CN205760029U - For chemical experiment defecator - Google Patents
For chemical experiment defecator Download PDFInfo
- Publication number
- CN205760029U CN205760029U CN201620475166.3U CN201620475166U CN205760029U CN 205760029 U CN205760029 U CN 205760029U CN 201620475166 U CN201620475166 U CN 201620475166U CN 205760029 U CN205760029 U CN 205760029U
- Authority
- CN
- China
- Prior art keywords
- filter
- filter element
- defecator
- chemical experiment
- rotating seat
- 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
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- Filtering Materials (AREA)
- Filtration Of Liquid (AREA)
Abstract
This utility model relates to experiment filter plant design field, disclose for chemical experiment defecator, include filter, filter element, firm banking and pressurization cleaning assembly, pass through Optimal Structure Designing, multistage composite filter element is used to replace filter cake or the sand core funnel of traditional chemical filtration, wherein multistage composite filter element uses micro-porous resin and polypropylene PP melt-blown filter compound suppressing, be can ensure that by pressurization cleaning assembly the high efficiente callback of filter element uses；Through the chemical experiment defecator of appropriate design, rotating seat can be set up at firm banking, drive filter element to rotate by rotating seat and form centrifugal force, improve the filter effect of filtrate, improve filter element overall utilization rate.
Description
Technical field
This utility model relates to experiment filter plant design field, filters dress especially for chemical experiment
Put.
Background technology
Composite fibre filtrate is that the combination granule filter material of development in recent years is new with the one of fiber filtering feature
Type filtrate, is a kind of up-to-date water environmental protection technology.It can play, and fiber filtering specific surface area is big, filter essence
Degree is high, pollutant holding capability is big, and filter cycle is long, the advantage that filtration flow-rate is high, possesses again granule filter material backwash
Advantage the easiest, that wash degree is high and water consumption is few.Composite fibre filtrate is in urban water supply and sewerage, work
Existing certain application such as factory's plumbing, but all must have the condition of electricity, filter plant just can use.
Under without electrical environment or in the wild, as long as water source has certain pressure both can complete to filter and backwash, can
With long Reusability；Extend the application space of this composite fibre filtrate.
In the lab, common defecator such as filter cloth, sand core funnel, vacuum filter, using
During often occur that leakage filter, the situation such as damaged, and the most many use materials are disposable consumption
Material, easily causes and excessively uses and wasting phenomenon.
Summary of the invention
The purpose of this utility model is to provide a kind of for chemical experiment defecator, uses multistage composite
Filter element, can carry out high efficiency separation to separating liquid needed for acid-base waste fluid common in laboratory and other,
And have additional pressurization cleaning assembly, it is ensured that the high efficiente callback ability of filter element.
For realizing above-mentioned technical purpose, reach above-mentioned technique effect, the utility model discloses for chemistry
Experiment defecator, includes filter, filter element, firm banking and pressurization cleaning assembly, and filter is
Column-shaped barrel, is installed on firm banking, and filter element is installed in filter, and pressurization cleaning assembly is by defeated
Pipe arrangement road is connected with the cleanout fluid inlet of filter bottom side.
Wherein, filter element is logical filter element in column, and filter element is compacted by micro-porous resin and polypropylene PP melt-blown filter
Compound, wherein, micro-porous resin and polypropylene PP melt-blown filter filter thickness are 2: 3, and filter element installs nesting
In filter middle portion.
Wherein, it is corresponding with through hole in filter element that filter top offers filtrate inlet, filtrate inlet
Side be provided with vent valve, filter top side offers cleanout fluid liquid outlet, filter bottom one
Side offers cleanout fluid inlet, and the sidewall of filter offers filtrate liquid outlet.
Wherein, pressurization cleaning assembly includes prelum main body, hydraulic push rod, slide damper and reservoir,
Slide damper is installed in reservoir, and prelum main body is connected with hydraulic push rod, one end peace of hydraulic push rod
Dress is fixed on slide damper.
Preferably, firm banking being provided with rotating seat, rotating seat is mutually matched with filter element size, is used for
Installing nested filter element, rotating seat is rotated by the driving driven by motor below rotating seat.
This utility model has the advantages that
1. this utility model passes through Optimal Structure Designing, uses multistage composite filter element to replace the filter that traditional chemical filters
Cake or sand core funnel, wherein multistage composite filter element uses micro-porous resin and the compound pressure of polypropylene PP melt-blown filter
System, can ensure that by pressurization cleaning assembly the high efficiente callback of filter element uses.
2. through the chemical experiment defecator of appropriate design, rotating seat can be set up at firm banking, by rotation
Swivel base drives filter element to rotate and forms centrifugal force, improves the filter effect of filtrate, improves filter element overall utilization rate.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Primary clustering symbol description:
1: filter, 2: filtrate inlet, 3: vent valve, 4: cleanout fluid liquid outlet, 5: clean
Liquid inlet, 6: filtrate liquid outlet, 7: filter element, 8: micro-porous resin, 9: polypropylene PP melt-blown filter
Core, 10: firm banking, 11: prelum main body, 12: hydraulic push rod, 13: slide damper, 14: storage
Liquid bath
Detailed description of the invention
In order to make the purpose of this utility model, technical scheme and advantage clearer, below in conjunction with attached
Figure and embodiment, be further elaborated to this utility model.
As it is shown in figure 1, the utility model discloses a kind of for chemical experiment defecator, included
Filter 1, filter element 7, firm banking 10 and pressurization cleaning assembly, wherein, pressurization cleaning assembly includes
Prelum main body 11, hydraulic push rod 12, slide damper 13 and reservoir 14.
Structure designs:
Filter 1 is installed on firm banking 10 for column-shaped barrel, and filter 1 top offers filtrate and enters
Liquid mouth 2 is corresponding with through hole in filter element 7, and the side of filtrate inlet 2 is provided with vent valve 3, filter
1 top side offers cleanout fluid liquid outlet 4, and filter 1 bottom side offers cleanout fluid inlet 5,
Offering filtrate liquid outlet 6 on the sidewall of filter 1, filter element 7 is installed and is nested in the middle part of filter 1, adds
Pressure cleaning assembly is connected with the cleanout fluid inlet 5 of filter 1 bottom side by transmission & distribution pipeline.
Filter element 7 is logical filter element in column, and filter element 7 is pressed by micro-porous resin 8 and polypropylene PP melt-blown filter 9
Real compound, wherein, micro-porous resin 8 and polypropylene PP melt-blown filter 9 filter thickness are 2: 3.
In pressurization cleaning assembly, gear 13 plates that slide are installed in reservoir 14, prelum main body 11 with
Hydraulic push rod 12 is connected, and one end of hydraulic push rod 12 is mounted on slide damper 13.
Operation principle:
The application chemical experiment defecator, uses multistage composite filter element to replace the filter cake that traditional chemical filters
Or sand core funnel, wherein multistage composite filter element uses micro-porous resin 8 and polypropylene PP melt-blown filter 9 to be combined
Compacting, and equipped with pressurization cleaning assembly, high-pressure cleaning liquid reverse cleaning filter element 7 can be passed through, it is achieved
The recycling of filter element 7.
And can be provided with rotating seat on firm banking 10, rotating seat is mutually matched with filter element 7 size,
For installing nested filter element 7, rotating seat is rotated by the driving driven by motor below rotating seat, passes through rotating seat
Drive filter element 7 to rotate and form centrifugal force, improve the filter effect of filtrate, improve filter element 7 overall utilization rate.
The above, only this utility model preferably detailed description of the invention, but protection of the present utility model
Scope is not limited thereto, the skill that any those familiar with the art discloses at this utility model
In the range of art, the change that can readily occur in or replacement, all should contain protection domain of the present utility model it
In.
Claims (5)
1. for chemical experiment defecator, it is characterised in that include filter, filter element, firm banking
With pressurization cleaning assembly, described filter is column-shaped barrel, is installed on firm banking, described filter element
It is installed in filter, the cleaning by transmission & distribution pipeline with filter bottom side of the described pressurization cleaning assembly
Liquid inlet is connected.
2. as claimed in claim 1 for chemical experiment defecator, it is characterised in that: described filter element
For filter element logical in column, described filter element is compacted compound by micro-porous resin and polypropylene PP melt-blown filter, wherein,
Micro-porous resin and polypropylene PP melt-blown filter filter thickness are 2: 3, and described filter element is installed and is nested in filter
Middle part.
3. as claimed in claim 1 or 2 for chemical experiment defecator, it is characterised in that: described
Filter top offers filtrate inlet, corresponding with through hole in filter element, and the side of filtrate inlet is provided with
Vent valve, filter top side offers cleanout fluid liquid outlet, and filter bottom side offers cleanout fluid
Inlet, the sidewall of filter offers filtrate liquid outlet.
4. as claimed in claim 3 for chemical experiment defecator, it is characterised in that: described pressurization
Cleaning assembly includes prelum main body, hydraulic push rod, slide damper and reservoir, described slide damper
Being installed in reservoir, described prelum main body is connected with hydraulic push rod, and one end of hydraulic push rod is installed solid
On slide damper.
5. as claimed in claim 1 for chemical experiment defecator, it is characterised in that: described is fixing
Being provided with rotating seat on base, described rotating seat is mutually matched with filter element size, is used for installing nested filter element,
Described rotating seat is rotated by the driving driven by motor below rotating seat.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620475166.3U CN205760029U (en) | 2016-05-24 | 2016-05-24 | For chemical experiment defecator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620475166.3U CN205760029U (en) | 2016-05-24 | 2016-05-24 | For chemical experiment defecator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205760029U true CN205760029U (en) | 2016-12-07 |
Family
ID=58116194
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620475166.3U Expired - Fee Related CN205760029U (en) | 2016-05-24 | 2016-05-24 | For chemical experiment defecator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205760029U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106975325A (en) * | 2017-05-03 | 2017-07-25 | 中国科学院新疆理化技术研究所 | A kind of trace standard explosive method for concentration based on molecular screen membrane |
| CN110302583A (en) * | 2019-08-13 | 2019-10-08 | 南京佳力图机房环境技术股份有限公司 | A kind of immersion liquid cooling refrigerant filtration system |
-
2016
- 2016-05-24 CN CN201620475166.3U patent/CN205760029U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106975325A (en) * | 2017-05-03 | 2017-07-25 | 中国科学院新疆理化技术研究所 | A kind of trace standard explosive method for concentration based on molecular screen membrane |
| CN110302583A (en) * | 2019-08-13 | 2019-10-08 | 南京佳力图机房环境技术股份有限公司 | A kind of immersion liquid cooling refrigerant filtration system |
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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 |
Granted publication date: 20161207 Termination date: 20170524 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |