CN205556651U - Integration device and including being somebody's turn to do device for gas delivery and material mixing - Google Patents
Integration device and including being somebody's turn to do device for gas delivery and material mixing Download PDFInfo
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- CN205556651U CN205556651U CN201620237901.7U CN201620237901U CN205556651U CN 205556651 U CN205556651 U CN 205556651U CN 201620237901 U CN201620237901 U CN 201620237901U CN 205556651 U CN205556651 U CN 205556651U
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- 239000000463 material Substances 0.000 title claims abstract description 52
- 238000002156 mixing Methods 0.000 title claims abstract description 30
- 230000010354 integration Effects 0.000 title description 2
- 238000003756 stirring Methods 0.000 claims abstract description 88
- 238000005273 aeration Methods 0.000 claims abstract description 17
- 238000012856 packing Methods 0.000 claims description 16
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 15
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- 230000003139 buffering effect Effects 0.000 abstract description 5
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- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 12
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Landscapes
- Mixers Of The Rotary Stirring Type (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
The utility model discloses a gas delivery and material mixing's integrated device, including rotatory (mixing) shaft and motor, be provided with the buffering air inlet housing that has the air inlet on the rotatory (mixing) shaft, linking department between rotatory (mixing) shaft and the buffering air inlet housing is sealed and is set up, be equipped with oblique leaf disc turbine agitator in the stirring portion of rotatory (mixing) shaft, the bottom is equipped with the micropore aeration device, the pore of ventilating is equipped with on the axial wall of the rotatory (mixing) shaft in the buffering air inlet housing, the pore should be ventilates through interior air intake chamber who sets up of rotatory (mixing) shaft and micropore aeration device intercommunication setting. The utility model discloses a to the impact of microorganism, the area of contact who just adopts the micropore aeration device to increase tiny bubble and microbial reaction coordinated the oblique leaf disc turbine agitator of multilayer simultaneously when increase buffering air inlet housing was used for reducing the intake velocity fluctuation, can make the material in the bioreactor strengthen gaseous biotransformation process by the downward inner wall all around of following the bioreactor main part again in center to the cocycle.
Description
Technical field
This utility model relates to a kind of for gas conveying and the integrated apparatus of material stirring and include the biological anti-of this device
Answer device.
Background technology
With H2With the synthesis gas wide material sources that CO is main component, including biomass pyrogenation gasification combustion gas, artificial coal gas,
Coke-stove gas etc., its yield is huge, can use as fuel thus alleviate Pressure on Energy, have good DEVELOPMENT PROSPECT.
But, its application there is problems in that H2Density liquefaction little, difficult, easily reveal, be difficult to storage and transport；CO has life
Thing toxic, potential safety hazard is big.Will be with H2It is converted into natural gas, not only with the synthesis gas methanation that CO is main component
It is prone to storage transport and uses, also improving safety, being beneficial to its popularization and application.
The method of synthesis gas methanation mainly includes chemical method, Physical and bioanalysis.Wherein chemical method is to utilize high temperature high
Pressure and catalyst be methane the conversion of other in addition to methane in synthesis gas, Physical be use pressure-variable adsorption separate,
Methane in synthesis gas is purified by the method such as cryogenic separation, membrance separation.Bioanalysis is to utilize anaerobic fermentation microorganism to incite somebody to action
H2It is converted into methane with CO, compares with Physical with chemical method and have that investment operating cost is low, H2High with CO conversion ratio,
The advantages such as non-secondary pollution, it is often more important that bioanalysis can complete the methanation of the organic wastes such as kitchen feces simultaneously,
Realize the synchronization process of many raw materials, utilize technology significant development and popularization synthesis gas high-grade.
