CN107551781A - A kind of centrifugal flue gas secondary purification device - Google Patents
A kind of centrifugal flue gas secondary purification device Download PDFInfo
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- CN107551781A CN107551781A CN201710897515.XA CN201710897515A CN107551781A CN 107551781 A CN107551781 A CN 107551781A CN 201710897515 A CN201710897515 A CN 201710897515A CN 107551781 A CN107551781 A CN 107551781A
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- flue gas
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Abstract
The invention discloses a kind of centrifugal flue gas secondary purification device, including support, purification pot, buncher, transmission mechanism, rotating shaft, conical head, along the conical head, uniform diameter becomes the throwing disc that big quantity is no less than 2 successively from top to bottom, flow guiding head, feed tube, with aerofoil, nylon wire, upper spacer, intubation, collector box, net gas outlet pipe, lower clapboard, decoction is continuously passed through purification pot by feed tube, flow guiding head is by decoction uniform divided flows that feed tube inputs and accelerates to rush at conical head, buncher drives the conical head high-speed rotation being connected with rotating shaft by transmission mechanism, drive throwing disc that decoction is thrown away into atomization, flue gas passes through slowly to fall with aerofoil through flue gas fully to react with the decoction being atomized.The apparatus structure is simple, and the decoction of flue gas and atomization carries out primary first-order equation, then carries out secondary response with decoction, self-purging is carried out to flue gas, effectively improves gas cleaning efficiency and clean-up effect, simultaneously, it is atomization system without complicated compression system, reduces purification cost.
Description
Technical field
The present invention relates to a kind of mechanical device, more particularly to a kind of centrifugal flue gas secondary purification device.
Background technology
With industrial expansion and the improvement of people's living standards, the craving to the energy is also continuously increased, in coal-fired flue-gas
SO2 the main reason for having become atmosphere pollution, reduce SO2 pollutions turns into the task of top priority that current atmospheric environment is administered,
Many flue gas desulfurization technique extensive uses in the industry, wherein, Wet Flue Gas Desulfurization Technique with its technology maturation, technique it is simple and
It is widely used, the technical process of wet desulphurization is typically as follows：Neutralization reaction will be carried out with decoction after flue gas removing dust, reacted
Decoction is supplemented according to pH value in journey, until desulfurization is completed, the method that existing flue gas mixes with decoction there are two kinds, and one kind is directly will
Flue gas, which is passed through in the container for fill decoction, to be reacted, and another kind is flue gas to be passed through in container and simultaneously by medical liquid atomizing and cigarette
Gas hybrid reaction.
When flue gas is passed directly into decoction, flue gas habitat is difficult to have flue gas to be sufficiently mixed with solution, causes purification to be imitated
Fruit is poor, and medical liquid atomizing is mixed with flue gas, needs substantial amounts of atomizer and compression system, causes cleaning equipment cost high.
In view of disadvantages described above, is necessary to design a kind of centrifugal flue gas secondary purification device in fact.
The content of the invention
It is an object of the invention to provide a kind of centrifugal flue gas secondary purification device, the centrifugal flue gas secondary purification dress
Put and designed using double purification, self-purging is carried out to flue gas, effectively improves gas cleaning efficiency and clean-up effect.
