CN207786322U - A kind of novel Flue Gas Desulfurization with Pyrolusite Pulp apparatus and system - Google Patents
A kind of novel Flue Gas Desulfurization with Pyrolusite Pulp apparatus and system Download PDFInfo
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- CN207786322U CN207786322U CN201721773018.0U CN201721773018U CN207786322U CN 207786322 U CN207786322 U CN 207786322U CN 201721773018 U CN201721773018 U CN 201721773018U CN 207786322 U CN207786322 U CN 207786322U
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Abstract
The utility model provides a kind of novel Flue Gas Desulfurization with Pyrolusite Pulp apparatus and system, is related to manganese ore technical field.Novel Flue Gas Desulfurization with Pyrolusite Pulp device includes：Device body, multiple packing sections, spray equipment and control device.Device body has the first opening and the second opening；Multiple packing sections are arranged along the length direction interval of device body, and packing section is used to hold the required filler of flue gas desulfurization operation, and from first opening to the second opening direction, the packing density of packing section is gradually reduced；Spray equipment includes the multiple spray pipings for being provided with the transport pipeline of spray pump and being connect with transport pipeline, and multiple spray pipings are correspondingly arranged in the top of multiple packing sections, for providing absorbing liquid for packing section；Control device is electrically connected with spray pump, and control device is configured as the absorbing liquid of the pumping predetermined amount in preset time.This device can effectively improve desulfuration efficiency, protect Health Status For Workers Exposed, ensure Environmental security.
Description
Technical field
The utility model is related to manganese ore technical field, in particular to a kind of novel Flue Gas Desulfurization with Pyrolusite Pulp device and
System.
Background technology
The SO in China at present2Discharge capacity has occupied the first in the world, and China has become the 3rd big Acid Rain Zone of the world, every year
Because acid rain loss is exceeded 100 billion, and the SO in sintering flue gas2It is to cause one of main source of acid rain.It is still both at home and abroad at present
Based on wet process of FGD, wet method accounts for about 85% and (accounts for 98% by major country such as Japan, wet method of Wet Flue Gas Desulfurization Technique；It is beautiful
State accounts for 92%；Germany accounts for 90%.), generally using limestone-gypsum method and sodium alkali etc., but the investment and fortune of this method
Costly, the easy fouling and clogging of system of row, and desulfuration byproduct price is low, waste residue application value is little, easily causes secondary pollution, warp
Ji benefit unobvious.As various countries are more stringent to environmental requirement, and the development and research of science and technology are continuous deeply,
The wet method of parts of traditional is gradually substituted by novel wet method, semidry method and dry desulfurizing process.
But the phenomenon that still have many desulfuration efficiencies poor for current desulfurization technology, and discharge does not reach index, these phenomenons
Enrichment drastically influence the environment of surrounding, or even hinder the progress and development of entire industry.
Utility model content
The purpose of this utility model is to provide a kind of novel Flue Gas Desulfurization with Pyrolusite Pulp devices, can effectively improve desulfurization effect
Rate protects operating personnel's health, while ensureing environmental sanitary safety.
The another object of the utility model is to provide a kind of novel Flue Gas Desulfurization with Pyrolusite Pulp system, this system can be effective
Ground improves desulfuration efficiency, protects operating personnel's health, while ensureing environmental sanitary safety.
The utility model is realized in this way：
A kind of novel Flue Gas Desulfurization with Pyrolusite Pulp device, including：
Device body, device body has the first opening and the second opening, and the first opening is gas inlet, and second opens
Mouth is exhanst gas outlet；
Multiple packing sections, multiple packing sections are arranged along the length direction interval of device body, and packing section is for holding cigarette
The required filler of desulfurization operation, and from first opening to the second opening direction, the packing density of packing section is gradually reduced；
Spray equipment, spray equipment include the multiple sprays for being provided with the transport pipeline of spray pump and being connect with transport pipeline
Shower pipe road, multiple spray pipings are correspondingly arranged in the top of multiple packing sections, for providing absorbing liquid for packing section；
Control device, control device are electrically connected with spray pump, and to be configured as the pumping in preset time pre- for control device
If the absorbing liquid of amount.
