CN114198057A - Paraffin removal vehicle - Google Patents

Paraffin removal vehicle Download PDF

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Publication number
CN114198057A
CN114198057A CN202111315426.2A CN202111315426A CN114198057A CN 114198057 A CN114198057 A CN 114198057A CN 202111315426 A CN202111315426 A CN 202111315426A CN 114198057 A CN114198057 A CN 114198057A
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China
Prior art keywords
pipe
chassis
branch pipe
pressurizing device
vehicle
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Granted
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CN202111315426.2A
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Chinese (zh)
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CN114198057B (en
Inventor
袁圣杰
刘元良
刘有仓
李平
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Yantai Jereh Petroleum Equipment and Technologies Co Ltd
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Yantai Jereh Petroleum Equipment and Technologies Co Ltd
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Application filed by Yantai Jereh Petroleum Equipment and Technologies Co Ltd filed Critical Yantai Jereh Petroleum Equipment and Technologies Co Ltd
Priority to CN202111315426.2A priority Critical patent/CN114198057B/en
Priority to CN202310934788.2A priority patent/CN116856883A/en
Publication of CN114198057A publication Critical patent/CN114198057A/en
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Publication of CN114198057B publication Critical patent/CN114198057B/en
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    • EFIXED CONSTRUCTIONS
    • E21EARTH OR ROCK DRILLING; MINING
    • E21BEARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B37/00Methods or apparatus for cleaning boreholes or wells
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B60VEHICLES IN GENERAL
    • B60PVEHICLES ADAPTED FOR LOAD TRANSPORTATION OR TO TRANSPORT, TO CARRY, OR TO COMPRISE SPECIAL LOADS OR OBJECTS
    • B60P3/00Vehicles adapted to transport, to carry or to comprise special loads or objects
    • EFIXED CONSTRUCTIONS
    • E21EARTH OR ROCK DRILLING; MINING
    • E21BEARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B36/00Heating, cooling or insulating arrangements for boreholes or wells, e.g. for use in permafrost zones
    • E21B36/005Heater surrounding production tube
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/56Reuse, recycling or recovery technologies of vehicles

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  • Engineering & Computer Science (AREA)
  • Geology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Mining & Mineral Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Fluid Mechanics (AREA)
  • Physics & Mathematics (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Transportation (AREA)
  • Mechanical Engineering (AREA)
  • Loading And Unloading Of Fuel Tanks Or Ships (AREA)
  • Vehicle Cleaning, Maintenance, Repair, Refitting, And Outriggers (AREA)

Abstract

The application discloses paraffin removal vehicle relates to oil field production increasing operation well technical field. A paraffin removal vehicle comprises: the device comprises a chassis, a heating device, a first pressurizing device and a manifold system; the heating device and the first pressurizing device are respectively arranged on the chassis; the manifold system comprises a liquid inlet pipe, a liquid outlet pipe and a first connecting pipe, the heating device is connected with the first pressurizing device through the first connecting pipe, the liquid inlet pipe is connected with the heating device, and the liquid outlet pipe is connected with the first pressurizing device. The problem that the high-pressure fluid medium is difficult to meet the high-pressure requirement due to the limitation of the boiler pressure can be at least relieved.

Description

Paraffin removal vehicle
Technical Field
The application belongs to the technical field of oilfield production increasing operation wells, and particularly relates to a paraffin removal vehicle.
Background
When some current hot oil paraffin removal vehicles are used, liquid is generally pressurized to high pressure through a plunger pump, then the liquid is conveyed to a boiler to be heated, and finally the high-temperature and high-pressure liquid is used for well washing paraffin removal operation.
However, some current hot oil paraffin removal trucks have the following problems:
1) the maximum working pressure is generally 20Mpa due to the limitation of a boiler, and the requirement of high-pressure operation working conditions of some deep wells is difficult to meet;
2) the working condition is single, only high-pressure hot water can be generated and injected into the well for paraffin removal and blockage removal;
3) the self-contained water tank is generally in a closed form and can only be used for containing single liquid such as water or crude oil and the like;
4) the low-pressure industrial working condition cannot be realized, and the liquid suction capacity of the plunger pump is insufficient when the plunger pump works in some deep wells, so that the plunger pump can suck air for a long time, and the service life of the plunger pump is influenced in the past;
5) after the well washing operation is finished, residual liquid is stored in the coiled tubing, so that the inner wall of the coiled tubing is corroded, and the service life of the coiled tubing is influenced;
6) when operating equipment in some severe environments for operation, operation is inconvenient, physical and psychological health of operators is affected, and the like.
Disclosure of Invention
It is an object of embodiments of the present application to provide a paraffin removal vehicle, which can solve at least one of the above-mentioned problems.
