A device for testing secondary treatment of coke oven raw gas
By forming a closed space through an oil fume separation device and an ignition device, the problem of raw coal gas overflow from the experimental coke oven was solved, achieving safe and environmentally friendly tar separation and flue gas treatment, and improving the production environment and ease of operation.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- ZHONGTIAN IRON & STEEL GRP (NANTONG) CO LTD
- Filing Date
- 2025-08-11
- Publication Date
- 2026-07-07
AI Technical Summary
The irritating, flammable and toxic raw coal gas produced by the experimental coke oven during the coking process is prone to overflow during tar separation, which endangers health and causes environmental pollution, and the tar splash is difficult to clean.
An oil fume separation device is used. The hose at the bottom of the condenser is connected to a tee and then into a tar barrel. The flue gas is burned by an ignition device to form a closed space. A small exhaust fan is used to remove the flue gas. Matching flanges and threaded covers are installed to improve the connection sealing.
To prevent flue gas from escaping, improve environmental and safety benefits, reduce tar splashing, lower cleaning difficulty, and ensure stable system operation.
Smart Images

Figure CN224462495U_ABST
Abstract
Description
Technical Field
[0001] This application relates to the field of experimental coke oven technology, and in particular to a device for secondary treatment of raw coal gas from experimental coke ovens. Background Technology
[0002] A test coke oven is a process testing instrument used in metallurgical engineering and chemical engineering fields. It is used to test many factors that affect coke quality, such as fineness of grinding, particle size, and coking speed. The experimental results are applied to actual production and combined with conventional coal analysis to make the coal blending structure more reasonable and the cost effectively controlled.
[0003] During the coking process, the experimental coke oven produces a large amount of irritating and toxic raw coal gas, such as a mixture of water vapor, coal gas, and tar gas. The raw coal gas flows into the condenser through the rising pipe of the experimental coke oven. Water, which has undergone a low-temperature constant-temperature reaction, is introduced from the bottom of the condenser. Through water cooling, the tar in the raw coal gas is liquefied and separated. The liquefied tar flows down the condenser tube wall to the bottom. The valve at the bottom of the condenser is opened periodically to collect the tar in the waste tar barrel. The raw coal gas after the tar is separated by the condenser is then discharged through the pipeline after being burned by the ignition device and meets the emission standards.
[0004] Because the condensers are interconnected and the tar is liquefied and separated from the raw coal gas, some raw coal gas will overflow along with the tar during the process of opening the valve at the bottom of the condenser to separate and discharge the tar. Raw coal gas is flammable, irritating, toxic, and easily adsorbed, which seriously endangers human health and causes environmental pollution. At the same time, due to the open external space, the tar splashes during the discharge process, which is difficult to clean, damages the site hygiene, and does not meet production standards. Therefore, it needs to be improved. Utility Model Content
[0005] In order to create a closed space, prevent flue gas from escaping, and improve environmental and safety benefits, this application provides a device for secondary treatment of experimental coke oven raw gas.
[0006] The device for secondary treatment of experimental coke oven raw gas provided in this application adopts the following technical solution:
[0007] An apparatus for secondary treatment of raw coke oven gas includes an oil fume separation device. A tar tank is installed inside the oil fume separation device. Two condensers are installed above the oil fume separation device. One condenser has a test coke oven installed on one side, and a riser pipe is installed on the top of the test coke oven. A flexible metal hose and elbow for connecting to the condenser are installed on the riser pipe. A wall is installed on one side of the other condenser, and an ignition device is installed on the outside of the wall. The ignition device is connected to a flexible hose, which is connected to the oil fume separation device. A tee is installed on the top of the oil fume separation device, and both condensers are connected to the oil fume separation device through the tee.
[0008] By adopting the above technical solution, the bottom of the two condensers of the test coke oven is connected to a flexible hose. The two hoses are connected to the oil fume separation device through a tee. The oil fume enters the tar barrel through the outlet of the oil fume separation device. After the tar is discharged, the tar discharge valve is closed. The flue gas in the oil fume separation device is burned by the ignition device and discharged in compliance with the standards, thereby forming a closed space to prevent the flue gas from escaping and improve environmental protection and safety benefits.
[0009] Preferably, a small exhaust fan is provided on the hose.
[0010] By adopting the above technical solution, the small exhaust fan can remove the smoke from the oil fume separation device, while creating a slight negative pressure inside the device to prevent the smoke from overflowing due to poor sealing.
[0011] Preferably, both ends of the metal hose are provided with mating flanges, and the metal hose is connected to the riser pipe and elbow through the mating flanges.
[0012] By adopting the above technical solution, the installation of matching flanges can improve the ease of connection and installation between metal hoses, riser pipes, and elbows.
[0013] Preferably, both the test coke oven and the condenser are equipped with supports at their bottoms.
[0014] By adopting the above technical solutions, the installation stability of the test coke oven and condenser can be effectively improved.
[0015] Preferably, a valve is provided on the connecting pipe between the condenser and the tee.
[0016] By adopting the above technical solution, the valve can be set to discharge the separated tar into the tar tank of the oil fume separation device through a three-way valve, thereby realizing the flow control of tar.
[0017] Preferably, the upper interface of the oil fume separation device is provided with a threaded cover.
[0018] By adopting the above technical solution, the threaded cap can achieve a sealing function.
[0019] Preferably, both the inlet and outlet of the condenser are connected to a low-temperature constant-temperature reaction bath.
[0020] By adopting the above technical solution, a low-temperature constant-temperature reaction bath can be used for cooling, thereby ensuring the safety and stability of the system.
[0021] Preferably, a connecting pipe is provided between the two condensers.
[0022] By adopting the above technical solution, a connecting pipe can be installed between the two condensers to optimize heat exchange efficiency, balance system load, enhance operational flexibility, and ensure safe and stable operation.
[0023] In summary, this application includes at least one of the following beneficial technical effects:
[0024] 1. Connect the bottom of the two condensers of the test coke oven to the bottom of the hoses. Connect the two hoses to the oil fume separation device through the tee. The oil fume enters the tar barrel through the outlet of the oil fume separation device. After the tar is discharged, close the tar discharge valve. The flue gas in the oil fume separation device is burned by the ignition device and discharged in compliance with the standard, thus forming a closed space to prevent the flue gas from escaping and improve environmental protection and safety benefits.
[0025] 2. Flue gas has hazardous properties such as flammability, toxicity, irritation, and adsorption. This device prevents flue gas from escaping by forming a closed space, thus providing both environmental and safety benefits.
[0026] 3. Tar is sticky and can cause splashing during discharge. This device can prevent tar splashing and reduce the labor intensity of employees cleaning up tar. Attached Figure Description
[0027] Figure 1 This is a schematic diagram of a device for secondary treatment of experimental coke oven raw gas according to an embodiment of this application.
[0028] Explanation of reference numerals in the attached drawings: 1. Test coke oven; 2. Ascension pipe; 3. Metal flexible hose; 4. Matching flange; 5. Condenser; 6. Ignition device; 7. Bracket; 8. Wall; 9. Connecting pipe; 10. Tee; 11. Valve; 12. Oil fume separation device; 13. Tar drum; 14. Small exhaust fan; 15. Flexible hose; 16. Elbow; 17. Inlet and outlet; 18. Threaded cap. Detailed Implementation
[0029] The following is in conjunction with the appendix Figure 1 This application will be described in further detail.
[0030] This application discloses an apparatus for secondary treatment of experimental coke oven raw gas. (Refer to...) Figure 1The system includes an oil fume separation device 12, which is a shell structure. A tar container 13 is installed inside the oil fume separation device 12. Two condensers 5 are installed above the oil fume separation device 12, and supports 7 are installed on the condensers 5 to improve their installation stability. The bottom outlets of both condensers 5 are connected to flexible hoses 15. A tee 10 is installed at the top of the oil fume separation device 12, and the flexible hoses 15 of both condensers 5 are connected to the tee 10. Kerosene is discharged into the tar container 13 inside the oil fume separation device 12 through the tee 10. In this embodiment, a threaded cap 18 is installed at the interface of the oil fume separation device 12 to improve its sealing performance. Valves 11 are installed on both flexible hoses 15 of the condensers 5 to control the flow of tar.
[0031] Reference Figure 1 A connecting pipe 9 is provided between the two condensers 5 to optimize heat exchange efficiency, balance system load, enhance operational flexibility, and ensure safe and stable operation; the inlet and outlet 17 of the two condensers 5 are connected to a low-temperature constant temperature reaction bath, which can be used for cooling and thus ensure the safety and stability of the system.
[0032] Reference Figure 1 One of the condensers 5 has a test coke oven 1 on one side. The test coke oven 1 has a riser pipe 2 at its upper end. A metal hose 3 is connected to one side of the riser pipe 2. The end of the metal hose 3 away from the riser pipe 2 is connected to an elbow 16. The other end of the elbow 16 is connected to the upper end of the condenser 5. Both ends of the metal hose 3 are equipped with matching flanges 4 for connecting to the riser pipe 2 and the elbow 16, thereby improving the ease of installation of the metal hose 3. In this embodiment, a support 7 is also provided at the bottom of the test coke oven 1. The test coke oven 1 is installed on the ground through the support 7, thereby improving the installation stability of the test coke oven 1.
[0033] Reference Figure 1 Another condenser 5 has a wall 8 on one side, and an ignition device 6 is installed outside the wall 8. The ignition device 6 is connected to the condenser 5 through a metal hose 3 and an elbow 16. The bottom end of the ignition device 6 is connected to a hose 15, and the other end of the hose 15 is connected to the oil fume separation device 12. A small exhaust fan 14 is installed on the hose 15. The small exhaust fan 14 can draw away the smoke in the oil fume separation device 12, and at the same time make the device have a slight negative pressure to prevent the smoke from overflowing the device due to poor sealing.
[0034] The implementation principle of the device for secondary treatment of raw coke oven gas in this application embodiment is as follows: the bottom of the two condensers 5 of the test coke oven 1 is connected to the bottom of the hoses 15, and the two hoses 15 are connected to the oil fume separation device 12 through the tee 10. The gas enters the tar tank 13 through the outlet of the oil fume separation device 12. After the tar is discharged, the tar discharge valve is closed, and the small exhaust fan 14 extracts the flue gas in the oil fume separation device 12. The flue gas in the oil fume separation device 12 is burned by the ignition device 6 and discharged in compliance with the standard, thereby forming a closed space to prevent the flue gas from escaping and improve environmental protection and safety benefits.
[0035] The above are all preferred embodiments of this application, and are not intended to limit the scope of protection of this application. Therefore, all equivalent changes made in accordance with the structure, shape and principle of this application should be covered within the scope of protection of this application.
Claims
1. An apparatus for secondary treatment of experimental coke oven raw gas, characterized in that: The device includes an oil fume separation unit, which contains a tar barrel. Two condensers are positioned above the oil fume separation unit. One condenser has a test coke oven on one side, and a riser pipe is installed on the top of the test coke oven. The riser pipe is equipped with a flexible metal hose and an elbow for connecting to the condenser. The other condenser has a wall on one side, and an ignition device is installed on the outside of the wall. The ignition device is connected to a flexible hose, which is connected to the oil fume separation unit. A tee is installed on the top of the oil fume separation unit, and both condensers are connected to the oil fume separation unit via the tee.
2. The apparatus for secondary treatment of experimental coke oven raw gas according to claim 1, characterized in that: A small exhaust fan is installed on the hose.
3. The apparatus for secondary treatment of experimental coke oven raw gas according to claim 1, characterized in that: The metal hose is equipped with matching flanges at both ends, and the metal hose is connected to the riser pipe and elbow through the matching flanges.
4. The apparatus for secondary treatment of experimental coke oven raw gas according to claim 1, characterized in that: Both the experimental coke oven and the condenser are equipped with supports at their bottoms.
5. The apparatus for secondary treatment of experimental coke oven raw gas according to claim 1, characterized in that: A valve is installed on the connecting pipe between the condenser and the tee.
6. The apparatus for secondary treatment of experimental coke oven raw gas according to claim 1, characterized in that: The upper interface of the oil fume separation device is equipped with a threaded cap.
7. The apparatus for secondary treatment of experimental coke oven raw gas according to claim 1, characterized in that: The inlet and outlet of the condenser are both connected to a low-temperature constant-temperature reaction bath.
8. The apparatus for secondary treatment of experimental coke oven raw gas according to claim 1, characterized in that: A connecting pipe is provided between the two condensers.