Further, in the preferred embodiment of the utility model, each packing section is arc-shaped, and the arc bottom of packing section
It is arranged towards the first opening.
Further, in the preferred embodiment of the utility model, packing section include set gradually from bottom to up it is porous
Support plate, packing layer, water accepting layer and permeable formation, and the thickness proportion of porous support plate, water accepting layer and permeable formation is 1:4~
5:1:2。
Further, in the preferred embodiment of the utility model, packing section further includes porous pressing plate, porous pressing plate setting
In the top of permeable formation.
Further, in the preferred embodiment of the utility model, spray piping, which has, to be stretched into above multiple packing sections
Drain side, drain side is arc-shaped, and arc bottom is open towards second, and the radian of drain side is identical as the radian of packing section.
Further, in the preferred embodiment of the utility model, there is spray piping the first linkage section to be connect with second
Section, the first linkage section is connected to transport pipeline, and is fixed on device body, and the second linkage section is welded in the first linkage section.
Further, in the preferred embodiment of the utility model, the first linkage section is set to multiple nozzles.
Further, in the preferred embodiment of the utility model, nozzle is gimbaled nozzle, and gimbaled nozzle is filled with control
Electrical connection is set, control device is configured as in preset time, and control gimbaled nozzle is centered on the axis direction of device body
Line rotates.
Further, in the preferred embodiment of the utility model, control device is programmable logic controller (PLC), microcontroller
And any one of computer.
A kind of novel Flue Gas Desulfurization with Pyrolusite Pulp system, including multiple above-mentioned novel Flue Gas Desulfurization with Pyrolusite Pulp systems.
The advantageous effect of said program：
The utility model provides a kind of novel Flue Gas Desulfurization with Pyrolusite Pulp apparatus and system.The novel pyrolusite flue gas provided
Desulfurizer includes device body, multiple packing sections, spray equipment and control system.Device body be each component installation with
Operation provides enough guarantees.Multiple packing sections are set gradually so that the process of multiple desulfurization is undergone in flue gas desulfurization, to make
It obtains desulfuration efficiency to be effectively improved, and then can ensure the quality of desulfurization.Spray equipment can be more than with assist absorption two
Sulfur oxide, and the absorbing liquid that sprays out of spray equipment can be attached to above the filler of packing section increases filler and sulfur dioxide
Active area further ensures desulfuration efficiency.Also, control system is electrically connected with the spray pump of spray equipment, can be used for
The amount of the absorbing liquid of the spray of the spray equipment in certain time is controlled, and then cost-effective, avoids waste.
Description of the drawings
It, below will be to required use in embodiment in order to illustrate more clearly of the technical solution of the utility model embodiment
Attached drawing be briefly described, it should be understood that the following drawings illustrates only some embodiments of the utility model, therefore should not be by
Regard the restriction to range as, for those of ordinary skill in the art, without creative efforts, may be used also
To obtain other relevant attached drawings according to these attached drawings.
Fig. 1 is the structural schematic diagram for the first Novel flue gas desulfurizer that the embodiments of the present invention provide；
Fig. 2 is the structural schematic diagram for second of Novel flue gas desulfurizer that the embodiments of the present invention provide.
Icon：The novel Flue Gas Desulfurization with Pyrolusite Pulp devices of 100-；101- device bodies；103- first is open；105- second is opened
Mouthful；107- packing sections；109- spray equipments；111- transport pipelines；113- spray pumps；115- spray pipings；117- open supports
Plate；119- packing layers；121- water accepting layers；123- permeable formations；The porous pressing plates of 125-；The drain sides 127-；The first linkage sections of 129-；
The second linkage sections of 131-；133- nozzles；135- collecting tanks.