In order to solve the technical problem, the present application is implemented as follows:
the embodiment of the application provides a paraffin removal car, this paraffin removal car includes: the device comprises a chassis, a heating device, a first pressurizing device and a manifold system;
the heating device and the first pressurizing device are respectively arranged on the chassis;
the manifold system comprises a liquid inlet pipe, a liquid outlet pipe and a first connecting pipe, the heating device is connected with the first pressurizing device through the first connecting pipe, the liquid inlet pipe is connected with the heating device, and the liquid outlet pipe is connected with the first pressurizing device.
In the embodiment of the application, the fluid medium flows through the liquid inlet pipe, the heating device, the first connecting pipe, the first pressurizing device and the liquid outlet pipe in sequence, when flowing through the heating device, the fluid medium is heated by the heating device to reach the required temperature, and when flowing through the first pressurizing device, the fluid medium is pressurized by the first pressurizing device to reach the required pressure, so that the high-temperature and high-pressure fluid medium can flow out through the liquid outlet pipe, and the paraffin removal and blockage removal requirements can be met. In addition, the wax removal vehicle can freely move through the vehicle chassis, so that the operation place can be conveniently changed. Based on above-mentioned setting, the paraffin car in this application can effectively alleviate high-pressure fluid medium and flow into in the boiler and receive boiler pressure's restriction to can satisfy the operation operating mode requirement of higher pressure, and can remove anytime and anywhere, improve the operating efficiency.
Drawings
FIG. 1 is a schematic structural view of a paraffin removal truck disclosed in an embodiment of the present application;
FIG. 2 is a schematic view of a combination of a liquid inlet pipe, a heating device, a first connecting pipe, a first pressurizing device and a liquid outlet pipe disclosed in the embodiment of the present application;
fig. 3 is a combined schematic view of structures of a liquid inlet pipe, a second pressurizing device, a heating device, a first connecting pipe, a first pressurizing device, a liquid outlet pipe and the like disclosed in the embodiment of the application;
fig. 4 is a combined schematic view of structures of a liquid inlet pipe, a second pressurizing device, a metering container, a second connecting pipe, a heating device, a first connecting pipe, a first pressurizing device, a liquid outlet pipe and the like, disclosed in the embodiment of the present application;
fig. 5 is a schematic diagram of the vehicle chassis outputting power through a transmission device according to the embodiment of the application.
Description of reference numerals:
100-vehicle chassis; 110-chassis engine; 120-chassis gearbox;
200-a heating device;
300-a first pressurizing device;
400-a second pressurizing means;
500-a metering container;
600-an air compression device;
700-a control room;
800-a transmission; 810-disconnected shaft power take-off transfer case; 821-a first transmission shaft; 822-a second drive shaft; 823-third Transmission shaft; 824-a fourth drive shaft; 830-an auxiliary gearbox; 841-first power takeoff; 842-a second power take-off; 851-a first hydraulic pump; 852-a second hydraulic pump; 861-a first motor; 862-a second motor; 863-a third motor; 864-fourth motor;
910-a liquid inlet pipe; 920-a liquid outlet pipe; 930 — a first connection pipe; 940-a second connecting tube; 950-a first branch pipe; 960-a second branch pipe; 970-third branch pipe; 980-a fourth branch pipe; 990-fifth branch pipe.
Detailed Description
The technical solutions in the embodiments of the present application will be clearly and completely described below with reference to the drawings in the embodiments of the present application, and it is obvious that the described embodiments are some, but not all, embodiments of the present application. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present application.
The terms first, second and the like in the description and in the claims of the present application are used for distinguishing between similar elements and not necessarily for describing a particular sequential or chronological order. It will be appreciated that the data so used may be interchanged under appropriate circumstances such that embodiments of the application may be practiced in sequences other than those illustrated or described herein, and that the terms "first," "second," and the like are generally used herein in a generic sense and do not limit the number of terms, e.g., the first term can be one or more than one. In addition, "and/or" in the specification and claims means at least one of connected objects, a character "/" generally means that a preceding and succeeding related objects are in an "or" relationship.
The embodiments of the present application are described in detail below with reference to the accompanying drawings through specific embodiments and application scenarios thereof.
Referring to fig. 1 to 5, an embodiment of the present application discloses a paraffin removal vehicle, which can be applied to a well-flushing paraffin removal operation. The disclosed paraffin removal truck includes a truck chassis 100, a heating device 200, a first pressurizing device 300, and a manifold system.
The chassis 100 is a base mounting part of the paraffin removal truck, and can provide a mounting base for the heating device 200, the first pressurizing device 300, the manifold system and the like, and the chassis 100 can also be used for enabling the paraffin removal truck to move to change the operation place. Alternatively, the vehicle chassis 100 may be fuel powered, electrically powered, or a hybrid fuel and electric drive. Alternatively, the heating device 200 and the first pressurizing device 300 are respectively disposed on the chassis 100, and the chassis 100 can carry the heating device 200, the first pressurizing device 300 and other components to travel, so as to perform work on different places.
Manifold systems are used to connect components and to transport fluid media. The manifold system comprises a liquid inlet pipe 910, a liquid outlet pipe 920 and a first connecting pipe 930, wherein the liquid inlet pipe 910 is connected with the heating device 200, the heating device 200 and the first pressurizing device 300 are connected through the first connecting pipe 930, and the liquid outlet pipe 920 is connected with the first pressurizing device 300. Thus, the liquid inlet pipe 910, the heating apparatus 200, the first connecting pipe 930, the first pressurizing apparatus 300, and the liquid outlet pipe 920 are connected in sequence along the flowing direction of the fluid medium, respectively. Based on this, the fluid medium may flow into the heating device 200 through the liquid inlet pipe 910, and the fluid medium is heated by the heating device 200 to reach a preset temperature, and then the heated fluid medium flows into the first pressurizing device 300 through the first connecting pipe 930, and is pressurized by the first pressurizing device 300 to reach a preset pressure, and then the pressurized fluid flows out through the liquid outlet pipe 920, so that the fluid medium with high temperature and high pressure is injected into the well to realize paraffin removal operation, and at the same time, the blockage removal operation may also be realized.
Based on the above arrangement, in the embodiment of the present application, the fluid medium is preferentially heated and then pressurized, so that the high-pressure fluid medium formed after pressurization is effectively prevented from flowing into the heating device 200, and therefore, the pressure of the fluid medium is not limited by the heating device 200, so that the fluid medium can reach a higher pressure, and the requirement of the deep well for the higher pressure of the fluid medium is met. In addition, the wax removal vehicle can freely move through the vehicle chassis 100, and operations in different places can be realized, so that the scheduling time can be saved, and the operation efficiency can be improved.
Referring to fig. 2, in some embodiments, the manifold system further includes a first branch pipe 950, one end of the first branch pipe 950 being connected to the first connection pipe 930, and the other end of the first branch pipe 950 being connected to the outlet pipe 920. Based on this, fluid medium can flow into through feed liquor pipe 910 to flow to heating device 200 and heat, in order to reach preset temperature, and then the high temperature fluid medium that passes through the heating flows to drain pipe 920, and flows out through drain pipe 920, thereby can be used to the cleaning operation of ground pipeline and equipment.
It should be noted here that the above process can produce high temperature liquid, and the high temperature liquid is not pressurized and thus is not used for injecting into a well to perform paraffin removal and blockage removal operation, but rather, the high temperature liquid is produced so as to be used for cleaning some components (such as ground pipelines, equipment and the like) and thus ensure the cleanness of the components. In addition, in order to switch the flow path of the fluid medium, control valves may be provided on the side of the first connection pipe 930 near the first pressurizing means 300 and on the first branch pipe 950, respectively, in which case the on/off of the side of the first connection pipe 930 near the first pressurizing means 300 and the on/off of the first branch pipe 950 may be controlled by the control valves, respectively.
Referring to fig. 3, in some embodiments, the paraffin removal truck may further include a second pressing device 400, and the second pressing device 400 is disposed on the truck chassis 100 and supported and loaded by the truck chassis 100. The second pressurizing device 400 is disposed on the liquid inlet pipe 910. Based on this, the second pressurizing device 400 is located at the upstream of the heating device 200, so that the fluid medium pressurized by the second pressurizing device 400 flows into the heating device 200, and then flows through the first pressurizing device 300 to be pressurized for the second time, so that the fluid medium reaches a higher pressure.
In view of the fact that the heating device 200 itself is not subjected to too high a pressure, the second pressurizing device 400 may be a low-pressure pressurizing device. Alternatively, the second pressurizing means 400 may be a centrifugal pump. Based on this, can realize that the low pressure supplies liquid operating mode demand, and can cooperate with first pressure device 300, effectively alleviate the not enough problem of first pressure device 300 imbibition ability to guaranteed that first pressure device 300 can not appear the phenomenon of resorption, prolonged first pressure device 300's life.
Based on the above arrangement, the fluid medium flows into the second pressurizing device 400 through the liquid inlet pipe 910, and is pressurized for the first time, so that the fluid medium has a certain pressure, and the fluid medium pressurized for the first time flows into the heating device 200 to be heated, and then the heated fluid medium flows into the first pressurizing device 300 through the first connecting pipe 930 to be pressurized for the second time, so as to obtain a high-pressure fluid medium.
Referring to fig. 3, in some embodiments, the manifold system may further include a second branch pipe 960, one end of the second branch pipe 960 is connected to the liquid inlet pipe 910, a junction of the second branch pipe 960 and the liquid inlet pipe 910 is located between the second pressurizing device 400 and the heating device 200, and the other end of the second branch pipe 960 is connected to the first connecting pipe 930. Based on this, the fluid medium that is primarily pressurized by the second pressurization device 400 may also flow to the first connection pipe 930 through the second branch pipe 960, and then flow into the first pressurization device 300 for secondary pressurization, and finally flow out through the outlet pipe 920.
Based on the above arrangement, the high-pressure fluid medium which can be formed by pressurizing twice is not heated by the heating device 200, so that the temperature of the fluid medium is relatively low, which is not beneficial to paraffin removal and blockage removal operation, however, the high-pressure fluid medium can be injected into the well for circulation or pressure test operation in the well.
It should be noted here that, in order to switch the flow path of the fluid medium, control valves may be respectively disposed on the end of the liquid inlet pipe 910 close to the heating apparatus 200 and the second branch pipe 960, and at this time, the on-off of the end of the liquid inlet pipe 910 close to the heating apparatus 200 and the on-off of the second branch pipe 960 may be controlled by the control valves.
Referring to fig. 3, in some embodiments, the manifold system may further include a third branch pipe 970, one end of the third branch pipe 970 is connected to the liquid inlet pipe 910, a junction of the third branch pipe 970 and the liquid inlet pipe 910 is located between the second pressurizing device 400 and the heating device 200, and the other end of the third branch pipe 970 is connected to the liquid outlet pipe 920. Based on this, the fluid medium that has undergone one-time pressurization by second pressurization device 400 may further flow out through liquid outlet pipe 920. Alternatively, the second pressurizing means 400 may be a low-pressure pressurizing means, and the pressurized fluid medium may be used for supplying other equipment.
It should be noted here that, since one end of the second branch pipe 960 is located between the second pressurizing device 400 and the heating device 200, and one end of the third branch pipe 970 is located between the second pressurizing device 400 and the heating device 200, one end of the second branch pipe 960 and one end of the third branch pipe 970 may be located at the same junction, and at this time, there is a common main path and respective branches between the second branch pipe 960 and the third branch pipe 970. Of course, one end of the second branch pipe 960 and one end of the third branch pipe 970 may also be located at different junctions, in which case the two branch pipes may each be used for channeling the fluid medium. In addition, in order to switch the flow path of the fluid medium, control valves may be provided at the end of the liquid inlet pipe 910 close to the heating apparatus 200 and the third branch pipe 970, respectively, and at this time, the on/off of the end of the liquid inlet pipe 910 close to the heating apparatus 200 and the on/off of the third branch pipe 970 may be controlled by the control valves.
Referring to fig. 4, in some embodiments, the paraffin vehicle further includes a metering container 500, and the metering container 500 may be used to hold a fluid medium. The weighing container 500 is disposed on the vehicle chassis 100 so that the weighing container 500 can be carried by the vehicle chassis 100. Alternatively, the metering container 500 may be a metering tank. In addition, the metering container 500 may also be used for mixing chemical solutions, thereby effectively alleviating the problem that the conventional water tank is only used for containing a single liquid such as water or crude oil.
The manifold system further comprises a fourth branch pipe 980, one end of the fourth branch pipe 980 is connected with the liquid inlet pipe 910, the junction of the fourth branch pipe 980 and the liquid inlet pipe 910 is located between the second pressurizing device 400 and the heating device 200, and the other end of the fourth branch pipe 980 is connected with the metering container 500. In this connection, the fluid medium flows via the inlet line 910 to the second pressurizing device 400, and the fluid medium pressurized by the second pressurizing device 400 can flow via the fourth branch 980 into the measuring container 500, so that it can be used to feed or cycle the measuring container 500.
It should be noted here that, in order to switch the flow path of the fluid medium, control valves may be respectively disposed on the end of the liquid inlet pipe 910 close to the heating apparatus 200 and the fourth branch pipe 980, and then the on-off of the end of the liquid inlet pipe 910 close to the heating apparatus 200 and the on-off of the fourth branch pipe 980 may be controlled by the control valves.
Referring to fig. 4, in some embodiments, the manifold system further includes a fifth branch pipe 990, one end of the fifth branch pipe 990 being connected to the first connection pipe 930, and the other end of the fifth branch pipe 990 being connected to the metering container 500. Based on this, the fluid medium flows to the second pressurizing device 400 through the liquid inlet pipe 910 for pressurization, the pressurized fluid medium flows to the heating device 200 for heating, so as to obtain the fluid medium with certain pressure and high temperature, and then the heated fluid medium flows back to the metering container 500 through the fifth branch pipe 990, so as to form the high temperature fluid medium in the metering container 500, at this time, other chemical agents can be mixed to form a process liquid for oil well stimulation operation.
