CN205926020U - Electricity dust collecting equipment and system - Google Patents

Electricity dust collecting equipment and system Download PDF

Info

Publication number
CN205926020U
CN205926020U CN201620735439.3U CN201620735439U CN205926020U CN 205926020 U CN205926020 U CN 205926020U CN 201620735439 U CN201620735439 U CN 201620735439U CN 205926020 U CN205926020 U CN 205926020U
Authority
CN
China
Prior art keywords
temperature
gas
electric dust
dust
regenerating unit
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.)
Active
Application number
CN201620735439.3U
Other languages
Chinese (zh)
Inventor
朱书成
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.)
Henan Longcheng Coal Efficient Technology Application Co Ltd
Original Assignee
Henan Longcheng Coal Efficient Technology Application Co Ltd
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 Henan Longcheng Coal Efficient Technology Application Co Ltd filed Critical Henan Longcheng Coal Efficient Technology Application Co Ltd
Priority to CN201620735439.3U priority Critical patent/CN205926020U/en
Application granted granted Critical
Publication of CN205926020U publication Critical patent/CN205926020U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Electrostatic Separation (AREA)

Abstract

The utility model relates to an electricity dust collecting equipment and system in pyrolysis of coal field, living beings pyrolysis field, electricity dust collecting equipment, including electric dust collecting equipment body, electricity dust collecting equipment body sets up preheating device, preheating device is whole preheating device, preheating device is high -temperature gas pipes, high -temperature gas pipes is connected with the inside cavity of electric dust collecting equipment body, electricity dust collecting equipment body sets up regenerating unit, regenerating unit is physics regenerating unit and/or chemical regenerating unit, physics regenerating unit constructs for the motivation of scraping that sets up on easily attaching grey part, chemistry regenerating unit is oxygen -poor gas input mechanism. The utility model discloses a to the whole back of preheating of electric dust collecting equipment body for interior each temperature regional, each parts of dust collecting equipment is relatively evenly unanimous, and the high innage dirt gas molecule of high temperature that gets into in the great environment of temperature unanimity can face still less the temperature variation and the change of state, even under the effect of dust, also the local space change of state of more difficult emergence appears with condensing.

