CN1570460A - Rotating liquid ring pipeline delivery method and equipment for high viscosity fluid - Google Patents
Rotating liquid ring pipeline delivery method and equipment for high viscosity fluid Download PDFInfo
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- CN1570460A CN1570460A CN 200410018060 CN200410018060A CN1570460A CN 1570460 A CN1570460 A CN 1570460A CN 200410018060 CN200410018060 CN 200410018060 CN 200410018060 A CN200410018060 A CN 200410018060A CN 1570460 A CN1570460 A CN 1570460A
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Abstract
The invention discloses a highly glutinous liquid's revolving liquid loop pipe transport method and device. Through the first pump, loop liquid storage pot is connected with revolving liquid loop synthesizer in which there are two spiral laminas whose phase difference is 180 DEG C. Through the second pump, highly glutinous liquid's storage pot is connected with highly glutinous liquid inner pipe which is in the middle of the synthesizer. Exit end of the synthesizer is connected with exit pipe in which there is spiral lamina. Rotary motion is generated while the liquid loop is moving forward in the invention. Liquid loop with higher density always lies around inner wall of the pipe through centrifugal force field generated by rotary motion. On the contrary, oil phase with lower density lies in the center of the pipe for lesser centrifugal force. Adopting the invention, driver fee and plenty of fuel oil is saved. In the process of fluxion, liquid film at two phases' interface will not break up to beget two phase liquids' blend.
Description
Affiliated technical field
The present invention relates to the fluid line conveying technology, relate in particular to a kind of rotating liquid ring pipeline delivery method and device thereof of high viscosity fluid.
Background technique
Oil comprises the viscous crude that resource potential is huge, is the modern most important energy.The development of petroleum industry is directly connected to various countries' process of industrialization, and the conveying of crude oil then is the pith of petroleum industry.Owing to line transportation is compared with other delivery method (transporting as train, automobile, oil carrier etc.) and is had obvious superiority to be developed rapidly on Technological Economy.
Crude oil has vicidity, and especially the crude oil of China belongs to paraffin stock more, has the high content of wax, height contains glue, high pour point, full-bodied characteristics, and these characteristics make crude oil will consume very big power when line transportation, can't manage defeated sometimes even at normal temperatures.Therefore the method for taking usually is a heating conveying method, this method also be present stage China to the main delivery method of the glutinous crude oil of height.In order to keep the oil temperature more than wax precipitation point, when carrying, long-distance pipe need consume a large amount of energy by the station heating, and simultaneously oily temperature rise meeting increases the evaporating loss of light ends in the crude oil, and environment is polluted.According to estimates, China every year can reach about 0.5% of pipeline oil transportation amount consuming fuel oil aspect the crude pipeline transportation, is equivalent to have the whole year 760000 tons of crude oil to be used to heat petroleum pipeline.Be not difficult to infer that the annual fuel oil that consumes aspect crude pipeline transportation in the whole world will be very surprising.
Liquid jacket transportation is that the liquid (as water) with low-viscosity forms pendular ring around the inner tube wall and the center portion that high viscosity crude oil is limited in pipeline flowed and a kind of technology of carrying.Because what directly contact with tube wall is thinlyfluid, thereby at normal temperatures, compare when sticking Crude Oil Transportation that resistance greatly reduces in the flow process with height.And be in the crude oil of tube hub, and how high no matter viscosity has, even be curdled appearance, all can be than carrying out line transportation under the low flow resistance.Obviously, the big advantage that utilization Liquid jacket transportation technology transports crude oil is exactly to save power cost greatly, and bigger advantage has been to save a large amount of fuel oil.So, aspect Crude Oil Transportation, the Liquid jacket transportation technology that can under the normal temperature low flow resistance, carry be subjected to people great attention and by a large amount of research.Yet, in the Liquid jacket transportation process, owing to have Rayleigh-Taylor (Rayleigh-Taylor) and Kelvin-Helmholtz (Kelvin-Hai Mu hertz) unstability, be the oil density at core place occur less than the density of water in the pendular ring eccentric flow and in flow process two-phase fluid liquid film is broken and cause the mixing of two-phase fluid at the interface, and the destruction that finally causes pendular ring, it is actual to make that this technology is difficult to directly apply to industry.Therefore, how to make pendular ring in movement process, keep the stable key issue that has just become the Liquid jacket transportation technology.
Summary of the invention
The object of the present invention is to provide a kind of rotating liquid ring pipeline delivery method and device thereof of high viscosity fluid, the bigger pendular ring of density is in around the inner tube wall all the time, and the less oil phase of density is in the pipeline middle part and carries owing to centrifugal force suffered in centrifugal field is less.
