CN208465883U - A kind of dustless automatic charging reactor tank - Google Patents
A kind of dustless automatic charging reactor tank Download PDFInfo
- Publication number
- CN208465883U CN208465883U CN201820559043.7U CN201820559043U CN208465883U CN 208465883 U CN208465883 U CN 208465883U CN 201820559043 U CN201820559043 U CN 201820559043U CN 208465883 U CN208465883 U CN 208465883U
- Authority
- CN
- China
- Prior art keywords
- reactor tank
- filter
- evacuator
- automatic charging
- intake pipe
- 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
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 239000002994 raw material Substances 0.000 abstract description 28
- 239000002245 particle Substances 0.000 abstract description 19
- 229910004682 ON-OFF Inorganic materials 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- 238000007906 compression Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 235000021050 feed intake Nutrition 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 229920002472 Starch Polymers 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 235000019362 perlite Nutrition 0.000 description 1
- 239000010451 perlite Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
Abstract
The utility model discloses a kind of dustless automatic charging reactor tank, includes reactor tank, vacuum intake pipe, filter；Evacuator and reactor tank are respectively communicated at the top and bottom of filter, filter is equipped with filter core, the upper end of all filter cores, which is open and is passed through compressed air, to be in charge of, compressed air, which is in charge of, connects compressed gas source by pneumatic manifold, solenoid valve, solenoid valve and evacuator is provided on pneumatic manifold to control by the time relay；Compared with prior art, the little particle raw material of lower can be drawn into the reactor tank of eminence by the utility model, eliminated the step that little particle raw material is transported on high operation platform by worker, reduced the labor intensity of worker, reduce cost of labor；Secondly, being not in the case where grit is flown upward when little particle raw material is drawn into reactor tank, the grit pollution in workshop can be greatly reduced, ensure that the clean environment in workshop, reduce the harm to worker, guarantee the health of worker.
Description
Technical field
The utility model belongs to bioengineering equipment technical field, particularly, is related to a kind of dustless automatic charging reactor tank.
Background technique
In the production process of biogenetic products, it is often necessary to various raw materials are put into reactor tank, wherein having had no lack of example
Such as starch, the little particles raw material such as perlite.These little particle raw materials are typically all to use manually to feed intake to reactor tank.Manually
The process to feed intake are as follows: these little particle raw materials are first transported on high operation platform by worker, then open the top cover of reactor tank,
Then by these little particle raw materials by being put into reactor tank after metering.But due to investment be little particle raw material,
It can be flown upward there are many grit during toppling over raw material, the environment in workshop can not only be polluted, be unfavorable for workshop
Running, but also certain harm can be generated to worker, influence the health of worker；Secondly, reactor tank is typically all installation settings
In relatively high elevated platform, worker needs two people cooperation raw material could be brought up to high operation when carrying raw material
Platform, labor intensity of workers is higher, and cost of labor is higher.
Utility model content
For overcome the deficiencies in the prior art, the utility model provides a kind of reduction labor intensity of workers, reduce manually at
This, keeps the clean dustless automatic charging reactor tank of workshop condition.
The technical scheme adopted by the utility model to solve the technical problem is as follows:
A kind of dustless automatic charging reactor tank includes reactor tank, the vacuum intake pipe being connected to inside the reactor tank, sets
Set the filter on the reactor tank top；Evacuator and the reaction are respectively communicated at the top and bottom of the filter
Tank, the inside of the filter are equipped with multiple hollow filter cores, and the upper end of all filter cores is open and is passed through compression sky
Gas is in charge of, and all compressed airs, which are in charge of, is communicated with compressed gas source by pneumatic manifold, on the pneumatic manifold
It is provided with solenoid valve, the solenoid valve and the evacuator to control by relay at the same time, the vacuum intake pipe
On be provided with switch valve, the top of the reactor tank is additionally provided with the sprinkler head at connection water source.
As an improvement of the above scheme, the top of the filter is connected to the evacuator by vacuumizing mouth, described
It vacuumizes and is provided with operated pneumatic valve on mouth, the operated pneumatic valve connects the pneumatic manifold.
As a further improvement of the foregoing solution, there are two the switch valves, one of them described switch valve is arranged in institute
The discharge end of vacuum intake pipe is stated, another is positioned close to the position of the feeding end of the vacuum intake pipe.
Further, the vacuum intake pipe is mounted on the top of the reactor tank by clamp connection.
Further, the reactor tank is equipped with vacuum meter.
The utility model has the beneficial effects that compared with prior art, the utility model can be by the little particle raw material of lower
It is drawn into the reactor tank of eminence, realizes the function of automatic charging, eliminate worker for little particle raw material and be transported to high-order behaviour
Make the step on platform, reduces the labor intensity of worker, reduce cost of labor；Secondly, being drawn into instead by little particle raw material
Be not in the case where grit is flown upward when answering tank, the grit pollution in workshop can be greatly reduced, ensure that workshop
Clean environment reduces the harm to worker, guarantees the health of worker.
Detailed description of the invention
The present invention will be further described with reference to the accompanying drawings and examples.
Fig. 1 is the overall structure diagram of the utility model；
Fig. 2 is the enlarged diagram in Fig. 1 at A.
Specific embodiment
Referring to Fig.1, Fig. 2, a kind of dustless automatic charging reactor tank include reactor tank 1, are connected to inside the reactor tank 1
Vacuum intake pipe 2, the filter 3 on 1 top of reactor tank is set；The top and bottom of the filter 3 are respectively communicated with
The inside of evacuator 4 and the reactor tank 1, the filter 3 is equipped with multiple hollow filter cores 31, all filter cores 31
Upper end, which is open and is passed through compressed air, is in charge of 51, and the compressed air is in charge of 51 and is connected with pressure by pneumatic manifold 53
Contracting gas source 5, be provided on the pneumatic manifold 53 solenoid valve 52, the solenoid valve 52 and the evacuator 4 pass through it is same
One time relay 6 controls, and is provided with switch valve 21 on the vacuum intake pipe 2, the top of the reactor tank 1 is additionally provided with
Connect the sprinkler head 7 at water source.
The reactor tank 1 is sealing, can be with vacuum-resistant, and the bottom of the filter 3 is connected to the reactor tank 1, described
Evacuator 4 is that the reactor tank 1 vacuumizes, and provides negative pressure；The feeding end of the vacuum intake pipe 2 is for being inserted into little particle original
In material tube or the raw material packaging of material, then when the vacuum degree of the reactor tank 1 reaches certain value, opened described in opening
Valve 21 is closed, the little particle raw material of lower can be drawn into the reactor tank 1 of eminence, realize the function of automatic charging
Can, the step that little particle raw material is transported on high operation platform by worker is eliminated, the labor intensity of worker is reduced, reduces
Cost of labor；Secondly, the reactor tank 1 and the vacuum intake pipe 2 are all sealings, it is described little particle raw material to be drawn into
Be not in the case where grit is flown upward when reactor tank 1, thus it is possible to which the grit pollution in workshop is greatly reduced, guarantee
The clean environment in workshop, reduces the harm to worker, guarantees the health of worker.
The filter core 31 is used for the grit of filter small particles raw material, only allows air by the filter core 31, prevents small
Grain raw material enters the filter 3 and the evacuator 4, guarantees the normal operation of the evacuator 4.The compressed air
It is in charge of 51 for projecting compressed air, blowback is carried out to the filter core 31, by the grit of the little particle raw material on the filter core 31
It blows back in reactor tank 1, the grit prevented on the filter core 31 is excessive, causes the load of the filter core 31 excessive, the filter
The case where core 31 damages, and also assure the unimpeded of evacuated path, guarantee the normal operation of the evacuator 4.
The time relay 6 is used to control the switch of the evacuator 4 and the on-off of the solenoid valve 52.Just start
When, the time relay 6 opens the evacuator 4, and closes the solenoid valve 52, and the evacuator 4 is right
The reactor tank 1 is vacuumized, and negative pressure is provided, and the solenoid valve 52 does not allow compressed air to enter institute from the compressed gas source 5
It states compressed air and is in charge of 51, stop the air blowing that the compressed air is in charge of 51；When having crossed on the time relay 6 set
Between after, the time relay 6 closes the evacuator 4, opens the solenoid valve 52, the compressed air is allowed to be in charge of 51
Blowback is carried out to the filter core 31.Then, it has crossed after the time set on the time relay 6, the time relay
Device 6 opens the evacuator 4, and closes the solenoid valve 52, carries out vacuuming action.Above-mentioned steps are recycled, it can
The checker for realizing the evacuated state and blowback state in the filter 3, guarantees the normal fortune of the evacuator 4
Make.The water that the sprinkler head 7 is used to spray shower shape can open the spray when little particle raw material, which feeds intake, to be finished
First 7 water spray is spilt, the raw material rapid subsidence floated in tank is gone down, dust from flying comes out when avoiding can opening.
Preferably, the installation of the vacuum intake pipe 2 for convenience, the vacuum intake pipe 2 are installed by clamp connection
On the top of the reactor tank 1.
Referring to Fig.1, it is preferable that there are two the switch valves 21, one of them described switch valve 21 is arranged in the vacuum
The discharge end of suction tube 2, another is positioned close to the position of the feeding end of the vacuum intake pipe 2.By being opened described in two
The on-off that valve 21 controls the vacuum intake pipe 2 is closed, facilitates worker and is controlled in time into the more of the raw material of the reactor tank 1
It is few.By the raw material of worker on the ground or when 1 side of reactor tank, the vacuum intake pipe 2 can be controlled
On-off facilitates the operation of worker.
Referring to Fig.1, Fig. 2, it is preferable that the top of the filter 3 connects the evacuator 4 by vacuumizing mouth 32,
Described vacuumize is provided with operated pneumatic valve 33 on mouth 32, the operated pneumatic valve 33 connects the pneumatic manifold 53.The gas
Movable valve 33 is controlled by PLC control unit, and the PLC control unit connects the time relay 6, when the time relay
Device 6 starts the solenoid valve 52, and when allowing the compressed gas source 5 to be connected to the compressed air to be in charge of 51, the PLC control unit is received
To the signal of the time relay 6, then start the operated pneumatic valve 33, the mouth 32 that vacuumizes is closed, does not allow compression empty
Gas, which enters, to be run out of, therefore compressed air can be allowed quickly to carry out blowback to the filter core 31, will be on the strainer of the filter core 31
Powder blow to the inside of the reactor tank 1.When the time relay 6 opens the evacuator 4 and closes the electromagnetism
When valve 52, the PLC control unit opens the operated pneumatic valve 33, vacuumizes mouth 32 described in unlatching, and the evacuator 4 is allowed to connect
The inside of the filter 3 is connect, to provide negative pressure for the reactor tank 1, is prepared to take out material.
Preferably, the vacuum degree in tank is checked for convenience, it is described in order to grasp the time for switching the switch valve 21
Reactor tank 1 is equipped with vacuum meter 11.
The workflow of the utility model are as follows: at first, the time relay 6 opens the evacuator 4, closes
The solenoid valve 52 is closed, the PLC control unit opens the operated pneumatic valve 33, and allow the reactor tank 1 is interior to improve vacuum degree, when
When vacuum degree reaches a certain level, two switch valves 21 are opened, little particle raw material is allowed to be inhaled into the reactor tank 1
It is interior；When having run the time set on the time relay 6, the time relay 6 closes the evacuator
4, the solenoid valve 52 is opened, the PLC control unit closes the operated pneumatic valve 33, the compressed air is allowed to be in charge of 51 for institute
State 31 blowback of filter core；When having run the time set on the time relay 6, the time relay 6 opens institute
Evacuator 4 is stated, the solenoid valve 52 is closed, the PLC control unit is opened the operated pneumatic valve 33, vacuumized.It follows
Ring opens and closes the evacuator 4, until the reactor tank 1, which feeds intake, to be finished.Then the sprinkler head 7 is sprayed water, and is sunk
The raw material of floating drops, and completion once feeds intake.
The above is the better embodiment of the utility model, but the utility model is not limited to above-described embodiment,
As long as its technical effect for reaching the utility model with any same or similar means, should all fall into the protection model of the utility model
Within enclosing.
Claims (5)
1. a kind of dustless automatic charging reactor tank, it is characterised in that: include reactor tank (1), connection reactor tank (1) inside
Vacuum intake pipe (2), setting the reactor tank (1) top filter (3)；The top and bottom of the filter (3)
It is respectively communicated with evacuator (4) and the reactor tank (1), the inside of the filter (3) is equipped with multiple hollow filter cores (31),
The upper end of all filter cores (31), which is open and is passed through compressed air, to be in charge of (51), and all compressed airs are in charge of (51)
It is communicated with compressed gas source (5) by pneumatic manifold (53), is provided with solenoid valve (52) on the pneumatic manifold (53),
The solenoid valve (52) and the evacuator (4) are controlled by relay (6) at the same time, the vacuum intake pipe (2)
On be provided with switch valve (21), the top of the reactor tank (1) be additionally provided with connection water source sprinkler head (7).
2. a kind of dustless automatic charging reactor tank according to claim 1, it is characterised in that: the top of the filter (3)
Portion is connected to the evacuator (4) by vacuumizing mouth (32), and described vacuumize is provided with operated pneumatic valve (33), institute on mouth (32)
It states operated pneumatic valve (33) and connects the pneumatic manifold (53).
3. a kind of dustless automatic charging reactor tank according to claim 1, it is characterised in that: the switch valve (21) has two
A, in the discharge end of the vacuum intake pipe (2), another is positioned close to described for one of them described switch valve (21) setting
The position of the feeding end of vacuum intake pipe (2).
4. a kind of dustless automatic charging reactor tank according to claim 1 to 3, it is characterised in that: the vacuum intake
Pipe (2) is mounted on the top of the reactor tank (1) by clamp connection.
5. a kind of dustless automatic charging reactor tank according to claim 1 to 3, it is characterised in that: the reactor tank
(1) vacuum meter (11) are equipped with.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820559043.7U CN208465883U (en) | 2018-04-18 | 2018-04-18 | A kind of dustless automatic charging reactor tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820559043.7U CN208465883U (en) | 2018-04-18 | 2018-04-18 | A kind of dustless automatic charging reactor tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208465883U true CN208465883U (en) | 2019-02-05 |
Family
ID=65207260
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820559043.7U Expired - Fee Related CN208465883U (en) | 2018-04-18 | 2018-04-18 | A kind of dustless automatic charging reactor tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208465883U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110205237A (en) * | 2019-06-21 | 2019-09-06 | 陈科 | A kind of self-feeding batch charging mechanism matched with enzymatic vessel |
-
2018
- 2018-04-18 CN CN201820559043.7U patent/CN208465883U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110205237A (en) * | 2019-06-21 | 2019-09-06 | 陈科 | A kind of self-feeding batch charging mechanism matched with enzymatic vessel |
| CN110205237B (en) * | 2019-06-21 | 2022-03-25 | 陈科 | With supporting autoloading of enzymolysis tank throw material mechanism |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190205 Termination date: 20210418 |
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| CF01 | Termination of patent right due to non-payment of annual fee |