CN207307345U - High pressure high-volume biochemical filtration equipment - Google Patents
High pressure high-volume biochemical filtration equipment Download PDFInfo
- Publication number
- CN207307345U CN207307345U CN201720489187.5U CN201720489187U CN207307345U CN 207307345 U CN207307345 U CN 207307345U CN 201720489187 U CN201720489187 U CN 201720489187U CN 207307345 U CN207307345 U CN 207307345U
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- CN
- China
- Prior art keywords
- net liquid
- liquid recovery
- recirculating zone
- recovery approach
- high pressure
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Abstract
The utility model discloses a kind of high pressure high-volume biochemical filtration equipment, including high input voltage pipe, filter screen and the circulatory system and net liquid recovery pond, input channel tilt upward arrangement, the end of input channel connects with net liquid recovery approach and sets filter screen, and net liquid recovery approach is arranged diagonally downward；Interlayer is set between recirculating zone and filtering falling area and is provided with automatic ration drainage mechanism；Prong is set in the minimum diameter position of the necking section of high input voltage pipe and suction tube is installed, the lower end of the suction tube is located in the reflux liquid bath of recirculating zone bottom.The utility model can make solids stop recycling of directly falling by filter screen after apical position is moved upward to, the moisturizing problem between filter falling area and recirculating zone is automatically controlled using automatic ration drainage mechanism, compensated by negative pressure hidden pipe by net liquid recovery approach, the negative pressure factor inside net liquid recovery approach is further increased, beneficial to increase net liquid recycling power.
Description
Technical field
The utility model belongs to biochemical filtration equipment technical field, and in particular to a kind of high pressure high-volume biochemical filtration is set
It is standby.
Background technology
Either the manufacturing process of chemicals or biomedical product usually all include filter out in suspension with
Product existing for solid matter form.Possibility and inspection are cleaned due to the quality and degree of purity of product and to filter for installation
The high standard of possibility is looked into, the filter process of the discontinuous batch of generally use in experiment or production process.Traditional filtering
Instrument can only be adapted to small batch filtering processing, experimental stage use is only applicable to substantially, in the larger biology of production scale or change
In work enterprise, not only treatment effeciency is very low for existing filter plant, but also ineffective, it is necessary to often replace inner part, and operation is numerous
It is trivial, labor intensity is added, there are security risk.
Utility model content
The purpose of this utility model is for there are poor filtration effect and effect in existing biochemistry or medicine production
A kind of the problem of rate is low, there is provided equipment that can realize mass cyclic filtering.
Adopt the following technical scheme that to achieve the above object：A kind of high pressure high-volume biochemical filtration equipment, including high pressure are defeated
Enter pipe, filter screen and the circulatory system and net liquid recovery pond, necking section and high pressure exit wound of bullet are communicated with as defeated with high input voltage pipe
Enter passage, which move towards arrangement, the end of input channel and net liquid recovery approach along tilting upward from the inlet to the outlet
Connection, arrangement is moved towards on edge to net liquid recovery approach diagonally downward from the inlet to the outlet；It is provided with filtering and falls area and recirculating zone after rise, in institute
State and filter screen is provided with the Connectivity Section between input channel and net liquid recovery approach, the filtering falls area after rise and is located under filter screen
Side；Interlayer is set between the recirculating zone and filtering falling area and is provided with automatic ration drainage mechanism；In the necking section
Minimum diameter position sets prong and is provided with suction tube, and the lower end of the suction tube is located in the reflux liquid bath of recirculating zone bottom；
Set with the negative pressure hidden pipe being communicated between net liquid recovery approach and recirculating zone；The lower part of the net liquid recovery approach is communicated in institute
Net liquid recovery pond is stated, and is provided with anti-suck interlayer in net liquid recovery pond and closes net liquid recovery pond into only bottom opening
Isolated area, the lower part of net liquid recovery approach are located in isolated area.It is described filtering fall after rise area bottom be provided with solid-liquid blending bin and
Solid recovery port.The automatic ration drainage mechanism is to fall after rise to set quantitative leakage fluid dram between area and recirculating zone in filtering, is located at
Stent is provided with recirculating zone, pedestal upper end is hinged with swing rod, swing rod one end installation floating body by shaft, and other end connection is slided
Block, the outer end face of the sliding block is convex arc surface, its center of circle is spindle central, while the inner wall by recirculating zone close to quantitative leakage fluid dram
Be arranged to concaved circular cambered surface, convex arc surface described in the concaved circular cambered surface is isocentric circular arc, both match contact, or in convex arc surface or
Compound one layer of gasket on concaved circular cambered surface.The outlet of suction tube can be provided with supercharging catch.
Beneficial effect：The utility model by input channel from the inlet to the outlet along tilt upward move towards arrangement, be conducive to consolidate
Body thing is fallen after rise, and net liquid recovery approach is conducive to return in input channel and net liquid from the inlet to the outlet along arrangement is moved towards diagonally downward
Towing area is formed between receipts passage（Net liquid recovery approach liquid falls downwards process after rise, and the net liquid fallen after rise diagonally downward is from gravity
With under the effect of impacting with high pressure power negative pressure can be formed to the top of net liquid recovery approach）.
Connectivity Section between input channel and net liquid recovery approach is located at top, is provided with filter screen in it, filters back
Settle in an area below filter screen.So as to which solids its power can decline relatively after apical position is moved upward to, again
Recycling of directly falling is stopped by filter screen.
The moisturizing problem between filter falling area and recirculating zone, normal conditions are automatically controlled using automatic ration drainage mechanism
Under, when recirculating zone water is more, recirculating zone is led to because of negative pressure problem in the region that is formed by high pressure swabbing action by negative pressure hidden pipe
Cross net liquid recovery approach to compensate, further increase the negative pressure factor inside net liquid recovery approach, returned beneficial to increase net liquid
Receive power.
Brief description of the drawings
Fig. 1 is the cross-sectional view of the utility model.
Figure label, 1 is high input voltage pipe, and 2 be necking section, and 3 be high pressure exit wound of bullet, and 4 be filter screen, and 5 be negative pressuren zone, 6
It is negative pressure hidden pipe for net liquid recovery approach, 7,8 be suction tube, and 9 be recirculating zone, and 10 be solid-liquid blending bin, and 11 be net liquid recovery pond,
12 be stent, and 13 be shaft, and 14 be swing rod, and 15 be sliding block, and 16 be gasket, and 17 be floating body, and 18 be anti-suck interlayer, and 19 were
Filter falls area after rise, and 20 be reflux liquid bath, and 21 be quantitative leakage fluid dram, and 22 be negative pressure entrance, and 23 be vacuum outlet, and 24 export for net liquid
Mouthful, 25 be supercharging catch, and 26,27 and 28 be solid recovery port.
Embodiment
Embodiment：High pressure high-volume biochemical filtration equipment as shown in Figure 1, including input channel and net liquid recovery approach 6,
Input channel move towards to arrange along tilting upward from the inlet to the outlet, and the end of input channel connects with net liquid recovery approach 6, net liquid
Arrangement is moved towards on edge to recovery approach 6 diagonally downward from the inlet to the outlet.Wherein, input channel high input voltage pipe 1, necking section 2 and height
Injection outlet 3.By input channel from the inlet to the outlet along tilt upward move towards arrangement, be conducive to solids falling, net liquid recycle
Passage 6 along arrangement is moved towards diagonally downward, is conducive to be formed between input channel and net liquid recovery approach 6 and leads from the inlet to the outlet
Draw area.6 liquid of net liquid recovery approach falls downwards process after rise, under the isolated instances of anti-suck interlayer 18, falls after rise diagonally downward
Net liquid can form negative pressure under gravity and the effect of impacting with high pressure power to the top of net liquid recovery approach 6.
Filter screen 4 is provided with Connectivity Section between input channel and net liquid recovery approach 6, high pressure exit wound of bullet 3 is located at
The lower section of filter screen 4.Connectivity Section between input channel and net liquid recovery approach 6 is located at top, is provided with filter screen 4 in it,
Filtering falls area 19 after rise and is located at the lower section of filter screen 4.So as to which solids its power can have relatively after apical position is moved upward to
Declined, and recycling of directly falling is stopped by filter screen 4.
It is additionally provided with filtering and falls area 19 and recirculating zone 9, reflux liquid bath 20, solid-liquid blending bin 10 and net liquid recovery pond 11 after rise.
Filtering falls area 19 after rise and is located at the lower section of filter screen 4.Interlayer is set between recirculating zone 9 and filtering falling area 19 and is provided with automatic ration
Drainage mechanism.Prong is set in the minimum diameter position of necking section 2 and suction tube 8 is installed, the lower end of the suction tube 8 is located at back
In the reflux liquid bath 20 for flowing 9 bottom of area.The lower part of net liquid recovery approach 6 is communicated in the net liquid recovery pond 11, and is returned in net liquid
The isolated area that net liquid recovery pond 11 is closed into only bottom opening by anti-suck interlayer 18 is provided with receives pond 11, net liquid recycling is logical
The lower part in road 6 is located in isolated area.19 bottom of area is fallen after rise in the filtering is provided with solid-liquid blending bin 10 and solid recovery port.
The outlet of suction tube is provided with supercharging catch, can not only prevent solid matter from entering in suction tube, Er Qieneng
The enough suction improved to suction tube.
