CN207137668U - A kind of outer drive vertical mixing reactor - Google Patents
A kind of outer drive vertical mixing reactor Download PDFInfo
- Publication number
- CN207137668U CN207137668U CN201720053006.4U CN201720053006U CN207137668U CN 207137668 U CN207137668 U CN 207137668U CN 201720053006 U CN201720053006 U CN 201720053006U CN 207137668 U CN207137668 U CN 207137668U
- Authority
- CN
- China
- Prior art keywords
- turbine
- shaft
- reaction tower
- discharge opeing
- cone bucket
- 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
Landscapes
- Physical Or Chemical Processes And Apparatus (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
The utility model discloses vertical mixing reactor is driven outside one kind, absorber tube is arranged on above stirring turbine, is entered cigarette interface and is arranged on below stirring turbine；The bottom of turbine shaft is provided with rotating shaft overcoat, discharge opeing cone bucket of the rotating shaft overcoat through the bottom of reaction tower, the discharge opeing cone bucket sealing welding of bottom of the outer wall of rotating shaft overcoat with reacting tower is firmly connected, and rotating shaft overcoat is provided with rotary seal structure between the port and turbine shaft inside reaction tower；It is arranged on the end connection that the motor output shaft outside reaction tower pays turbine shaft by driving cog.Buncher is not set in the utility model reaction tower, also eliminates umbrella tooth transmission, the relative rotation of only rotating shaft and bearing cap needs to seal, and this has been greatly lowered engineering difficulty, increases reliability.Stirring turbine or stirring structure both can plural serial stage realize pollutant minimum discharge, also can multiple parallel connections meet the requirement of engineering of large-scale gas flow purification.
Description
Technical field
The utility model belongs to the chemical purifying device that gas to be clean is handled with stripping liquid, and in particular to a kind of outer
Drive vertical mixing reactor.
Background technology
Existing Pneumatic emulsifying technology and double-cyclone tandem pneumatic emulsifying technology are most widely used efficient chemical purifications
Device, above-mentioned Pneumatic emulsifying technology are based on air-flow and carry out chemistry in suspension emulsification state by cyclone liquid-gas rotation occurs
Mass transfer reaction, eddy flow flow velocity size more cause chemical cleaning method rate to carry again greatly because being limited to be difficult to reach by flow parameter and cyclone
Height, especially because air flow rate change is difficult to reach stable state emulsification.Vertical type module integrated reaction device is reachable using agitating mode
Chemical transmitter reaction is carried out in suspension emulsification state to liquid and gas, also can dynamic speed adjustment under air flow rate significantly change operating mode
And Multi-stage stirring reaction and high-efficiency operation, this for it is small, in and giant chemical cleaning project minimum discharge highly significant.So
And unfortunately stir motor and be located among air-flow, it is necessary to which electric motor operation should be very reliable, the driving of peripheral hardware horizontal machine is tied
Structure, then need to be driven driving agitator arm structure through umbrella tooth so that complicated；Also Multi-stage stirring vertical type module integrated reaction
In device, do not propose that liquid-gas is most preferably sufficiently mixed the concrete measure of effect.
The content of the invention：
The defects of in order to overcome above-mentioned background technology, the utility model provide a kind of outer drive vertical mixing reactor, had
The liquid-gas mixed effect more optimized, it is in order to solve the above-mentioned technical problem of the present utility model used by technical scheme be：
A kind of outer drive vertical mixing reactor, including reaction tower, reaction tower top are provided with exhanst gas outlet, and bottom is provided with
Discharge opeing cone bucket, discharge opeing export the bottom for being arranged at discharge opeing cone bucket, react and are additionally provided with tower into cigarette interface and absorber tube, reaction
Turbine shaft is provided with tower, turbine shaft is provided with stirring turbine, and absorber tube is arranged on above stirring turbine, enters cigarette interface
It is arranged on below stirring turbine；The bottom of turbine shaft is provided with rotating shaft overcoat, and rotating shaft overcoat passes through discharge opeing cone bucket, rotating shaft overcoat
Outer wall is tightly connected with discharge opeing cone bucket, and two of rotating shaft overcoat are respectively equipped with rotary seal structure between port and turbine shaft；
The end that motor output shaft pays turbine shaft by driving cog connects.
It is preferred that the exhanst gas outlet at the top of reaction tower is provided with purification chimney.The outer wall of rotating shaft overcoat and discharge opeing cone bucket
It is tightly connected.
It is preferred that it is provided with demister above the absorber tube reacted in tower.
It is preferred that discharge opeing cone bucket is eccentric structure, the set location of discharge opeing outlet is not on the central axis of reaction tower.
It is preferred that including at least two stirring turbines, the inwall for reacting tower is additionally provided with drain inclined-plane, and adjacent two are stirred
Mix and be provided with a drain inclined-plane between turbine.
It is preferred that multiple reaction towers are interconnected and form ring-type tower, hollow tower body inner cylinder is formed at center, it is multiple
Each exhanst gas outlet of reaction atop a tower is connected to a purification chimney, and the discharge opeing cone bucket of multiple reaction tower bottoms is connected to
One discharge opeing outlet.
It is preferred that each turbine shaft at each reaction tower difference center is along using ring-type tower central shaft as the center of circle
Circumference uniform distribution set.
It is preferred that turbine shaft bottom is arranged with tubular shaft, the end of turbine shaft passes through the bottom of tubular shaft；Pipe
Shape rotating shaft is externally provided with axle sleeve, and the bottom of tubular shaft passes through the bottom of axle sleeve；Axle sleeve passes through discharge opeing cone bucket, the outer wall of axle sleeve and row
Liquid cone bucket is tightly connected；The end of turbine shaft pays connection the first motor by the first driving cog, and the end of tubular shaft passes through
Second driving cog pays connection the second motor.
It is preferred that port of the tubular shaft inside reaction tower is connected by rotary seal structure with turbine shaft,
Port of the axle sleeve inside reaction tower is connected by rotary seal structure with tubular shaft.
It is preferred that the outer wall of reaction tower is provided with the depressed part to ring-type tower central axis, reaction tower is positioned at depression
Cylinder above and below portion is designated as upper shell and lower shell respectively, drain cone bucket between upper shell and depressed part；In upper shell
Provided with upper turbine shaft, through the upper motor of drain cone bucket connection, the bottom of upper turbine shaft passes through upper for the end of upper turbine shaft
Rotating shaft overcoat is tightly connected with drain cone bucket, and it is close that rotation is respectively equipped between two ports of upper rotating shaft overcoat and upper turbine shaft
Seal structure；Lower turbine shaft is provided with lower shell, the end of lower turbine shaft turns through the lower motor of discharge opeing cone bucket connection, lower turbine
The bottom of axle is tightly connected by lower rotary shaft overcoat and discharge opeing cone bucket, between two ports of lower rotary shaft overcoat and lower turbine shaft
It is respectively equipped with rotary seal structure.
The beneficial effects of the utility model are：The utility model one is that leather goes umbrella tooth to be driven, using outer drive vertical machine
Driving, second, in Multi-stage stirring, most upper stirring wheel overcentre is located at by the liquid outlet of absorber tube, in upper level with
Drain inclined-plane is set between one-level stirring, stripping liquid is flowed to the mixing center of next stage as far as possible, reaches in the gas flow
Flow through path and the time is longer.Outer drive vertical machine can be both put in reactor head, can also place it in reactor
Bottom.Comparatively speaking it is put in that substructure is more compact, and installation and repairing is more convenient.By buncher, driving cog pay, rotating shaft overcoat,
Turbine shaft, stirring turbine composition stirring structure.The gas purification of big flow is in parallel using multiple stirring structures；High efficiency chemistry
Purification uses multistage turbine or Multi-stage stirring structures in series.
It is outer drive vertical mixing reactor reaction tower bottom be liquid-gas react after product waste liquid cone bucket, discharge opeing
The leakage fluid dram of cone bucket namely the location bias of discharge opeing outlet avoid the center of reaction tower, pass through the rotating shaft overcoat of stirring structure
The upper round mouth center of waste liquid cone bucket namely with reaction tower it is concentric.Rotating shaft overcoat is built with rolling bearing, rolling bearing supporting whirlpool
Take turns rotating shaft.Several stirring turbines are connected firmly in turbine shaft, the lower end of turbine shaft is inserted in the hole that driving cog is paid and by bonded
Connect driving cog to pay, the axle of buncher is paid also by hole and key with driving cog to be coupled.Stirring structure both can be multiple independent and stir
Mix structure parallel connection or circumferentially distributed multiple stirring structures in a large-sized tank body；Multi-stage stirring series connection both can be
Axially arranged more stirring turbines or the suit multi-layer rotating outer shaft sleeve outside turbine shaft, even if intermediate rotary shaft overcoat turns into pipe
The turbine shaft of shape structure, outermost layer rotating shaft overcoat are connected firmly with discharge opeing cone bucket, and each turbine shaft is driven by variable-speed motor respectively
It is dynamic；Can also be in the independent stirring structure of the reaction axially arranged multistage of tower.
