CN208003727U - Magnesia FGD tower pulping system and combustion apparatus - Google Patents
Magnesia FGD tower pulping system and combustion apparatus Download PDFInfo
- Publication number
- CN208003727U CN208003727U CN201820040526.6U CN201820040526U CN208003727U CN 208003727 U CN208003727 U CN 208003727U CN 201820040526 U CN201820040526 U CN 201820040526U CN 208003727 U CN208003727 U CN 208003727U
- Authority
- CN
- China
- Prior art keywords
- conveyance conduit
- conveyer
- milk tank
- magnesia
- pulping system
- 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.)
- Expired - Fee Related
Links
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 title claims abstract description 173
- 239000000395 magnesium oxide Substances 0.000 title claims abstract description 91
- 238000004537 pulping Methods 0.000 title claims abstract description 19
- 238000002485 combustion reaction Methods 0.000 title claims abstract description 17
- 239000008267 milk Substances 0.000 claims abstract description 73
- 210000004080 milk Anatomy 0.000 claims abstract description 73
- 235000013336 milk Nutrition 0.000 claims abstract description 73
- 239000000945 filler Substances 0.000 claims abstract description 19
- 238000006243 chemical reaction Methods 0.000 claims description 9
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims description 4
- 230000003647 oxidation Effects 0.000 claims description 4
- 238000007254 oxidation reaction Methods 0.000 claims description 4
- 230000001133 acceleration Effects 0.000 claims description 3
- 230000003009 desulfurizing effect Effects 0.000 claims description 3
- 238000009434 installation Methods 0.000 claims description 3
- 229910052749 magnesium Inorganic materials 0.000 claims description 2
- 239000011777 magnesium Substances 0.000 claims description 2
- 239000007789 gas Substances 0.000 abstract description 20
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 abstract description 13
- 239000000347 magnesium hydroxide Substances 0.000 abstract description 13
- 229910001862 magnesium hydroxide Inorganic materials 0.000 abstract description 13
- 238000002425 crystallisation Methods 0.000 abstract description 10
- 230000008025 crystallization Effects 0.000 abstract description 10
- 239000003517 fume Substances 0.000 abstract description 2
- 239000000843 powder Substances 0.000 description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 14
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 9
- 238000010586 diagram Methods 0.000 description 8
- 230000000903 blocking effect Effects 0.000 description 4
- 239000003245 coal Substances 0.000 description 4
- 239000000779 smoke Substances 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 3
- 239000006210 lotion Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000009835 boiling Methods 0.000 description 2
- 238000006477 desulfuration reaction Methods 0.000 description 2
- 230000023556 desulfurization Effects 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000003287 bathing Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 230000006870 function Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000004044 response Effects 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
A kind of magnesia FGD tower pulping system of the utility model offer and combustion apparatus, are related to the technical field of fume treatment auxiliary.Magnesia FGD tower pulping system includes filler bin, conveyer, conveyance conduit and milk tank；The outlet of the filler bin is connect with the entrance of the conveyer, and the outlet of the conveyer is connect with the entrance of the conveyance conduit, and the outlet of the conveyance conduit is connect with the milk tank；Control valve is connected on the conveyance conduit, the control valve controls the opening and closing of the conveyance conduit；The milk tank is connected with discharge duct, and the discharge duct discharges the gas after being reacted in the milk tank.The both ends for solving conveyance conduit are always in the open state, and the steam in milk tank enters the problem of conveyer generates the crystallization of multilayer magnesium hydroxide.The utility model installs control valve on conveyance conduit, prevents the steam in milk tank from entering in conveyer using control valve, is protected to conveyer.
Description
Technical field
The utility model is related to the technical fields of fume treatment auxiliary, more particularly, to a kind of magnesia FGD tower slurrying system
System and combustion apparatus.
Background technology
Coal-burning boiler refers to generating steam after the coal heat of fuel combustion is inverted or becoming the boiler of hot water.I
State's coal-burned industrial boiler has hundreds of thousands platform, coal-burning boiler to classify according to purposes, is broadly divided into coal-fired hot water boiler, coal fuel heating
Homogeneous solution-type reactor, coal-fired steam boiler, coal burning heat-conducting oil boiler, for supplying boiling water, coal-fired hot-water boiler is used for coal-fired hot water boiler
Heating and bathing, coal-fired steam boiler are used for boiling and drying for supplying steam, coal burning heat-conducting oil boiler.The use of coal-burning boiler
Way is different, and combustion system, heat-supplying mode and exhaust gas temperature are also different.Coal-burning boiler is during burning, general body
The efficiency of combustion of the bigger boiler of product can be relatively high, and efficiency of combustion is usually between 60%-80%.
Currently, when boiler oxidation magnesium desulfurization refers to that magnesia cures in milk tank, directly uses and be steam heated to 68 DEG C
Magnesia slurry, is then delivered in magnesia FGD tower, magnesium hydroxide is reacted with boiler smoke in desulfurizing tower by left and right.
The both ends of magnesium oxide delivery pipeline are always in the open state, and the hot water and steam in milk tank is defeated by magnesia
Send pipeline that will be directly entered in magnesia conveyer, keep the inner wall of magnesia conveyer moist, be magnesia and vapor it
Between reaction, production magnesium hydroxide create good condition.When conveying magnesia toward milk tank, magnesia is defeated with magnesia
Water on material machine inner wall will react generation magnesium hydroxide, and one layer of hard magnesium hydroxide is generated on magnesia conveyer inner wall
Crystallization, it is intermittent to carry out conveying magnesia, since the both ends of magnesium oxide delivery pipeline are always in the open state, in milk tank
Steam can enter magnesia conveyer all along magnesium oxide delivery pipeline, the crystallization of magnesium hydroxide in magnesia conveyer
Surface on just can adhere to vapor again, react one layer of new magnesium hydroxide of production again with magnesia and crystallizes, repeat this for a long time
The process of sample will generate the crystallization of multilayer magnesium hydroxide on the inner wall of magnesia conveyer, make the sky of magnesium oxide delivery pipeline
Between become smaller, result even in magnesium oxide delivery pipeline blocking, at this point, the inner wall of magnesia conveyer will be with magnesia delivery pipe
Hard friction occurs for the crystallization of hard magnesium hydroxide on road inner wall, has damaged the component of magnesia conveyer.
Utility model content
The purpose of this utility model is to provide a kind of magnesia FGD tower pulping systems, to solve to exist in the prior art
, the both ends of magnesium oxide delivery pipeline are always in the open state, and the steam in milk tank will be along magnesia delivery pipe
Road enters magnesia conveyer, and the crystallization of multilayer magnesium hydroxide will be generated on the inner wall of magnesia conveyer, causes magnesia
The space of conveyance conduit becomes smaller, or even the technical issues of blocking magnesium oxide delivery pipeline.
The utility model also provides a kind of combustion apparatus, to solve in the prior art, the both ends one of magnesium oxide delivery pipeline
The straight state in opening is easy to generate the crystallization of multilayer magnesium hydroxide in the inner wall of magnesia conveyer, magnesia is caused to convey
The space of pipeline becomes smaller, or even the technical issues of blocking magnesium oxide delivery pipeline.
A kind of magnesia FGD tower pulping system provided by the utility model, including filler bin, conveyer, conveyance conduit and
Milk tank；
The outlet of the filler bin is connect with the entrance of the conveyer, the outlet of the conveyer and the conveyance conduit
Entrance connection, the outlet of the conveyance conduit is connect with the milk tank；
Control valve is connected on the conveyance conduit, the control valve controls the opening and closing of the conveyance conduit
System；
The milk tank is connected with discharge duct, and the discharge duct releases the gas after being reacted in the milk tank
It puts.
Further, the control valve is manually-operated gate, and the manually-operated gate is convenient for manually to the opening and closing of valve progress
Control.
Further, the control valve is electrically operated valve.
Further, check device is connected in the conveyance conduit, the check device can prevent the delivery pipe
Magnesia in road and gas backflow.
Further, the height of one end that the conveyance conduit is connect with the conveyer, be more than the conveyance conduit with
The height of described tank connected one end of lotion.
Further, the conveyer uses spiral conveyer.
Further, filter is connected in the discharge duct, after the filter in the milk tank to reacting
Gas is filtered.
Further, fan is connected in the discharge duct, the fan is to the gas after being reacted in the milk tank
Carry out acceleration discharge.
Further, the quantity of the conveyance conduit is multiple, and the quantity of the outlet of the conveyer is and the conveying
The quantity of pipeline is corresponding multiple；
The entrance of each conveyance conduit is connect with the outlet of the conveyer, the outlet of each conveyance conduit and the lotion
Tank connects.
The utility model also provides a kind of combustion apparatus, the combustion apparatus installation magnesia FGD tower slurrying system
System.
A kind of magnesia FGD tower pulping system provided by the utility model, the filler bin are interior for storing magnesia
The outlet of powder, the filler bin is connect with the entrance of the conveyer, enables magnesia powder along the entrance of the conveyer
Conveying, the outlet of the conveyer are connect with the entrance of the conveyance conduit, keep the magnesia powder in conveyer defeated along exporting
After going out, it is directly entered the conveyance conduit, magnesia powder is conveyed using the conveyance conduit, the conveyance conduit goes out
Mouth is connect with the milk tank, magnesia powder is delivered in milk tank, slurries after curing are delivered to desulfurization by emulsion pumps
In tower, reacted with the flue gas in desulfurizing tower；Control valve is connected on the conveyance conduit, the control valve is to institute
The opening and closing for stating conveyance conduit is controlled, and enters the conveying along conveyance conduit so as to avoid the steam in the milk tank
In machine, steam and magnesia powder is made repeatedly to crystallize, the damage caused by conveyer；It is connected with exhaust pipe on the milk tank
Road discharges the gas after being reacted in the milk tank using the discharge duct, avoids the gas in the milk tank
Body pressure is excessive, is protected to milk tank.
The utility model also provides a kind of combustion apparatus, which is equipped with above-mentioned magnesia FGD tower slurrying system
System, control valve is installed on conveyance conduit, prevents the steam in milk tank from entering in conveyer using control valve, with oxidation
The crystallization of multilayer that magnesium powder is combined into needs in use, just open control valve, to make magnesia powder along conveyer and delivery pipe
Road enters in milk tank, to be protected to conveyer.
Description of the drawings
It, below will be right in order to illustrate more clearly of specific embodiment of the present invention or technical solution in the prior art
Specific implementation mode or attached drawing needed to be used in the description of the prior art are briefly described, it should be apparent that, it is described below
In attached drawing be that some embodiments of the utility model are not paying creativeness for those of ordinary skill in the art
Under the premise of labour, other drawings may also be obtained based on these drawings.
Fig. 1 is the structural schematic diagram for the first connection type that the utility model embodiment provides；
Fig. 2 is the structural schematic diagram for second of connection type that the utility model embodiment provides；
Fig. 3 is the structural schematic diagram for the third connection type that the utility model embodiment provides；
Fig. 4 is the structural schematic diagram for the 4th kind of connection type that the utility model embodiment provides.
Icon：100- filler bins；200- conveyers；300- conveyance conduits；400- milk tanks；301- control valves；
302- check devices；401- discharge ducts；402- filters；403- fans.
Specific implementation mode
The technical solution of the utility model is clearly and completely described below in conjunction with attached drawing, it is clear that described
Embodiment is the utility model a part of the embodiment, instead of all the embodiments.Based on the embodiments of the present invention, originally
The every other embodiment that field those of ordinary skill is obtained without making creative work, belongs to this practicality
Novel protected range.
It is in the description of the present invention, it should be noted that term "center", "upper", "lower", "left", "right", " perpendicular
Directly ", the orientation or positional relationship of the instructions such as "horizontal", "inner", "outside" is to be based on the orientation or positional relationship shown in the drawings, and is only
The utility model and simplifying describes for ease of description, do not indicate or imply the indicated device or element must have it is specific
Orientation, with specific azimuth configuration and operation, therefore should not be understood as limiting the present invention.In addition, term " the
One ", " second ", " third " are used for description purposes only, and are not understood to indicate or imply relative importance.