It should be noted here that the other end of the fourth branch pipe 980 is connected to the metering container 500, and the other end of the fifth branch pipe 990 is also connected to the metering container 500, in which case there may be a common main path between the fourth branch pipe 980 and the fifth branch pipe 990, and respective branches. Of course, the other end of the fourth branch pipe 980 and the other end of the fifth branch pipe 990 may also be connected to the metering container 500 at different locations, in which case the two branch pipes may each be used to dredge fluid medium into the metering container 500.
Referring to fig. 4, in some embodiments, the manifold system may further include a second connection pipe 940, one end of the second connection pipe 940 is connected to the metering container 500, the other end of the second connection pipe 940 is connected to the liquid inlet pipe 910, and the junction of the second connection pipe 940 and the liquid inlet pipe 910 is close to the liquid inlet port of the liquid inlet pipe 910. Based on this, the fluid medium in the metering container 500 may be returned to the liquid inlet pipe 910, thereby flowing to other devices, such as the heating device 200, the second pressurizing device 400, and the like, via the liquid inlet pipe 910. It should be noted here that a control valve may be further disposed on second connection pipe 940 to control on/off of second connection pipe 940.
Based on the above arrangement, the fluid medium in the metering container 500 can be conveyed into the liquid inlet pipe 910 through the second connecting pipe 940, so as to realize liquid supply; at the same time, the release of the fluid medium in the metering container 500 may also be achieved through the second connection pipe 940, or the process liquid mixed in the metering container 500 may be delivered into the liquid inlet pipe 910 to deliver the process fluid to a desired location.
Referring to fig. 1, in some embodiments, the paraffin removal truck further includes an air compression device 600, and the air compression device 600 is disposed on the truck chassis 100, and the air compression device 600 is supported and carried by the truck chassis 100. Considering that liquid can be remained in the coiled tubing after the well washing operation is finished, the remained liquid has a certain corrosion effect on the coiled tubing, and the coiled tubing can be damaged in the past, so that the oil well operation is influenced. Based on this, can be connected air compressor arrangement 600 with coiled tubing to can blow to among the coiled tubing, sweep the discharge with the remaining liquid in the coiled tubing, thereby guarantee the inside drying of coiled tubing, alleviate the corrosive action of remaining liquid to coiled tubing, thereby prolonged coiled tubing's life.
Alternatively, the air compressor 600 may be an air compressor. The air compressor machine is a component that has certain pressure, and its high-pressure gas that produces probably produces certain injury to operating personnel, so, sets up pneumatics 600 at the afterbody of vehicle bottom dish 100 to make the discharge port of pneumatics 600 towards the rear of vehicle bottom dish 100, so, can make the discharge port of pneumatics 600 outwards, avoid the operating personnel on the vehicle bottom dish 100, thereby guaranteed operating personnel's personal safety.
Referring to fig. 1, in some embodiments, the paraffin removal truck may further include a control room 700, the control room 700 being disposed on the truck chassis 100. Alternatively, the control room 700 is located at the rear of the metering container 500, the metering container 500 is located at the rear of the heating apparatus 200, and the second pressurizing apparatus 400 is located at the lower portion of the metering container 500 and is connected to the metering container 500.
Through the setting of control room 700, can provide operating space for operating personnel, make things convenient for in the operation, and even the paraffin removal car is in operation in adverse circumstances, because operating personnel operates in control room 700 for operating personnel does not basically receive external adverse circumstances's influence, has guaranteed operating personnel's personal safety, and has improved the convenience of operation.
Optionally, the metering container 500 is mounted on the chassis 100 by legs; the second pressurizing device 400 is connected with the metering container 500 through a pipeline (i.e., a fourth branch pipe 980) so that the fluid medium can flow back into the metering container 500, and the metering container 500 is cleaned or supplied with liquid; the control room 700 is mounted on the chassis 100 through a base.
In addition, the heating device 200 is located at the rear of the cab of the vehicle chassis 100. Alternatively, the heating device 200 may be mounted on the main beam of the vehicle chassis 100 through a base.
The first pressurizing device 300 is provided at the rear of the vehicle chassis 100, and the discharge port of the first pressurizing device 300 is provided toward the rear of the vehicle chassis 100.
Based on the arrangement, the arrangement position of the control room 700 is far away from the heating device 200, so that the influence of high temperature in the control room 700 on the operation of the paraffin removal truck by operators can be effectively relieved; the air compression device 600 and the first pressurization device 300 are respectively arranged at the tail part of the vehicle chassis 100, and the discharge ports of the air compression device 600 and the first pressurization device 300 respectively face the rear part of the vehicle chassis 100, so that the air compression device deviates from the operator in the control room 700, and the personal safety of the operator is ensured to a certain extent.
Referring to fig. 1 and 5, in some embodiments, the paraffin removal vehicle may further include a transmission 800, the transmission 800 including a disconnect shaft power take-off transfer case 810, a plurality of drive shafts, and an auxiliary gearbox 830. In order to provide power for each device, the chassis 100 may include a chassis engine 110 and a chassis gearbox 120, the chassis engine 110 may serve as a power source which may provide power for each device, and the chassis gearbox 120 is in driving connection with the chassis engine 110 to transmit and distribute the power output by the chassis engine 110 to distribute the power to each device.
Optionally, the disconnected shaft power-taking transfer case 810 is in transmission connection with the chassis gearbox 120 through a first transmission shaft 821, the auxiliary gearbox 830 is in transmission connection with the disconnected shaft power-taking transfer case 810 through a second transmission shaft 822, and the first pressure device 300 is in transmission connection with the auxiliary gearbox 830 through a third transmission shaft 823. Based on this, the power output by the chassis engine 110 is transmitted to the chassis gearbox 120, and after being distributed, a part of the power is transmitted to the disconnected shaft power-taking transfer case 810 through the first transmission shaft 821, then transmitted to the auxiliary gearbox 830 through the second transmission shaft 822, and finally transmitted to the first pressurizing device 300 through the third transmission shaft 823, so that the pressurizing movement of the first pressurizing device 300 is realized, and the pressurizing of the fluid medium is realized.
It should be noted that, the specific structures and operating principles of the components of the chassis engine 110, the chassis gearbox 120, the disconnected shaft power take-off transfer case 810, the auxiliary gearbox 830, etc. are all referred to the related art, and will not be described in detail herein.
In addition, a part of the power transmitted to the disconnected shaft power take-off transfer case 810 is transmitted to the rear shaft of the chassis 100 through the fourth transmission shaft 824, so that the chassis 100 can walk, and transportation of all devices is achieved.
Based on the arrangement, in the embodiment of the application, the power of each device of the paraffin removal vehicle is derived from the chassis engine 110, so that no additional engine or generator set is needed to provide power. In addition, chassis gearbox 120 has multiple gears, such as 16 gears, so that power output can be adjusted by changing gears to meet the requirements of multiple operating conditions. The auxiliary gearbox 830 may further include a plurality of gears, such as 4 gears, so that the first pressure device 300 can have more gears, and thus the operating condition requirement of the first pressure device 300 can be met. When the first pressure device 300 is a plunger pump, displacement points can be increased by a plurality of gears of the chassis gearbox 120 and a plurality of units of the auxiliary gearbox 830, so that the use working condition range of the displacement of the whole vehicle is wider.
Referring to fig. 5, in some embodiments, the paraffin removal truck may further include a transmission 800, the transmission 800 further including a first power take-off 841, a second power take-off 842, a first hydraulic pump 851, a second hydraulic pump 852, a first motor 861, a second motor 862, a third motor 863, and a fourth motor 864.
Wherein, the first motor 861 and the second motor 862 are respectively connected with the first hydraulic pump 851 through an oil path, the first hydraulic pump 851 is drivingly connected with the chassis gearbox 120 through the first power takeoff 841, so that the other part of the power in the chassis gearbox 120 is transmitted to the first hydraulic pump 851, thereby driving the first hydraulic pump 851 to work, driving the hydraulic oil to flow in the oil path, and driving the first motor 861 and the second motor 862 to rotate through the hydraulic oil. In the embodiment of the present application, the first motor 861 is used for driving the second pressurizing device 400 to work, and specifically, the first motor 861 drives the centrifugal pump to rotate so as to generate the low-pressure fluid medium. The second motor 862 is used to drive the stirring device inside the metering container 500 to rotate, so as to stir the solution in the metering container 500 by the stirring device, so as to mix the solution more uniformly.
The third motor 863 and the fourth motor 864 are respectively connected with the second hydraulic pump 852 through oil paths, and the second hydraulic pump 852 is in transmission connection with the chassis gearbox 120 through the second power takeoff 842, so that a part of power in the chassis gearbox 120 is transmitted to the second hydraulic pump 852, thereby driving the second hydraulic pump 852 to work, driving hydraulic oil to flow in the oil paths, and driving the third motor 863 and the fourth motor 864 to rotate through the hydraulic oil. In the embodiment of the present application, the third motor 863 is used to drive the air compressor 600 to work, so that gas can be blown into the coiled tubing to blow away residual liquid in the coiled tubing, thereby ensuring that the coiled tubing is not corroded by the residual liquid. The fourth motor 864 is used for driving the burner fan of the heating apparatus 200 to operate, so as to increase oxygen in the burner, thereby enhancing the heating effect of the heating apparatus 200.
It should be noted that the specific structure and operation principle of the first power take-off device 841 and the second power take-off device 842 can refer to the related art, and will not be described in detail herein.
Based on the above arrangement, the power of the chassis gearbox 120 is transmitted to the first motor 861, the second motor 862, the third motor 863 and the fourth motor 864 through the first power takeoff 841 and the second power takeoff 842, so that an engine or an electric machine does not need to be separately arranged, the structure is simpler, the size is smaller, and the arrangement space of a power system and the whole machine is saved.
In summary, the embodiment of the application effectively solves the problem that the pressure of the fluid medium is limited by the boiler and is difficult to meet the requirement of the high-pressure working condition of the deep well; the paraffin removal vehicle in the embodiment of the application can not only remove paraffin and remove blockage, but also clean pipelines and equipment, perform well circulation or pressure test operation, supply liquid to the metering container 500 or evacuate the metering container 500, clean the metering container 500, mix chemical reagents in the metering container 500 to form process liquid and the like, so that the paraffin removal vehicle in the embodiment of the application can realize switching of multiple operation modes, has more functions and is wider in application range; moreover, the coiled tubing can be purged to avoid the corrosion of the coiled tubing by the residual liquid; and an operation space can be provided for an operator, so that the operation is more convenient.
While the present embodiments have been described with reference to the accompanying drawings, it is to be understood that the invention is not limited to the precise embodiments described above, which are meant to be illustrative and not restrictive, and that various changes may be made therein by those skilled in the art without departing from the spirit and scope of the invention as defined by the appended claims.

Claims (10)

1. The utility model provides a paraffin removal car which characterized in that includes: the system comprises a chassis (100), a heating device (200), a first pressurizing device (300) and a manifold system;
the heating device (200) and the first pressurizing device (300) are respectively arranged on the vehicle chassis (100);
the manifold system comprises a liquid inlet pipe (910), a liquid outlet pipe (920) and a first connecting pipe (930), the heating device (200) and the first pressurizing device (300) are connected through the first connecting pipe (930), the liquid inlet pipe (910) is connected with the heating device (200), and the liquid outlet pipe (920) is connected with the first pressurizing device (300).
2. The paraffin vehicle of claim 1, wherein the manifold system further comprises a first branch pipe (950), one end of the first branch pipe (950) is connected to the first connecting pipe (930), and the other end of the first branch pipe (950) is connected to the drain pipe (920).
3. The paraffin vehicle of claim 1, further comprising a second pressurizing device (400) disposed on the vehicle chassis (100), wherein the second pressurizing device (400) is disposed on the liquid inlet pipe (910).
4. A paraffin vehicle according to claim 3, characterized in that the manifold system further comprises a second branch pipe (960), one end of the second branch pipe (960) is connected with the liquid inlet pipe (910), and the junction of the second branch pipe (960) and the liquid inlet pipe (910) is located between the second pressurizing device (400) and the heating device (200), and the other end of the second branch pipe (960) is connected with the first connecting pipe (930).
5. A paraffin vehicle according to claim 3, wherein the manifold system further comprises a third branch pipe (970), one end of the third branch pipe (970) is connected with the liquid inlet pipe (910), the junction of the third branch pipe (970) and the liquid inlet pipe (910) is positioned between the second pressurizing device (400) and the heating device (200), and the other end of the third branch pipe (970) is connected with the liquid outlet pipe (920).
6. A paraffin vehicle according to claim 3, further comprising a metering container (500) provided to the chassis (100);
the manifold system further comprises a fourth branch pipe (980), one end of the fourth branch pipe (980) is connected with the liquid inlet pipe (910), the junction of the fourth branch pipe (980) and the liquid inlet pipe (910) is located between the second pressurizing device (400) and the heating device (200), and the other end of the fourth branch pipe (980) is connected with the metering container (500);
and/or the manifold system comprises a fifth branch pipe (990), one end of the fifth branch pipe (990) is connected with the first connecting pipe (930), and the other end of the fifth branch pipe (990) is connected with the metering container (500).
7. A paraffin vehicle according to any one of claims 1 to 6, characterized in that it further comprises a metering container (500);
the manifold system still includes second connecting pipe (940), the one end of second connecting pipe (940) with measurement container (500) is connected, the other end of second connecting pipe (940) with feed liquor pipe (910) is connected, just second connecting pipe (940) with the junction department of feed liquor pipe (910) is close to the feed liquor port of feed liquor pipe (910).
8. The paraffin removal vehicle as claimed in claim 1, further comprising an air compression device (600), wherein the air compression device (600) is arranged on the vehicle chassis (100) and located at the tail part of the vehicle chassis (100), and a discharge port of the air compression device (600) is arranged towards the rear part of the vehicle chassis (100);
and/or the paraffin removal truck further comprises a control chamber (700), a metering container (500) and a second pressurizing device (400) which are respectively arranged on the truck chassis (100), wherein the metering container (500) is positioned at the rear part of the heating device (200), the second pressurizing device (400) is positioned at the lower part of the metering container (500) and is connected with the metering container (500), and the control chamber (700) is positioned at the rear part of the metering container (500);
and/or the first pressurizing device (300) is positioned at the tail part of the vehicle chassis (100), and a discharge port of the first pressurizing device (300) is arranged towards the rear part of the vehicle chassis (100);
and/or the heating device (200) is positioned at the rear part of the cab of the vehicle chassis (100).
9. The paraffin vehicle of claim 1, further comprising a transmission (800), the transmission (800) comprising a disconnected shaft power take-off transfer case (810), a plurality of drive shafts, and an auxiliary gearbox (830);
the chassis (100) comprises a chassis engine (110) and a chassis gearbox (120) in transmission connection with the chassis engine (110), the broken shaft power taking transfer case (810) is in transmission connection with the chassis gearbox (120) through a first transmission shaft (821), the auxiliary gearbox (830) is in transmission connection with the broken shaft power taking transfer case (810) through a second transmission shaft (822), and the first pressurizing device (300) is in transmission connection with the auxiliary gearbox (830) through a third transmission shaft (823).
10. The paraffin vehicle according to claim 1, further comprising a transmission (800), the transmission (800) further comprising a first power takeoff (841), a second power takeoff (842), a first hydraulic pump (851), a second hydraulic pump (852), a first motor (861), a second motor (862), a third motor (863) and a fourth motor (864), wherein the first motor (861) and the second motor (862) are respectively connected with the first hydraulic pump (851) through an oil path, and the third motor (863) and the fourth motor (864) are respectively connected with the second hydraulic pump (852) through an oil path;
the vehicle chassis (100) comprises a chassis engine (110) and a chassis gearbox (120) in transmission connection with the chassis engine (110), the first hydraulic pump (851) is in transmission connection with the chassis gearbox (120) through the first power takeoff (841), and the second hydraulic pump (852) is in transmission connection with the chassis gearbox (120) through the second power takeoff (842).
CN202111315426.2A 2021-11-08 2021-11-08 Paraffin removal vehicle Active CN114198057B (en)

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CN202111315426.2A CN114198057B (en) 2021-11-08 2021-11-08 Paraffin removal vehicle
CN202310934788.2A CN116856883A (en) 2021-11-08 2021-11-08 Paraffin removal vehicle

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Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2596004Y (en) * 2002-10-26 2003-12-31 中原石油勘探局特种车辆修造总厂 Well-flushing paraffin removal vehicle
CN203452731U (en) * 2013-04-13 2014-02-26 中原特种车辆有限公司 Paraffin removing vehicle
CN203769724U (en) * 2014-04-16 2014-08-13 通化石油化工机械制造有限责任公司 Well flushing and paraffin removal vehicle
WO2016184529A1 (en) * 2015-05-21 2016-11-24 Alfred Kärcher Gmbh & Co. Kg High-pressure-cleaning system and dispensing unit for such a high-pressure-cleaning system
CN109113656A (en) * 2017-06-25 2019-01-01 西安瑞杰油田物资实业开发有限公司 A kind of device of hot cleanout and paraffin removal of oil well nominal output
CN208534457U (en) * 2018-05-16 2019-02-22 山东科瑞机械制造有限公司 A kind of novel and multifunctional well-washing wax-cleaning vehicle
CN211342832U (en) * 2020-06-12 2020-08-25 兰州矿场机械有限公司 Well-flushing paraffin removal vehicle for well-flushing paraffin removal operation

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2596004Y (en) * 2002-10-26 2003-12-31 中原石油勘探局特种车辆修造总厂 Well-flushing paraffin removal vehicle
CN203452731U (en) * 2013-04-13 2014-02-26 中原特种车辆有限公司 Paraffin removing vehicle
CN203769724U (en) * 2014-04-16 2014-08-13 通化石油化工机械制造有限责任公司 Well flushing and paraffin removal vehicle
WO2016184529A1 (en) * 2015-05-21 2016-11-24 Alfred Kärcher Gmbh & Co. Kg High-pressure-cleaning system and dispensing unit for such a high-pressure-cleaning system
CN109113656A (en) * 2017-06-25 2019-01-01 西安瑞杰油田物资实业开发有限公司 A kind of device of hot cleanout and paraffin removal of oil well nominal output
CN208534457U (en) * 2018-05-16 2019-02-22 山东科瑞机械制造有限公司 A kind of novel and multifunctional well-washing wax-cleaning vehicle
CN211342832U (en) * 2020-06-12 2020-08-25 兰州矿场机械有限公司 Well-flushing paraffin removal vehicle for well-flushing paraffin removal operation

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CN116856883A (en) 2023-10-10

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