CN205535856U - Incinerator - Google Patents
Incinerator Download PDFInfo
- Publication number
- CN205535856U CN205535856U CN201620278564.6U CN201620278564U CN205535856U CN 205535856 U CN205535856 U CN 205535856U CN 201620278564 U CN201620278564 U CN 201620278564U CN 205535856 U CN205535856 U CN 205535856U
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- CN
- China
- Prior art keywords
- incinerator
- heating chamber
- sulphur
- accumulation
- air port
- 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.)
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- 238000010438 heat treatment Methods 0.000 claims abstract description 50
- 238000009825 accumulation Methods 0.000 claims abstract description 39
- 238000002485 combustion reaction Methods 0.000 claims abstract description 34
- 206010001497 Agitation Diseases 0.000 claims description 47
- 238000013019 agitation Methods 0.000 claims description 47
- 229910052760 oxygen Inorganic materials 0.000 claims description 19
- 239000001301 oxygen Substances 0.000 claims description 19
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 18
- 239000003818 cinder Substances 0.000 claims description 13
- 239000007789 gas Substances 0.000 claims description 10
- 238000007664 blowing Methods 0.000 claims description 7
- 239000013589 supplement Substances 0.000 claims description 7
- 238000012423 maintenance Methods 0.000 claims description 5
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 abstract description 68
- 239000005864 Sulphur Substances 0.000 abstract description 59
- 239000000126 substance Substances 0.000 abstract description 49
- 239000000463 material Substances 0.000 abstract description 14
- 238000006243 chemical reaction Methods 0.000 abstract description 6
- QAOWNCQODCNURD-UHFFFAOYSA-L sulfate group Chemical group S(=O)(=O)([O-])[O-] QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 abstract description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 abstract description 3
- 235000011149 sulphuric acid Nutrition 0.000 abstract description 3
- 239000001117 sulphuric acid Substances 0.000 abstract description 3
- 230000002459 sustained effect Effects 0.000 abstract description 3
- 235000003891 ferrous sulphate Nutrition 0.000 abstract description 2
- 239000011790 ferrous sulphate Substances 0.000 abstract description 2
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 abstract description 2
- 229910000359 iron(II) sulfate Inorganic materials 0.000 abstract description 2
- 229940010514 ammonium ferrous sulfate Drugs 0.000 abstract 1
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 abstract 1
- 229910052921 ammonium sulfate Inorganic materials 0.000 abstract 1
- 235000011130 ammonium sulphate Nutrition 0.000 abstract 1
- SOIFLUNRINLCBN-UHFFFAOYSA-N ammonium thiocyanate Chemical compound [NH4+].[S-]C#N SOIFLUNRINLCBN-UHFFFAOYSA-N 0.000 abstract 1
- 238000000354 decomposition reaction Methods 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 150000003839 salts Chemical class 0.000 abstract 1
- 229910021653 sulphate ion Inorganic materials 0.000 abstract 1
- 238000002156 mixing Methods 0.000 description 18
- 239000000203 mixture Substances 0.000 description 14
- 239000000567 combustion gas Substances 0.000 description 12
- 229910052717 sulfur Inorganic materials 0.000 description 9
- 239000011593 sulfur Substances 0.000 description 9
- 238000009835 boiling Methods 0.000 description 7
- 239000002737 fuel gas Substances 0.000 description 6
- 239000002912 waste gas Substances 0.000 description 5
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 4
- 230000005484 gravity Effects 0.000 description 4
- 238000009413 insulation Methods 0.000 description 4
- 239000002893 slag Substances 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 206010002660 Anoxia Diseases 0.000 description 3
- 241000976983 Anoxia Species 0.000 description 3
- 206010021143 Hypoxia Diseases 0.000 description 3
- 230000007953 anoxia Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000004576 sand Substances 0.000 description 3
- 210000000038 chest Anatomy 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- 206010027295 Menometrorrhagia Diseases 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000005276 aerator Methods 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 150000002926 oxygen Chemical class 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 208000024891 symptom Diseases 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Abstract
The utility model relates to a chemical industry field especially relates to one kind and burns the incinerator that ammonium thiocyanate, ammonium sulfate and ferrous sulfate etc. Contain the thick sulphur of salt when preparing sulphuric acid. For the improvement mixes the conbustion ratio including the sulphur material, improve the conversion rate and the economic benefits of element sulphur, the utility model provides an incinerator, this incinerator include the furnace body, and the upper portion of furnace body is the combustion chamber, and the lower part is the heating chamber, be provided with the feed inlet on the lateral wall of combustion chamber and overhaul the clearance mouth, be provided with the air curtain machine in the feedstock channel of feed inlet, the top of heating chamber is provided with the heat accumulation roof that has the hole of exhausting, is provided with the gas burner on the lateral wall of heating chamber. This incinerator utilizes the gas sustained combustion to last the heating to the heat accumulation roof of heating chamber, keeps furnace bottom temperature, improves to mix including the conbustion ratio of sulphur material element sulphur and the rate of decomposition of sulphate, utilizes the exothermic increase combustion chamber bottom temperature of the burning production of sulphur, reduces the gas use amount of heating chamber, and reduce cost improves economic benefits.