In order to solve the above technical problems, the technical scheme is that：A kind of centrifugal flue gas secondary purification device, including
Support, purification pot, buncher, transmission mechanism, rotating shaft, conical head, along the conical head, uniform diameter becomes successively from top to bottom
Throwing disc of the big quantity no less than 2, flow guiding head, feed tube, go out with aerofoil, nylon wire, upper spacer, intubation, collector box, net gas
Pipe, lower clapboard, described purification pot are located at pedestal upper end, and described purification pot is connected with support screw thread, described buncher
Positioned at pedestal lower end, described buncher is connected with support screw thread, and described transmission mechanism is located at buncher upper end and position
In pedestal upper end, described transmission mechanism is connected with buncher key and is connected with holder pivots, and described rotating shaft is through purification
Tank and it is located at transmission mechanism upper end, described rotating shaft is rotatedly connected with purification pot and is connected with transmission mechanism key, described taper
Head is positioned at rotating shaft upper end and on the inside of purification pot, and described conical head is connected with shaft thread, and described throwing disc is located at taper
Head outside, described throwing disc are weldingly connected with conical head, and described flow guiding head is located at conical head upper end, described flow guiding head and cone
Forming head is weldingly connected, and described feed tube lower end is stretched into purification pot and on the outside of flow guiding head, described feed tube and purification
Tank screw thread is connected, and described is located at purification pot inner top side with aerofoil and is run through by flow guiding head, and described matches somebody with somebody aerofoil and purification pot
Screw thread is connected, and described nylon wire is positioned at aerofoil upper end is matched somebody with somebody, and described nylon wire is connected with aerofoil screw thread, described upper spacer
Run through positioned at conical head lower end and by rotating shaft, described upper spacer is connected with axis of rotation, and described intubation runs through upper spacer, institute
The intubation stated is connected with upper spacer close-fitting, and described collector box is located at upper spacer lower end, described collector box and upper spacer screw thread
It is connected, described net gas outlet pipe is located at collector box side and runs through purification pot, and described net gas outlet pipe is connected with collector box screw thread
And be connected with purification pot screw thread, described lower clapboard is located at purification pot inside lower end and run through by rotating shaft, described lower clapboard with
Purification pot screw thread is connected and is connected with rotating shaft gap.
Further improvement of the invention is as follows：
Further, described purification pot is additionally provided with flue gas inlet pipe, and described flue gas inlet pipe is located at purification pot upper end, described
Flue gas inlet pipe be connected with purification pot screw thread.
Further, described flow guiding head is additionally provided with ball head, and described ball head is located at flow guiding head upper end, described ball
Head is integrally connected with flow guiding head, and ball head is used for highly pressurised liquid uniform divided flows and accelerated so that highly pressurised liquid is through flow guiding head
Uniformly rapidly flow toward conical head.
Further, described collector box is additionally provided with air-vent, and described air-vent runs through collector box.
Further, described collector box is additionally provided with screen pack, and described screen pack is located on the inside of collector box, described mistake
Filter screen is connected with collector box screw thread.
Further, described lower clapboard is additionally provided with discharging tube, and described discharging tube is located at lower clapboard lower end and through net
Change tank, described discharging tube is connected with lower clapboard screw thread and is connected with purification pot screw thread.
Further, described lower clapboard is additionally provided with seal receptacle, and described seal receptacle is located at lower clapboard center and turned
Axle runs through, and described seal receptacle is connected with lower clapboard screw thread and is connected with rotating shaft gap, and seal receptacle is used for sealing pivot.
Compared with prior art, the centrifugal flue gas secondary purification device, during work, decoction is continuously passed through only by feed tube
Change tank, decoction uniform divided flows that feed tube input and acceleration are rushed at conical head by flow guiding head, and buncher passes through transmission mechanism band
The dynamic conical head high-speed rotation being connected with rotating shaft, so as to drive throwing disc that decoction is thrown away into atomization, flue gas enters net through flue gas inlet pipe
Change tank, then slowly whereabouts is fully reacted with the decoction being atomized through matching somebody with somebody aerofoil, the decoction of atomization is condensed into after drop through intubation outflow
And lower clapboard upper end is collected in, reacted flue gas enters secondary response again in decoction through intubation, so as to complete to purify, after purification
Gas is discharged after collector box is collected through net gas outlet pipe, and sewage is slowly discharged through dirty discharging tube.The apparatus structure is simple, flue gas with
The decoction of atomization carries out primary first-order equation, then carries out secondary response with decoction, so as to carry out self-purging to flue gas, effectively improves cigarette
Gas purification efficiency and clean-up effect, meanwhile, the compression system without complexity is atomization system, reduces purification cost.
