A processor and a processing system capable of treating wastewater and waste oil in organic exhaust gas

Abstract

The utility model discloses a kind of processor and processing system that can handle wastewater, waste oil in organic waste gas, processor includes liquid inlet tank, vapor-liquid separation tank being set on the top of liquid inlet tank and the vaporization pipe fixedly communicated with vapor-liquid separation tank and liquid inlet tank at two ends;First heating device is equipped on the vaporization pipe, the liquid inlet tank is fixedly communicated with processor import pipe, the vapor-liquid separation tank top is fixedly communicated with exhaust pipe, the vapor-liquid separation tank bottom is fixedly communicated with liquid guide pipe.Reclaimed rubber in production process, the hot dirty organic waste gas containing water vapor, oil gas and the wastewater and waste oil that pipeline is cooled out during waste gas conveying are all purified and gasified then enter incinerator and are incinerated, so impurity is almost none, to be more easily combusted, and combustion is more sufficient and thorough, residue after combustion will be little, incinerator is not easy to block, more durable, prolong the service life of incinerator.

Description

Technical Field

[0001] This utility model relates to the field of organic waste gas treatment technology, and in particular to a processor and treatment system that can treat wastewater and waste oil in organic waste gas. Background Technology

[0002] The production of reclaimed rubber generates hot, dirty organic waste gas. However, the small amounts of accompanying wastewater, waste oil, and dust that leach out during pipeline transportation are difficult to treat. While incinerators can currently treat the organic waste gas, they cannot simultaneously handle the small amounts of wastewater and waste oil, a problem that plagues many reclaimed rubber manufacturers and environmental equipment manufacturers. Directly feeding this organic waste gas containing small amounts of wastewater and waste oil into the incinerator will cause coking, leading to a decreasing capacity for organic waste gas treatment and, over time, blockage, making the incinerator less durable. Therefore, how to simultaneously treat the wastewater and waste oil leached from the organic waste gas, while ensuring stable, simple, and durable operation of the treatment equipment, is a common challenge faced by every company. Utility Model Content

[0003] The technical problem to be solved by this utility model is to provide a processor and processing system that can treat wastewater and waste oil in organic waste gas, so as to solve the problem that current incinerators are not easy to use and not durable when treating organic waste gas containing small amounts of wastewater and waste oil.

[0004] To solve the above-mentioned technical problems, the technical solution adopted by this utility model is as follows:

[0005] A processor capable of treating wastewater and waste oil in organic waste gas includes an inlet tank, a vapor-liquid separation tank disposed above the inlet tank, and a vaporization pipe whose two ends are fixedly connected to the vapor-liquid separation tank and the inlet tank, respectively; the vaporization pipe is provided with a first heating device, the inlet tank is fixedly connected to a processor inlet pipe, the top of the vapor-liquid separation tank is fixedly connected to an exhaust pipe, and the bottom of the vapor-liquid separation tank is fixedly connected to a liquid guide pipe.

[0006] Furthermore, it also includes a secondary separation tank connected to the bottom of the liquid inlet tank. The secondary separation tank is fixedly connected to the liquid guide pipe. The processor oil drain pipe is fixedly connected to the middle of the secondary separation tank. A water inlet pipe is fixedly connected to the top of the vapor-liquid separation tank. A drain pipe is fixedly connected to the bottom of the secondary separation tank. A water pump is connected between the drain pipe and the water inlet pipe. The liquid in the water pump flows from the drain pipe to the water inlet pipe.

[0007] Furthermore, at least two vertical partitions are spaced apart inside the vapor-liquid separator, and adjacent partitions are staggered in the horizontal direction. The partitions divide the interior of the vapor-liquid separator into a vapor chamber and a liquid chamber. The vaporization pipe is connected to the vapor chamber, and the liquid guide pipe is connected to the vapor chamber. The vapor chamber and the liquid chamber are connected by a serpentine flow channel formed by the partitions.

[0008] Furthermore, it also includes an insulation box, in which the liquid inlet box, vapor-liquid separation box, vaporization pipe and liquid guide pipe are all installed. The processor inlet pipe and exhaust pipe extend outside the insulation box. The two sides of the insulation box are respectively fixedly connected to a waste heat inlet pipe and a waste heat outlet pipe.

[0009] A treatment system for treating wastewater and waste oil in organic waste gas, using the aforementioned processor for treating wastewater and waste oil in organic waste gas, further includes a gas-liquid dust separation filter and an oil evaporator. The gas-liquid dust separation filter includes a closed cylindrical body and a filter inlet pipe, a filter exhaust pipe, and a filter oil drain pipe, which are respectively fixedly connected to the cylindrical body. The filter exhaust pipe and the exhaust pipe are both connected to the incinerator inlet pipe of the incinerator. The oil evaporator is connected between the incinerator inlet pipe and the processor oil drain pipe, and the filter oil drain pipe is connected to the processor inlet pipe.

[0010] Furthermore, the filter exhaust pipe is located at the upper part of the cylinder, the filter inlet pipe is located tangentially to the middle part of the cylinder, the filter oil drain pipe is located at the bottom of the cylinder, and the gas-liquid dust separation filter also includes a filter cylinder located in the middle of the cylinder and an isolation cylinder sleeved between the filter cylinder and the cylinder. Inside the cylinder, a spacer is fixedly connected between the filter exhaust pipe and the filter inlet pipe, and the tops of the filter cylinder and the isolation cylinder are both fixedly connected to the spacer.

[0011] Furthermore, the spacer ring includes an outer ring, a middle ring, and an inner ring that are fixedly connected in sequence along the axial direction of the cylinder. The inner ring is fixedly connected to the top of the filter cylinder, the top of the spacer cylinder is fixedly connected to the middle ring, and the outer ring is fixedly connected to the cylinder body.

[0012] Furthermore, the filter cylinder includes several vertical stiffeners evenly distributed along the circumference of the inner hole of the spacer, steel wires wound around the stiffeners, and a filter screen covering the steel wires. The upper ends of the stiffeners are fixedly connected to the spacer, and the lower ends of the stiffeners are fixedly connected to a bottom plate that blocks the bottom of the filter screen. The bottom of the cylinder is fixedly connected to a third cleaning pipe, and the bottom of the third cleaning pipe is detachably connected to a sealing plate.

[0013] Furthermore, the waste heat intake short pipe is connected to the incinerator exhaust pipe of the incinerator through the first connecting pipe, and the waste heat exhaust short pipe is fixedly connected to the exhaust main pipe; a bypass pipe is fixedly connected between the exhaust main pipe and the first connecting pipe, the bypass pipe is provided with a first valve, and the first connecting pipe is provided with a second valve at the part between the bypass pipe and the waste heat intake short pipe.

[0014] Furthermore, the oil evaporator includes a shell, the top of which is sealed, and a three-way pipe is provided on the top of the shell. One port of the three-way pipe is fixedly connected to the top of the shell through a flange, the other port of the three-way pipe is the oil evaporator outlet pipe, and the third port of the three-way pipe is the oil evaporator inlet pipe. A second heating device is provided outside the shell. The oil evaporator outlet pipe is connected to the incinerator air inlet pipe. An oil evaporator oil inlet pipe is fixedly connected near the top of the shell and is connected to the processor oil discharge pipe.

[0015] The positive effects of this utility model are:

[0016] The hot, dirty organic waste gas generated during reclaimed rubber production is separated by a gas-liquid dust separator. The resulting wastewater and waste oil are then treated by a processor. The water is vaporized into steam and incinerated in the incinerator. The oil, after purification, is heated and vaporized in an oil evaporator before entering the incinerator for further combustion. This process purifies and vaporizes the hot, dirty organic waste gas generated during reclaimed rubber production, as well as the wastewater and waste oil released during pipeline transport, before incinerating them. Because evaporation and combustion result in almost no impurities entering the incinerator, combustion is easier, more complete, and more thorough, leaving minimal residue. This also reduces the likelihood of clogging in the incinerator, making it more durable and extending its lifespan. Furthermore, the processor uses a vertically oriented vaporization pipe, which reduces scale buildup on its inner walls, extending the processor's maintenance and cleaning intervals and further increasing its lifespan. Attached Figure Description

[0017] Figure 1 This is a schematic diagram of the processor's structure;

[0018] Figure 2 yes Figure 1 A cross-sectional view of the AA section;

