CN220132135U - Tire schizolysis oil refining equipment - Google Patents
Tire schizolysis oil refining equipment Download PDFInfo
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- CN220132135U CN220132135U CN202321490525.9U CN202321490525U CN220132135U CN 220132135 U CN220132135 U CN 220132135U CN 202321490525 U CN202321490525 U CN 202321490525U CN 220132135 U CN220132135 U CN 220132135U
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- gas
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- 238000007670 refining Methods 0.000 title claims abstract description 11
- 239000003921 oil Substances 0.000 claims abstract description 104
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 34
- 239000010779 crude oil Substances 0.000 claims abstract description 33
- 238000004227 thermal cracking Methods 0.000 claims abstract description 32
- 238000005336 cracking Methods 0.000 claims abstract description 25
- 239000000428 dust Substances 0.000 claims description 10
- 230000001877 deodorizing effect Effects 0.000 claims description 7
- 230000000694 effects Effects 0.000 abstract description 5
- 238000000926 separation method Methods 0.000 abstract description 3
- 238000007789 sealing Methods 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 64
- 238000000034 method Methods 0.000 description 23
- 230000008569 process Effects 0.000 description 21
- 238000000197 pyrolysis Methods 0.000 description 20
- 238000009833 condensation Methods 0.000 description 11
- 230000005494 condensation Effects 0.000 description 11
- 229910000831 Steel Inorganic materials 0.000 description 8
- 239000006229 carbon black Substances 0.000 description 8
- 239000010959 steel Substances 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 6
- 230000009471 action Effects 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 150000002894 organic compounds Chemical class 0.000 description 3
- 239000000779 smoke Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 239000000295 fuel oil Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 229920002521 macromolecule Polymers 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 238000004806 packaging method and process Methods 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000010920 waste tyre Substances 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 244000043261 Hevea brasiliensis Species 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 230000003712 anti-aging effect Effects 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 239000012752 auxiliary agent Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000003776 cleavage reaction Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000009089 cytolysis Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 210000001503 joint Anatomy 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229920003052 natural elastomer Polymers 0.000 description 1
- 229920001194 natural rubber Polymers 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000002296 pyrolytic carbon Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000005060 rubber Substances 0.000 description 1
- 238000010079 rubber tapping Methods 0.000 description 1
- 230000007017 scission Effects 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 229920003051 synthetic elastomer Polymers 0.000 description 1
- 239000005061 synthetic rubber Substances 0.000 description 1
- 239000011269 tar Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- 238000005491 wire drawing Methods 0.000 description 1
- 239000011787 zinc oxide Substances 0.000 description 1
Landscapes
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
Abstract
The utility model relates to the technical field of tire oil refining, and provides tire cracking oil refining equipment, which comprises a thermal cracking furnace and a buffer tank, wherein one end of the thermal cracking furnace is communicated with the buffer tank, the buffer tank is connected with a first oil gas pipe, and the first oil gas pipe is respectively connected with a first condenser and a water sealing device; the lower end of the first condenser is connected with an oil-gas separator, the oil-gas separator is communicated with a first crude oil tank, the water seal device is connected with a first oil conveying pipe, the tail end of the first oil conveying pipe is connected with a second crude oil tank, the water seal device is connected with a second oil pipe, the tail end of the second oil pipe is connected with a second condensing pipe, the bottom of the second condenser is connected with a second oil conveying pipe, and the other end of the second oil conveying pipe is connected with a third crude oil tank; the third crude oil tank is connected with a third oil pipe, the tail end of the third oil pipe is connected with a third condenser, the bottom of the third condenser is connected with a third oil pipe, and the third oil pipe is connected back to the third crude oil tank. The utility model can make the oil-gas separation more thorough and the oil-obtaining effect better.
Description
Technical Field
The utility model relates to the technical field of tire oil refining, in particular to tire cracking oil refining equipment.
Background
The tyre is mainly composed of rubber (including natural rubber and synthetic rubber), carbon black and various organic and inorganic auxiliary agents (including plasticizer, anti-aging agent, sulfur, zinc oxide and the like). Most organic compounds have thermal instability, if they are placed under anoxic and high temperature conditions, under the combined action of decomposition and condensation, macromolecular organic compounds are decomposed and converted into gaseous, liquid and solid components with relatively small molecular mass, and the chemical conversion process of the organic compounds under the conditions is called pyrolysis. And the gases (including oil gas and noncondensable gases) generated by thermal cracking need to be condensed and recovered. Traditional condensation collection mode adopts the coil pipe to condense, passes the coil pipe through oil gas and cools off, and the oil gas condensation of adopting this kind of mode is incomplete, can't retrieve in grades, and the oil obtaining effect after the thermal cracking is accomplished is general.
Disclosure of Invention
The utility model aims to provide a tire cracking oil refining device which can be used for condensing oil gas more fully and obtaining better oil grading effect.
The embodiment of the utility model is realized by the following technical scheme: the tire cracking oil refining equipment comprises a thermal cracking furnace and a buffer tank, wherein one end of the thermal cracking furnace is communicated with the buffer tank, the buffer tank is connected with a first oil gas pipe, and the first oil gas pipe is respectively connected with a first condenser and a water sealing device; the lower end of the first condenser is connected with an oil-gas separator, the lower end of the oil-gas separator is communicated with a first crude oil tank, the bottom end of the water seal device is connected with a first oil conveying pipe, the tail end of the first oil conveying pipe is connected with a second crude oil tank, the upper end of the water seal device is connected with a second oil pipe, the tail end of the second oil pipe is connected with a second condensing pipe, the bottom of the second condenser is connected with a second oil conveying pipe, and the other end of the second oil conveying pipe is connected with a third crude oil tank; the top of the third crude oil tank is connected with a third oil pipe, the tail end of the third oil pipe is connected with a third condenser, the bottom of the third condenser is connected with a third oil pipe, and the third oil pipe is connected back to the third crude oil tank.
Preferably, the condenser further comprises a condensate pipe, circulating water flows in the condensate pipe, and the condensate pipe is respectively connected to the first condenser, the second condenser and the third condenser.
Preferably, the first condenser is a vertical condenser, and the first condenser is provided with two groups which are arranged side by side.
Preferably, the second condenser adopts a horizontal condenser, and the second condenser is provided with two groups of overlapping arrangement.
Preferably, the oil pump is arranged on the main pipe, and the main pipe is respectively communicated with the first oil tank, the second oil tank and the third oil tank.
Preferably, the thermal cracking furnace further comprises a vacuum device, wherein the vacuum device is connected with a vacuum tube, and one end of the vacuum tube is connected to the pipeline of the thermal cracking furnace and the buffer tank.
Preferably, the top of the thermal cracking furnace is connected with a water film dust remover, one end of the water film dust remover is connected with a fan through a pipeline, and the fan is communicated with an exhaust pipe.
Preferably, the thermal cracking furnace is connected with a first tail gas pipe, and one end of the first tail gas pipe is connected with a deodorizing device; the top of the third condenser is connected with a second tail gas pipe communicated with the deodorizing device.
The technical scheme of the embodiment of the utility model has at least the following advantages and beneficial effects: compared with the prior art, the utility model has the advantages that the waste tires are placed in the thermal cracking furnace for heating, the generated oil gas firstly enters the buffer tank, the oil gas in the buffer tank is filled up and then is separated from the smoke gas along the first oil gas pipe by the first condenser, the residual oil gas firstly passes through the water seal, the second condenser and the third condenser, and is condensed and collected according to the heavy oil and the light oil in a fractional manner, so that the oil gas is more thoroughly condensed, and the graded oil collecting effect is better.
Drawings
In order to more clearly illustrate the technical solutions of the embodiments of the present utility model, the drawings that are needed in the embodiments will be briefly described below, it being understood that the following drawings only illustrate some embodiments of the present utility model and therefore should not be considered as limiting the scope, and other related drawings may be obtained according to these drawings without inventive effort for a person skilled in the art.
