CN207805276U - The handwarmer fire coal barn dust-removal and desulfurizing denitrification apparatus of temperature triggered - Google Patents
The handwarmer fire coal barn dust-removal and desulfurizing denitrification apparatus of temperature triggered Download PDFInfo
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- CN207805276U CN207805276U CN201721547689.5U CN201721547689U CN207805276U CN 207805276 U CN207805276 U CN 207805276U CN 201721547689 U CN201721547689 U CN 201721547689U CN 207805276 U CN207805276 U CN 207805276U
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- 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
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Abstract
The utility model discloses the handwarmer fire coal barn dust-removal and desulfurizing denitrification apparatus of temperature triggered, structure is:Air atomizer spray nozzle setting connects gas path pipe in barn chimney outlet for spraying into spray liquid, one end of air atomizer spray nozzle into chimney, and the other end of air atomizer spray nozzle connects fluid path pipeline;The other end of gas path pipe connects air compressor;The other end of fluid path pipeline connects peristaltic pump;The output end of the included wet system of intelligent temperature control control of control terminal connection handwarmer fire coal barn of peristaltic pump;Temperature sensor detects in-furnace temperature, and when temperature is more than predetermined temperature threshold, the wet system of intelligent temperature control control then starts peristaltic pump and implements dust-removal and desulfurizing denitration.The utility model is sprayed using temperature triggered, and using flue as reactor, gas-liquid contact is more abundant, desulfuration efficiency is greatly improved, desulfurization purpose has been reached, device is simply effective, without individually establishing desulfurizing tower or desulfurizer, the smoke pollution of handwarmer fire coal barn is solved the problems, such as.
Description
Technical field
The utility model belongs to handwarmer fire coal barn dust-removal and desulfurizing denitration technology field, more particularly, to a kind of temperature
Spend the handwarmer fire coal barn dust-removal and desulfurizing denitrification apparatus of triggering.
Background technology
Coal-burning boiler operated by handwork belongs to fire grate layer combustion directly burning type stove, universal in China's handwarmer fire coal barn Tobacco Leaf Curing
To provide heat with coal-burning boiler operated by handwork, due to the discontinuity of coal in combustion process, cause paroxysmal that flue dust generates,
Discontinuity and larger instantaneous concentration cause to purify difficulty increase.Therefore, the flue gas formation characteristic of coal-burning boiler operated by handwork is furtherd investigate
And rule, there is certain theoretical foundation to formulating rational flue gas ash removal and desulphurization denitration technology.The handwarmer in China at present
Few mating dedustings or desulfurizer in coal-fired barn, therefore the coal-fired soot dust granule generated, SO2With the pollutions such as NOx
Object can be exhausted directly in air, not only cause the inhalable particles in air to increase, it is also possible to cause acid rain, to a certain extent
Influence the quality of life of resident.Bituminous coal and anthracite, calorific value 28878J/g, sulfur-bearing are usually used when hothouse baking tobacco leaf
Amount 0.48%, average coal consumption is about 134kg/d/.Therefore, dust-removal and desulfurizing denitration of the research for handwarmer fire coal barn
Technology is highly desirable.
Xue Yong document (coal-burning boiler operated by handwork flue dust generate feature and its control [J] Techniques and Equipment for Environmental Pollution Controls,
2005,(05):71-73. [2017-09-05]) in have developed a kind of flue gas purification system, which includes calcium injection and desulfurization system
System, water-bath flue gas cleaner, the wastewater sedimentation circulatory system, stainless steel boiler induced-draft fan and chimney.The technology is that barn is specially set
A set of desulfurization dedirt device is set, it is complicated, it is of high cost.And the larger instantaneous of coal-burning boiler operated by handwork flue dust generation is not accounted for
The characteristic of concentration should increase spray liquid (increasing calcium sulfur ratio) when sulfur content instantaneous concentration is larger to ensure desulfuration efficiency.
The patent of publication number CN2700725Y discloses a kind of combustion water dust-removing desulfurizing device suitable for handwarmer, including straight
Pipe, vaporizer, it is characterized in that the device is made of combustion water dispenser structure, deduster and desulfurizer three parts, scheme is to utilize cigarette
The waste heat of gas vaporizes water into and leads to furnace bottom and contacts to form water-gas and combustion-supporting with red-hot coal, improves burning condition.But
Adsorbent used in desulfurization is solid absorbent, and adsorption efficiency is relatively low, and needs to replace at any time, increases cost of labor.
