CN206778353U - Biology enzyme Formaldehyde decomposition liquid continuous process system - Google Patents
Biology enzyme Formaldehyde decomposition liquid continuous process system Download PDFInfo
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- CN206778353U CN206778353U CN201720672515.5U CN201720672515U CN206778353U CN 206778353 U CN206778353 U CN 206778353U CN 201720672515 U CN201720672515 U CN 201720672515U CN 206778353 U CN206778353 U CN 206778353U
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- stirred tank
- discharge nozzle
- decomposition liquid
- formaldehyde decomposition
- valve
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
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- Apparatus Associated With Microorganisms And Enzymes (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
It the utility model is related to a kind of biology enzyme Formaldehyde decomposition liquid continuous process system,Including multiple head tanks,Connected between head tank by pipeline,The discharging opening of head tank is connected by pipeline with stirred tank,Mateiral pump is provided with the pipeline connected before adjacent feed tank and on pipeline that head tank connects with stirred tank,The discharging opening of mateiral pump is provided with magnetic valve,The stirred tank is provided with discharge nozzle,Valve is provided with discharge nozzle,Valve is connected with drive mechanism,Drive mechanism driving valve realizes the unlatching and closing to discharge nozzle,By in above-mentioned raw material input head tank,Start mateiral pump,So as to which raw material is endlessly imported in stirred tank,Implement the full and uniform stirring to material using the agitating unit in stirred tank,After material stirring is uniform,Start drive mechanism,So that valve is opened,So as to facilitate the Formaldehyde decomposition liquid of finished product to be exported from discharge nozzle,The system can realize the continuous production of biology enzyme Formaldehyde decomposition liquid,Improve production efficiency.
Description
Technical field
It the utility model is related to chemical products production technical field, and in particular to a kind of biology enzyme Formaldehyde decomposition liquid is continuously given birth to
Production system.
Background technology
With the improvement of living standards, people are increasingly paid close attention to health problem, the particularly gas emission problem of furniture,
Substantial amounts of formaldehyde be present in the furniture or paint newly bought, formaldehyde emission comes out, and spreads in room air, to the body of people
Body injury is extremely serious, therefore newly-decorated house is, it is necessary to carry out except formaldehyde operates, in the prior art, to eliminate in air
Formaldehyde, typically handled using biology enzyme Formaldehyde decomposition liquid, above-mentioned biology enzyme Formaldehyde decomposition liquid energy it is enough by Formaldehyde decomposition into
Other harmless components, it can so reduce injury of the formaldehyde to body.
Above-mentioned Formaldehyde decomposition liquid includes Multiple components, in actual production, it is necessary to which above-mentioned Multiple components input is stirred
Mix in device, start agitating device to realize abundant, uniform stirring to above-mentioned Multiple components, you can Formaldehyde decomposition liquid is formed,
Because above-mentioned each component is in production, the combination of each component is realized essentially by artificial mode, therefore formaldehyde can not be accomplished
The continuous production of decomposed solution, cause yield relatively low, the large-scale market demand can not be adapted to.
Utility model content
The purpose of this utility model is：A kind of biology enzyme Formaldehyde decomposition liquid continuous process system is provided, can be realized to upper
The continuous production of biology enzyme Formaldehyde decomposition liquid is stated, improves production efficiency.
To achieve the above object, the technical solution adopted in the utility model is：
Biology enzyme Formaldehyde decomposition liquid continuous process system, including multiple head tanks, pass through pipeline string between the head tank
Connection, the discharging opening of head tank connect by pipeline with stirred tank, before adjacent feed tank on the pipeline of connection and head tank and
Mateiral pump is provided with the pipeline of stirred tank connection, the discharging opening of the mateiral pump is provided with magnetic valve, and the stirred tank is set
Discharge nozzle is equipped with, valve is provided with the discharge nozzle, the valve is connected with drive mechanism, and drive mechanism driving valve is realized
Unlatching and closing to discharge nozzle.
Following characteristics also be present in the utility model：
Mix tube is provided with the stirred tank, the upper end of the mix tube and the upper end of stirred tank connect, mixing
Batch mixing bar is provided with expects pipe, flight, length direction cloth of the flight along batch mixing bar are provided with the batch mixing bar
Put, the upper end of batch mixing bar is connected with actuating unit, and actuating unit driving batch mixing bar rotates forward and reversion, the upper end of the mix tube
Tube wall is provided with the first opening, and the lower end tube wall of the mix tube is provided with the second opening.
