively provided with 1 rotary electric machine 54, it is connected with the magnetization ferrite stainless steel mesh 53 being positioned at inside reactor via 2 driving connecting rods 55, reactor bottom is provided with 1 group of deslagging conveyer belt 56, deslagging conveyer belt 56 is connected to waste residue row's mouth 59 of reactor right lower quadrant；nullWaste gas containing lead dust enters inside reactor through the air intake valve 51 of microwave electron spin resonance reactor 5 lower left quarter，2 the multicavity magnetron microwave generators 52 being positioned at the reactor upper left corner and the upper right corner are started working，The microwave radiation that frequency is 172.60MHz can be produced，It is fully radiated to whole inside reactor，In waste gas, the shared eletron of lead dust (mainly each oxides of lead) is by the radiation effects of this frequency microwave，Electron spin resonance phenomenon can occur，So that the covalent bond strength reduction in molecule，Simultaneously，Driven by the rotary electric machine 54 being positioned at reactor both sides，Start to rotate at inside reactor through the magnetization ferrite stainless steel mesh 53 of 2 driving connecting rods 55 transmission，With the lead dust molecule contacts that electron spin resonance occurs，Owing to occurring the lead dust surrounding molecules of electron spin resonance to also exist through magnetized metal object，Its covalent bond can be broken，And recombine as lead metal simple substance microgranule on magnetization ferrite stainless steel mesh 53 surface，Drop on the deslagging conveyer belt 56 of reactor bottom due to the dynamic produced centrifugal action of the not stall of magnetization ferrite stainless steel mesh 53，The waste residue row's mouth 59 being delivered to reactor right lower quadrant through deslagging conveyer belt 56 discharges reactor，And carry out recycling；Wherein, the dischargeable capacity of microwave electron spin resonance reactor 5 is 275m3, working pressure range is 0.10 ~ 0.95MPa, and operating temperature range is 105 ~ 300 DEG C；Wherein, microwave electron spin resonance reactor 5, the output of multicavity magnetron microwave generator 52 is 1.32kW, and anode voltage is 4.25kV, and anode current is 300mA, and can produce microwave frequency is 172.60MHz, is about 9000 hours service life；Wherein, microwave electron spin resonance reactor 5, the running voltage of rotary electric machine 54 is 380V, and output is 25kW, and rotation period is 5.0s.
Waste gas after being processed by native system, the removal efficiency of its lead dust is up to 99.5%.

Claims (6)

1. a non-ferrous metal metallurgy waste gas except lead cleaning system; it is characterized in that, this system includes residual-heat exchanger, gas superheat protection device, thermal type gas quality flow meter, mixed gas flow regulation valve, microwave electron spin resonance reactor, fiber bag precipitator, VOC burning processing device, gas fume washing cooling tower, air-introduced machine etc.；nullWherein，Non-ferrous metal metallurgy waste gas enters residual-heat exchanger by gas piping，The outlet of residual-heat exchanger connects gas superheat protection device by gas piping，The outlet of gas superheat protection device connects thermal type gas quality flow meter by gas piping，The outlet of thermal type gas quality flow meter connects mixed gas flow regulation valve by gas piping，The outlet of mixed gas flow regulation valve connects microwave electron spin resonance reactor by gas piping，The outlet of microwave electron spin resonance reactor connects fiber bag precipitator by gas piping，The outlet of fiber bag precipitator connects VOC burning processing device by gas piping，The outlet of VOC burning processing device connects gas fume washing cooling tower by gas piping，The outlet of gas fume washing cooling tower connects air-introduced machine by gas piping，The outlet of air-introduced machine connects atmospheric environment by gas piping.
Non-ferrous metal metallurgy waste gas the most according to claim 1 except lead cleaning system, it is characterized in that, microwave electron spin resonance reactor lower left quarter is provided with air intake valve, upper right quarter is provided with drain tap, the reactor upper left corner and position, the upper right corner are separately installed with 1 multicavity magnetron microwave generator, in the middle part of reactor, both sides are respectively provided with 1 rotary electric machine, it is connected with the magnetization ferrite stainless steel mesh being positioned at inside reactor via 2 driving connecting rods, reactor bottom is provided with 1 group of deslagging conveyer belt, and deslagging conveyer belt is connected to waste residue row's mouth of reactor right lower quadrant.
nullNon-ferrous metal metallurgy waste gas the most according to claim 1 except lead cleaning system，It is characterized in that，Waste gas containing lead dust enters inside reactor through the air intake valve of microwave electron spin resonance reactor lower left quarter，2 the multicavity magnetron microwave generators being positioned at the reactor upper left corner and the upper right corner are started working，The microwave radiation that frequency is 172.60MHz can be produced，It is fully radiated to whole inside reactor，In waste gas, the shared eletron of lead dust (being each oxides of lead) is by the radiation effects of this frequency microwave，Electron spin resonance phenomenon can occur，So that the covalent bond strength reduction in molecule，Driven by the rotary electric machine being positioned at reactor both sides simultaneously，Start to rotate at inside reactor through the magnetization ferrite stainless steel mesh of 2 driving connecting rod transmissions，With the lead dust molecule contacts that electron spin resonance occurs，Owing to occurring the lead dust surrounding molecules of electron spin resonance to also exist through magnetized metal object，Its covalent bond can be broken，And recombine as lead metal simple substance microgranule at magnetization ferritic stainless steel net surface，Drop on the deslagging conveyer belt of reactor bottom due to the dynamic produced centrifugal action of the not stall of magnetization ferrite stainless steel mesh，Waste residue row's mouth discharge reactor through deslagging tape transport to reactor right lower quadrant，And carry out recycling.
Non-ferrous metal metallurgy waste gas the most according to claim 1 except lead cleaning system, it is characterised in that the dischargeable capacity of microwave electron spin resonance reactor is 275m3, working pressure range is 0.10 ~ 0.95MPa, and operating temperature range is 105 ~ 300 DEG C.
Non-ferrous metal metallurgy waste gas the most according to claim 1 except lead cleaning system, it is characterized in that, the output of the multicavity magnetron microwave generator of microwave electron spin resonance reactor is 1.32kW, anode voltage is 4.25kV, anode current is 300mA, and generation microwave frequency is 172.60MHz.
Non-ferrous metal metallurgy waste gas the most according to claim 1 except lead cleaning system, it is characterised in that the running voltage of the rotary electric machine of microwave electron spin resonance reactor is 380V, and output is 25kW, and rotation period is 5.0s.
CN201610384955.0A 2016-06-02 2016-06-02 Lead-removing purification system for non-ferrous metal smelting waste gas Pending CN105833658A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610384955.0A CN105833658A (en) 2016-06-02 2016-06-02 Lead-removing purification system for non-ferrous metal smelting waste gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610384955.0A CN105833658A (en) 2016-06-02 2016-06-02 Lead-removing purification system for non-ferrous metal smelting waste gas

Publications (1)

Publication Number Publication Date
CN105833658A true CN105833658A (en) 2016-08-10

Family

ID=56596172

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610384955.0A Pending CN105833658A (en) 2016-06-02 2016-06-02 Lead-removing purification system for non-ferrous metal smelting waste gas

Country Status (1)

Country Link
CN (1) CN105833658A (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050034666A1 (en) * 2003-03-21 2005-02-17 Roman Chistyakov Plasma generation using multi-step ionization
JP2006032272A (en) * 2004-07-21 2006-02-02 Hosoda Denki:Kk Plasma treatment device
CN103262663A (en) * 2011-04-28 2013-08-21 东海橡塑工业株式会社 Microwave plasma generation device, and magnetron sputtering film deposition device using same
CN105396443A (en) * 2015-11-05 2016-03-16 张文国 Industrial refuse cracking incineration tail gas deacidifying treatment system

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050034666A1 (en) * 2003-03-21 2005-02-17 Roman Chistyakov Plasma generation using multi-step ionization
JP2006032272A (en) * 2004-07-21 2006-02-02 Hosoda Denki:Kk Plasma treatment device
CN103262663A (en) * 2011-04-28 2013-08-21 东海橡塑工业株式会社 Microwave plasma generation device, and magnetron sputtering film deposition device using same
CN105396443A (en) * 2015-11-05 2016-03-16 张文国 Industrial refuse cracking incineration tail gas deacidifying treatment system

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
胡一贯: "电子回旋共振等离子技术", 《半导体技术》 *

Similar Documents

Publication Publication Date Title
CN105749679A (en) High-temperature smoke dust removal method and system
CN108310955A (en) A method of mercury is recycled in situ from non-ferrous metal metallurgy mercury fume
CN108237137A (en) Flying dust mercury removal device and demercuration method
CN103130234B (en) Device and method for recovering boron oxide and carbon monoxide from boron carbide smelting tail gas
CN105771997A (en) Preparation method and application of dealkalized red mud
CN109331625A (en) Vanadium trioxide restores tail gas purification tower
CN107233783A (en) A kind of hot chamber machine useless cigarette processing system of waste gas
CN106944259A (en) A kind of industrial smoke dust collection method
CN110354670A (en) A kind of boiler with tailed flue gas takes off white system and method
CN105944479A (en) Purifying device for lead-containing sulfur-containing flue gas
CN105833658A (en) Lead-removing purification system for non-ferrous metal smelting waste gas
CN105833653A (en) Lead-removing purification method for non-ferrous metal smelting waste gas
CN201729772U (en) Limekiln for processing and recycling waste-gas
CN102631830A (en) Method and device for reducing wastewater amount of smelting smoke acid-making process
CN104075586A (en) Process and equipment for co-operatively removing dust and dioxin
CN204891506U (en) Aluminium is multiple -effect dust collector for lime -ash
CN213747840U (en) Hazardous waste high-temperature smelting waste gas waste heat recovery and pollutant treatment device
CN203043793U (en) Dust-collecting purifying device for flue gas
CN109173649A (en) A kind of coke oven exhaust gas processing method and system
CN202666636U (en) Smoke-gas treating system for ferromolybdenum smelting
CN208115429U (en) Flue gas processing device
CN206778128U (en) The exhaust treatment system that a kind of metal sludge is smelted
CN108187429B (en) Purification device and purification method for flue gas in molybdenum concentrate drying process
CN207493429U (en) A kind of betel nut preliminary working smoke processing system
CN105688565A (en) Metallurgical mine calcining tail gas purifying and heat recycling device and process

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20160810

RJ01 Rejection of invention patent application after publication