A low temperature pyrolysis three-phase separation device

By introducing the structure of the temperature guide tube and the water tank into the three-phase separator, fine control of the temperature is achieved, and the problem of difficult separation of pyrolytic products in the prior art is solved, simplifying the separation process and improving efficiency.

CN222723685UActive Publication Date: 2025-04-08HENAN TIANCHEN XINYUAN ENVIRONMENTAL PROTECTION TECH RES INST CO LTD
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Patent Information

Application Number
CN202421490654.2
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-06-26
Publication Date
2025-04-08
Estimated Expiration
2034-06-26

AI Technical Summary

Technical Problem

The existing three-phase separators are difficult to effectively separate the pyrolysis products during the pyrolysis process, and the temperature control is complex, which affects the separation efficiency.

Method used

A low-temperature pyrolysis three-phase separation device is designed, using a structure that combines the shell and the three-phase separator body. Through the cooperation of the temperature guide tube and the water tank, the temperature in the three-phase separator is controlled, ensuring the temperature is between 60 and 80℃, and simplifying the separation process.

Benefits of technology

The fine control of the temperature in the body of the three-phase separator is achieved, the separation process is simplified, the difficulty of difficult separation of pyrolysis products is reduced, and the separation efficiency is improved.

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Abstract

The utility model belongs to the technical field of three-phase separation, and particularly relates to a low-temperature pyrolysis three-phase separation device. A low-temperature pyrolysis three-phase separation device comprises a shell and a three-phase separator body arranged in the shell, the outer walls on both sides of the shell are respectively provided with a water tank 1 and a water tank 2, a temperature conducting pipe is wound around the three-phase separator body, and the two ends of the temperature conducting pipe extend to the outside of the two sides of the shell respectively, the water tank 1 and the water tank 2 are both provided with a partition plate, and the space in the water tank 1 and the water tank 2 is divided into a cold water storage space and a hot water storage space by the partition plate; the cold water storage space and the hot water storage space in the water tank 1 and the water tank 2 are both provided with a water pump 1, and a water pump 2 is provided on one side of the outer wall of the shell. The low-temperature pyrolysis three-phase separation device provided by the utility model has a simple structure, and the temperature in the three-phase separator body can be controlled to 60-80°C, so that it can be separated quickly, reducing the difficulty of mixing and separating pyrolysis products.
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Description

Technical Field

[0001] The utility model belongs to the technical field of three-phase separation, and in particular relates to a low-temperature pyrolysis three-phase separation device. Background Art

[0002] Crude oil contains water and natural gas after being extracted from oil fields and oil wells, and needs to be separated before transportation. The purified crude oil and natural gas after treatment are exported as products, and the separated water can be used as reinjection water for oil wells. The separation of crude oil extracted from oil fields and oil wells generally uses a three-phase separator.

[0003] A three-phase separator is disclosed in the utility model patent with the announcement number CN 218811542 U, which relates to the technical field of three-phase separators, including a device body, an inlet pipe is installed at the input end of the device body, an air outlet pipe is connected to the top output end of the device body, and a drain pipe and an oil outlet pipe are respectively connected to the bottom output end of the device body, and the drain pipe is closer to the inlet pipe than the oil outlet pipe. The wave-proof mechanism can control the height of the waves rolled up by the liquid inside the device body, which can accelerate the separation of oil and water, and adjust the interlaced area of ​​the circular hole and the flow hole, so as to adjust the speed of liquid inflow, which plays a role in reducing the height of the waves. When the liquid flows into the wave-proof mechanism and the penetration buffer plate, the floating plate can further slow down the generation of waves, and the connecting rope can pull the floating plate to prevent the floating plate from moving significantly. The pyrolysis oil, gas and slag can be separated by the three-phase separator, but the pyrolysis products are mixed and difficult to separate.

[0004] Therefore, it is necessary to provide a new low-temperature pyrolysis three-phase separation device to solve the above technical problems. Utility Model Content

[0005] The technical problem solved by the utility model is to provide a low-temperature pyrolysis three-phase separation device with a simple structure, which can control the temperature in the three-phase separator body to 60-80°C, thereby achieving rapid separation and reducing the difficulty of separating mixed pyrolysis products.

[0006] In order to solve the above technical problems, the utility model provides a low-temperature pyrolysis three-phase separation device adopts the following technical solutions:

[0007] A low-temperature pyrolysis three-phase separation device comprises a shell and a three-phase separator body arranged in the shell, a water tank 1 and a water tank 2 are respectively arranged on the outer walls of both sides of the shell, a temperature conducting pipe is wound around the three-phase separator body, and both ends of the temperature conducting pipe extend to the outside of both sides of the shell, a partition plate is arranged in each of the water tanks 1 and 2, and the space in each of the water tanks 1 and 2 is divided into a cold water storage space and a hot water storage space by the partition plate;

[0008] The cold water storage space and the hot water storage space in the water tank 1 and the water tank 2 are both provided with a water pump 1, and the outer wall of one side of the shell is provided with a water pump 2;

[0009] A concave tube 1 is installed on the outer wall of one side of the water tank 1, and the two ends of the concave tube 1 extend into the cold water storage space and the hot water storage space in the water tank 1 respectively and are connected with the water pump 1 in the cold water storage space and the hot water storage space in the water tank 1. A concave tube 2 is installed on the outer wall of one side of the water tank 2, and the two ends of the concave tube 2 extend into the cold water storage space and the hot water storage space in the water tank 2 respectively.

[0010] As a further solution of the utility model, one end of the temperature conducting tube is connected to concave tube one, the other end of the temperature conducting tube is connected to concave tube two, and concave tube three is installed on the outer wall of the water tank one away from concave tube one.

[0011] As a further solution of the utility model, a concave tube four is installed on the outer wall of the water tank two away from the concave tube two, a drain pipe one is installed on the water outlet of the water pump two, and one end of the drain pipe one is connected to the concave tube three.

[0012] As a further solution of the utility model, a water suction pipe is installed on the water suction port of the water pump 2, one end of the water suction pipe is connected to the concave pipe 4, and an air outlet pipe and an inlet pipe are installed on the shell, and the bottom ends of the air outlet pipe and the inlet pipe extend into the three-phase separator body.

[0013] As a further solution of the utility model, a second drain pipe, an oil outlet pipe and a slag discharge pipe are installed on the shell, and the top ends of the second drain pipe, the oil outlet pipe and the slag discharge pipe all extend into the three-phase separator body.

[0014] As a further solution of the utility model, a temperature sensor is provided in the housing.

[0015] Compared with the related art, the low-temperature pyrolysis three-phase separation device provided by the utility model has the following beneficial effects:

[0016] The utility model has a simple structure and can control the temperature in the three-phase separator body to 60-80° C., so that the separation can be rapid and the difficulty of separating mixed pyrolysis products can be reduced. BRIEF DESCRIPTION OF THE DRAWINGS

[0017] The drawings constituting part of the present application are used to provide a further understanding of the present application. The exemplary embodiments and descriptions of the present application are used to explain the present application and do not constitute an improper limitation on the present application. Among them:

[0018] Figure 1 The structure of the utility model is shown in FIG. Figure 1 ;

[0019] Figure 2 The structure of the utility model is shown in FIG. Figure 2 ;

[0020] Figure 3 It is a schematic diagram of the principle of water circulation in the utility model.

[0021] In the figure: 1. Shell; 2. Three-phase separator body; 3. Water tank 1; 4. Water tank 2; 5. Water pump 2; 6. Temperature conduction pipe; 7. Partition plate; 8. Concave pipe 1; 9. Concave pipe 2; 10. Concave pipe 3; 11. Concave pipe 4; 12. Drain pipe 1; 13. Water suction pipe; 14. Air outlet pipe; 15. Inlet pipe; 16. Drain pipe 2; 17. Oil outlet pipe; 18. Slag discharge pipe. DETAILED DESCRIPTION

[0022] The present application will be described in detail below with reference to the accompanying drawings and in conjunction with embodiments. Each example is provided by way of explanation of the present application and does not limit the present application. In fact, it will be clear to those skilled in the art that modifications and variations may be made in the present application without departing from the scope or spirit of the present application. For example, a feature shown or described as a part of an embodiment may be used in another embodiment to produce yet another embodiment. All other embodiments obtained by those of ordinary skill in the art based on the embodiments in the present utility model embodiments shall fall within the scope of protection of the present utility model embodiments.

