CN109678307A - A kind of Three-section type heating non-stick pan oily sludge pyrolysis installation - Google Patents
A kind of Three-section type heating non-stick pan oily sludge pyrolysis installation Download PDFInfo
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- CN109678307A CN109678307A CN201910130204.XA CN201910130204A CN109678307A CN 109678307 A CN109678307 A CN 109678307A CN 201910130204 A CN201910130204 A CN 201910130204A CN 109678307 A CN109678307 A CN 109678307A
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- type heating
- section type
- oily sludge
- stick pan
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- 238000000197 pyrolysis Methods 0.000 title claims abstract description 37
- 238000010438 heat treatment Methods 0.000 title claims abstract description 30
- 239000010802 sludge Substances 0.000 title claims abstract description 25
- 238000009434 installation Methods 0.000 title claims abstract description 17
- 239000000463 material Substances 0.000 claims abstract description 15
- BGOFCVIGEYGEOF-UJPOAAIJSA-N helicin Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1OC1=CC=CC=C1C=O BGOFCVIGEYGEOF-UJPOAAIJSA-N 0.000 claims abstract description 5
- 239000000779 smoke Substances 0.000 claims abstract description 5
- 238000002347 injection Methods 0.000 claims description 20
- 239000007924 injection Substances 0.000 claims description 20
- 239000007787 solid Substances 0.000 claims description 10
- 238000012216 screening Methods 0.000 claims description 8
- 239000007921 spray Substances 0.000 claims description 6
- 238000007599 discharging Methods 0.000 claims description 5
- 239000000843 powder Substances 0.000 claims description 4
- 239000003921 oil Substances 0.000 abstract description 33
- 239000007788 liquid Substances 0.000 abstract description 13
- 239000002699 waste material Substances 0.000 abstract description 10
- 238000004939 coking Methods 0.000 abstract description 5
- 239000004058 oil shale Substances 0.000 abstract description 5
- 239000010721 machine oil Substances 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 17
- 238000000034 method Methods 0.000 description 17
- 238000004064 recycling Methods 0.000 description 8
- 239000004744 fabric Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000012530 fluid Substances 0.000 description 4
- 239000005416 organic matter Substances 0.000 description 4
- 238000005336 cracking Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000003292 glue Substances 0.000 description 3
- 239000004033 plastic Substances 0.000 description 3
- 229920003023 plastic Polymers 0.000 description 3
- 238000003672 processing method Methods 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000839 emulsion Substances 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000010806 kitchen waste Substances 0.000 description 2
- 239000010687 lubricating oil Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000003027 oil sand Substances 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 239000011435 rock Substances 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000008961 swelling Effects 0.000 description 2
- 239000010913 used oil Substances 0.000 description 2
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 238000004026 adhesive bonding Methods 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 239000003280 clastogen Substances 0.000 description 1
- 231100000506 clastogen Toxicity 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 230000001804 emulsifying effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000010813 municipal solid waste Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 230000000505 pernicious effect Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/10—Treatment of sludge; Devices therefor by pyrolysis
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B47/00—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
- C10B47/28—Other processes
- C10B47/32—Other processes in ovens with mechanical conveying means
- C10B47/44—Other processes in ovens with mechanical conveying means with conveyor-screws
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
- C10B57/02—Multi-step carbonising or coking processes
-
- 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
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/40—Valorisation of by-products of wastewater, sewage or sludge processing
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Combustion & Propulsion (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
A kind of Three-section type heating non-stick pan oily sludge pyrolysis installation.Existing processing unit is mainly solved when handling oil field waste, emission problem not up to standard after processing.It is characterized by: being fixed with spiral helicine material impelling sheet (5) outside the shaft (3), the protection walls (10) of annular space are fixed with outside the cylinder (11), heating chamber (8) are formed between cylinder (11) and protection walls (10), protection walls (10) bottom is opened there are three gas inlet, and top is provided with smoke outlet (7).The Three-section type heating non-stick pan oily sludge pyrolysis installation is suitable for the processing of the wastes such as oil field dreg liquid, the oil shale of rich in oil, various discarded machine oil, house refuse simultaneously, and device will not coking, pollution emission will not be generated after processing.
Description
Technical field
The present invention relates to solid organic matters (containing solidliquid mixture) process field, specifically a kind of Three-section type heating does not glue
Pot oily sludge pyrolysis installation.
Background technique
For the oil sludge that the industries such as petroleum, petrochemical industry generate, it is made of water, oil emulsion, absorption oil, solid-state silt particle etc.,
Complicated component, processing difficulty are big.Currently, the processing method of this oil sludge had WATER-WASHING METHOD, incineration method etc., due to country in 2015
Environmental law clear stipulaties, it is desirable that treated solid outlet oil-containing < 0.3%, and above two method is not achieved environmental protection and wants
It asks.Wherein WATER-WASHING METHOD has the following problems: one, treated solid-state silt oil-containing > 1%, can not outlet, also can not recycling
It utilizes；Two, new pollutant can be generated after handling, one is serious oil emulsion is emulsified, due to Na+It is high with active agent content,
When it returns the defeated contact apparatus for electrodewatering to multi-purpose station, device instantaneous short circuit can be made, seriously affect normal safe operation；One is
Oil-containing, containing the exceeded sewage of suspended matter, when it returns defeated time Sewage Disposal, be difficult to realize oil, water quick separating；Three, no
It is able to achieve serialization operation；Four, front end feed impurities are required strictly, when block is excessive or has braided fabric, to seriously affect
The operation of subsequent process equipment.Incineration method has the following problems: one, the premise burned needs two aspects, one is can burn
Liquid need to be atomized to 20 μm hereinafter, the second is aqueous especially liquid water no more than 0.5%, due to all kinds of oil sludges
In it is aqueous exceeded, emulsifying serious liquid can not be atomized to 20 μm hereinafter, therefore being difficult normal combustion；Two, dress used in incineration method
It is serious to set coking；If three, containing chlorine component (such as all kinds of braided fabrics, plastic cloth) in organic matter, incomplete combustion is also easy to produce
The harmful components such as dioxin.
For oil shale, oil-sand, main component is rock and rock pore internal solid oil.Currently, processing method is both at home and abroad
Conventional character pyrolytic process, the technique main problem are that coking is serious, influence to be safely operated.
For used oil, waste lubricating oil, useless cooling oil, kitchen waste oil, waste plastics, scrap rubber, useless braided fabric, house refuse
Deng the processing method taken at present mainly has the pyrolysis of incineration method and conventional character, the problem of equally existing above-mentioned analysis.
As stated above, current processing unit is handling the oil shale of above-mentioned oil field dreg liquid, rich in oil, various useless
When abandoning the wastes such as machine oil, house refuse, emission is not up to standard after processing, and none of these methods or device can fit simultaneously
With the processing of above-mentioned various wastes, it is even more impossible to guarantee emission compliance after handling.
Summary of the invention
In order to overcome existing processing unit when handling above-mentioned waste, emission deficiency not up to standard after processing, this
Invention provides a kind of Three-section type heating non-stick pan oily sludge pyrolysis installation, Three-section type heating non-stick pan oily sludge pyrolysis dress
The processing of the wastes such as oil field dreg liquid, the oil shale of rich in oil, various discarded machine oil, house refuse is set while being suitable for,
And device will not glue pot, and pollution emission will not be generated after processing.
The technical scheme is that a kind of Three-section type heating non-stick pan oily sludge pyrolysis installation, including cylinder, cylinder
It is equipped with shaft at center, is fixed with spiral helicine material impelling sheet outside the shaft, is fixed with annular space outside the cylinder
Protection walls, form heating chamber between cylinder and protection walls, the protection walls bottom opens that there are three gas inlets, and top is provided with smoke evacuation
Mouthful.
Several injection devices are equipped with outside the cylinder, injection device is equipped with injection pipe, and the injection pipe connection is defeated
Pipe is sent, several delivery branch pipes are connected in delivery pipe, delivery branch pipe end is fixed with spray head.
Rotating electric machine and microseism device are connected separately on the cylinder body outer wall.
The bladed body perpendicular to barrel is fixed on the cylinder inboard wall, the bladed body is axially arranged along cylinder, and sword
There is gap between shape body front end and cylinder inboard wall.
One end of the material impelling sheet is connected with feeding device, and charging lock gas dress is equipped between feeding device and cylinder
It sets, one end top opposite with feeding device is fixed with gas vent on the cylinder, and lower end is fixed with discharge nozzle.
The discharge nozzle upper end is equipped with discharging air-lock device, and discharge nozzle side is connected with bulky grain release and manages, under discharge nozzle
End is connected with out screening separator, and screening separator bottom is provided with solid powder outlet out.
The invention has the following beneficial effects: due to taking above scheme, the Three-section type heating non-stick pan oily sludge is warm
Device pot not easy to stick is solved, the insecurity factors such as local heating's swelling and cracking will not be generated, pollution outlet object will not be generated, be free of
Secondary pollution is generated, can run to safety economy, save operating cost.The outlet object of device processing simultaneously realizes harmless
Change simultaneously recycling, it can legal outlet and resource utilization.
Detailed description of the invention
Fig. 1 is structural schematic diagram of the invention；
Fig. 2 is the structural schematic diagram that the present invention has injection device；
Fig. 3 is the cross-sectional view of the A-A along Fig. 2.
1- material propulsion electric machine in figure, 2- bearing block, 3- shaft, 4- gas vent, 5- material impelling sheet, 6- sealing device,
7- smoke outlet, 8- heating chamber, 9- are pyrolyzed chamber, 10- protection walls, 11- cylinder, 12- charging air-lock device, 13- feeding device, 14-
First gas inlet, 15- discharge nozzle, 16- discharging air-lock device, 17- go out screening separator, the outlet of 18- solid powder, 19-
Bulky grain release pipe, 20- injection device, 21- injection pipe, 22- delivery pipe, 23- delivery branch pipe, 24- microseism device, 25- rotation
Motor, 26- speed changer, 27- gear, 28- spray head, 29- bladed body, the second gas inlet of 30-, 31- third gas inlet, I-
First pyrolysis section, II-the second pyrolysis section, III-third pyrolysis section.
Specific embodiment
The present invention will be further explained below with reference to the attached drawings:
As shown in Fig. 1 to Fig. 3, a kind of Three-section type heating non-stick pan oily sludge pyrolysis installation, including cylinder 11, cylinder 11
Shaft 3 is equipped at center, 3 both ends of shaft are supported by bearing block 2, and 3 end of shaft is connected with material propulsion electric machine 1.It is described
Spiral helicine material impelling sheet 5 is fixed with outside shaft 3, one end of the material impelling sheet 5 is connected with feeding device 13, and into
Expect to be equipped with charging air-lock device 12 between device 13 and cylinder 11, the feeding into cylinder 11 of feeding device 13 can be passed through.It is described
One end top opposite with feeding device 13 is fixed with gas vent 4 on cylinder 11, and lower end is fixed with discharge nozzle 15.The discharge nozzle
15 upper ends are equipped with discharging air-lock device 16, and 15 side of discharge nozzle is connected with bulky grain release pipe 19, and 15 lower end of discharge nozzle is connected with
Screening separator 17 out, bulky grain release pipe 19 are fixed on out the side on 17 top of screening separator, out 17 bottom of screening separator
Portion is provided with solid powder outlet 18.
It is fixed with the protection walls 10 of annular space outside the cylinder 11, and is equipped with sealing between 10 both ends of protection walls and cylinder 11
Device 6 makes to form heating chamber 8 between cylinder 11 and protection walls 10, opposite with heating chamber 8, is pyrolysis chamber 9 inside cylinder 11.
For sake of convenience, pyrolysis chamber 9 is in axial direction divided into three sections herein, is followed successively by first the I, second heat of pyrolysis section from left to right
Section II, third pyrolysis section III are solved, 10 bottom of protection walls is opened there are three gas inlet, it is followed successively by the first gas inlet 14, the
Two gas inlets 30, third gas inlet 31, respectively with the position of the first pyrolysis section I, the second pyrolysis section II, third pyrolysis section III
Set one-to-one correspondence.Smoke outlet 7 is provided at the top of 10 right end of protection walls.
Several injection devices 20 are equipped with outside the cylinder 11, injection device 20 is fixed on shaft 3 by rotary joint
On, when so that shaft 3 rotating, injection device 20 can be remained stationary.The injection device 20 is equipped with injection pipe 21, the note
Entering 21 bottom connecting conveying pipe 22 of pipe, delivery pipe 22 is located inside shaft 3, several delivery branch pipes 23 are connected in delivery pipe 22,
Delivery branch pipe 23 is stretched out outside shaft 3, and end is fixed with spray head 28.The injection device 20 is four, 11 both ends of cylinder point
Two are not fixed, and each injection device 20 is separately connected individual delivery pipe 22.Each injection device 20 can inject as needed
Different medical fluids, such as catalytic thermal storage liquid, lightweight liquid, clastogen, destabiliser, when shaft 3 rotates, delivery pipe 22 and conveying branch
Pipe 23 can rotate together therewith, thus by spray head 28 by liquid circumferentially to external comprehensive sprinkling.
Rotating electric machine 25 and microseism device 24, the connection of 25 output end of rotating electric machine are connected separately on 11 outer wall of cylinder
Speed changer 26, speed changer 26 drive cylinder 11 to rotate by being fixed on the gear 27 outside cylinder 11.Microseism device 24 passes through tooth
When wheel is with starting, cylinder 11 can be made integrally to generate microseismic activity, so that reducing barrel glues pot phenomenon.
The bladed body 29 perpendicular to barrel is fixed on 11 inner wall of cylinder, the bladed body 29 is axial along cylinder 11
Arrangement, 29 front end of bladed body are sharp sword, have gap between 11 inner wall of sharp sword and cylinder.Bladed body 29 along the circumferential direction can be set
It is multiple, it is along the circumferential direction uniformly distributed.The device at work, the direction of rotation of cylinder 11 and the direction of rotation of shaft 3 on the contrary, to
The sharp sword of bladed body 29, with the rotation of cylinder, can be pyrolyzed under the substance shovel for gluing pot on barrel spiral helicine in cylinder
Substance can be raised by bladed body 29, be sufficiently pyrolyzed.
The Three-section type heating non-stick pan oily sludge pyrolysis installation at work, by feeding device 13 by object to be pyrolyzed
Material is sent into pyrolysis chamber 9, drives material impelling sheet 5 to rotate by the rotation of shaft 3, so that material is fed forward.Pass through three
Gas inlet inputs high-temperature flue gas into heating chamber 8, and the flue-gas temperature of three gas inlet inputs is different, so that wherein the first heat
Temperature≤350 DEG C in section I are solved, II temperature of the second pyrolysis section is 350~550 DEG C, and III temperature of third pyrolysis section is 550~750
℃.Due to cylinder 11 partition when so that an only transmission heat between heating chamber 8 and pyrolysis chamber 9, does not mix mutually between medium.With
This is different according to medium to be pyrolyzed simultaneously, injects different medical fluids from different injection devices 20 to pyrolysis chamber, such as has and urge
Change and stores the medical fluid of (putting) heat function, for blocking the lightweight liquid, organic for cracking macromolecular for being pyrolyzed side heating surface impurities accumulation
The chain-breaker of object strand, destabiliser for promoting macromolecular chain organic matter fast pyrogenation etc., with the rotation of shaft 3, this
A little medical fluids, to external comprehensive sprinkling, promote the pyrolysis of medium by spray head 28.During medium pyrolysis, bladed body 29
Material can be raised, in conjunction with the shock effect of microseism device 24, to greatly reduce the viscous pots such as coking, knot carbon, fouling
It happens.
The scope of application of the Three-section type heating non-stick pan oily sludge pyrolysis installation: one, it is suitable for oil field or petrochemical field
Oil sludge, ageing oil in tank in the drilling well dreg liquid being related to, oil field or all kinds of stations of petrochemical industry, in pond after dredging, underground work
The oil sludge that well site generates, the oil sludge that pipeline leakage generates, oil sludge that land vehicle-mounted, marine boat-carrying oil tank generates etc. are harmless
Change, recycling, minimizing processing.Two, the front-end processing suitable for the oil shale of rich in oil, oil-sand refining process, can be by it
In solid harmless treatment, by the water of generation, incoagulable gas removing and resource utilization, the oil of remaining purity is high is to refining
Process is without adverse effect.Three, various used oil, waste lubricating oil, useless cooling oil, kitchen waste oil is harmless and recycling treatment.Four, each
Kind of solid organic matters: such as waste plastics, scrap rubber take that braided fabric is innoxious and recycling treatment.Five, containing the life of organic matter
Rubbish etc. is innoxious and recycling treatment.
The Three-section type heating non-stick pan oily sludge pyrolysis installation will not generate pollution outlet compared with washing equipment
Object, without the normal safe operation secondary pollution for having an impact other process flows.Compared with incineration method, two evils will not be generated
The pernicious gases such as English can be run to safety economy, and investment reduction saves operating cost, and has recycling output.With it is existing often
Rule pyrolysis oven compare, will not coking, the insecurity factors such as local heating's swelling and cracking, short processing time, running cost will not be generated
With low.And can continuous, safety, economy, it is closed, environmentally friendly run, since feed needs are not harsh, before capable of saving when building a station
The investment of the equipment such as end sorting.Due to energy continuous operation, the investment such as pond, tank of material storing has been saved.Have after equipment processing
Four kinds of innoxious and recycling outputs: the first is the powdery solid containing organic matter < 0.2%, can legal outlet and
It can resource utilization；Second is light liquids, mainly oily, can resource utilization；The third is heavy liquid, mainly
Water, contained oil < 10ppm, suspended matter < 10ppm, and salinity are lower than 100mg/l, Ca2++Mg2+< 2mg/l, can be legal outer
Row, and can resource utilization；4th kind is incoagulability imflammable gas, can be used as fuel use.
Claims (6)
1. a kind of Three-section type heating non-stick pan oily sludge pyrolysis installation, including cylinder (11), it is equipped with and turns at cylinder (11) center
Axis (3), it is characterised in that: spiral helicine material impelling sheet (5) is fixed with outside the shaft (3), the cylinder (11) is external
The protection walls (10) of annular space are fixed with, form heating chamber (8) between cylinder (11) and protection walls (10), protection walls (10) bottom
Portion is opened there are three gas inlet, and top is provided with smoke outlet (7).
2. Three-section type heating non-stick pan oily sludge pyrolysis installation according to claim 1, it is characterised in that: the cylinder
(11) external to be equipped with several injection devices (20), injection device (20) is equipped with injection pipe (21), and the injection pipe (21) is even
It connects delivery pipe (22), several delivery branch pipes (23) is connected in delivery pipe (22), delivery branch pipe (23) end is fixed with spray head
(28)。
3. Three-section type heating non-stick pan oily sludge pyrolysis installation according to claim 2, it is characterised in that: the cylinder
(11) rotating electric machine (25) and microseism device (24) are connected separately on outer wall.
4. Three-section type heating non-stick pan oily sludge pyrolysis installation according to claim 3, it is characterised in that: the cylinder
(11) the bladed body (29) perpendicular to barrel is fixed on inner wall, the bladed body (29) is axially arranged along cylinder (11), and sword
There is gap between shape body (29) front end and cylinder (11) inner wall.
5. Three-section type heating non-stick pan oily sludge pyrolysis installation according to claim 4, it is characterised in that: the material
One end of impelling sheet (5) is connected with feeding device (13), and charging lock gas dress is equipped between feeding device (13) and cylinder (11)
It sets (12), one end top opposite with feeding device (13) is fixed with gas vent (4) on the cylinder (11), and lower end is fixed with out
Expects pipe (15).
6. Three-section type heating non-stick pan oily sludge pyrolysis installation according to claim 5, it is characterised in that: the discharging
It manages (15) upper end and is equipped with discharging air-lock device (16), discharge nozzle (15) side is connected with bulky grain release pipe (19), discharge nozzle
(15) lower end is connected with out screening separator (17), and screening separator (17) bottom is provided with solid powder outlet (18) out.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201910130204.XA CN109678307A (en) | 2019-02-21 | 2019-02-21 | A kind of Three-section type heating non-stick pan oily sludge pyrolysis installation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910130204.XA CN109678307A (en) | 2019-02-21 | 2019-02-21 | A kind of Three-section type heating non-stick pan oily sludge pyrolysis installation |
Publications (1)
| Publication Number | Publication Date |
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| CN109678307A true CN109678307A (en) | 2019-04-26 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114873899A (en) * | 2022-07-12 | 2022-08-09 | 四川君和环保股份有限公司 | Feeding device and oil-based rock debris treatment system adopting same |
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