CN206014633U - A kind of double slurry greasy filth pyrolysis installation - Google Patents
A kind of double slurry greasy filth pyrolysis installation Download PDFInfo
- Publication number
- CN206014633U CN206014633U CN201620932686.2U CN201620932686U CN206014633U CN 206014633 U CN206014633 U CN 206014633U CN 201620932686 U CN201620932686 U CN 201620932686U CN 206014633 U CN206014633 U CN 206014633U
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- helical axis
- greasy filth
- chamber
- casing
- pyrolysis
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- 238000000197 pyrolysis Methods 0.000 title claims abstract description 34
- 238000009434 installation Methods 0.000 title claims abstract description 12
- 239000002002 slurry Substances 0.000 title abstract description 9
- 238000000926 separation method Methods 0.000 claims abstract description 9
- 238000002309 gasification Methods 0.000 claims description 11
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 238000001816 cooling Methods 0.000 claims description 5
- 229910052757 nitrogen Inorganic materials 0.000 claims description 4
- 230000008878 coupling Effects 0.000 claims description 3
- 238000010168 coupling process Methods 0.000 claims description 3
- 238000005859 coupling reaction Methods 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims description 3
- 238000009413 insulation Methods 0.000 claims description 3
- 229920002472 Starch Polymers 0.000 claims 5
- 235000019698 starch Nutrition 0.000 claims 5
- 239000007787 solid Substances 0.000 claims 1
- 238000004821 distillation Methods 0.000 abstract description 7
- 238000005406 washing Methods 0.000 abstract description 3
- 238000010438 heat treatment Methods 0.000 abstract description 2
- 239000002689 soil Substances 0.000 abstract description 2
- 239000003921 oil Substances 0.000 description 21
- 239000010802 sludge Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 239000010779 crude oil Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 102000002322 Egg Proteins Human genes 0.000 description 1
- 108010000912 Egg Proteins Proteins 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- -1 asphalitine Substances 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 239000008394 flocculating agent Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 210000004681 ovum Anatomy 0.000 description 1
- 244000045947 parasite Species 0.000 description 1
- 244000052769 pathogen Species 0.000 description 1
- 230000001717 pathogenic effect Effects 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000002285 radioactive effect Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000007634 remodeling Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Classifications
-
- 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
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Treatment Of Sludge (AREA)
Abstract
The utility model provides a kind of double slurry greasy filth pyrolysis installation, including：Casing, pyrolysis chamber is installed in the casing, pyrolysis is provided with hot blast wall-sandwiched layer on the outside of chamber, two parallel helical axis are provided with the pyrolysis chamber, propeller blade is provided with by cross spiral axle on the outside of helical axis, the propeller blade along helical axis a pitch helical pitch built with 4 blades, the two ends of two helical axis are arranged on casing by the bearing that operates respectively, two helical axis are mutually reversely rotated by the one end near feed pipe on helical axis by meshing gear group, the utility model is using heating distillation principle, in device, make greasy filth temperature reach the end point of distillation, so, oil in greasy filth all gasifies, gas is fully incorporated washing separation device again, reclaim oil.The complete oil-free of the later soil of the end point of distillation is reached, the harmless discharge of greasy filth is reached.
Description
Technical field
The utility model is related to the oil removing field of purification of greasy filth, specially a kind of double slurry greasy filth pyrolysis installation.
Background technology
Oil recovery and oil refining process can produce waste water of the substantial amounts of oil-containing containing mud, the dirt after current oil-sludge treatment technical finesse
Mud oil-containing is typically more than 5%, it is impossible to realize the harmless discharge of mud.First, oil extraction produces oily sludge.Oil extraction
During the oily sludge of middle generation is mainly derived from Ground Processing System, oil recovery treatment.Besides oil field gathering and transportation and storage
Deposit process and produce greasy filth.We be accustomed to sewage from oil refinery is processed in produce oil interceptor bed mud, floation tank scum silica frost, Bottom Plate of Crude Oil Storage
Mud etc. is commonly called as three mud.The constituent of Sludge in Oilfields is extremely complex, is a kind of suspension emulsion system of stabilizer pole, except certainly
Body contains a large amount of aged crude oils, wax, asphalitine, colloid etc., also includes a large amount of flocculating agents, the inhibition added in production process
The water treatment agents such as agent, antisludging agent.Sludge is also containing the difficult drop such as substantial amounts of pathogen, parasite (ovum), heavy metal, radioactive element
The poisonous and harmful substance of solution, this health and natural environment to the mankind are all one and greatly endanger.Therefore Sludge in Oilfields
Dangerous solid waste has been listed in.