Description

Electric dust-removing equipment and system
Technical field
The utility model is related to electric dust-removing equipment technical field, especially pyrolysis of coal field, the electricity in biomass pyrolytic field Cleaner and system.
Background technology
Electric precipitation is one kind of dedusting method.Dusty gas is electrically isolated when high-voltage electrostatic field, grit with negative After negative electricity on ions binding band, tend to anode surface electric discharge and deposit.Metallurgical, chemical etc. industry in order to purification gas or return Receive useful grit.Make gas ionization using electrostatic field so that dust particles are adsorbed onto the collecting method on electrode.In highfield Middle air molecule is ionized as cation and electronics, and electronics marches on towards in anode process and runs into grit, makes that grit is negatively charged to be adsorbed onto Positive pole is collected.It is usually used in factory with coal as fuel, power station, collect the coal ash in flue gas and dust.It is used for collecting in metallurgy The oxide of tin, zinc, lead, aluminium etc..Electric cleaner is the indispensable corollary equipment in thermal power plant, and its function is by combustion stove or combustion The particle flue dust that thermo oil boiler discharges in flue gas is removed, thus the fume amount that enter in atmosphere is greatly lowered, this is to change Kind environmental pollution, improves the important environmental protection equipment of air quality.Its operation principle is that flue gas passes through electric cleaner agent structure So as to flue dust is positively charged during front flue, then electric precipitation flue gas in Luohe enters the electric cleaner of setting multilayer cathode plate and leads to Road.Due to the mutual suction-operated of positively charged flue dust and negative electrode electroplax, the particle flue dust in flue gas is made to adsorb on negative electrode, fixed When hit minus plate, make to have certain thickness flue dust and fall under electric cleaner structure under the double action of deadweight and vibration In the ash bucket of side, thus reaching the purpose removing the flue dust in flue gas.
Electric cleaner has lot of advantages:(1) purification efficiency is high, is capable of the grain dust of more than 0.01 micron of paved set.? Required purification efficiency can be met by different operating parameters in design.(2) drag losses is little, typically in 20 millis Below meter water column, and cyclone dust collectors compare, even if considering power supply unit and vibration body power consumption, its total power consumption still compares Little.(3) allow operation temperature high, as SHWB type circuit dirt device preferably allows for 250 DEG C of operation temperature, other types also reach 350~400 DEG C or higher.(4) processing gas scope amount is big.(5) operation can be fully achieved automatically control.
Often produce high-temperature dusty gas in chemical industry, oil, metallurgy, building materials, oil shale, biological pyrolysis art, especially Be generate coal tar oil gas in low order pyrolysis of coal, during decomposition gas, low-order coal material rolled with less particulate form or Person is pyrolyzed under air-flow drive, and in the admixture of gas producing in pyrolytic process, coal dust content is very high, and contains in mixed gas Carbons easily separate out material such as tar Jiao, class bituminous material can be existed with gaseous state only in the environment of high temperature, and temperature is slightly Too low or environment, once changing, is easy for separating out from gaseous mixture and is attached on filter mechanism, causes filter mechanism to be lost Filter function, makes production cannot continue.Recent decades, the mixed oil and gas dust removal problem of high Dust Capacity, main in dozens of both at home and abroad Under the effort of scientific research institution of country, also fail all the time to obtain effectively solving, cause low-order coal pyrolytic technique can not form industry Metaplasia is produced, and directly affects the overall Coal Industrial general layout of our times, and the low-order coal of staggering amount can not obtain clean and effective and utilize.
In coal tar, colloid and asphalt content are higher, and resin and asphalt is the predecessor of coking.Resin and asphalt Cellular construction be all structure with polycyclic aromatic ring system as core, both difference be only molecular structure and molecular size range not With.When coal tar pyrolysis effusion from coal in a gaseous form, react below generation in filtering bodies:Asphalitine bulky grain thermal depolymerization For asphalitine little particle, asphalitine little particle pyrolytic reaction generates fused ring compound or polycondensation reaction graphitization forms coke, It is oil distillate that fused ring compound is pyrolyzed or polycondensation is coke.
CN104147862A is to solve problem present in above-mentioned technique it is proposed that a kind of high-temperature oil gas, vapor, containing The filtering dust system of the gaseous mixture of the easy precipitate of carbons, including the airtight disengagement chamber connecting admission line and discharge duct, institute State setting filter mechanism in airtight disengagement chamber, the outer surface of described filter mechanism is connected with admission line, inner surface and blast pipe Road connects, setting filter regeneration mechanism in described filtering dust system.By including connecting admission line and discharge duct Airtight disengagement chamber in setting filter regeneration mechanism, can filter body running for a period of time after, filtering bodies filter capacity because Decline to a great extent when can not meet normal work for the tar coal ash attachment of the gentle in the hole in surface, by filter regeneration machine Structure works, and filtering bodies is restored to due level up, repeated regeneration directly decreases the input of filtering bodies, also significantly Improve the service life of filtering bodies.
United States Patent (USP) US 09/271,741 disclose " for the method and apparatus of filter synthetic gas ", which employs one To rod cleaner, each cleaner have one for receive need to filter the entrance side of non-filter synthetic gas of heat, with And one be used for discharge filtration forming gas outlet side.Two cleaners can be accommodated with a housing, or be each Cleaner provides a single housing.Alternately supply combustion air to each rod cleaner, so that heavy burning Another cleaner is allowed to filter the non-filter synthetic gas of heat while amassing the oxidable particle on a cleaner.One Or multiple switching valve is connected to described combustion air feedway, for alternately supply combustion between two rod cleaners Burn air.
However, above-mentioned patent yet suffers from following some defects:
(1)Although technical scheme disclosed in above-mentioned patent solves to a certain extent asking present in high-temperature oil gas dedusting Topic, but, with the carrying out of filter process, still there are part tar precipitate and dust to combine, formed and even quickly form ash Cake is attached to filtering bodies surface, so that cleaner is comparatively fast blocked, lead to one or one group filtering bodies normal work when Between shorten, particularly during the industrialized production of the high Dust Capacity of atm number, be unfavorable for entirely interacting the steady of regenerating unit Qualitative, and then greatly increase operation expense.
(2)United States Patent (USP) US 09/271,741 disclosed " for the methods and apparatus of filter synthetic gas ", however, should Cleaner is limited only to the less gas cleaning at high temperature to tolerance, and atm number is such as even more big in thousands of m3/h, m3/h up to ten thousand For the filtration yield of numerical value, technical scheme disclosed in this patent is obviously also helpless, and one is that filter area is too small, only pin A kind of possible thinking and idea are provided for laboratory stage.The air intake that two is faint is difficult to ensure regenerating unit Interior a large amount of filtering bodies carry out uniformity and the uniformity of regenerative response, also cannot obtain the harmony of reaction temperature.
At present, the record of the solid and gas separation problem of high-temperature high dust oil gas is not still solved using electric dust-removing equipment.In addition, When biomass pyrolytic, from the point of view of situation about retrieving at present, either compression blocks or bulk thing, after its pyrolysis Gas there is also the situation of the high dirt of oil-containing, and various dedusters and its change all can not fundamentally solve atm number high-temperature high dust height A dedusting difficult problem in oil gas body.In addition, a problem put in face of the technical staff in art is, in combustible gas In body dust removal process, by the way of electric precipitation, it is extremely hazardous behavior, because during electric precipitation, often occur The phenomenon producing electric discharge because of the enrichment of electric charge occurs, and producing spark inside fuel gas is in art Technical staff must avoid.
Content of the invention
For solving the above problems, the utility model provide a kind of be used in pyrolysis of coal, dust-laden in biomass pyrolysis process, containing Jiao Oily pyrolysis gas remove electric dust-removing equipment and the system of dust.
A kind of electric dust-removing equipment, including electric dust-removing equipment body, described electric dust-removing equipment body arranges preheating device.
Described preheating device is overall preheating device.
Described preheating device is hot-gas channel, the internal cavity of described hot-gas channel and electric dust-removing equipment body Connect.
Described electric dust-removing equipment body arranges regenerating unit.
Described regenerating unit is physics regenerating unit and/or chemical regeneration device.
Described physics regenerating unit is to be arranged on to scrape mechanism on easily attached ash part.
Described chemical regeneration device is Poor oxygen gas input mechanism.
A kind of electric dust removing system, described electric dust removing system includes two sets or many set electric dust-removing equipments are in parallel.
The present inventor's research finds, for atm number dust-laden, the dedusting containing tar pyrolysis gas, because coal material, living beings Stir or be pyrolyzed under air-flow drives, lead to dust content in the admixture of gas producing very high, and contain in mixed gas Carbons easily separate out material such as tar Jiao, class bituminous material can be existed with gaseous state, not right only in the environment of high temperature Under conditions of it is preheated, the such as tar containing the easy precipitate of carbons in high-temperature high dust oil gas is burnt, class bituminous material from rapid from In gaseous mixture separate out phenomenon, be enriched in electric dust-removing equipment inner surface, collecting polar plate and corona discharge electrode rod, precipitate with except in dust and gas Dust combine rapidly and generate filter cake, and be attached in electric dust-removing equipment inner component surface and space, have a strong impact on gas Ionization and the absorption to powered dust for the collecting polar plate, and the dust of oil-containing not easily passs through hammering to remove on collecting polar plate Dust, this is also the reason high-temperature oil gas dust removal field can not carry out dedusting using electric dust-removing equipment for a long time place.And Before electric dust-removing equipment is started working, electric dust-removing equipment is preheated so that electric dust-removing equipment internal temperature and by except dust and gas Temperature is close, will preferably avoid because excessive temperature differentials bring containing carbons easy precipitate precipitation phenomenon from gaseous mixture Occur.
Those skilled in the art it is also believed that, either cleaner maximize or the feelings of lab pilot plant, lab scale Under condition, after high-temperature oil gas dust removal process starts, the temperature value that the temperature of cleaner will soon be increased to dedusting gas is attached Closely, a whole set of complicated pre-heating system need not be further added by preheating is exclusively carried out to it, belong to the behavior that at all there is no need, so Do not see any record that electric dust-removing equipment is preheated in the prior art.