Buncher is not set in the utility model reaction tower, also eliminates umbrella tooth transmission, only rotating shaft and bearing cap
Relative rotation needs to seal, and this has been greatly lowered engineering difficulty, increases reliability.Stirring turbine or stirring structure both can be multistage
Pollutant minimum discharge is realized in series connection, also can multiple parallel connections meet the requirement of engineering of large-scale gas flow purification.
Brief description of the drawings
Fig. 1 is the vertical section structure schematic diagram of the utility model embodiment one；
Fig. 2 is the vertical section structure schematic diagram of the utility model embodiment two；
Fig. 3 is the vertical section structure schematic diagram of the utility model embodiment three；
Fig. 4 is the vertical section structure schematic diagram of the utility model embodiment four；
Fig. 5 is the vertical section structure schematic diagram of the utility model embodiment five；
Fig. 6 is Fig. 3 along the profile at A-A.
Embodiment
The utility model is described further with reference to the accompanying drawings and examples.
Embodiment one, as shown in figure 1, one kind of the present embodiment is outer to drive vertical mixing reactor, including reaction tower 11, instead
The top of tower 11 is answered to be provided with exhanst gas outlet, bottom is provided with discharge opeing cone bucket 4, and discharge opeing outlet 13 is arranged at the bottom of discharge opeing cone bucket 4, instead
Answer and be additionally provided with tower 11 into cigarette interface 5 and absorber tube 9, it is characterised in that：Turbine shaft 6, whirlpool are provided with reaction tower 11
Take turns rotating shaft 6 and be provided with stirring turbine 7, absorber tube 9 is arranged on the top of stirring turbine 7, enters cigarette interface 5 and is arranged on stirring turbine 7
Lower section；The bottom of turbine shaft 6 is provided with rotating shaft overcoat 3, and rotating shaft overcoat 3 passes through discharge opeing cone bucket 4, the outer wall of rotating shaft overcoat 3 and row
Liquid cone bucket 4 is tightly connected, and rotary seal structure is respectively equipped between two ports of rotating shaft overcoat 3 and turbine shaft 6；Motor 1
Output shaft is paid 2 by driving cog and is connected with the end of turbine shaft 6.
The exhanst gas outlet for reacting the top of tower 11 is provided with purification chimney 12.
Discharge opeing cone bucket 4 is the eccentric structure with an inclined-plane, the outer wall of rotating shaft overcoat 3 and the inclined-plane of discharge opeing cone bucket 4
It is tightly connected by way of welding.The set location of discharge opeing outlet 13 is not on the central axis of reaction tower 11, in conceding
The position of mandrel line is used to set turbine shaft 6.
Multistage demister 10 is provided with above absorber tube 9 in reaction tower 11.
The present embodiment includes at least two stirring turbines 7, and the inwall of reaction tower 11 is additionally provided with drain inclined-plane 8, and drain is oblique
Face 8 is between two stirring turbines 7.
Axially supporting is circumferential rotatable by the bearing in rotating shaft overcoat 3 for the turbine shaft 6 of the present embodiment, on rotating shaft overcoat 3
Bearing seal structure sealing protection bearing in it.
Rotating shaft overcoat 3 through bottom run in liquid cone bucket 4 be fixed on reaction tower 11 symmetrical centre at, buncher 1 with
Reaction tower 11 is each attached on support.
