CN203648245U - Novel agglomerate separation oil filter - Google Patents
Novel agglomerate separation oil filter Download PDFInfo
- Publication number
- CN203648245U CN203648245U CN201320720099.3U CN201320720099U CN203648245U CN 203648245 U CN203648245 U CN 203648245U CN 201320720099 U CN201320720099 U CN 201320720099U CN 203648245 U CN203648245 U CN 203648245U
- Authority
- CN
- China
- Prior art keywords
- oil
- filter
- tank
- rotary barrel
- coarse separation
- 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 - Lifetime
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- 238000000926 separation method Methods 0.000 title claims abstract description 23
- 238000001914 filtration Methods 0.000 claims abstract description 17
- 239000012528 membrane Substances 0.000 claims description 14
- 230000008676 import Effects 0.000 claims description 7
- 239000002699 waste material Substances 0.000 claims description 6
- 239000007788 liquid Substances 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 238000010521 absorption reaction Methods 0.000 abstract 2
- 238000009833 condensation Methods 0.000 abstract 2
- 230000005494 condensation Effects 0.000 abstract 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 2
- 230000002035 prolonged effect Effects 0.000 abstract 1
- 239000000047 product Substances 0.000 description 16
- 239000012535 impurity Substances 0.000 description 4
- 238000005119 centrifugation Methods 0.000 description 2
- 238000003828 vacuum filtration Methods 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 1
- 238000004581 coalescence Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
Images
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- Centrifugal Separators (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses a novel agglomerate separation oil filter which comprises a first stage filtering device, a second stage filtering device and a third stage filtering device, wherein the first stage filtering device comprises an oil inlet, a first outlet, an agglomerate separator and a water collection tank; the water collection tank is arranged at the lower part of the agglomerate separator; the second stage filtering device comprises a shell, a second inlet, an oil absorption pump, a second outlet and a rotary barrel; the oil absorption pump is provided with the second inlet and is connected with the top of the rotary barrel; the rotary barrel is provided with a through hole and a plurality of layers of filter films; the third stage filtering device comprises a third inlet, an oil outlet, a preheating tank, a vacuum chamber and a condensation tank; the oil outlet is arranged under the vacuum chamber, and the condensation tank is arranged above the vacuum chamber. According to the novel agglomerate separation oil filter, agglomerate separation filtering, centrifugal separation filtering and vacuum filtering are combined together, so that the oil product can be effectively purified, the purity of the oil product is improved, and the purified oil product can be used for a second time; the novel agglomerate separation oil filter is simple in structure and high in efficiency, the production cost is lowered, and the service life of an oil consumption device can be prolonged.
Description
Technical field
The utility model relates to plant equipment field, is specifically related to a kind of oil filter.
Background technology
After machine run, in oil product, bring impurity into, can not reuse, the existence of impurity can affect the service life of the operation of a machine and infringement machine.Oil product also has great waste simultaneously.Oil filter is the filter of removing mechanical admixture, oxidized byproduct and moisture in impure absolute oil with technical methods such as gravity, centrifugal, pressure, vacuum distillation, mass transfers.Interaction energy by oil filter is purified to oil product, is convenient to its secondary and uses.
Utility model content
For solving the deficiencies in the prior art, the purpose of this utility model is to provide a kind of novel coarse separation oil filter, improves the purity that oil product is filtered.
In order to realize above-mentioned target, the utility model adopts following technical scheme:
A kind of novel coarse separation oil filter, it is characterized in that: comprise three-level filter device, first order filter is coarse separation filter, and described first order filter comprises oil-in, the first outlet, coalescing separator and collecting-tank, and the bottom of described coalescing separator is provided with collecting-tank; Second level filter is centrifugal separating device, and described second level filter comprises housing, the second import, oil scavenge pump, the second outlet and rotary barrel; Described oil scavenge pump is provided with the second import, and is connected with rotary barrel top; Described rotary barrel is provided with through hole and some layers of filter membrane, described filter membrane is arranged on rotary barrel inner side, described rotary barrel is subject to drive unit to drive rotation, described third level filter is vacuum apparatus, described third level filter comprises triple feed inlet, oil-out, preheats tank, vacuum chamber and drainer, the described tank that preheats is connected with triple feed inlet, and the below of described vacuum chamber is provided with oil-out, and top is connected with drainer.
The number of plies of aforementioned filter membrane is at least 3 layers.
Aforementioned filter membrane is macromolecular filtering film.
The below of aforementioned rotary barrel is provided with waste liquid tank.
The aforementioned tank that preheats is constant temperature heating device, comprises thermostat and the heater that is subject to thermostat control.
The aforementioned temperature that preheats tank is 50 DEG C-55 DEG C.
Usefulness of the present utility model is: the novel coarse separation oil filter of one that the utility model provides, utilize the acting in conjunction of coarse separation filtration, centrifugation filtration and vacuum filtration, oil product is effectively purified, improve the purity of oil product, the oil product of purifying can be used by secondary, efficiency simple in structure is high, has reduced production cost, has extended the service life of oil product use equipment.
Brief description of the drawings
Fig. 1 is the schematic diagram of the preferred embodiment of a kind of novel coarse separation oil filter that provides of the utility model;
The implication of Reference numeral in figure: 1 oil-in, 2 coalescing separators, 3 collecting-tanks, 4 first outlets, 5 second imports, 6 oil scavenge pumps, 7 housings, 8 rotary barrels, 9 second outlets, 10 through holes, 11 filter membranes, 12 triple feed inlets, 13 preheat tank, 14 vacuum chambers, 15 oil-outs, 16 drainers, 17 waste liquid tanks.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the utility model is done to concrete introduction.