Specific implementation mode
It is new below in conjunction with this practicality to keep the purpose, technical scheme and advantage of the utility model embodiment clearer
Attached drawing in type embodiment, the technical scheme in the utility model embodiment is clearly and completely described, it is clear that is retouched
The embodiment stated is the utility model a part of the embodiment, instead of all the embodiments.Usually here described in attached drawing and
The component of the utility model embodiment shown can be arranged and be designed with a variety of different configurations.Therefore, below to attached
The detailed description of the embodiments of the present invention provided in figure is not intended to limit claimed the scope of the utility model,
But it is merely representative of the selected embodiment of the utility model.Based on the embodiments of the present invention, ordinary skill people
The every other embodiment that member is obtained without creative efforts belongs to the model of the utility model protection
It encloses.
It should be noted that：Similar label and letter indicate similar terms in following attached drawing, therefore, once a certain Xiang Yi
It is defined, then it further need not be defined and explained in subsequent attached drawing in a attached drawing.
In the description of the utility model embodiment, it should be noted that term "center", "upper", "lower", " left side ",
The orientation or positional relationship of the instructions such as " right side ", "vertical", "horizontal", "inner", "outside" is orientation based on ... shown in the drawings or position
Relationship or the utility model product using when the orientation or positional relationship usually put, be merely for convenience of describing this reality
With novel and simplified description, does not indicate or imply the indicated device or element must have a particular orientation, with specific
Azimuth configuration and operation, therefore should not be understood as limiting the present invention.In addition, term " first ", " second ", " third "
It is described etc. being only used for distinguishing, is not understood to indicate or imply relative importance.
In the description of the utility model embodiment, it is also necessary to which explanation is unless specifically defined or limited otherwise, art
Language " setting ", " installation ", " connected ", " connection " shall be understood in a broad sense, and can also be detachable for example, it may be being fixedly connected
Connection, or be integrally connected；It can be mechanical connection, can also be electrical connection；It can be directly connected, centre can also be passed through
Medium is indirectly connected, and can be the connection inside two elements.It for the ordinary skill in the art, can specific feelings
Condition understands the concrete meaning of above-mentioned term in the present invention.
In the present invention unless specifically defined or limited otherwise, fisrt feature is on or below second feature
It may include that the first and second features are in direct contact, can also not be to be in direct contact but pass through it including the first and second features
Between other characterisation contact.Moreover, fisrt feature is on second feature, top and above include fisrt feature the
Right over two features and oblique upper, or be merely representative of fisrt feature level height and be higher than second feature.Fisrt feature is in the second spy
Under sign, lower section and fisrt feature included below are immediately below second feature and obliquely downward, or are merely representative of fisrt feature level
Height is less than second feature.
Fig. 1 is the structural schematic diagram of the first novel Flue Gas Desulfurization with Pyrolusite Pulp device 100 provided in this embodiment.Refering to figure
1, in the present embodiment, novel Flue Gas Desulfurization with Pyrolusite Pulp device 100 includes：Device body 101, multiple packing sections 107, spray dress
Set 109 and control system.Device body 101 provides enough guarantees for the installation of each component with operation.Multiple packing sections
107 set gradually so that the process of multiple desulfurization is undergone in flue gas desulfurization, so that desulfuration efficiency is effectively improved, in turn
It can ensure the quality of desulfurization.The sulfur dioxide that spray equipment 109 can be more than with assist absorption, and spray equipment 109 sprays out
Absorbing liquid can be attached to above the filler of packing section 107, increase the active area of filler and sulfur dioxide, further ensure
Desulfuration efficiency.Also, control system is electrically connected with the spray pump 113 of spray equipment 109, can be used for controlling in certain time
The amount of the absorbing liquid of the spray of spray equipment 109, so it is cost-effective, avoid waste.
Referring to Fig. 1, device body 101 has the first opening 103 and the second opening 105, and the first opening 103
For gas inlet, the second opening 105 is exhanst gas outlet.First opening 103 is both provided with the second opening 105 for optionally opening
The valve closed.Also, the first opening 103 is located at the side-lower of device body 101, and the second opening 105 is located at device body 101
Above side.Flue gas is passed through from the lower section of device body 101, by natural buoyancy up migration to come into full contact with to fill with filler
Divide desulfurization.Device body 101 provides enough guarantees for the installation of each component with operation.Certainly, in the reality of the utility model
It applies in example, device body 101 further includes some installing components, such as screw, bolt etc., simultaneously due to the embodiments of the present invention
It does not make improvements, therefore this embodiment is not repeated.
In the present embodiment, multiple packing sections 107 are arranged along the length direction interval of device body 101, and packing section 107
Required filler for holding flue gas desulfurization operation, and from 103 to the second 105 directions of opening of the first opening, packing section 107
Packing density is gradually reduced.Since flue gas is passed through from the lower section of device body 101, overflowed from the top of device body 101, because
This during flue gas migration from the bottom up, closer to second opening 105 positions sulfur dioxide in flue gas concentration be by
It gradually reduces, therefore in order to save desulphurization cost, the density of the filler of packing section 107 can be gradually reduced.It designs in this way, also
It is more smooth can so that the flue gas after desulfurization overflows, avoids causing to block.
Specifically, each packing section 107 is arc-shaped, and the arc bottom of packing section 107 is arranged towards the first opening 103.By
It can be acted on due to ambient air toward middle part migration in the flue gas being passed through, the packing section 107 of arc setting can pass through its arc
The shape of shape effectively disperses flue gas so that flue gas and the filler of packing section 107 come into full contact with, to improve desulfuration efficiency.
Wherein, packing section 107 includes porous support plate 117, packing layer 119, the water accepting layer 121 set gradually from bottom to up
And permeable formation 123, and the thickness proportion of porous support plate 117, water accepting layer 121 and permeable formation 123 is 1:4~5:1:2.It is more
The setting of hole support plate 117 can facilitate filler to hold, and packing layer 119 is for stacking filler, by the branch of porous support plate 117
Support, flue gas can penetrate porous support plate 117 and the filler of packing layer 119 comes into full contact with.Water accepting layer 121 can adequately absorb
The absorbing liquid that spray equipment 109 sprays out, and then ensure the abundance of filler surface liquid, then improve desulfuration efficiency.Infiltration
Layer 123 can facilitate interpenetrating for flue gas and absorbing liquid, increase contact area, improve desulfuration efficiency.
It should be noted that in the other embodiment of the utility model, porous support plate 117, packing layer 119, water suction
The thickness of layer 121 and permeable formation 123 can also be selected according to demand, can when sulfur dioxide in flue gas content is higher
With the laying depth of the filler appropriate for increasing packing layer 119.It is opposite, it, can be with when sulfur dioxide in flue gas concentration is relatively low
Correspondingly reduce the thickness of filler in packing layer 119.Filler can be adequately utilized by the adjusting of thickness, avoids wasting, into
And it is cost-effective, it increases economic efficiency.
Fig. 2 is second provided in this embodiment novel Flue Gas Desulfurization with Pyrolusite Pulp device 100.Referring to Fig.2, as preferred
Scheme, packing section 107 further include porous pressing plate 125, and porous pressing plate 125 is set to the top of permeable formation 123.Porous pressing plate 125
Setting can be taken out of by flue gas to avoid filler, saved filler cost.
In the present embodiment, it please refers to Fig.1 and Fig. 2, spray equipment 109 includes the transport pipeline for being provided with spray pump 113
111 and multiple spray pipings 115 for being connect with transport pipeline 111, multiple spray pipings 115 be correspondingly arranged in multiple packing sections
107 top, for providing absorbing liquid for packing section 107.At the same time it can also which collecting tank is arranged in the lower section of device body 101
135, collecting tank 135 can collect the absorbing liquid after spray to wait for secondary use.
Specifically, it is in arc that spray piping 115, which has the drain side 127 for stretching into 107 top of multiple packing sections, drain side 127,
Shape, arc bottom is towards the second opening 105, and the radian of drain side 127 is identical as the radian of packing section 107.Setting can make in this way
The absorbing liquid that must be sprayed out is fully sprayed and packing section 107, and improves the granularity of spray so that the absorbing liquid sprayed out is mutually touched
Atomization is hit, and then improves the contact area between absorbing liquid and flue gas, to improve desulfuration efficiency.
Wherein, spray piping 115 has the first linkage section 129 and the second linkage section 131, the first linkage section 129 and transport
Pipeline 111 is connected to, and is fixed on device body 101, and the second linkage section 131 is welded in the first linkage section 129.Welding can improve
Bonding strength avoids being broken.
As a preferred option, the first linkage section 129 is set to multiple nozzles 133.In the present embodiment, nozzle 133
Quantity is 10, and in the other embodiment of the utility model, the quantity of nozzle 133 can also be according to the ruler of device body 101
Very little to be adjusted, the utility model does not limit.
It is further preferred that nozzle 133 is gimbaled nozzle 133, and gimbaled nozzle 133 is electrically connected with control device, control
Device is configured as in preset time, and control gimbaled nozzle 133 line centered on the axis direction of device body 101 rotates.
Using for gimbaled nozzle 133 makes absorbing liquid in each direction be evenly distributed, and then ensures desulfurization effect.
In the present embodiment, control device is programmable logic controller (PLC) (PLC), microcontroller or computer.It is programmable to patrol
Volume controller is used for its internally stored program using a kind of programmable memory, execute logical operation, sequential control, timing,
The user oriented instruction such as counting and arithmetical operation, and pass through number or analog pattern input/various types of machineries of output control
Or production process.Certainly, in the other embodiment of the utility model, the type of control device can be selected according to demand
It selects, the utility model does not limit.
The present embodiment additionally provides a kind of novel Flue Gas Desulfurization with Pyrolusite Pulp system (not shown), this novel pyrolusite flue gas is de-
Sulphur system includes multiple above-mentioned novel Flue Gas Desulfurization with Pyrolusite Pulp devices 100.Multiple novel Flue Gas Desulfurization with Pyrolusite Pulp devices 100 are simultaneously
Connection uses, and can improve operating efficiency, reduces the activity duration, increases economic efficiency.
The novel Flue Gas Desulfurization with Pyrolusite Pulp device 100 and novel Flue Gas Desulfurization with Pyrolusite Pulp that the embodiments of the present invention provide
The working principle and beneficial effect of system is：
The novel Flue Gas Desulfurization with Pyrolusite Pulp device 100 provided includes device body 101, multiple packing sections 107, spray equipment
109 and control system.Device body 101 provides enough guarantees for the installation of each component with operation.Flue gas is from device sheet
First opening 103 of body 101 enters, and passes through multiple packing sections 107 successively, and multiple packing sections 107 are set gradually so that flue gas is de-
Sulphur undergoes the process of multiple desulfurization, so that desulfuration efficiency is effectively improved, and then can ensure the quality of desulfurization.Spray
The sulfur dioxide that shower device 109 can be more than with assist absorption, and the absorbing liquid that spray equipment 109 sprays out can be attached to packing section
Above 107 filler, increases the active area of filler and sulfur dioxide, further ensure desulfuration efficiency.Also, control system
It is electrically connected with the spray pump 113 of spray equipment 109, can be used for controlling the suction of the spray of the spray equipment 109 in certain time
The amount of liquid is received, and then cost-effective, avoids waste.
The above descriptions are merely preferred embodiments of the present invention, is not intended to limit the utility model, for this
For the technical staff in field, various modifications and changes may be made to the present invention.It is all in the spirit and principles of the utility model
Within, any modification, equivalent replacement, improvement and so on should be included within the scope of protection of this utility model.