In order to achieve the above object, the technical solution used in the present invention is as follows:
One, the rotating liquid ring pipeline delivery method of high viscosity fluid
Employing makes pendular ring rotatablely move proal the generation simultaneously, producing centrifugal field by rotatablely moving is in around the inner tube wall the bigger pendular ring of density all the time, make pendular ring keep stable by rotatablely moving, the less oil phase of density is in the pipeline middle part owing to centrifugal force suffered in centrifugal field is less on the contrary, thereby high viscosity fluid is rotated the pendular ring line transportation.
Two, the rotating liquid ring pipeline feedway of high viscosity fluid, become the ring wet tank in first pump inserts, the rotation pendular ring synthesizer that phase difference is 180 ° of two spiral plates to be housed, the high viscosity fluid storage tank is managed in second pump inserts the logical high viscosity fluid that is contained in rotation pendular ring synthesizer center, and the outlet conduit of spiral plate is housed in the outlet termination of rotation pendular ring synthesizer.
The ratio 0.5: 1～0.9: 1 of the internal diameter of pipe and the internal diameter of outlet conduit in the logical high viscosity fluid, preferred 0.6: 1～0.8: 1; The ratio 0.4: 1～0.7: 1 of the internal diameter of pipe and the internal diameter of rotation pendular ring synthesizer in the logical high viscosity fluid, preferred 0.5: 1～0.6: 1.
The ratio of the spiral plate pitch of outlet conduit and the internal diameter of outlet conduit 2: 1～1: 2, preferred 1: 1; The ratio of the spiral plate thickness of outlet conduit and the internal diameter of outlet conduit 0.05: 1～0.3: 1, preferred 0.1: 1～0.2: 1.
The ratio of the spiral plate pitch of rotation pendular ring synthesizer and the internal diameter b of rotation pendular ring synthesizer 2: 1～1: 2, preferred 1: 1; Rotation pendular ring synthesizer the ratio 0.05: 1～0.3: 1 of spiral plate thickness and the internal diameter of rotation pendular ring synthesizer, preferred 0.1: 1～0.2: 1.
The present invention compares with background technique, the useful effect that has is: it adopts pendular ring is rotatablely moved proal the generation simultaneously, producing centrifugal field by rotatablely moving is in around the inner tube wall the bigger pendular ring of density all the time, the less oil phase of density is in the pipeline middle part owing to centrifugal force suffered in centrifugal field is less on the contrary, and high viscosity fluid is carried out line transportation.Save power cost greatly, economized a large amount of fuel oil.Liquid film can be not broken and cause the mixing of two-phase fluid at the interface for two-phase fluid in flow process.
Description of drawings
The invention will be further described below in conjunction with drawings and Examples.
Fig. 1 is a structural representation of the present invention;
Fig. 2 is a rotation pendular ring synthesizer structural representation of the present invention;
Fig. 3 is an outlet conduit structural representation of the present invention.
Embodiment
Employing makes pendular ring rotatablely move proal the generation simultaneously, producing centrifugal field by rotatablely moving is in around the inner tube wall the bigger pendular ring of density all the time, make pendular ring keep stable by rotatablely moving, the less oil phase of density is in the pipeline middle part owing to centrifugal force suffered in centrifugal field is less on the contrary, thereby high viscosity fluid is rotated the pendular ring line transportation.
As Fig. 1, Fig. 2, shown in Figure 3, the present invention includes into ring wet tank 1 and in first pump 3 inserts, the rotation pendular ring synthesizer 5 that phase difference is 180 ° of two spiral plates 5.1 is housed, high viscosity fluid storage tank 2 manages 5.2 in second pump 4 inserts the logical high viscosity fluid that is contained in rotation pendular ring synthesizer 5 centers, the outlet conduit 6 of spiral plate 6.1 is housed in the outlet termination of rotation pendular ring synthesizer 5.
The internal diameter a of pipe 5.2 is 0.5: 1～0.9: 1 with the ratio of the inner diameter d of outlet conduit 6 in the logical high viscosity fluid, preferred 0.6: 1～0.8: 1; The internal diameter a of pipe 5.2 is 0.4: 1～0.7: 1 with the ratio of the internal diameter b of rotation pendular ring synthesizer 5 in the logical high viscosity fluid, preferred 0.5: 1～0.6: 1.
The spiral plate 6.1 pitch c of outlet conduit 6 are 2: 1～1: 2 with the ratio of the inner diameter d of outlet conduit 6, preferred 1: 1; Spiral plate 6.1 thickness of outlet conduit 6 are 0.05: 1～0.3: 1 with the ratio of the internal diameter of outlet conduit 6, preferred 0.1: 1～0.2: 1.