[0019] Figure 3 This is a schematic diagram of the processing system;

[0020] Figure 4 This is a schematic diagram of the structure of a gas-liquid dust separation filter;

[0021] In the picture:

[0022] 1. Secondary Separator; 2. Processor Oil Drain Pipe; 3. First Cleaning Pipe; 4. Liquid Inlet Tank; 5. Waste Heat Inlet Short Pipe; 6. Insulation Box; 7. Processor Inlet Pipe; 8. Exhaust Pipe; 9. Vapor-Liquid Separator; 10. Baffle Plate; 11. Liquid Guide Pipe; 12. Vaporization Pipe; 13. Heating Wire; 14. Waste Heat Outlet Short Pipe; 15. Second Cleaning Pipe; 16. Water Level Sensor; 17. Drain Pipe; 18. Water Inlet Pipe; 19. Third Cleaning Pipe; 20. Filter Oil and Drain Pipe; 21. Cylinder; 22. Isolation Cylinder; 23. Outer Ring; 24. Filter Exhaust Pipe; 25. Plug; 26. Inner Ring; 27. Intermediate Ring; 28. Filter Inlet Pipe; 29. ​​Rib Plate; 30. Steel Wire; 31. Filter Screen; 3 2. Base plate; 33. Filter cartridge; 34. Bypass pipe; 35. First valve; 36. First connecting pipe; 37. Exhaust fan; 38. Incinerator exhaust pipe; 39. Second valve; 40. Incinerator; 41. Second connecting pipe; 42. Oil evaporator; 43. Incinerator air inlet pipe; 44. Third connecting pipe; 45. Oil evaporator outlet pipe; 46. Oil evaporator inlet pipe; 47. Oil evaporator oil inlet pipe; 48. Fourth connecting pipe; 49. Fifth connecting pipe; 50. Sixth connecting pipe; 51. Processor; 52. Main exhaust pipe; 53. Water pump; 54. Oil pump; 55. Gas-liquid-dust separator filter; 56. Steam chamber; 57. Flow channel; 58. Liquid chamber; 59. Spacer ring; 60. Cover. Detailed Implementation

[0023] Example 1

[0024] like Figures 1 to 3 As shown, a processor capable of treating wastewater and waste oil in organic waste gas includes a secondary separation tank 1, a liquid inlet tank 4, vaporization pipes 12, and a vapor-liquid separation tank 9, welded sequentially from bottom to top. Three vaporization pipes 12 are arranged side-by-side (the number of vaporization pipes 12 can be selected according to the processing capacity; the number can be increased accordingly for larger processing capacities). All three vaporization pipes 12 are vertically arranged, with their upper and lower ends connected to the bottom of the vapor-liquid separation tank 9 and the top of the liquid inlet tank 4, respectively. The top of the vapor-liquid separation tank 9 has an inspection port corresponding to each vaporization pipe 12. Each inspection port is covered with a cover 60, which is connected to the vapor-liquid separation tank 9 by screws. Opening the cover 60 allows for cleaning of the inner wall of the vaporization pipes 12 and the interior of the vapor-liquid separation tank 9.

[0025] The secondary separation tank 1, the liquid inlet tank 4, and the vapor-liquid separation tank 9 are all rectangular box structures welded from steel plates. The vaporization pipe 12 is cylindrical and equipped with a first heating device, which is a heating wire 13 wound around the vaporization pipe 12. A second cleaning pipe 15 is welded to the right side of the secondary separation tank 1, and a first cleaning pipe 3 is welded to the left side of the liquid inlet tank 4. Both the second cleaning pipe 15 and the first cleaning pipe 3 are covered with sealing caps at their outer ends. By opening the corresponding sealing caps, dirt or sediment inside the secondary separation tank 1 or the liquid inlet tank 4 can be cleaned.

[0026] The vapor-liquid separator 9 has two vertical partitions 10 spaced apart on its right side. Adjacent partitions 10 are staggered horizontally, dividing the internal cavity of the vapor-liquid separator 9 into a vapor chamber 56 on the left and a liquid chamber 58 on the right. A vertical liquid guide pipe 11 is fixedly connected to the bottom of the vapor-liquid separator 9 near the right end. The upper end of the liquid guide pipe 11 is connected to the liquid chamber 58, and the upper end of the liquid guide pipe 11 extends 3 to 5 cm above the bottom surface of the liquid chamber 58. The lower end of the liquid guide pipe 11 is fixedly connected to the top of the secondary separator 1.

[0027] A vertical exhaust pipe 8 is fixedly connected to the top of the vapor-liquid separator 9 near the left end. The upper end of the vaporization pipe 12 is connected to the bottom of the vapor collection chamber 56, and the lower end is connected to the top of the liquid inlet tank 4. The vapor collection chamber 56 and the liquid collection chamber 58 are connected by a serpentine flow channel 57 formed by two partitions 10. The upper end of the liquid guide pipe 11 is connected to the liquid collection chamber 58 at the position away from the outlet of the flow channel 57. The liquid inlet tank 4 is fixedly connected to the processor inlet pipe 7 at the top left. The processor oil drain pipe 2, which is connected to the interior of the secondary separator 1, is welded to the top left side.

[0028] The liquid inlet tank 4 is fixedly connected to a water inlet pipe 18 at its bottom right. The vapor-liquid separator 9 is fixedly connected to a drain pipe 17 at its top left position. A water pump 53 is connected between the drain pipe 17 and the water inlet pipe 18. The liquid in the water pump 53 flows from the drain pipe 17 to the water inlet pipe 18. The secondary separator 1 is also equipped with a water level sensor 16 at its bottom right, which is used to detect the water level in the secondary separator 1 (using the principle that water conducts electricity while oil does not, so only the water level is detected). When the water level in the secondary separator 1 reaches a set value (e.g., 10cm), the water pump 53 starts and discharges the water in the secondary separator 1 into the vapor-liquid separator 9, so that this part of the water is vaporized again.

[0029] The working process of this utility model is as follows:

[0030] The wastewater and waste oil generated from the separation and filtration of organic hot and dirty exhaust gas produced in the reclaimed rubber production process enter the inlet tank 4 through the processor inlet pipe 7. The heating wire 13 outside the vaporization pipe 12 is energized to heat the vaporization pipe 12 to a temperature of about 120°C. The water in the waste liquid boils and vaporizes, and is discharged from the exhaust pipe 8 and enters the incinerator 40 for incineration. The oil in the waste liquid, because its density is less than that of water and it is immiscible with water, floats on the water surface and forms a stratification. After being stabilized and stratified by the flow channel 57, it enters the collection chamber 58. Since the upper end of the liquid guide pipe 11 is slightly higher than the bottom surface of the collection chamber 58, the oil level in the collection chamber 58 is higher than the top of the liquid guide pipe 11, and the oil flows down from the liquid guide pipe 11 into the secondary separation tank 1.

[0031] When the vaporization tube 12 heats the waste liquid, it produces some gelatinous material, which, along with some impurities in the waste liquid, settles to the bottom of the inlet tank 4 under gravity and solidifies into lumps. These solidified lumps can be cleaned by periodically opening the sealing cap on the first cleaning tube 3. Because the vaporization tube 12 is vertical, these gelatinous materials do not condense or scale on the vaporization tube 12 as they fall under the thrust of air bubbles and gravity, thus ensuring the unobstructed flow of the vaporization tube 12. This vertical design of the vaporization tube 12 is characterized by its resistance to scaling, reducing the maintenance workload of the processor 51 and extending its service life.

[0032] The oil in the secondary separation box 1 is discharged through the processor oil drain pipe 2, and after being gasified, it enters the incinerator 40 for incineration.

[0033] Because the waste oil entering the secondary separation tank 1 through the liquid guide pipe 11 contains a small amount of water, and since oil density is less than water and they are immiscible, this water will collect at the bottom of the secondary separation tank 1. When the set value is reached, it will be discharged into the vapor-liquid separation tank 9 by the water pump 53. After flowing into the vaporization pipe 12, it will be vaporized again through the vaporization pipe 12, thereby preventing excessive water deposition in the secondary separation tank 1, thus making the oil discharged from the processor oil drain pipe 2 purer.

[0034] Example 2

[0035] The difference between this embodiment and Embodiment 1 is that:

[0036] The processor 51 also includes an insulation box 6, an inlet tank 4, a vapor-liquid separation box 9, a vaporization pipe 12 and a liquid guide pipe 11, all of which are located inside the insulation box 6. The outer ends of the processor inlet pipe 7, the exhaust pipe 8, the first cleaning pipe 3 and the water inlet pipe 18 all extend outside the insulation box 6. The two sides of the insulation box 6 are respectively fixedly connected to a waste heat inlet short pipe 5 and a waste heat outlet short pipe 14.

[0037] The incinerator exhaust pipe 38 of the incinerator 40 is connected to the waste heat inlet pipe 5, thereby guiding the hot waste gas generated during the operation of the incinerator 40 into the insulation box 6, and then discharging it from the waste heat outlet pipe 14. The waste heat of the incinerator 40 is used to heat the liquid inlet box 4 and the gas-liquid separator 9, thereby saving the electrical energy consumed by the heating wire 13 and achieving the effect of energy saving.

[0038] Example 3

[0039] Combination Figure 4 As shown, this embodiment discloses a treatment system that can treat wastewater and waste oil in organic waste gas. It adopts the processor 51 in embodiment 2 and also includes a gas-liquid-dust separation filter 55 and an oil evaporator 42.

[0040] The gas-liquid dust separator 55 includes a closed cylindrical body 21, a filter exhaust pipe 24 fixedly connected to the upper left side of the body 21, a filter oil drain pipe 20 fixedly connected to the lower left side of the body 21, and a filter inlet pipe 28 fixedly connected tangentially to the middle right side of the body 21. A plug 25 is bolted to the top of the body 21 to seal the top and facilitate maintenance and replacement of the internal filter components. A circular plug plate is welded to the bottom of the body 21, and a third cleaning pipe 19 communicating with the interior of the body 21 is welded to the center of the plug plate. The lower end of the third cleaning pipe 19 is also bolted to a plug plate.

[0041] A filter cylinder 33 is provided in the middle of the cylinder body 21, and an isolation cylinder 22 is sleeved between the filter cylinder 33 and the cylinder body 21. Inside the cylinder body 21, a spacer ring 59 is fixedly connected between the filter exhaust pipe 24 and the filter inlet pipe 28. The tops of the filter cylinder 33 and the isolation cylinder 22 are both fixedly connected to the spacer ring 59.

[0042] The spacer 59 includes an outer ring 23, an intermediate ring 27, and an inner ring 26 that are fixedly connected sequentially along the axial direction of the cylinder 21. The inner ring 26 is welded to the top of the filter cylinder 33, the top of the isolation cylinder 22 is welded to the intermediate ring 27, and the outer ring 23 is welded to the cylinder 21. The outer ring 23, the intermediate ring 27, and the inner ring 26 are all located between the filter exhaust pipe 24 and the filter inlet pipe 28, dividing the internal space of the cylinder 21 into upper and lower parts.

[0043] The filter cartridge 33 includes ten vertical stiffeners 29 evenly distributed along the circumference of the inner ring 26, steel wires 30 wound around the stiffeners 29, and a filter screen 31 covering the steel wires 30. The stiffeners 29 have semi-circular grooves at their contact points with the steel wires 30 to prevent the steel wires 30 from slipping on the stiffeners 29. A cylinder is welded inside the inner ring 26, and the upper ends of the stiffeners 29 are welded to the inner wall of the cylinder. A circular bottom plate 32 is welded to the lower end of the stiffeners 29, blocking the bottom of the filter screen 31.

[0044] The filter exhaust pipe 24 and the steam exhaust pipe 8 are both connected to the incinerator inlet pipe 43 of the incinerator 40. The oil evaporator 42 is connected between the incinerator inlet pipe 43 and the processor oil drain pipe 2. The filter oil drain pipe 20 and the processor inlet pipe 7 are connected through the sixth connecting pipe 50.

[0045] The oil evaporator 42 includes a cylindrical, enclosed shell. A T-shaped tee pipe is located at the top of the shell. The bottom end of the tee pipe is fixedly connected to the top of the shell via a flange. The left end of the tee pipe is the oil evaporator outlet pipe 45, and the right end is the oil evaporator inlet pipe 46. A second heating device, also a heating wire 13, is located outside the shell and is wound around it to heat the shell, causing the oil inside to vaporize. The oil evaporator inlet pipe 46 and the filter exhaust pipe 24 are fixedly connected via a fourth connecting pipe 48. The exhaust pipe 8 is fixedly connected to the fourth connecting pipe 48 via a fifth connecting pipe 49. The oil evaporator outlet pipe 45 is fixedly connected to the incinerator inlet pipe 43 via a third connecting pipe 44. An oil evaporator inlet pipe 47 is fixedly connected near the top of the shell. The oil evaporator inlet pipe 47 is fixedly connected to the processor exhaust pipe 2 via a second connecting pipe 41, on which an oil pump 54 is mounted.

[0046] exist Figure 3 In the diagram, dashed arrows indicate the direction of gas flow, while solid arrows indicate the direction of liquid flow.

[0047] The hot, dirty organic waste gas (containing wastewater, waste oil, and dust) generated during the production of reclaimed rubber enters the cylinder 21 tangentially from right to left through the filter inlet pipe 28 and rotates in the gap between the cylinder 21 and the isolation cylinder 22. Liquid and impurities (including dust and rubber particles) in the organic waste gas are thrown against the inner wall of the cylinder 21 by centrifugal force, then slide down the inner wall and fall to the bottom of the cylinder 21. Dust settles at the bottom of the cylinder 21 and can be cleaned by periodically opening the sealing plate at the bottom of the third cleaning pipe 19. Wastewater and waste oil enter the liquid inlet tank 4 through the sixth connecting pipe 50.

[0048] Because the filter screen 31 is equipped with an isolation cylinder 22, organic waste gas is prevented from blowing directly onto the filter screen 31, which would cause the filter screen 31 to become clogged, thus extending the time for cleaning and replacing the filter screen 31.

[0049] The organic waste gas continues to flow to the left and enters the fourth connecting pipe 48 through the filter exhaust pipe 24, and together with the water vapor discharged from the exhaust pipe 8, it enters the shell through the oil evaporator inlet pipe 46. Then, it enters the incinerator 40 for incineration after passing through the oil evaporator outlet pipe 45, the third connecting pipe 44 and the incinerator inlet pipe 43 in sequence.

[0050] Under the action of oil pump 54, the oil in the secondary separation tank 1 enters the housing after passing through the processor drain pipe 2, the second connecting pipe 41, and the oil evaporator inlet pipe 47. The housing is heated by the heating wire 13 outside the housing (the heating temperature is about 200 to 240°C; since the temperature in the reclaimed rubber production process does not exceed 400°C, the vaporization temperature of the separated oil also does not exceed 400°C), causing the oil in the housing to vaporize. Then, it enters the incinerator 40 for incineration after passing through the oil evaporator outlet pipe 45, the third connecting pipe 44, and the incinerator inlet pipe 43. The gel-like substances and other impurities produced by the heated oil in the housing will settle at the bottom of the housing. These gel-like substances and impurities can be cleaned by periodically opening the cover at the bottom of the housing.

[0051] After being processed by the gas-liquid dust separator 55, the waste dust, colloids, and impurities in the organic hot and dirty waste gas are filtered out. The waste oil and wastewater in the organic waste gas are processed by the processor 51 and the oil evaporator 42. The wastewater is evaporated into water vapor, and the waste oil is heated into gas, both of which enter the incinerator 40 for treatment, thus treating the wastewater and waste oil in the organic waste gas. At the same time, since water and oil enter the incinerator 40 in gaseous form, there are almost no impurities, making it easier to burn and resulting in more complete and thorough combustion. There are very few residues after combustion, and the heat exchange tubes inside the incinerator 40 are less prone to clogging, making them more durable and extending the maintenance and cleaning intervals and service life of the incinerator 40. In addition, the heating elements (such as heating strips) in the incinerator 40, which uses electric auxiliary heating, are less prone to the adhesion of inorganic matter, which does not affect the heating of these heating elements and extends their service life.

[0052] The outlet of the waste heat intake short pipe 5 is connected to an induced draft fan 37. The outlet of the induced draft fan 37 is connected to the incinerator exhaust pipe 38 of the incinerator 40 through a first connecting pipe 36. The waste heat exhaust short pipe 14 is fixedly connected to the exhaust main pipe 52. A bypass pipe 34 is fixedly connected between the exhaust main pipe 52 and the first connecting pipe 36. A first valve 35 is provided on the bypass pipe 34. A second valve 39 is provided on the first connecting pipe 36 at the position between the bypass pipe 34 and the waste heat intake short pipe 5.

[0053] By opening the second valve 39 and closing the first valve 35, the waste heat from the incinerator 40 can be used to heat the processor 51, achieving energy conservation. When the furnace temperature inside the incinerator 40 exceeds the set temperature (e.g., 750℃ to 760℃), the first valve 35 can be opened and the second valve 39 closed to prevent damage to the processor 51 and the incinerator 40 due to overheating. (This is because when the temperature inside the incinerator 40 exceeds the set temperature, the exhaust temperature of the incinerator 40 rises, causing the temperature of the processor 51 to rise accordingly. The gas discharged from the processor 51 also contains more oil and gas, meaning the calorific value of the gas discharged from the processor 51 is high. Combustion inside the incinerator 40 generates a large amount of heat, further increasing the temperature of the incinerator 40, which in turn further increases the temperature of the processor 51, leading to a vicious cycle that ultimately damages either the incinerator 40 or the processor 51 due to overheating.)

[0054] The above embodiments are described in detail and specifically, illustrating preferred embodiments of the present utility model. They are only used to illustrate the technical ideas and features of the present utility model, with the aim of enabling those skilled in the art to understand the content of the present utility model and implement it accordingly. However, they are not limited to the present utility model, and the patent scope of the present utility model cannot be limited by this embodiment alone. That is, any equivalent changes or modifications made to the spirit disclosed in the present utility model, without departing from the structure of the present utility model, such as local improvements within the system and modifications or transformations between subsystems, are still within the patent scope of the present utility model.

Claims

1. A processor capable of treating wastewater and waste oil in organic waste gas, characterized in that, It includes an inlet tank (4), a vapor-liquid separation tank (9) located above the inlet tank (4), and a vaporization pipe (12) whose two ends are fixedly connected to the vapor-liquid separation tank (9) and the inlet tank (4) respectively; the vaporization pipe (12) is provided with a first heating device, the inlet tank (4) is fixedly connected to a processor inlet pipe (7), the top of the vapor-liquid separation tank (9) is fixedly connected to a steam exhaust pipe (8), and the bottom of the vapor-liquid separation tank (9) is fixedly connected to a liquid guide pipe (11).

2. The processor for treating wastewater and waste oil in organic waste gas according to claim 1, characterized in that, It also includes a secondary separation tank (1) connected to the bottom of the liquid inlet tank (4). The secondary separation tank (1) is fixedly connected to the liquid guide pipe (11). The processor oil drain pipe (2) is fixedly connected to the middle of the secondary separation tank (1). The water inlet pipe (18) is fixedly connected to the top of the vapor-liquid separation tank (9). The drain pipe (17) is fixedly connected to the bottom of the secondary separation tank (1). A water pump (53) is connected between the drain pipe (17) and the water inlet pipe (18). The liquid in the water pump (53) flows from the drain pipe (17) to the water inlet pipe (18).

3. The processor for treating wastewater and waste oil in organic waste gas according to claim 1, characterized in that, The vapor-liquid separator (9) is provided with at least two vertical partitions (10) spaced apart. The adjacent partitions (10) are staggered in the horizontal direction. The partitions (10) divide the interior of the vapor-liquid separator (9) into a vapor chamber (56) and a liquid chamber (58). The vaporization pipe (12) is connected to the vapor chamber (56), and the liquid guide pipe (11) is connected to the vapor chamber (56). The vapor chamber (56) and the liquid chamber (58) are connected by a serpentine flow channel (57) formed by the partitions (10).

4. The processor for treating wastewater and waste oil in organic waste gas according to claim 2, characterized in that, It also includes an insulation box (6), the liquid inlet box (4), the vapor-liquid separation box (9), the vaporization pipe (12) and the liquid guide pipe (11) are all installed inside the insulation box (6), the processor inlet pipe (7) and the exhaust pipe (8) extend outside the insulation box (6), and the two sides of the insulation box (6) are respectively fixedly connected to the waste heat inlet pipe (5) and the waste heat outlet pipe (14).

5. A treatment system for treating wastewater and waste oil in organic waste gas, characterized in that, The processor, which can treat wastewater and waste oil in organic waste gas as described in claim 4, further includes a gas-liquid dust separation filter (55) and an oil evaporator (42). The gas-liquid dust separation filter (55) includes a closed cylinder (21) and a filter inlet pipe (28), a filter exhaust pipe (24), and a filter oil drain pipe (20) respectively fixedly connected to the cylinder (21). The filter exhaust pipe (24) and the exhaust pipe (8) are both connected to the incinerator inlet pipe (43) of the incinerator (40). The oil evaporator (42) is connected between the incinerator inlet pipe (43) and the processor oil drain pipe (2). The filter oil drain pipe (20) is connected to the processor inlet pipe (7).

6. A treatment system for treating wastewater and waste oil in organic waste gas according to claim 5, characterized in that, The filter exhaust pipe (24) is located at the upper part of the cylinder (21), the filter inlet pipe (28) is located tangentially to the middle part of the cylinder (21), the filter oil drain pipe (20) is located at the bottom of the cylinder (21), the gas-liquid dust separation filter (55) also includes a filter cylinder (33) located in the middle of the cylinder (21) and an isolation cylinder (22) sleeved between the filter cylinder (33) and the cylinder (21), a spacer (59) is fixedly connected inside the cylinder (21) between the filter exhaust pipe (24) and the filter inlet pipe (28), and the tops of the filter cylinder (33) and the isolation cylinder (22) are fixedly connected to the spacer (59).

7. A treatment system for treating wastewater and waste oil in organic waste gas according to claim 6, characterized in that, The spacer (59) includes an outer ring (23), a middle ring (27) and an inner ring (26) that are fixedly connected in sequence along the axial direction of the cylinder (21). The inner ring (26) is fixedly connected to the top of the filter cylinder (33), the top of the isolation cylinder (22) is fixedly connected to the middle ring (27), and the outer ring (23) is fixedly connected to the cylinder (21).

8. A treatment system for treating wastewater and waste oil in organic waste gas according to claim 6, characterized in that, The filter cylinder (33) includes several vertical stiffeners (29) evenly distributed along the circumference of the inner hole of the partition ring (59), steel wires (30) wrapped around the stiffeners (29), and a filter screen (31) covering the steel wires (30). The upper ends of the stiffeners (29) are fixedly connected to the partition ring (59), and the lower ends of the stiffeners (29) are fixedly connected to a bottom plate (32) that blocks the bottom of the filter screen (31). The bottom of the cylinder (21) is fixedly connected to a third cleaning pipe (19), and the bottom of the third cleaning pipe (19) is detachably connected to a sealing plate.

9. A treatment system for treating wastewater and waste oil in organic waste gas according to claim 5, characterized in that, The waste heat intake short pipe (5) is connected to the incinerator exhaust pipe (38) of the incinerator (40) through the first connecting pipe (36). The waste heat exhaust short pipe (14) is fixedly connected to the exhaust main pipe (52). A bypass pipe (34) is fixedly connected between the exhaust main pipe (52) and the first connecting pipe (36). A first valve (35) is provided on the bypass pipe (34). A second valve (39) is provided on the first connecting pipe (36) between the bypass pipe (34) and the waste heat intake short pipe (5).

10. A treatment system for treating wastewater and waste oil in organic waste gas according to claim 5, characterized in that, The oil evaporator (42) includes a shell, the top of which is sealed, and a three-way pipe is provided on the top of the shell. One of the ports of the three-way pipe is fixedly connected to the top of the shell through a flange. The other port of the three-way pipe is the oil evaporator outlet pipe (45), and the third port of the three-way pipe is the oil evaporator inlet pipe (46). A second heating device is provided outside the shell. The oil evaporator outlet pipe (45) is connected to the incinerator air inlet pipe (43). An oil evaporator oil inlet pipe (47) is fixedly connected near the top of the shell. The oil evaporator oil inlet pipe (47) is connected to the processor oil drain pipe (2).

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