Brief description of the drawings
Fig. 1 shows that front view Fig. 2 of the present invention shows collector box structural representation of the present invention
The purification pot 2 of support 1
The transmission mechanism 4 of buncher 3
The conical head 6 of rotating shaft 5
The flow guiding head 8 of throwing disc 7
Feed tube 9 matches somebody with somebody aerofoil 10
The upper spacer 12 of nylon wire 11
It is intubated 13 collector boxs 14
The net lower clapboard 16 of gas outlet pipe 15
The ball head 801 of flue gas inlet pipe 201
The screen pack 1402 of air-vent 1401
The seal receptacle 1602 of discharging tube 1601
Embodiment
As shown in Figure 1 and Figure 2, a kind of centrifugal flue gas secondary purification device, including support 1, purification pot 2, buncher 3,
Transmission mechanism 4, rotating shaft 5, conical head 6, along the conical head 6, uniform diameter becomes big quantity no less than 2 successively from top to bottom
Throwing disc 7, flow guiding head 8, feed tube 9, with aerofoil 10, nylon wire 11, upper spacer 12, intubation 13, collector box 14, net gas outlet pipe 15,
Lower clapboard 16, described purification pot 2 are located at the upper end of support 1, and described purification pot 2 is connected with the screw thread of support 1, described speed governing electricity
Machine 3 is located at the lower end of support 1, and described buncher 3 is connected with the screw thread of support 1, and described transmission mechanism 4 is located at buncher 3
Upper end and it is located at the upper end of support 1, described transmission mechanism 4 is connected with the key of buncher 3 and is rotatedly connected with support 1, described
Rotating shaft 5 is through purification pot 2 and be located at the upper end of transmission mechanism 4, described rotating shaft 5 and purification pot 2 be rotatedly connected and with transmission mechanism 4
Key is connected, and described conical head 6 is located at the upper end of rotating shaft 5 and positioned at the inner side of purification pot 2, described conical head 6 and the screw thread phase of rotating shaft 5
Even, described throwing disc 7 is located at the outside of conical head 6, and described throwing disc 7 is weldingly connected with conical head 6, and described flow guiding head 8 is located at
The upper end of conical head 6, described flow guiding head 8 are weldingly connected with conical head 6, and the described lower end of feed tube 9 is stretched into purification pot 2 and position
In the outside of flow guiding head 8, described feed tube 9 is connected with the screw thread of purification pot 2, and described is located on the inner side of purification pot 2 with aerofoil 10
Hold and run through by flow guiding head 8, described is connected with aerofoil 10 with the screw thread of purification pot 2, and described nylon wire 11 is located at and matches somebody with somebody aerofoil 10
Upper end, described nylon wire 11 are connected with the screw thread of aerofoil 10, and described upper spacer 12 is located at the lower end of conical head 6 and by rotating shaft 5
Run through, described upper spacer 12 is rotatedly connected with rotating shaft 5, and described intubation 13 runs through upper spacer 12, described intubation 13 with it is upper
The close-fitting of dividing plate 12 is connected, and described collector box 14 is located at the lower end of upper spacer 12, described collector box 14 and the screw thread phase of upper spacer 12
Even, described net gas outlet pipe 15 is located at the side of collector box 14 and runs through purification pot 2, described net gas outlet pipe 15 and the spiral shell of collector box 14
Line is connected and is connected with the screw thread of purification pot 2, and described lower clapboard 16 is located at the inside lower end of purification pot 2 and run through by rotating shaft 5, described
Lower clapboard 16 be connected with the screw thread of purification pot 2 and be connected with the gap of rotating shaft 5, described purification pot 2 is additionally provided with flue gas inlet pipe 201,
Described flue gas inlet pipe 201 is located at the upper end of purification pot 2, and described flue gas inlet pipe 201 is connected with the screw thread of purification pot 2, and described leads
Stream first 8 is additionally provided with ball head 801, and described ball head 801 is located at the upper end of flow guiding head 8, described ball head 801 and flow guiding head 8
One is connected, and ball head 801 is used for highly pressurised liquid uniform divided flows and accelerated so that highly pressurised liquid is uniformly quick through flow guiding head 8
Conical head 6 is flowed to, described collector box 14 is additionally provided with air-vent 1401, and described air-vent 1401 runs through collector box 14, described
Collector box 14 be additionally provided with screen pack 1402, described screen pack 1402 is located at the inner side of collector box 14, described screen pack 1402
It is connected with the screw thread of collector box 14, described lower clapboard 16 is additionally provided with discharging tube 1601, and described discharging tube 1601 is located at lower clapboard
16 lower ends and run through purification pot 2, described discharging tube 1601 is connected with the screw thread of lower clapboard 16 and is connected with the screw thread of purification pot 2, institute
The lower clapboard 6 stated is additionally provided with seal receptacle 1602, and described seal receptacle 1602 is located at the center of lower clapboard 16 and run through by rotating shaft 5,
