CN209161961U - A kind of purification-recovery system for damaged tire cracking oil gas - Google Patents
A kind of purification-recovery system for damaged tire cracking oil gas Download PDFInfo
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- CN209161961U CN209161961U CN201821993420.4U CN201821993420U CN209161961U CN 209161961 U CN209161961 U CN 209161961U CN 201821993420 U CN201821993420 U CN 201821993420U CN 209161961 U CN209161961 U CN 209161961U
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Abstract
A kind of purification-recovery system for damaged tire cracking oil gas disclosed by the utility model, including cracking gas wash tower, it is followed successively by light oil washing section and heavy oil washing section up and down in cracking gas wash tower, the heavy oil washing section of cracking gas wash tower has been sequentially communicated heavy oil cycling element and heavy oil cooler by pipeline, the light oil washing section of cracking gas wash tower is communicated with light oil cycling element by pipeline, and the top for cracking gas wash tower has been sequentially communicated purified gas aftercooler and knockout drum by pipeline.A kind of purification-recovery system for damaged tire cracking oil gas of the utility model, by the way that cracking gas is sent directly into cracking gas wash tower lower part, cooling down is carried out to cracking gas using returning in tower after the oily phase circulating cooling of cracking gas condensation gained, while also having reached washing, purifying effect;Cooling mutually with cracking gas directly contact in tower using hydronic oil, compare with water-cooled indirect heat exchange, increase heat exchange efficiency.
Description
Technical field
The utility model belongs to chemical gases purification-recovery system technical field, and in particular to one kind is cracked for damaged tire
The purification-recovery system of oil gas.
Background technique
With the fast development of auto industry, a large amount of waste tire incredible amounts are cracked using heating and carry out resource reclaim
It is a kind of good mode.In recent years, people develop and use waste tire production gasoline, diesel oil and pyrolytic carbon black, are waste and old wheel
The utilization of tire provides a good direction.
In existing waste tire cracking recovery process, as shown in Figure 1, straight for the cracking gas wherein generated by cracking
Pick into condenser i.e. cracking gas forecooler 9 and cracking gas aftercooler 10, be classified and cooled down by recirculated water, successively obtain light oil,
Heavy oil and cracking gas.Cracking gas returns to combustion heating furnace and recycles heat supply, and light oil, heavy oil are collected as crude product into tank.But
Since the condensation collection process process of oil gas lacks purification device, collects oil product and contain more carbon black particle, and cause device
Heat-exchanger rig easily blocks in operational process;Most of during simultaneously is that steam-water heat exchanging condenses, and heat exchange efficiency is lower, required to change
Heat area is larger.
Utility model content
The purpose of this utility model is to provide a kind of purification-recovery systems for damaged tire cracking oil gas, in cracking gas
It can be purified while condensing recovery.
The technical scheme adopted by the utility model is a kind of purification-recovery system for damaged tire cracking oil gas, packet
Cracking gas wash tower is included, cracks in gas wash tower and is followed successively by light oil washing section and heavy oil washing section up and down, crack gas wash tower
Heavy oil washing section has been sequentially communicated heavy oil cycling element and heavy oil cooler by pipeline, cracks the light oil washing section of gas wash tower
Be communicated with light oil cycling element by pipeline, crack the top of gas wash tower by pipeline be sequentially communicated purified gas aftercooler and
Knockout drum.
The utility model is also characterized by
Heavy oil cycling element includes the heavy oil heavy oil circulating pump that is sequentially communicated of washing pars infrasegmentalis and again for cracking gas wash tower
Oily recirculation cooler, the other end of heavy oil recirculation cooler pass through the heavy oil washing section that pipeline is connected to cracking gas wash tower respectively
Top and heavy oil cooler.
Light oil cycling element includes cracking the light oil light oil circulating pump that is sequentially communicated of washing pars infrasegmentalis of gas wash tower and light
The other end of oily recirculation cooler, light oil recirculation cooler is connected on the light oil washing section of cracking gas wash tower by pipeline
Portion.
The beneficial effects of the utility model are: a kind of Recovery Purifying system for damaged tire cracking oil gas of the utility model
System is returned after condensing the oily phase circulating cooling of gained using cracking gas by the way that cracking gas is sent directly into cracking gas wash tower lower part
Gives cracking gas to carry out cooling down in tower, while also having reached washing, purifying effect, in the process in cracking gas carbon black,
The impurity such as dust are removed, and the accumulation of impurities such as carbon black are interrupted discharge after tower reactor is cooling;Using it is hydronic oil mutually with split
Vent one's spleen in tower directly contact cooling, compared to water-cooled indirect heat exchange, increase heat exchange efficiency.
Detailed description of the invention
Fig. 1 is the structural schematic diagram for cracking the purification-recovery system of oil gas for damaged tire in the prior art;
Fig. 2 is a kind of structural schematic diagram of the purification-recovery system for damaged tire cracking oil gas of the utility model.
In figure, 1. cracking gas wash towers, 2. heavy oil coolers, 3. purified gas aftercoolers, 4. knockout drums, 5. heavy oil are followed
Ring pump, 6. heavy oil recirculation coolers, 7. light oil circulating pumps, 8. light oil recirculation coolers, 9. cracking gas forecoolers, 10. cracking gases
Aftercooler.
Specific embodiment
With reference to the accompanying drawing and the utility model is described in detail in specific embodiment.
The utility model provides a kind of purification-recovery system for damaged tire cracking oil gas, as shown in Fig. 2, including splitting
Gas wash tower 1 is solved, cracks and is followed successively by light oil washing section and heavy oil washing section in gas wash tower 1 up and down, cracks the weight of gas wash tower 1
Oil wash section has been sequentially communicated heavy oil cycling element and heavy oil cooler 2 by pipeline, cracks the light oil washing section of gas wash tower 1
It is communicated with light oil cycling element by pipeline, the top of cracking gas wash tower 1 has been sequentially communicated purified gas aftercooler 3 by pipeline
With knockout drum 4.Wherein, heavy oil cycling element includes the weight for cracking the heavy oil washing pars infrasegmentalis of gas wash tower 1 and being sequentially communicated
Oil circulating pump 5 and heavy oil recirculation cooler 6, the other end of heavy oil recirculation cooler 6 pass through pipeline respectively and are connected to cracking air purge
Wash heavy oil washing section top and the heavy oil cooler 2 of tower 1.Light oil cycling element includes the light oil washing section for cracking gas wash tower 1
The other end of the light oil circulating pump 7 and light oil recirculation cooler 8 that lower part is sequentially communicated, light oil recirculation cooler 8 is connected by pipeline
Pass to the light oil washing section top of cracking gas wash tower 1.
When work, the cracking gas come from upper workshop section is sent into cracking 1 lower part of gas wash tower, cracking gas into after tower by efficient
Inertia demister removes the impurity in cracking gas, and the solid slag after removing flow to tower reactor with the cracked oil that top elutes
Bottom collection slot, after cooling interruption discharge.
Crack in 1 tower of gas wash tower and washed using light oil, heavy oil two stage formula, tower reactor lower section is attached most importance to oil wash section, spray and
Under low temperature heavy oil cracking gas is washed, be mingled with the heavy cracked oil of carbon black and assemble in tower reactor.The heavy oil of tower reactor passes through heavy oil
Circulating pump 5, which is sent to heavy oil recirculation cooler 6, is cooled to 110 DEG C or so.A part is sent to the anti-stifled grid circulating cooling washing of tower lower section,
Another part is cooled to 70 DEG C or so by heavy oil cooler 2 and is used as heavy oil product carrying device.
Light oil is adopted on the upside of washing midsection oil sump tank, light oil send cold to light oil recirculation cooler 8 by light oil circulating pump 7
To 40 DEG C or so, a part is sent to the anti-stifled grid circulating cooling washing of tower upper section after cooling, another part is as light oil products
Carrying device.
Cracking gas in tower after heavy oil, the washing of light oil two-part, by the efficient inertia vortex-flow and defrosting device of tower top into one
It send after step gas-liquid separation to purified gas aftercooler 3, is cooled to 37 DEG C or so rear feeding knockout drums 4, incoagulable gas
Downstream blower is sent to by going out device after the efficient inertia vortex-flow and defrosting device in gas-liquid separation tank top, 4 bottom of knockout drum contains
Oily water is then sent to sewage-treatment plant.
By the above-mentioned means, a kind of purification-recovery system for damaged tire cracking oil gas of the utility model will be by that will crack
Gas is sent directly into cracking 1 lower part of gas wash tower, returns in tower after condensing the oily phase circulating cooling of gained using cracking gas to cracking gas
Carry out cooling down, while also having reached washing, purifying effect, in the process to the impurity such as carbon black, dust in cracking gas into
Row removing, the accumulation of impurities such as carbon black are interrupted discharge after tower reactor is cooling;It is straight in tower using hydronic oil phase and cracking gas
Contact cooling, compared to water-cooled indirect heat exchange, increase heat exchange efficiency.
Claims (3)
1. a kind of purification-recovery system for damaged tire cracking oil gas, which is characterized in that including cracking gas wash tower (1), split
Light oil washing section and heavy oil washing section are followed successively by solution gas wash tower (1) up and down, the heavy oil washing section of cracking gas wash tower (1) is logical
Piping has been sequentially communicated heavy oil cycling element and heavy oil cooler (2), and the light oil washing section of cracking gas wash tower (1) passes through pipe
Road is communicated with light oil cycling element, crack the top of gas wash tower (1) by pipeline be sequentially communicated purified gas aftercooler (3) and
Knockout drum (4).
2. a kind of purification-recovery system for damaged tire cracking oil gas as described in claim 1, which is characterized in that described heavy
Oily cycling element includes that the heavy oil circulating pump (5) that the heavy oil washing pars infrasegmentalis of cracking gas wash tower (1) is sequentially communicated and heavy oil follow
Ring cooler (6), the other end of heavy oil recirculation cooler (6) pass through the heavy oil that pipeline is connected to cracking gas wash tower (1) respectively
Washing section top and heavy oil cooler (2).
3. a kind of purification-recovery system for damaged tire cracking oil gas as described in claim 1, which is characterized in that described light
Oily cycling element includes that the light oil circulating pump (7) that the light oil washing pars infrasegmentalis of cracking gas wash tower (1) is sequentially communicated and light oil follow
The other end of ring cooler (8), light oil recirculation cooler (8) is washed by the light oil that pipeline is connected to cracking gas wash tower (1)
Section top.
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CN201821993420.4U CN209161961U (en) | 2018-11-29 | 2018-11-29 | A kind of purification-recovery system for damaged tire cracking oil gas |
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CN201821993420.4U CN209161961U (en) | 2018-11-29 | 2018-11-29 | A kind of purification-recovery system for damaged tire cracking oil gas |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110437859A (en) * | 2019-08-30 | 2019-11-12 | 中国电建集团长春发电设备有限公司 | One kind can continuous garbage cracking rotary processing equipment |
CN111718765A (en) * | 2020-06-28 | 2020-09-29 | 河南恒天久大实业有限公司 | Device and absorption method for fuel oil in plastic pyrolysis gas |
CN113862045A (en) * | 2020-06-30 | 2021-12-31 | 湖南万容科技股份有限公司 | A pyrolysis gas cutting and processing system |
CN114317022A (en) * | 2022-01-24 | 2022-04-12 | 广东国禹装备有限公司 | Pyrolysis oil quality improvement treatment process |
-
2018
- 2018-11-29 CN CN201821993420.4U patent/CN209161961U/en active Active
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110437859A (en) * | 2019-08-30 | 2019-11-12 | 中国电建集团长春发电设备有限公司 | One kind can continuous garbage cracking rotary processing equipment |
CN111718765A (en) * | 2020-06-28 | 2020-09-29 | 河南恒天久大实业有限公司 | Device and absorption method for fuel oil in plastic pyrolysis gas |
CN113862045A (en) * | 2020-06-30 | 2021-12-31 | 湖南万容科技股份有限公司 | A pyrolysis gas cutting and processing system |
CN114317022A (en) * | 2022-01-24 | 2022-04-12 | 广东国禹装备有限公司 | Pyrolysis oil quality improvement treatment process |
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