CN211537281U - Fracturing fluid blending device - Google Patents
Fracturing fluid blending device Download PDFInfo
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- CN211537281U CN211537281U CN201922062638.9U CN201922062638U CN211537281U CN 211537281 U CN211537281 U CN 211537281U CN 201922062638 U CN201922062638 U CN 201922062638U CN 211537281 U CN211537281 U CN 211537281U
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Abstract
A fracturing fluid blending device. The continuous mixing device mainly solves the problems that the existing continuous mixing device for the on-site fracturing fluid has large volume, long time for reaching the viscosity for use and environmental pollution caused by adding a defoaming agent. The method is characterized in that: the powder tank comprises a powder tank A (601) and a powder tank B (602), the inlet of the powder tank is connected with a powder tank header pipe (17), the outlet of the powder tank is connected with a storage tank (12), the outlet of the storage tank (12) is connected with a mixer (8), the feed inlet of the mixer (8) is simultaneously connected with a water inlet pipe, the outlet of the mixer is connected with a tackifying device (7), the outlet of the tackifying device (7) is connected with a liquid collecting tank (19), and the liquid collecting tank (19) is connected with a sand mixing truck through a liquid discharge manifold (9); a spraying device (18) is arranged in the liquid collecting tank (19). The fracturing fluid blending device is small in size, the tackifying time is shortened, the use of a defoaming agent is avoided, the waste and the environmental pollution are avoided, the fracturing period of a single well is shortened, and the fracturing efficiency is improved.
Description
Technical Field
The utility model relates to an oil field, a fracturing fluid blending device specifically says so.
Background
The water conservancy fracturing technology has been developed for many years, and along with the progress of the fracturing technology, the water conservancy fracturing technology has higher requirements on fracturing equipment, not only has the requirements on discharge capacity and pressure continuously improved, but also has new height on continuous liquid injection quantity. At present, two main ways are available for continuous injection of fracturing fluid, the first way is mixing of common guar gum powder and water, the first way is to directly introduce the mixture into a relay tank for stirring and swelling after the mixing is finished, the stirring and swelling are generally carried out for 10-15 minutes, the viscosity of the fracturing fluid can reach the use viscosity, and in order to ensure the continuity, the time from the fracturing fluid to the outlet of a drainage manifold in the relay tank must be higher than 15 minutes to ensure the viscosity requirement, so that the tank body has large volume, the drainage manifold is long, the structure is complex, and the operation is complicated. The second mode is a mode of mixing modified instant guar gum with water by using an additive, and although the mode shortens the stirring swelling time, the use concentration can be reached within 3 minutes, and the equipment volume is reduced, in order to avoid generating a large amount of bubbles which seriously affect the pumping efficiency when the instant guar gum is mixed, a defoaming agent is used, so that the fracturing and mixing cost is greatly increased, and the environment is polluted.
SUMMERY OF THE UTILITY MODEL
In order to overcome current continuous blending unit of on-spot fracturing fluid bulky, viscosity reach use viscosity time long, add the defoaming agent and cause environmental pollution's not enough, the utility model provides a fracturing fluid blending unit, this fracturing fluid blending unit is small, has shortened the tackification time, avoids using the defoaming agent and avoids extravagant and polluted environment, shortens the fracturing cycle of single well, improves fracturing efficiency.
The technical scheme of the utility model is that: a fracturing fluid blending device comprises a skid-mounted base, wherein a motor, a storage tank and a powder tank are fixed on the skid-mounted base respectively, the powder tank comprises a powder tank A and a powder tank B, inlets of the powder tank A and the powder tank B are connected with a powder tank header pipe respectively, outlets of the powder tank A and the powder tank B are connected with the storage tank, an outlet of the storage tank is connected with a mixer through a spiral feeder, a feed inlet of the mixer is connected with a water inlet pipe simultaneously, an outlet of the mixer is connected with a tackifying device, an outlet of the tackifying device is connected with a liquid collecting tank, and the liquid collecting tank is connected with a sand mixer through a liquid discharge manifold; and a spraying device is arranged in the liquid collecting tank.
The powder tank A is provided with an inlet and an outlet which are respectively provided with a feeding electromagnetic valve A and a discharging electromagnetic valve A, and the powder tank B is provided with an inlet and an outlet which are respectively provided with a feeding electromagnetic valve B and a discharging electromagnetic valve B.
The spraying device is connected with the water inlet pipe.
The utility model discloses following beneficial effect has: by adopting the scheme, the device has the characteristics of simple structure and small volume, the total length is within 9 meters, the operation is convenient, the operation is safe and reliable, the material is sucked by using the negative pressure of the alternative powder tanks, the material is continuously supplemented, and the continuous mixing of the large-discharge fracturing fluid is realized; the viscosity of the common guar gum during mixing is quickly released, and the common guar gum is quickly tackified and hydrated, so that the prepared fracturing fluid can meet the requirements of preparation and injection; simultaneously, adopt spray set to carry out the defoaming, not only solved because a large amount of bubbles lead to the problem that pumping efficiency is low to also avoid the use of various additives such as defoaming agent, practice thrift the cost, safety ring protects, makes the fracturing cycle of single-port well shorten, improves fracturing operating efficiency greatly. The device not only has better practical application value, but also is approved by users from the integral design of the scheme to the operation and use process on the spot, and can be popularized to various oil and gas fields for use.
Drawings
Fig. 1 is a schematic view of the present invention;
FIG. 2 is a schematic view of the continuous operation of the powder tank;
fig. 3 is a schematic view of a rapid viscosity increasing device.
In the figure, 2-motor, 3-hydraulic oil tank, 4-transfer case, 5-hydraulic pump, 601-powder tank A, 602-powder tank B, 6011-feeding electromagnetic valve A, 6012-discharging electromagnetic valve A, 6021-feeding electromagnetic valve B, 6022-discharging electromagnetic valve B, 7-rapid tackifying device, 8-mixer, 9-feeding and discharging pipe manifold, 10-fuel oil tank, 11-screw feeder, 12-storage tank, 13-water inlet centrifugal pump, 14-liquid outlet centrifugal pump, 15-tackifying centrifugal pump, 16-feeding pump, 17-powder tank header pipe, 18-spraying device, 19-liquid collecting tank and 20-conveying pipe manifold.
Detailed Description
The present invention will be further explained with reference to the accompanying drawings:
as shown in fig. 1 to 3, a fracturing fluid blending device comprises a skid-mounted base, wherein a motor 2, a hydraulic oil tank 3, a storage tank 12, a fuel oil tank 10 and a powder tank are fixed on the skid-mounted base respectively, the fuel oil tank 10 provides fuel oil, the engine 2 provides power for the device, the power is transmitted to a hydraulic pump 5 through a transfer case 4, the whole device is provided with four hydraulic pumps, a water inlet centrifugal pump 13, a liquid outlet centrifugal pump 14, a viscosity increasing centrifugal pump 15 and a feeding pump 16 are driven by the hydraulic pump 5 respectively, and finally mechanical energy of the engine is transmitted to each pump through a hydraulic system.
The powder tank comprises a powder tank A601 and a powder tank B602, the inlets of the powder tank A601 and the powder tank B602 are respectively connected with a powder tank header pipe 17, the outlets of the powder tank A601 and the powder tank B602 are connected with a storage tank 12, the inlet and the outlet of the powder tank A601 are respectively provided with a feeding electromagnetic valve A6011 and a discharging electromagnetic valve A6012, and the inlet and the outlet of the powder tank B602 are respectively provided with a feeding electromagnetic valve B6021 and a discharging electromagnetic valve B6022. In operation, the powder tanks A601 and B602 operate alternately, thus ensuring the feeding continuity of the storage tank 12. The outlet of the storage tank 12 is connected with the mixer 8 through a screw feeder 11, and the guar gum powder in the storage tank 12 is conveyed into the mixer 8. The feed inlet of the mixer 8 is simultaneously connected with a water inlet pipe, and water is supplied into the mixer 8 through a water inlet centrifugal pump 13. The mixer 8 adopts a high-energy constant-pressure mixer, has the characteristics of high mixing energy and constant mixing pressure of clear water when the flow changes, and ensures that the high-energy solid and liquid of the guar gum powder and the water are uniform. The high-energy constant-pressure mixer 8 can generate enough negative pressure to suck materials, and has no environmental pollution. In the working process, the liquid pressure is equal to the control pressure of the mixer, and the control pressure of the mixer is a constant value, so that no matter which position the nozzle is positioned, the liquid pressure is constant, the continuously and uniformly sucked powder is instantly dissolved in the high-pressure mixed liquid, the mixing energy is high, and the phenomenon of powder in water is avoided. The control system adjusts the feeding speed of the spiral feeder 11 according to the water quantity change, realizes negative pressure feeding and metering feeding at the same time, forms working liquid meeting the proportion requirement, and finally realizes the control of the concentration of the mixed liquid. The outlet of the blender 8 is connected with a tackifying device 7 through a conveying manifold 20, the outlet of the tackifying device 7 is connected with a liquid collecting tank 19, the liquid collecting tank 19 is connected with a sand mixer through a liquid discharge manifold 9, a spraying device 18 is arranged in the liquid collecting tank 19, and the spraying device 18 is connected with a water inlet pipe.
When the fracturing fluid is mixed, starting the high-efficiency fracturing fluid mixing device, operating the feeding pump 16, as shown in fig. 2, generating negative pressure by the powder tank main pipe 17, and conveying the guar gum powder to the powder tank, wherein at the moment, the feeding electromagnetic valve A6011 is opened, the feeding electromagnetic valve B6021 is closed, the discharging electromagnetic valve A6012 is closed, the discharging electromagnetic valve B6022 is closed, after the powder tank A601 starts to suck the materials until the powder tank is full, the feeding electromagnetic valve A6011 is closed, the feeding electromagnetic valve B6021 is opened, the discharging electromagnetic valve A6012 is opened, the discharging electromagnetic valve B6022 is closed, the powder tank A601 starts to discharge, and the powder tank B602 starts to feed; after the powder tank B602 is in a full state, all the materials in the powder tank A601 fall into the storage tank 12, at the moment, the feeding electromagnetic valve A6011 is opened, the feeding electromagnetic valve B6021 is closed, the discharging electromagnetic valve A6012 is closed, the discharging electromagnetic valve B6022 is opened, and the powder tank A601 and the powder tank B602 alternately operate in feeding, blanking and feeding, so that the feeding continuity of the storage tank 12 and the material existence state are guaranteed. The spiral feeder 11 forwards pushes the guar gum powder in the storage tank 12 to the feed inlet of the mixer 8, the water inlet centrifugal pump 13 supplies water to the mixer 8, and the guar gum powder and the water are preliminarily mixed in the mixer 8 and then are conveyed to the rapid tackifying device 7 through the conveying manifold 20. The tackifying centrifugal pump 15 operates to enable the rapid tackifying device 7 to rotate at a high speed to operate to form a centrifugal force field, the relative speed between the guar gum powder and water in the mixed liquid is fully contacted under the action of the centrifugal force field to further realize high-efficiency mass transfer, and the mass transfer rate is improved by 2-3 orders of magnitude compared with the traditional stirring, so that the effects of rapid tackifying and hydration are achieved. The outlet of the tackifying device 7 is connected with a liquid collecting tank 19, the liquid collecting tank 19 is connected with a sand mixing truck through a liquid discharge manifold 9, a spraying device 18 is arranged in the liquid collecting tank 19, the spraying device 18 is connected with a branch of a water inlet pipe of a water inlet centrifugal pump 13, the water inlet centrifugal pump 13 operates to deliver liquid to the spraying device 18 at a high speed, the mixed liquid in the liquid collecting tank 19 is sprayed, bubbles generated in the process can be eliminated, the bubbles are discharged out of a container, the mixed liquid which is fully tackified and hydrated flows into the liquid discharge manifold 9, and a viscometer is arranged on the liquid discharge manifold 9 and can monitor the viscosity of the fracturing liquid in real time. Finally, the liquid outlet centrifugal pump 14 operates to distribute the fracturing fluid meeting the requirements to the fracturing blender truck through the supply and discharge manifold 9.
Claims (3)
1. The utility model provides a fracturing fluid blending device, includes the sled dress base, is fixed with motor (2), storage tank (12), powder jar on the sled dress base respectively, its characterized in that: the powder tank comprises a powder tank A (601) and a powder tank B (602), the inlets of the powder tank A (601) and the powder tank B (602) are respectively connected with a powder tank header pipe (17), the outlets of the powder tank A (601) and the powder tank B (602) are connected with a storage tank (12), the outlet of the storage tank (12) is connected with a mixer (8) through a spiral feeder (11), the feed inlet of the mixer (8) is simultaneously connected with a water inlet pipe, the outlet of the mixer (8) is connected with a tackifying device (7), the outlet of the tackifying device (7) is connected with a liquid collecting tank (19), and the liquid collecting tank (19) is connected with a sand mixing truck through a liquid discharge manifold (9); a spraying device (18) is arranged in the liquid collecting tank (19).
2. The fracturing fluid compounding assembly of claim 1, wherein: the powder tank A (601) is provided with a feeding electromagnetic valve A (6011) and a discharging electromagnetic valve A (6012) at the inlet and the outlet respectively, and the powder tank B (602) is provided with a feeding electromagnetic valve B (6021) and a discharging electromagnetic valve B (6022) at the inlet and the outlet respectively.
3. The fracturing fluid blending assembly of claim 2, wherein: the spraying device (18) is connected with the water inlet pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922062638.9U CN211537281U (en) | 2019-11-26 | 2019-11-26 | Fracturing fluid blending device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922062638.9U CN211537281U (en) | 2019-11-26 | 2019-11-26 | Fracturing fluid blending device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN211537281U true CN211537281U (en) | 2020-09-22 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201922062638.9U Active CN211537281U (en) | 2019-11-26 | 2019-11-26 | Fracturing fluid blending device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN211537281U (en) |
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2019
- 2019-11-26 CN CN201922062638.9U patent/CN211537281U/en active Active
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210827 Address after: 163453 Heilongjiang Province, Daqing City Ranghulu District No. 263 South Central Avenue Patentee after: DAQING PETROLEUM ADMINISTRATION Co.,Ltd. Patentee after: CHINA NATIONAL PETROLEUM Corp. Address before: 163453 Heilongjiang Province, Daqing City Ranghulu District No. 263 South Central Avenue Patentee before: DAQING PETROLEUM ADMINISTRATION Co.,Ltd. |
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| TR01 | Transfer of patent right |