As shown in Figure 1, a kind of novel coarse separation oil filter, comprises three-level filter device, and first order filter is coarse separation filter, first order filter comprises oil-in 1, the first outlet 4, coalescing separator 2 and collecting-tank 3, and the bottom of coalescing separator 2 is provided with collecting-tank 3; Second level filter is centrifugal separating device, and second level filter comprises housing 7, the second import 5, oil scavenge pump 6, the second outlet 9 and rotary barrel 8; Oil scavenge pump 6 is provided with the second import 5, and is connected with rotary barrel 8 tops; Rotary barrel 8 is provided with through hole 10 and some layers of filter membrane 11, and filter membrane 11 is arranged on rotary barrel 8 inner sides, and preferably, the number of plies of filter membrane 11 is at least 3 layers.Filter membrane 11 is macromolecular filtering film 11.Rotary barrel 8 is subject to drive unit to drive rotation, and the below of rotary barrel 8 is provided with waste liquid tank 17.Third level filter is vacuum apparatus, third level filter comprises triple feed inlet 12, oil-out 15, preheats tank 13, vacuum chamber 14 and drainer 16, preheating tank 13 is connected with triple feed inlet 12, preheat tank 13 for constant temperature heating device, comprise thermostat and the heater that is subject to thermostat control.Preferably, the temperature that preheats tank 13 is 50 DEG C-55 DEG C.The below of vacuum chamber 14 is provided with oil-out 15, and top is connected with drainer 16.
When work, need filter oil enter coalescing separator, Coalescence filter core with separate under the effect of filter core, filter, impurity is stayed in collecting-tank.Next enters centrifugal separating device, due to the centrifugal force that the rotation of rotary barrel produces, oil product is entered in housing after the filtration of layer high molecule filter membrane on rotary barrel through hole, and impurity and moisture are trapped and enter waste liquid tank.Oil product enters and preheats tank and preheat 50 DEG C-55 DEG C through the second outlet, makes temperature be unlikely to too high and too low, enters subsequently in vacuum tank, and in oil product, moisture evaporation enters in drainer and collects, and the clean oil product finally obtaining is flowed out by oil-out.Utilize the acting in conjunction of coarse separation filtration, centrifugation filtration and vacuum filtration, oil product is effectively purified, improve the purity of oil product, the oil product of purifying can be used by secondary, efficiency simple in structure is high, has reduced production cost, has extended the service life of oil product use equipment.
More than show and described general principle of the present utility model, principal character and advantage.The technical staff of the industry should understand, and above-described embodiment does not limit the utility model in any form, and all employings are equal to replaces or technical scheme that the mode of equivalent transformation obtains, all drops in protection domain of the present utility model.
Claims (6)
1. a novel coarse separation oil filter, it is characterized in that: comprise three-level filter device, first order filter is coarse separation filter, and described first order filter comprises oil-in, the first outlet, coalescing separator and collecting-tank, and the bottom of described coalescing separator is provided with collecting-tank; Second level filter is centrifugal separating device, and described second level filter comprises housing, the second import, oil scavenge pump, the second outlet and rotary barrel; Described oil scavenge pump is provided with the second import, and is connected with rotary barrel top; Described rotary barrel is provided with through hole and some layers of filter membrane, described filter membrane is arranged on rotary barrel inner side, described rotary barrel is subject to drive unit to drive rotation, described third level filter is vacuum apparatus, described third level filter comprises triple feed inlet, oil-out, preheats tank, vacuum chamber and drainer, the described tank that preheats is connected with triple feed inlet, and the below of described vacuum chamber is provided with oil-out, and top is connected with drainer.
2. the novel coarse separation oil filter of one according to claim 1, is characterized in that: the number of plies of described filter membrane is at least 3 layers.
3. the novel coarse separation oil filter of one according to claim 2, is characterized in that: described filter membrane is macromolecular filtering film.
4. the novel coarse separation oil filter of one according to claim 1, is characterized in that: the below of described rotary barrel is provided with waste liquid tank.
5. the novel coarse separation oil filter of one according to claim 1, is characterized in that: described in to preheat tank be constant temperature heating device, comprise thermostat and be subject to the heater of thermostat control.
6. the novel coarse separation oil filter of one according to claim 5, is characterized in that: described in preheat tank temperature be 50 DEG C-55 DEG C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320720099.3U CN203648245U (en) | 2013-11-15 | 2013-11-15 | Novel agglomerate separation oil filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320720099.3U CN203648245U (en) | 2013-11-15 | 2013-11-15 | Novel agglomerate separation oil filter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203648245U true CN203648245U (en) | 2014-06-18 |
Family
ID=50914688
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320720099.3U Expired - Lifetime CN203648245U (en) | 2013-11-15 | 2013-11-15 | Novel agglomerate separation oil filter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203648245U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103611360A (en) * | 2013-11-15 | 2014-03-05 | 昆山威胜达环保设备有限公司 | Novel coalescence-separation oil filtering machine |
| CN104096414A (en) * | 2014-08-01 | 2014-10-15 | 廖婕 | Centrifugal vacuum oil filter |
-
2013
- 2013-11-15 CN CN201320720099.3U patent/CN203648245U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103611360A (en) * | 2013-11-15 | 2014-03-05 | 昆山威胜达环保设备有限公司 | Novel coalescence-separation oil filtering machine |
| CN104096414A (en) * | 2014-08-01 | 2014-10-15 | 廖婕 | Centrifugal vacuum oil filter |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140618 |