Burning needs the pollutant of after-treatment few using calorific value and pyrolysis processing, it may be achieved complete final process, suitably
Scale process, is worth with research and extension, and being wherein pyrolyzed has preferable economic benefit compared with burning, excellent with more preferable market
Gesture.Pyrolytic technique is the means that current foreign countries are widely used in oily sludge harmless treatment, is at a kind of sludge high temperature of remodeling
Science and engineering skill.Greasy filth is heated to uniform temperature under anoxic condition and makes hydro carbons and organic matter desorption, remaining body refuse, hydro carbons after hydrocarbon pyrolysis
Can recycle.Then the useful resources in greasy filth can be reclaimed well, be difficult to form secondary pollution, it is achieved that resource and
Energy is recycled.Simultaneously, because pyrolysis is under middle low-temperature reduction atmosphere, so the life of the harmful substances such as two English is not tended to have
Into, and the raising for being conducive to reclaiming oil quality, it is also beneficial to the static stabilization of heavy metal.
Utility model content
The technical problem solved by the utility model is to provide a kind of double slurry greasy filth pyrolysis installation, to solve the above-mentioned back of the body
The problem proposed in scape technology.
The technical problem solved by the utility model employs the following technical solutions to realize：A kind of double slurry greasy filth pyrolysis dress
Put, including：Casing, is provided with pyrolysis chamber in the casing, pyrolysis is provided with hot blast wall-sandwiched layer, pyrolysis chamber upper end one on the outside of chamber
Side is provided with feed cavity, opposite side and is provided with gasification separation chamber, is connected with feed pipe in the feed cavity, installs on gasification separation chamber
There is air-introduced machine, on the outside of gasification separation chamber, be provided with security window, the pyrolysis chamber is provided with discharging opening, hot blast away from one end of feed pipe
Wall-sandwiched layer one end is provided with air inlet, the other end and is provided with air outlet, is provided with two parallel helical axis, helical axis in the pyrolysis chamber
Outside is provided with propeller blade by cross spiral axle, the propeller blade along helical axis a pitch helical pitch built with
4 blades, the two ends of two helical axis are respectively by operating bearing on casing, near feed pipe on helical axis
One end two helical axis are mutually reversely rotated by meshing gear group, wherein in two helical axis passes through
Shaft coupling is connected to power set.
The power set are installed by fixed seat and are fixed, and fixed seat is installed by fixing bolt and fixed, meshing gear group
By gear train fixed support on casing.
Water cooling plant, operating bearing and 1 junction of casing are installed at the operating bearing that the helical axis is connected with casing
Nitrogen protection device is installed.
The hot blast wall-sandwiched layer be U-shape structure, hot blast wall-sandwiched layer will be pyrolyzed chamber parcel, be provided with insulation on the outside of hot blast wall-sandwiched layer
Layer.
Adpting flange is installed on the air inlet, feed pipe, air outlet.
Compared with prior art, the beneficial effects of the utility model are：The utility model is being filled using heating distillation principle
Make greasy filth temperature reach the end point of distillation in putting, so, the oil in greasy filth all gasifies, then gas be fully incorporated washing to separate dress
Put, reclaim oil.The complete oil-free of the later soil of the end point of distillation is reached, the harmless discharge of greasy filth is reached.Wherein double slurry structure,
During conveying greasy filth, also there are crushing and stirring action to greasy filth group, improve pyrolysis efficiency.
Description of the drawings
Fig. 1 is front view schematic diagram of the present utility model.
Fig. 2 is left view schematic diagram of the present utility model.
Fig. 3 is top view schematic diagram of the present utility model.
Fig. 4 is screw shaft structure schematic diagram of the present utility model.
Fig. 5 is propeller blade structural representation of the present utility model.
Fig. 6 is propeller blade scheme of installation of the present utility model.
Specific embodiment
In order that of the present utility model realize that technological means, creation characteristic, reached purpose and effect are easy to understand, under
Face combines and is specifically illustrating, and the utility model is expanded on further.
As shown in figs. 1 to 6, a kind of double slurry greasy filth pyrolysis installation, including：Casing 1, is provided with pyrolysis in the casing 1
Chamber, is provided with hot blast wall-sandwiched layer 18 on the outside of pyrolysis chamber, pyrolysis chamber upper end side is provided with feed cavity, opposite side and is provided with gasification point
Feed pipe 8 is connected with chamber 10, the feed cavity, air-introduced machine 11 is installed, outside gasification separation chamber 10 on gasification separation chamber 10
Side is provided with security window 9, and the pyrolysis chamber is provided with discharging opening 15 away from one end of feed pipe 8, and 18 one end of hot blast wall-sandwiched layer is provided with
The air inlet 2, other end is provided with air outlet 16, is provided with two parallel helical axis 3, passes through on the outside of helical axis 3 in the pyrolysis chamber
Cross spiral axle 19 is provided with propeller blade 17, the propeller blade 17 along helical axis 3 a pitch helical pitch built with 4
Individual blade, the two ends of two helical axis 3 are respectively by operating bearing on casing 1, near charging on helical axis 3
Two helical axis 3 are mutually reversely rotated by one end of pipe 8 by meshing gear group 4, wherein in two helical axis 3
Root is connected to power set 6 by shaft coupling 7.
The power set 6 are installed by fixed seat 5 and are fixed, and fixed seat 5 is installed by fixing bolt and fixed, meshing gear
Group 4 is by gear train fixed support 12 on casing 1.
Water cooling plant 13 is installed at the operating bearing that the helical axis 3 is connected with casing 1, operating bearing is connected with casing 1
The place of connecing is provided with nitrogen protection device 14.
The hot blast wall-sandwiched layer 18 is U-shape structure, hot blast wall-sandwiched layer 18 will pyrolysis chamber parcel, set on the outside of hot blast wall-sandwiched layer 18
There is heat-insulation layer 20.
Adpting flange is installed on the air inlet 2, feed pipe 8, air outlet 16.
The present invention devises the screw conveying structure of double slurry, and two parallel helical axis are passed by the gear of a pair of meshing
Move and reversely rotate.Blade is installed on helical axis, (i.e. 360 °) 4 oars is housed along helix in the helical pitch of a pitch
Leaf, one left-handed, another dextrorotation.When greasy filth is entered at spiral, the blade of rotation just promotes walk to travel forward, and works as mud
When group is pulled to the centre of two axles, blade continues up rotation, and walk lies on the table, at this moment, an other spiral
Blade insertion walk walk is cut, stir, while walk is advanced 1/4 pitch again.So circulate repeatedly, walk
Thin silt is ground into by cutting progressively and agitation, the hot blast blown in the casing for being designed to double wall is passed heat by double wall
Silt is passed, by adjusting inputiing mud volume and helix speed and intake and EAT can just make silt before separating device
The end point of distillation of contained oil is reached, all oils is all gasified and is left silt.Silt is made to reach oil-free discharge.Gasification
Oil and moisture spray washing device is transported to by the air-introduced machine that device is set up, fast cooling reaches oil and moisture
Condensation point, makes oil and moisture separate with air, reclaims oil and moisture, the air discharge of purification.The retort gas of device is logical
Air-introduced machine conveying is crossed, therefore internal system is negative pressure state, can both make running safer, also reduce evaporating temperature
Degree, more energy-conservation.System is provided with nitrogen protection and security window, provides reliable guarantee for safety in production.In order to protect fortune
The damage from high temperature is held in rotating shaft, and helical axis have also been devised water cooling plant.
Due to the effect of air-introduced machine, device is in negative pressure state.Negative pressure causes device in comparatively safe state, then plus
The security window that upper nitrogen gas seal equipment and device itself are arranged, and warning system, the safe handling of device are protected.Negative pressure
State can also reduce the gasification temperature of oil and water so that the dry condensation point of walk reduces, and realizes energy-saving run.
General principle of the present utility model and principal character and advantage of the present utility model has been shown and described above.One's own profession
The technical staff of industry it should be appreciated that the utility model is not restricted to the described embodiments, described in above-described embodiment and specification
Principle of the present utility model is described simply, on the premise of without departing from the utility model spirit and scope, the utility model is also
Various changes and modifications are had, these changes and improvements are both fallen within the range of claimed the utility model.The utility model
Claimed scope by appending claims and its equivalent thereof.
Claims (5)
1. one kind is double starches greasy filth pyrolysis installation, including：Casing, it is characterised in that：Pyrolysis chamber, pyrolysis are installed in the casing
Hot blast wall-sandwiched layer is provided with the outside of chamber, and pyrolysis chamber upper end side is provided with feed cavity, opposite side and is provided with gasification separation chamber, described
Feed pipe being connected with feed cavity, air-introduced machine being installed on gasification separation chamber, gasification separation is provided with security window on the outside of chamber, the heat
Solution chamber is provided with discharging opening away from one end of feed pipe, and hot blast wall-sandwiched layer one end is provided with air inlet, the other end and is provided with air outlet, institute
State in pyrolysis chamber and be provided with two parallel helical axis, propeller blade is provided with by cross spiral axle on the outside of helical axis, the spiral shell
Rotation blade along helical axis a pitch helical pitch built with 4 blades, the two ends of two helical axis are respectively by fortune
Rotating shaft is held on casing, and two helical axis are mutually done by the one end near feed pipe on helical axis by meshing gear group
Reversely rotate, wherein in two helical axis is connected to power set by shaft coupling.
2. one kind according to claim 1 is double starches greasy filth pyrolysis installation, it is characterised in that：The power set are by solid
Reservation is installed and is fixed, and fixed seat is installed by fixing bolt and fixed, and meshing gear group is arranged on machine by gear train fixed support
On shell.
3. one kind according to claim 1 is double starches greasy filth pyrolysis installation, it is characterised in that：The helical axis is connected with casing
Water cooling plant is installed at the operating bearing for connecing, operating bearing is provided with nitrogen protection device with 1 junction of casing.
4. one kind according to claim 1 is double starches greasy filth pyrolysis installation, it is characterised in that：The hot blast wall-sandwiched layer is U
Type structure, hot blast wall-sandwiched layer will be pyrolyzed chamber parcel, be provided with heat-insulation layer on the outside of hot blast wall-sandwiched layer.
5. one kind according to claim 1 is double starches greasy filth pyrolysis installation, it is characterised in that：The air inlet, feed pipe,
Adpting flange is installed on air outlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620932686.2U CN206014633U (en) | 2016-08-24 | 2016-08-24 | A kind of double slurry greasy filth pyrolysis installation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620932686.2U CN206014633U (en) | 2016-08-24 | 2016-08-24 | A kind of double slurry greasy filth pyrolysis installation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206014633U true CN206014633U (en) | 2017-03-15 |
Family
ID=58252546
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620932686.2U Active CN206014633U (en) | 2016-08-24 | 2016-08-24 | A kind of double slurry greasy filth pyrolysis installation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206014633U (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108929012A (en) * | 2018-08-04 | 2018-12-04 | 盘锦宁泰能源科技有限公司 | The innoxious intelligent oil sludge pyrolysis treatment device of one kind and processing method |
| CN109650691A (en) * | 2019-01-29 | 2019-04-19 | 北京云水浩瑞环境科技有限公司 | The system and method for continuous processing municipal sludge |
| CN110194581A (en) * | 2019-05-31 | 2019-09-03 | 上海恒埠环保科技有限公司 | A kind of safety-type greasy filth resource utilization system |
| CN110194580A (en) * | 2019-05-31 | 2019-09-03 | 上海恒埠环保科技有限公司 | A kind of greasy filth resource utilization system and technique |
| CN110194579A (en) * | 2019-05-31 | 2019-09-03 | 上海恒埠环保科技有限公司 | A kind of energy-saving oil mud resource utilizes system |
| CN110194578A (en) * | 2019-05-31 | 2019-09-03 | 上海恒埠环保科技有限公司 | A kind of efficient greasy filth resource utilization system |
| CN110194582A (en) * | 2019-05-31 | 2019-09-03 | 上海恒埠环保科技有限公司 | A kind of environment-friendly type greasy filth resource utilization system |
-
2016
- 2016-08-24 CN CN201620932686.2U patent/CN206014633U/en active Active
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108929012A (en) * | 2018-08-04 | 2018-12-04 | 盘锦宁泰能源科技有限公司 | The innoxious intelligent oil sludge pyrolysis treatment device of one kind and processing method |
| CN109650691A (en) * | 2019-01-29 | 2019-04-19 | 北京云水浩瑞环境科技有限公司 | The system and method for continuous processing municipal sludge |
| CN110194581A (en) * | 2019-05-31 | 2019-09-03 | 上海恒埠环保科技有限公司 | A kind of safety-type greasy filth resource utilization system |
| CN110194580A (en) * | 2019-05-31 | 2019-09-03 | 上海恒埠环保科技有限公司 | A kind of greasy filth resource utilization system and technique |
| CN110194579A (en) * | 2019-05-31 | 2019-09-03 | 上海恒埠环保科技有限公司 | A kind of energy-saving oil mud resource utilizes system |
| CN110194578A (en) * | 2019-05-31 | 2019-09-03 | 上海恒埠环保科技有限公司 | A kind of efficient greasy filth resource utilization system |
| CN110194582A (en) * | 2019-05-31 | 2019-09-03 | 上海恒埠环保科技有限公司 | A kind of environment-friendly type greasy filth resource utilization system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190401 Address after: Room 1602A-2607, 803 Lane 11, Shuangcheng Road, Baoshan District, Shanghai, 201900 Patentee after: Shanghai Hengbu Environmental Protection Technology Co., Ltd. Address before: 215331 No. 80 Wupu Road, Shengpu Town, Suzhou Industrial Park, Jiangsu Province Patentee before: SUZHOU RUIWEI CENTRIFUGAL SEPARATION TECHNOLOGY CO., LTD. |
|
| TR01 | Transfer of patent right |