[0023] Example

[0024] Please refer to Figure 1 , Figure 2 and Figure 3 A low-temperature pyrolysis three-phase separation device comprises a shell 1 and a three-phase separator body 2 arranged in the shell 1, a water tank 1 3 and a water tank 2 4 are respectively arranged on the outer walls of both sides of the shell 1, a temperature conducting pipe 6 is wound around the three-phase separator body 2, and both ends of the temperature conducting pipe 6 extend to the outside of both sides of the shell 1, a partition plate 7 is respectively arranged in the water tank 1 3 and the water tank 2 4, and the space in the water tank 1 3 and the water tank 2 4 is divided into a cold water storage space and a hot water storage space by the partition plate 7;

[0025] The cold water storage space and the hot water storage space in the water tank 1 3 and the water tank 2 4 are both provided with a water pump 1, and a water pump 2 5 is provided on one side outer wall of the housing 1;

[0026] A concave pipe 8 is installed on the outer wall of one side of water tank 1 3, and the two ends of the concave pipe 8 extend to the cold water storage space and the hot water storage space in water tank 1 3 respectively and are connected with the water pump 1 in the cold water storage space and the hot water storage space in water tank 1 3. A concave pipe 2 9 is installed on the outer wall of one side of water tank 2 4, and the two ends of the concave pipe 2 9 extend to the cold water storage space and the hot water storage space in water tank 2 4 respectively.

[0027] One end of the temperature conducting tube 6 is connected to the concave tube 1 8 , and the other end of the temperature conducting tube 6 is connected to the concave tube 2 9 . A concave tube 3 10 is installed on the outer wall of the water tank 1 3 away from the concave tube 1 8 .

[0028] A concave pipe 4 11 is installed on the outer wall of the water tank 2 4 away from the concave pipe 2 9 , and a drain pipe 12 is installed on the water outlet of the water pump 2 5 , and one end of the drain pipe 12 is connected to the concave pipe 3 10 .

[0029] A water suction pipe 13 is installed on the water suction port on the water pump 2 5, and one end of the water suction pipe 13 is connected to the concave pipe 4 11. An air outlet pipe 14 and an inlet pipe 15 are installed on the shell 1, and the bottom ends of the air outlet pipe 14 and the inlet pipe 15 extend into the three-phase separator body 2.

[0030] A second drain pipe 16 , an oil outlet pipe 17 and a slag discharge pipe 18 are installed on the shell 1 , and the top ends of the second drain pipe 16 , the oil outlet pipe 17 and the slag discharge pipe 18 all extend into the three-phase separator body 2 .

[0031] A temperature sensor is disposed in the housing 1 , and the temperature sensor is not limited and is therefore not shown in the figure.

[0032] The structures of water pump 1 and water pump 2 5 are the same, so water pump 1 also has no Figure 1 and Figure 2 It is shown that the cold water storage space and the hot water storage space in the water tank 3 are respectively provided with a heating device and a cooling device. The heating device and the cooling device are not limited, and can heat and cool water. Therefore, the heating device and the cooling device are also not in Figure 1 and Figure 2 It is shown in the table.

[0033] Two valves are provided on each of the concave pipe 1 8 , the concave pipe 2 9 , the concave pipe 3 10 and the concave pipe 4 11 , and the discharge circulation of hot water and cold water is controlled by the valves.

[0034] The working principle of the low-temperature pyrolysis three-phase separation device provided by the utility model is as follows:

[0035] The first step: the temperature in the three-phase separator body 2 is detected by the temperature sensor, and the detection result is transmitted to the controller for display. During separation, the temperature in the three-phase separator body 2 is controlled at 60-80°C (originally more than 300 degrees Celsius). Therefore, when cooling is required, the corresponding valve is opened, and water is pumped through the water pump 1 in the cold water storage space in the water tank 3, and then discharged into the temperature conducting pipe 6 through the concave pipe 1 8, so that the cold water flows in the temperature conducting pipe 6, so as to cool the three-phase separator body 2, and then the cold water enters the cold water storage space in the partition plate 7 through the concave pipe 2 9, and finally discharged into the cold water storage space in the water tank 3 through the cooperation of the concave pipe 4 11, the pumping pipe 13, the water pump 2 5 and the drain pipe 12, and finally refrigerated and cooled by the cooling equipment, so as to achieve the water circulation effect;

[0036] The second step: when heating is required, the same operation as the above steps is performed, the corresponding valve is opened, water is pumped through the water pump 1 in the hot water storage space in the water tank 3, and then discharged into the temperature conducting pipe 6 through the concave pipe 8, so that the hot water flows in the temperature conducting pipe 6, thereby heating the three-phase separator body 2, and then the hot water enters the hot water storage space in the partition plate 7 through the concave pipe 2 9, and finally discharged into the hot water storage space in the water tank 3 through the cooperation of the concave pipe 4 11, the pumping pipe 13, the water pump 2 5 and the drain pipe 12, and finally the water is heated by the heating equipment to achieve the water circulation effect.

[0037] It should be noted that the equipment structure and drawings of the utility model mainly describe the principle of the utility model. In terms of the technology of the design principle, the settings of the power mechanism, power supply system and control system of the device are not fully described. On the premise that the technical personnel in this field understand the principle of the above utility model, the details of the power mechanism, power supply system and control system can be clearly known. The control method of the application document is automatic control through a controller, and the control circuit of the controller can be realized by simple programming by the technical personnel in this field;

[0038] The standard parts used therein can all be purchased from the market and can be customized according to the instructions and drawings. The specific connection methods of each part adopt conventional means such as mature bolts, rivets, welding, etc. in the prior art. The machinery, parts and equipment all adopt conventional models in the prior art, and the structures and principles of the components known to technical personnel in this field can be known by these technical personnel through technical manuals or through conventional experimental methods.

[0039] Although the embodiments of the present invention have been shown and described, it is understood by those skilled in the art that various changes, modifications, substitutions and variations or direct or indirect applications may be made to these embodiments without departing from the principles and spirit of the present invention. In other related technical fields, the scope of the present invention is defined by the attached claims and their equivalents, which are equally included in the scope of patent protection of the present invention.

Claims

1. A low-temperature pyrolysis three-phase separation device, characterized in that: It comprises a shell and a three-phase separator body arranged in the shell, the outer walls of both sides of the shell are respectively provided with a water tank 1 and a water tank 2, a temperature conducting pipe is wound around the three-phase separator body, and the two ends of the temperature conducting pipe extend to the outside of both sides of the shell respectively, and the water tank 1 and the water tank 2 are both provided with a partition plate, and the space in the water tank 1 and the water tank 2 is divided into a cold water storage space and a hot water storage space by the partition plate; The cold water storage space and the hot water storage space in the water tank 1 and the water tank 2 are both provided with a water pump 1, and the outer wall of one side of the shell is provided with a water pump 2; A concave tube 1 is installed on the outer wall of one side of the water tank 1, and the two ends of the concave tube 1 extend into the cold water storage space and the hot water storage space in the water tank 1 respectively and are connected with the water pump 1 in the cold water storage space and the hot water storage space in the water tank 1. A concave tube 2 is installed on the outer wall of one side of the water tank 2, and the two ends of the concave tube 2 extend into the cold water storage space and the hot water storage space in the water tank 2 respectively.

2. The low-temperature pyrolysis three-phase separation device according to claim 1, characterized in that: One end of the temperature conducting tube is connected to the concave tube 1, and the other end of the temperature conducting tube is connected to the concave tube 2. The outer wall of the water tank 1 away from the concave tube 1 is installed with a concave tube 3.

3. The low-temperature pyrolysis three-phase separation device according to claim 2, characterized in that: A concave pipe four is installed on the outer wall of the water tank two away from the concave pipe two, and a drain pipe one is installed on the water outlet of the water pump two, and one end of the drain pipe one is connected to the concave pipe three.

4. The low-temperature pyrolysis three-phase separation device according to claim 3, characterized in that: A water suction pipe is installed on the water suction port of the water pump 2, one end of which is connected to the concave pipe 4, and an air outlet pipe and an inlet pipe are installed on the shell, and the bottom ends of the air outlet pipe and the inlet pipe extend into the three-phase separator body.

5. The low-temperature pyrolysis three-phase separation device according to claim 1, characterized in that: A second drain pipe, an oil outlet pipe and a slag discharge pipe are installed on the shell, and the top ends of the second drain pipe, the oil outlet pipe and the slag discharge pipe all extend into the body of the three-phase separator.

6. The low-temperature pyrolysis three-phase separation device according to claim 1, characterized in that: A temperature sensor is arranged in the shell.

Citation Information

Patent Citations

  • Three-phase separator

    CN218811542U