The spiral plate 5.1 pitch e of rotation pendular ring synthesizer 5 are 2: 1～1: 2 with the ratio of the internal diameter b of rotation pendular ring synthesizer 5, preferred 1: 1; Rotation pendular ring synthesizer 5 the ratio of spiral plate 5.1 thickness and the internal diameter b of rotation pendular ring synthesizer 5 be 0.05: 1～0.3: 1, preferred 0.1: 1～0.2: 1.
High viscosity fluid is 10: 1～1: 10 with the ratio that becomes ring liquid volume flow, preferred 8: 2～6: 4.
Embodiment 1:
Water is carried high glutinous crude oil at normal temperatures for becoming to encircle liquid, and water is 3: 7 with the ratio of the volume flowrate of crude oil.The outlet conduit structural parameter: pitch is 1: 1 with the ratio of caliber; The wide ratio with caliber of spiral plate is 0.1: 1.Rotation pendular ring synthesizer structural parameter: the internal diameter of pipe is 0.75: 1 with the ratio of the internal diameter of outlet conduit in the logical high viscosity fluid; The internal diameter of pipe is 0.5: 1 with the ratio of the internal diameter of rotation pendular ring synthesizer in the logical high viscosity fluid.The fuel saving, also do not reduce transmitting power more than 81% except that not needing heating in crude oil during conveying.
Embodiment 2:
Water is carried high glutinous crude oil at normal temperatures for becoming to encircle liquid, and water is 2:8 with the ratio of the volume flowrate of crude oil.Spiral stream guidance apparatus structure parameter: pitch is 1: 1 with the ratio of caliber; The wide ratio with caliber of spiral plate is 0.07: 1.Rotation pendular ring synthesizer structural parameter: the internal diameter of pipe is 0.8: 1 with the ratio of the internal diameter of outlet conduit in the logical high viscosity fluid; The internal diameter of pipe is 0.6: 1 with the ratio of the internal diameter of rotation pendular ring synthesizer in the logical high viscosity fluid.The fuel saving, also do not reduce transmitting power more than 76% except that not needing heating in crude oil during conveying.
Claims (5)
1, a kind of rotating liquid ring pipeline delivery method of high viscosity fluid, it is characterized in that: adopt pendular ring is rotatablely moved proal the generation simultaneously, producing centrifugal field by rotatablely moving is in around the inner tube wall the bigger pendular ring of density all the time, make pendular ring keep stable by rotatablely moving, the less oil phase of density is in the pipeline middle part owing to centrifugal force suffered in centrifugal field is less on the contrary, thereby high viscosity fluid is rotated the pendular ring line transportation.
2, the device that is used for the rotating liquid ring pipeline delivery method of the described a kind of high viscosity fluid of claim 1, it is characterized in that: become ring wet tank (1) in first pump (3) inserts, the rotation pendular ring synthesizer (5) that phase difference is 180 ° two spiral plates (5.1) to be housed, high viscosity fluid storage tank (2) is pipe (5.2) in second pump (4) inserts the logical high viscosity fluid that is contained in rotation pendular ring synthesizer (5) center, and the outlet conduit (6) of spiral plate (6.1) is housed in the outlet termination of rotation pendular ring synthesizer (5).
3, the device of the rotating liquid ring pipeline delivery method of a kind of high viscosity fluid according to claim 2, it is characterized in that: the ratio of the internal diameter (a) of the logical interior pipe of high viscosity fluid (5.2) and the internal diameter (d) of outlet conduit (6) 0.5: 1～0.9: 1, preferred 0.6: 1～0.8: 1; The ratio of the internal diameter (b) of the internal diameter (a) of the logical interior pipe of high viscosity fluid (5.2) and rotation pendular ring synthesizer (5) 0.4: 1～0.7: 1, preferred 0.5: 1～0.6: 1.
4, the device of the rotating liquid ring pipeline delivery method of a kind of high viscosity fluid according to claim 2 is characterized in that: the ratio of spiral plate (6.1) pitch (c) of outlet conduit (6) and the internal diameter (d) of outlet conduit (6) 2: 1～1: 2, preferred 1: 1; The ratio of spiral plate (6.1) thickness of outlet conduit (6) and the internal diameter of outlet conduit (6) 0.05: 1～0.3: 1, preferred 0.1: 1～0.2: 1.