Claims (10)
1. a kind of novel Flue Gas Desulfurization with Pyrolusite Pulp device, which is characterized in that including：
Device body, described device ontology has the first opening and the second opening, and first opening is gas inlet, institute
It is exhanst gas outlet to state the second opening；
Multiple packing sections, multiple packing sections are arranged along the length direction interval of described device ontology, and the packing section is used
In the required filler for holding flue gas desulfurization operation, and from first opening to second opening direction, the packing section
Packing density be gradually reduced；
Spray equipment, the spray equipment include being provided with the transport pipeline of spray pump and being connect with the transport pipeline more
A spray piping, multiple spray pipings are correspondingly arranged in the top of multiple packing sections, for being carried for the packing section
For absorbing liquid；
Control device, the control device are electrically connected with the spray pump, and the control device is configured as in preset time
The absorbing liquid of interior pumping predetermined amount.
2. novel Flue Gas Desulfurization with Pyrolusite Pulp device according to claim 1, which is characterized in that each the packing section is in
Arc, and the arc bottom of the packing section is arranged towards first opening.
3. novel Flue Gas Desulfurization with Pyrolusite Pulp device according to claim 2, which is characterized in that the packing section includes under
The supreme porous support plate set gradually, packing layer, water accepting layer and permeable formation, and the porous support plate, the water accepting layer
And the thickness proportion of the permeable formation is 1:4~5:1:2.
4. novel Flue Gas Desulfurization with Pyrolusite Pulp device according to claim 3, which is characterized in that the packing section further includes more
Hole pressing plate, the porous pressing plate are set to the top of the permeable formation.
5. novel Flue Gas Desulfurization with Pyrolusite Pulp device according to claim 2, which is characterized in that the spray piping, which has, to be stretched
Enter the drain side above multiple packing sections, the drain side is arc-shaped, and the arc bottom is open towards described second, and described
The radian of drain side is identical as the radian of the packing section.
6. novel Flue Gas Desulfurization with Pyrolusite Pulp device according to claim 1, which is characterized in that the spray piping has the
One linkage section and the second linkage section, first linkage section is connected to the transport pipeline, and is fixed on described device ontology, institute
It states the second linkage section and is welded in first linkage section.
7. novel Flue Gas Desulfurization with Pyrolusite Pulp device according to claim 6, which is characterized in that the first linkage section setting
In multiple nozzles.
8. novel Flue Gas Desulfurization with Pyrolusite Pulp device according to claim 7, which is characterized in that the nozzle is universal spray
Head, and the gimbaled nozzle is electrically connected with the control device, the control device is configured as in preset time, controls institute
Gimbaled nozzle line centered on the axis direction of described device ontology is stated to rotate.
9. novel Flue Gas Desulfurization with Pyrolusite Pulp device according to any one of claim 1 to 8, which is characterized in that the control
Device processed is any one of programmable logic controller (PLC), microcontroller and computer.
10. a kind of novel Flue Gas Desulfurization with Pyrolusite Pulp system, which is characterized in that described in any one of multiple claims 1 to 9
Novel Flue Gas Desulfurization with Pyrolusite Pulp system.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721773018.0U CN207786322U (en) | 2017-12-18 | 2017-12-18 | A kind of novel Flue Gas Desulfurization with Pyrolusite Pulp apparatus and system |
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| CN201721773018.0U CN207786322U (en) | 2017-12-18 | 2017-12-18 | A kind of novel Flue Gas Desulfurization with Pyrolusite Pulp apparatus and system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109621645A (en) * | 2019-01-29 | 2019-04-16 | 宁波航天吉麦克环保科技有限公司 | A kind of organic pollutant equipment for treating industrial waste gas |
-
2017
- 2017-12-18 CN CN201721773018.0U patent/CN207786322U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109621645A (en) * | 2019-01-29 | 2019-04-16 | 宁波航天吉麦克环保科技有限公司 | A kind of organic pollutant equipment for treating industrial waste gas |
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