Above-mentioned desulfurization method is to have used for reference boiler of power plant desulfurization, i.e., the desulfurization that flue gas is introduced into a special desulfurization fills
It sets, spray liquid makes the SO in flue gas in desulfurizer2Reach the SO in de- flue gas removing with alkali substance reaction2Purpose, but
It is that boiler of power plant is different from intensive baking room situation, first, because the fired coal combustion situation in handwarmer has paroxysmal, interruption
The characteristic of property and larger instantaneous concentration, combustion characteristics and combustion characteristics coal-fired in boiler of power plant are inconsistent;Second is that establishing
Individually establish the expensive of desulfurizing tower.Therefore the mode of boiler of power plant desulfurization is not suitable for handwarmer fire coal barn, is badly in need of out
Dust-removal and desulfurizing denitrating technique of the hair suitable for handwarmer fire coal barn.
Utility model content
The utility model provides a kind of handwarmer fire coal barn desulfation dust-extraction device of temperature triggered, it is intended that
Device is simply effective, without individually establishing desulfurizing tower or desulfurizer, solves the problems, such as the smoke pollution of handwarmer fire coal barn.
In order to realize that the utility model technical purpose, the utility model provide following technical scheme:
The dust-removal and desulfurizing denitrification apparatus of the handwarmer fire coal barn of temperature triggered, including the compression of air atomizer spray nozzle, air
Machine, air cutoff valve, air pressure-adjusting valve, peristaltic pump, liquid stop valve and liquid pressure regulator valve.
Air atomizer spray nozzle setting is used to spray into spray liquid into chimney in barn chimney outlet, air atomizer spray nozzle
One end connects gas path pipe, and the other end of air atomizer spray nozzle connects fluid path pipeline;The other end of gas path pipe connects air pressure
Contracting machine;The other end of fluid path pipeline connects peristaltic pump;Air cutoff valve and it is located at gas circuit with the air pressure-adjusting valve with pressure gauge
In pipeline;Liquid stop valve and liquid pressure regulator valve are located in fluid path pipeline;The control terminal connection handwarmer fire coal of peristaltic pump is roasting
The output end of the included wet system of intelligent temperature control control in room;Temperature sensor is for detecting in-furnace temperature, when temperature is more than pre- constant temperature
Threshold value is spent, the wet system of intelligent temperature control control then starts peristaltic pump and implements dust-removal and desulfurizing denitration.
Further, the atomizer includes ontology, and the upper end of ontology is rotation button, and lower end is jet expansion, empty
The middle part side of aerosolization nozzle connects gas path pipe, and the other side connects fluid path pipeline, and there is body interior a cavity, screw rod to insert
Enter cavity and upper end connection rotation button, screw rod can be driven to move up and down by turn knob, moving up and down for thimble is controllable
The input of liquid, when thimble rises to top, liquid input is maximum, and when thimble is down to bottommost, liquid input is zero.
Further, the temperature sensor uses the temperature sensor that the wet system of intelligent temperature control control carries.
The advantageous effects of the utility model are embodied in:
The utility model is based on CO2Concentration variable quantity can reflect SO2Concentration variation, and CO2Concentration variation tendency and barn
Positively related relationship is presented in interior temperature changing trend, is sprayed using temperature triggered, implements dust-removal and desulfurizing denitration.The utility model without
Temperature sensor and temperature control system need to be additionally set, the intelligence that the control signal of peristaltic pump is carried with handwarmer fire coal barn here
Energy temperature and humidity control system is connected, and monitoring temperature and control are executed using the included wet system of intelligent temperature control control of handwarmer fire coal barn
The task of spray liquid processed realizes the adaptive process of barn dust-removal and desulfurizing denitration.When can start to spray in handwarmer when the temperature is excessively high
Leaching is just coal-fired vigorous combustion release volume of smoke when the temperature is excessively high according to the combustion case of field measurement fire coal, in handwarmer
(it is more than 15mg/m3) and SO2The stage of (being more than 70ppm), temperature do not spray into spray liquid when being not above the difference of setting, this is
The periodic process of one pulsed.
