CN203379642U - Impurity separation device - Google Patents
Impurity separation device Download PDFInfo
- Publication number
- CN203379642U CN203379642U CN201320496117.4U CN201320496117U CN203379642U CN 203379642 U CN203379642 U CN 203379642U CN 201320496117 U CN201320496117 U CN 201320496117U CN 203379642 U CN203379642 U CN 203379642U
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- container
- valve
- liquid
- tube
- pipe
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- 239000012535 impurity Substances 0.000 title claims abstract description 23
- 238000000926 separation method Methods 0.000 title abstract description 9
- 239000007788 liquid Substances 0.000 claims abstract description 82
- 239000003814 drug Substances 0.000 claims abstract description 32
- 229940079593 drug Drugs 0.000 claims description 28
- 239000010865 sewage Substances 0.000 claims description 15
- 238000001914 filtration Methods 0.000 abstract description 16
- 238000004519 manufacturing process Methods 0.000 abstract description 7
- 238000001556 precipitation Methods 0.000 abstract description 5
- 238000005516 engineering process Methods 0.000 abstract description 3
- 230000007547 defect Effects 0.000 abstract 1
- 238000000975 co-precipitation Methods 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 238000004062 sedimentation Methods 0.000 description 4
- 238000003860 storage Methods 0.000 description 4
- 238000005119 centrifugation Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 230000005484 gravity Effects 0.000 description 2
- 230000035515 penetration Effects 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000011001 backwashing Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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Abstract
The utility model relates to the field of a solution separation device manufacturing technology, and in particular relates to an impurity separation device. The impurity separation device comprises a first container and a second container, wherein the first container comprises a liquid inlet pipe, a first liquid medicine pipe, a first liquid medicine valve, a first discharge pipe, a first valve, a pneumatic tube and a pneumatic valve; the second container comprises a second liquid medicine pipe, a second liquid medicine valve, a second discharge pipe and a second discharge valve; the first container is communicated with the second container by a connecting pipe; the connecting pipe is provided with a connecting valve; the connecting pipe is horizontally arranged on the bottom circular arc surfaces of the first container and the second container and is higher than the bottommost ends of the bottom circular arc surfaces of the first container and the second container by 10-20cm. The impurity separation device is simple in structure, overcomes the defects of the filtering in the traditional precipitation way, saves the precipitation and filtration time and improves the filtering accuracy and the production efficiency.
Description
Technical field
The utility model relates to solution separating device manufacturing technology field, particularly a kind of impurity separating device.
Background technology
Fluid separation applications is filtered three kinds of basic modes: i.e. physics mode, chemical mode and biological mode, and wherein physics mode is called again mechanical system, has simple and easy to doly, and the advantage that use cost is low, so use the most extensive.Liquid is carried out to the physical separation filtration three kinds of basic modes are also arranged: be i.e. penetration mode, centrifugation and coprecipitation mode.
Liquid, under the effect of certain pressure, by filter medium, is dammed the material that is greater than filter bores, and the material that is less than filter bores can pass through smoothly, and this filter type is called penetration mode and filters.But there is a drawback in this mode, i.e. filtering accuracy and the contradiction of filter medium between service life, filtering accuracy is higher, and its filter capacity is more weak, and the plugging rate of filter medium is also higher.Therefore, very high to the requirement of the service condition of high-precision filtration medium, thus its range of application is subject to certain restrictions.So usually need to carry out coarse filtration to filtrate, otherwise high-accuracy filter medium can't be used at all.In actual applications, once filter medium stops up, because its invertibity is poor, the imperfection of backwash, be restricted the efficiency of backwashing system.Therefore, in order to guarantee filter effect, after usually using a period of time, have to be changed filter medium, this not only makes troubles to use, but also has increased the cost of filtering material.
When liquid is in while to same direction, making High Rotation Speed, under the effect of centrifugal force, weight in liquid is moved to peripheral direction, light thing moves to rotor shaft direction, thereby realizes the separation of liquid, and this mode is called centrifugation and filters.But, in centrifugation is separated, the separation of liquid should be subject to the impact of difference in specific gravity between separated object in liquid, is subject to again the impact of centrifugal force.Therefore, the separated object difference in specific gravity is larger, and it is easier to separate, otherwise separates just more difficult; On the other hand, centrifugal force is larger, and its separating power is stronger, but requires the rotary drum rotating speed higher, and the power of the motor configured is larger, causes power consumption to increase, and simultaneously because the rotary drum rotating speed is very high, explosion or blast easily occur rotary drum, have potential safety hazard in use procedure.
Coprecipitation mode filter be liquid under static conditions, utilize terrestrial gravitation, after certain hour, make the mode that in liquid, the heavy material material little with proportion separated.Although it is inexpensive that the coprecipitation mode filtration has advantages of, filter efficiency is lower.The present invention is in conjunction with actual conditions, and the change by prior art, improved filter efficiency, has overcome this drawback.
Summary of the invention
The utility model, for the deficiencies in the prior art, provides a kind of impurity separating device, has overcome the drawback that traditional coprecipitation mode filters, and has saved the sedimentation and filtration time, has improved filtering accuracy and production efficiency.
The main technical schemes that the utility model adopts is: a kind of impurity separating device, it is characterized in that: it comprises the first container and second container, described the first container comprises feed tube, the first drug liquid tube, the first liquid valve, the first blow-off pipe, the first sewage draining valve, pneumatic tube, air pressure valve, described second container comprises the second drug liquid tube, the second liquid valve, the second blow-off pipe, the second sewage draining valve, described the first container and second container are connected by tube connector, the connection valve is installed on described tube connector, described tube connector level is positioned on the bottom arc surface of the first container and second container, and higher than 10 centimetres～20 centimetres of the first container and second container bottom arc surface lowermost ends.
The utility model also adopts following attached technical scheme:
The first drug liquid tube is positioned on the bottom arc surface of the first container, and stretches into interior 10 centimetres～20 centimetres high of the first container, and the first liquid valve is installed on described the first drug liquid tube.
The first blow-off pipe is positioned at the bottom arc surface lowermost end of the first container, on described the first blow-off pipe, the first sewage draining valve is installed.
Pneumatic tube is positioned on the top arc face of the first container, on described pneumatic tube, air pressure valve is installed.
The second drug liquid tube is positioned on the bottom arc surface of second container, and stretches into interior 5 centimetres～10 centimetres high of second container, and the second liquid valve is installed on described the second drug liquid tube.
The second blow-off pipe is positioned at the bottom arc surface lowermost end of second container, on described the second blow-off pipe, the second sewage draining valve is installed.
The beneficial effect that adopts the utility model to bring is: overcome the drawback that traditional coprecipitation mode filters, saved the sedimentation and filtration time, improved filtering accuracy and production efficiency.
The accompanying drawing explanation
Below in conjunction with accompanying drawing, be described further:
The structural representation that Fig. 1 is a kind of impurity separating device of the utility model.
The label that wherein component names is corresponding is as follows:
The first container 1, second container 2, feed tube 3, the first drug liquid tube 4, the first liquid valve 5, the first blow-off pipe 6, the first sewage draining valve 7, pneumatic tube 8, air pressure valve 9, the second drug liquid tube 10, the second liquid valve 11, the second blow-off pipe 12, the second sewage draining valve 13, tube connector 14, connection valve 15.
The specific embodiment
As shown in Figure 1, in the present embodiment, a kind of impurity separating device, before liquid enters the first container 1 from feed tube 3, the first liquid valve 5, the first sewage draining valve 7, air pressure valve 9, connecting valve 15 all closes, until liquid is filled the first container 1, close feed tube 3, then the liquid in the first container 1 is carried out to quiescent setting, after a period of time, muddy liquid will be deposited on the bottom arc surface of the first container 1, then the technical staff opens the first liquid valve 5 of installing on the first drug liquid tube 4 be positioned on the first container 1 bottom arc surface, clean liquid will enter subsequent processing by the first drug liquid tube 4, because the first drug liquid tube 4 is to stretch into interior 10 centimetres～20 centimetres high of the first container 1, so the liquid of turbidity and precipitation can't enter the first drug liquid tube 4, play the purpose that impurity separates, when liquid can't be discharged from the first drug liquid tube 4, open the first sewage draining valve 7 of installing on the first blow-off pipe 6, the liquid with impurity of muddiness is discharged to the first container 1 by the first blow-off pipe 6, although this structure is simple, the impurity separating effect is fairly obvious.
But sometimes because of product, supply falls short of demand, need to strengthen production capacity, certain because of the time of liquid precipitation again, shortening the sedimentation time can affect the purity of liquid, so a second container 2 is installed in addition, by tube connector 14, with the first container 1, be connected, tube connector 14 levels are positioned on the bottom arc surface of the first container 1 and second container 2, and higher than 10 centimetres～20 centimetres of the first container 1 and second container 2 bottom arc surface lowermost ends.When the first container 1 liquid storage stores up completely, open the connection valve 15 of installing on tube connector 14, liquid in the first container 1 starts to enter second container 2, because the first container 1 has precipitated a part of impurity in the liquid storage process, so the liquid in second container 2 is higher than the purity of the liquid in the first container 1, therefore, the second drug liquid tube 10 in second container 2 stretches into interior 5 centimetres～10 centimetres high of second container 2, a little less than the height that stretches into of the first drug liquid tube 4 in the first container 1.Second container 2 is when liquid storage, the first liquid valve 5, the first sewage draining valve 7, the second liquid valve 11, the second sewage draining valve 13 closes, open simultaneously and be positioned at the air pressure valve 9 be arranged on pneumatic tube 8, air after purifying by the interior injection of the pneumatic tube 8 on the first container 1 top arc face, liquid in the first container 1 is pressed in second container 2 by tube connector 14, until the liquid in the first container 1 is pressed into second container 2 fully, first close and connect valve 15, close again air pressure valve 9, then the liquid in second container 2 is carried out to quiescent setting, after a period of time, muddy liquid will be deposited on the bottom arc surface of second container 2, then the technical staff opens the second liquid valve 11 of installing on the second drug liquid tube 10 be positioned on second container 2 bottom arc surfaces, clean liquid will enter subsequent processing by the second drug liquid tube 10, because the second drug liquid tube 10 is to stretch into interior 5 centimetres～10 centimetres high of second container 1, so the liquid of turbidity and precipitation can't enter the second drug liquid tube 10, play the purpose that impurity separates, when liquid can't be discharged from the second drug liquid tube 10, open the second sewage draining valve 13 of installing on the second blow-off pipe 12, the liquid with impurity of muddiness is discharged to second container 2 by the second blow-off pipe 12.When second container 2 inner liquid medicines enter subsequent processing by the second drug liquid tube 10, the feed tube 3 on the first container 1 can carry out liquid storage again, goes round and begins again, and completes the whole procedure that impurity separates.This structure has improved filtering accuracy, has shortened the sedimentation and filtration time, and production efficiency at least improves 50%.
The utility model is not limited to above embodiment, and every other embodiments that drawn according to the technical solution of the utility model by those skilled in the art, within dropping on equally protection domain of the present utility model.
Claims (6)
1. an impurity separating device, it is characterized in that: it comprises the first container (1) and second container (2), described the first container (1) comprises feed tube (3), the first drug liquid tube (4), the first liquid valve (5), the first blow-off pipe (6), the first sewage draining valve (7), pneumatic tube (8), air pressure valve (9), described second container (2) comprises the second drug liquid tube (10), the second liquid valve (11), the second blow-off pipe (12), the second sewage draining valve (13), described the first container (1) and second container (2) are connected by tube connector (14), be equipped with on described tube connector (14) and connect valve (15), described tube connector (14) level is positioned on the bottom arc surface of the first container (1) and second container (2), and higher than 10 centimetres～20 centimetres of the first container (1) and second container (2) bottom arc surface lowermost ends.
2. a kind of impurity separating device as claimed in claim 1, it is characterized in that: described the first drug liquid tube (4) is positioned on the bottom arc surface of the first container (1), and stretch into interior 10 centimetres～20 centimetres high of the first container (1), the first liquid valve (5) is installed on described the first drug liquid tube (4).
3. a kind of impurity separating device as claimed in claim 1, it is characterized in that: described the first blow-off pipe (6) is positioned at the bottom arc surface lowermost end of the first container (1), and the first sewage draining valve (7) is installed on described the first blow-off pipe (6).
4. a kind of impurity separating device as claimed in claim 1, it is characterized in that: described pneumatic tube (8) is positioned on the top arc face of the first container (1), and air pressure valve (9) is installed on described pneumatic tube (8).
5. a kind of impurity separating device as claimed in claim 1, it is characterized in that: described the second drug liquid tube (10) is positioned on the bottom arc surface of second container (2), and stretch into interior 5 centimetres～10 centimetres high of second container (2), the second liquid valve (11) is installed on described the second drug liquid tube (10).
6. a kind of impurity separating device as claimed in claim 1, it is characterized in that: described the second blow-off pipe (12) is positioned at the bottom arc surface lowermost end of second container (2), and the second sewage draining valve (13) is installed on described the second blow-off pipe (12).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320496117.4U CN203379642U (en) | 2013-08-15 | 2013-08-15 | Impurity separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320496117.4U CN203379642U (en) | 2013-08-15 | 2013-08-15 | Impurity separation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203379642U true CN203379642U (en) | 2014-01-08 |
Family
ID=49868176
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320496117.4U Expired - Fee Related CN203379642U (en) | 2013-08-15 | 2013-08-15 | Impurity separation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203379642U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107298192A (en) * | 2017-06-08 | 2017-10-27 | 苏州首达机械有限公司 | Filling batch can |
-
2013
- 2013-08-15 CN CN201320496117.4U patent/CN203379642U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107298192A (en) * | 2017-06-08 | 2017-10-27 | 苏州首达机械有限公司 | Filling batch can |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| 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: 20140108 |