Automatic ration drainage mechanism is to fall after rise to set quantitative leakage fluid dram 21 between area 19 and recirculating zone 9 in filtering, positioned at returning
Stent 12 is provided with stream area 9,12 upper end of stent is hinged with swing rod 14 by shaft 13, and floating body 17 is installed in 14 one end of swing rod, separately
One end connection sliding block 15, the outer end face of the sliding block 15 is convex arc surface, its center of circle is 13 center of shaft, while recirculating zone 9 is leaned on
The nearly inner wall for quantifying leakage fluid dram 21 is arranged to concaved circular cambered surface, and convex arc surface described in the concaved circular cambered surface is isocentric circular arc, both match
Contact, or compound one layer of gasket 16 in convex arc surface or concaved circular cambered surface.
It is provided with the negative pressure hidden pipe 7 being communicated between net liquid recovery approach 6 and recirculating zone 9, the negative pressure entrance of negative pressure hidden pipe 7
22 are located at the top of net liquid recovery approach 6, and amount of liquid is minimum herein.Fallen after rise using automatic ration drainage mechanism to automatically control filter
Moisturizing problem between area and recirculating zone 9, it is generally the case that when 9 water of recirculating zone is more, recirculating zone 9 is made because being aspirated by high pressure
With negative pressure problem in the region formed, compensated, further increased net by net liquid recovery approach 6 by negative pressure hidden pipe 7
Negative pressure factor inside liquid recovery approach 6, beneficial to increase net liquid recycling power.
Claims (5)
1. a kind of high pressure high-volume biochemical filtration equipment, including high input voltage pipe, filter screen and the circulatory system and net liquid recovery pond,
It is characterized in that：Be communicated with necking section and high pressure exit wound of bullet as input channel with high input voltage pipe, the input channel from entrance to
Outlet move towards to arrange along tilting upward, and the end of input channel connects with net liquid recovery approach, net liquid recovery approach from entrance to
Arrangement is moved towards diagonally downward in outlet edge；It is provided with filtering and falls area and recirculating zone after rise, in the input channel and net liquid recovery approach
Between Connectivity Section in be provided with filter screen, the filtering falls area after rise and be located at filter screen lower section；Fallen after rise with filtering the recirculating zone
Interlayer is set between area and is provided with automatic ration drainage mechanism；Prong is set in the minimum diameter position of the necking section and is pacified
Equipped with suction tube, the lower end of the suction tube is located in the reflux liquid bath of recirculating zone bottom；The lower part of the net liquid recovery approach connects
The net liquid recovery pond is passed through, and is provided with anti-suck interlayer in net liquid recovery pond and closes net liquid recovery pond into only bottom
The isolated area of opening, the lower part of net liquid recovery approach are located in isolated area.
2. high pressure high-volume biochemical filtration equipment according to claim 1, it is characterized in that：Setting is recycled with net liquid is communicated in
Negative pressure hidden pipe between passage and recirculating zone.
3. high pressure high-volume biochemical filtration equipment according to claim 1, it is characterized in that：Area bottom is fallen after rise in the filtering
It is provided with solid-liquid blending bin and solid recovery port.
4. high pressure high-volume biochemical filtration equipment according to claim 1, it is characterized in that：The automatic ration drainage mechanism
It is to fall after rise to set quantitative leakage fluid dram between area and recirculating zone in filtering, stent is provided with recirculating zone, pedestal upper end passes through
Shaft is hinged with swing rod, and swing rod one end installation floating body, other end connection sliding block, the outer end face of the sliding block is convex arc surface, it is justified
The heart is spindle central, while inner wall of the recirculating zone close to quantitative leakage fluid dram is arranged to concaved circular cambered surface, convex described in the concaved circular cambered surface
Arc surface is isocentric circular arc, both match contact, or compound one layer of gasket in convex arc surface or concaved circular cambered surface.
5. high pressure high-volume biochemical filtration equipment according to claim 1, it is characterized in that：It is provided with the outlet of suction tube
It is pressurized catch.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720489187.5U CN207307345U (en) | 2017-05-05 | 2017-05-05 | High pressure high-volume biochemical filtration equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720489187.5U CN207307345U (en) | 2017-05-05 | 2017-05-05 | High pressure high-volume biochemical filtration equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207307345U true CN207307345U (en) | 2018-05-04 |
Family
ID=62436947
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720489187.5U Expired - Fee Related CN207307345U (en) | 2017-05-05 | 2017-05-05 | High pressure high-volume biochemical filtration equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207307345U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106938159A (en) * | 2017-05-05 | 2017-07-11 | 黄河科技学院 | The biochemistry filtered equipment of high pressure high-volume |
-
2017
- 2017-05-05 CN CN201720489187.5U patent/CN207307345U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106938159A (en) * | 2017-05-05 | 2017-07-11 | 黄河科技学院 | The biochemistry filtered equipment of high pressure high-volume |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180504 Termination date: 20200505 |