Using flue as reactor, the atomized drop with initial velocity that nozzle sprays is formed the utility model with flue gas
Turbulent flow, the turbulent motion between fluid enhance gas-liquid mixed, not only increase denitrification efficiency, moreover it is possible to increase water fog particle with
The effective collision number of dust particles forms aggregate after agglomerating, aggregate constantly becomes larger again, until being finally settled down to
Cleanout, to achieve the purpose that eliminate dust.So that the process of flue gas discharge is also the process of dust-removal and desulfurizing denitration simultaneously, dedusting
Efficiency reaches 85% or more, and desulfuration efficiency reaches 63% or more, and denitration efficiency reaches 26% or more.
The utility model method and apparatus reduce reaction unit using flue as reactor, pacify without in exit
Air-introduced machine is filled, stove combustion process is influenced smaller.This product reaches 85%-90%, desulfurization effect by experimental verification efficiency of dust collection
Rate is up to 63% or more, and denitration efficiency 26% or so, nozzle location optimizes, high degree of automation, certainly by adjusting calcium sulfur ratio
Adapt to SO in chimney2Concentration changes, most of dust, SO2Just gone before going out flue outlet with nitrogen oxides it is de-, significantly
The discharge for reducing noxious material, device is simple, simple to install, greatly reduces cost.Discharge flue gas can reach national mark
Accurate (《Emission standard of air pollutants for boilers》GB13271-2014).The utility model method and apparatus are simply effective, at low cost
Honest and clean, operability is strong, without individually establishing desulfurizing tower or desulfurizer, solves the problems, such as the smoke pollution of intensive tobacco baking room.
Description of the drawings
Fig. 1 is coal of the present invention and smashes the combustion law schematic diagram of smoke components variation during coal;
Fig. 2 is apparatus of the present invention structural schematic diagram;
Fig. 3 is nozzle arrangements schematic diagram of the present invention;
Fig. 4 is the wet system construction drawing of intelligent temperature control control of the present invention.
Specific implementation mode
In order to make the purpose of the utility model, technical solutions and advantages more clearly understood, below in conjunction with attached drawing and implementation
Example, the present invention will be further described in detail.It should be appreciated that specific embodiment described herein is only used to explain
The utility model is not used to limit the utility model.In addition, institute in the various embodiments of the present invention described below
The technical characteristic being related to can be combined with each other as long as they do not conflict with each other.
By test coal repeatedly and smash smoke components during coal variation find its combustion law as shown in Figure 1, by
SO known to Fig. 12Change curve and CO2The trend of concentration curve is almost the same. CO2Concentration reflects the combustion of stove chamber inner combustion
Burn situation, CO2Concentration height illustrates that fired coal combustion is violent, CO2Concentration is low to illustrate that fired coal combustion is insufficient or by after-flame.After coal,
Coal starts to burn, and consumes a large amount of oxygen in air, and thus oxygen content decline leads to CO2Concentration increases, at this time coal-fired wink
Between be ignited, start vigorous combustion, the flue dust moment of generation increases;Organic sulfur first a large amount of releases in simultaneous coal,
So SO2Concentration also will increase.And then fire coal fully burns, at this time CO2Concentration is stablized in a higher numerical value, and fire coal fills
Divided combustion causes after-flame good, and the flue dust of generation is gradually increased to a stationary value;And gradually release leads to SO to inorganic sulfur2Value by
Gradually rise to a stationary value.Coal-fired burning degree weakens after a period of stabilisation, and after-flame is gradually deteriorated, and leads to the cigarette generated
Dirt gradually decreases;The release decline of inorganic sulfur leads to SO2Value gradually drop to minimum.After smashing coal, unburned portion in fire coal
Separately begin vigorous combustion, thus leads to CO2Concentration, dust concentration and SO2It is synchronous to increase;But the because coal of unburned part
It is less, therefore CO quickly2Concentration, dust concentration and SO2Synchronous downward trend is presented.By analysis it can be found that although hand is burnt
The flue gas generating process of stove and its coal and to smash coal mode directly related, but dust concentration and SO2The variation tendency of concentration with
CO2The variation tendency of concentration shows surprising similitude.In brief, because of CO2Concentration reflects the burning feelings of stove chamber inner combustion
Condition, and pollutant is due to caused by combustion burning of coal, it is possible to use CO2Concentration change this amount can reflect it is all
The concentration of pollutant changes.
Meanwhile the positively related relationship of burning degree presentation of the temperature in burner hearth and fire coal, and CO2Concentration exactly reflects combustion
One important positive correlation linear index of burning of coal degree, therefore CO2Concentration is that positively related pass is presented with the temperature in burner hearth
System.