The upper end of the mix tube forms detachable connection, the connecting tube upper end and stirred tank upper end with connecting tube
It is connected, the batch mixing club body is connected through connecting tube and with the rotating shaft of the motor of stirred tank upper end.
The rotating shaft of the motor is additionally provided with puddle support, and stirring sheet, the stirring sheet are provided with the puddle support
Plate face it is vertical and multiple along the length direction arranged for interval of puddle support.
The bottom of the stirred tank is in spherical, and bottom is provided with material spreading cone, and the discharge nozzle is arranged on the kettle of stirred tank
On the outer wall sphere of bottom.
The inner tubal wall of the discharge nozzle is provided with step surface, and the valve is plate-like and plate face edge is provided with sealing ring,
The sealing ring is formed against with the inner tubal wall table top of discharge nozzle or separates cooperation, and discharging is offered on the pipe shaft of the discharge nozzle
Mouthful.
The drive mechanism is cylinder, and the cylinder body of the cylinder is fixed on the mouth of pipe of discharge nozzle and tailpiece of the piston rod connects with valve
Connect.
The lower end of the puddle support is provided with material scraping plate, and the material scraping plate is rubber slab and bottom plate edge and stirred tank
Bottom against.
Compared with prior art, the technique effect that the utility model possesses is：By in above-mentioned raw material input head tank, open
Dynamic mateiral pump, so as to which raw material is endlessly imported in stirred tank, implemented using the agitating unit in stirred tank to material
Full and uniform stirring, after material stirring is uniform, start drive mechanism so that valve is opened, so as to facilitate the formaldehyde of finished product
Decomposed solution exports from discharge nozzle, and the system can realize the continuous production of biology enzyme Formaldehyde decomposition liquid, improves production efficiency.
Brief description of the drawings
Fig. 1 is the structural representation of biology enzyme Formaldehyde decomposition liquid continuous process system；
Fig. 2 is the stirred tank cross section view in biology enzyme Formaldehyde decomposition liquid continuous process system；
Fig. 3 and Fig. 4 is that the stirred tank discharge nozzle in biology enzyme Formaldehyde decomposition liquid continuous process system is in closing and opened
Two states schematic diagram.
Embodiment
With reference to Fig. 1 to Fig. 4, the utility model is further described：
Biology enzyme Formaldehyde decomposition liquid continuous process system, including multiple head tanks 10, pass through pipe between the head tank 10
Road is connected, and the discharging opening of head tank 10 connected by pipeline with stirred tank 40, before adjacent feed tank 10 on the pipeline of connection with
And mateiral pump 20 is provided with the pipeline that is connected with stirred tank 40 of head tank 10, the discharging opening of the mateiral pump 20 is provided with electricity
Magnet valve 30, the stirred tank 40 are provided with discharge nozzle 41, and valve 42, the valve 42 and driving are provided with the discharge nozzle 41
Mechanism connects, and drive mechanism driving valve 42 realizes the unlatching and closing to discharge nozzle 41；
With reference to shown in Fig. 1, enter in head tank 10, start mateiral pump 20, so as to which raw material is endlessly imported into stirred tank
In 40, the regulation to flow can be realized using magnetic valve 30, it is ensured that the throughput rate of Formaldehyde decomposition liquid, using in stirred tank 40
Agitating unit implement full and uniform stirring to material, after material stirring is uniform, start drive mechanism so that valve 42
Open, so as to facilitate the Formaldehyde decomposition liquid of finished product to be exported from discharge nozzle 41, the system can realize biology enzyme Formaldehyde decomposition liquid
Continuous production, improve production efficiency.