Fig. 1 is a schematic diagram of the overall structure of a tire-cracking oil refining apparatus according to an embodiment of the present utility model;
FIG. 2 is a left half detail of the schematic of FIG. 1;
fig. 3 is a right half detail of the schematic of fig. 1.
Icon: the device comprises a 1-thermal cracking furnace, a 2-buffer tank, a 3-first oil pipe, a 4-first condenser, a 5-oil-gas separator, a 6-first oil tank, a 7-first oil pipe, a 8-second oil tank, a 9-second oil pipe, a 10-second condenser, a 11-second oil pipe, a 12-third oil tank, a 13-third oil pipe, a 14-third oil pipe, a 15-third condenser, a 16-condensed water pipe, a 17-main pipe, a 18-oil pump, a 19-vacuum device, a 20-vacuum pipe, a 21-water film dust remover, a 22-fan, a 23-exhaust pipe, a 24-first tail gas pipe, a 25-second tail gas pipe, a 26-water seal device and a 27-deodorizing device.
Detailed Description
For the purpose of making the objects, technical solutions and advantages of the embodiments of the present utility model more apparent, the technical solutions of the embodiments of the present utility model will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present utility model, and it is apparent that the described embodiments are some embodiments of the present utility model, but not all embodiments of the present utility model. The components of the embodiments of the present utility model generally described and illustrated in the figures herein may be arranged and designed in a wide variety of different configurations.
Thus, the following detailed description of the embodiments of the utility model, as presented in the figures, is not intended to limit the scope of the utility model, as claimed, but is merely representative of selected embodiments of the utility model. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
It should be noted that: like reference numerals and letters denote like items in the following figures, and thus once an item is defined in one figure, no further definition or explanation thereof is necessary in the following figures.
Examples
The following is further described with reference to specific embodiments, and referring to fig. 1-3, the present embodiment is a tire cracking oil refining apparatus, which includes a thermal cracking furnace 1 and a buffer tank 2, wherein one end of the thermal cracking furnace 1 is communicated with the buffer tank 2, the buffer tank 2 is connected with a first oil gas pipe 3, and the first oil gas pipe 3 is respectively connected with a first condenser 4 and a water seal device 26; the lower end of the first condenser 4 is connected with an oil-gas separator 5, the lower end of the oil-gas separator 5 is communicated with a first crude oil tank 6, the bottom end of a water seal device 26 is connected with a first oil conveying pipe 7, the tail end of the first oil conveying pipe 7 is connected with a second crude oil tank 8, the upper end of the water seal device 26 is connected with a second oil pipe 9, the tail end of the second oil pipe 9 is connected with a second condensing pipe, the bottom of the second condenser 10 is connected with a second oil conveying pipe 11, and the other end of the second oil conveying pipe 11 is connected with a third crude oil tank 12; the top of the third crude oil tank 12 is connected with a third oil pipe 13, the tail end of the third oil pipe 13 is connected with a third condenser 15, the bottom of the third condenser 15 is connected with a third oil pipe 14, and the third oil pipe 14 is connected back to the third crude oil tank 12; specifically, the tire pyrolysis process used in the present utility model can be represented by the following formula: organic solid waste- & gt gas (H2, CH4, CO 2) +organic liquid (organic acid, aromatic hydrocarbon, tar, kerosene, alcohol, aldehydes, etc) +solid (carbon black, slag), wherein the essence of pyrolysis is to heat organic macromolecules to crack the organic macromolecules into small molecules for precipitation. In the process, the reactions carried out in different temperature ranges are different, the product compositions are different, the organic matters are different, and the starting temperatures of the whole pyrolysis process are different. The tire is heated in the thermal cracking furnace 1 and then generates oil gas which gradually enters the buffer tank 2, is firstly discharged along the first oil gas pipe 3, is condensed and enters the first crude oil tank 6 for storage under the action of the first condensation pipe and the oil-gas separator 5, and the rest oil gas is partially input into the second crude oil tank 8 for storage after passing through the water seal device 26, the water seal device 26 carries out desulfurization purification on combustible gas, the oil gas passing through the water seal device 26 enters the second condenser 10 for condensation again along the second oil gas pipe 9, the liquefied oil enters the third crude oil tank 12 for storage, and a small amount of non-condensable gas and oil gas flow back and forth in the third crude oil tank 12 and the third condenser 15 for repeated condensation for multiple times so as to achieve the purpose of thorough oil-gas separation.
The embodiment also comprises a condensation water pipe 16, circulating water flows in the condensation water pipe 16, and the condensation water pipe 16 is respectively connected to the first condenser 4, the second condenser 10 and the third condenser 15; specifically, ma Caiyun circulating cold water acts on and cools each condenser, so that the oil gas condensation effect can be improved, and the condensation time can be shortened.
As shown in fig. 2, the first condenser 4 in the present embodiment adopts a vertical condenser, and the first condenser 4 is provided with two sets of parallel arrangement, the second condenser 10 adopts a horizontal condenser, and the second condenser 10 is provided with two sets of overlapping arrangement; specifically, the first condenser 4 and the second condenser 10 are different in setting modes and different in condensing time according to different condensed oil gas components and contents.
The embodiment also comprises a main pipe 17, an oil pump 18 is arranged on the main pipe 17, and the main pipe 17 is respectively communicated with the first crude oil tank 6, the second crude oil tank 8 and the third crude oil tank 12; specifically, the oil in the three crude oil tanks can be pumped out through the oil pump 18 for secondary treatment.
The embodiment also comprises a vacuum device 19, wherein the vacuum device 19 is connected with a vacuum tube 20, and one end of the vacuum tube 20 is connected to the pipeline of the thermal cracking furnace 1 and the buffer tank 2; specifically, the oil gas has a relatively high mass, and the oil gas is pumped from the thermal cracking furnace 1 into the buffer tank 2 by the vacuum device 19 so that the oil gas can flow normally.
The top of the thermal cracking furnace 1 in the embodiment is connected with a water film dust remover 21, one end of the water film dust remover 21 is connected with a fan 22 through a pipeline, and the fan 22 is communicated with an exhaust pipe 23; specifically, the tires in the thermal cracking furnace 1 generate smoke dust and exhaust gas after being heated, the smoke dust is removed by the water film dust remover 21, and the residual exhaust gas is discharged out of the exhaust pipe 23 by the fan 22, so that the thermal cracking furnace is relatively environment-friendly.
In order to reduce the odor discharged from the noncondensable gases, the thermal cracking furnace 1 in the embodiment is connected with a first tail gas pipe 24, and one end of the first tail gas pipe 24 is connected with a deodorizing device 27; a second tail gas pipe 25 communicated with a deodorizing device 27 is connected to the top of the third condenser 15; specifically, the exhaust gas in the thermal cracking furnace 1 and the residual exhaust gas after being completely condensed by the third condenser 15 are treated by the deodorizing device 27, and then discharged for tail gas recovery.
The production process flow comprises the following steps: the pyrolysis temperature of the tire is 120-380 ℃, the pyrolysis furnace is operated by adopting the external heating, micro negative pressure and anoxic pyrolysis process, the furnace body is closed, the gas is ensured not to leak in the production process, the pyrolysis efficiency is improved, and meanwhile, the unsafe hidden trouble and secondary pollution caused by the gas leak in the production process are fundamentally eliminated. The main raw materials of the technology are outsourced clean junked tires, pretreatment procedures such as cleaning, crushing, steel wire drawing and the like are not needed, the junked tires directly enter the pyrolysis furnace automatically under the spiral action of the rotary pyrolysis furnace, and the feeding process is high in automation degree, safe, convenient, time-saving and labor-saving. Since the cracking process is a complex physicochemical reaction process, the cracking process is performed in multiple stages according to the chemical reaction process mentioned in the tire cracking principle. The specific cleavage process is as follows:
1. when the cracking temperature is between 0 and 150 ℃, an equipment exhaust valve is opened to slowly exhaust air in the thermal cracking furnace 1, an anaerobic condition of the cracking process is realized, and as the thermal cracking process is just started, the waste wheel needs to conduct heat absorption and heat transfer processes at the stage, so that the waste wheel needs to be slowly heated at the stage, generally at the rate of 2K/min, and when the temperature reaches about 120 ℃, the temperature in the furnace is found to be maintained for a period of time without obvious heating phenomenon, and at the moment, a great amount of waste tires begin to absorb heat, the thermal cracking reaction process gradually begins, and pyrolysis gas and oil begin to be generated. This stage is typically around 2 hours.
2. When the cracking temperature is between 150 and 380 ℃, closing an exhaust valve to start collecting oil, gas and other products generated by pyrolysis, and enabling high-temperature flue gas to enter two oil-water separators connected in series to realize separation of the flue gas and heavy oil; then the oil product is collected in the oil tank through a condenser; the generated combustible gas is connected to a combustion chamber for combustion, so that heat is provided for the pyrolysis process; in order to prevent too severe pyrolysis, the temperature of this stage still needs to be raised slowly, generally about 4 hours, and in order to prevent the combustible gas from burning too fast, which results in too high temperature raising rate, it is necessary to control the flow of the combustible gas, and store the excess combustible gas for the pyrolysis process of the next stage.
3. When the pyrolysis temperature range is 380 ℃ in the constant-temperature reaction process, the pyrolysis process at the stage is similar to the process at the second stage, the process flow is still carried out, the generation of combustible gas at the stage is gradually reduced, and when the heat value provided by the combustible gas is insufficient, the biomass fuel needs to be supplemented to maintain the heat of the pyrolysis process. This stage typically takes about 2 hours.
4. And the pyrolysis is completed in a cooling stage, heating is stopped in the process, the project adopts an air cooling mode, the heat of the outer wall of the furnace body is continuously taken away through the air draft of the fan 22, and the duration of the cooling section is about 8 hours. When the furnace body is cooled to 120 ℃, steam is introduced into the cracking furnace chamber to drive out residual cracking gas in the furnace and the residual cracking gas is introduced into the waste gas combustion chamber to burn out, and the duration of driving away the cracking gas is about 10min. At this time, the carbon black screw conveyor was started, and the pyrolytic carbon black was collected. After the carbon black is collected, an evacuation valve above the furnace body is opened, the normal pressure in the furnace is recovered, the tank body is opened, and the pyrolysis steel wire is automatically discharged under the spiral action on the furnace wall. This stage generally takes about 2-4 hours and then fills with new junked tires, followed by the above-described cracking process. Because the tire in this technical scheme is whole tire when feeding, does not have cutting broken workshop section, and the furnace body is constantly rotated in the schizolysis process, so steel wire kink together when the ejection of compact, the small amount of carbon black that is stained on the steel wire just can fall through the tapping, and the direct packing outward transport after the steel wire ejection of compact. Then the steel wire outlet is closed, the carbon black discharge outlet (the diameter is about 0.4 m) is opened, the steel wire outlet is in butt joint with a closed spiral slag extractor, carbon black (the particle size is about 80-100 meshes) is discharged and then directly enters into a packaging bag, and the packaging bag is packaged and leaves a factory after being weighed by a platform scale. The discharge time of the carbon black steel wire of each equipment is 2 hours respectively. The total time for the entire tire lysis procedure was 20 hours.
The above is only a preferred embodiment of the present utility model, and is not intended to limit the present utility model, but various modifications and variations can be made to the present utility model by those skilled in the art. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present utility model should be included in the protection scope of the present utility model.
