Treatment device and treatment system capable of treating wastewater and waste oil in organic waste gas

Abstract

The invention discloses a treater and a treatment system capable of treating wastewater and waste oil in organic waste gas. The treater comprises a liquid inlet box, a vapor-liquid separation box arranged above the liquid inlet box and a vaporization pipe, wherein the two ends of the vaporization pipe are fixedly communicated with the vapor-liquid separation box and the liquid inlet box respectively; the vaporizing pipe is provided with a first heating device, the liquid inlet box is fixedly communicated with a processor inlet pipe, the top of the vapor-liquid separation box is fixedly communicated with a vapor exhaust pipe, and the bottom of the vapor-liquid separation box is fixedly communicated with a liquid guide pipe. In the production process of reclaimed rubber, generated hot dirty organic waste gas containing water vapor and oil gas and waste water and waste oil separated out by cooling in a pipeline during waste gas conveying are purified and gasified and then enter an incinerator to be incinerated, so that almost no impurity exists, combustion is easier, combustion is more sufficient and thorough, and the environment-friendly effect is achieved. And after combustion, residues are few, and the incinerator is not easy to block and is more durable, so that the service life of the incinerator is prolonged.

Description

TECHNICAL FIELD

[0001] The present application relates to the technical field of organic waste gas treatment, and particularly relates to a processor and a treatment system capable of treating wastewater and waste oil in organic waste gas. BACKGROUND

[0002] In the production process of reclaimed rubber, hot dirty organic waste gas is generated, but a small amount of associated wastewater and waste oil and dust separated out in the pipeline conveying of the organic waste gas are difficult to treat. At present, although the organic waste gas can be treated by a burning furnace, the small amount of wastewater and waste oil separated out cannot be treated at the same time, which puzzles the reclaimed rubber production manufacturers and environmental protection equipment manufacturers. If the organic waste gas containing a small amount of wastewater and waste oil is directly burned in the burning furnace, coking will occur in the burning furnace, the treatment capacity of the burning furnace for the organic waste gas will become smaller and smaller, and the burning furnace will be blocked after a long time, so that the burning furnace is not durable. Therefore, while the organic waste gas is treated, how to treat the wastewater and waste oil separated out in the organic waste gas at the same time, and how to make the treatment equipment run stably, simply and durably are difficult problems faced by each enterprise. SUMMARY

[0003] The present application solves the technical problem of providing a processor and a treatment system capable of treating wastewater and waste oil in organic waste gas, so as to solve the problems that the burning furnace is not easy to use and not durable when treating the organic waste gas containing a small amount of wastewater and waste oil.

[0004] To solve the above technical problems, the technical scheme adopted by the present application is as follows:

[0005] A processor capable of treating wastewater and waste oil in organic waste gas, comprising a liquid inlet tank, a vapor-liquid separation tank arranged above the liquid inlet tank, and a vaporization pipe fixedly communicated with the vapor-liquid separation tank and the liquid inlet tank at two ends; a first heating device is arranged on the vaporization pipe; a processor inlet pipe is fixedly communicated with the liquid inlet tank; a steam discharge pipe is fixedly communicated with the top of the vapor-liquid separation tank; and a liquid guide pipe is fixedly communicated with the bottom of the vapor-liquid separation tank.

[0006] Further, a secondary separation tank is connected to the bottom of the liquid inlet tank, the secondary separation tank is fixedly communicated with the liquid guide pipe, a processor oil discharge pipe is fixedly communicated with the middle of the secondary separation tank, a water inlet pipe is fixedly communicated with the vapor-liquid separation tank, a water discharge pipe is fixedly communicated with the bottom of the secondary separation tank, a water pump is connected between the water discharge pipe and the water inlet pipe, and the flow direction of the liquid in the water pump is from the water discharge pipe to the water inlet pipe.

[0007] Further, at least two vertical baffles are arranged in the vapor-liquid separation tank at intervals, adjacent baffles are arranged in a staggered manner in the horizontal direction, the baffles divide the vapor-liquid separation tank into a vapor collecting chamber and a liquid collecting chamber, the vaporization pipe is communicated with the vapor collecting chamber, the liquid guide pipe is communicated with the vapor collecting chamber, and the vapor collecting chamber and the liquid collecting chamber are communicated through a serpentine flow channel formed by the baffles.

[0008] Further, the heat preservation box is provided with a waste heat inlet short pipe and a waste heat outlet short pipe.

[0009] The treatment system for treating waste water and waste oil in organic waste gas comprises the treatment device for treating waste water and waste oil in organic waste gas, a gas-liquid-dust separation filter and an oil evaporator.

[0010] Further, the filter outlet pipe is arranged at the upper part of the cylinder body, the filter inlet pipe is arranged at the middle part of the cylinder body along the tangential direction of the cylinder body, and the filter oil-water discharge pipe is arranged at the bottom of the cylinder body.

[0011] Further, the spacer ring comprises an outer ring, an intermediate ring and an inner ring which are fixedly connected along the axial direction of the cylinder body in sequence, the inner ring is fixedly connected with the top of the filter cylinder, the top of the isolation cylinder is fixedly connected with the intermediate ring, and the outer ring is fixedly connected with the cylinder body.

[0012] Further, the filter cylinder comprises a plurality of vertical rib plates which are uniformly distributed along the circumferential direction of the inner hole of the spacer ring, a steel wire which is wound outside the rib plates, and a filter screen which is coated outside the steel wire, the upper ends of the rib plates are fixedly connected with the spacer ring, and the lower ends of the rib plates are fixedly connected with a bottom plate which is blocked at the bottom of the filter screen.

[0013] Further, the waste heat inlet short pipe is communicated with the incinerator exhaust pipe of the incinerator through a first connecting pipe, the waste heat outlet short pipe is fixedly communicated with an exhaust main pipe, a bypass pipe is fixedly communicated between the exhaust main pipe and the first connecting pipe, a first valve is arranged on the bypass pipe, and a second valve is arranged on the first connecting pipe between the bypass pipe and the waste heat inlet short pipe.

[0014] Further, the oil evaporator comprises a shell, the shell top is blocked, the shell top is provided with a tee pipe, one of the pipe openings of the tee pipe is fixedly communicated with the shell top through a flange, the other pipe opening of the tee pipe is an oil evaporator outlet pipe, the third pipe opening of the tee pipe is an oil evaporator inlet pipe, the shell is externally provided with a second heating device, the oil evaporator outlet pipe is communicated with an incinerator inlet pipe, the shell is fixedly communicated with an oil evaporator oil inlet pipe close to the top, and the oil evaporator oil inlet pipe is communicated with a processor oil discharge pipe.

[0015] The positive effects of the present application are:

[0016] The waste liquid formed by the waste water and waste oil separated after the hot dirty organic waste gas generated in the production of reclaimed rubber is separated by the gas-liquid dust separation filter is treated by the processor, the water therein is vaporized into water vapor and enters the incinerator for incineration, and the oil therein is purified and then enters the incinerator for incineration after being heated and vaporized by the oil evaporator. Thus, the hot dirty organic waste gas generated in the production of reclaimed rubber and the waste water and waste oil separated during pipeline transportation are all purified, separated and vaporized, and then enter the incinerator for incineration. Since the incineration after vaporization has almost no impurities entering the incinerator, the combustion is easier, more complete and thorough, the residue after combustion is very little, the incinerator is not easy to be blocked, is more durable, and the service life of the incinerator is prolonged. In addition, the vaporization pipe of the processor is vertically arranged, so that the inner wall is not easy to be scaled, thereby prolonging the maintenance and cleaning interval of the processor and increasing the service life of the processor. BRIEF DESCRIPTION OF DRAWINGS

[0017] Figure 1 is a structural schematic view of the processor;

[0018] Figure 2 is Figure 1 is a sectional view of the A-A part in

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

[0020] Figure 4 is a structural schematic view of the gas-liquid dust separation filter;

[0021] In the drawings:

[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 tank bodies welded by steel plates, and the vaporization pipe 12 is a cylinder, on which a first heating device is arranged, and the first heating device is a heating wire 13 wound on the vaporization pipe 12. A second cleaning pipe 15 is welded on the right side of the secondary separation tank 1, and a first cleaning pipe 3 is welded on the left side of the liquid inlet tank 4, and the outer ends of the second cleaning pipe 15 and the first cleaning pipe 3 are covered with blocking covers. By opening the corresponding blocking cover, the dirt or sediment inside the secondary separation tank 1 or the liquid inlet tank 4 can be cleaned.

[0026] Two vertical baffle plates 10 are arranged at intervals in the right part of the vapor-liquid separation tank 9, and adjacent baffle plates 10 are staggered in the horizontal direction, and the two baffle plates 10 divide the cavity inside the vapor-liquid separation tank 9 into a left vapor collecting chamber 56 and a right liquid collecting chamber 58. The bottom of the vapor-liquid separation tank 9 is fixedly communicated with a vertical liquid guide pipe 11 near the right end, the upper end of the liquid guide pipe 11 is communicated with the liquid collecting chamber 58, and the upper end of the liquid guide pipe 11 is 3-5 cm higher than the bottom surface of the liquid collecting chamber 58. The lower end of the liquid guide pipe 11 is fixedly communicated with the top of the secondary separation tank 1.

[0027] A vertical steam discharge pipe 8 is fixedly communicated with the top of the vapor-liquid separation tank 9 near the left end, the upper end of the vaporization pipe 12 is communicated with the bottom of the vapor collecting chamber 56, and the lower end is communicated with the top of the liquid inlet tank 4. The vapor collecting chamber 56 and the liquid collecting chamber 58 are communicated through the serpentine flow channel 57 formed by the two baffle plates 10, the upper end of the liquid guide pipe 11 is communicated with the position of the liquid collecting chamber 58 away from the outlet of the flow channel 57, the liquid inlet tank 4 is fixedly communicated with a processor inlet pipe 7 at the left top, and the secondary separation tank 1 is welded with a processor oil discharge pipe 2 communicated with the inside thereof at the left top.

[0028] The liquid inlet tank 4 is fixedly communicated with a water inlet pipe 18 at the right bottom, and the vapor-liquid separation tank 9 is fixedly communicated with a water discharge pipe 17 at the left position near the top, and a water pump 53 is connected between the water discharge pipe 17 and the water inlet pipe 18, and the flow direction of the liquid in the water pump 53 is from the water discharge pipe 17 to the water inlet pipe 18. The secondary separation tank 1 is also provided with a water level sensor 16 at the right bottom, which is used to detect the water level in the secondary separation tank 1 (using the principle that water conducts electricity and oil does not conduct electricity, so only the water level is detected), when the water level in the secondary separation tank 1 reaches a set value (such as 10 cm), the water pump 53 is started, and the water in the secondary separation tank 1 is discharged into the vapor-liquid separation tank 9, so that the water is vaporized again.

[0029] The working process of the present application is as follows:

[0030] The waste liquid formed by the waste water and waste oil separated from the organic heat dirty exhaust gas produced in the production of reclaimed rubber enters into the liquid inlet tank 4 through the processor inlet pipe 7. The heating wire 13 outside the vaporization pipe 12 is electrified to heat the vaporization pipe 12. The heating temperature is about 120℃. The water in the waste liquid is boiled and vaporized. The vaporized water is discharged from the exhaust pipe 8 and enters into the incinerator 40 to be incinerated. The oil in the waste liquid is less dense than water and immiscible with water, and thus forms a layer on the water surface. The oil is stably layered through the flow channel 57 and then enters into the liquid collecting chamber 58. Since the upper end of the liquid guide pipe 11 is slightly higher than the bottom surface of the liquid collecting chamber 58, when the oil liquid surface in the liquid collecting chamber 58 is higher than the top end of the liquid guide pipe 11, the oil flows downward from the liquid guide pipe 11 into the secondary separation tank 1.

[0031] When the vaporization pipe 12 heats the waste liquid, part of the waste liquid is in the form of glue and some impurities in the waste liquid are deposited at the bottom of the liquid inlet tank 4 under the action of gravity and coagulate into blocks. The blocking cap on the first cleaning pipe 3 is opened regularly to clean the coagulated blocks through the first cleaning pipe 3. Since the vaporization pipe 12 is vertical, the glue blocks do not coagulate and deposit on the vaporization pipe 12 when falling under the action of the bubble thrust and gravity, thereby ensuring the smoothness of the vaporization pipe 12. The vertical design of the vaporization pipe 12 has the characteristics of not being easy to coagulate and deposit, reducing the maintenance workload of the processor 51 and prolonging the service life of the processor 51.

[0032] The oil in the secondary separation tank 1 is discharged through the processor oil discharge pipe 2, vaporized and then enters into the incinerator 40 to be incinerated.

[0033] Since the waste oil entering into the secondary separation tank 1 through the liquid guide pipe 11 may contain a small amount of water, the water is collected at the bottom of the secondary separation tank 1 due to the immiscibility of oil and water. When the water reaches a set value, it is discharged into the vapor-liquid separation tank 9 through the water pump 53, vaporized again through the vaporization pipe 12 after flowing into the vaporization pipe 12, thereby preventing excessive deposition of water in the secondary separation tank 1 and making the oil discharged from the processor oil discharge pipe 2 purer.

[0034] Example 2

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

[0036] The processor 51 further comprises a heat preservation tank 6. The liquid inlet tank 4, the vapor-liquid separation tank 9, the vaporization pipe 12 and the liquid guide pipe 11 are arranged in the heat preservation tank 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 extend out of the heat preservation tank 6. The heat preservation tank 6 is fixedly connected with the waste heat inlet short pipe 5 and the waste heat outlet short pipe 14 on the two sides.

[0037] The incinerator exhaust pipe 38 of the incinerator 40 is communicated with the waste heat inlet short pipe 5, so that the hot exhaust gas generated during the operation of the incinerator 40 is introduced into the heat preservation box 6, and then discharged from the waste heat outlet short pipe 14, thereby heating the liquid inlet box 4 and the vapor-liquid separation box 9 by using the waste heat of the incinerator 40, saving the electric energy consumed by the heating wire 13, and achieving the effect of energy saving.

[0038] Embodiment 3

[0039] In combination Figure 4 As shown in the figure, the embodiment discloses a treatment system capable of treating wastewater and waste oil in organic waste gas, adopts the processor 51 in embodiment 2, and further comprises a gas-liquid dust separation filter 55 and an oil evaporator 42.

[0040] The gas-liquid dust separation filter 55 comprises a closed cylindrical barrel 21, a filter exhaust pipe 24 fixedly communicated with the upper left side of the barrel 21, a filter oil and water discharge pipe 20 fixedly communicated with the lower left side of the barrel 21, and a filter inlet pipe 28 fixedly communicated with the right middle part of the barrel 21 in the tangential direction. A plug cover 25 is fixedly connected to the top of the barrel 21 by bolts, which is used for plugging the top of the barrel 21 and is also conducive to the maintenance and replacement of the filter components in the barrel 21. A circular plug plate is welded to the bottom of the barrel 21, and a third cleaning pipe 19 communicated with the inside of the barrel 21 is welded to the center of the plug plate. The lower end of the third cleaning pipe 19 is also connected to the plug plate by bolts.

[0041] A filter cylinder 33 is arranged in the middle of the barrel 21, and a separation cylinder 22 is sleeved between the filter cylinder 33 and the barrel 21. A partition ring 59 is fixedly connected to the inside of the barrel 21 between the filter exhaust pipe 24 and the filter inlet pipe 28. The top of the filter cylinder 33 and the top of the separation cylinder 22 are fixedly connected to the partition ring 59.

[0042] The partition ring 59 comprises an outer ring 23, an intermediate ring 27 and an inner ring 26 fixedly connected in sequence in the axial direction of the barrel 21. The inner ring 26 is welded to the top of the filter cylinder 33, the top of the separation cylinder 22 is welded to the intermediate ring 27, and the outer ring 23 is welded to the barrel 21. The outer ring 23, the intermediate ring 27 and the inner ring 26 are located between the filter exhaust pipe 24 and the filter inlet pipe 28, and divide the space inside the barrel 21 into two parts.

[0043] The filter cylinder 33 comprises ten vertical rib plates 29 uniformly distributed along the circumferential direction of the inner hole of the inner ring 26, a steel wire 30 wound around the rib plates 29, and a filter screen 31 wrapped outside the steel wire 30. The rib plates 29 are semicircular grooves at the positions in contact with the steel wire 30, so as to prevent the steel wire 30 from slipping on the rib plates 29. A cylinder is welded inside the inner ring 26, and the upper ends of the rib plates 29 are welded to the inner wall of the cylinder. The lower ends of the rib plates 29 are welded to a circular bottom plate 32 plugged at the bottom of the filter screen 31.

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

[0045] The oil evaporator 42 comprises a cylindrical closed shell, and a T-shaped tee pipe is arranged at the top of the shell, the bottom pipe opening of the tee pipe is fixedly communicated with the top of the shell through a flange, the left pipe opening of the tee pipe is the oil evaporator outlet pipe 45, and the right pipe opening of the tee pipe is the oil evaporator inlet pipe 46. A second heating device is arranged outside the shell, and the second heating device is also the heating wire 13, which is wound outside the shell and used for heating the shell to vaporize the oil inside the shell. The oil evaporator inlet pipe 46 and the filter exhaust pipe 24 are fixedly communicated through the fourth connecting pipe 48, the steam exhaust pipe 8 is fixedly communicated with the fourth connecting pipe 48 through the fifth connecting pipe 49, and the oil evaporator outlet pipe 45 is fixedly communicated with the incinerator inlet pipe 43 through the third connecting pipe 44. The shell is fixedly communicated with the oil evaporator oil inlet pipe 47 close to the top, the oil evaporator oil inlet pipe 47 is fixedly communicated with the processor oil discharge pipe 2 through the second connecting pipe 41, and the second connecting pipe 41 is provided with an oil pump 54.

[0046] In Figure 3 , the arrow with a dashed line represents the flow direction of the gas, and the arrow with a solid line represents the flow direction of the liquid.

[0047] The hot dirty organic waste gas (containing waste water, waste oil and dust) generated in the production of reclaimed rubber enters the cylinder 21 from the filter inlet pipe 28 from right to left along the tangential direction, and rotates in the gap between the cylinder 21 and the isolation cylinder 22. The liquid and impurities (including dust and rubber particles) in the organic waste gas are thrown to the inner wall of the cylinder 21 under the action of centrifugal force, then slide down along the inner wall of the cylinder 21, and fall to the bottom of the cylinder 21. The dust is deposited at the bottom of the cylinder 21, and these deposits can be cleaned by periodically opening the blocking plate at the bottom of the third cleaning pipe 19. The waste water and waste oil enter the liquid inlet tank 4 through the sixth connecting pipe 50.

[0048] Since the filter screen 31 is provided with the isolation cylinder 22, the organic waste gas is prevented from directly blowing to the filter screen 31, thereby prolonging the cleaning and replacement time of the filter screen 31.

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

[0050] Under the action of the oil pump 54, the oil in the secondary separation tank 1 enters into the shell through the processor oil discharge pipe 2, the second connecting pipe 41 and the oil evaporator inlet pipe 47 in turn, and the shell is heated by the heating wire 13 outside the shell (the heating temperature is about 200 to 240℃, since the temperature in the production process of the reclaimed rubber does not exceed 400 degrees, so the gasification temperature of the separated oil also does not exceed 400 degrees), so that the oil in the shell is gasified, and then enters into the incinerator 40 through the oil evaporator outlet pipe 45, the third connecting pipe 44 and the incinerator inlet pipe 43 in turn for incineration treatment. The glue-like substances produced after the oil in the shell is heated and some other impurities will deposit at the bottom of the shell, and these glue-like substances and impurities can be cleaned by opening the lid at the bottom of the shell regularly.

[0051] After being treated by the gas-liquid dust separation filter 55, the waste dust, glue particles and impurities in the organic waste gas are filtered out, and the waste water and waste oil in the organic waste gas are treated by the processor 51 and the oil evaporator 42, so that the waste water and waste oil in the organic waste gas can be treated. At the same time, since the water and oil are in the form of gas entering into the incinerator 40, the impurities are almost none, so that the combustion is easier, more complete and thorough, the residue after combustion is very little, the heat exchange pipe inside the incinerator 40 is not easy to be blocked, and is more durable, which prolongs the maintenance and cleaning interval time of the incinerator 40 and the service life. At the same time, the heating elements (such as heating flat belts) in the electric auxiliary heating incinerator 40 are not easy to attach inorganic substances, which does not affect the heating of these heating elements, and prolongs the service life of the heating elements.

[0052] The outlet of the waste heat inlet short pipe 5 is connected with the induced draft fan 37, the air outlet of the induced draft fan 37 is communicated with the incinerator exhaust pipe 38 of the incinerator 40 through the first connecting pipe 36, and the waste heat outlet short pipe 14 is fixedly communicated with the exhaust main pipe 52. The exhaust main pipe 52 and the first connecting pipe 36 are fixedly communicated with the bypass pipe 34, the first valve 35 is arranged on the bypass pipe 34, and the second valve 39 is arranged on the first connecting pipe 36 between the bypass pipe 34 and the waste heat inlet short pipe 5.

[0053] When the second valve 39 is opened and the first valve 35 is closed, the waste heat of the incinerator 40 can be used to heat the processor 51, so as to achieve the purpose of energy saving. When the temperature of the incinerator 40 exceeds the set temperature (for example, 750-760°C), the first valve 35 is opened and the second valve 39 is closed, so as to prevent the processor 51 and the incinerator 40 from being damaged due to excessive temperature. (Because the temperature of the incinerator 40 exceeds the set temperature, the exhaust temperature of the incinerator 40 rises, which causes the temperature of the processor 51 to rise, and the oil gas contained in the exhaust gas of the processor 51 also increases, that is, the calorific value of the exhaust gas of the processor 51 is high. The combustion in the incinerator 40 generates a large amount of heat, which further increases the temperature of the incinerator 40, and further increases the temperature of the processor 51, thereby causing a vicious cycle, and finally causing the incinerator 40 to be damaged due to over-temperature or causing the processor 51 to be damaged due to over-temperature.

[0054] The above embodiments are described in detail and specifically, express the preferred embodiments of the present application, and are only used to illustrate the technical ideas and characteristics of the present application, and the purpose is to enable those skilled in the art to understand the content of the present application and to implement it, but not only limited to the present application, and cannot be limited to the patent range of the present application only by the above embodiments, that is, any equivalent changes or modifications made according to the spirit disclosed by the present application, and within the structure of the present application, the internal partial improvement of the system and the change between the subsystems, etc., are still within the patent range of the present application.

Claims

1. A processor which can treat waste water, waste oil in organic exhaust gas, characterized by, The device comprises a liquid inlet tank (4), a vapor-liquid separation tank (9) arranged above the liquid inlet tank (4), and a vaporization pipe (12) fixedly communicated with the vapor-liquid separation tank (9) and the liquid inlet tank (4) respectively; the vaporization pipe (12) is provided with a first heating device; the liquid inlet tank (4) is fixedly communicated with a processor inlet pipe (7); the vapor-liquid separation tank (9) is fixedly communicated with a steam discharge pipe (8) at the top and a liquid guide pipe (11) at the bottom.

2. The processor according to claim 1, wherein the processor is capable of treating waste water and waste oil in the organic exhaust gas. The device further comprises a secondary separation tank (1) connected to the bottom of the liquid inlet tank (4); the secondary separation tank (1) is fixedly communicated with the liquid guide pipe (11); the secondary separation tank (1) is fixedly communicated with a processor oil discharge pipe (2) at the middle; the vapor-liquid separation tank (9) is fixedly communicated with a water inlet pipe (18); the secondary separation tank (1) is fixedly communicated with a water discharge pipe (17) at the bottom; a water pump (53) is connected between the water discharge pipe (17) and the water inlet pipe (18); the flow direction of the liquid in the water pump (53) is from the water discharge pipe (17) to the water inlet pipe (18).

3. The processor according to claim 1, wherein the processor is capable of treating waste water and waste oil in the organic exhaust gas. The vapor-liquid separation tank (9) is provided with at least two vertical baffles (10) arranged at intervals; adjacent baffles (10) are arranged in a staggered manner in the horizontal direction; the baffles (10) divide the vapor-liquid separation tank (9) into a vapor collection chamber (56) and a liquid collection chamber (58); the vaporization pipe (12) is communicated with the vapor collection chamber (56); the liquid guide pipe (11) is communicated with the vapor collection chamber (56); the vapor collection chamber (56) and the liquid collection chamber (58) are communicated through a serpentine flow channel (57) formed by the baffles (10).

4. The processor according to claim 2, wherein the processor is characterized by comprising: The device further comprises an insulation tank (6); the liquid inlet tank (4), the vapor-liquid separation tank (9), the vaporization pipe (12), and the liquid guide pipe (11) are arranged in the insulation tank (6); the processor inlet pipe (7) and the steam discharge pipe (8) extend out of the insulation tank (6); the insulation tank (6) is fixedly communicated with a waste heat inlet short pipe (5) and a waste heat outlet short pipe (14) respectively at two sides.