In the description of the present invention, it should be noted that unless otherwise clearly defined and limited, term " is pacified
Dress ", " connected ", " connection " shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integrally
Connection；It can be mechanical connection, can also be electrical connection；Can be directly connected, can also indirectly connected through an intermediary,
It can be the connection inside two elements.For the ordinary skill in the art, it can understand above-mentioned art with concrete condition
The concrete meaning of language in the present invention.
Fig. 1 is the structural schematic diagram for the first connection type that the utility model embodiment provides.
As shown in Figure 1, a kind of magnesia FGD tower pulping system provided by the utility model, including filler bin 100, conveying
Machine 200, conveyance conduit 300 and milk tank 400；
The outlet of the filler bin 100 is connect with the entrance of the conveyer 200, the outlet of the conveyer 200 and institute
The entrance connection of conveyance conduit 300 is stated, the outlet of the conveyance conduit 300 is connect with the milk tank 400；
Control valve 301 is connected on the conveyance conduit 300, the control valve 301 is to the conveyance conduit 300
Opening and closing controlled；
The milk tank 400 is connected with discharge duct 401, after the discharge duct 401 is to reaction in the milk tank 400
Gas discharged.
Filler bin 100 connects for storing magnesia powder, the outlet of 100 lower end of filler bin with the entrance of 200 left end of conveyer
It connects, after so that the magnesia powder in filler bin 100 is flowed out along the outlet of lower end, is directly entered the entrance of conveyer 200, utilization is defeated
Material machine 200 conveys magnesia powder.
The outlet of 200 right end of conveyer is connect with the entrance of 300 upper end of conveyance conduit, makes magnesia powder in filler bin 100
Outlet along conveyer 200 downwards conveying after, along conveyance conduit 300 entrance convey, magnesia powder is along conveyance conduit
It after 300 are delivered to outlet, is directly entered in milk tank 400, water is passed through in milk tank 400, carrying out steam to milk tank 400 adds
Heat makes to generate steam in milk tank 400, and the water be conducive in milk tank 400 is reacted with magnesia powder.
Control valve 301 is set on conveyance conduit 300, when carrying out steam heating to milk tank 400, opens control valve
Door 301 makes the magnesia powder in filler bin 100 be conveyed downwards along conveyer 200, is delivered to then along conveyance conduit 300
It is reacted in milk tank 400, at this moment, control valve 301 is closed, to prevent in milk tank 400 generated steam again
Enter in conveyer 200 along conveyance conduit 300, is reacted with the magnesia powder in conveyer 200 and generate magnesium hydroxide crystallization, it is right
Blocking caused by 200 inner wall of conveyer.
It is connected with discharge duct 401 in the upper end of milk tank 400, when the air pressure in milk tank 400 is relatively high, can be beaten
The feed channel that begins to rehearse 401 discharges the gas in milk tank 400, excessively high to avoid the air pressure in milk tank 400, to lotion
Tank 400 damages.
Further, the control valve 301 be manually-operated gate, the manually-operated gate convenient for manually to the opening and closing of valve into
Row control.
Manually-operated gate is as the control unit in Pipeline transport, for changing opening and closing and the magnesia powder of conveyance conduit 300
Flow direction, have the function of water conservancy diversion, cut-off, adjusting, throttling, non-return etc..
It can be at any time according to the response situation in milk tank 400, manually to the opening and closing of conveyance conduit 300 using manually-operated gate
It is controlled, since using manually mode, more convenient operating personnel control the opening and closing of conveyance conduit 300.
Further, the control valve 301 is electrically operated valve.
Electrically operated valve is exactly with electronic actuator control valves door, to realize the on and off of valve.The action of electrically operated valve
Moment is bigger than common valve, but the breaker acting speed of electrically operated valve can adjust, and simple in structure, easy care, to liquid
Body medium and Large Diameter Pipeline gas effectiveness are good, weatherproof, in use, not by the pressure influence of compressed air, it is adaptable.
Fig. 2 is the structural schematic diagram for second of connection type that the utility model embodiment provides.
As shown in Fig. 2, it is further, check device 302, the check device 302 are connected in the conveyance conduit 300
It can prevent the magnesia in the conveyance conduit 300 and gas backflow.
Check-valves may be used in check device 302, and check-valves is arranged in the lower part of control valve 301, can prevent from conveying
Medium in pipeline 300 and milk tank 400 is flow backwards, and is protected to the medium in conveyance conduit 300, to conveyance conduit
300 are protected.
Check device 302 can also use non-return pad, and non-return pad is arranged in the lower part of control valve 301, makes magnesia powder
Downwards when conveying, non-return pad can be opened from centre position, and after conveying, non-return pad is closed automatically, prevents milk tank
Medium in 400 is flow backwards along conveyance conduit 300.
Further, the height of one end that the conveyance conduit 300 is connect with the conveyer 200 is more than the conveying
The height of one end that pipeline 300 is connect with the milk tank 400.
As shown in Fig. 2, conveyance conduit 300, by the way of being obliquely installed, the left end height of conveyance conduit 300 is more than conveying
The height of 300 right end of pipeline so that magnesia powder in conveyance conduit 300 can along conveyance conduit 300 left end gradually to
Right end conveys, and by the way of being obliquely installed, easily facilitates magnesia powder and conveys downwards.
Further, the conveyer 200 uses spiral conveyer.
Spiral conveyer is a kind of utilization motor drive spiral revolution, to elapse the magnesia powder in conveyer 200, to
Realize the purpose of conveying magnesia powder.
Spiral conveyer is horizontally disposed with, the outlet of the left end connection filler bin 100 of spiral conveyer makes filler bin 100
It after interior magnesia powder outflow, is pushed using spiral conveyer, there is simple in structure, cross-sectional area using spiral conveyer
Small, good airproof performance, it is easy to operate, be convenient for enclosed conveying the advantages that.
Fig. 3 is the structural schematic diagram for the third connection type that the utility model embodiment provides.
As shown in figure 3, it is further, filter 402 is connected in the discharge duct 401, the filter 402 is to institute
The gas in milk tank 400 after reaction is stated to be filtered.
In the outlet side of milk tank 400, i.e.,：Filter 402 is connected in discharge duct 401, filter 402 uses boiler
Smoke filter, the gas that milk tank 400 is discharged in smoke dust filter of boiler first carry out filtration treatment, avoid some smoke contaminations
Discharge duct 401, after so that clean gas is entered discharge duct 401, then discharge outward, air is made to effectively avoid
At pollution.
Further, fan 403 is connected in the discharge duct 401, the fan 403 is in the milk tank 400
Gas after reaction carries out acceleration discharge.
As shown in figure 3, being connected with fan 403 in the outlet side of milk tank 400, fan 403 is connected under filter 402
Portion position makes the gas in milk tank 400 after reaction be diluted first with fan 403, prevents the gas of overrich from entering exhaust
Pipeline 401.
After being diluted to gas using fan 403, gas flows to filter 402 and carried out under the driving of fan 403
Filter is handled, and is then just gradually conveyed outward along discharge duct 401.
Fig. 4 is the structural schematic diagram for the 4th kind of connection type that the utility model embodiment provides.
As shown in figure 4, further, the quantity of the conveyance conduit 300 be it is multiple, the outlet of the conveyer 200
Quantity is corresponding with the quantity of the conveyance conduit 300 multiple；
The entrance of each conveyance conduit 300 is connect with the outlet of the conveyer 200, the outlet of each conveyance conduit 300
It is connect with the milk tank 400.
When in filler bin 100 magnesia powder need comparison it is more, can be defeated when the volume of milk tank 400 is bigger
Multiple conveyance conduits 300 are set between material machine 200 and milk tank 400, using multiple conveyance conduits 300 simultaneously to conveyer 200
On magnesia powder conveyed.
It is used alternatively, only opening a conveyance conduit 300, the conduct of other conveyance conduits 300 is spare, when wherein one
When a conveyance conduit 300 blocks, other conveyance conduits 300 can be opened and continue to convey.
In Fig. 4, in one embodiment of the utility model, conveyance conduit 300 is set as two, two conveyance conduits
300 are arranged in parallel, and can only open one of conveyance conduit 300 as needed, are carried out to the magnesia powder on conveyer 200
Conveying；Two conveyance conduits 300 can also be opened simultaneously according to the needs used, at this moment, the oxidation that conveyer 200 conveys
The amount of magnesium powder is relatively more, disclosure satisfy that the use of milk tank 400.
Magnesia FGD tower pulping system provided by the utility model carries out heat to milk tank using steam-heated mode
When change, when need not convey magnesia into milk tank, closing control valve, avoid the hot water and steam in milk tank pass through it is defeated
It send pipeline to enter in conveyer, makes the inner wall humidity of conveyer, moist steam is prevented to be easy to send out with magnesia
Raw reaction；When needing to convey magnesia into milk tank, opening controlling valve door makes magnesia be directly transported along conveyance conduit
It is reacted in milk tank；When the conveying capacity abundance of magnesia, closing control valve effectively prevents the heat in milk tank
Water vapour enters in conveyance conduit, makes the reaction condition for not having magnesia and steam in conveyer, to be carried out to conveyer
Protection.The setting of the control valve of the utility model can effectively prevent the hot water and steam in milk tank from entering delivery pipe
In road, into conveyer, so that vapor is reacted the phenomenon that generating magnesium hydroxide crystallization with magnesia, extend the use of conveyer
Service life.
The utility model also provides a kind of combustion apparatus, the combustion apparatus installation magnesia FGD tower slurrying system
System.
Control valve is installed on the conveyance conduit of combustion apparatus, can effectively avoid hot water and steam in milk tank into
Enter conveyance conduit, and then enter conveyer, to be protected to the safe operation of whole equipment.
Finally it should be noted that：The above various embodiments is only to illustrate the technical solution of the utility model, rather than limits it
System；Although the utility model has been described in detail with reference to the foregoing embodiments, those skilled in the art should
Understand：It still can be with technical scheme described in the above embodiments is modified, either to which part or whole
Technical characteristic carries out equivalent replacement；And these modifications or replacements, this practicality that it does not separate the essence of the corresponding technical solution are new
The range of each embodiment technical solution of type.
Claims (10)
1. a kind of magnesia FGD tower pulping system, which is characterized in that including filler bin (100), conveyer (200), delivery pipe
Road (300) and milk tank (400)；
The outlet of the filler bin (100) is connect with the entrance of the conveyer (200), the outlet of the conveyer (200) with
The entrance of the conveyance conduit (300) connects, and the outlet of the conveyance conduit (300) is connect with the milk tank (400)；
Control valve (301) is connected on the conveyance conduit (300), the control valve (301) is to the conveyance conduit
(300) opening and closing is controlled；
The milk tank (400) is connected with discharge duct (401), and the discharge duct (401) is to anti-in the milk tank (400)
Gas after answering is discharged.
2. magnesia FGD tower pulping system according to claim 1, which is characterized in that the control valve (301) is
Manually-operated gate, the manually-operated gate are convenient for manually controlling the opening and closing of valve.
3. magnesia FGD tower pulping system according to claim 1, which is characterized in that the control valve (301) is
Electrically operated valve.
4. magnesia FGD tower pulping system according to claim 1, which is characterized in that in the conveyance conduit (300)
It is connected with check device (302), the check device (302) can prevent the magnesia in the conveyance conduit (300) gentle
Body is flow backwards.
5. magnesia FGD tower pulping system according to claim 1, which is characterized in that the conveyance conduit (300) with
The height of one end of conveyer (200) connection, is more than what the conveyance conduit (300) was connect with the milk tank (400)
The height of one end.
6. magnesia FGD tower pulping system according to claim 1, which is characterized in that the conveyer (200) uses
Spiral conveyer.
7. magnesia FGD tower pulping system according to claim 1, which is characterized in that in the discharge duct (401)
It is connected with filter (402), the filter (402) is filtered the gas after reaction in the milk tank (400).
8. magnesia FGD tower pulping system according to claim 1, which is characterized in that in the discharge duct (401)
It is connected with fan (403), the fan (403) carries out acceleration discharge to the gas after reaction in the milk tank (400).
9. magnesia FGD tower pulping system according to claim 1, which is characterized in that the conveyance conduit (300)
Quantity is multiple, and the quantity of the outlet of the conveyer (200) is corresponding more with the quantity of the conveyance conduit (300)
It is a；
The entrance of each conveyance conduit (300) is connect with the outlet of the conveyer (200), and each conveyance conduit (300) go out
Mouth is connect with the milk tank (400).
10. a kind of combustion apparatus, which is characterized in that combustion apparatus installation oxidation as claimed in any one of claims 1-9 wherein
Magnesium desulfurizing tower pulping system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820040526.6U CN208003727U (en) | 2018-01-10 | 2018-01-10 | Magnesia FGD tower pulping system and combustion apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820040526.6U CN208003727U (en) | 2018-01-10 | 2018-01-10 | Magnesia FGD tower pulping system and combustion apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208003727U true CN208003727U (en) | 2018-10-26 |
Family
ID=63882742
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820040526.6U Expired - Fee Related CN208003727U (en) | 2018-01-10 | 2018-01-10 | Magnesia FGD tower pulping system and combustion apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208003727U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114789915A (en) * | 2022-04-11 | 2022-07-26 | 福建省龙德新能源有限公司 | Continuous automatic production method of phosphorus pentafluoride |
-
2018
- 2018-01-10 CN CN201820040526.6U patent/CN208003727U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114789915A (en) * | 2022-04-11 | 2022-07-26 | 福建省龙德新能源有限公司 | Continuous automatic production method of phosphorus pentafluoride |
| CN114789915B (en) * | 2022-04-11 | 2023-10-24 | 福建省龙德新能源有限公司 | Continuous automatic production method of phosphorus pentafluoride |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| BR112020004963A2 (en) | system and method of desulphurization and dedusting gases from an oven | |
| CN106546124A (en) | A kind of anti-blocking apparatus for ash of circulated air and rotary regenerative air preheater | |
| CN212309123U (en) | Useless tail gas treatment ash backflow equipment that burns of danger | |
| CN208003727U (en) | Magnesia FGD tower pulping system and combustion apparatus | |
| CN105664704A (en) | Semidry flue gas desulfurization dust collector | |
| CN206203115U (en) | A kind of air-transport system | |
| CN204494473U (en) | The anti-blocking apparatus for ash of air pre-heater with rotary heating surface | |
| CN208560957U (en) | A kind of closed intelligent transportation system of weathering coal dust | |
| JPS6084131A (en) | Waste gas treating method and apparatus thereof | |
| CN219539931U (en) | A device for realizing dry desulfurization of flue gas by using metal filter bag to remove dust | |
| CN219043293U (en) | Wind-force compounding device | |
| CN202089599U (en) | Ash conveying system for economizer | |
| CN207778455U (en) | A kind of mechanism for preventing sour vapour burner from blocking | |
| CN216726595U (en) | Sodium bicarbonate desulfurizer preparation facilities | |
| CN205925420U (en) | Flue gas desulphurization device of thermal power plant | |
| CN203790824U (en) | High-efficiency boiler smoke desulphurization tower | |
| CN206927271U (en) | The Anti-blocking structure of Industrial Boiler electric precipitation pneumatic ash transmitting system | |
| CN207316955U (en) | A kind of desulfurization fume exhaust system | |
| CN209923376U (en) | Converter gas one-time dry dedusting coarse ash pneumatic conveying system | |
| CN106395173A (en) | Rotational-flow downward induction type material sending device | |
| CN209188471U (en) | A kind of out of stock integrated treatment unit of dust-removal and desulfurizing | |
| CN206215034U (en) | A kind of dry method desulfuration system | |
| CN219551223U (en) | Waste heat utilization system of smelting furnace | |
| CN218379381U (en) | Reaction device of heat medium furnace | |
| CN218421971U (en) | Kiln desulfurization system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20181026 Termination date: 20210110 |