CN105194928A - Refined oil purifying and processing system - Google Patents
Refined oil purifying and processing system Download PDFInfo
- Publication number
- CN105194928A CN105194928A CN201510587051.3A CN201510587051A CN105194928A CN 105194928 A CN105194928 A CN 105194928A CN 201510587051 A CN201510587051 A CN 201510587051A CN 105194928 A CN105194928 A CN 105194928A
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- filter
- oil
- screen pack
- treatment system
- cleaning treatment
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Abstract
The invention provides a refined oil purifying and processing system which comprises a filtering mechanism, an oil pump, a dehydration mechanism and an oil storage mechanism. An inlet of the filtering mechanism is connected with an inlet of a refined oil storage mechanism, an outlet of the filtering mechanism is connected with an inlet of the dehydration mechanism, and an outlet of the dehydration mechanism is connected with the oil storage mechanism. The filtering mechanism comprises two or more levels of filters, the filters are provided with filtering meshes, the oil pump is arranged between the first-level filter and the second-level filter, the first-level filter and the second-level filter are provided with a first filtering mesh and the second filtering mesh, and the aperture of the first filtering mesh is 45-60 micron. The dehydration mechanism is provided with a filtering element. The multi-level filter achieves filtration level by level, and efficiency is high. The oil pump is effectively prevented from being damaged through the filter before the oil pump, and the equipment fault rate is lowered; water in oil is effectively separated through the dehydration mechanism, the dirty oil can be processed to be standard just in a filtering mode, the cost is low, and operation is facilitated.
Description
Technical field
The invention belongs to separation equipment field, especially relate to a kind of product oil cleaning treatment system.
Background technology
After product oil pollutes, need process it, the product oil purified treatment mode of prior art mainly contains: 1) transport contaminated product oil back oil plant refinery again, cost is higher; 2) in contaminated product oil, add chemical agent, impurity is polymerized and the measures such as precipitation, and reduce the quality of oil product, and treatment effect is not ideal, oil product is not easy up to standard; Secondly 3) absolute oil is blent, and blends with pure oil, first can reduce the quality of product oil, and the amount of sump oil is too large, needs a large amount of pure oil to blend, and efficiency is low, be not easy to operation.
Summary of the invention
In view of this, the present invention is intended to propose a kind of product oil cleaning treatment system, adopts the oil that the direct quality of production of mode of filtration is up to standard, improves treatment effeciency, reduce costs.
For achieving the above object, technical scheme of the present invention is achieved in that
Product oil cleaning treatment system, for the treatment of the product oil containing mechanical admixture and water, this system comprises filter mechanism, oil pump, dewatering device and oil-bearing structure, described filter mechanism entrance connects product oil storing mechanism entrance, the outlet of this filter mechanism connects dewatering device entrance, and described dewatering device outlet connects oil-bearing structure;
Described filter mechanism at least comprises two-stage filter, i.e. grade one filter and secondary filter, described filter is provided with screen pack, oil pump is provided with between described grade one filter and secondary filter, and grade one filter and secondary filter are respectively equipped with the first screen pack and the second screen pack, the pore diameter range of described first screen pack is 45-60 μm;
Described dewatering device is provided with filter core.
Further, this system is also provided with base, and described filter mechanism and dewatering device are located on base.
Further, be provided with valve, be provided with valve between filter mechanism and oil-bearing structure between described filter mechanism and dewatering device, when the moisture content of sump oil is up to standard, sump oil directly enters oil-bearing structure after filtering.
Further, the screen pack material of described grade one filter and secondary filter is stainless steel.
Further, described filter mechanism is provided with tertiary filter, and tertiary filter is connected in turn with secondary filter.
Further, described tertiary filter is provided with the 3rd screen pack, and the pore diameter range of described 3rd screen pack is 3-10 μm, and the pore diameter range of described second screen pack is 10-45 μm.
Further, described tertiary filter is provided with the 3rd screen pack, and the material of described 3rd screen pack is glass fibre.
Further, described 3rd screen pack inside is provided with supporting network, and described supporting network is stainless steel wire, for supporting the 3rd screen pack with cover glass fiber.
Further, described oil pump filters at different levels below at least one, and to be arranged in parallel with the filter of one-level, be arranged in parallel and can improve the rate of filtration.
Further, described filter core comprises breakdown of emulsion filter core and water-oil separating filter core, and described water-oil separating filter core is located at the top of breakdown of emulsion filter core, and described breakdown of emulsion filter core pore diameter range is 0.5-10 μm.