Description
Technical field
This utility model relates to chemical field, particularly relates to burn with sulfate and sulfur when one prepares sulphuric acid
The incinerator of the thick sulfur that acid is ferrous.
Background technology
At present, when preparing sulphuric acid, it is common that use fluidized bed furnace to containing sulfate or ferrous sulfate, sulfur
The sulphur-containing substance that mixes burn, to generate SO2(sulfur dioxide) gas.Mix sulphur-containing substance in boiling
When stove carries out Boiling Combustion, relatively big owing to mixing the density of sulphur-containing substance, have part in combustion
Also have not enough time to fully burn and just stored by the sand etc. being laid on air compartment top in fluidized bed furnace because action of gravity falls
On the material bed that hot material and a small amount of comburant are formed, and high temperature material bed is utilized to mix sulphur-containing substance to fall
Carry out second-time burning, thus be allowed to burning fully, and then improve conversion ratio and the economic benefit of element sulphur.But
Be, existing fluidized bed furnace to mix sulphur-containing substance burn time, be all to be blown into cold in burner hearth by air compartment
Wind is so that mixing sulphur-containing substance Boiling Combustion in burner hearth, and after the comburant burning to the greatest extent on material bed, expects bed
By absorb sulphur-containing substance Boiling Combustion produce heat maintain high temperature, therefore, when mix sulphur-containing substance because of
When the cold wind being filled with seethes with excitement above burner hearth, mix sulphur-containing substance burning position distance material bed in burner hearth relatively
Far, it is unfavorable for expecting that bed absorbs heat, causes expecting that bed tempertaure reduces because absorbing enough heats, and
In burner hearth, it is filled with cold wind by air compartment and further reduces the temperature of material bed.As can be seen here, fluidized bed furnace is worked as
After comburant burning to the greatest extent on middle material bed, material bed tempertaure declines, and then causes falling mixing sulfur-bearing on material bed
The combustion rate of material declines, and is allowed to fully to burn, and even can form sulfur because of the sulfur fallen on material bed
Sulphur frit or be combined into husky block with the sand on material bed and the air inlet of burner hearth bottom is blocked cause fluidized bed furnace to stop
Fire, it is impossible to run continuously.
Utility model content
For improving the combustion rate mixing sulphur-containing substance, improve conversion ratio and economic benefit, this practicality of element sulphur
Novel proposition one incinerator, this incinerator includes body of heater, and the top of described body of heater is combustor, bottom
For heating chamber；It is provided with charging aperture on the sidewall of described combustor and overhauls clean-up port, and described charging aperture
Air curtain it is provided with in feeding-passage；The top of described heating chamber is provided with the accumulation of heat top board with steam vent,
And it is provided with gas nozzle on the sidewall of described heating chamber.Gas nozzle is utilized to spray into combustion gas in heating chamber,
Combustion gas sustained combustion carries out continuous heating to the accumulation of heat top board of heating chamber, can keep burner hearth bottom temp, it is simple to
The sulphur-containing substance that mixes fallen in burner hearth on accumulation of heat top board carries out second-time burning, thus solves to mix sulphur-containing substance
Because burner hearth bottom temperature be difficult to raise and cannot clean-burning problem, improve mix the combustion of sulfur in sulphur-containing substance
Burning rate and the resolution ratio of sulfate, and then improve the conversion ratio of the element sulphur mixed in sulphur-containing substance；Profit simultaneously
The heat produced with combustion of sulfur is heated the accumulation of heat top board absorption of room and promotes or maintain temperature, can reduce heating
The usage amount of required combustion gas, reduces cost, increases economic efficiency.It addition, arrange band at heating chamber top
There is the accumulation of heat top board of steam vent, thus the high-temp waste gas that fuel gas buring produces is drained into burning by steam vent
Indoor, reduce the usage amount of combustion gas further, reduce cost, increase economic efficiency.
Preferably, described steam vent is provided with on switch cover, and the sidewall of described heating chamber and is provided with aerofluxus
Mouthful.So, when the temperature in burner hearth is sufficiently high, the high temperature that fuel gas buring produces can be made to give up by closing switch lid
Gas is discharged to outside body of heater from air vent, it is to avoid temperature in burner hearth continues to raise, and in keeping heating chamber
Air circulates, it is to avoid combustion gas cannot be burnt because of anoxia.
Preferably, being provided with agitation air port on the sidewall of described combustor, described agitation air port includes main stirring
Wind symptom mouth and secondary agitation air port, and described main agitation air port is less than the height of described charging aperture in the vertical direction
Degree, described secondary agitation air port is higher than the height of described charging aperture in the vertical direction.So, staff
Agitation air-flow and oxygen can be filled into step by step in burner hearth as desired by agitation air port, and by agitation air-flow
Drive mixes sulphur-containing substance and rises, thus extends and mix sulphur-containing substance burning time in burner hearth, and passes through
The oxygen filled into improves the oxygen concentration in burner hearth, thus improves and mix sulphur-containing substance combustion rate in burner hearth.
Further, described main agitation air port is thrown with the level of described charging aperture line on described Inner Wall of Combustion Chamber
Shadow is camber line, and the arc range of this camber line is (0, π), to avoid stirring air-flow and air curtain discharge
In the same direction or front Xiang Chong, impact mixes sulphur-containing substance and rises with air-flow air-flow.It is further preferred that described combustion
Burn and be provided with oxygen supplement mouth on the sidewall of room, and described oxygen supplement mouth is positioned at the lower section in described main agitation air port close
Described main agitation air port, to fill into oxygen in burner hearth, improves the oxygen content in burner hearth, and then improves mixed
The combustion rate of miscellaneous sulphur-containing substance.
Preferably, the sidewall of described combustor being provided with observation panel, this observation panel is phase with described charging aperture
To arranging and near described heating chamber.So, staff can be observed by observation panel and mix sulphur-containing substance and exist
Combustion case in burner hearth, and result carries out corresponding operating according to the observation, thus improve and mix sulphur-containing substance
Combustion rate.
Preferably, described accumulation of heat top board is provided with leakage cinder hole, and this leakage cinder hole is near described accumulation of heat top board
Edge；It is provided with slag-drip opening on the sidewall of described heating chamber, and this slag-drip opening is near the bottom of described heating chamber.
Further, the sidewall of described combustor being provided with ash blowing mouth, this ash blowing mouth is relative with described leakage cinder hole to be set
Put and near described accumulation of heat top board.So, when burner hearth is cleared up, only one drum need to be set in ash blowing mouth
Blower fan is air blast in burner hearth, the slag ash piled up can be blowed to Lou cinder hole, and menometrorrhagia cinder hole falls on accumulation of heat top board
At slag-drip opening, simple to operation.
Preferably, in described heating chamber, it is provided with support column, and this support column is positioned at described accumulation of heat top board and institute
State between the bottom of heating chamber and accumulation of heat top board described in vertical support, to avoid accumulation of heat top board to drop.Further
Ground, described accumulation of heat top board includes supporting layer and recuperation layer, and described recuperation layer is positioned at the top of described supporting layer.
Can further improve the heat insulation effect of heating chamber, reduce heat losses, thus reduce heating cost.
The incinerator that the utility model proposes by the heating chamber being arranged on burner hearth bottom combustion gas to stove
Carry out continuous heating bottom thorax, thus keep the temperature of burner hearth bottom, and then make mixing at burner hearth bottom
Sulphur-containing substance is heated second-time burning, improves the combustion rate mixing sulphur-containing substance, and then improves element sulphur
Conversion ratio, and by the steam vent on accumulation of heat top board, the high-temp waste gas that fuel gas buring produces is discharged in burner hearth,
Temperature in liter blast furnace hearth, and reduce the usage amount of combustion gas, and then reduce heating cost, increase economic efficiency.
Burner hearth sidewall arranges main agitation air port and secondary agitation air port in burner hearth, blasts agitation air-flow, and by stirring
Moving air flow drives and mixes sulphur-containing substance rising, thus extends the burning time mixing sulphur-containing substance, improves burning
Rate.Below agitation air port, oxygen supplement mouth is set to fill into oxygen in burner hearth, improves the oxygen content in burner hearth,
And then improve the combustion rate mixing sulphur-containing substance.
Accompanying drawing explanation
Fig. 1 is the front sectional view of this utility model incinerator.
Detailed description of the invention
As it is shown in figure 1, this utility model incinerator includes body of heater also known as Li Shi stove, the top of body of heater is for burning
Mixing the burner hearth 1 i.e. combustor of sulphur-containing substance, bottom is heating chamber 2.It is provided with on the sidewall of heating chamber 2
Spraying into the gas nozzle 21 of combustion gas in heating chamber 2, combustion gas is burnt in heating chamber 2 can be to burner hearth 1
Bottom is heated, and to improve or to maintain the temperature bottom burner hearth 1, and then avoids mixing the combustion of sulphur-containing substance
Burning rate reduces because the temperature bottom burner hearth 1 reduces.
The sidewall of burner hearth 1 is provided with charging aperture 11, and in the feeding-passage connected with this charging aperture 11
It is provided with and the sulphur-containing substance that mixes entering in burner hearth 1 from charging aperture 11 is dispelled the air curtain in burner hearth 1
12, in order to improve and mix the sulphur-containing substance combustion rate on burner hearth 1 top, what minimizing fell mixes sulfur-bearing thing
The amount of matter；The sidewall of burner hearth 1 is provided with maintenance clean-up port 18, and this maintenance clean-up port 18 and charging aperture
11 in being arranged oppositely, in order to staff enters through this maintenance clean-up port 18 the most as required
To burner hearth 1 is internal, burner hearth is carried out maintenance cleaning, especially remove the interior combustion residue piled up of burner hearth 1.Excellent
Selection of land, is provided with main agitation air port 13, and main agitation air port 13 in the vertical direction on the sidewall of burner hearth 1
Height less than charging aperture 11, so, in burning process, blast in burner hearth 1 from main agitation air port 13
Agitation air-flow, this agitation air-flow can drive and mix sulphur-containing substance rising, thus extend and mix sulphur-containing substance at stove
Boiling time in thorax 1 i.e. burning time, both improve the combustion rate mixing sulphur-containing substance, and decreased again
Under the amount mixing sulphur-containing substance.Main agitation air port 13 and the charging aperture 11 line on burner hearth 1 inwall
Floor projection is camber line, and the arc range of this camber line is (0, π), so, can avoid because of main agitation wind
Mouth 13 is positioned at the underface of charging aperture 11 and causes being entered by main agitation air port 13 the agitation air-flow of burner hearth 1
In the same direction, or because main agitation air port 13 and charging aperture 11 are in vis-a-vis for the air-flow discharged with air curtain 12
The air-flow arranged and cause the agitation air-flow being entered in burner hearth 1 by main agitation air port 13 to be discharged with air curtain 12
Front Xiang Chong, makes the sulphur-containing substance that mixes fallen by action of gravity rise with agitation air-flow, thus extends and mix
Sulphur-containing substance boiling time in burner hearth 1, and then improve the combustion rate mixing sulphur-containing substance.Preferably,
The sidewall of burner hearth 1 is provided with oxygen supplement mouth 14, and this oxygen supplement mouth 14 is positioned at below main agitation air port 13 and
Near this main agitation air port 13.So, in burning process, can be supplemented in burner hearth 1 by oxygen supplement mouth 14
Air or oxygen, to improve the oxygen content in burner hearth 1, improves the combustion rate mixing sulphur-containing substance further.
Preferably, being provided with secondary agitation air port on the sidewall of burner hearth 1, this secondary agitation air port is at vertical direction
On height be i.e. positioned at the upside of charging aperture 11 higher than charging aperture 11, for filling into air in burner hearth 1,
Extend further and mix sulphur-containing substance boiling time in burner hearth 1, and fill into oxygen in burner hearth 1, with
The sulphur-containing substance that mixes exempted from burner hearth 1 burns insufficient because of anoxia.Preferably, secondary agitation air port includes
Two grades stir air ports 15 and three grades of agitation air ports 16, and three grades of agitation air ports 16 are positioned at two grades of agitation air ports 15
Top, thus utilize agitation air port to fill into agitation air-flow and oxygen step by step in burner hearth 1, and then improve mixed
The combustion rate of miscellaneous sulphur-containing substance.Preferably, the sidewall of burner hearth 1 is provided with observation panel 17, and this observation
Mouth 17 and charging aperture 11 are in being oppositely arranged and near heating chamber 2.So, in burning process, staff
Can directly be observed mixing sulphur-containing substance combustion case in burner hearth 1 by observation panel 17, it is possible to
Result carries out corresponding operating according to the observation, to improve the combustion rate mixing sulphur-containing substance.
The top of heating chamber 2 is provided with accumulation of heat top board 22, owing to the combustion gas sustained combustion in heating chamber 2 adds
Heat, the temperature of accumulation of heat top board 22 can maintain a higher temperature, mixes sulphur-containing substance made by gravity when having
After falling on accumulation of heat top board 22, because of being heated, second-time burning can occur.So, accumulation of heat top board 22 is fallen
On mix sulphur-containing substance because fully being burnt through second-time burning, improve the combustion mixing sulphur-containing substance
Burning rate, and then improve the conversion ratio of element sulphur.Accumulation of heat top board 22 is provided with one or more leakage cinder hole
23, this leakage cinder hole 23 is near the edge of accumulation of heat top board, and is provided with on the sidewall of heating chamber 2 and leaks cinder hole
The slag-drip opening 24 that 23 positions are corresponding.So, too high because of the temperature of burner hearth 1 when the combustion residue in burner hearth 1
And when melting as pulp water, this pulp water leaves and drops into, by leakage cinder hole 23, the slag chute connected with slag-drip opening 24
In, then it is discharged to outside body of heater through slag-drip opening 24, it is simple to furnace interior is cleared up.The top of heating chamber 2
Being provided with a steam vent 27 on portion i.e. accumulation of heat top board 22, this steam vent 27 sets in relative with gas nozzle 21
Putting, so, during fuel gas buring, the high-temp waste gas that burning produces can be entered into by this steam vent 27
In burner hearth 1, thus rise the temperature in blast furnace hearth 1, improve the utilization rate of the heat that fuel gas buring produces, fall
The low consumption of combustion gas, and then reduce and burn the cost mixing sulphur-containing substance.Preferably, at steam vent
It is provided with on 27 for opening or the switch cover (not shown) of closed grate hole 27, and in heating chamber 2
Sidewall on an air vent 28 is set, and this air vent 28 with gas nozzle 21 in being oppositely arranged and close
Accumulation of heat top board 22.So, when in burner hearth 1, temperature is sufficiently high or the high-temp waste gas shadow that is drained in burner hearth 1
Ring SO in body of heater2During the concentration of gas, close the steam vent 27 on accumulation of heat top board 22 and open heating 2 sides
Air vent 28 on wall, the high-temp waste gas making fuel gas buring produce is discharged to, outside body of heater, both may be used from air vent 28
To avoid the temperature in burner hearth 1 to continue to raise, the air in heating chamber 2 can be kept again circulate, it is to avoid fire
Gas jets 21 is sprayed onto the combustion gas in heating chamber 2 and cannot burn because of anoxia.Preferably, at the sidewall of burner hearth 1
On be provided with ash blowing mouth 25, and this ash blowing mouth 25 near accumulation of heat top board 22 and with mud hole 23 in just to setting.
So, when needing the slag ash piled up on the waste residue in burner hearth 1 especially accumulation of heat top board 22 is cleared up,
One aerator air blast in burner hearth 1 can be set at ash blowing mouth 25, thus will fall on accumulation of heat top board 22
Slag ash blow to Lou cinder hole 23, then be discharged to outside body of heater through slag-drip opening 24.Preferably, in heating chamber 2
It is provided perpendicular to the support column 26 of the heat-insulation layer of the bottom of heating chamber 2, and this support column 26 is used for supporting storage
Hot top plate 22, so as not to accumulation of heat top board 22 by action of gravity or load-bearing bigger time drop.Preferably, accumulation of heat top
Plate 22 includes supporting layer and recuperation layer, and supporting layer is positioned at the lower section of recuperation layer, and supporting layer can use insulation
Brick one-tenth, recuperation layer can use sand or fire clay to lay and form, improve the accumulation of heat of accumulation of heat top board 22 further
Heat insulation effect.