Chinese patent: " a kind of gas-liquid mixed agitating device " (application number: 201510119968.0, application publication number CN
104772083 A)；It discloses a kind of gas-liquid mixed agitating device, it includes that frame and support, described support are fixed on
In frame, described frame being installed with reductor, the input of described reductor is connected with motor, and outfan is connected with and stirs
Mixing axle, described shaft inner hollow, the upper end of shaft is connected with air inlet pipe, and lower end is provided with the stirring of orbital curved leaf
Device, described shaft bottom is positioned at orbital curved leaf agitator center, and has the solarization air cap of ventilation.This patent master
Wanting feature is to be broken up by gas and liquid mixing when air inlet, for Air Bubble Size and degree of scatter not requirement, it is impossible to have
Effect increases gas residence time, also cannot be sufficiently mixed the reaction mass that solid concentration is of a relatively high, be only applicable to some anti-
Answer the gas-liquid chemical reaction that speed is fast.
Utility model content
First technical problem to be solved in the utility model is to provide a kind of for gas conveying and the integration of material stirring
Device；This device is for H2With CO biotransformation in anaerobic biological reactor, increase be buffered into air chamber for
Reduce the percussion to microorganism when intake velocity fluctuates, and use microporous aeration device to increase tiny bubble and microorganism
The contact area of reaction, coordinates multilamellar oblique leaf disc turbine stirrer simultaneously, it is possible to make material in bioreactor by
The heart downwards the most again surrounding inwall along bioreactor main body be circulated up, not only achieve being sufficiently mixed of anaerobic reaction material,
Also effectively increase gas and microorganism catalytic time, enhance the biotransformation of gas.
Second technical problem to be solved in the utility model is to provide one and includes above-mentioned for gas conveying and material stirring
The bioreactor of integrated apparatus；Described bioreactor coordinates above-mentioned integrated apparatus, it is possible to make biological respinse
Material in device by center downwards the most again surrounding inwall along bioreactor main body be circulated up, not only achieve anaerobic reaction
Being sufficiently mixed of material, also effectively increases gas and microorganism catalytic time, and this bioreactor is provided with
Gas circulation line, this gas circulation line can adapt to different air inlet compositions, and by the inner chamber of reactor body with
Circulation between the described inner chamber being buffered into air chamber realizes efficiently converting thoroughly.
For solving above-mentioned first technical problem, this utility model employing following technical proposals:
A kind of for gas conveying and the integrated apparatus of material stirring, described device includes Stirring axle and for driving
The motor that Stirring axle rotates；
Being provided with the air chamber that is buffered into air inlet on described Stirring axle, described Stirring axle can enter by current buffer
Air chamber rotates, and described Stirring axle and the described joining place being buffered between air chamber seal and arrange；
The mixing part of described Stirring axle is buffered into outside air chamber described in being placed in, and the mixing part of this Stirring axle is provided with
Tiltedly leaf disc turbine stirrer, the bottom of described Stirring axle is provided with microporous aeration device；Microporous aeration device is used for increasing
Add the contact area of tiny bubble and microbial reaction, and coordinate multilamellar oblique leaf disc turbine stirrer, it is possible to make biological anti-
Answer material in device by center the most again surrounding inwall along bioreactor main body be circulated up, it is achieved that anaerobic reaction thing
Being sufficiently mixed of material, is effectively increased gas and microorganism catalytic time, enhances the bioconversion mistake of gas
Journey.
Being provided with vent cap on the axial wall of the described Stirring axle being buffered in air chamber, this vent cap is stirred by rotation
The inlet plenum arranged in mixing axle connects setting with described microporous aeration device.
Further, being buffered into air chamber described in is body structure.
Further, described Stirring axle and the described joining place being buffered between air chamber are close by oiliness graphite packing case
Envelope is arranged, and this oiliness graphite packing case is arranged around described Stirring axle.Oiliness graphite packing case, is arranged at one
It is buffered on the end face outside air chamber；It is arranged at one on the intracavity bottom being buffered into air chamber；It is buffered in air chamber described
Chamber is with under outside opposing seal isolation, and the Stirring axle through this oiliness graphite packing case can carry out rotation freely.
Further, described motor by frame be installed in described in be buffered into above air chamber, and the main shaft of this motor is with described
Stirring axle connects, and the axis of the axis of the main shaft of described motor and described Stirring axle is same axis.This kind
Drive mechanism is relatively easy, energy utilization efficiency is high, it is to avoid the possibility of mechanical problem occur.
Further, the tilt angle theta of described oblique leaf disc turbine stirrer Leaf is identical, and this tilt angle theta
It it is 30 °～45 °.Used in the prior art is vertical vane, and it can only play dispersion radially and stirring action, and
This patent uses the blade with tilt angle theta, and it can realize radial and axial mixing, and increase in bioreactor
The time of staying of gas.
Further, the mixing part of described Stirring axle is provided with at least three layers of oblique leaf disc turbine stirrer, and three layers tiltedly
Leaf disc turbine stirrer specification is identical, and spacing between layers is identical；The top of the mixing part of described Stirring axle
The length leaving 1/5～1/4 does not installs oblique leaf disc turbine stirrer, its role is to, and need to fully make on mixing part
Tiltedly leaf disc turbine stirrer must be positioned at reaction mass, and ensures that the oblique leaf disc turbine stirrer of every layer has one up and down
Fixed material, so when Stirring axle Stirring, just can enable to material in bioreactor by center to
Under again surrounding inwall along bioreactor main body be circulated up, it is achieved being sufficiently mixed of anaerobic reaction material.
For solving above-mentioned second technical problem, this utility model employing following technical proposals:
A kind of bioreactor including above-mentioned integrated apparatus, described bioreactor includes a reactor with inner chamber
Main body, described in be buffered into air chamber and be arranged on above described reactor body, the mixing part of described Stirring axle is positioned at described
In the inner chamber of reactor body；
By the air inlet arranged in Stirring axle between inner chamber and the described inner chamber being buffered into air chamber of described reactor body
Chamber is arranged.By this setting make the gas being buffered in air chamber can only from the axial wall of Stirring axle set
Vent cap enters in the inner chamber of reactor body.
Further, it is additionally provided with gas circulating tube between inner chamber and the described inner chamber being buffered into air chamber of described reactor body
Road.This gas circulation line can adapt to different air inlet compositions, and is buffered into described by the inner chamber of reactor body
Circulation between the inner chamber of air chamber realizes efficiently converting thoroughly.
Further, the oblique leaf disc turbine stirrer being positioned in the inner chamber of described reactor body, its a diameter of reactor
The 20%～50% of inner major diameter.Play the purpose so arranged to be, it is simple to the material in bioreactor is by center the most again
Surrounding inwall along bioreactor main body is circulated up.
Further, in the described inner chamber being buffered into air chamber, described Stirring axle is provided with oiliness graphite packing case；
The effect of the oiliness graphite packing case arranged at this is, the inner chamber being buffered into air chamber described in opposing seal packing is empty with outside
Between, and then the opposing seal isolation inner chamber of reactor body and the inner chamber being buffered into air chamber.
Described reactor body is provided with charging aperture, discharging opening and gas outlet.Charging aperture is used for, into anaerobic reaction material, going out
Material mouth is used for the material that reaction is complete, and gas outlet is stated for output and reacted the gas after converting in the inner chamber of reactor body.
Described charging aperture is positioned at the bottom of described reactor body, and described discharging opening and gas outlet lay respectively at described reactor
The top of main body.Described charging aperture is arranged on the bottom of reactor body, it is to avoid have just enter in bioreactor main body
The direct overflow of material is gone out from discharging opening.
The height and position of the oblique leaf disc turbine stirrer being arranged in described reactor body is less than the position of described discharging opening
Put.Owing to oblique leaf disc turbine stirrer is when stirring, the most all there is material, and then when the thing in bioreactor main body
When material liquid level is exactly the height of discharging opening, it is simple to discharging opening overflow discharging.
Operation principle of the present utility model is as follows:
Material is added in entrance bioreactor main body by charging aperture, is realized the most mixed by oblique leaf disc turbine stirrer
Closing, reacted leftover materials are discharged by discharging opening；After needing synthesis gas to be processed entrance to be buffered into air chamber, by rotating
Vent cap set on the axial wall of shaft enters in the inner chamber of bioreactor main body, and synthesis gas is by microporous aeration device
Form microporous bubble and enter in bioreactor main body, disperse under the effect of Stirring axle and be fully contacted with microorganism
Reaction converts, and discharges from gas outlet, according to entrance together with the biogas that the gas of generation finally generates with bioreactor self
The difference of gas composition can be realized effective conversion of synthesis gas by gas circular treatment.
This utility model compared with prior art, has a following actively beneficial effect:
1, the integrated apparatus provided in this utility model, for H2Turn with CO biology in anaerobic biological reactor
Change process, increases the percussion to microorganism when being buffered into air chamber for reducing intake velocity fluctuation.
2, the bioreactor provided in this utility model is provided with gas circulation line, and this gas circulation line can be fitted
Answer different air inlet compositions, and by the Circulation between inner chamber and the described inner chamber being buffered into air chamber of reactor body
Realize efficiently converting thoroughly.
3, the microporous aeration device employed in this utility model adds the contact area of tiny bubble and microbial reaction,
Coordinate multilamellar oblique leaf disc turbine stirrer, it is possible to make the material in bioreactor by center the most again along biological anti-simultaneously
The surrounding inwall answering device main body is circulated up, and not only achieves being sufficiently mixed of anaerobic reaction material, also effectively increases gas
Body and microorganism catalytic time, enhance the biotransformation of gas.
4, this utility model is by the oblique leaf disc above the microporous aeration device of Stirring axle bottom and microporous aeration device
The design of turbine stirrer, make when Stirring axle starts to rotate the material in bioreactor main body in stirring area by
On be moved down into bottom after, then the inwall mobile circulation from bottom to top along reactor body inner chamber, it is achieved bioreactor
The stirring mixing of interior material, makes the synthesis gas in microporous aeration device entrance bioreactor main body along with material shifting simultaneously
Move and float up again after scattering, be no longer limited to central area in reactor body, it is achieved that good gas-liquid mass transfer effect
Really.
5, by being buffered into air chamber, the coordinating of microporous aeration device leaf disc turbine stirrer oblique with multilamellar in this utility model,
Can realize, to synthesis gas transfer of gas and the agitating function to gas-liquid mixed material, effectively having disperseed synthesis gas gas simultaneously
Body also increases response time of synthesis gas gas and microorganism, promotes system biological method methanation.
6, this utility model is in the case of reducing system structure complexity, by being passed through synthesis gas gas in bioreactor
Body, and make it effectively disperse, increase synthesis gas gas mass transfer effect in fermentation materials and the time of staying, simultaneously to being
System material mix and blend, fully to realize bioanalysis methanation.
Accompanying drawing explanation
Fig. 1 is the overall structure schematic diagram of this utility model first embodiment.
Fig. 2 is the overall structure schematic diagram of this utility model the second embodiment.
Gas and the motion mode schematic diagram of material when Fig. 3 is stirring in this utility model the second embodiment.
Detailed description of the invention
Detailed description of the invention of the present utility model is described below in conjunction with the accompanying drawings.
Embodiment 1:
As it is shown in figure 1, a kind of for gas conveying and the integrated apparatus of material stirring, described device includes Stirring
Axle 1 and for driving the motor 2 that Stirring axle 1 rotates；Described motor 2 by frame 21 be installed in described in be buffered into
Above air chamber 3, and the main shaft of this motor 2 is connected by shaft coupling with described Stirring axle 1, and described motor 2
The axis of main shaft is same axis with the axis of described Stirring axle 1.
Be provided with on described Stirring axle 1 there is air inlet 31 be buffered into air chamber 3, described in be buffered into air chamber be casing
Structure, described Stirring axle 1 can rotate by current buffer inlet plenum 3, and described Stirring axle 1 is buffered into described
Joining place between air chamber 3 is sealed by oiliness graphite packing case 6 and arranges, and this oiliness graphite packing case 6 is around described rotation
Turn shaft 1 to arrange.Being provided with two oiliness graphite packing casees 6 in the present embodiment, one is arranged on and is buffered into outside air chamber 3
End face on；One is arranged on and is buffered on bottom the inner chamber 32 of air chamber 3；At the described inner chamber 32 being buffered into air chamber 3
With under outside opposing seal isolation, the Stirring axle 1 through this oiliness graphite packing case 6 can carry out rotation freely.
Further, the mixing part 11 of described Stirring axle 1 be placed in described in be buffered into outside air chamber 3, and this Stirring
The mixing part 11 of axle 1 is provided with three layers of oblique leaf disc turbine stirrer 4, and the bottom of described Stirring axle 1 is provided with micropore
Aerator 5, is provided with vent cap 12, this ventilation on the axial wall of the described Stirring axle 1 being buffered in air chamber 3
Duct 12 connects setting by the inlet plenum arranged in Stirring axle 1 with described microporous aeration device 5.
Further, three layers of set on the mixing part 11 of described Stirring axle 1 oblique leaf disc turbine stirrer 4 are advised
Lattice are identical, and spacing between layers is identical, and the tilt angle theta phase of described oblique leaf disc turbine stirrer 4 Leaf
Together, and this tilt angle theta is 30 °～45 °, and the top of the mixing part 11 of the most described Stirring axle 1 leaves 1/5～1/4
Length oblique leaf disc turbine stirrer 4 is not installed, by above-mentioned setting so that the oblique leaf disc turbine on mixing part 11
Agitator 4 is positioned at reaction mass, and ensure that the oblique leaf disc turbine stirrer about 4 of every layer has certain material,
So when Stirring axle 1 Stirring so that the material in bioreactor is downward again along bioreactor by center
The surrounding inwall of main body is circulated up, it is achieved being sufficiently mixed of anaerobic reaction material.
Embodiment 2:
As shown in Figure 1, 2, 3, a kind of bioreactor including above-mentioned integrated apparatus, described bioreactor includes
One reactor body 7 with inner chamber 71, described reactor body 7 is provided with charging aperture 72, discharging opening 73 and gives vent to anger
Mouth 74, wherein said charging aperture 72 is positioned at the bottom of described reactor body 7, described discharging opening 73 and gas outlet 74
Lay respectively at the top of described reactor body 7；The described air chamber 3 that is buffered into is arranged on above described reactor body 7,
The mixing part 11 of described Stirring axle 1 is positioned in the inner chamber 71 of described reactor body 7.
By Stirring axle 1 between inner chamber 71 and the described inner chamber 32 being buffered into air chamber 3 of described reactor body 7
The inlet plenum connection of interior setting is arranged.Make the gas being buffered in air chamber 3 can only be from Stirring axle by this setting
Vent cap 12 set on the axial wall of 1 enters in the inner chamber 71 of reactor body 7.
Further, in the described inner chamber 32 being buffered into air chamber 3, described Stirring axle 1 is provided with oiliness graphite
Stuffing box 6.The effect of the oiliness graphite packing case 6 set by this is, is buffered into air chamber 3 described in opposing seal packing
Inner chamber 32 and space outerpace, and then opposing seal isolation reactor body 7 inner chamber 71 be buffered in air chamber 3
Chamber 32.
Further, it is provided with gas between inner chamber 71 and the described inner chamber 32 being buffered into air chamber 3 of described reactor body 7
Body circulation line 8, in the present embodiment, gas circulation line 8 connects setting with the air inlet 31 being buffered on air chamber 3,
This gas circulation line 8 can adapt to different air inlet compositions, and passes through the inner chamber 71 of reactor body 7 and described buffering
Circulation between the inner chamber 32 of inlet plenum 3 realizes efficiently converting thoroughly.
Further, the height and position of the oblique leaf disc turbine stirrer 4 being arranged in described reactor body 7 is less than institute
State the position of discharging opening 73, and the oblique leaf disc turbine stirrer 4 being positioned in the inner chamber 71 of described reactor body 7,
The 20%～50% of its a diameter of reactor body 7 internal diameter.Play the purpose so arranged to be, it is simple in bioreactor
Material by center downwards the most again surrounding inwall along bioreactor main body 7 be circulated up.
This utility model specific works flow process is as follows:
Synthesis gas enters from air inlet 31 after being buffered into air chamber 3, by Stirring axle 1 axial wall being buffered in air chamber 3
Vent cap 12 enter in Stirring axle 1, and formed micropore by the microporous aeration device 5 of Stirring axle 1 bottom
Bubble enters in the inner chamber 71 of reactor body 7, and under the effect of oblique leaf disc turbine stirrer 4, synthesis gas is long-time
Stop and be evenly distributed in the inner chamber 71 of reactor body 7, and under microbial action, realize the methanation of synthesis gas,
Generate the final biogas based on methane and carbon dioxide to leave from gas outlet 74.
Gas circulation line 8 in the bioreactor that this utility model provides can be according to the composition of final biogas
Different and treatment effect requirement switchs, when (such as including H containing more impurity in final biogas2And CO) time, open
Opening gas circulation line 8, part aerogenesis is circulated entrance reactor body by gas circulation line 8 by air inlet 31
In 7, again there is methanation, it is achieved the further lifting of conversion ratio.
In maintenance bioreactor main body 7, the material of microflora includes (e.g., the Sewage Plant dirt of organic waste mixed liquor
Sewage sludge, kitchen, rubbish, organic wastewater, fowl and animal excrement) and organic nutrient solution for cultivating, material is entered reaction by charging aperture 72
In the inner chamber 71 of device main body 7, formed under the effect of oblique leaf disc turbine stirrer 4 by center downward tailing edge inner chamber 71
Surrounding medial wall shuttling movement upwards, the most not only makes microorganism and material be sufficiently mixed reaction thus maintains department of microbiology
System activity, also makes microorganism and synthesis gas be sufficiently mixed and extend the methanation reaction time, and the complete material of end reaction is by going out
Material mouth 73 leaves.
The word in the description orientation employed in Ben Wen " on ", D score, "left", "right" etc. be for explanation
Convenience based on the orientation shown in drawing in accompanying drawing for, in actual device, these orientation are likely to be due to putting of device
Mode and different.
In sum, embodiment described in the utility model only provides a kind of optimal embodiment, of the present utility model
Technology contents and technical characterstic have revealed that as above, but one skilled in the art scholar is still potentially based on this utility model and is taken off
The content shown and make the various replacement without departing substantially from this utility model creation spirit and modification；Therefore, protection of the present utility model
Scope is not limited to the technology contents disclosed in embodiment, thus all according to shape of the present utility model, structure and principle done etc.
Effect change, is encompassed by protection domain of the present utility model.
Claims (10)
1. one kind carries and the integrated apparatus of material stirring for gas, it is characterised in that: described device includes Stirring axle and for the motor driving Stirring axle to rotate；
Being provided with the air chamber that is buffered into air inlet on described Stirring axle, described Stirring axle can rotate by current buffer inlet plenum, and described Stirring axle and the described joining place being buffered between air chamber seal and arrange；
The mixing part of described Stirring axle is buffered into outside air chamber described in being placed in, and the mixing part of this Stirring axle is provided with oblique leaf disc turbine stirrer, and the bottom of described Stirring axle is provided with microporous aeration device；
Being provided with vent cap on the axial wall of the described Stirring axle being buffered in air chamber, this vent cap connects setting by the inlet plenum arranged in Stirring axle with described microporous aeration device.
The most according to claim 1 a kind of for gas conveying and the integrated apparatus of material stirring, it is characterised in that being buffered into air chamber described in: is body structure.
The most according to claim 1 a kind of for gas conveying and the integrated apparatus of material stirring, it is characterized in that: described Stirring axle and the described joining place being buffered between air chamber are sealed by oiliness graphite packing case and arrange, and this oiliness graphite packing case is arranged around described Stirring axle.
The most according to claim 1 a kind of for gas conveying and the integrated apparatus of material stirring, it is characterized in that: described motor by frame be installed in described in be buffered into above air chamber, and the main shaft of this motor is connected with described Stirring axle, and the axis of the axis of the main shaft of described motor and described Stirring axle is same axis.
It is the most according to claim 1 a kind of for gas conveying and the integrated apparatus of material stirring, it is characterised in that: the tilt angle theta of described oblique leaf disc turbine stirrer Leaf is identical, and this tilt angle theta is 30 °～45 °.
