A kind of centrifugal smoke eliminator
Technical field
The present invention relates to a kind of mechanical device, more particularly to a kind of centrifugal smoke eliminator.
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.
Flue gas is often passed through in container and will be passed through container after medical liquid atomizing simultaneously by existing smoke eliminator so that mist
Flue gas and decoction hybrid reaction after change, it is well mixed to ensure, generally require to set multiple atomizers and be equipped with compression train
System, cause cleaning equipment cost of manufacture and maintenance cost high.In view of disadvantages described above, it is necessary to design a kind of centrifugal flue gas in fact net
Makeup is put.
The content of the invention
The technical problems to be solved by the invention are:A kind of centrifugal smoke eliminator is provided, come the use solved
Atomizer carries out being atomized the problem of cost is high.
In order to solve the above technical problems, the technical scheme is that:A kind of centrifugal smoke eliminator, including branch
Frame, purification pot, buncher, transmission mechanism, rotating shaft, conical head, along the conical head, uniform diameter becomes big successively from top to bottom
Throwing disc of the quantity no less than 2, flow guiding head, feed tube, it is located on support with aerofoil, nylon wire, upper spacer, 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.
Further improvement of the invention is as follows:
Further, described purification pot is additionally provided with lower clapboard, described lower clapboard be located at purification pot inside lower end and by
Rotating shaft runs through, and described lower clapboard is connected with purification pot screw thread and is connected with rotating shaft gap.
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.
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 purification pot is additionally provided with net gas outlet pipe, and described net gas outlet pipe is located on the outside of purification pot, described
Net gas outlet pipe be connected with purification pot screw thread.
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 upper spacer is additionally provided with steam vent, and described steam vent runs through upper spacer.
Compared with prior art, the centrifugal smoke eliminator, during work, decoction is continuously passed through purification by feed tube
Tank, flow guiding head is by decoction uniform divided flows that feed tube inputs and accelerates to rush at conical head, and buncher is driven by transmission mechanism
The 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 through flue gas inlet pipe to be purified
Tank, then fully reacted with the decoction of atomization through slowly being fallen with aerofoil, it is configured in upper spacer that the decoction of atomization is condensed into drop
On steam vent fall and discharged in lower clapboard, purified gas through net gas outlet pipe, sewage is slowly discharged through discharging tube.The device knot
Structure is simple, using centrifugal principle, decoction is thrown away into atomization at a high speed so that flue gas is well mixed with the decoction being atomized, is continuous, effectively
Improve gas cleaning efficiency and clean-up effect, meanwhile, without being equipped with compression system and atomizer, effectively reduce production cost and
Maintenance cost.
Brief description of the drawings
Fig. 1 shows front view of the present invention
Fig. 2 shows upper spacer top view of the present invention
The buncher 2 of support 1
The transmission mechanism 4 of purification pot 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
The seal receptacle 202 of lower clapboard 201
The net gas outlet pipe 204 of discharging tube 203
The ball head 801 of flue gas inlet pipe 205
Steam vent 1201
Embodiment
As shown in Figure 1 and Figure 2, a kind of centrifugal smoke eliminator, 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 and is no less than the throwing disc of 2 successively from top to bottom
7th, flow guiding head 8, feed tube 9, with aerofoil 10, nylon wire 11, upper spacer 12, described purification pot 2 is located at the upper end of support 1, described
Purification pot 2 be connected with the screw thread of support 1, described buncher 3 is located at the lower end of support 1, described buncher 3 and support 1
Screw thread is connected, and described transmission mechanism 4 is located at the upper end of buncher 3 and is located at the upper end of support 1, and described transmission mechanism 4 is with adjusting
The key of speed motor 3 is connected and is rotatedly connected with support 1, and described rotating shaft 5 is through purification pot 2 and is located at the upper end of transmission mechanism 4, described