The present inventor finds in very long research process finally, the correlation in whole cleaner internal cavity and cavity Between part, regional, temperature consistency is very crucial and important.Gaseous mixture containing the easy precipitate of tar gas enters airtight point After in chamber, gas molecule on the microcosmic moment after air inlet pipe enters cavity leads to greatly pressure to become due to the unexpected change in space Little, and close to outlet pipe when make pressure become big, the easy precipitate containing carbons is done by pressure change in hot environment Disturb and be just very easy to separate out, be liquefied as tar Jiao and class bituminous material, if gas molecule is during flowing, and because Lead to that large area irregular Temperature Distribution occurs in cleaner for local heating, non-uniform heat flux, temperature province is indirectly The height heat radiation that necessarily occurs of inequality and heat transfer, uneven irregular fever transmission can distort gas molecule, easy containing carbons Precipitate molecule particles are moved towards with the flowing in the attaching space of dust granules, greatly increase containing carbons easy precipitate molecule particles Collide the probability of simultaneously conglomerate polymers with dust granules, oily asphalitine aggregate becomes big and becomes heavy, also cannot maintain Vaporized state, simultaneously irregular air motion also increase tar Jiao molecule and dust molecule, the contact frequency of internal part, increase Add the probability that asphalitine polymerization separates out, very easy appearance such as tar containing the easy precipitate of carbons is burnt, class bituminous material is from mixing In gas, quick precipitation is attached to the phenomenon affecting normal dedusting on dust.
During industrialized production, cleaner is very huge, hundreds of easily, thousands of cubes of volume, the inside Parts are more, and the inlet chamber to whole system and outlet chamber are that dedusting environment carries out high temperature preheating, can produce larger economy Cost;Even more important property is, using high-temperature gas or other modes, whole dedusting cavity is carried out heating generally to introduce big Amount high-temperature gas, and the high-temperature combustion gas being introduced into easily are mixed into and treat in dedusting high temperature oil-containing gases, change pyrolysis gas Composition, reduces its economy, and the gas separating treatment in later stage is just more complicated.General high temperature oil-containing gases are all inflammable and explosive simultaneously , with heat forms such as high-temperature gas, electric heating, whole cavity being preheating to the condition of high temperature is a kind of dangerous behavior, so to height Warm oil-containing gases cleaner is preheated, and on the one hand can reduce the economy treating dedusting gas, on the other hand as increasing Plus the operation such as electrothermal mechanism, switching high-temperature gas, reduce the safety and reliability of its warm, dust removal process.
Therefore, the generally teaching of this area is:It is not necessary to right in high temperature dust, the dust removal process of pyrolysis gas containing tar Cleaner is preheated because pyrolysis gas start dedusting will firing equipment rapidly;Even if preheating, also without preheating electrode plate With the space outside corona wire and part, less will recognize that and preheated using overall, because the result that it is integrally preheated not only can Increase heating cost and equipment cost, and also likely bring reduction and the whole system security of pyrolysis gas economic benefit Reduction.
A kind of electric dust-removing equipment of the present invention, described electric dust-removing equipment body arranges preheating device, and electric dust-removing equipment body is even Tap into tracheae, outlet chamber connects escape pipe, using the preheating device being connected with electric dust-removing equipment chamber body, the electricity of cold conditions is removed Dirt apparatus body inner chamber carries out being preheating near the Temperature numerical that high-temperature high dust contains during tar gas entrance cleaner, after preheating Electric dust-removing equipment chamber body be passed through high-temperature high dust contain tar gas, high-temperature high dust contain tar gas in the charged rear quilt of dust Battery lead plate adsorbs, and filter mechanism regenerating unit is capable of the removing to floating dust on battery lead plate and ash cake, to ensure whole dedusting Equipment normal work.
In the prior art, in the electric dust-removing equipment of a large amount of high temperature oil-containing gases and method document, not to cleaner The related record heated.More not overall to the electric dust-removing equipment uniformly record of preheating and needs.So-called uniform, it is preheating All regions of whole cleaner inner chamber and the temperature of all parts are relatively uniform afterwards, and the result of preheating is cleaner inner chamber The each part temperatures in each position are consistent or basically identical.The scope of overall preheating, is may to lead to filtration gas in cleaner Cross or possible contact area or position.
The utility model by after electric dust-removing equipment body is integrally preheated so that each region, each part in cleaner Temperature relatively uniform consistent, the high oily high dirt gas molecule of high temperature that enters in the consistent overall situation of temperature can face less Temperature change and states of matter change, even if in the presence of dust, are also less susceptible to the change of local space states of matter and cohesion analysis Go out.It is whole to cleaner that the entirety preheating such as high-temperature gas of Wind Volume of preheating mechanism is passed directly into electric dust-removing equipment chamber body Body heats, and is capable of three below feature:The precise control of contact, no dead angle, heating-up temperature and heating process, and in advance Thermal velocity is fast, energy-conservation, remarkable in economical benefits;Other mode of heatings such as outside sandwich of overall heating leads to hot blast, cavity surrounding entirety The ways of realization such as parcel heat generating components can also realize no dead angle, comprehensive preheating, and pre- thermal result is each region in cleaner Temperature is basically identical, but a large amount of high-temperature gases more preferably remaining circulating air participation integrally heat the preheating of cleaner Form.In addition, it is critical that because by the way of using overall preheating, in filter process, cleaner cavity inner wall, The temperature of many interior fittings such as cathod system, anode system, vibrated system is relatively uniform, and the heat transfer in cavity is less, Substantially increase the controllability of system, reliability of operation and uniformity.Avoid appearance during dedusting locally and whole Body, central authorities and fringe region dedusting work out of step conditions.
The molecular state of oil gas is unstable in itself, in hot environment, often because heat absorption and lead to two or Two or more organic molecule is interacted and is combined to form a macromolecular in the form of covalent bond, and with shaking off of small molecule Constantly there is condensation reaction, molecule is solid-state from gaseous, liquid coking, be combined generation ash cake obstruction with dust and filter.And the present invention Technical scheme cavity is carried out with overall preheating, it is relatively uniform all even stable to filter environment temperature, asphalitine occur pyrolysis and Polycondensation reaction probability substantially reduces, and also occurs without low-temperature liquefaction phenomenon, and tar is burnt, the minimizing of class bituminous material amount of precipitation directly presses down The speed that filter cake processed generates.
Two electric dust-removing equipment parallel connections, are capable of dedusting gas and switch on two cleaners, you can to make simultaneously With realizing the double of dedusting tolerance, wherein maintenance do not stopped work can be regenerated, complete electric dust-removing equipment overall again Giving birth to online, when regeneration especially with chemical regeneration device, two sets of electric dust-removing equipments in parallel are more convenient, It is capable of two sets of electric dust-removing equipments in parallel and does not stop production alternately regenerating.
Brief description:
The present invention is described further below in conjunction with the accompanying drawings:
Fig. 1 is the overall structure diagram of the utility model embodiment one cleaner;
Fig. 2 is the structural representation of the utility model embodiment one collecting polar plate regeneration sector;
Fig. 3 is the structural representation of the utility model embodiment one corona discharge electrode rod regeneration sector;
Fig. 4 is the structural representation of the utility model embodiment three cleaner;
Specific embodiment:
Embodiment one:
As shown in Figure 1, Figure 2, Figure 3 shows:A kind of electric dust-removing equipment, including electric dust-removing equipment body 1, electric dust-removing equipment described in 1 Body 1 connects admission line 3 and outlet pipe 2, and electric dust-removing equipment body 1 arranges preheating device 4, and described preheating device 4 is height Warm gas pipeline, described hot-gas channel is connected with the internal cavity of electric dust-removing equipment body 1, and hot-gas channel can be with High-temperature gas generating mechanism connects, such as burner, boiler afterheat.Described electric dust-removing equipment body arranges regenerating unit, institute Stating regenerating unit is physics regenerating unit, and described physics regenerating unit is included being arranged on collecting polar plate 8 two side and set with electric precipitation Close to the track 5 of position or connection member, setting between described track 5 is flexibly connected standby body 1 inwall with collecting polar plate 8 Scraper 6, described scraper 6 is moved on the rail 5 by actuating unit, is capable of the cleaning to collecting polar plate 8, the ash cleaning out Dirt or putty cake are fallen in ash bucket 7;Described physics regenerating unit also includes the scraper plate 9 being flexibly connected with corona discharge electrode rod 10, institute State setting through hole on scraper plate 9, the inner periphery of described through hole is adapted with the excircle of corona discharge electrode rod 10;Described scraper plate 9 passes through dynamic Force mechanisms move in orbit, are capable of the cleaning to corona discharge electrode rod 10, and ash bucket 7 fallen by the dust cleaning out or putty cake In.
Before starting in dust-removing process, electric dust-removing equipment body 1 is preheated, is passed through high-temperature gas, according to height The size of wet body wind flow, such as 58 m3/min, with the time of 17 to 23 hours, are capable of electric dust-removing equipment originally internal Portion's temperature is basically identical with dedusting gas temperature, and the preheating of particularly the inside parts temperature puts in place, after preheating terminates, that is, whole After body preheating, then switch into dust pelletizing system, start dedusting work, dedusting during electric dust-removing equipment can be greatly decreased The internal quick generation producing ash cake phenomenon of body 1.And the carrying out with dedusting work, collecting polar plate 8 and corona discharge electrode rod 10 are attached The putty or ash cake, as needed, by physics regenerating unit timing slide, putty or ash cake are come off with attachment, And fall in ash bucket 7, realize the regeneration of dedusting function, the electric dust-removing equipment implemented in this way can continuously work 350 400 hours.
Embodiment two:
As shown in Figure 1:A kind of electric dust-removing equipment, including electric dust-removing equipment body 1, described in 1, electric dust-removing equipment body 1 connects Admission line 3 and outlet pipe 2, electric dust-removing equipment body 1 arranges preheating device 4, and described preheating device 4 is high-temperature gas pipe Road, described hot-gas channel is connected with the internal cavity of electric dust-removing equipment body 1, and hot-gas channel can be with high-temperature gas Generating mechanism connects, such as burner, boiler afterheat.Described electric dust-removing equipment body arranges regenerating unit, described regeneration dress It is set to physics regenerating unit, described physics regenerating unit includes the high-temperature gas injection machine being arranged on electric dust-removing equipment body Structure, timing can carry out gases at high pressure injection to easily attached ash position, ash fallen by the dust cleaning out or putty cake as needed In bucket 7.
Before starting in dust-removing process, electric dust-removing equipment body 1 is preheated, is passed through high-temperature gas, according to height The size of wet body wind flow, such as 10 12 m3/min, with the time of 5 to 10 hours, are capable of electric dust-removing equipment originally internal Portion's temperature is basically identical with dedusting gas temperature, but being also far not by far up to the mark of the inside parts temperature, that is, achieve The space preheating of fluid mass, then switch into dust pelletizing system, can partly reduce electric dust-removing equipment basis during dedusting The internal quick generation producing ash cake phenomenon of body 1.
High-temperature dust removal equipment contains tar gas by high-temperature high dust filter, filters 2000 mark side's pyrolysis gas per hour, In the case of injection once in every 15 to 20 minutes, can continuously produce 250~300 hours, after switching, after regeneration, surface does not almost have There is floating ash, realize the regeneration of its dedusting function.
Embodiment three:
As shown in Figure 4:As shown in Figure 1:A kind of electric dust-removing equipment, including electric dust-removing equipment body 1, described in 1, electric precipitation sets Standby body 1 connects admission line 3 and outlet pipe 2, and electric dust-removing equipment body 1 arranges preheating device 4, and described preheating device 4 is Hot-gas channel, described hot-gas channel is connected with the internal cavity of electric dust-removing equipment body 1, and hot-gas channel is permissible It is connected with high-temperature gas generating mechanism, such as burner, boiler afterheat.Before starting in dust-removing process, to electric precipitation Apparatus body 1 is preheated, and is passed through high-temperature gas, according to the size of high-temperature gas wind flow, such as 8 16 m3/min, are arrived with 8 The time of 12 hours, it is capable of electric dust-removing equipment body interior temperature consistent with dedusting gas temperature, in electric dust-removing equipment Also the temperature reaching dedusting gas of face parts temperature, that is, achieve the space preheating of fluid mass, then switch into dedusting System, can be greatly improved suppression inside electric dust-removing equipment body 1 during dedusting and produce the time that ash cake phenomenon produces.
Described electric dust-removing equipment body arranges regenerating unit, and described regenerating unit is physics regenerating unit, described regeneration dress It is set to chemical regeneration device, described chemical regeneration device is Poor oxygen gas input mechanism 11.Allowed short by electric dust-removing equipment body Quit work in time, input appropriate Poor oxygen gas with Poor oxygen gas input mechanism 11, allow collecting polar plate and corona discharge electrode rod table Face deposition oxidable particle oxidized fall, recover the normal dedusting function of electric dust-removing equipment, controlled with appropriate Poor oxygen gas The temperature when oxidation rate of oxidable particle of filtering bodies surface processed deposition and cleaner regeneration.
High-temperature dust removal equipment contains tar gas by high-temperature high dust filter, filters 2500 mark side's pyrolysis gas per hour, In the case of injection once in every 20 to 25 minutes, can continuously produce 280~350 hours, after switching, after regeneration, surface does not almost have There is floating ash, realize the regeneration of its dedusting function.
Example IV:
As shown in Figure 2, Figure 3, Figure 4:A kind of electric dust-removing equipment, including electric dust-removing equipment body 1, electric dust-removing equipment described in 1 Body 1 connects admission line 3 and outlet pipe 2, and electric dust-removing equipment body 1 arranges preheating device 4, and described preheating device 4 is height Warm gas pipeline, described hot-gas channel is connected with the internal cavity of electric dust-removing equipment body 1.
Before starting in dust-removing process, electric dust-removing equipment body 1 is preheated, is passed through high-temperature gas, according to height The size of wet body wind flow, such as 15 25 m3/min, with the time of 10 to 15 hours, it is capable of electric dust-removing equipment body Internal temperature is consistent with dedusting gas temperature, the temperature also reaching dedusting gas of parts temperature inside electric dust-removing equipment, Achieve the space preheating of fluid mass, then switch into dust pelletizing system, dedusting during electricity can be greatly improved and remove The internal suppression of dirt apparatus body 1 produces the time that ash cake phenomenon produces.
Described electric dust-removing equipment body arranges regenerating unit, and described regenerating unit is physics regenerating unit and chemical regeneration dress Put.Described physics regenerating unit is to be arranged on to scrape mechanism on easily attached ash part, and described chemical regeneration device is Poor oxygen gas Input mechanism.Physics regenerating unit and chemical regeneration device are used in conjunction with, and can effectively improve efficiency and the effect of regeneration.Tool The way of body, first using physics regenerating unit, putty or floating ash that quick removing is adhered to, are removed with scraper or scraping blade machinery Ash, for the putty removing not thorough and comprehensive tiny piece, realizes thoroughly removing with chemical regeneration device comprehensively, that is, with lean Carrier of oxygen oxidation is removed.