The most according to claim 1 a kind of for gas conveying and the integrated apparatus of material stirring, it is characterized in that: the mixing part of described Stirring axle is provided with at least three layers of oblique leaf disc turbine stirrer, three layers of oblique leaf disc turbine stirrer specification are identical, and spacing between layers is identical；The top of the mixing part of described Stirring axle is left the length of 1/5～1/4 and is not installed oblique leaf disc turbine stirrer.
7. one kind includes the bioreactor of integrated apparatus as described in one of claim 1 to 6, it is characterized in that: described bioreactor includes a reactor body with inner chamber, the described air chamber that is buffered into is arranged on above described reactor body, and the mixing part of described Stirring axle is positioned in the inner chamber of described reactor body；
Between the inner chamber of described reactor body with the described inner chamber being buffered into air chamber, the inlet plenum by arranging in Stirring axle connects setting.
A kind of bioreactor the most according to claim 7, it is characterised in that: it is additionally provided with gas circulation line between inner chamber and the described inner chamber being buffered into air chamber of described reactor body.
A kind of bioreactor the most according to claim 7, it is characterised in that: the oblique leaf disc turbine stirrer being positioned in the inner chamber of described reactor body, the 20%～50% of its a diameter of reactor body internal diameter.
A kind of bioreactor the most according to claim 7, it is characterised in that: in the described inner chamber being buffered into air chamber, described Stirring axle is provided with oiliness graphite packing case；Described reactor body is provided with charging aperture, discharging opening and gas outlet, and described charging aperture is positioned at the bottom of described reactor body, and described discharging opening and gas outlet lay respectively at the top of described reactor body；The height and position of the oblique leaf disc turbine stirrer being arranged in described reactor body is less than the position of described discharging opening.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620237901.7U CN205556651U (en) | 2016-03-25 | 2016-03-25 | Integration device and including being somebody's turn to do device for gas delivery and material mixing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620237901.7U CN205556651U (en) | 2016-03-25 | 2016-03-25 | Integration device and including being somebody's turn to do device for gas delivery and material mixing |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205556651U true CN205556651U (en) | 2016-09-07 |
Family
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620237901.7U Expired - Fee Related CN205556651U (en) | 2016-03-25 | 2016-03-25 | Integration device and including being somebody's turn to do device for gas delivery and material mixing |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105695309A (en) * | 2016-03-25 | 2016-06-22 | 北京化工大学 | Integrated device for conveying gas and stirring materials, and bioreactor comprising same |
| CN108675491A (en) * | 2018-05-18 | 2018-10-19 | 南通劲凌智能科技有限公司 | A kind of dosing aerating system for water body purification |
| CN112410576A (en) * | 2020-10-21 | 2021-02-26 | 重庆大学 | Device and system for dissolving platinum-rhodium alloy in waste platinum-rhodium thermocouple |
| CN113740240A (en) * | 2021-09-09 | 2021-12-03 | 中国石油化工股份有限公司 | Corrosion inhibition performance testing device and method of corrosion inhibitor and application |
-
2016
- 2016-03-25 CN CN201620237901.7U patent/CN205556651U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105695309A (en) * | 2016-03-25 | 2016-06-22 | 北京化工大学 | Integrated device for conveying gas and stirring materials, and bioreactor comprising same |
| CN108675491A (en) * | 2018-05-18 | 2018-10-19 | 南通劲凌智能科技有限公司 | A kind of dosing aerating system for water body purification |
| CN112410576A (en) * | 2020-10-21 | 2021-02-26 | 重庆大学 | Device and system for dissolving platinum-rhodium alloy in waste platinum-rhodium thermocouple |
| CN113740240A (en) * | 2021-09-09 | 2021-12-03 | 中国石油化工股份有限公司 | Corrosion inhibition performance testing device and method of corrosion inhibitor and application |
| CN113740240B (en) * | 2021-09-09 | 2023-11-14 | 中国石油化工股份有限公司 | Corrosion inhibition performance testing device and method for corrosion inhibitor and application |
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