Rotating shaft 5 be rotatedly connected with purification pot 2 and be connected with the key of transmission mechanism 4, described conical head 6 is located at the upper end of rotating shaft 5 and is located at
The inner side of purification pot 2, described conical head 6 are connected with the screw thread of rotating shaft 5, and described throwing disc 7 is located at the outside of conical head 6, and described gets rid of
Disk 7 is weldingly connected with conical head 6, and described flow guiding head 8 is located at the upper end of conical head 6, and described flow guiding head 8 is welded with conical head 6
It is connected, the described lower end of feed tube 9 is stretched into purification pot 2 and positioned at the outside of flow guiding head 8, described feed tube 9 and the spiral shell of purification pot 2
Line is connected, and described is located at the inner top side of purification pot 2 with aerofoil 10 and is run through by flow guiding head 8, and described matches somebody with somebody aerofoil 10 and purification
The screw thread of tank 2 is connected, and positioned at the upper end of aerofoil 10 is matched somebody with somebody, described nylon wire 11 is connected described nylon wire 11 with the screw thread of aerofoil 10,
Described upper spacer 12 is located at the lower end of conical head 6 and run through by rotating shaft 5, and described upper spacer 12 is rotatedly connected with rotating shaft 5, described
Purification pot 2 be additionally provided with lower clapboard 201, described lower clapboard 201 is located at the inside lower end of purification pot 2 and run through by rotating shaft 5, described
Lower clapboard 201 be connected with the screw thread of purification pot 2 and be connected with the gap of rotating shaft 5, described lower clapboard 201 is additionally provided with seal receptacle 202,
Described seal receptacle 202 is located at the center of lower clapboard 201 and run through by rotating shaft 5, described seal receptacle 202 and the spiral shell of lower clapboard 201
Line is connected and is connected with the gap of rotating shaft 5, and seal receptacle 202 is used for sealing pivot 5, and described lower clapboard 201 is additionally provided with discharging tube
203, described discharging tube 203 is located at the lower end of lower clapboard 201 and runs through purification pot 2, described discharging tube 203 and lower clapboard 201
Screw thread is connected and is connected with the screw thread of purification pot 2, and described purification pot 2 is additionally provided with net gas outlet pipe 204, described net gas outlet pipe 204
Positioned at the outside of purification pot 2, described net gas outlet pipe 204 is connected with the screw thread of purification pot 2, and described purification pot 2 is additionally provided with flue gas and entered
Pipe 205, described flue gas inlet pipe 205 are located at the upper end of purification pot 2, and described flue gas inlet pipe 205 is connected with the screw thread of purification pot 2, institute
The flow guiding head 8 stated is additionally provided with ball head 801, and described ball head 801 is located at the upper end of flow guiding head 8, and described ball head 801 is with leading
First 8 one of stream is connected, and ball head 801 is used for highly pressurised liquid uniform divided flows and accelerated so that highly pressurised liquid is uniform through flow guiding head 8
Conical head 6 is rapidly flowed toward, described upper spacer 12 is additionally provided with steam vent 1201, and described steam vent 1201 runs through upper spacer 12,
The centrifugal smoke eliminator, during work, decoction is continuously passed through purification pot 3 by feed tube 9, and flow guiding head 8 inputs feed tube 9
Decoction uniform divided flows and accelerate to rush at conical head 6, buncher 2 passes through transmission mechanism 4 and drives the conical head being connected with rotating shaft 5
6 high-speed rotations, 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 fall fully reacts with the decoction being atomized, and the decoction of atomization is condensed into the configured steam vent on upper spacer 12 of drop
1201 fall and are discharged in lower clapboard 201, purified gas through net gas outlet pipe 204, and sewage is slowly discharged through discharging tube 203.The dress
To put simple in construction, using centrifugal principle, decoction is thrown away into atomization at a high speed so that flue gas is well mixed, continuously with the decoction of atomization,
Gas cleaning efficiency and clean-up effect are effectively improved, meanwhile, without being equipped with compression system and atomizer, effectively reduce and be produced into
Sheet and maintenance 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.