High-temperature dust removal equipment contains tar gas by high-temperature high dust filter, filters 2500 mark side's pyrolysis gas per hour, In the case of injection once in every 20 to 25 minutes, can continuously produce 500~650 hours, after switching, after regeneration, surface does not have completely There is floating ash, realize the regeneration of its dedusting function.
Embodiment five:
As shown in Figure 1:A kind of electric dust-removing equipment, including electric dust-removing equipment body 1, described in 1, electric dust-removing equipment body 1 connects Admission line 3 and outlet pipe 2, electric dust-removing equipment body 1 arranges preheating device 4, and described preheating device 4 is high-temperature gas pipe Road, described hot-gas channel is connected with the internal cavity of electric dust-removing equipment body 1, and hot-gas channel can be with high-temperature gas Generating mechanism connects, such as burner, boiler afterheat.Before starting in dust-removing process, electric dust-removing equipment body 1 is entered Row preheating, is passed through high-temperature gas, according to the size of high-temperature gas wind flow, such as 69 m3/min, with 20 to 25 hours when Between, it is consistent with dedusting gas temperature to be capable of electric dust-removing equipment body interior temperature, parts temperature inside electric dust-removing equipment Also the temperature reaching dedusting gas of degree, that is, achieve the space preheating of fluid mass, then switch into dust pelletizing system, Ke Yi great Width improves suppression inside electric dust-removing equipment body 1 during dedusting and produces the time that ash cake phenomenon produces.
Described electric dust-removing equipment body arranges regenerating unit, and described regenerating unit is physics regenerating unit, and described physics is again Generating apparatus are included for beating mechanism.Described hammering mechanism is to beat mechanism, is able to battery lead plate and corona wire surface are floated Ash, putty and ash cake carry out departing from cleaning, and the floating grey, putty according to battery lead plate and corona wire surface and ash cake carry out departing from cleaning Difficulty, with select different hammering dynamics, amplitude and frequency it is ensured that depart from effect more preferable.
High-temperature dust removal equipment contains tar gas by high-temperature high dust filter, filters 2500 mark side's pyrolysis gas per hour, In the case of injection once in every 20 to 25 minutes, can continuously produce 280~350 hours, after switching, after regeneration, surface does not almost have There is floating ash, realize the regeneration of its dedusting function.
Embodiment six:
As example IV:Battery lead plate and corona wire are set to hollow-core construction, by the sky within battery lead plate and corona wire Center portion divides and outer surface between setting pore, anti-by the gases at high pressure that connect with the hollow parts within corona wire in battery lead plate Blow mechanism, horizontal high voltage blowback can be entered inside a period of time is to battery lead plate and corona wire, gases at high pressure pass through battery lead plate and electricity Between hachure boring part and outer surface setting pore it is also possible to the floating ash on surface is blown off, extend its work when Between.
The utility model electric dust-removing equipment, is not only limited to the way of realization in above-described embodiment, including tubular, circle , one pole, structure multipole and that person of ordinary skill in the field can be realized as without creative work, reach To essentially identical effect, broadly fall within protection scope of the present invention.
For chemical regeneration is better achieved, improve the dust removing effects of cleaner, ad hoc two cleaner parallel connections of meter, group Become a dust pelletizing system.It is capable of a dedusting, another one is using the method regeneration of chemistry.After this regeneration ending, Displace the gas that regeneration generates, then be switched on cleaning shaft, the cleaner that another one can not normally be used enters Row chemical regeneration, or physics and chemical bond regeneration, improve regeneration efficiency, realize preferably regeneration effect.
" in parallel " is the parallel connection of two or more cleaners herein.Two or more cleaners will not be mutual Interference, both can be simultaneously using the concept in parallel it is also possible to be used alone, such as in lighting circuit.
Parallel connection as herein described, can be that two or more cleaners access between air inlet pipe and escape pipe side by side, Can access side by side between pyrolysis plant and equipment for after-treatment, to realize the dedusting of gas.
Two or more cleaners of " in parallel " specifically described herein, can be identical, and two dedustings such as in parallel set Standby, it is all the cleaner described in embodiment one.Can also be incomplete same, such as one is that the dedusting that embodiment one is recorded sets Standby, connected in parallel another is the cleaner that embodiment three is recorded.
Description below is done for the term in specification:
" atm number " particularly relates to the tolerance by air quantity more than 50 more than m3 per minute at ambient pressure;
" Poor oxygen gas " particularly relate to the gas that oxygen content is 0.1~5%;
" high temperature " in high-temperature gas containing dust and tar and filter cavity particularly relates to 250~750 DEG C.
" high dirt " particularly relates to dust content in gas is 100~2000 grams/cubic metre.
" high tar content " particularly relates to tar in gas content is 100~3000 grams/cubic metre.

Claims (2)

1. a kind of electric dust-removing equipment, including electric dust-removing equipment body it is characterised in that:Described electric dust-removing equipment body setting preheating Device;Described preheating device is overall preheating device;Described preheating device be hot-gas channel, described hot-gas channel with The internal cavity of electric dust-removing equipment body connects;Described electric dust-removing equipment body arranges regenerating unit;Described regenerating unit is thing Reason regenerating unit and/or chemical regeneration device;Described physics regenerating unit is to be arranged on to scrape mechanism on easily attached ash part;Institute Stating chemical regeneration device is Poor oxygen gas input mechanism.
2. a kind of electric dust removing system it is characterised in that:Described electric dust removing system includes two sets or many set electric dust-removing equipments are in parallel.
CN201620735439.3U 2016-07-13 2016-07-13 Electricity dust collecting equipment and system Active CN205926020U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620735439.3U CN205926020U (en) 2016-07-13 2016-07-13 Electricity dust collecting equipment and system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620735439.3U CN205926020U (en) 2016-07-13 2016-07-13 Electricity dust collecting equipment and system

Publications (1)

Publication Number Publication Date
CN205926020U true CN205926020U (en) 2017-02-08

Family

ID=57928964

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620735439.3U Active CN205926020U (en) 2016-07-13 2016-07-13 Electricity dust collecting equipment and system

Country Status (1)

Country Link
CN (1) CN205926020U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105964406A (en) * 2016-07-13 2016-09-28 河南龙成煤高效技术应用有限公司 Electrical dust removal equipment and electrical dust removal system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105964406A (en) * 2016-07-13 2016-09-28 河南龙成煤高效技术应用有限公司 Electrical dust removal equipment and electrical dust removal system

Similar Documents

Publication Publication Date Title
CN105879508B (en) The dust pelletizing system and its dust removal method that cleaner, the cleaner for the atm number gas that dustiness is 100-2000g/m3, tar content is 100-3000g/m3 form
US7981835B2 (en) System and method for coproduction of activated carbon and steam/electricity
CN102329653B (en) Plasma garbage gasification device and process
CN100563783C (en) A kind of bitumen flue gas purifying method
RU111024U1 (en) SYSTEM FOR DRY DUST DEPOSITION AND DRY CLEANING OF A GAS CONTAMINATED BY DUST AND HAZARDOUS SUBSTANCES FORMED IN IRON PRODUCTION UNITS IN THE CAST IRON PRODUCTION OR IN THE DEVICE FOR A DISASTER
CN103058536B (en) Heat-accumulation dividing-wall heating rotary kiln device
CN104258676B (en) A kind of catalytic ceramics film reaction device
US20100113267A1 (en) System and method for coproduction of activated carbon and steam/electricity
CN203440329U (en) Catalytic cracking and dust removal integration system for medium-and-low-temperature dry distillation gas
CN103818902B (en) Multi-stage oven is adopted to manufacture desulphurization denitration activated coke production technique and production unit
CN105273733B (en) A kind of coupling multi-stage subtracts the small particle low order pyrolytic process of coal and equipment of dirt
CN105964141A (en) Treatment method and system for sprayed VOCs (Volatile Organic Chemicals) mixed gas
CN106753494B (en) Activated coke preparation facilities and method
CN205926020U (en) Electricity dust collecting equipment and system
CN111001239A (en) Pyrolysis gas dust removal method and device
WO2013173951A1 (en) Combustion heating system
CN104154762A (en) Smelting gas dedusting and purifying method for submerged arc furnace and smelting system of submerged arc furnace
CN110054185A (en) The system and method for active carbon is produced in a kind of thermal power plant coal pyrolysis charring activation
CN204159171U (en) A kind of catalytic ceramics film reaction device
CN207347513U (en) A kind of device using fluid bed production charcoal
CN111545003A (en) Method for purifying tar in carbon electrode roasting furnace flue gas
CN104197725A (en) Method for dedusting and purifying of smelting smoke of submerged arc furnace and comprehensive utilization of sensible heat and latent heat of smelting smoke
CN207552265U (en) A kind of biomass gasifying furnace gas separation equipment
CN106238207A (en) A kind of electro dust removing method of high temperature height innage dust and gas body
CN109437204A (en) A kind of processing technology of silicon carbide smelting

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant