CN104368208B - Combination bubble-cap formula triphase separator - Google Patents
Combination bubble-cap formula triphase separator Download PDFInfo
- Publication number
- CN104368208B CN104368208B CN201410637986.3A CN201410637986A CN104368208B CN 104368208 B CN104368208 B CN 104368208B CN 201410637986 A CN201410637986 A CN 201410637986A CN 104368208 B CN104368208 B CN 104368208B
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- Prior art keywords
- upper cover
- reactor
- feed
- pipe
- oil
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 20
- 239000000203 mixture Substances 0.000 claims abstract description 14
- 238000000926 separation method Methods 0.000 claims abstract description 12
- 210000003205 muscle Anatomy 0.000 claims description 16
- 239000000945 filler Substances 0.000 claims description 5
- 239000010865 sewage Substances 0.000 claims description 3
- 238000005191 phase separation Methods 0.000 abstract description 4
- 238000000034 method Methods 0.000 description 3
- 238000005336 cracking Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
Landscapes
- Processing Of Solid Wastes (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
<b>the present invention relates to a kind of combination bubble-cap formula triphase separator, comprise primary separator and second-stage separator, primary separator comprises the first reactor and the first upper cover, second-stage separator comprises the 2nd reactor and the 2nd upper cover, first upper cover is provided with the first steam drain, 2nd reactor is provided with the 2nd opening for feed, first steam drain is connected with the 2nd opening for feed, like this, through primary separator initial gross separation process steam again through the further separating treatment of second-stage separator, it is achieved efficiently, in high quality oil, water, vapour three phase separation. Adopting the mode of two-stage separating treatment, the mixture after primary separator initial gross separation processes is again through second-stage separator separating treatment, it is to increase separation accuracy and efficiency, rational in infrastructure, reliable, is suitable for applying in field of garbage disposal.</b>
Description
Technical field
The present invention relates to a kind of bubble-cap formula triphase separator, for the oil obtained after garbage cracking process, water, vapour mixture are carried out three phase separation.
Background technology
After being processed by garbage cracking, one of them product is oil, water, vapour mixture, therefore the process of the three phase separation of oil, water, vapour mixture is also one of judgment criteria of garbage treatment efficiency and quality.
Summary of the invention
It is an object of the invention to provide a kind of combination bubble-cap formula triphase separator, the mixture after primary separator initial gross separation processes carries out separating treatment through second-stage separator again, it is to increase separation efficiency and quality.
For solving the problems of the technologies described above, the present invention adopts following technical scheme:
A kind of bubble-cap formula triphase separator, for by oil, water, oil in vapour mixture, water, vapour three-phase is separated, comprise primary separator and second-stage separator, described primary separator comprises the first reactor that bottom has sewage draining exit, it is located at first upper cover on the top of the first described reactor, it is inserted with the first feed-pipe in the first described upper cover, the bottom of the first described feed-pipe is stretched in the first described reactor, the upper end of the first described feed-pipe has the first opening for feed, the first oil guide plate of closed annular it is tiltedly installed with between the inwall of the first described upper cover and the outer wall of the first described reactor, the first described upper cover has offered the first oil discharge outlet, the part of the first described oil discharge outlet under being tilted to of the first described oil guide plate, lower part of the first described reactor has offered the first water port, upper part of the first described upper cover is offered the first steam drain that the mixture for initial gross separation is discharged, described second-stage separator comprises the 2nd reactor, it is located at the 2nd upper cover on the top of the 2nd described reactor, 2nd feed-pipe extends to the top in the 2nd described upper cover through the inside of the 2nd described reactor, it is provided with reversing tube in the 2nd described upper cover, the upper end of described reversing tube is closed, the 2nd feed-pipe described in part stretches in described reversing tube, the bottom of described reversing tube is stretched in the 2nd described reactor, the bottom of the 2nd described feed-pipe has the 2nd opening for feed, the 2nd oil guide plate of closed annular it is tiltedly installed with between the inwall of the 2nd described upper cover and the outer wall of the 2nd described reactor, the 2nd described upper cover has been offered second row oil mouth, the revenge grace of described second row oil mouth under being tilted to of the 2nd described oil guide plate, lower part of the 2nd described reactor has offered the second row mouth of a river, upper part of the 2nd described upper cover is offered the second row steam ports that the steam Gong isolating is discharged, the 2nd described opening for feed is through is connected to the first described steam drain, has all been filled with reaction filler in the first described reactor and the 2nd described reactor.
Preferably, the first support muscle of radial extension it is provided with between the outer wall of the first described feed-pipe and the inwall of the first described upper cover.
Preferably, the 2nd support muscle of radial extension it is provided with between the outer wall of the 2nd described feed-pipe and the inwall of the 2nd described reactor.
Preferably, the 3rd support muscle of radial extension it is provided with between the outer wall of described reversing tube and the inwall of the 2nd described upper cover.
Preferably, the 4th support muscle of radial extension it is provided with between the inwall of the 2nd described feed-pipe and the inwall of described reversing tube.
Preferably, the bottom of the first described reactor is funnel-form, and the bottom of the 2nd described reactor is funnel-form.
Preferably, the top of the first described upper cover is inverted funnel-form, and the top of the 2nd described upper cover is inverted funnel-form.
Preferably, the first described steam drain is provided with steam discharge pipe, and described second-stage separator is positioned at the top of described primary separator, and described steam discharge pipe is coaxially fixedly connected with the 2nd described feed-pipe.
Owing to technique scheme is used, the present invention compared with prior art has following advantage: the mode adopting two-stage separating treatment, mixture after primary separator initial gross separation processes is again through second-stage separator separating treatment, improve separation accuracy and efficiency, rational in infrastructure, reliable, be suitable for applying in field of garbage disposal.
Accompanying drawing explanation
Accompanying drawing 1 is the structural representation (perspective) of the primary separator in the present embodiment;
Accompanying drawing 2 is the structural representation (perspective) of the second-stage separator in the present embodiment.
In accompanying drawing: 1, the first reactor; 2, the first upper cover; 3, the first feed-pipe; 4, the first oil guide plate; 5, the first oil discharge outlet; 6, the first water port; 7, the first steam drain; 8, the 2nd reactor; 9, the 2nd upper cover; 10, the 2nd feed-pipe; 11, reversing tube; 12, the 2nd oil guide plate; 13, second row oil mouth; 14, the second row mouth of a river; 15, second row steam ports; 16, the first support muscle; 17, the 2nd support muscle; 18, the 3rd support muscle; 19, the 4th support muscle; 20, steam discharge pipe.
Embodiment
Below in conjunction with embodiment shown in the drawings, the present invention is described in detail below:
Upper and lower in specification sheets to for upper and lower when this separator normally uses to, namely the upper and lower in accompanying drawing 1 and accompanying drawing 2 to.
A kind of bubble-cap formula triphase separator, for by oil, water, oil in vapour mixture, water, vapour three-phase is separated, comprise primary separator and second-stage separator, as shown in Figure 1, primary separator comprises the first reactor 1 that bottom has sewage draining exit, it is located at first upper cover 2 on the top of the first reactor 1, the first feed-pipe 3 it is inserted with in first upper cover 2, the bottom of the first feed-pipe 3 is stretched in the first reactor 1, the upper end of the first feed-pipe 3 has the first opening for feed, the first oil guide plate 4 of closed annular it is tiltedly installed with between the inwall of the first upper cover 2 and the outer wall of the first reactor 1, first upper cover 2 has been offered the first oil discharge outlet 5, the part of the first oil discharge outlet 5 under being tilted to of the first oil guide plate 4, lower part of first reactor 1 has been offered the first water port 6, upper part of first upper cover 2 is offered the first steam drain 7 that the mixture for initial gross separation is discharged, as shown in Figure 2, second-stage separator comprises the 2nd reactor 8, it is located at the 2nd upper cover 9 on the top of the 2nd reactor 8, 2nd feed-pipe 10 extends to the top in the 2nd upper cover 9 through the inside of the 2nd reactor 8, it is provided with reversing tube 11 in 2nd upper cover 9, the upper end of reversing tube 11 is closed, part the 2nd feed-pipe 10 stretches in reversing tube 11, the bottom of reversing tube 11 is stretched in the 2nd reactor 8, the bottom of the 2nd feed-pipe 10 has the 2nd opening for feed, the 2nd oil guide plate 12 of closed annular it is tiltedly installed with between the inwall of the 2nd upper cover 9 and the outer wall of the 2nd reactor 8, 2nd upper cover 9 has been offered second row oil mouth 13, the revenge grace of second row oil mouth 13 under being tilted to of the 2nd oil guide plate 12, lower part of 2nd reactor 8 has offered the second row mouth of a river 14, upper part of 2nd upper cover 9 is offered the second row steam ports 15 that the steam Gong isolating is discharged,Through being connected in the first steam drain 7, first reactor 1 and the 2nd reactor 8 of 2nd opening for feed has all been filled with reaction filler, more specifically, the first support muscle 16 of radial extension it is provided with between the outer wall of the first feed-pipe 3 and the inwall of the first upper cover 2, the 2nd support muscle 17 of radial extension it is provided with between the outer wall of the 2nd feed-pipe 10 and the inwall of the 2nd reactor 8, the 3rd support muscle 18 of radial extension it is provided with between the outer wall of reversing tube 11 and the inwall of the 2nd upper cover 9, the 4th support muscle 19 of radial extension it is provided with between the inwall of the 2nd feed-pipe 10 and the inwall of reversing tube 11, the bottom of the first reactor 1 is funnel-form, the bottom of the 2nd reactor 8 is funnel-form, the top of the first upper cover 2 is inverted funnel-form, the top of the 2nd upper cover 9 is inverted funnel-form, first steam drain 7 is provided with steam discharge pipe 20, second-stage separator is positioned at the top of primary separator, steam discharge pipe 20 is coaxially fixedly connected with the 2nd feed-pipe 10.