Specific work process includes：When gas to be clean from enter cigarette interface 5 enter reaction 11 interior lower end of tower when, adjust
The rotation of speed motor 1 causes stirring turbine 7 that stirring rotation occurs through driving cog pair 2 and turbine shaft 6, and gas stream to be clean occurs
Just there is the helical rotation for rising and rotating.While gas stream to be clean flows into cigarette interface 5, from being located at for absorber tube 9
Port outside reaction tower 11 flows into, and is scattered from the stripping liquid of the jet outflow outside reaction tower 11 upper
The center of the stirring turbine 7 in portion.Air-flow screw effect under, stripping liquid by dispersion mixing among air-flow, liquid
State absorbent closes in occurring with the acid in gas to be clean to react.Reaction product and the liquid suction for going back unreacted consumption
Agent is received in the presence of centrifugal force and gravity, under fall on the inwall of reaction tower cylinder 11, under gravity, then from reaction tower
11 inwall is flowed in the upper inclined surface on drain inclined-plane 8, then is wandered to the center of following stirring turbine 7 toward flowing down, and is being stirred
Under the stirring for mixing turbine 7, reaction product and go back unreacted consumption stripping liquid in the presence of centrifugal force and gravity again
It is secondary that conjunction reaction in soda acid is occurred among air-flow by dispersion mixing, and shed the inwall of reaction tower 11 bottom in centrifugal action
On, wander into discharge opeing cone bucket 4 and discharged from discharge opeing as depicted outlet 13 under gravity.Gas stream to be clean exists
During stirring turbine 7 by reacting tower 11 bottom, with scattering lower stripping liquid hair on drain inclined-plane 8 in spiral
Raw primarily broken mixing and absorption.It is that the second fraction occurs again in air-flow when by the stirring turbine 7 on reaction tower 11 top
Dissipate mixing and absorbing reaction.The rotating speed of buncher 1 is adjusted, also just have adjusted the rotating speed of stirring turbine 7, its linear velocity can be long-range
Linear velocity in Pneumatic emulsifying technology, this i.e. adjustable increase absorption efficiency.It is to be clean by two-stage dispersion mixing and absorption
The airflow passes of processing remove the moisture in air-flow at demister 10, then purified chimney 12 is discharged, and the water in air-flow
Divide then the inwall of cistron tower 11 is dirty finally to be discharged from discharge opeing outlet 13.
Deviate the center line of reaction tower 11, the lower space cloth merged out in the discharge opeing outlet of the present embodiment discharge opeing cone bucket 4
2 and buncher 1 are paid setting in the driving cog of the axle lower end of the stirring structure of the center line of reaction tower 11；Absorber tube 9 goes out
The outlet on mouth and drain inclined-plane 8 is on stirring turbine 7 and around its center.
The outer turbine shaft 6 for driving vertical mixing reactor only has with rotating shaft overcoat 3 at one inside reaction tower 11
Rotatory sealing, handling rotatory sealing well, this be not difficult matter in engineering now, and reliability is high.Stripping liquid, which scatters, to be stirred
Mix the efficiency that dispersion mixing and absorbing reaction are improved at the center of turbine 7.Vertical outer drive stirring uses buncher 1, structure
Simple and reliable, speed governing is convenient, and under the operating mode of the flow parameter change of processing to be clean, both absorbing reaction easily reaches energy-efficient,
There is working stability.
Embodiment two, as shown in Fig. 2 the present embodiment is additionally arranged a stirring turbine 7 and one on the basis of embodiment one
Individual drain inclined-plane 8, includes three stirring turbines 7 and two drain inclined-planes 8 in the reaction tower 11 of the present embodiment, adjacent two
A drain inclined-plane 8 is provided between stirring turbine 7.The present embodiment is that vertical mixing reactor and Fig. 1 monotubulars are driven outside monocular tertiary
It is essentially identical that vertical mixing reactor is driven outside twin-stage, it, which is distinguished, is more stirring turbines 7 and the structure of drain inclined-plane 8, that is,
More one-levels stir absorption cleaning, reach and increase absorption cleaning efficiency.
Embodiment three, the present embodiment is as shown in figure 3, multiple reaction towers 11 are interconnected and form ring-type tower, at center
Hollow tower body inner cylinder 18 is formed, each exhanst gas outlet at multiple tops of reaction tower 11 is connected to a purification chimney 12, more
The discharge opeing cone bucket 4 of individual reaction tower 11 bottom is connected to a discharge opeing outlet 13.Formed in each reaction tower of ring-type tower
Include the outer all parts for driving vertical mixing reactor kind described in embodiment one and embodiment two.In addition, as shown in fig. 6,
Each turbine shaft 6 at center is set each reaction tower 11 along the circumference uniform distribution using ring-type tower central shaft as the center of circle respectively
Put.
The present embodiment is that vertical mixing reactor is driven outside more three-levels, is to drive vertical stir outside multiple Fig. 1 or Fig. 2 monocular tertiaries
Reactor parallel-connection structure is mixed, suitable for big flow gas engineering to be clean.Compared with Fig. 2, the discharge opeing cone bucket in Fig. 3 is multiple rows
The sharing structure that liquid cone bucket 4 gathers together, is a large-scale cone bucket, and its center is shared discharge opeing outlet 13；Purify chimney
12 are arranged on the top of annular tower above, form public cleaning chimney.At the inclined-plane of middle part, there are multiple rotating shaft overcoats 3 vertically to wear
Cross and connect firmly structure；Annular tower is that reaction tower 11 maximizes structure, and tower body inner cylinder is set in it, reacts tower 11 and tower body
Inner cylinder 13c is constituted and each stirring structure is dispersed with annular space, and the absorbing liquid outlet of each end of absorber tube 9 is sitting at
It is each most on stirring turbine 7 in top.Down, each drain inclined-plane 8 is arranged in stirring whirlpool around respective turbine shaft 6
Top in wheel 7.Enter cigarette interface 5 both but as Fig. 1 or Fig. 2 each independently enter cigarette interface may also be merge share it is large-scale enter cigarette
Interface.After stripping liquid and gas to be clean and pneumatic each agitating device is passed through, annular space is just produced around each whirlpool
The helical rotation of rotating shaft 6 is taken turns, the result is that the gas to be clean of big flow is able to efficient process, realizes minimum discharge.
Example IV, as shown in figure 4, improvement of the present embodiment for the above embodiments one to embodiment three is：Whirlpool
Wheel rotating shaft 6 bottom is arranged with tubular shaft 15, and the end of turbine shaft 6 passes through the bottom of tubular shaft 15；Outside tubular shaft 15
Provided with axle sleeve 16, the bottom of tubular shaft 15 passes through the bottom of axle sleeve 16；Axle sleeve 16 passes through discharge opeing cone bucket 4, the outer wall of axle sleeve 16
It is tightly connected with discharge opeing cone bucket 4；2.1 the first motors 1.1 of connection are paid in the end of turbine shaft 6 by the first driving cog, and tubulose turns
2.2 the second motors 1.2 of connection are paid by the second driving cog in the end of axle 15.
And it is connected respectively by rotary seal structure with turbine shaft 6 at two ports of tubular shaft 15, axle sleeve 16
Two ports at be connected respectively by rotary seal structure with tubular shaft 15.
The present embodiment is that vertical mixing reactor is driven outside monotubular multistage double-shaft concentric, vertical with being driven outside Fig. 1 or Fig. 2 monotubulars twin-stage
Formula stirred reactor is essentially identical, and it, which is distinguished, is that Fig. 4 transfer outer shaft sleeves are that the turbine shaft of a tubular-shaped structures namely tubulose turn
Axle 15, its endoporus carry turbine shaft 6 built with bearing, and its outside cylinder top installation stirring turbine 7, lower cylindrical is by axle sleeve
Bearing supporting in 16.Axle sleeve 16 is fixed at the center of the lower inclined plane of discharge opeing cone bucket 4.The transmission of lower end insertion second of axle sleeve 16
Tooth is paid in 2.2 hole and key connecting, and hole and key connecting are also used between the rotating shaft of the second motor 1.2 and driving cog pair 2.2.In most
Between be solid long turbine shaft, remaining is the gradually turbine shaft of short tubular structure successively, and can be filled in each turbine shaft is
There are multiple stirring turbines.The structure in Fig. 4 is to add a set of and turbine on the basis of embodiment one, two or three in other words
The stirring structure of 6 identical axial line of rotating shaft.Stirring turbine 7 on turbine shaft 6 can with the stirring turbine 7 on axle sleeve 16
There is different rotating speeds, the rotating speed for adjusting the first motor 1.1 and the second motor 1.2 just can preferably dynamic control chemical cleaning method
Journey.
Embodiment five, as shown in figure 5, the outer wall of reaction tower 11 is provided with the depressed part 14 to ring-type tower central axis,
The cylinder that reaction tower 11 is located above and below depressed part 14 is designated as upper shell 11.1 and lower shell 11.2, upper shell respectively
Drain cone bucket 17 between 11.1 and depressed part 14；Upper turbine shaft 6.1, the end of upper turbine shaft 6.1 are provided with upper shell 11.1
End connects upper motor 1.3 through drain cone bucket 17, and the bottom of upper turbine shaft 6.1 is close by upper rotating shaft overcoat and drain cone bucket 17
Envelope connection, rotary seal structure is respectively equipped between two ports of upper rotating shaft overcoat and upper turbine shaft 6.1；Lower shell 11.2
Interior to be provided with lower turbine shaft 6.2, the end of lower turbine shaft 6.2 connects lower motor 1.4, lower turbine shaft through discharge opeing cone bucket 4
6.2 bottom is tightly connected by lower rotary shaft overcoat and discharge opeing cone bucket 4, two ports and the lower turbine shaft of lower rotary shaft overcoat
Rotary seal structure is respectively equipped between 6.2.
The present embodiment can be changing of being carried out on the basis of any one embodiment of above-described embodiment one to example IV
Enter.
The essence of embodiment five is the combination in parallel and serial of multiple stirring structures, its discharge opeing cone bucket with embodiment three
Discharge opeing cone bucket 4, tower body inner cylinder are similar with tower body inner cylinder.It is reaction tower outer barrel to react tower 11, and its middle part external cylindrical surface has contracting
The space of small reaction tower cylinder size, buncher 1 is covered this space mounting more and driving cog pays 2；In the tower body of size reduction
Annular space between cylinder 11 and tower body inner cylinder is both gas flow channel to be clean, and stirs turbine center to next stage and supply
The drain cone bucket 17 of liquid.The combination in parallel and serial of this stirring structure may insure that big flow gas engineering to be clean is able to
Realize minimum discharge.
The utility model one is that leather goes umbrella tooth to be driven, using outer drive vertical machine driving, second, in Multi-stage stirring, will
The liquid outlet of absorber tube 9 is located at most upper stirring wheel overcentre, and drain inclined-plane is set between upper level and next stage stirring
8, make mixing center of the stripping liquid sulphur as far as possible to next stage, reach and flow through path in the gas flow and the time is longer.Outer drive
Vertical machine 1 can be both put in reactor head, can also place it in the bottom of reactor.Comparatively speaking it is put in lower junction
Structure is more compact, and installation and repairing is more convenient.7 groups 2, rotating shaft overcoat 3, turbine shaft 6, stirring of turbine are paid by buncher 1, driving cog
Into stirring structure.The gas purification of big flow is in parallel using multiple stirring structures；High efficiency chemical cleaning method using multistage turbine or
Multi-stage stirring structures in series.
It is outer drive vertical mixing reactor reaction tower bottom be liquid-gas react after product waste liquid cone bucket, discharge opeing
The leakage fluid dram of cone bucket 4 namely the location bias of discharge opeing outlet 13 avoid the center of reaction tower 11, make outside the rotating shaft of stirring structure
Set is concentric through the upper round mouth center of waste liquid cone bucket namely with reaction tower.Rotating shaft overcoat 3 is built with rolling bearing, rolling bearing
Support turbine shaft 6.Several stirring turbines 7 are connected firmly in turbine shaft 6, the lower end insertion driving cog of turbine shaft 6 is paid in 2 hole
And paid by key connecting driving cog, the axle of buncher is paid 2 with driving cog also by hole and key and coupled.Stirring structure both can be more
Individual independent stirring structure it is in parallel or in a large-sized tank body the uniform multiple stirring structures of ring；Multi-stage stirring string
Connection both can be in axially arranged more stirring turbines 7 or be set with multi-layer rotating outer shaft sleeve outside turbine shaft, most make intermediate rotary shaft
Overcoat turns into the turbine shaft of tubular-shaped structures, and outermost layer rotating shaft overcoat connects firmly with discharge opeing cone bucket 4, and each turbine shaft is respectively by adjusting
Electric motor with speed drives；Can also be in the independent stirring structure of the reaction axially arranged multistage of tower 11.
Buncher is not set in the utility model reaction tower, also eliminates umbrella tooth transmission, only rotating shaft and bearing cap
Relative rotation needs to seal, and this has been greatly lowered engineering difficulty, increases reliability.Stirring turbine or stirring structure both can be multistage
Pollutant minimum discharge is realized in series connection, also can multiple parallel connections meet the requirement of engineering of large-scale gas flow purification.
It should be appreciated that for those of ordinary skills, can according to the above description be improved or converted,
And all these modifications and variations should all belong to the protection domain of the appended claims for the utility model.
Claims (10)
1. a kind of outer drive vertical mixing reactor, including reaction tower (11), described reaction tower (11) top go out provided with flue gas
Mouthful, bottom is provided with discharge opeing cone bucket (4), and discharge opeing outlet (13) is arranged at the bottom of the discharge opeing cone bucket (4), the reaction tower
(11) it is additionally provided with into cigarette interface (5) and absorber tube (9), it is characterised in that：Turn in the reaction tower (11) provided with turbine
Axle (6), the turbine shaft (6) are provided with stirring turbine (7), and the absorber tube (9) is arranged on the stirring turbine (7)
Side, it is described enter cigarette interface (5) be arranged on below stirring turbine (7)；The bottom of the turbine shaft (6) is provided with rotating shaft overcoat
(3), the rotating shaft overcoat (3) passes through the discharge opeing cone bucket (4), the outer wall of the rotating shaft overcoat (3) and the discharge opeing cone bucket (4)
It is tightly connected, rotary seal structure is respectively equipped between two ports of the rotating shaft overcoat (3) and the turbine shaft (6)；
Motor (1) output shaft is paid (2) by driving cog and is connected with the end of the turbine shaft (6).
A kind of 2. outer drive vertical mixing reactor according to claim 1, it is characterised in that：The reaction tower (11)
The exhanst gas outlet at top is provided with purification chimney (12), and the outer wall of the rotating shaft overcoat (3) connects with the discharge opeing cone bucket (4) sealing
Connect.
A kind of 3. outer drive vertical mixing reactor according to claim 2, it is characterised in that：In the reaction tower (11)
Demister (10) is provided with above the interior absorber tube (9).
A kind of 4. outer drive vertical mixing reactor according to claim 3, it is characterised in that：The discharge opeing cone bucket (4) is
Eccentric structure, the set location of the discharge opeing outlet (13) is not on the central axis of reaction tower (11).
A kind of 5. outer drive vertical mixing reactor according to claim 4, it is characterised in that：Including being stirred described at least two
Mix turbine (7), the inwall of the reaction tower (11) is additionally provided with drain inclined-plane (8), adjacent two stirring turbines (7) it
Between be provided with a drain inclined-plane (8).
A kind of 6. outer drive vertical mixing reactor according to claim 5, it is characterised in that：Multiple reaction towers
(11) it is interconnected and forms ring-type tower, hollow tower body inner cylinder (18), multiple reaction tower (11) tops is formed at center
Each exhanst gas outlet in portion is connected to a purification chimney (12), the discharge opeing of multiple described reaction tower (11) bottoms
Cone bucket (4) is connected to a discharge opeing outlet (13).
A kind of 7. outer drive vertical mixing reactor according to claim 6, it is characterised in that：Each reaction tower
(11) each turbine shaft (6) respectively at center sets along the circumference uniform distribution using the ring-type tower central shaft as the center of circle
Put.
8. the outer drive vertical mixing reactor of one kind according to claim 6 or 7, it is characterised in that：The turbine shaft (6)
Bottom is arranged with tubular shaft (15), and the end of the turbine shaft (6) passes through the bottom of the tubular shaft (15)；The pipe
Shape rotating shaft (15) is externally provided with axle sleeve (16), and the bottom of the tubular shaft (15) passes through the bottom of the axle sleeve (16)；The axle
Set (16) passes through the discharge opeing cone bucket (4), and the outer wall of the axle sleeve (16) is tightly connected with the discharge opeing cone bucket (4)；The whirlpool
(2.1) first motor of connection (1.1), the end of the tubular shaft (15) are paid by the first driving cog in the end for taking turns rotating shaft (6)
(2.2), which are paid, by the second driving cog connects the second motor (1.2).
A kind of 9. outer drive vertical mixing reactor according to claim 8, it is characterised in that：Tubular shaft (15) position
It is connected in the internal port of reaction tower (11) by rotary seal structure with the turbine shaft (6), axle sleeve (16) position
It is connected in the internal port of reaction tower (11) by rotary seal structure with the tubular shaft (15).
A kind of 10. outer drive vertical mixing reactor according to claim 8, it is characterised in that：The reaction tower (11)
Outer wall be provided with to the ring-type tower central axis depressed part (14), it is described reaction tower (11) be located at the depressed part
(14) cylinder above and below is designated as upper shell (11.1) and lower shell (11.2) respectively, the upper shell (11.1) and described
Drain cone bucket (17) between depressed part (14)；Upper turbine shaft (6.1) is provided with the upper shell (11.1), the upper turbine turns
Through motor (1.3) in drain cone bucket (17) connection, the bottom of the upper turbine shaft (6.1) leads to for the end of axle (6.1)
Cross rotating shaft overcoat to be tightly connected with the drain cone bucket (17), two ports and the upper turbine of the upper rotating shaft overcoat turn
Axle is respectively equipped with rotary seal structure between (6.1)；Lower turbine shaft (6.2) is provided with the lower shell (11.2), under described
The end of turbine shaft (6.2) is through the lower motor (1.4) of the discharge opeing cone bucket (4) connection, under the lower turbine shaft (6.2)
Portion is tightly connected by lower rotary shaft overcoat and the discharge opeing cone bucket (4), two ports and the lower whirlpool of the lower rotary shaft overcoat
Rotary seal structure is respectively equipped between wheel rotating shaft (6.2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720053006.4U CN207137668U (en) | 2017-01-16 | 2017-01-16 | A kind of outer drive vertical mixing reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720053006.4U CN207137668U (en) | 2017-01-16 | 2017-01-16 | A kind of outer drive vertical mixing reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207137668U true CN207137668U (en) | 2018-03-27 |
Family
ID=61657814
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720053006.4U Expired - Fee Related CN207137668U (en) | 2017-01-16 | 2017-01-16 | A kind of outer drive vertical mixing reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207137668U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106964248A (en) * | 2017-01-16 | 2017-07-21 | 余汉明 | A kind of outer drive vertical mixing reactor |
| CN110548320A (en) * | 2019-08-19 | 2019-12-10 | 马鞍山市铔冠重工机械有限公司 | Sewage purification device is used in production of multistage mould of coordinated type |
-
2017
- 2017-01-16 CN CN201720053006.4U patent/CN207137668U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106964248A (en) * | 2017-01-16 | 2017-07-21 | 余汉明 | A kind of outer drive vertical mixing reactor |
| CN110548320A (en) * | 2019-08-19 | 2019-12-10 | 马鞍山市铔冠重工机械有限公司 | Sewage purification device is used in production of multistage mould of coordinated type |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206762811U (en) | A kind of Chemical Manufacture powder material mixing arrangement | |
| CN1040930A (en) | Apparatus for desulfurization of waste pases by wet process | |
| CN207137668U (en) | A kind of outer drive vertical mixing reactor | |
| CN108554151A (en) | A kind of flue gas high-efficiency desulfurization dust separation device | |
| CN100577277C (en) | Self-suction type inner circulation overweight field gas-liquid reactor | |
| CN205517446U (en) | Chemistry detects uses agitating unit | |
| CN217490366U (en) | High-efficient flue gas desulfurization tower | |
| CN205759800U (en) | Combined type Multi-stage rotary packed bed mass transfer reaction device | |
| CN109987668B (en) | Dual-rotation gas-liquid separation device and wastewater treatment equipment | |
| CN205892858U (en) | Pneumatic rotatory aeration equipment of automatically cleaning | |
| CN202430047U (en) | Flocculation mixer | |
| CN107055824A (en) | A kind of high efficiency aeration device for treating sewage | |
| CN106964248A (en) | A kind of outer drive vertical mixing reactor | |
| CN1152733C (en) | Cyclone dispersion absorbing/separating process and absorbing tower | |
| CN205672618U (en) | A kind of high-efficiency concentrator with self-cleaning pressure-preventing rake function | |
| CN110327765A (en) | A kind of flue-gas dust-removing and desulfurization device | |
| CN106215656A (en) | A kind of ozone mixing reactor | |
| CN212417483U (en) | Tower body and water tank split type washing tower device | |
| CN107626199A (en) | A kind of gas cleaning reactor and flue gas purification system | |
| CN209885551U (en) | Two-stage coupled mechanical stirring and gas-gas reactor | |
| CN208003924U (en) | A kind of probiotic microcapsule preparation facilities | |
| CN106422740A (en) | Centrifugal type deep flue gas purification device provided with shunting ring and desulfurization tower | |
| CN208008498U (en) | A kind of sewage air-flotation device | |
| CN201040226Y (en) | Vertical type module integration reaction device | |
| CN207016569U (en) | A kind of mushroom head for being used to fluidize cyclic aeration device |
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: 20180327 Termination date: 20200116 |