Relative to prior art, product oil cleaning treatment system of the present invention, has following advantage:
Sump oil pumps in follow-up filter by oil pump, and the filter before oil pump effectively prevent the damage of oil pump, reduces the fault rate of equipment; According to the size of impurity particle particle diameter in sump oil, arrange the filter of three or more level, achieve classified filtering, filter efficiency is high, extends the service life of filter core simultaneously; Dewatering device has been separated the moisture in oil product effectively, and adopt filter type completely by sump oil process to state up to standard, cost is low, convenient operation.
Accompanying drawing explanation
The accompanying drawing forming a part of the present invention is used to provide a further understanding of the present invention, and schematic description and description of the present invention, for explaining the present invention, does not form inappropriate limitation of the present invention.In the accompanying drawings:
Fig. 1 is the block diagram representation of the product oil cleaning treatment system described in the embodiment of the present invention;
Fig. 2 contains the system block diagram schematic diagram of filters in parallel for the product oil cleaning treatment system described in the embodiment of the present invention;
Fig. 3 is the equipment connection front view of the product oil cleaning treatment system described in the embodiment of the present invention;
Fig. 4 is the equipment connection top view of the product oil cleaning treatment system described in the embodiment of the present invention;
The tertiary filter filter cartridge construction schematic diagram that Fig. 5 is the product oil cleaning treatment system described in the embodiment of the present invention;
Fig. 6 is the sectional view of the dewatering device of the product oil cleaning treatment system described in the embodiment of the present invention;
Fig. 7 is the right view of the dewatering device of the product oil cleaning treatment system described in the embodiment of the present invention;
The dewatering device A direction view that Fig. 8 is the product oil cleaning treatment system described in the embodiment of the present invention.
Description of reference numerals:
11-grade one filter, 12-secondary filter, 13-tertiary filter, 131-support tube, 132-supporting network, 133-glass fibre filter core, 2-oil pump, 3-dewatering device, 31-end socket, 32-flange, 33-hanger, 34-drain, 35-gauge port, 36-filter core mounting board, 37-imports and exports adapter, 38-imports and exports dividing plate, 39-bearing, 310-water storage tank is taken over, 311-adapter end socket, 312-draining is taken over, 3131-water-oil separating filter core, 3132-breakdown of emulsion filter core, 314-fixing hole, 34-base, 5-filter inlet, 6-valve, 7-oil-bearing structure, 8-product oil stocking mechanism.
Detailed description of the invention
It should be noted that, when not conflicting, the embodiment in the present invention and the feature in embodiment can combine mutually.
Below with reference to the accompanying drawings and describe the present invention in detail in conjunction with the embodiments.
As shown in figures 1-8, product oil cleaning treatment system, for the treatment of the product oil containing mechanical admixture and water, this system comprises filter mechanism, oil pump 2, dewatering device 3 and oil-bearing structure 7, described filter mechanism entrance connects product oil storing mechanism entrance, the outlet of this filter mechanism connects dewatering device 3 entrance, and described dewatering device 3 exports and connects oil-bearing structure 7;
Described filter mechanism at least comprises two-stage filter, i.e. grade one filter 11 and secondary filter 12, described filter is provided with screen pack, oil pump 2 is provided with between described grade one filter 11 and secondary filter 12, and grade one filter 11 and secondary filter 12 are respectively equipped with the first screen pack and the second screen pack, the pore diameter range of described first screen pack is 45-60 μm, is more preferably 48-55 μm;
Described dewatering device 3 is provided with filter core.
Preferably, this system is also provided with base 4, and described filter mechanism, oil pump 2 are all located on base 4 with dewatering device 3.
Preferably, be provided with valve 6 between described filter mechanism and dewatering device 3, be provided with valve 6 between filter mechanism and oil-bearing structure 7, when the moisture content of sump oil is up to standard, sump oil directly enters oil-bearing structure 7 after filtering.
Preferably, described grade one filter 11 is stainless steel with the material of the screen pack of secondary filter 12.
Preferably, described filter mechanism is provided with tertiary filter 13, and tertiary filter 13 is connected in turn with secondary filter 12, more preferably, described tertiary filter 13 is provided with the 3rd screen pack, and the material of described 3rd screen pack is glass fibre, and its inside is provided with stainless supporting network 132, the pore diameter range of described 3rd screen pack is 3-10 μm, more has the pore diameter range of choosing to be 3-7 μm; The pore diameter range of described second screen pack is 10-45 μm, and preferred pore diameter range is 12-40 μm.
Preferably, described oil pump 2 filters at different levels below at least one, and to be arranged in parallel with the filter of one-level.
Preferably, described filter core comprises breakdown of emulsion filter core 3132 and water-oil separating filter core 3131, and described water-oil separating filter core 3131 is located at the top of breakdown of emulsion filter core 3132, and the pore diameter range of described breakdown of emulsion filter core 3132 is 0.5-10 μm, more preferably, the pore diameter range of described breakdown of emulsion filter core 3132 is 0.8-3 μm.