As preferred scheme of the present utility model, with reference to shown in Fig. 2, mix tube 43, the mix tube are inside provided with
43 upper end is connected with the upper end of stirred tank 40, and batch mixing bar 44 is provided with mix tube 43, is provided with the batch mixing bar 44
Flight 441, length direction arrangement of the flight 441 along batch mixing bar 44, upper end and the actuating unit of batch mixing bar 44 connect
Connecing, actuating unit driving batch mixing bar 44 is rotated forward and inverted, and the upper end tube wall of the mix tube 43 is provided with the first opening 431,
The lower end tube wall of the mix tube 43 is provided with the second opening 432；
During above-mentioned actuating unit driving batch mixing bar 44 rotates, material to be mixed by mix tube 43 upper end
Or lower ending opening enters, and under the turning effort of flight 441 so that above-mentioned each component is sufficiently stirred, from
And improving the reaction sufficient degree of above-mentioned material, it is ensured that the quality of Formaldehyde decomposition liquid, mixed material are discharged from above-mentioned opening,
It is again introduced into stirred tank 40.
Further, the upper end of the mix tube 43 forms detachable connection, the connecting tube with connecting tube 433
433 upper ends are connected with the upper end of stirred tank 40, the shaft of batch mixing bar 44 through connecting tube 433 and with the driving of the upper end of stirred tank 40
The rotating shaft connection of motor 45；
Above-mentioned motor 45 starts, and is located at rotation in connecting tube 433 so as to interlock batch mixing bar 44.
To realize being sufficiently stirred to the material in stirred tank 40, the rotating shaft of the motor 45 is additionally provided with puddle support
46, it is provided with stirring sheet 461 on the puddle support 46, the plate face of the stirring sheet 461 is vertical and along the length of puddle support 46
Direction arranged for interval is multiple；
Above-mentioned puddle support 46 rotates, and stirring sheet 461 causes the component in stirred tank 40 sufficiently to rotate, Jin Ershi
Now being sufficiently mixed to stirred tank 40.
Mixed material to ensure in stirred tank 40 is discharged from discharge nozzle 41 completely, and the bottom of the stirred tank 40 is in
It is spherical, and bottom is provided with material spreading cone 47, the discharge nozzle 41 is arranged on the bottom outer wall sphere of stirred tank 40.
With reference to shown in Fig. 3 and Fig. 4, the plugging effect of discharge nozzle 41, the inner tubal wall of the discharge nozzle 41 is provided with step surface,
The valve 42 is plate-like and plate face edge is provided with sealing ring 421, the inner tubal wall table top structure of the sealing ring and discharge nozzle 41
Into against or separation coordinate, offer discharging opening 411 on the pipe shaft of the discharge nozzle 41；
Above-mentioned valve 42 moved along discharge nozzle 41 and away from discharging opening 411 when, the material in stirred tank 40
It can be discharged out of this discharging opening 411.
The drive mechanism is cylinder 412, and the cylinder body of the cylinder 412 is fixed on the mouth of pipe and tailpiece of the piston rod of discharge nozzle 41
It is connected with valve 42.
To avoid material from being deposited on the bottom of stirred tank 40, the lower end of the puddle support 46 is provided with material scraping plate 462, described
Material scraping plate 462 be rubber slab and bottom plate edge with the bottom of stirred tank 40 against；
During above-mentioned puddle support 46 rotates, material scraping plate 462 can be by the material of the bottom of stirred tank 40 all from going out
Expects pipe 411 is discharged.
It is obvious to a person skilled in the art that the utility model is not limited to the details of above-mentioned one exemplary embodiment, and
And in the case of without departing substantially from spirit or essential attributes of the present utility model, it can realize that this practicality is new in other specific forms
Type.Therefore, no matter from the point of view of which point, embodiment all should be regarded as exemplary, and is nonrestrictive, this practicality is new
The scope of type limits by appended claims rather than described above, it is intended that the equivalency fallen in claim is contained
All changes in justice and scope are included in the utility model.Any reference in claim should not be considered as limitation
Involved claim.
Moreover, it will be appreciated that although the present specification is described in terms of embodiments, not each embodiment is only wrapped
Containing an independent technical scheme, this narrating mode of specification is only that those skilled in the art should for clarity
Using specification as an entirety, the technical solutions in the various embodiments may also be suitably combined, forms those skilled in the art
It is appreciated that other embodiment.