Claims (10)
1. an incinerator, it is characterised in that this incinerator includes body of heater, and the top of described body of heater is combustor,
Bottom is heating chamber；Charging aperture and maintenance clean-up port, and described charging it is provided with on the sidewall of described combustor
It is provided with air curtain in the feeding-passage of mouth；The top of described heating chamber is provided with the accumulation of heat top with steam vent
It is provided with gas nozzle on plate, and the sidewall of described heating chamber.
Incinerator the most according to claim 1, it is characterised in that be provided with switch cover on described steam vent,
And it is provided with air vent on the sidewall of described heating chamber.
Incinerator the most according to claim 2, it is characterised in that be provided with on the sidewall of described combustor
Agitation air port, described agitation air port includes main agitation air port and secondary agitation air port, and described main agitation air port
Less than the height of described charging aperture in the vertical direction, described secondary agitation air port is being erected higher than described charging aperture
Nogata height upwards.
Incinerator the most according to claim 3, it is characterised in that described main agitation air port and described charging aperture
The floor projection of the line on described Inner Wall of Combustion Chamber is camber line, and the arc range of this camber line is (0, π).
Incinerator the most according to claim 3, it is characterised in that be provided with benefit on the sidewall of described combustor
Oxygen mouth, and described oxygen supplement mouth is positioned at the lower section in described main agitation air port and near described main agitation air port.
6. according to the incinerator described in any one in claim 1-5, it is characterised in that the side of described combustor
Being provided with observation panel on wall, this observation panel and described charging aperture are in being oppositely arranged and near described heating chamber.
7. according to the incinerator described in any one in claim 1-5, it is characterised in that on described accumulation of heat top board
It is provided with leakage cinder hole, and this leakage cinder hole is near the edge of described accumulation of heat top board；Set on the sidewall of described heating chamber
It is equipped with slag-drip opening, and this slag-drip opening is near the bottom of described heating chamber.
Incinerator the most according to claim 7, it is characterised in that be provided with on the sidewall of described combustor and blow
Ash mouth, this ash blowing mouth and described leakage cinder hole are oppositely arranged and near described accumulation of heat top board.
9. according to the incinerator described in any one in claim 1-5, it is characterised in that set in described heating chamber
It is equipped with support column, and this support column and vertically props up between described accumulation of heat top board and the bottom of described heating chamber
Support described accumulation of heat top board.
10. according to the incinerator described in any one in claim 1-5, it is characterised in that described accumulation of heat top board bag
Include supporting layer and recuperation layer, and described recuperation layer is positioned at the top of described supporting layer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620278564.6U CN205535856U (en) | 2016-04-06 | 2016-04-06 | Incinerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620278564.6U CN205535856U (en) | 2016-04-06 | 2016-04-06 | Incinerator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205535856U true CN205535856U (en) | 2016-08-31 |
Family
ID=57142097
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620278564.6U Active CN205535856U (en) | 2016-04-06 | 2016-04-06 | Incinerator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205535856U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105698195A (en) * | 2016-04-06 | 2016-06-22 | 李金山 | Incinerator |
| CN116161627A (en) * | 2022-12-13 | 2023-05-26 | 福建天甫电子材料有限公司 | Sulfur incinerator for electronic grade sulfuric acid preparation |
-
2016
- 2016-04-06 CN CN201620278564.6U patent/CN205535856U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105698195A (en) * | 2016-04-06 | 2016-06-22 | 李金山 | Incinerator |
| CN116161627A (en) * | 2022-12-13 | 2023-05-26 | 福建天甫电子材料有限公司 | Sulfur incinerator for electronic grade sulfuric acid preparation |
| CN116161627B (en) * | 2022-12-13 | 2023-08-22 | 福建天甫电子材料有限公司 | Sulfur incinerator for electronic grade sulfuric acid preparation |
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Effective date of registration: 20210702 Address after: 337000 beside 320 National Road, santian management office, Pingxiang economic and Technological Development Zone, Pingxiang City, Jiangxi Province Patentee after: PINGXIANG XIN'AN ENVIRONMENTAL PROTECTION ENGINEERING Co.,Ltd. Address before: 337000 Room 101, unit 2, building 1, No.3, Yijing lane, Fenghuang street, Anyuan District, Pingxiang City, Jiangxi Province Patentee before: Li Jinshan |