Further, the temperature association in the temperature and barn in burner hearth, i.e., the temperature in burner hearth increase, cause preferably
Heat-transfer effect causes heat exchange more abundant, to make the temperature in barn also increase.
It is possible thereby to deduce:Dust concentration and SO2Temperature changing trend in the variation tendency and barn of concentration is presented just
Relevant relationship so far can trigger the dust-removal and desulfurizing denitration of handwarmer fire coal barn by monitoring the temperature change in barn.
The utility model nozzle-type handwarmer fire coal barn dust-removal and desulfurizing method of denitration is specially:In the chimney breast of barn
Air atomizer spray nozzle is disposed, sprays into the spray liquid of atomization, spray liquid and flue gas in chimney into chimney by air atomizer spray nozzle
Counter current contacting strengthens gas-liquid mixed by the turbulent motion of fluid, adsorbs flue dust and removing SO in flue gas2And NOx, reaction production
Object falls de- clearly in a manner of sweeping up dust after chimney bottom cleanout.
The wet system detectio in-furnace temperature of intelligent temperature control control carried using handwarmer fire coal barn, in the wet system of intelligent temperature control control
Set temperature value in system starts spray when actual temperature is more than this setting value so that the wet system of intelligent temperature control control can root
Spray liquid is controlled according to the temperature fluctuation in burner hearth, it is adaptive to achieve the purpose that.
Spray liquid is any one in calcium hydroxide solution, magnesium hydroxide solution, limestone/gypsum slurries.It considers
The SO removed is needed in the design2And NOXAmount and little, so the higher magnesia of absorption efficiency does not have clear superiority,
On the contrary since calcium oxide is cheap and easy acquisition, technical maturity, therefore preferred white lime/gypsum is more in the present invention
For economic and reliable.
CaO+H2O→Ca(OH)2
Ca(OH)2+SO2→CaSO3·1/2H2O+1/2H2O
CaCO3+SO2+1/2H2O→CaSO3·1/2H2O+CO2↑
CaSO3·1/2H2O+SO2+1/2H2O→Ca(HSO3)2
Ca(OH)2+NO+NO2→Ca(NO2)2+H2O
Calcium hydroxide slurry is spray liquid, and mass concentration generally takes 10%.Flue gas flows from the bottom up, and spray liquid exists
Top sprays, and the two adverse current is mixed, the SO in calcium hydroxide and flue gas that slurries contain2It is come into full contact with NOx, exhausted big portion
Divide and be dissolved in slurries by absorption, generates calcium sulfite, calcium bisulfite and calcium nitrite, reach SO in flue gas removing2And NOx
Purpose.
As shown in Fig. 2, the utility model provides the device for realizing the above method, handwarmer fire coal barn desulfurization and dedusting dress
It sets including air atomizer spray nozzle 4, air compressor 1, the air cutoff valve 2 being connected with gas circuit and with the air pressure-adjusting valve of pressure gauge
3, peristaltic pump 7, slurry pool 8, the liquid stop valve 6 being connected with fluid path and liquid pressure regulator valve 5, cleanout 9, flue with pressure gauge
10, separately there is temperature sensor not shown in the diagram.
The air atomizer spray nozzle 4 for spraying into spray liquid into chimney in barn chimney outlet, air atomizing spray are set
One end of mouth 4 connects gas path pipe, and the other end of air atomizer spray nozzle connects fluid path pipeline;The other end for connecting gas path pipe connects
Connect air compressor 1;The other end of fluid path pipeline connects peristaltic pump;Air cutoff valve 2 and with the air pressure regulation with pressure gauge
Valve 3 is located in gas path pipe;Liquid stop valve 6 and liquid pressure regulator valve 5 are located in fluid path pipeline;The control terminal of peristaltic pump 7 connects
Connect the output end of the wet system of the included intelligent temperature control control of handwarmer fire coal barn 11.Temperature sensor monitors are more than to in-furnace temperature
Desired value, the then wet system startup peristaltic pump 7 implementation dust-removal and desulfurizing denitration of intelligent temperature control control.
Temperature sensor can be separately provided, it also may be preferable for carry temperature sensor using the wet system of intelligent temperature control control and realize.
As shown in figure 3, the utility model provides realization by the nozzle of solution atomization, which is excellent by experiment test progress
Type selecting after change.Air atomizer spray nozzle includes ontology, and the upper end of ontology is rotation button, and lower end is jet expansion, air atomizing
The middle part side of nozzle connects gas path pipe, and the other side connects fluid path pipeline, and there is body interior a cavity, screw rod to be inserted into cavity
And upper end connection rotation button, screw rod can be driven to move up and down by turn knob, thimble moves up and down controllable liquid
Input, when thimble rises to top, liquid input is maximum, and when thimble is down to bottommost, liquid input is zero.
Drop after atomization, which is carried secretly by gas from nozzle, to be come out, and is had certain initial velocity, is sprayed from the point of view of hydrodynamics
Gas-liquid mixture be turbulence form.
Air atomizer spray nozzle is the gas circuit of air inlet on one side, is the fluid path into slurries on one side, gas, liquid are in air cap and liquid
Atomized inside mixes in body cap cavity, and atomizing principles are that air is ruptured and hit, and atomizing effect is ideal, belongs to internal-mixing atomization.
Embodiment:
The utility model provides a kind of intelligent nozzle-type dust-removing desulfurating apparatus, includes the following steps:
(1) gas circuit of nozzle is sequentially connected air compressor machine 1, shut-off valve 2, the air pressure-adjusting valve 3 with pressure gauge.Air compressor machine provides
Compressed air, air pressure-adjusting valve adjust gas circuit flow.
(2) fluid path of nozzle is sequentially connected peristaltic pump 7, shut-off valve 6, the liquid pressure regulator valve 5 with pressure gauge.Peristaltic pump is to use
In give liquid provide pressure, liquid pressure regulation valve regulation fluid path flow.
(3) the wet system of the control terminal of peristaltic pump and barn carry intelligent temperature control control 11 is connected.
(4) in chimney dust concentration it is excessively high or when flue gas flow rate is excessively high by increase calcium sulfur ratio maintain efficiency of dust collection and
Denitrification efficiency, i.e., dust concentration is excessively high in chimney or the excessively high namely barn of flue gas flow rate in temperature it is excessively high, will lead
It causes the signal of the wet system output of intelligent temperature control control stronger, spray liquid can be increased when peristaltic pump receives stronger signal, this just increases
Calcium sulfur ratio is added.(show that dust concentration drops to zone of reasonableness) after temperature drops to setting value by intelligence control system to subtract
Less or closing sprays.
In actual industrial process, nozzle is mounted on the top of chimney, after the white lime solution of ejection is mixed with flue gas adverse current
The cleanout in stack base is fallen, it is de- clearly in the form of sweeping up dust.
Test result shows that efficiency of dust collection reaches 85% or more, 63% or more desulfuration efficiency, 26% or more denitration efficiency.
The dust-removal and desulfurizing denitration technology feature of the handwarmer fire coal barn of the temperature triggered of the application patent is:
1, there is certain initial velocity by the fine droplet spray that gas shock flow generates in nozzle, it is this to carry initial velocity
Gas jet is formd when the atomized drop of degree sprays downwards in a longitudinal direction, the flowing of air-flow is disorderly because being presented when speed is excessive
Stream mode, turbulent pulsation cause that quality and momentum-exchange occur between jet stream and surrounding medium, make jet stream mass flow and
Vertical section product is continuously increased along the longitudinal direction, forms the cone-shaped field of flow spread to surrounding.The flowing of this gas jet
Characteristic exactly makes the effective collision number of water fog particle and dust particles increase, and the dust particles in flue gas are because staiing to water droplet
And be fixed, the SO in flue gas2It is removed because being dissolved in water droplet, as the contamination amount of soot dust granule becomes larger and water droplet
Mutual collision and fusion, the gravity suffered by final water droplet is more than that soot dust granule will be with water droplet when buoyancy caused by ascending air
Cleanout is fallen to, and water droplet is evaporated because of cleanout temperature excessively high (300 DEG C), then remaining soot dust granule is left in
Cleanout is removed in the form of sweep up dust.
It is to reach desulfurization effect by increasing calcium sulfur ratio when 2. organic sulfur largely discharges during coal.Coal
When quantity combusted is big, CO2Concentration it is high, fume amount is big, SO2Concentration it is high, the flow velocity of flue gas becomes larger;It is anti-under the chimney of equal length
It is just short between seasonable, it at this moment needs to spray into more Ca, the Ca/S ratios reflected at this time need higher.Practical measure shows to stablize
Calcium sulfur ratio needs between 3-5 when burning, in flue dust and SO2Calcium sulfur ratio, which needs to increase to 9 or more, when abrupt release can be only achieved
85% or more efficiency of dust collection, 63% or more desulfuration efficiency, 26% or more denitration efficiency.