Described seal receptacle 1602 is connected with the screw thread of lower clapboard 16 and is connected with the gap of rotating shaft 5, and seal receptacle 1602 is used for sealing pivot 5,
The centrifugal flue gas secondary purification device, during work, decoction is continuously passed through purification pot 3 by feed tube 9, and flow guiding head 8 is by feed tube 9
The decoction uniform divided flows of input simultaneously accelerate to rush at conical head 6, and buncher 2 drives the cone being connected with rotating shaft 5 by transmission mechanism 4
The high-speed rotation of forming head 6, so as to drive throwing disc 7 that decoction is thrown away into atomization, flue gas enters purification pot 3 through flue gas inlet pipe 205, then through matching somebody with somebody
Aerofoil 10 slowly falls fully to react with the decoction being atomized, and the decoction of atomization, which is condensed into after drop, to flow out and collect in through intubation 13
The upper end of lower clapboard 16, reacted flue gas is through being intubated in 13 entrance decoctions secondary response again, so as to complete to purify, purified gas
Discharged after the collection of collector box 14 through net gas outlet pipe 15, sewage is slowly discharged through dirty discharging tube 1601.The apparatus structure is simple, cigarette
Gas and the decoction of atomization carry out primary first-order equation, then carry out secondary response with decoction, so as to carry out self-purging to flue gas, effectively carry
High gas cleaning efficiency and clean-up effect, meanwhile, the compression system without complexity is atomization system, reduces purification cost.
The present invention is not limited to above-mentioned specific embodiment, one of ordinary skill in the art from above-mentioned design,
Without performing creative labour, a variety of conversion made, it is within the scope of the present invention.
Claims (7)
- A kind of 1. centrifugal flue gas secondary purification device, it is characterised in that including support, purification pot, buncher, transmission mechanism, Rotating shaft, conical head, along the conical head, uniform diameter becomes throwing disc of the big quantity no less than 2, flow guiding head, entered successively from top to bottom Liquid pipe, it is located on support with aerofoil, nylon wire, upper spacer, intubation, collector box, net gas outlet pipe, lower clapboard, described purification pot End, described purification pot are connected with support screw thread, and described buncher is located at pedestal lower end, described buncher and support Screw thread is connected, and described transmission mechanism is located at buncher upper end and is located at pedestal upper end, described transmission mechanism and speed governing electricity Switch is connected and is connected with holder pivots, and described rotating shaft is through purification pot and be located at transmission mechanism upper end, described rotating shaft and Purification pot is rotatedly connected and is connected with transmission mechanism key, and described conical head is located at rotating shaft upper end and on the inside of purification pot, institute The conical head stated is connected with shaft thread, and described throwing disc is located on the outside of conical head, and described throwing disc is weldingly connected with conical head, Described flow guiding head is located at conical head upper end, and described flow guiding head is weldingly connected with conical head, and described feed tube lower end is stretched into In purification pot and on the outside of flow guiding head, described feed tube is connected with purification pot screw thread, and described is located at purification pot with aerofoil Inner top side and run through by flow guiding head, described is connected with aerofoil with purification pot screw thread, and described nylon wire is located at on aerofoil End, described nylon wire are connected with aerofoil screw thread, and described upper spacer is located at conical head lower end and run through by rotating shaft, described Upper spacer is connected with axis of rotation, and described intubation runs through upper spacer, and described intubation is connected with upper spacer close-fitting, described collection Gas box is located at upper spacer lower end, and described collector box is connected with upper spacer screw thread, and described net gas outlet pipe is located at collector box side And running through purification pot, described net gas outlet pipe is connected with collector box screw thread and is connected with purification pot screw thread, described lower clapboard position Run through in purification pot inside lower end and by rotating shaft, described lower clapboard is connected with purification pot screw thread and is connected with rotating shaft gap.
- 2. centrifugal flue gas secondary purification device as claimed in claim 1, it is characterised in that described purification pot is additionally provided with cigarette Gas inlet pipe, described flue gas inlet pipe are located at purification pot upper end, and described flue gas inlet pipe is connected with purification pot screw thread.
- 3. centrifugal flue gas secondary purification device as claimed in claim 1, it is characterised in that described flow guiding head is additionally provided with ball Head, described ball head are located at flow guiding head upper end, and described ball head is integrally connected with flow guiding head.