Claims (8)
1. biology enzyme Formaldehyde decomposition liquid continuous process system, it is characterised in that：Including multiple head tanks (10), the head tank
(10) connected between by pipeline, the discharging opening of head tank (10) is connected by pipeline with stirred tank (40), adjacent feed tank
(10) mateiral pump (20) is provided with the pipeline of connection and on the pipeline that is connected with stirred tank (40) of head tank (10) before,
The discharging opening of the mateiral pump (20) is provided with magnetic valve (30), and the stirred tank (40) is provided with discharge nozzle (41), it is described go out
Valve (42) is provided with expects pipe (41), the valve (42) is connected with drive mechanism, and drive mechanism driving valve (42) is realized
Unlatching and closing to discharge nozzle (41).
2. biology enzyme Formaldehyde decomposition liquid continuous process system according to claim 1, it is characterised in that：The stirred tank
(40) mix tube (43) is provided with, the upper end of the mix tube (43) is connected with the upper end of stirred tank (40), compound
Batch mixing bar (44) is provided with pipe (43), flight (441), flight (441) edge are provided with the batch mixing bar (44)
The length direction arrangement of batch mixing bar (44), the upper end of batch mixing bar (44) is connected with actuating unit, actuating unit driving batch mixing bar
(44) rotate forward and invert, the upper end tube wall of the mix tube (43) is provided with the first opening (431), the mix tube (43)
Lower end tube wall be provided with the second opening (432).
3. biology enzyme Formaldehyde decomposition liquid continuous process system according to claim 2, it is characterised in that：The mix tube
(43) upper end forms detachable connection with connecting tube (433), and connecting tube (433) upper end and stirred tank (40) upper end are solid
Even, batch mixing bar (44) shaft connects through connecting tube (433) and with the rotating shaft of the motor (45) of stirred tank (40) upper end
Connect.
4. biology enzyme Formaldehyde decomposition liquid continuous process system according to claim 3, it is characterised in that：The motor
(45) rotating shaft is additionally provided with puddle support (46), and stirring sheet (461), the stirring sheet are provided with the puddle support (46)
(461) plate face is vertical and multiple along the length direction arranged for interval of puddle support (46).
5. biology enzyme Formaldehyde decomposition liquid continuous process system according to claim 4, it is characterised in that：The stirred tank
(40) bottom is in spherical, and bottom is provided with material spreading cone (47), and the discharge nozzle (41) is arranged on the bottom of stirred tank (40)
On outer wall sphere.
6. biology enzyme Formaldehyde decomposition liquid continuous process system according to claim 5, it is characterised in that：The discharge nozzle
(41) inner tubal wall is provided with step surface, and the valve (42) is plate-like and plate face edge is provided with sealing ring (421), described close
Seal forms against with the inner tubal wall table top of discharge nozzle (41) or separates cooperation, is offered out on the pipe shaft of the discharge nozzle (41)
Material mouth (411).
7. biology enzyme Formaldehyde decomposition liquid continuous process system according to claim 6, it is characterised in that：The drive mechanism
For cylinder (412), the cylinder body of the cylinder (412) is fixed on the mouth of pipe of discharge nozzle (41) and tailpiece of the piston rod connects with valve (42)
Connect.
8. biology enzyme Formaldehyde decomposition liquid continuous process system according to claim 7, it is characterised in that：The puddle support
(46) lower end is provided with material scraping plate (462), and the material scraping plate (462) is rubber slab and bottom plate edge and stirred tank (40)
Bottom against.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720672515.5U CN206778353U (en) | 2017-06-09 | 2017-06-09 | Biology enzyme Formaldehyde decomposition liquid continuous process system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720672515.5U CN206778353U (en) | 2017-06-09 | 2017-06-09 | Biology enzyme Formaldehyde decomposition liquid continuous process system |
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| Publication Number | Publication Date |
|---|---|
| CN206778353U true CN206778353U (en) | 2017-12-22 |
Family
ID=60716959
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720672515.5U Active CN206778353U (en) | 2017-06-09 | 2017-06-09 | Biology enzyme Formaldehyde decomposition liquid continuous process system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206778353U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109095963A (en) * | 2018-10-29 | 2018-12-28 | 天津绿之本生物科技有限公司 | A kind of novel organic fertilizer steam fermentor |
-
2017
- 2017-06-09 CN CN201720672515.5U patent/CN206778353U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109095963A (en) * | 2018-10-29 | 2018-12-28 | 天津绿之本生物科技有限公司 | A kind of novel organic fertilizer steam fermentor |
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