3. the smoke exhaust process of chimney are the cyclically-varyings of a pulsed, when can start to spray in barn when the temperature is excessively high
Or spray is increased, just it is that coal-fired vigorous combustion release volume of smoke (is more than 15mg/m when the temperature is excessively high in barn3) and SO2It is (big
In 70ppm) stage, temperature do not spray into spray liquid when being not above set temperature value.
4. the circuit of peristaltic pump is connected with the wet system of intelligent temperature control control so that the wet system of intelligent temperature control control can be according to barn
Interior temperature change controls spray liquid, to achieve the purpose that adaptive.And does not increase additional control system, keep system simple
Reduction.
As it will be easily appreciated by one skilled in the art that the above is only the preferred embodiment of the utility model only, not
To limit the utility model, any modification made within the spirit and principle of the present invention, equivalent replacement and change
Into etc., it should be included within the scope of protection of this utility model.
Claims (4)
1. the handwarmer fire coal barn dust-removal and desulfurizing denitrification apparatus of temperature triggered, which is characterized in that including air atomizer spray nozzle
(4), air compressor (1), air cutoff valve (2), air pressure-adjusting valve (3), peristaltic pump (7), liquid stop valve (6), liquid tune
Pressure valve (5) and temperature sensor;
Air atomizer spray nozzle (4) setting is in barn chimney outlet for spraying into spray liquid, air atomizer spray nozzle (4) into chimney
One end connect gas path pipe, the other end of air atomizer spray nozzle connects fluid path pipeline;The other end of gas path pipe connects air
Compressor (1);The other end of fluid path pipeline connects peristaltic pump;Air cutoff valve (2) and with the air pressure-adjusting valve with pressure gauge
(3) it is located in gas path pipe;Liquid stop valve (6) and liquid pressure regulator valve (5) are located in fluid path pipeline;The control of peristaltic pump (7)
The output end of the included wet system of intelligent temperature control control of connection handwarmer fire coal barn in end processed;Temperature sensor is warm in stove for detecting
Degree, when temperature is more than predetermined temperature threshold, the wet system of intelligent temperature control control then starts peristaltic pump (7) and implements dust-removal and desulfurizing denitration.
2. the handwarmer fire coal barn dust-removal and desulfurizing denitrification apparatus of temperature triggered according to claim 1, which is characterized in that
The air atomizer spray nozzle includes ontology, and the upper end of ontology is rotation button, and lower end is jet expansion, in air atomizer spray nozzle
Portion side connects gas path pipe, and the other side connects fluid path pipeline, and body interior has a cavity, and screw rod is inserted into cavity and upper end connects
Rotation button is connect, screw rod can be driven to move up and down by turn knob, the input for moving up and down controllable liquid of thimble works as top
When needle rises to top, liquid input is maximum, and when thimble is down to bottommost, liquid input is zero.
3. the handwarmer fire coal barn dust-removal and desulfurizing denitrification apparatus of temperature triggered according to claim 1, which is characterized in that
The temperature sensor uses the temperature sensor that the wet system of intelligent temperature control control carries.
4. the handwarmer fire coal barn dust-removal and desulfurizing denitrification apparatus of temperature triggered according to claim 1, which is characterized in that
The spray liquid is any one in calcium hydroxide solution, magnesium hydroxide solution, limestone/gypsum slurries.
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CN201721547689.5U CN207805276U (en) | 2017-11-17 | 2017-11-17 | The handwarmer fire coal barn dust-removal and desulfurizing denitrification apparatus of temperature triggered |
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CN201721547689.5U CN207805276U (en) | 2017-11-17 | 2017-11-17 | The handwarmer fire coal barn dust-removal and desulfurizing denitrification apparatus of temperature triggered |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107837626A (en) * | 2017-11-17 | 2018-03-27 | 安徽中科自动化股份有限公司 | The handwarmer fire coal barn dust-removal and desulfurizing method of denitration and device of temperature triggered |
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2017
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
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CN107837626A (en) * | 2017-11-17 | 2018-03-27 | 安徽中科自动化股份有限公司 | The handwarmer fire coal barn dust-removal and desulfurizing method of denitration and device of temperature triggered |
CN107837626B (en) * | 2017-11-17 | 2023-05-12 | 安徽中科自动化股份有限公司 | Temperature-triggered dust removal, desulfurization and denitration method and device for hand-fired furnace coal-fired flue-curing barn |
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