5. A treatment system capable of treating waste water, waste oil in organic exhaust gas, characterized by, The device comprises the processor for treating waste water and waste oil in the organic waste gas according to claim 4, further comprising a gas-liquid-dust separation filter (55) and an oil evaporator (42); the gas-liquid-dust separation filter (55) comprises a closed cylinder (21) and a filter inlet pipe (28), a filter exhaust pipe (24), and a filter oil and water discharge pipe (20) fixedly communicated with the cylinder (21) respectively; the filter exhaust pipe (24) and the steam discharge pipe (8) are communicated with a incinerator inlet pipe (43) of an incinerator (40); the oil evaporator (42) is connected between the incinerator inlet pipe (43) and the processor oil discharge pipe (2); the filter oil and water discharge pipe (20) and the processor inlet pipe (7) are communicated.

6. The treatment system according to claim 5, wherein the treatment system is characterized by The filter exhaust pipe (24) is arranged at the upper part of the cylinder (21), the filter inlet pipe (28) is arranged at the middle part of the cylinder (21) along the tangential direction of the cylinder (21), the filter oil and water exhaust pipe (20) is arranged at the bottom of the cylinder (21), the gas-liquid-dust separation filter (55) further comprises a filter cylinder (33) located at the middle part of the cylinder (21) and a separation cylinder (22) sleeved between the filter cylinder (33) and the cylinder (21), the inside of the cylinder (21) is fixedly connected with a separation ring (59) between the filter exhaust pipe (24) and the filter inlet pipe (28), and the top of the filter cylinder (33) and the separation cylinder (22) are fixedly connected with the separation ring (59).

7. The treatment system according to claim 6, wherein the treatment system is capable of treating wastewater and waste oil in the organic exhaust gas. The separation ring (59) comprises an outer ring (23), an intermediate ring (27) and an inner ring (26) fixedly connected along the axial direction of the cylinder (21) in sequence, the inner ring (26) is fixedly connected with the top of the filter cylinder (33), the top of the separation cylinder (22) is fixedly connected with the intermediate ring (27), and the outer ring (23) is fixedly connected with the cylinder (21).

8. The treatment system according to claim 6, wherein the treatment system is capable of treating wastewater and waste oil in the organic exhaust gas. The filter cylinder (33) comprises a plurality of vertical rib plates (29) uniformly distributed along the circumferential direction of the inner hole of the separation ring (59), a steel wire (30) wound outside the rib plate (29) and a filter screen (31) coated outside the steel wire (30), the upper end of the rib plate (29) is fixedly connected with the separation ring (59), and the lower end of the rib plate (29) is fixedly connected with a bottom plate (32) blocked at the bottom of the filter screen (31); the bottom of the cylinder (21) is fixedly connected with a third cleaning pipe (19), and the bottom of the third cleaning pipe (19) is detachably connected with a blocking plate.

9. The treatment system for organic exhaust gas, waste water, and waste oil according to claim 5, characterized by, The waste heat gas inlet stub (5) is communicated with the incinerator exhaust pipe (38) of the incinerator (40) through the first connecting pipe (36), the waste heat gas outlet stub (14) is fixedly communicated with an exhaust main pipe (52), the exhaust main pipe (52) and the first connecting pipe (36) are fixedly communicated with a bypass pipe (34), the first valve (35) is arranged on the bypass pipe (34), and the second valve (39) is arranged on the first connecting pipe (36) between the bypass pipe (34) and the waste heat gas inlet stub (5).

10. The treatment system for organic exhaust gas, waste water, and waste oil according to claim 5, characterized by, The oil evaporator (42) comprises a shell, the top of the shell is blocked, the top of the shell is provided with a tee pipe, one of the pipe openings of the tee pipe is fixedly communicated with the top of the shell through a flange, the other pipe opening of the tee pipe is an oil evaporator outlet pipe (45), the third pipe opening of the tee pipe is an oil evaporator inlet pipe (46), the shell is externally provided with a second heating device, the oil evaporator outlet pipe (45) is communicated with the incinerator inlet pipe (43), the shell is fixedly communicated with an oil evaporator oil inlet pipe (47) close to the top, and the oil evaporator oil inlet pipe (47) is communicated with the processor oil discharge pipe (2).

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