- 4. centrifugal flue gas secondary purification device as claimed in claim 1, it is characterised in that described collector box is additionally provided with Stomata, described air-vent run through collector box.
- 5. centrifugal flue gas secondary purification device as claimed in claim 1, it is characterised in that described collector box was additionally provided with Filter screen, described screen pack are located on the inside of collector box, and described screen pack is connected with collector box screw thread.
- 6. centrifugal flue gas secondary purification device as claimed in claim 1, it is characterised in that described lower clapboard is additionally provided with row Liquid pipe, described discharging tube are located at lower clapboard lower end and run through purification pot, described discharging tube be connected with lower clapboard screw thread and with Purification pot screw thread is connected.
- 7. centrifugal flue gas secondary purification device as claimed in claim 1, it is characterised in that described lower clapboard is additionally provided with close Seal seat, described seal receptacle is located at lower clapboard center and run through by rotating shaft, described seal receptacle be connected with lower clapboard screw thread and It is connected with rotating shaft gap.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710897515.XA CN107551781B (en) | 2017-09-28 | 2017-09-28 | Centrifugal type secondary flue gas purifying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710897515.XA CN107551781B (en) | 2017-09-28 | 2017-09-28 | Centrifugal type secondary flue gas purifying device |
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| Publication Number | Publication Date |
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| CN107551781A true CN107551781A (en) | 2018-01-09 |
| CN107551781B CN107551781B (en) | 2023-09-22 |
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| CN201710897515.XA Active CN107551781B (en) | 2017-09-28 | 2017-09-28 | Centrifugal type secondary flue gas purifying device |
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| DE102010009347A1 (en) * | 2010-02-25 | 2011-08-25 | Bastian, Helmut, 94447 | Device for washing flue gas e.g. sulfur di-oxide, from incinerator for incineration of timber for reducing pollutant emissions in exhaust gas stream in industry, has turbulence plates provided for turbulence of wash water and flue gas |
| CN102872694A (en) * | 2012-08-03 | 2013-01-16 | 常州大学 | Device for purifying gas through liquid phase mediums |
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| CN105709580A (en) * | 2016-04-13 | 2016-06-29 | 中冶焦耐工程技术有限公司 | Smoke distributor for rotary atomizing desulfurization and smoke distribution method |
| KR101761093B1 (en) * | 2016-09-09 | 2017-08-04 | 주식회사 지엔비 | Fume purification |
| CN107051161A (en) * | 2017-05-11 | 2017-08-18 | 金柯楠 | A kind of environmentally friendly flue gas spray dries desulfurizer |
| CN207371326U (en) * | 2017-09-28 | 2018-05-18 | 苏州百硕自动化环保设备有限公司 | A kind of centrifugal flue gas secondary purification device |
-
2017
- 2017-09-28 CN CN201710897515.XA patent/CN107551781B/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102010009347A1 (en) * | 2010-02-25 | 2011-08-25 | Bastian, Helmut, 94447 | Device for washing flue gas e.g. sulfur di-oxide, from incinerator for incineration of timber for reducing pollutant emissions in exhaust gas stream in industry, has turbulence plates provided for turbulence of wash water and flue gas |
| CN102872694A (en) * | 2012-08-03 | 2013-01-16 | 常州大学 | Device for purifying gas through liquid phase mediums |
| CN105413441A (en) * | 2015-12-09 | 2016-03-23 | 安徽中泰创展环境科技有限公司 | Flue gas treatment spraying tower |
| CN105709580A (en) * | 2016-04-13 | 2016-06-29 | 中冶焦耐工程技术有限公司 | Smoke distributor for rotary atomizing desulfurization and smoke distribution method |
| KR101761093B1 (en) * | 2016-09-09 | 2017-08-04 | 주식회사 지엔비 | Fume purification |
| CN107051161A (en) * | 2017-05-11 | 2017-08-18 | 金柯楠 | A kind of environmentally friendly flue gas spray dries desulfurizer |
| CN207371326U (en) * | 2017-09-28 | 2018-05-18 | 苏州百硕自动化环保设备有限公司 | A kind of centrifugal flue gas secondary purification device |
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| CN107551781B (en) | 2023-09-22 |
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