5, the device of the rotating liquid ring pipeline delivery method of a kind of high viscosity fluid according to claim 2, it is characterized in that: the ratio of the internal diameter (b) of spiral plate (5.1) pitch (e) of rotation pendular ring synthesizer (5) and rotation pendular ring synthesizer (5) 2: 1～1: 2, preferred 1: 1; Rotation pendular ring synthesizer (5) the ratio 0.05: 1～0.3: 1 of spiral plate (5.1) thickness and the internal diameter (b) of rotation pendular ring synthesizer (5), preferred 0.1: 1～0.2: 1.
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| Application Number | Priority Date | Filing Date | Title |
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| CN 200410018060 CN1258054C (en) | 2004-04-27 | 2004-04-27 | Rotating liquid ring pipeline delivery method and equipment for high viscosity fluid |
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| CN 200410018060 CN1258054C (en) | 2004-04-27 | 2004-04-27 | Rotating liquid ring pipeline delivery method and equipment for high viscosity fluid |
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| CN1570460A true CN1570460A (en) | 2005-01-26 |
| CN1258054C CN1258054C (en) | 2006-05-31 |
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100436932C (en) * | 2005-05-24 | 2008-11-26 | 辽河石油勘探局 | Dehydrated ultra thick oil pipeline transportation method and corollary arrangement |
| CN103159574A (en) * | 2011-12-19 | 2013-06-19 | 薛世忠 | Water ring injection device |
| CN105351751A (en) * | 2015-11-10 | 2016-02-24 | 中国石油大学(华东) | Liquid ring conveying system and method for high-thickness materials |
| CN105351750A (en) * | 2015-11-10 | 2016-02-24 | 中国石油大学(华东) | Liquid ring maintaining device used for liquid conveying |
| CN106640668A (en) * | 2016-11-09 | 2017-05-10 | 中国石油大学(华东) | Magnetic suspension water ring conveying pump |
| CN107270128A (en) * | 2017-05-17 | 2017-10-20 | 太仓液压元件有限公司 | A kind of length of high viscosity liquid is away from induction system and carrying method |
| CN108343839A (en) * | 2018-04-20 | 2018-07-31 | 郑州大学 | MHD cyclones based on water ring oil transportation |
| CN108343841A (en) * | 2018-04-20 | 2018-07-31 | 郑州大学 | MHD flow straighteners based on water ring oil transportation |
| CN108413253A (en) * | 2018-04-03 | 2018-08-17 | 巩长勇 | A kind of method of pipeline pug, pug recombiner and pug transport system |
-
2004
- 2004-04-27 CN CN 200410018060 patent/CN1258054C/en not_active Expired - Fee Related
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100436932C (en) * | 2005-05-24 | 2008-11-26 | 辽河石油勘探局 | Dehydrated ultra thick oil pipeline transportation method and corollary arrangement |
| CN103159574A (en) * | 2011-12-19 | 2013-06-19 | 薛世忠 | Water ring injection device |
| CN105351750B (en) * | 2015-11-10 | 2019-04-23 | 中国石油大学(华东) | Pendular ring for Liquid jacket transportation maintains device |
| CN105351750A (en) * | 2015-11-10 | 2016-02-24 | 中国石油大学(华东) | Liquid ring maintaining device used for liquid conveying |
| CN105351751A (en) * | 2015-11-10 | 2016-02-24 | 中国石油大学(华东) | Liquid ring conveying system and method for high-thickness materials |
| CN105351751B (en) * | 2015-11-10 | 2019-11-29 | 中国石油大学(华东) | Highly viscous substance Liquid jacket transportation system and method |
| CN106640668A (en) * | 2016-11-09 | 2017-05-10 | 中国石油大学(华东) | Magnetic suspension water ring conveying pump |
| CN107270128A (en) * | 2017-05-17 | 2017-10-20 | 太仓液压元件有限公司 | A kind of length of high viscosity liquid is away from induction system and carrying method |
| CN107270128B (en) * | 2017-05-17 | 2019-06-18 | 太仓液压元件有限公司 | A kind of the long-distance delivery system and delivery method of high viscosity liquid |
| CN108413253A (en) * | 2018-04-03 | 2018-08-17 | 巩长勇 | A kind of method of pipeline pug, pug recombiner and pug transport system |
| CN108343839A (en) * | 2018-04-20 | 2018-07-31 | 郑州大学 | MHD cyclones based on water ring oil transportation |
| CN108343841A (en) * | 2018-04-20 | 2018-07-31 | 郑州大学 | MHD flow straighteners based on water ring oil transportation |
| CN108343839B (en) * | 2018-04-20 | 2023-11-10 | 郑州大学 | MHD cyclone based on water ring oil transportation |
| CN108343841B (en) * | 2018-04-20 | 2023-11-10 | 郑州大学 | MHD current stabilizer based on water ring oil transportation |
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| CN1258054C (en) | 2006-05-31 |
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