CN218762712U - Ground cold transportation device for high-condensation and high-viscosity crude oil - Google Patents
Ground cold transportation device for high-condensation and high-viscosity crude oil Download PDFInfo
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- CN218762712U CN218762712U CN202222340519.7U CN202222340519U CN218762712U CN 218762712 U CN218762712 U CN 218762712U CN 202222340519 U CN202222340519 U CN 202222340519U CN 218762712 U CN218762712 U CN 218762712U
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Abstract
The utility model discloses a high congeals high viscous crude oil ground cold transfer device, wherein, include: the barrel, the inside of barrel is by the left to by having set gradually lower clutch, feed liquor divertor, fin formula high frequency oscillation mixing phase ware, self-excited pulse atomizer, stranded efflux generator, supersonic generator, multistage turbine mixing phase ware and top connection, and the one end of self-excited pulse atomizer is provided with the feed liquor nozzle, the middle part of self-excited pulse atomizer is provided with middle sleeve, middle sleeve's one end is provided with out the liquid nozzle, the other end of self-excited pulse atomizer is provided with fixation nut. Through the structure, a plurality of processing devices are matched with one another, the operation is simple, the efficiency is high, the energy is saved, the environment is protected, the production cost is greatly saved, and the economic benefit is improved.
Description
Technical Field
The utility model relates to a defeated technical field of crude oil ground collection, in particular to high congealing high viscous crude oil ground cold transportation device.
Background
The basic physical properties of the high pour point oil are that the freezing point is higher than 35 ℃, and the wax content is more than 30 percent, the production of the high pour point and high viscosity crude oil brings great challenges to the ground gathering and transportation process technology, a great amount of scientific research strength and funds are invested for many years for carrying out attack and customs research, a great amount of scientific research achievements are obtained and implemented, and the application effect is obvious.
At present, the prior art has the defects of complex process, large investment, high energy consumption and high operation cost during working; meanwhile, the corrosion to equipment, the increase of running load, the environmental pollution, the waste of energy and the waste of precious rare resources exist.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a high congealing high viscous crude oil ground cold transportation device solves among the prior art complicated, the investment of technology is big, the energy consumption is high, the high technical problem of operating cost when carrying high congealing high viscous crude oil.
To achieve the above object, there is provided a ground cold transportation device for highly condensed and highly viscous crude oil, comprising:
the cooling device comprises a cylinder body, wherein a lower connector, a liquid inlet flow guider, a fin type high-frequency oscillation phase mixer, a self-excitation pulse atomizer, a multi-strand jet generator, an ultrasonic generator, a multi-stage turbine phase mixer and an upper connector are sequentially arranged in the cylinder body from left to right, a plurality of processing devices are mutually matched to replace the traditional process technologies of heating, water mixing, medicine adding, strong magnetism and the like, so that the cooling transportation of high-condensation and high-viscosity crude oil is realized, and the tool is simple to operate, efficient, energy-saving, environment-friendly and the like, so that the production cost is greatly saved, and the economic benefit is improved;
a liquid inlet nozzle is arranged at one end of the self-excited pulse atomizer, a middle sleeve is arranged in the middle of the self-excited pulse atomizer, a liquid outlet nozzle is arranged at one end of the middle sleeve, a fixing nut is arranged at the other end of the self-excited pulse atomizer, fluid is discharged from the self-excited liquid outlet nozzle by the self-excited pulse atomizer to form pulse oscillation liquid flow, and the effects of flow state change and phase mixing are realized;
the middle part of multistage turbine ware of mixing with phase is provided with the dabber, the both ends of multistage turbine ware of mixing with phase are provided with closure plate and lower closure plate respectively, the outside of multistage turbine ware of mixing with phase is provided with the casing, the inner wall of casing is provided with the spacer bush, the middle part interval of multistage turbine ware of mixing with phase is provided with a plurality of stator and rotor, two all be provided with slide bearing between rotor and the dabber, the one end of multistage turbine ware of mixing with phase is provided with the nut, utilizes multistage turbine ware turbine to constitute an elementary level by a set of driving wheel and a set of fixed wheel, and when fluid flow passed through an elementary level, inside pressure and temperature all can rise, and oil gas water three-phase flow passes through a plurality of elementary levels, and inside pressure and temperature can rise by a wide margin, and simultaneously under the combined action of centrifugal force and border impact wave, each component was by the very intensive dispersion, opacification, made wax scale molecular group and molecule be shielded and cladding by heterogeneous phase, made it lose the gathering condition.
