CN206014633U - A kind of double slurry greasy filth pyrolysis installation - Google Patents

A kind of double slurry greasy filth pyrolysis installation Download PDF

Info

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
Authority
CN
China
Prior art keywords
helical axis
greasy filth
chamber
casing
pyrolysis
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.)
Active
Application number
CN201620932686.2U
Other languages
Chinese (zh)
Inventor
王亚洲
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shanghai Hengbu Environmental Protection Technology Co., Ltd.
Original Assignee
SUZHOU RUIWEI CENTRIFUGAL SEPARATION TECHNOLOGY Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by SUZHOU RUIWEI CENTRIFUGAL SEPARATION TECHNOLOGY Co Ltd filed Critical SUZHOU RUIWEI CENTRIFUGAL SEPARATION TECHNOLOGY Co Ltd
Priority to CN201620932686.2U priority Critical patent/CN206014633U/en
Application granted granted Critical
Publication of CN206014633U publication Critical patent/CN206014633U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/40Valorisation 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

A kind of double slurry greasy filth pyrolysis installation
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.
CN201620932686.2U 2016-08-24 2016-08-24 A kind of double slurry greasy filth pyrolysis installation Active CN206014633U (en)

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)

* Cited by examiner, † Cited by third party
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
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
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
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

Cited By (7)

* Cited by examiner, † Cited by third party
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
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
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
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

Similar Documents

Publication Publication Date Title
CN206014633U (en) A kind of double slurry greasy filth pyrolysis installation
CN104341081B (en) Greasy filth separates and the method for innocent treatment reclaimed
CN103739175A (en) Method for processing oil sludge
CN104178200B (en) The hot analyzing and processing method of a kind of oil base drilling cuttings
WO2020052109A1 (en) Rotational flow rotation deoiling method and device for oil-based mud rock debris
CN204571890U (en) Discarded oil-base mud is with brill treating apparatus
CN107117787A (en) A kind of process of oily sludge addition microalgae biomass collaboration pyrolysis
CN103539325A (en) Processing method and system for sludge containing oil
CN105399294A (en) Recycling and harmless treating process for oily sludge and sand
CN104438297A (en) Method and device for treating organic refuse
CN104787993B (en) Oil sludge sand three-phase separation treatment method
CN101250421A (en) Method for extracting hydrocarbon oil from oil sand and oil shales and special equipment therefor
CN108105790A (en) Oily sludge glows processing unit
CN207271789U (en) A kind of oil-containing solid waste microwave thermal desorbs recycling treatment system
CN203295333U (en) External heated sludge carbonizing kiln
CN203382621U (en) Resourceful treatment system of oily sludge
CN207738704U (en) Equipment is desorbed in a kind of electromagnetic heating sea oil-containing, hydrocarbon contamination castoff heat
CN212713185U (en) Oil-based detritus processing apparatus
CN203360242U (en) Oil sludge treatment system
CN211367360U (en) High-liquid-content oil sludge cracking treatment device
CN204874404U (en) Ternary an organic whole processing system useless admittedly and integrative heating furnace of ternary
CN206736169U (en) A kind of energy-efficient indirect thermal desorption carbonizing apparatus
CN105000782A (en) Plate-type vaporizing drying system and technology for treating oily sludge
CN104745155A (en) Recycling and harmless treatment process of waste oil-based drilling fluid
CN115011369A (en) Thermal desorption treatment method for oil-based detritus mud

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