Claims (8)
1. A tire cracking oil refining device, which is characterized in that: the thermal cracking furnace comprises a thermal cracking furnace (1) and a buffer tank (2), wherein one end of the thermal cracking furnace (1) is communicated with the buffer tank (2), the buffer tank (2) is connected with a first oil gas pipe (3), and the first oil gas pipe (3) is respectively connected with a first condenser (4) and a water seal device (26);
the oil-gas separator (5) is connected to the lower end of the first condenser (4), the first crude oil tank (6) is communicated to the lower end of the oil-gas separator (5), the first crude oil tank (7) is connected to the bottom end of the water seal device (26), the second crude oil tank (8) is connected to the tail end of the first crude oil tank (7), the second oil pipe (9) is connected to the upper end of the water seal device (26), the second condenser (10) is connected to the tail end of the second oil pipe (9), the second oil pipe (11) is connected to the bottom of the second condenser (10), and the third crude oil tank (12) is connected to the other end of the second oil pipe (11);
the top of the third crude oil tank (12) is connected with a third oil pipe (13), the tail end of the third oil pipe (13) is connected with a third condenser (15), the bottom of the third condenser (15) is connected with a third oil pipe (14), and the third oil pipe (14) is connected back to the third crude oil tank (12).
2. The tire-cracking refinery apparatus according to claim 1, wherein: the condenser also comprises a condensate pipe (16), circulating water flows in the condensate pipe (16), and the condensate pipe (16) is respectively connected into the first condenser (4), the second condenser (10) and the third condenser (15).
3. The tire-cracking refinery apparatus according to claim 1, wherein: the first condenser (4) adopts a vertical condenser, and the first condenser (4) is provided with two groups which are arranged side by side.
4. The tire-cracking refinery apparatus according to claim 1, wherein: the second condenser (10) adopts a horizontal condenser, and the second condenser (10) is provided with two groups of overlapping arrangement.
5. The tire-cracking refinery apparatus according to claim 1, wherein: the oil pump is characterized by further comprising a main pipe (17), wherein an oil pump (18) is arranged on the main pipe (17), and the main pipe (17) is respectively communicated with the first crude oil tank (6), the second crude oil tank (8) and the third crude oil tank (12).
6. The tire-cracking refinery apparatus according to claim 1, wherein: the thermal cracking furnace further comprises a vacuum device (19), wherein the vacuum device (19) is connected with a vacuum tube (20), and one end of the vacuum tube (20) is connected to the pipeline of the thermal cracking furnace (1) and the buffer tank (2).
7. The tire-cracking refinery apparatus according to claim 1, wherein: the top of the thermal cracking furnace (1) is connected with a water film dust remover (21), one end of the water film dust remover (21) is connected with a fan (22) through a pipeline, and the fan (22) is communicated with an exhaust pipe (23).
8. The tire-cracking refinery apparatus according to claim 1, wherein: the thermal cracking furnace (1) is connected with a first tail gas pipe (24), and one end of the first tail gas pipe (24) is connected with a deodorizing device (27);
the top of the third condenser (15) is connected with a second tail gas pipe (25) communicated with the deodorizing device (27).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321490525.9U CN220132135U (en) | 2023-06-12 | 2023-06-12 | Tire schizolysis oil refining equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321490525.9U CN220132135U (en) | 2023-06-12 | 2023-06-12 | Tire schizolysis oil refining equipment |
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| Publication Number | Publication Date |
|---|---|
| CN220132135U true CN220132135U (en) | 2023-12-05 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321490525.9U Active CN220132135U (en) | 2023-06-12 | 2023-06-12 | Tire schizolysis oil refining equipment |
Country Status (1)
| Country | Link |
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| CN (1) | CN220132135U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117586797A (en) * | 2023-12-21 | 2024-02-23 | 山东省科学院能源研究所 | Method for recycling antibiotic fungus residues |
-
2023
- 2023-06-12 CN CN202321490525.9U patent/CN220132135U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117586797A (en) * | 2023-12-21 | 2024-02-23 | 山东省科学院能源研究所 | Method for recycling antibiotic fungus residues |
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