Embodiment 1:
As shown in figs 6-8, one end of dewatering device is provided with imports and exports adapter 37, filter core mounting board 36 is provided with perpendicular to import and export adapter 37 in dehydrated structure, filter core is installed on filter core mounting board 36, filter core comprises breakdown of emulsion filter core 3132 and water-oil separating filter core 3131, and breakdown of emulsion filter core 3132 is positioned at the below of water-oil separating filter core 3131, water storage tank is provided with bottom dewatering device, water storage tank outlet connects water storage tank discharge connection 310, water storage tank adapter 310 connects drainpipe 312, and the top of dehydrated structure is provided with gauge port 34 and drain 35.
As shown in Fig. 1,3 and 4, grade one filter 11 connects outlet and oil pump 2 entrance of product oil storing mechanism 8, oil pump 2 exports and connects secondary filter 12, secondary filter 12 connects tertiary filter 13, two passes is had between tertiary filter 13 and oil-bearing structure 7, one is directly be connected by pipeline, and another is connected by processed mechanism 3, and tertiary filter 13 and oil-bearing structure 7, is equipped with valve 6 between dewatering device 3;
When in sump oil, water content exceeds standard, sump oil filters out through grade one filter 11 impurity that particle diameter is greater than 45-60 micron, sump oil after filtration pumps into secondary filter 12 through oil pump 2, secondary filter 12 filters out the impurity of 10-45 μm of particle diameter, then remove through tertiary filter 13 impurity that particle diameter is 3-10 μm, then enter dewatering device 3 and carry out processed, first dewatering device 3 inside is entered by the breakdown of emulsion filter core 3132 of 0.5-3 μm, abolish the emulsified state of sump oil simultaneously, because profit density is different, water in oil separates by water-oil separating filter core 3131, finally obtain pure product oil up to standard.
When in sump oil, water content is up to standard, time namely without the need to carrying out processed, sump oil directly enters oil-bearing structure 7 through pipeline after metre filter at different levels.
Embodiment 2:
As shown in Figure 2, grade one filter 11 connects outlet and oil pump 2 entrance of product oil storing mechanism 8, oil pump 2 exports, secondary filter 12, tertiary filter 13 connect in turn, secondary filter 12 and tertiary filter 13 include two parallel filters, valve 6 is equipped with after each filters in parallel, two passes is had between tertiary filter 13 and oil-bearing structure 7, one is directly be connected by pipeline, another is connected by processed mechanism 3, and tertiary filter 13 and oil-bearing structure 7, be equipped with valve 6 between dewatering device 3;
When in sump oil, water content exceeds standard, sump oil filters out through grade one filter 11 impurity that particle diameter is greater than 48-55 micron, sump oil after filtration pumps into two parallel secondary filters 12 through oil pump 2, secondary filter 12 filters out the impurity of 12-40 μm of particle diameter, then remove through two parallel tertiary filters 13 impurity that particle diameter is 3-7 μm, the setting of filters in parallel improves the filter efficiency of sump oil, then enter dewatering device 3 and carry out processed, first dewatering device 3 inside is entered by the breakdown of emulsion filter core 3132 of 0.8-3 μm, abolish the emulsified state of sump oil simultaneously, because profit density is different, water in oil separates by water-oil separating filter core 3131, finally obtain pure product oil up to standard
When in sump oil, water content is up to standard, time namely without the need to carrying out processed, sump oil directly enters oil-bearing structure 7 through pipeline after metre filter at different levels.
The foregoing is only preferred embodiment of the present invention, not in order to limit the present invention, within the spirit and principles in the present invention all, any amendment done, equivalent replacement, improvement etc., all should be included within protection scope of the present invention.
Claims (10)
1. product oil cleaning treatment system, for the treatment of the product oil containing mechanical admixture and water, it is characterized in that: this system comprises filter mechanism, oil pump, dewatering device and oil-bearing structure, described filter mechanism entrance connects product oil storing mechanism entrance, the outlet of this filter mechanism connects dewatering device entrance, and described dewatering device outlet connects oil-bearing structure;
Described filter mechanism at least comprises two-stage filter, i.e. grade one filter and secondary filter, described filter is provided with screen pack, oil pump is provided with between described grade one filter and secondary filter, and grade one filter and secondary filter are respectively equipped with the first screen pack and the second screen pack, the pore diameter range of described first screen pack is 45-60 μm;
Described dewatering device is provided with filter core.
2. product oil cleaning treatment system according to claim 1, it is characterized in that: this system is also provided with base, described filter mechanism and dewatering device are located on base.
3. product oil cleaning treatment system according to claim 2, is characterized in that: be provided with valve between described filter mechanism and dewatering device, be provided with valve between filter mechanism and oil-bearing structure.
4. product oil cleaning treatment system according to claim 1, is characterized in that: the screen pack material of described grade one filter and secondary filter is stainless steel.
5., according to the arbitrary described product oil cleaning treatment system of claim 1-4, it is characterized in that: described filter mechanism is provided with tertiary filter, and tertiary filter is connected in turn with secondary filter.
6. product oil cleaning treatment system according to claim 5, is characterized in that: described tertiary filter is provided with the 3rd screen pack, and the pore diameter range of described 3rd screen pack is 3-10 μm, and the pore diameter range of described second screen pack is 10-45 μm.
7. product oil cleaning treatment system according to claim 5, is characterized in that: described tertiary filter is provided with the 3rd screen pack, and the material of described 3rd screen pack is glass fibre.
8. the product oil cleaning treatment system according to claim 6 or 7, is characterized in that: described 3rd screen pack inside is provided with supporting network.
9. product oil cleaning treatment system according to claim 1, is characterized in that: described oil pump filters at different levels below at least one, and to be arranged in parallel with the filter of one-level.
10. product oil cleaning treatment system according to claim 1, is characterized in that: described filter core comprises breakdown of emulsion filter core and water-oil separating filter core, and described breakdown of emulsion filter core pore diameter range is 0.5-10 μm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510587051.3A CN105194928A (en) | 2015-09-15 | 2015-09-15 | Refined oil purifying and processing system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510587051.3A CN105194928A (en) | 2015-09-15 | 2015-09-15 | Refined oil purifying and processing system |
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| Publication Number | Publication Date |
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| CN105194928A true CN105194928A (en) | 2015-12-30 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510587051.3A Pending CN105194928A (en) | 2015-09-15 | 2015-09-15 | Refined oil purifying and processing system |
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| CN (1) | CN105194928A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105664571A (en) * | 2016-02-29 | 2016-06-15 | 邹城市北华机电设备有限公司 | Three-layer water filter system |
| CN108479154A (en) * | 2018-06-21 | 2018-09-04 | 农业部规划设计研究院 | The continuous dust removal by filtration system and method for pyrolysis oil high pressure |
| CN113350869A (en) * | 2021-06-03 | 2021-09-07 | 国网江苏省电力有限公司南通供电分公司 | Transformer oil filtering control system and control method thereof |
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| GB2148268A (en) * | 1983-08-11 | 1985-05-30 | Yks Co Ltd | Separating equipment and water treatment apparatus |
| CN201298425Y (en) * | 2008-11-13 | 2009-08-26 | 济南安塞自动化技术有限公司 | Polymerization-separation on-line filter |
| CN201711041U (en) * | 2010-06-03 | 2011-01-19 | 马琳 | Oil product on-line purification treatment device |
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| CN103599661A (en) * | 2013-10-18 | 2014-02-26 | 周建伟 | Oil-water separation filter core and device for integrated fuel oil filtration and oil-water separation |
| CN203900100U (en) * | 2014-04-15 | 2014-10-29 | 天津太钢天管不锈钢有限公司 | Twenty-roller strip mill rolling oil recycler |
| CN205073773U (en) * | 2015-09-15 | 2016-03-09 | 天津惠博普管道技术有限公司 | Novel quick purification treatment system of product oil |
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2015
- 2015-09-15 CN CN201510587051.3A patent/CN105194928A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
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| GB2148268A (en) * | 1983-08-11 | 1985-05-30 | Yks Co Ltd | Separating equipment and water treatment apparatus |
| CN201298425Y (en) * | 2008-11-13 | 2009-08-26 | 济南安塞自动化技术有限公司 | Polymerization-separation on-line filter |
| CN102233210A (en) * | 2010-04-29 | 2011-11-09 | 陈静 | Oil product purification treatment apparatus |
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| CN202146673U (en) * | 2011-06-09 | 2012-02-22 | 镇江市科能电力设备有限公司 | Vacuum oil filter |
| CN103599661A (en) * | 2013-10-18 | 2014-02-26 | 周建伟 | Oil-water separation filter core and device for integrated fuel oil filtration and oil-water separation |
| CN203900100U (en) * | 2014-04-15 | 2014-10-29 | 天津太钢天管不锈钢有限公司 | Twenty-roller strip mill rolling oil recycler |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105664571A (en) * | 2016-02-29 | 2016-06-15 | 邹城市北华机电设备有限公司 | Three-layer water filter system |
| CN108479154A (en) * | 2018-06-21 | 2018-09-04 | 农业部规划设计研究院 | The continuous dust removal by filtration system and method for pyrolysis oil high pressure |
| CN113350869A (en) * | 2021-06-03 | 2021-09-07 | 国网江苏省电力有限公司南通供电分公司 | Transformer oil filtering control system and control method thereof |
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Application publication date: 20151230 |