CN109796997A - A kind of continous way cracking distillation integration organic waste materials processing system - Google Patents

A kind of continous way cracking distillation integration organic waste materials processing system Download PDF

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Publication number
CN109796997A
CN109796997A CN201910150334.XA CN201910150334A CN109796997A CN 109796997 A CN109796997 A CN 109796997A CN 201910150334 A CN201910150334 A CN 201910150334A CN 109796997 A CN109796997 A CN 109796997A
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oil
continous way
distillation
connects
gas
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CN201910150334.XA
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朱存福
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朱存福
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/141Feedstock
    • Y02P20/143Feedstock the feedstock being recycled material, e.g. plastics

Abstract

The embodiment of the invention discloses a kind of continous way cracking distillation integration organic waste materials processing system, including the main furnace of continous way cracking apparatus, the auger of connection feed inlet and slag notch is equipped in the main furnace of continous way cracking apparatus;Condensing unit is equipped with collection gas bag, the first condenser pipe and pre-stored tank;Oil liquid separative unit is equipped with oil-liquid separator, and the liquid feeding end of oil-liquid separator connects pre-stored tank, and waste water end connects effluent treatment plant, and oil outlet connects the first oil storage tank;Distilation unit is equipped with distillation still, and the liquid feeding end of distillation still connects the first oil storage tank, and the outlet side of distillation still connects the second condenser pipe, and the outlet end of the second condenser pipe connects the second oil storage tank.Present system has set gradually the main furnace of continous way cracking apparatus, condensing unit, oil liquid separative unit, distilation unit and tail gas treating unit, it realizes to the pollution-free cracking treatment process of organic waste materials, whole process is without acidification or basification, safety and environmental protection, and being equipped with exhaust gas recirculation is main stove heating, saves the energy.

Description

A kind of continous way cracking distillation integration organic waste materials processing system
Technical field
The present invention relates to gas management technical fields, and in particular at a kind of continous way cracking distillation integration organic waste materials Reason system.
Background technique
China's plastic product sharply increases, so that plastic garbage content has reached developed country in China's house refuse Level, especially China are the big countries of a productive consumption, even if content of the rural city plastic garbage in part in house refuse It is relatively small, but be also that cannot be neglected resource to be processed for total amount.However, processing technique of the China to plastic garbage Research start to walk evening, it is horizontal not as good as developed country.The processing of plastic garbage is concerned because plastics it is in distress compression, it is airtight, The problems such as expansive property, it be easy to cause water pollution, land occupation, sewer blockage, so country forbids a large amount of plastics Rubbish is handled in a manner of filling.And burn except the harm with plastic garbage, the expense of burning is also that can not be ignored The problem of, so the burning of national strict control and limitation to plastic garbage total amount.Plastic garbage is extracted from petroleum With the chemical substance compared with high heating value, its mean calorie highest in house refuse, in order to make plastic garbage energy and warp Jiization.Therefore, how effectively, thoroughly, health processing and most effectively utilize waste plastic, have become the whole society and be concerned about extensively A big problem.
Treatment of waste plastics processing method is being explored always by each enterprise and scientific research institution for many years, and it is difficult for many years to solve this The problem of to break off relations, domestic existing cracking apparatus has the following deficiencies: with distillation equipment at present
1, cracking apparatus discontinuous operation, one furnace of primary charging cracking, after need to wait for cooling and can slag tap to carry out next cracking.
2, hand feed is needed, the main furnace return air fryer risk of Batch Process is high.
3, the not further processed purification of fuel oil produced, oil product are inferior.
4, the fuel oil moisture produced is more, without separation.
5, a large amount of waste water are generated in production process, pollute environment.
6, vent gas treatment effect is poor, and national emission standard is not achieved.
7, main furnace is excessive can reduce the service life by heating cooling procedure, increase security risk.
8, distillation equipment uses pickling tank, caustic treater equipment, generates acid and alkaline waste, pollutes environment.
Summary of the invention
The embodiment of the present invention is designed to provide a kind of continous way cracking distillation integration organic waste materials processing system, uses To solve the problems in background technique.
To achieve the above object, the embodiment of the present invention provides one kind:
A kind of continous way cracking distillation integration organic waste materials processing system, the integration assembly line are successively split including continous way Solve the main furnace of equipment, condensing unit, oil liquid separative unit and distilation unit;Wherein, on the main furnace of continous way cracking apparatus Equipped with feed inlet, oil gas vent, waste gas outlet and slag notch;The condensing unit is equipped with the gas collection being connected with oil gas vent The outlet side of packet, the collection gas bag connects the first condenser pipe, and first condenser pipe connects pre-stored tank;The oil liquid separation is single Member is equipped with oil-liquid separator, and the liquid feeding end of the oil-liquid separator connects pre-stored tank, the oil-liquid separator point by oil pump From waste water end connect effluent treatment plant through water pump, the oil outlet of the oil-liquid separator connects the first oil storage tank through oil pump; The distilation unit is equipped with distillation still, and the liquid feeding end of the distillation still connects the first oil storage tank, the distillation by oil pump The outlet side of kettle connects the second condenser pipe, and the outlet end of second condenser pipe connects the second oil storage tank.
Another preferred embodiment, the heat supply of the waste gas outlet connection distillation still of the main furnace of continous way cracking apparatus The gas side that goes out at end, heat supply end is connected into tail gas treating unit, and the tail gas treating unit, which is equipped with, receives the main furnace of continous way cracking apparatus Adsorption tower is connected with the outlet side of the sprayed tank group of both distillation stills tail gas, the sprayed tank group.
Another preferred embodiment, the waste gas outlet connection of the main furnace of continous way cracking apparatus is in parallel with distillation still to be connected The outlet side of the waste gas condensation device connect, the waste gas condensation device connects tail gas treating unit.
Another preferred embodiment, the exhaust end of pre-stored tank connects auxiliary condenser in the condensing unit, described The exhaust end of auxiliary condenser connects the first water seal, the combustion of the exhaust end connection main furnace of continous way cracking apparatus of first water seal Burn room.
Another preferred embodiment, the collection gas bag are equipped with upper gas outlet and lower gas outlet, the upper gas outlet connection Light oil pre-stored tank, the lower gas outlet connect heavy oil pre-stored tank.
Another preferred embodiment is equipped with distillation preheating can, the distillation between first oil storage tank and distillation still Preheating can and distillation still supplying heat source, if distillation preheating can be it is multiple, be connected in series between multiple distillation preheating cans.
Another preferred embodiment, the outlet side of second oil storage tank are equipped with the second water seal, and second water seal connects Connect the combustion chamber of the main furnace of continous way cracking apparatus.
Another preferred embodiment, the oil-liquid separator are Water by Power Free Oil-water Separator, the Unpowered oil-water point Include cabinet from device, longitudinal baffle is equipped in the cabinet, the bottom of the longitudinal baffle is equipped with filter screen, the longitudinal baffle and filtering Space in cabinet is divided into front cavity and rear chamber by net, is equipped with the first inclined plate in the front cavity, the inlet tube is deep into The top of first inclined plate, the rear chamber is interior to be equipped with the second inclined plate, and the top of second inclined plate connects outlet tube.
Another preferred embodiment, the oil gas vent of the main furnace of continous way cracking apparatus connect the condensation being connected in parallel Unit and moisture condensation unit, the moisture condensation unit includes the water vapor condenser being sequentially connected in series, water pot and water pot water Envelope is equipped with the first ball valve, is equipped between the oil gas vent and moisture condensation unit between the oil gas vent and condensing unit Second ball valve.
The embodiment of the present invention has the advantages that
A kind of continous way cracking distillation integration organic waste materials processing system described in the embodiment of the present invention is split provided with continous way Solve the main furnace of equipment, condensing unit, oil liquid separative unit, distilation unit and tail gas treating unit, thus realize to damaged tire, The treatment process of uncontaminated gases is discharged in the organic waste materials cracking such as plastics processing, and whole process is without acidification or basification, safety Environmental protection, and being equipped with exhaust gas recirculation is main stove heating, saves the energy.
Detailed description of the invention
Fig. 1 is a kind of system of continous way cracking distillation integration organic waste materials processing system provided in an embodiment of the present invention Structure chart;
Fig. 2 is the pipeline connection figure of moisture condensation unit in the embodiment of the present invention;
Fig. 3 is the internal structure chart of oil-liquid separator in Fig. 1;
Fig. 4 is the heat supply output channel figure of the main furnace of continous way cracking apparatus in the embodiment of the present invention.
In figure:
1, the main furnace of continous way cracking apparatus;2, feed screw;3, conveyer belt;4, residue receiving box;5, collect gas bag;6, the first condensation Pipe;7, pre-stored tank;8, auxiliary condenser;9, the first water seal;10, combustion chamber;11, water vapor condenser;12, water pot;13, water pot Water seal;14, oil-liquid separator;15, waste gas condensation device;16, effluent treatment plant;17, the first oil storage tank;18, cabinet;19, Longitudinal baffle;20, filter screen;21, front cavity;22, rear chamber;23, the first inclined plate;24, the second inclined plate;25, inlet tube;26, go out Liquid pipe;27, distillation still;28, the second condenser pipe;29, the second oil storage tank;30, preheating can is distilled;31, the second water seal;32, it sprays Tank group;33, adsorption tower;34, chimney;35, the first ball valve;36, the second ball valve.
Specific embodiment
Embodiments of the present invention are illustrated by particular specific embodiment below, those skilled in the art can be by this explanation Content disclosed by book is understood other advantages and efficacy of the present invention easily.
It should be clear that structure depicted in this specification, ratio, size etc., only to cooperate the revealed content of specification, So that those skilled in the art understands and reads, enforceable qualifications are not intended to limit the invention, therefore do not have technology On essential meaning, the modification of any structure, the change of proportionate relationship or the adjustment of size can be generated not influencing the present invention The effect of and the purpose that can reach under, should all still fall in the range of disclosed technology contents obtain and can cover.Together When, cited such as "upper" in this specification, "lower", " left side ", right ", the term of " centre ", be merely convenient to describe bright , rather than to limit the scope of the invention, relativeness is altered or modified, and is changing technology contents without essence Under, when being also considered as the enforceable scope of the present invention.
As shown in Figure 1, a kind of continous way cracking distillation integration organic waste materials processing system, the integration assembly line according to Secondary includes the main furnace 1 of continous way cracking apparatus, condensing unit, oil liquid separative unit and distilation unit, below with reference to embodiment Illustrate the realization principle and beneficial effect of each unit.
1, the main furnace 1 of continous way cracking apparatus
The main furnace 1 of continous way cracking apparatus is equipped with feed inlet, oil gas vent, waste gas outlet and slag notch, connects at feed inlet Connect feed screw 2, the feed inlet of the feed screw 2 is equipped with hopper, and conveyer belt 3 is by the damaged tire of crushing, waste plastics etc. Organic waste materials convey feed hopper, and hopper is provided with level switch, can control 3 feeding speed of conveyer belt, prevent excessive velocities Blocking is also avoided that the excessively slow poor sealing of speed, it can be achieved that automatically controlling charging rate according to charging situation, avoids fed material from being blocked Or the insufficient generation gas leakage phenomenon of charging.
Feed screw 2 conveys organic waste materials into intracavitary in the main furnace 1 of continous way cracking apparatus from feed inlet, interior intracavitary Equipped with auger, the head and the tail both ends of the auger are separately connected feed inlet and slag notch, and auger conveys organic waste materials from feed inlet To slag notch, cracking processing is carried out in transmission process, the main furnace 1 of continous way cracking apparatus is using material envelope mechanism, with raw material by auger The seal request that inner space is filled up to meet charging with slag tap.Slag notch connects residue receiving box 4, and slag case is equipped with level switch, when When waste residue (such as carbon black) is stacked into certain altitude, level switch feedback, control cabinet controls mucking machine deslagging, and the waste residue of discharge passes through Water cooling plant carries out continuous low temperature and slags tap, and realizes that automation low temperature is slagged tap.
2, condensing unit
The condensing unit is equipped with the collection gas bag 5 being connected with oil gas vent, the first condensation of outlet side connection of the collection gas bag 5 Pipe 6, first condenser pipe 6 connect pre-stored tank 7, the oil-gas transportation that collection gas bag 5 will crack in the main furnace 1 of continous way cracking apparatus To the first condenser pipe 6, condensation cooling stores to be transported to pre-stored tank 7 after oil liquid.
In order to avoid extra oil gas discharge and the problem of pollute environment, the exhaust end of pre-stored tank 7 connects in condensing unit Auxiliary condenser 8 is connect, the exhaust end of the auxiliary condenser 8 connects the first water seal 9, the exhaust end connection of first water seal 9 The combustion chamber 10 of the main furnace 1 of continous way cracking apparatus, the oil gas of not condensed condensation is drained into combustion chamber 10, to connect continous way The main furnace 1 of cracking apparatus increases fuel, realizes waste utilization, prevents oil vapour pollution.
The collection gas bag 5 is equipped with upper gas outlet and lower gas outlet, and upper gas outlet oil gas cleaning, lower gas outlet oil gas is muddy, The upper gas outlet connects light oil pre-stored tank 7, and the lower gas outlet connects heavy oil pre-stored tank 7.According to different purity oil gas Characteristic, the oil gas of different purity is passed through into two gas outlets respectively, the process of refinement, it can be achieved that oil gas is discharged respectively, save Save the energy.Light oil pre-stored tank 7 individually stores and connect subsequent processing equipment with heavy oil pre-stored tank 7, therebetween Independently of each other.
In order to improve the purity of 7 inner fluid of pre-stored tank, as shown in Fig. 2, the oil gas of the main furnace 1 of the continous way cracking apparatus The condensing unit and moisture condensation unit that outlet connection is connected in parallel, the moisture condensation unit includes the water being sequentially connected in series Vapour condenser 11, water pot 12 and water pot water seal 13 are equipped with the first ball valve 35, the oil between the oil gas vent and condensing unit The second ball valve 36 is equipped between gas outlet and moisture condensation unit.When cracking stock (such as polybag plastics system containing large quantity of moisture Product), since raw material moisture height, calciner temperature are lower than 100 °C after main furnace igniting, the second ball valve 36 is opened before this, closes the One ball valve 35, vapor enter water vapor condenser 11, after condensation enter water pot 12 in, water pot water seal 13 completely cut off outside air into Enter.After main in-furnace temperature is higher than 130 °C, the first ball valve 35 is opened, and the second ball valve 36 is closed, the high-purity oil gas of main furnace cracking Condensing unit, the treatment process gone after progress are arrived by collection gas bag 5.
3, oil liquid separative unit
The oil liquid separative unit is equipped with oil-liquid separator 14, and the liquid feeding end of the oil-liquid separator 14 connects pre- storage by oil pump Tank 7 is deposited, the isolated waste water end of the oil-liquid separator 14 connects effluent treatment plant 16 through water pump, and effluent treatment plant 16 purifies Purified processing water is conveyed to adsorption tanks, adsorption tanks by the pollutants such as organic matter, heavy metal element and particulate matter in waste water It can remove sewage peculiar smell, finally the water for meeting national emission standard be discharged.The oil outlet of the oil-liquid separator 14 is through oil pump The first oil storage tank 17 is connected, isolated fuel oil is stored in the first oil storage tank 17 by oil-liquid separator 14.
In order to increase the feature of environmental protection of oil liquid separation, oil-liquid separator 14 is preferably Unpowered oil-water separation in the present embodiment Device is equipped with longitudinal baffle 19, the vertical gear in the cabinet 18 as shown in figure 3, the Water by Power Free Oil-water Separator includes cabinet 18 The bottom of plate 19 is equipped with filter screen 20, and space in cabinet 18 is divided into front cavity 21 with after with filter screen 20 by the longitudinal baffle 19 Cavity 22, the front cavity 21 is interior to be equipped with the first inclined plate 23, and the inlet tube 25 is deep into the top of the first inclined plate 23, after described The second inclined plate 24 is equipped in cavity 22, the top of second inclined plate 24 connects outlet tube 26, front cavity 21 and rear chamber 22 Bottom is equipped with slag notch.After mixed liquor enters front cavity 21 from inlet tube 25, is slowly slid from the first inclined plate 23, prevent oil Liquid, which is freely fallen into the deposition liquid of lower part, upsets separated part, and the oil liquid residue in front cavity 21 is filtered laggard by filter screen 20 Enter to rear chamber 22,22 inner fluid of rear chamber is automatically separated by the second inclined plate 24, and top oil liquid is flowed out from outlet tube 26, bottom water Part is discharged from slag notch, bubbles through the water column after making the collision of oil liquid unhurried current and partition, does not need any power, can automatically will be oily It is separated from water and stores respectively, oil liquid separation process is convenient and efficient, safety and environmental protection.
4, distilation unit
The distilation unit is equipped with distillation still 27, and the liquid feeding end of the distillation still 27 connects the first oil storage tank by oil pump 17, the outlet side of the distillation still 27 connects the second condenser pipe 28, and the outlet end of second condenser pipe 28 connects the second oil storage Tank 29, the oil gas after 27 distilation of distillation still enters cooling liquid in the second condenser pipe 28, after cooling liquid Liquid is flowed into storage in the second oil storage tank 29, and second oil storage tank 29 connects the second water seal 31, makes in the second oil storage tank 29 Non- blau gas avoids oil gas from overflowing pollution environment through 31 return combustion of the second water seal, and can reduce the loss of the energy, saves energy Source.
Distillation preheating can 30, the distillation preheating can 30 and distillation are equipped between first oil storage tank 17 and distillation still 27 27 supplying heat source of kettle, distillation preheating can 30 is 3 in the present embodiment, such as distills preheating can 30a, distillation preheating can 30b, distillation preheating Tank 30c is then connected in series between 3 distillation preheating cans 30, and distillation preheating can 30 is according to from the first oil storage tank 17 and distillation still 27 Sequence preheating temperature gradually increase, if in figure distill preheating can 30a temperature be less than distillation preheating can 30b, distill preheating can The temperature of 30b is less than distillation preheating can 30c, preheats the oil liquid in the first oil storage tank 17 by multiple distillation preheating cans 30, will Moisture separates in oil liquid, and flows into distillation still 27 after increase crude oil temperature staged, carries out heating evaporation and goes out oil gas, makes to distill Pre-heating system production is more safe and reliable.
The distilation unit of the present embodiment, without pickling tank and caustic treater, is not deposited compared with Conventional espresso purifier units In acid or alkalinity waste material, safety, the feature of environmental protection of distilation are improved.
5, tail gas treating unit
The main furnace 1 of continous way cracking apparatus waste gas outlet connection distillation still 27 for being connected into tail gas treating unit after hot side, The tail gas treating unit is equipped with the sprayed tank group 32 for receiving both the main furnace 1 of continous way cracking apparatus and distillation still 27 tail gas, institute The spray column that sprayed tank group 32 is equipped with multiple series connections is stated, spray column is equipped with dismounting spraying shower device, facilitates maintenance to replace, position Adsorption tower 33 is connected in the outlet side of the last one spray column, the gas in adsorption tower 33 is discharged after adsorbing from chimney 34.
As shown in figure 4, the waste gas outlet connection of the main furnace 1 of continous way cracking apparatus is connected in parallel exhaust gas with distillation still 27 Condensing unit 15, the outlet side of the waste gas condensation device 15 connect tail gas treating unit, are equipped with ball in two parallel branches Valve control conducting.Waste gas outlet of the heat source of distilation unit from the main furnace 1 of continous way cracking apparatus can thus make continuous In the extra heat absorption to distillation still 27 of the main furnace 1 of formula cracking apparatus, this structure design can efficiently use exhaust combustion generation Heat, really realize energy conservation and environmental protection, economical and efficient and the high purpose of space utilization rate.And by two ball valve controls, if steaming It evaporates after heat reaches established standards in kettle 27, closes the heat supply of distillation still 27, open the branch of waste gas condensation device 15, exhaust gas is cold Solidifying device 15 absorbs the high temperature heat in main furnace exhaust, is lowered into the gas temperature of spray column, reduces the entirety of system operation Damage, environmental protection and the saving energy.
Distillation still 27 for hot side on the pipeline of tail gas treating unit can multiple distillation preheating cans 30 in parallel for hot side, The waste heat for realizing main furnace is distillation still 27 and the distillation equal heat supply of preheating can 30, efficiently uses the heat that exhaust combustion generates, really Realize energy conservation and environmental protection, economical and efficient and the high purpose of space utilization rate.
Although above having used general explanation and specific embodiment, the present invention is described in detail, at this On the basis of invention, it can be made some modifications or improvements, this will be apparent to those skilled in the art.Therefore, These modifications or improvements without departing from theon the basis of the spirit of the present invention are fallen within the scope of the claimed invention.

Claims (9)

1. a kind of continous way cracking distillation integration organic waste materials processing system, it is characterised in that: it is described integration assembly line according to Secondary includes the main furnace of continous way cracking apparatus, condensing unit, oil liquid separative unit and distilation unit;Wherein,
The main furnace of continous way cracking apparatus is equipped with feed inlet, oil gas vent, waste gas outlet and slag notch;
The condensing unit is equipped with the collection gas bag being connected with oil gas vent, the first condensation of outlet side connection of the collection gas bag Pipe, first condenser pipe connect pre-stored tank;
The oil liquid separative unit is equipped with oil-liquid separator, and the liquid feeding end of the oil-liquid separator connects pre-stored by oil pump The waste water end of tank, the oil-liquid separator separation connects effluent treatment plant, the oil outlet warp of the oil-liquid separator through water pump Oil pump connects the first oil storage tank;
The distilation unit is equipped with distillation still, and the liquid feeding end of the distillation still connects the first oil storage tank by oil pump, described The outlet side of distillation still connects the second condenser pipe, and the outlet end of second condenser pipe connects the second oil storage tank.
2. continous way cracking distillation integration organic waste materials processing system according to claim 1, it is characterised in that: described The heat supply end of the waste gas outlet connection distillation still of the main furnace of continous way cracking apparatus, the gas side that goes out of heat supply end are connected into vent gas treatment list Member, the tail gas treating unit is equipped with the sprayed tank group for receiving both the main furnace of continous way cracking apparatus and distillation still tail gas, described The outlet side of sprayed tank group connects adsorption tower.
3. continous way cracking distillation integration organic waste materials processing system according to claim 2, it is characterised in that: described The waste gas condensation device that the waste gas outlet connection of the main furnace of continous way cracking apparatus is connected in parallel with distillation still, the waste gas condensation dress The outlet side connection tail gas treating unit set.
4. continous way cracking distillation integration organic waste materials processing system according to claim 1, it is characterised in that: described The exhaust end of pre-stored tank connects auxiliary condenser in condensing unit, and the exhaust end of the auxiliary condenser connects the first water seal, The combustion chamber of the exhaust end connection main furnace of continous way cracking apparatus of first water seal.
5. continous way cracking distillation integration organic waste materials processing system according to claim 1, it is characterised in that: described Collect gas bag and be equipped with upper gas outlet and lower gas outlet, the upper gas outlet connects light oil pre-stored tank, the lower gas outlet connection weight Oily pre-stored tank.
6. continous way cracking distillation integration organic waste materials processing system according to claim 1, it is characterised in that: described Distillation preheating can, the distillation preheating can and distillation still supplying heat source are equipped between first oil storage tank and distillation still, if distillation preheating Tank be it is multiple, then be connected in series between multiple distillation preheating cans.
7. continous way cracking distillation integration organic waste materials processing system according to claim 1, it is characterised in that: described The outlet side of second oil storage tank is equipped with the second water seal, the combustion chamber of the second water seal connection main furnace of continous way cracking apparatus.
8. continous way cracking distillation integration organic waste materials processing system according to claim 1, it is characterised in that: described Oil-liquid separator is Water by Power Free Oil-water Separator, and the Water by Power Free Oil-water Separator includes cabinet, and vertical gear is equipped in the cabinet Plate, the bottom of the longitudinal baffle are equipped with filter screen, the longitudinal baffle and filter screen and space in cabinet are divided into front cavity with after Cavity, the front cavity is interior to be equipped with the first inclined plate, and the inlet tube is deep into the top of the first inclined plate, is equipped in the rear chamber The top of second inclined plate, second inclined plate connects outlet tube.
9. continous way cracking distillation integration organic waste materials processing system according to claim 1, it is characterised in that: described The condensing unit and moisture condensation unit that the oil gas vent connection of the main furnace of continous way cracking apparatus is connected in parallel, the moisture condensation Unit includes the water vapor condenser being sequentially connected in series, water pot and water pot water seal, is set between the oil gas vent and condensing unit There is the first ball valve, the second ball valve is equipped between the oil gas vent and moisture condensation unit.
CN201910150334.XA 2019-02-28 2019-02-28 A kind of continous way cracking distillation integration organic waste materials processing system Pending CN109796997A (en)

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WO2021232946A1 (en) * 2020-05-19 2021-11-25 青岛科技大学 Precise and efficient multi-stage condensation separation apparatus
CN112251251A (en) * 2020-09-29 2021-01-22 无锡金球机械有限公司 Industrial continuous classified cracking system and process for mixed waste plastics

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Application publication date: 20190524