According to the ground cold transportation device for the high-condensation and high-viscosity crude oil, the fin type high-frequency oscillation phase mixer is composed of an overflow plate and three guide plates, a first sleeve is arranged outside the fin type high-frequency oscillation phase mixer, and when fluid flows through a guide plate of the fin type high-frequency oscillation phase mixer, the segregation and segregation states of wax crystals or dirt crystals are eliminated in a mode of dispersing wax molecules or wax crystal clusters and dirt crystal clusters.
According to the high-condensation high-viscosity crude oil ground cold transfer device, a sealing rubber ring is arranged at the joint of the lower joint and the liquid inlet fluid director, and is used for guaranteeing the sealing performance between equipment.
According to the ground cold transportation device for the high-condensation and high-viscosity crude oil, a second sleeve and a third sleeve are sequentially arranged between the multi-strand jet generator and the ultrasonic generator.
According to the high-condensation high-viscosity crude oil ground cold conveying device, the first sleeve, the second sleeve and the third sleeve are located inside the cylinder body, and the outer diameters of the first sleeve, the second sleeve and the third sleeve are matched with the inner diameter of the cylinder body.
According to the high-condensation high-viscosity crude oil ground cold transportation device, the lower joint and the upper joint are respectively positioned at two ends of the cylinder body.
According to the high-condensation high-viscosity crude oil ground cold conveying device, one end of the second sleeve is in threaded connection with one end of the third sleeve, an external thread is arranged at one end of the third sleeve, an internal thread is arranged at one end of the second sleeve, and therefore the service life of equipment is guaranteed in order to ensure the pressure difference bearing capacity of the whole set of tool.
Additional aspects and advantages of the invention will be set forth in part in the description which follows and, in part, will be obvious from the description, or may be learned by practice of the invention.
Drawings
The present invention will be further described with reference to the accompanying drawings and examples;
FIG. 1 is a sectional view of the ground cold transportation device for high-coagulation and high-viscosity crude oil of the present invention;
FIG. 2 is a structural diagram of the self-excited pulse atomizer of the ground cold transportation device for high-coagulation and high-viscosity crude oil of the present invention;
FIG. 3 is a structural diagram of a liquid inlet flow guider of the ground cold transportation device for high-condensation and high-viscosity crude oil of the utility model;
FIG. 4 is a structural diagram of an ultrasonic generator of the ground cold transportation device for high-coagulation and high-viscosity crude oil of the utility model;
FIG. 5 is a structural diagram of a finned high-frequency oscillation phase mixer of the ground cold transportation device for high-coagulation and high-viscosity crude oil of the utility model;
FIG. 6 is a structure diagram of a multi-stage turbine phase mixer of the ground cold transportation device for high-condensation and high-viscosity crude oil of the present invention;
fig. 7 is a structure diagram of a multi-strand jet generator of the ground cold transportation device for high-condensation and high-viscosity crude oil of the present invention.
Illustration of the drawings:
1. a lower joint; 2. sealing the rubber ring; 3. a liquid inlet flow guider; 4. a finned high-frequency oscillation phase mixer; 5. a first sleeve; 6. a self-excited pulse atomizer; 7. a barrel; 8. a multi-strand jet generator; 9. a second sleeve; 10. a third sleeve; 11. an ultrasonic generator; 12. a multi-stage turbine phase mixer; 13. an upper joint; 14. an overflow plate; 15. a guide piece; 16. a liquid inlet nozzle; 17. an intermediate sleeve; 18. a liquid outlet nozzle; 19. fixing a nut; 20. an upper blocking plate; 21. a stator; 22. a rotor; 23. a sliding bearing; 24. a housing; 25. a mandrel; 26. a spacer sleeve; 27. a lower blocking plate; 28. and a nut.
Detailed Description
This section will describe in detail the embodiments of the present invention, preferred embodiments of the present invention are shown in the attached drawings, which are used to supplement the description of the text part of the specification with figures, so that one can intuitively and vividly understand each technical feature and the whole technical solution of the present invention, but they cannot be understood as the limitation of the protection scope of the present invention.
Referring to fig. 1-7, the embodiment of the utility model provides a high congealing high viscous crude oil ground cold transportation device, it includes:
the device comprises a cylinder body 7, wherein a lower connector 1, a liquid inlet fluid director 3, a fin type high-frequency oscillation phase mixer 4, a self-excited pulse atomizer 6, a multi-jet flow generator 8, an ultrasonic generator 11, a multi-stage turbine phase mixer 12 and an upper connector 13 are sequentially arranged in the cylinder body 7 from left to right, the liquid inlet fluid director 3 enables formation produced liquid to enter the fluid director, firstly, fluid impacts a dome of the fluid director, impact flow reversely flows to enter a guide channel, the multi-jet flow is sprayed out from the channel, and a rapid turbulent flow is formed in a cavity above the fluid director, so that the oil, gas and water effluent is subjected to primary phase mixing, the multi-jet flow generator 8 adopts a stamping jet engine principle to change oil, gas and water three-phase flow into multi-jet flow, the multi-jet flow is focused on one point after being sprayed out from a pore channel, and simultaneously, the various components in the three-phase flow are completely atomized, namely dispersed, so that the 'bubble flow' of the oil, gas and water is realized, the ultrasonic generator 11, the fluid flows through a guide plate of the ultrasonic generator 11, the fluid impacts a cantilever beam vibrating piece of the ultrasonic generator 11, and the vibrating piece of the vibrating piece;
a liquid inlet nozzle 16 is arranged at one end of the self-excited pulse atomizer 6, an intermediate sleeve 17 is arranged in the middle of the self-excited pulse atomizer 6, a liquid outlet nozzle 18 is arranged at one end of the intermediate sleeve 17, a fixing nut 19 is arranged at the other end of the self-excited pulse atomizer 6, the fixing nut 19 is positioned inside the cylinder body 7, and the outer part of the fixing nut 19 is in threaded connection with the inner wall of the cylinder body 7;
the middle part of multistage turbine phase mixer 12 is provided with dabber 25, the both ends of multistage turbine phase mixer 12 are provided with closure plate 20 and lower closure plate 27 respectively, be used for fixing a position stator 21 and rotor 22, avoid taking place to drop, the outside of multistage turbine phase mixer 12 is provided with casing 24, the inner wall of casing 24 is provided with spacer 26, the middle part interval of multistage turbine phase mixer 12 is provided with a plurality of stator 21 and rotor 22, stator 21 and rotor 22 link to each other the setting, all be provided with slide bearing 23 between two rotors 22 and the dabber 25, the one end of multistage turbine phase mixer 12 is provided with nut 28.
The finned high-frequency oscillation phase mixer 4 is composed of an overflow plate 14 and guide pieces 15, a first sleeve 5 is arranged outside the finned high-frequency oscillation phase mixer 4, the finned high-frequency oscillation phase mixer 4 is located in the middle of the first sleeve 5, the number of the finned high-frequency oscillation phase mixer 4 is three, a sealing rubber ring 2 is arranged at the joint of a lower connector 1 and a liquid inlet fluid director 3, a second sleeve 9 and a third sleeve 10 are sequentially arranged between a multi-strand jet generator 8 and an ultrasonic generator 11, the first sleeve 5, the second sleeve 9 and the third sleeve 10 are located inside a barrel 7, the outer diameters of the first sleeve 5, the second sleeve 9 and the third sleeve 10 are matched with the inner diameter of the barrel 7, the lower connector 1 and an upper connector 13 are located at two ends of the barrel 7 respectively, one end of the second sleeve 9 is in threaded connection with one end of the third sleeve 10, one end of the third sleeve 10 is provided with external threads, and one end of the second sleeve 9 is provided with internal threads.
The working principle is as follows: in use the utility model discloses the time, earlier with lower clutch 1, sealed rubber ring 2, feed liquor divertor 3, fin formula high-frequency oscillation phase blender 4, first sleeve 5, self-excited pulse atomizer 6, stranded efflux generator 8, second sleeve 9, third sleeve 10, supersonic generator 11, multistage turbine phase blender 12 and top connection 13 are installed in proper order in the inside of barrel 7, be connected lower clutch 1 with the one end of conveyer pipe, top connection 13 is connected with the one end of discharging pipe, install sealed rubber ring 2 respectively at lower clutch 1 and top connection 13 tip and realize the sealed with barrel 7, and be connected second sleeve 9 and third sleeve 10 through internal thread and external screw thread, make second sleeve 9 and third sleeve 10 can bear the pressure differential of instrument, avoid receiving the damage, ensure the normal use of instrument.
The embodiments of the present invention have been described in detail with reference to the accompanying drawings, but the present invention is not limited to the above embodiments, and various changes can be made without departing from the spirit of the present invention within the knowledge of those skilled in the art.
Claims (7)
1. High congealing high viscous crude oil ground cold transportation device, its characterized in that includes:
the device comprises a cylinder body (7), wherein a lower connector (1), a liquid inlet fluid director (3), a fin type high-frequency oscillation phase mixer (4), a self-excitation pulse atomizer (6), a multi-strand jet generator (8), an ultrasonic generator (11), a multi-stage turbine phase mixer (12) and an upper connector (13) are sequentially arranged in the cylinder body (7) from left to right;
a liquid inlet nozzle (16) is arranged at one end of the self-excited pulse atomizer (6), a middle sleeve (17) is arranged in the middle of the self-excited pulse atomizer (6), a liquid outlet nozzle (18) is arranged at one end of the middle sleeve (17), and a fixing nut (19) is arranged at the other end of the self-excited pulse atomizer (6);
the middle part of multistage turbine phase blender (12) is provided with dabber (25), the both ends of multistage turbine phase blender (12) are provided with closure plate (20) and lower closure plate (27) respectively, the outside of multistage turbine phase blender (12) is provided with casing (24), the inner wall of casing (24) is provided with spacer sleeve (26), the middle part interval of multistage turbine phase blender (12) is provided with a plurality of stator (21) and rotor (22), two all be provided with slide bearing (23) between rotor (22) and dabber (25), the one end of multistage turbine phase blender (12) is provided with nut (28).
2. The ground cold transportation device for the high-coagulation high-viscosity crude oil according to claim 1, characterized in that the finned high-frequency oscillation phase mixer (4) consists of a flow passing plate (14) and a guide plate (15), a first sleeve (5) is arranged outside the finned high-frequency oscillation phase mixer (4), and the finned high-frequency oscillation phase mixer (4) is positioned in the middle of the first sleeve (5) and is three in number.
3. The ground cold transportation device for high-coagulation and high-viscosity crude oil as claimed in claim 1, wherein a sealing rubber ring (2) is arranged at the joint of the lower joint (1) and the liquid inlet flow guider (3).
4. The ground cold transportation device for high-coagulation and high-viscosity crude oil as claimed in claim 2, wherein a second sleeve (9) and a third sleeve (10) are sequentially arranged between the multi-jet generator (8) and the ultrasonic generator (11).
5. The ground cold transportation device for high-coagulation and high-viscosity crude oil is characterized in that the first sleeve (5), the second sleeve (9) and the third sleeve (10) are all positioned inside the cylinder body (7), and the outer diameters of the first sleeve (5), the second sleeve (9) and the third sleeve (10) are matched with the inner diameter of the cylinder body (7).
6. The ground cold transportation device for high-coagulation and high-viscosity crude oil as claimed in claim 1, wherein the lower joint (1) and the upper joint (13) are respectively positioned at two ends of the cylinder body (7).
7. The ground cold transfer device for high-coagulation and high-viscosity crude oil according to claim 4, characterized in that one end of the second sleeve (9) is in threaded connection with one end of the third sleeve (10), one end of the third sleeve (10) is provided with external threads, and one end of the second sleeve (9) is provided with internal threads.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222340519.7U CN218762712U (en) | 2022-09-02 | 2022-09-02 | Ground cold transportation device for high-condensation and high-viscosity crude oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222340519.7U CN218762712U (en) | 2022-09-02 | 2022-09-02 | Ground cold transportation device for high-condensation and high-viscosity crude oil |
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| Publication Number | Publication Date |
|---|---|
| CN218762712U true CN218762712U (en) | 2023-03-28 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202222340519.7U Active CN218762712U (en) | 2022-09-02 | 2022-09-02 | Ground cold transportation device for high-condensation and high-viscosity crude oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN218762712U (en) |
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2022
- 2022-09-02 CN CN202222340519.7U patent/CN218762712U/en active Active
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