Oil, water, vapour mixture enters the first reactor 1 from the first opening for feed along the first feed-pipe 3, under the effect of reaction filler therein, the water isolated is discharged from the first water port 6, oil is discharged from the first oil discharge outlet 5, the steam being also mixed with a small amount of oil and water enters from the first steam drain 7 along steam discharge pipe 20 and the 2nd feed-pipe 10, and under the acting in opposition of reversing tube 11, enter in the 2nd reactor 8, under the effect of reaction filler therein, the water isolated further is discharged from the second row mouth of a river 14, oil is discharged from second row oil mouth 13, the steam isolated is discharged from second row steam ports 15, thus complete oil, water, vapour three phase separation.
The design adopts the mode of two-stage separating treatment, and the mixture after primary separator initial gross separation processes is again through second-stage separator separating treatment, it is to increase separation accuracy and efficiency, rational in infrastructure, reliable, is suitable for applying in field of garbage disposal.
The above is only the preferred embodiment of the present invention; it is noted that for those skilled in the art, under the premise without departing from the principles of the invention; can also making some improvements and modifications, these improvements and modifications also should be considered as protection scope of the present invention.
Claims (8)
1. a combination bubble-cap formula triphase separator, for by oil, water, oil in vapour mixture, water, vapour three-phase is separated, it is characterized in that: comprise primary separator and second-stage separator, described primary separator comprises the first reactor that bottom has sewage draining exit, it is located at first upper cover on the top of the first described reactor, it is inserted with the first feed-pipe in the first described upper cover, the bottom of the first described feed-pipe is stretched in the first described reactor, the upper end of the first described feed-pipe has the first opening for feed, the first oil guide plate of closed annular it is tiltedly installed with between the inwall of the first described upper cover and the outer wall of the first described reactor, the first described upper cover has offered the first oil discharge outlet, the part of the first described oil discharge outlet under being tilted to of the first described oil guide plate, lower part of the first described reactor has offered the first water port, upper part of the first described upper cover is offered the first steam drain that the mixture for initial gross separation is discharged, described second-stage separator comprises the 2nd reactor, it is located at the 2nd upper cover on the top of the 2nd described reactor, 2nd feed-pipe extends to the top in the 2nd described upper cover through the inside of the 2nd described reactor, it is provided with reversing tube in the 2nd described upper cover, the upper end of described reversing tube is closed, the 2nd feed-pipe described in part stretches in described reversing tube, the bottom of described reversing tube is stretched in the 2nd described reactor, the bottom of the 2nd described feed-pipe has the 2nd opening for feed, the 2nd oil guide plate of closed annular it is tiltedly installed with between the inwall of the 2nd described upper cover and the outer wall of the 2nd described reactor, the 2nd described upper cover has been offered second row oil mouth, the part of described second row oil mouth under being tilted to of the 2nd described oil guide plate, lower part of the 2nd described reactor has offered the second row mouth of a river, upper part of the 2nd described upper cover is offered the second row steam ports that the steam Gong isolating is discharged,The 2nd described opening for feed is through is connected to the first described steam drain, has all been filled with reaction filler in the first described reactor and the 2nd described reactor.
2. combination bubble-cap formula triphase separator according to claim 1, it is characterised in that: the first support muscle being provided with radial extension between the outer wall of the first described feed-pipe and the inwall of the first described upper cover.
3. combination bubble-cap formula triphase separator according to claim 1, it is characterised in that: the 2nd support muscle being provided with radial extension between the outer wall of the 2nd described feed-pipe and the inwall of the 2nd described reactor.
4. combination bubble-cap formula triphase separator according to claim 1, it is characterised in that: the 3rd support muscle being provided with radial extension between the outer wall of described reversing tube and the inwall of the 2nd described upper cover.
5. combination bubble-cap formula triphase separator according to claim 1, it is characterised in that: the 4th support muscle being provided with radial extension between the inwall of the 2nd described feed-pipe and the inwall of described reversing tube.
6. combination bubble-cap formula triphase separator according to claim 1, it is characterised in that: the bottom of the first described reactor is funnel-form, and the bottom of the 2nd described reactor is funnel-form.
7. combination bubble-cap formula triphase separator according to claim 1, it is characterised in that: the top of the first described upper cover is inverted funnel-form, and the top of the 2nd described upper cover is inverted funnel-form.
8. combination bubble-cap formula triphase separator according to claim 1, it is characterized in that: the first described steam drain is provided with steam discharge pipe, described second-stage separator is positioned at the top of described primary separator, and described steam discharge pipe is coaxially fixedly connected with the 2nd described feed-pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410637986.3A CN104368208B (en) | 2014-11-13 | 2014-11-13 | Combination bubble-cap formula triphase separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410637986.3A CN104368208B (en) | 2014-11-13 | 2014-11-13 | Combination bubble-cap formula triphase separator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104368208A CN104368208A (en) | 2015-02-25 |
| CN104368208B true CN104368208B (en) | 2016-06-08 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410637986.3A Expired - Fee Related CN104368208B (en) | 2014-11-13 | 2014-11-13 | Combination bubble-cap formula triphase separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104368208B (en) |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5143611A (en) * | 1992-02-06 | 1992-09-01 | Summit Oil Company, Inc. | Apparatus for separating oil from water |
| JP4125810B2 (en) * | 1997-10-09 | 2008-07-30 | オリオン機械株式会社 | Oil / water separator and oil / water separator |
| CN2391871Y (en) * | 1999-07-14 | 2000-08-16 | 江苏海鸥冷却塔股份有限公司 | Three-phase separator |
| CN100445701C (en) * | 2007-08-16 | 2008-12-24 | 浙江大学 | Defoaming device used for oil-water-gas three phase continuously metering separator |
| CN204193719U (en) * | 2014-11-13 | 2015-03-11 | 常熟市高压容器制造有限公司 | Combination bubble-cap type three phase separator |
-
2014
- 2014-11-13 CN CN201410637986.3A patent/CN104368208B/en not_active Expired - Fee Related
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| Publication number | Publication date |
|---|---|
| CN104368208A (en) | 2015-02-25 |
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| C14 | Grant of patent or utility model | ||
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| CB03 | Change of inventor or designer information |
Inventor after: Shi Jun Inventor after: Lu Wei Inventor after: Tao Minghua Inventor after: Zhu Hongming Inventor before: Shi Jun Inventor before: Chen Gefei Inventor before: Lu Wei Inventor before: Tao Minghua Inventor before: Zhu Hongming |
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| TR01 | Transfer of patent right |
Effective date of registration: 20170418 Address after: Changshou City Yushan Town Suzhou city Jiangsu province 215556 Mo to Chenghuan Jing Road, No. 3 Patentee after: SUZHOU LYUDAO ENVIRONMENTAL PROTECTION EQUIPMENT MANUFACTURING Co.,Ltd. Address before: Changshou City Yushan Town Suzhou city Jiangsu province 215556 Mocheng West Ring Road No. 3 Jing Patentee before: CHANGSHU HIGH PRESSURE VESSEL MANUFACTURING Co.,Ltd. |
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Effective date of registration: 20190905 Address after: 312000 Huanyu Building 509-5, 300 Fenglin West Road, Lingzhi Street, Yuecheng District, Shaoxing City, Zhejiang Province Patentee after: Zhejiang Huanyu Environmental Technology Co.,Ltd. Address before: 215556 No. 3 Laijing Road, Huancheng, Mocheng, Yushan Town, Changshu City, Jiangsu Province Patentee before: SUZHOU LYUDAO ENVIRONMENTAL PROTECTION EQUIPMENT MANUFACTURING Co.,Ltd. |
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Effective date of registration: 20210831 Address after: 312000 room 2301, Huanyu building, No. 300, Fenglin West Road, Shaoxing City, Zhejiang Province Patentee after: Zhejiang Huanyu Holding Co.,Ltd. Address before: Room 509-5, Huanyu building, 300 Fenglin West Road, lingzhi street, Yuecheng District, Shaoxing City, Zhejiang Province, 312000 Patentee before: Zhejiang Huanyu Environmental Technology Co.,Ltd. |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160608 |