CN109280216A - Intelligent environmental protection type Waste plastic treatment apparatus - Google Patents
Intelligent environmental protection type Waste plastic treatment apparatus Download PDFInfo
- Publication number
- CN109280216A CN109280216A CN201811091898.2A CN201811091898A CN109280216A CN 109280216 A CN109280216 A CN 109280216A CN 201811091898 A CN201811091898 A CN 201811091898A CN 109280216 A CN109280216 A CN 109280216A
- Authority
- CN
- China
- Prior art keywords
- heating furnace
- environmental protection
- treatment apparatus
- waste plastic
- protection type
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000002699 waste material Substances 0.000 title claims abstract description 23
- 239000004033 plastic Substances 0.000 title claims abstract description 22
- 229920003023 plastic Polymers 0.000 title claims abstract description 22
- 230000007613 environmental effect Effects 0.000 title claims abstract description 16
- 238000005336 cracking Methods 0.000 claims abstract description 44
- 238000010438 heat treatment Methods 0.000 claims abstract description 34
- 230000007246 mechanism Effects 0.000 claims abstract description 33
- 230000003197 catalytic effect Effects 0.000 claims abstract description 18
- 239000002893 slag Substances 0.000 claims abstract description 18
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 claims abstract description 10
- 239000002283 diesel fuel Substances 0.000 claims abstract description 9
- 239000003502 gasoline Substances 0.000 claims abstract description 9
- 239000002253 acid Substances 0.000 claims abstract description 8
- 239000000295 fuel oil Substances 0.000 claims abstract description 6
- 238000003756 stirring Methods 0.000 claims abstract description 6
- 239000000428 dust Substances 0.000 claims description 33
- 210000004907 gland Anatomy 0.000 claims description 8
- 239000000203 mixture Substances 0.000 claims description 3
- 230000007306 turnover Effects 0.000 claims description 2
- 238000002485 combustion reaction Methods 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 7
- 238000010926 purge Methods 0.000 abstract description 6
- 239000003921 oil Substances 0.000 abstract description 5
- 230000008569 process Effects 0.000 abstract description 5
- 230000000505 pernicious effect Effects 0.000 abstract description 2
- 230000035939 shock Effects 0.000 abstract description 2
- 230000001737 promoting effect Effects 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 16
- 230000006872 improvement Effects 0.000 description 9
- 238000009833 condensation Methods 0.000 description 4
- 230000005494 condensation Effects 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 238000006555 catalytic reaction Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000008676 import Effects 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 239000006229 carbon black Substances 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 238000005194 fractionation Methods 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 230000000007 visual effect Effects 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000004523 catalytic cracking Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000000523 sample Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J11/00—Recovery or working-up of waste materials
- C08J11/04—Recovery or working-up of waste materials of polymers
- C08J11/10—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2300/00—Characterised by the use of unspecified polymers
- C08J2300/30—Polymeric waste or recycled polymer
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention discloses intelligent environmental protection type Waste plastic treatment apparatus, including rack, stir hopper, screw feed mechanism, crack mechanism, catalytic tower, fractionating column, condenser, compressor, diesel oil pans, heavy oil pans, gasoline pans, screw feed mechanism is equipped with chlorine gas collector, chlorine gas collector is connected with acid storage tank by pipeline, cracking mechanism is made of cracking chamber and heating furnace, the lower end of heating furnace is equipped with combustor, combustor is by sending fire tube to be connected with flame distributor, flame distributor is set to the tip position of heating furnace, the top of heating furnace is equipped with vapour dirt separating mechanism, the end for cracking mechanism is equipped with helical slag removing machine structure.The advantage of the invention is that promoting catalytic process progress, the purity of oil distillate is improved；The stability and shock resistance of structure are increased, overall structure occupies little space, and is able to achieve intelligence and is uniformly controlled；Active control bed drain purge increases device air-tightness, and internal pernicious gas is prevented to be discharged, and pollutes environment.
Description
Technical field
The present invention relates to Treatment of Waste Plastics technical fields, and in particular to intelligent environmental protection type Waste plastic treatment apparatus.
Background technique
It is disclosed in the patent document of Publication No. CN205341474U a kind of for refuse plastic harmless treatment and energy
The special equipment that source utilizes is realized by processes such as charging, conveying, degassing, cracking, catalysis, fractionation, condensation, deslagginves
The harmless treatment of waste plastic, and diesel oil, gasoline has been made etc. and can use the energy.
But device structure has a variety of defects: (1) bed drain purge is unable to control, it is understood that there may be melt is split in cracking still
Solve insufficient situation；And the waste residue of slag-drip opening is in rarefaction, and poor air-tightness is easy to cause outside internal contamination gas
It lets out, pollutes environment；(2) combustor flame pipeline causes heating uneven from the bottom of burner hearth directly against cracking chamber heating, and
It is easy to damage collection hot spot；(3) catalytic tower, the carbon powder dust of cracking gas doping are introduced directly into the cracking gas after cracking
It will affect the progress of catalytic process, and cause the gasoline produced, diesel oil purity unqualified, long-time service also will cause pipeline
Blocking；(4) in addition, other defects such as structure occupied space are big, the degree of automation is low, heat and cold consumption are big.
Summary of the invention
The purpose of the present invention is to provide a kind of intelligent environmental protection type Waste plastic treatment apparatus, and which solve at traditional waste plastics
Manage device bed drain purge can not active control, poor air-tightness, structural stability are poor, renewable sources of energy purity is low, the degree of automation is low etc.
Problem.
The present invention through the following technical solutions to achieve the above objectives:
Intelligent environmental protection type Waste plastic treatment apparatus, including rack, stirring hopper, screw feed mechanism, cracking mechanism, catalysis
Tower, fractionating column, condenser, compressor, diesel oil pans, heavy oil pans, gasoline pans are set in the screw feed mechanism
Have a chlorine gas collector, the chlorine gas collector is connected with acid storage tank by pipeline, the cracking mechanism by internal layer cracking chamber and
The heating furnace of outer layer forms, and the cracking is intracavitary to be equipped with blender, and the lower end of the heating furnace is equipped with combustor, the combustor
By sending fire tube to be connected with flame distributor, the flame distributor is set to the tip position of heating furnace, and flame distributor
Along axial direction, into heating furnace burner hearth, flame, the top of the heating furnace are equipped with vapour dirt separating mechanism, the vapour dirt separating mechanism one
End is connected to intracavitary portion is cracked, and is connected to inside the other end and catalytic tower, and the end of the cracking mechanism is equipped with helical slag removing machine structure.
Further improvement lies in that the vapour dirt separating mechanism includes knockout drum, connecting tube, vapour dirt channel, dust compartment, connects dirt
Bucket, gland steam exhauster, the knockout drum are connected to heating furnace top vertically, and the bottom end of the connecting tube is connected to intracavitary portion is cracked, even
The top of adapter tube is connected to vapour dirt channel, and vapour dirt channel, dust compartment and dust receiving bucket are set in knockout drum, and vapour dirt channel
Top be connected to the top of dust compartment, the dust receiving bucket is located at the lower section of dust compartment, and dust receiving bucket bottom end is connected to knockout drum
Outside tank, described gland steam exhauster one end is connected to the top of dust compartment, and the other end is connected to catalytic tower.
Further improvement lies in that the connecting tube be double-wall corrugated pipe structure, and the bottom end of connecting tube and cracking chamber chamber
Wall connection, the top of connecting tube and the furnace wall of heating furnace connect.
Further improvement lies in that the helical slag removing machine structure includes pipe sleeve, deslagging screw rod and overturning lid, the pipe sleeve inner end
Head is connected to cracking chamber, and the deslagging screw rod is located in pipe sleeve, and the inner termination of deslagging screw rod and blender are coaxially connected, described
Overturning lid is hinged through the hinge to the external end head top of pipe sleeve；
The length of the deslagging screw rod is less than pipe sleeve length, forms one between the external end head and overturning lid of deslagging screw rod
Cavity.
Further improvement lies in that the length of the deslagging screw rod is the 2/3 of pipe sleeve length.
Further improvement lies in that the helical slag removing machine structure further includes the shield being located at outside pipe sleeve, set on the shield
There is the three-link driving member for controlling overturning lid folding angle.
Further improvement lies in that the bottom end of the shield is equipped with slag notch, the top of the shield is equipped with switch cover.
Further improvement lies in that the outside of the overturning lid is connected with weighted spherical ball.
Further improvement lies in that the flame distributor is the flame distributor with double boccas.
The beneficial effects of the present invention are:
(1) it is additionally arranged vapour dust separating device, the carbon powder dust and other impurities that will be adulterated in the cracking gas of cracking generation
Deposition is removed, then carries out the catalysis of next step, fractionation, has been effectively facilitated the progress of catalytic process, has been improved the purity of oil distillate,
And help to prevent line clogging.
(2) and using in heating furnace burner hearth is double-wall corrugated pipe structure, effectively increases the stability of structure and resists
Pinking；The structural arrangements such as catalytic tower, fractionating column, condenser are reasonable, and overall structure occupies little space, and are able to achieve intelligent unified
Control, high degree of automation.
(3) energy active control bed drain purge ensure that cracking intracavitary melt is sufficiently cracked, and is also avoided melt and is being cracked
The case where intracavitary residence time is too long, excessively heats, while slag-drip opening is got lodged in by squeezing waste residue powder, increase the gas of device
Close property prevents internal pernicious gas to be discharged, and pollutes environment.
(4) heating method of heating furnace is improved, so that it is more uniform to crack intracavitary temperature, and avoids temperature excessively
Concentration causes burning out for structural member.
Detailed description of the invention
Fig. 1 is a kind of structural schematic diagram of the present invention under visual angle；
Fig. 2 is structural schematic diagram of the present invention under another visual angle；
Fig. 3 is the structural schematic diagram of helical slag removing machine structure；
In figure: 1- rack, 2- stir hopper, 3- screw feed mechanism, 4- catalytic tower, 5- fractionating column, 6- condenser, 7- pressure
Contracting machine, 8- diesel oil pans, 9- heavy oil pans, 10- gasoline pans, 11- chlorine gas collector, 12- acid storage tank, 13- cracking
Chamber, 14- heating furnace, 15- blender, 16- combustor, 17- flame distributor, 18- knockout drum, 19- connecting tube, 20- vapour dirt are logical
Road, 21- dust compartment, 22- dust receiving bucket, 23- gland steam exhauster, 24- pipe sleeve, 25- deslagging screw rod, 26- overturning lid, 27- shield, 28- tri-
Link transmission part, 29- slag notch, 30- switch cover, 31- weighted spherical ball.
Specific embodiment
The application is described in further detail with reference to the accompanying drawing, it is necessary to it is indicated herein to be, implement in detail below
Mode is served only for that the application is further detailed, and should not be understood as the limitation to the application protection scope, the field
Technical staff can make some nonessential modifications and adaptations to the application according to above-mentioned application content.
In conjunction with shown in Fig. 1 to Fig. 3, intelligent environmental protection type Waste plastic treatment apparatus, including rack 1, stirring hopper 2, screw rod into
Expect mechanism 3, cracking mechanism, catalytic tower 4, fractionating column 5, condenser 6, compressor 7, diesel oil pans 8, heavy oil pans 9 and vapour
Oily pans 10, these are not described in detail here using conventional connection type.Wherein, it is set in screw feed mechanism 3
There is chlorine gas collector 11, chlorine gas collector 11 is connected with acid storage tank 12 by pipeline, and chlorine is converted to salt by chlorine gas collector 11
Acid (hydrogen synthesis can be used, add water) is simultaneously stored in acid storage tank 12；Mechanism is cracked by the cracking chamber 13 and outer layer of internal layer
Heating furnace 14 forms, and blender 15 is equipped in cracking chamber 13, and the lower end of heating furnace 14 is equipped with combustor 16, and combustor 16 is by sending
Fire tube is connected with flame distributor 17, and flame distributor 17 is set to the tip position of heating furnace 14, and 17 edge of flame distributor
The axial flame into 14 burner hearth of heating furnace, flame distributor 17 are the flame distributor with double boccas, the top of heating furnace 14
End is equipped with vapour dirt separating mechanism, is connected to inside vapour dirt separating mechanism one end and cracking chamber 13, connects inside the other end and catalytic tower 4
Logical, the end for cracking mechanism is equipped with helical slag removing machine structure.
Wherein, vapour dirt separating mechanism include knockout drum 18, connecting tube 19, vapour dirt channel 20, dust compartment 21, dust receiving bucket 22,
Gland steam exhauster 23, knockout drum 18 are connected to 14 top of heating furnace vertically, are connected to, connect inside the bottom end of connecting tube 19 and cracking chamber 13
The top of pipe 19 is connected to vapour dirt channel 20, and vapour dirt channel 20, dust compartment 21 and dust receiving bucket 22 are set in knockout drum 18, and vapour
The top in dirt channel 20 is connected to the top of dust compartment 21, and dust receiving bucket 22 is located at the lower section of dust compartment 21, and 22 bottom end of dust receiving bucket
It is connected to outside 18 tank of knockout drum, 23 one end of gland steam exhauster is connected to the top of dust compartment 21, and the other end is connected to catalytic tower 4.Especially
, connecting tube 19 is double-wall corrugated pipe structure, and the bottom end of connecting tube 19 is connect with the cavity wall of cracking chamber 13, the top of connecting tube 19
End is connect with the furnace wall of heating furnace 14, effectively increases the stability and shock resistance of structure.
Wherein, helical slag removing machine structure include pipe sleeve 24, deslagging screw rod 25 and overturning lid 26,24 inner termination of pipe sleeve and cracking chamber
13 connections, deslagging screw rod 25 is located in pipe sleeve 24, and the inner termination of deslagging screw rod 25 and blender 15 are coaxially connected, overturns lid 26
It is hinged through the hinge to the external end head top of pipe sleeve 24；The length of deslagging screw rod 25 is less than 24 length of pipe sleeve, generally may be configured as
The length of deslagging screw rod 25 is the 2/3 of 24 length of pipe sleeve, is formed between the external end head of deslagging screw rod 25 and overturning lid 26 in this way
One cavity.When in use, it can be filled waste residue powder in cavity, ensure that internal gas will not be discharged.
Also, helical slag removing machine structure further includes the shield 27 being located at outside pipe sleeve 24, and shield 27 is equipped with to be turned over for controlling
The three-link driving member 28 of the folding angle of hub cap 26.The intermediate position and 27 top of shield of the first connecting rod of three-link driving member 28
It is flexibly connected, second connecting rod is flexibly connected with first connecting rod head and the tail, and third connecting rod is flexibly connected with second connecting rod head and the tail, and third
The end of connecting rod is fixedly connected with overturning lid 26.When dialing up first connecting rod, it will drive overturning lid 26 and increase opening angle, this
When bed drain purge increase so that cracking chamber 13 in the melt residence time reduce, when stirring first connecting rod downwards, will drive overturning lid
26 tend to be closed, so that the melt residence time in cracking chamber 13 increases.So only need to outside shield 27 can active control turn over
The opening and closing angle of hub cap 26, also achieves the control to bed drain purge.
In addition, the bottom end of shield 27 is equipped with slag notch 29, the top of shield 27 is equipped with switch cover 30, overturns the outside of lid 26
It is connected with weighted spherical ball 31.
Specific workflow of the invention are as follows:
The smashed waste plastics of investment in hopper 2 is stirred, is conveyed through screw feed mechanism 3, in transmission process, heating furnace 14
It is to be heated in screw feed mechanism 3 by pipeline, heating temperature is at 300 DEG C or so, so that plastics become molten condition, and makes to mould
Chlorine evolution in material, is collected by chlorine gas collector 11 and is converted, and become hydrochloric acid and be stored in acid tube 12；Melt enters cracking
Chamber 13, heating and temperature control is at 500 DEG C or so, and blender 15 is stirred continuously, and melt is gradually cleaved, formed cracking gas and
Carbon black granulated slag, carbon black are discharged from helical slag removing machine structure, and the cooling circulating water of condenser 6 is connected in helical slag removing machine structure.Cracking gas
It by connecting tube 15, imports in knockout drum, carries out the separation of vapour dirt, deposit the carbon powder dust to get off and be discharged by dust receiving bucket 22, separate
Cracking gas afterwards is imported in catalytic tower 4 by gland steam exhauster, is heated, is heated using the hot exhaust gas of heating cracking mechanism in catalytic tower 4
About 380 DEG C~420 DEG C of temperature, catalytic cracking reaction occurs when cracking gas passes through the catalyst being heated in catalytic tower 4, generates
Fuel-air mixture, fuel-air mixture import fractionating column 5 after collecting.Fractionating column 5 is using reflux packed tower certainly, tower top cooling temperature 35
~55 DEG C, filler temperature is about maintained at 160~185 DEG C, and filler uses stainless steel rectangular saddle ring, and fractionating column 5 is deposited after slipping out diesel oil
Enter diesel oil pans 8, the mixed oil and gas of gasoline and tail gas is sent into condenser 6 from the tracheae on tower top, and condenser 6 uses shell and tube
Water condensation tower, for condensation temperature at 20~30 DEG C, mixed oil and gas enters gasoline condensation deposit gasoline pans 9 after condenser 6, is left
Oil distillate be stored in heavy oil pans 10, remaining tail gas from tower top tracheae submitting after enter compressor 7 pressurize, then
Import corresponding liquefaction system carry out liquefaction deposit tank.
Particularly, the present invention is also integrated with control system, control system include industrial control computer, pressure sensor,
Temperature sensor, speed probe, flow sensor, monitor and execution electric appliance etc., control system is collected by sensor
Real-time display comes out and record while carrying out the data of these data and computer settings various data on a monitor
After comparison, instruction is issued to electric appliance is executed, automatically correcting implementation deviation amount makes device remain normal operation, when device occurs
When failure, control system will alarm and voluntarily start safety device or autostop, ensure that equipment safety, and realize complete
The intelligent management of process.
The embodiments described above only express several embodiments of the present invention, and the description thereof is more specific and detailed, but simultaneously
Limitations on the scope of the patent of the present invention therefore cannot be interpreted as.It should be pointed out that for those of ordinary skill in the art
For, without departing from the inventive concept of the premise, various modifications and improvements can be made, these belong to guarantor of the invention
Protect range.
Claims (9)
1. intelligent environmental protection type Waste plastic treatment apparatus, including rack (1), stirring hopper (2), screw feed mechanism (3), decomposing machine
Structure, catalytic tower (4), fractionating column (5), condenser (6), compressor (7), diesel oil pans (8), heavy oil pans (9), in gasoline
Between tank (10), it is characterised in that: the screw feed mechanism (3) be equipped with chlorine gas collector (11), the chlorine gas collector
(11) it is connected with acid storage tank (12) by pipeline, the cracking mechanism is by the cracking chamber (13) of internal layer and the heating furnace (14) of outer layer
Composition, the cracking chamber (13) is interior to be equipped with blender (15), and the lower end of the heating furnace (14) is equipped with combustor (16), the combustion
For burning machine (16) by sending fire tube to be connected with flame distributor (17), the flame distributor (17) is set to the end of heating furnace (14)
Head position, and along axial direction, the flame into heating furnace (14) burner hearth, the top of the heating furnace (14) are equipped with flame distributor (17)
It is connected to inside vapour dirt separating mechanism, described vapour dirt separating mechanism one end and cracking chamber (13), connects inside the other end and catalytic tower (4)
Logical, the end of the cracking mechanism is equipped with helical slag removing machine structure.
2. intelligent environmental protection type Waste plastic treatment apparatus according to claim 1, it is characterised in that: the vapour dirt separating mechanism
It is described including knockout drum (18), connecting tube (19), vapour dirt channel (20), dust compartment (21), dust receiving bucket (22), gland steam exhauster (23)
Knockout drum (18) is connected to heating furnace (14) top vertically, is connected to inside the bottom end of the connecting tube (19) and cracking chamber (13),
The top of connecting tube (19) is connected to vapour dirt channel (20), and vapour dirt channel (20), dust compartment (21) and dust receiving bucket (22) are equal
In knockout drum (18), and the top in vapour dirt channel (20) is connected to the top of dust compartment (21), and the dust receiving bucket (22) sets
In the lower section of dust compartment (21), and dust receiving bucket (22) bottom end is connected to outside knockout drum (18) tank, and described gland steam exhauster (23) one end connects
The top in dust compartment (21) is connect, the other end is connected to catalytic tower (4).
3. intelligent environmental protection type Waste plastic treatment apparatus according to claim 2, it is characterised in that: the connecting tube (19) is
Double-wall corrugated pipe structure, and the bottom end of connecting tube (19) with cracking chamber (13) cavity wall connect, the top of connecting tube (19) with add
The furnace wall of hot stove (14) connects.
4. intelligent environmental protection type Waste plastic treatment apparatus according to claim 1, it is characterised in that: the helical slag removing machine structure
Including pipe sleeve (24), deslagging screw rod (25) and overturning lid (26), pipe sleeve (24) inner termination is connected to cracking chamber (13), described
Deslagging screw rod (25) is located in pipe sleeve (24), and the inner termination of deslagging screw rod (25) and blender (15) are coaxially connected, described to turn over
Hub cap (26) is hinged through the hinge to the external end head top of pipe sleeve (24)；
The length of the deslagging screw rod (25) is less than pipe sleeve (24) length, in the external end head and overturning lid (26) of deslagging screw rod (25)
Between formed a cavity.
5. intelligent environmental protection type Waste plastic treatment apparatus according to claim 4, it is characterised in that: the deslagging screw rod (25)
Length be pipe sleeve (24) length 2/3.
6. intelligent environmental protection type Waste plastic treatment apparatus according to claim 4, it is characterised in that: the helical slag removing machine structure
It further include being located at the external shield (27) of pipe sleeve (24), the shield (27), which is equipped with, opens and closes angle for controlling overturning lid (26)
Three-link driving member (28).
7. intelligent environmental protection type Waste plastic treatment apparatus according to claim 6, it is characterised in that: the bottom of the shield (27)
End is equipped with slag notch (29), and the top of the shield (27) is equipped with switch cover (30).
8. intelligent environmental protection type Waste plastic treatment apparatus according to claim 4, it is characterised in that: the overturning lid (26)
Outside is connected with weighted spherical ball (31).
9. intelligent environmental protection type Waste plastic treatment apparatus according to claim 1, it is characterised in that: the flame distributor
It (17) is the flame distributor with double boccas.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811091898.2A CN109280216B (en) | 2018-09-19 | 2018-09-19 | Intelligent environment-friendly waste plastic treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811091898.2A CN109280216B (en) | 2018-09-19 | 2018-09-19 | Intelligent environment-friendly waste plastic treatment device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN109280216A true CN109280216A (en) | 2019-01-29 |
| CN109280216B CN109280216B (en) | 2023-12-05 |
Family
ID=65180806
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811091898.2A Active CN109280216B (en) | 2018-09-19 | 2018-09-19 | Intelligent environment-friendly waste plastic treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109280216B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117270478A (en) * | 2023-11-20 | 2023-12-22 | 江苏华旭环卫科技有限公司 | Production control system for waste plastic film forming and thermal cracking device |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5811606A (en) * | 1995-11-23 | 1998-09-22 | Plastic Advanced Recycling Corp. | Process and equipment for treatment of waste plastics |
| CN204042278U (en) * | 2014-06-26 | 2014-12-24 | 昆明德远电气技术有限公司 | Double-wall corrugated pipe mechanical compaction junction button |
| CN204400006U (en) * | 2014-12-30 | 2015-06-17 | 浙江大道环保科技有限公司 | There is the spiral slag-discharging device of dust cover |
| CN105583213A (en) * | 2015-12-29 | 2016-05-18 | 杨成志 | Method and special equipment for innocent treatment and energy utilization of rubbish plastic |
| CN205261528U (en) * | 2015-12-10 | 2016-05-25 | 容长青 | Biomass particle burner |
| CN205481008U (en) * | 2016-03-01 | 2016-08-17 | 赵吉冲 | Air circulation system is discharged to garbage cracking furnace's nothing |
| CN205948564U (en) * | 2016-03-01 | 2017-02-15 | 赵君华 | Condenser is retrieved in garbage cracking furnace's oil, gas, dirt separation |
| CN106701140A (en) * | 2017-03-01 | 2017-05-24 | 安徽中陆环保设备科技有限公司 | Molten cracking device for harmless treatment of metal plastic garbage |
| CN208869535U (en) * | 2018-09-19 | 2019-05-17 | 汪维平 | Intelligent environmental protection type Waste plastic treatment apparatus |
-
2018
- 2018-09-19 CN CN201811091898.2A patent/CN109280216B/en active Active
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5811606A (en) * | 1995-11-23 | 1998-09-22 | Plastic Advanced Recycling Corp. | Process and equipment for treatment of waste plastics |
| CN204042278U (en) * | 2014-06-26 | 2014-12-24 | 昆明德远电气技术有限公司 | Double-wall corrugated pipe mechanical compaction junction button |
| CN204400006U (en) * | 2014-12-30 | 2015-06-17 | 浙江大道环保科技有限公司 | There is the spiral slag-discharging device of dust cover |
| CN205261528U (en) * | 2015-12-10 | 2016-05-25 | 容长青 | Biomass particle burner |
| CN105583213A (en) * | 2015-12-29 | 2016-05-18 | 杨成志 | Method and special equipment for innocent treatment and energy utilization of rubbish plastic |
| CN205481008U (en) * | 2016-03-01 | 2016-08-17 | 赵吉冲 | Air circulation system is discharged to garbage cracking furnace's nothing |
| CN205948564U (en) * | 2016-03-01 | 2017-02-15 | 赵君华 | Condenser is retrieved in garbage cracking furnace's oil, gas, dirt separation |
| CN106701140A (en) * | 2017-03-01 | 2017-05-24 | 安徽中陆环保设备科技有限公司 | Molten cracking device for harmless treatment of metal plastic garbage |
| CN208869535U (en) * | 2018-09-19 | 2019-05-17 | 汪维平 | Intelligent environmental protection type Waste plastic treatment apparatus |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117270478A (en) * | 2023-11-20 | 2023-12-22 | 江苏华旭环卫科技有限公司 | Production control system for waste plastic film forming and thermal cracking device |
| CN117270478B (en) * | 2023-11-20 | 2024-01-23 | 江苏华旭环卫科技有限公司 | Production control system for waste plastic film forming and thermal cracking device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN109280216B (en) | 2023-12-05 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202530040U (en) | Continuous biomass dry-distillation carbonization apparatus | |
| CN207193198U (en) | A kind of stalk carbonizing device | |
| CN110184080A (en) | A kind of fused salt is pyrolyzed biogas residue and prepares the technique and device of phenol compound | |
| CN205261566U (en) | Solid organic waste resource is made up and is put | |
| CN101781585B (en) | Gasification agent injection device of biomass gasifier | |
| CN208869535U (en) | Intelligent environmental protection type Waste plastic treatment apparatus | |
| CN201686664U (en) | Universal rotary and continuous automatic oil refining machine | |
| CN204841700U (en) | Anti -coking reation kettle and have this anti -coking reation kettle's refining equipment | |
| CN110184094B (en) | Method and device for removing tar in biomass pyrolysis gas by using molten salt | |
| CN101962558B (en) | Biomass combustible gas high-temperature oxygen-free reinforced dry-distillation pyrolysis plant | |
| CN109280216A (en) | Intelligent environmental protection type Waste plastic treatment apparatus | |
| CN111944546A (en) | Movable container system for treating organic solid waste | |
| CN105602584B (en) | Continuous internal heat type solid organic matters bitubular pyrolysis furnace | |
| CN100441664C (en) | Method of preparing boiler fuel from metal bath cracking waste tyre rubber and plastics | |
| CN110129085A (en) | A kind of novel blob of viscose pyrolysis oil preparation system | |
| CN204111645U (en) | A kind of waste and old organic glass rotates spiral shell formula and advances continuous cracking equipment | |
| CN204097408U (en) | A kind of medical waste cracking refining equipment | |
| CN105295985A (en) | Method used for producing fuel oil and combustible gas from abandoned tyres | |
| CN107057725A (en) | Rubbish biomass high-temperature low-pressure pyrolysis gasification system | |
| CN106867559A (en) | A kind of multistage cracking quantity-produced oil refining method | |
| CN110283617A (en) | A kind of high efficiency Waste plastic treatment apparatus and application method | |
| CN107413819A (en) | Fully automatic integral acrylic is innoxious and comprehensive utilization of resources system | |
| CN101684410A (en) | New technology and equipment for continuous oil refining from liquid raw materials and discarded plastics and tires | |
| CN210340784U (en) | High efficiency waste plastic processing apparatus | |
| CN103387842B (en) | A kind of oil refining cracker with heat pipe |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |