CN207944062U - Industrial continuous oil sludge pyrolysis device - Google Patents

Industrial continuous oil sludge pyrolysis device Download PDF

Info

Publication number
CN207944062U
CN207944062U CN201721598710.4U CN201721598710U CN207944062U CN 207944062 U CN207944062 U CN 207944062U CN 201721598710 U CN201721598710 U CN 201721598710U CN 207944062 U CN207944062 U CN 207944062U
Authority
CN
China
Prior art keywords
transmission chain
chain belt
pyrolysis
pyrolysis furnace
oil sludge
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
CN201721598710.4U
Other languages
Chinese (zh)
Inventor
蒲文忠
陈明晟
蒲曼
庞计锁
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.)
Mianyang Youpu Energy Technology Co Ltd
Original Assignee
Mianyang Youpu Energy 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 Mianyang Youpu Energy Technology Co Ltd filed Critical Mianyang Youpu Energy Technology Co Ltd
Priority to CN201721598710.4U priority Critical patent/CN207944062U/en
Application granted granted Critical
Publication of CN207944062U publication Critical patent/CN207944062U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Treatment Of Sludge (AREA)

Abstract

The utility model discloses industrial continuous oil sludge pyrolysis devices, belong to disposal of oily sludge field.Including pyrolysis furnace and heating cabinet, heating cabinet is arranged on the outside of pyrolysis furnace, includes overall height warm area or low-temperature space high-temperature region inside pyrolysis furnace;Transmission chain belt is equipped in pyrolysis furnace, transmission chain belt multi-layer intercrossed can be distributed, and the end of transmission chain belt is discharge port, and discharge port is connected with one end of rotation seal joint, and the other end of rotation seal joint is connected with cooling cylinder.Transmission chain belt vertically interlaced distribution in the present apparatus, increases residence time of the oily sludge in pyrolysis furnace, keeps pyrolysis more abundant;Device length is shortened, equipment volume is reduced, saves equipment investment.The rate of transmission chain belt is adjusted using AC frequency conversion stepless time adjustment motor, is effectively controlled pyrolysis rate and residence time, is accurately controlled the granularity and aridity of tailings.

Description

Industrial continuous oil sludge pyrolysis device
Technical field
The utility model is related to greasy filth, oil-sand, greasy dirt process fields, and in particular to a kind of oil sludge continuous pyrolysis dress It sets.
Background technology
About 30,000,000 tons of the yield of the annual oily sludge in China, and its processing mode is predominantly burned and landfill, however Both processing modes can not accomplish the harmless treatment of requirement.Dioxin is easy tod produce in burning process containing sludge, And dioxin is carcinogenic gaseous matter, influences air, causes secondary pollution, while both conventional process modes are of high cost.And Oily sludge pyrolytic technique is to solve the effective ways of oil in oily sludge.After temperature is heated up, moisture first evaporates, then again Temperature is increased, light oil volatilization, mink cell focus is then cracked into the volatilization of small molecule light oil and collects, and then removes the moisture in greasy filth And oil, obtained dry matter then can direct emission, avoid secondary pollution.The existing equipment master for oily sludge pyrolysis If heated by rotating, energy consumption is big;Occupation area of equipment is big, and manufacturing cost is high;It cannot the good grain for controlling tailings discharging Degree, and greasy filth coking is generated in processing procedure, keep pyrolysis insufficient, equipment cleaning is difficult.
Utility model content
To solve the above-mentioned problems, the utility model proposes a kind of oil sludge continuous pyrolysis device, pass through Multi-layer belt type Transmission saves pyrolysis furnace and rotates energy consumption, while reducing equipment volume, reduces equipment cost, accurately controls tailings granularity and drying Degree reduces secondary pollution.
To achieve the goals above, the utility model is achieved through the following technical solutions:
A kind of industrial continuous oil sludge pyrolysis device, including pyrolysis furnace and heating cabinet, the heating cabinet setting are being split The arbitrary side on the outside of stove or a few sides are solved, the pyrolysis furnace front is equipped with feed inlet, includes overall height warm area inside the pyrolysis furnace Or low-temperature space-high-temperature region;Transmission chain belt is equipped in the pyrolysis furnace, the end of the transmission chain belt is discharge port, the discharging Mouth is connected with one end of rotation seal joint, and the other end of the rotation seal joint is connected with cooling cylinder;
Transmission chain belt is equipped in the overall height warm area, the transmission chain belt includes at least two layers, it is every layer described between biography Send chain belt vertically interlaced distribution;
The low-temperature space of the low-temperature space-high-temperature region is adjacent with feed inlet, and transmission is equipped between the low-temperature space-high-temperature region Chain belt is equipped with thermal insulation board between the low-temperature space and high-temperature region, the transmission chain belt of the low-temperature space includes feed end and discharge end; The transmission chain belt of the feed end and discharge end is at least one layer, between every layer of feed end and the transmission chain belt of discharge end Vertically interlaced distribution;The transmission chain belt of the high-temperature region is at least two layers, and the transmission chain belt of the high-temperature region exists High-temperature region vertically interlaced distribution;
The burner for the furnace body heating to pyrolysis furnace is equipped in the heating cabinet, the burner connects with fuel input unit It connects.
Further, the feed inlet includes feeding-in solid body mouth, semifluid feed inlet.
Further, oil gas vent and dust-extraction unit are equipped at the top of the pyrolysis furnace.Oil gas is mainly that light oil and water steam Gas, out after oil gas by condense by water-oil separation, obtained oil product can utilize again.Dust-extraction unit is mainly wet dust removal Device reduces the dust in pyrolysis furnace.
Further, the furnace body of the pyrolysis furnace be rectangle, circle and it is tubular in any one.But it is several to be not limited only to this Kind, the shape of furnace body can be selected and designed according to specific actual conditions.
Further, the cracking furnace bottom is equipped with scraper plate.Scraper plate is mainly used for scraping the clout in transmission chain belt Go out, strengthening device operation.
Further, the low-temperature space-high-temperature region includes low-temperature space and high-temperature region;The burner is arranged in the overall height In warm area or the heating cabinet of high-temperature region.
Further, including control device and transfer motion power device, the control device and transfer motion power device electricity Even;The transfer motion power device is connect with transmission chain belt.
Further, the front end of the feeding-in solid body mouth is connected with the solid conveyor belt for conveying solid substance.
Further, the front end of the semifluid feed inlet is connected with for conveying viscid fluid delivery pump.
Further, the transfer motion power device includes motor, retarder, driving wheel and tensioning wheel, the retarder point It is not connect with driving wheel and motor;The motor is AC frequency conversion stepless time adjustment motor;The tensioning wheel is arranged on driving wheel, The transmission chain belt is arranged between the driving wheel and tensioning wheel.
The industrial continuous oil sludge pyrolysis device of the utility model, advantage are:
(1) transmission and the cracking for carrying out solid or half dry solid by transmission chain belt inside pyrolysis furnace, avoid because of stove Body rotates and increased energy consumption.It is transmitted and is cracked using transmission chain belt, it is more energy saving.
(2) the vertically interlaced distribution of the transmission chain belt in pyrolysis furnace, increases oily sludge in pyrolysis furnace In residence time, keep pyrolysis more abundant;
(3) the vertically interlaced distribution of the transmission chain belt in pyrolysis furnace shortens device length, reduces equipment Volume saves equipment investment.
(4) it uses AC frequency conversion stepless time adjustment motor to adjust the rate of transmission chain belt, effectively controls pyrolysis rate and stop Time accurately controls the granularity and aridity of tailings.
(5) in the pyrolysis furnace with low-temperature space-high-temperature region, high-temperature region is equipped with burner, and burner is not arranged for low-temperature space, high The material of warm area is directly entered low-temperature space after coming out, and since low-temperature space is adjacent with feed inlet, the material waste heat that high-temperature region comes out can The raw material of low-temperature space after feed inlet is heated, thermal energy is made full use of.The setting of burner can be reduced, while saving energy consumption. Sludge is contained using pyrolysis, heavy oil conversion therein is collected for light oil, does not generate atmosphere pollution, is recycled, It is environmentally protective.
Description of the drawings
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only It is some embodiments of the utility model, for those of ordinary skill in the art, before not making the creative labor property It puts, other drawings may also be obtained based on these drawings.
Fig. 1 is the structural schematic diagram that pyrolysis furnace is overall height warm area in the utility model;
Fig. 2 is the structural schematic diagram that pyrolysis furnace is low-temperature space-high-temperature region in the utility model and low-temperature space is two layers;
Fig. 3 is the structural schematic diagram that pyrolysis furnace is low-temperature space-high-temperature region in the utility model and low-temperature space is multilayer;
1- pyrolysis furnaces, 2- heating cabinets, 3- transmission chain belts, 4- overall height warm areas, 5- low-temperature spaces, the high-temperature regions 6-, 7- discharge ports, 8- Rotation seal joint, 9- cooling cylinders, 10- burners, 11- feeding-in solid bodies mouth, 12- semifluid feed inlets, 13- oil gas vents, 14- are solid Body conveyer belt, 15- fluid delivery pumps, 16- scraper plates, 17- dust-extraction units, 18- thermal insulation boards.
Specific implementation mode
The utility model is further described with reference to specific embodiment and attached drawing.
Embodiment 1
A kind of industrial continuous oil sludge pyrolysis device as shown in Figure 1, include pyrolysis furnace 1 and heating cabinet 2, can be according to need It asks and heating cabinet is arranged in the either side in the outside of pyrolysis furnace or both sides or three sides or four sides.And adding in the present embodiment For the setting of hot storehouse 2 in the downside of pyrolysis furnace 1,1 front of pyrolysis furnace is equipped with feed inlet, feed inlet include feeding-in solid body mouth 11, semifluid into Material mouth 12 can be directly transported when raw material is solid by solid conveyor belt 14;When raw material is viscid, at this time may be used Conveying charging is carried out to raw material with fluid delivery pump 15.1 inside of pyrolysis furnace includes overall height warm area 4;Conveyer chain is equipped in pyrolysis furnace 1 The end of band 3, transmission chain belt 3 is discharge port 7, and discharge port 7 is connected with one end of rotation seal joint 8, rotation seal joint 8 The other end is connected with cooling cylinder 9;Transmission chain belt 3 is equipped in overall height warm area 4, transmission chain belt 3 is including between at least two layers, every layer The vertically interlaced distribution of transmission chain belt 3;The burner 10 for the furnace body heating to pyrolysis furnace 1 is equipped in heating cabinet 2, Burner 10 is connect with combustion gas input unit.Fuel may include coal gas, coal gas, natural gas and fuel oil etc., and according to different Fuel, burner 10 carry out matched change.The furnace body of pyrolysis furnace 1 be rectangle, circle and it is tubular in any one, but not only It is limited to these types, the shape of furnace body can be selected and designed according to specific actual conditions.1 top of pyrolysis furnace goes out equipped with oil gas Mouth 13 and dust-extraction unit 17.Oil gas is mainly light oil and vapor, out after oil gas by condensing water-oil separation, obtain Oil product can utilize again.The bottom of pyrolysis furnace 1 is equipped with scraper plate 16, and scraper plate 16 is mainly disposed to close to the place of discharge port 7, just It is struck off in the tailing on the transmission chain band at discharge port 7, ensures equipment trouble-free operation.
And the utility model mainly uses control device and transfer motion power device, control device for the control of transmission chain band It is electrically connected with transfer motion power device;Transfer motion power device includes AC frequency conversion stepless time adjustment motor, retarder, driving wheel and tensioning Wheel, retarder are connect with driving wheel and motor respectively;Tensioning wheel is arranged on driving wheel, and transmission chain belt 3 is arranged in the active Between wheel and tensioning wheel, driving wheel rotation, and drive transmission chain band to be moved by frictional force.And control device can be controlled directly The frequency of AC frequency conversion stepless time adjustment motor processed then controls the rotating speed of retarder and driving wheel, reaches control raw material and is cracking Operating rate in stove 1 ensures the granularity and aridity of tailings.
Embodiment 2
A kind of industrial continuous oil sludge pyrolysis device is as shown in Figures 2 and 3, including pyrolysis furnace 1 and heating cabinet 2, can Heating cabinet is arranged in the either side in the outside of pyrolysis furnace or both sides or three sides or four sides according to demand.And the present embodiment In the setting of heating cabinet 2 in the downside of pyrolysis furnace 1,1 front of pyrolysis furnace is equipped with feed inlet, and feed inlet includes feeding-in solid body mouth 11, half Fluid feed mouth 12 can be directly transported when raw material is solid by solid conveyor belt 14;When raw material is viscid, Conveying charging can be carried out to raw material with fluid delivery pump 15 at this time.1 inside of pyrolysis furnace includes low-temperature space-high-temperature region;In pyrolysis furnace 1 Equipped with transmission chain belt 3, the end of transmission chain belt 3 is discharge port 7, and discharge port 7 is connected with one end of rotation seal joint 8, is rotated The other end of seal nipple 8 is connected with cooling cylinder 9;Low-temperature space 5 is adjacent with feed inlet, and biography is equipped between low-temperature space-high-temperature region Chain belt 3 is sent, thermal insulation board 18 is equipped between low-temperature space 5 and high-temperature region 6, the transmission chain belt 3 of low-temperature space 5 includes feed end and discharging End;The transmission chain belt 3 of feed end and discharge end is at least one layer, edge between every layer of feed end and the transmission chain belt 3 of discharge end The interlaced distribution of vertical direction;The transmission chain belt 3 of high-temperature region 6 is at least two layers, and the transmission chain belt 3 of high-temperature region 6 is in high-temperature region 6 Vertically interlaced distribution;The burner 10 for the furnace body heating to pyrolysis furnace 1 is equipped in heating cabinet 2, burner 10 is led It is set in the lower section of high-temperature region 6, burner 10 is connect with combustion gas input unit.Fuel may include coal gas, coal gas, natural gas and Fuel oil etc., and according to different fuel, burner 10 carries out matched change.The furnace body of pyrolysis furnace 1 is rectangle, circle and pipe Any one in shape, but it is not limited only to these types, the shape of furnace body can be selected and designed according to specific actual conditions. 1 top of pyrolysis furnace is equipped with oil gas vent 13 and dust-extraction unit 17.Oil gas is mainly light oil and vapor, out after oil gas it is logical Condensation is crossed by water-oil separation, obtained oil product can utilize again.The bottom of pyrolysis furnace 1 is equipped with scraper plate 16, and scraper plate 16 is mainly arranged Close to the place of discharge port 7, convenient for being struck off to the tailing on the transmission chain band at discharge port 7, ensure that equipment is smoothly transported Row.
And the utility model mainly uses control device and transfer motion power device, control device for the control of transmission chain band It is electrically connected with the transfer motion power device;Transfer motion power device includes AC frequency conversion stepless time adjustment motor, retarder, driving wheel and opens Bearing up pulley, retarder are connect with driving wheel and motor respectively;Tensioning wheel is arranged on driving wheel, and transmission chain belt 3 is arranged in the master Between driving wheel and tensioning wheel, driving wheel rotation, and drive transmission chain band to be moved by frictional force.And control device can be direct The frequency of AC frequency conversion stepless time adjustment motor is controlled, the rotating speed of retarder and driving wheel is then controlled, reaches control raw material and is splitting The operating rate in stove 1 is solved, ensures the granularity and aridity of tailings.
The technical solution provided above the utility model embodiment is described in detail, used herein specifically A example is expounded the principle and embodiment of the utility model embodiment, and the explanation of above example is only applicable to help Assistant solves the principle of the utility model embodiment;Meanwhile for those of ordinary skill in the art, implementing according to the utility model Example, the there will be changes in specific implementation mode and application range, in conclusion the content of the present specification should not be construed as Limitations of the present invention.

Claims (10)

1. a kind of industrial continuous oil sludge pyrolysis device, it is characterised in that:Including pyrolysis furnace and heating cabinet, the heating cabinet The arbitrary side or a few sides being arranged on the outside of pyrolysis furnace, the pyrolysis furnace front are equipped with feed inlet, include inside the pyrolysis furnace Overall height warm area or low-temperature space-high-temperature region;Transmission chain belt is equipped in the pyrolysis furnace, the end of the transmission chain belt is discharge port, The discharge port is connected with one end of rotation seal joint, and the other end of the rotation seal joint is connected with cooling cylinder;
Transmission chain belt is equipped in the overall height warm area, the transmission chain belt includes at least two layers, it is every layer described between conveyer chain Band vertically interlaced distribution;
The low-temperature space of the low-temperature space-high-temperature region is adjacent with feed inlet, and conveyer chain is equipped between the low-temperature space-high-temperature region Band is equipped with thermal insulation board between the low-temperature space and high-temperature region, the transmission chain belt of the low-temperature space includes feed end and discharge end;Institute The transmission chain belt for stating feed end and discharge end is at least one layer, edge between every layer of feed end and the transmission chain belt of discharge end The interlaced distribution of vertical direction;The transmission chain belt of the high-temperature region is at least two layers, and the transmission chain belt of the high-temperature region is in height Warm area vertically interlaced distribution;
The burner for the furnace body heating to pyrolysis furnace is equipped in the heating cabinet, the burner is connect with fuel input unit.
2. industrial continuous oil sludge pyrolysis device according to claim 1, it is characterised in that:The feed inlet includes solid Body feed inlet, semifluid feed inlet.
3. industrial continuous oil sludge pyrolysis device according to claim 1, it is characterised in that:It is set at the top of the pyrolysis furnace There are oil gas vent and dust-extraction unit.
4. industrial continuous oil sludge pyrolysis device according to claim 1, it is characterised in that:The furnace body of the pyrolysis furnace For rectangle, circle and it is tubular in any one.
5. industrial continuous oil sludge pyrolysis device according to claim 1, it is characterised in that:The cracking furnace bottom is set There is scraper plate.
6. industrial continuous oil sludge pyrolysis device according to claim 1, it is characterised in that:Low-temperature space-the high temperature Area includes low-temperature space and high-temperature region;The burner is arranged in the heating cabinet of the overall height warm area or high-temperature region.
7. industrial continuous oil sludge pyrolysis device according to claim 1, it is characterised in that:Including control device and biography Dynamic power plant, the control device are electrically connected with the transfer motion power device;The transfer motion power device is connect with transmission chain belt.
8. industrial continuous oil sludge pyrolysis device according to claim 2, it is characterised in that:The feeding-in solid body mouth Front end is connected with the solid conveyor belt for conveying solid substance.
9. industrial continuous oil sludge pyrolysis device according to claim 2, it is characterised in that:The semifluid feed inlet Front end be connected with for conveying viscid fluid delivery pump.
10. industrial continuous oil sludge pyrolysis device according to claim 7, it is characterised in that:The transfer motion power dress It sets including motor, retarder, driving wheel and tensioning wheel, the retarder is connect with driving wheel and motor respectively;The motor is AC frequency conversion stepless time adjustment motor;The tensioning wheel is arranged on driving wheel, the transmission chain belt setting in the driving wheel and Between tensioning wheel.
CN201721598710.4U 2017-11-20 2017-11-20 Industrial continuous oil sludge pyrolysis device Active CN207944062U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721598710.4U CN207944062U (en) 2017-11-20 2017-11-20 Industrial continuous oil sludge pyrolysis device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721598710.4U CN207944062U (en) 2017-11-20 2017-11-20 Industrial continuous oil sludge pyrolysis device

Publications (1)

Publication Number Publication Date
CN207944062U true CN207944062U (en) 2018-10-09

Family

ID=63703620

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721598710.4U Active CN207944062U (en) 2017-11-20 2017-11-20 Industrial continuous oil sludge pyrolysis device

Country Status (1)

Country Link
CN (1) CN207944062U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019096019A1 (en) * 2017-11-20 2019-05-23 绵阳油普能源科技有限责任公司 Industrial continuous oily sludge thermal decomposition equipment

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019096019A1 (en) * 2017-11-20 2019-05-23 绵阳油普能源科技有限责任公司 Industrial continuous oily sludge thermal decomposition equipment
CN109810718A (en) * 2017-11-20 2019-05-28 绵阳油普能源科技有限责任公司 Industrial continuous oil sludge pyrolysis device

Similar Documents

Publication Publication Date Title
CN201010609Y (en) Belt type sludge stirring multilevel secondary steam recycling and drying device
CN104628237B (en) Sludge drying incineration system based on thermal power plant
CN108101335A (en) A kind of oily sludge continuous processing technique and processing unit
CN102311215B (en) Urban life sludge locally self-circulation comprehensive utilization device and method
CN105737167B (en) Heat accumulating type rotating bed segmentation utilizes the method and system of carbonaceous organic material thermal decomposition product
CN206289157U (en) A kind of oily sludge carbonization treatment apparatus
WO2020029654A1 (en) Harmless intelligent oil sludge pyrolysis treatment apparatus and treatment method
CN109179939A (en) A kind of process for treating oil-containing sludge and device
CN104017594A (en) Low-temperature dry distillation method of coal
CN102643703A (en) Novel external heating type lignite pyrolysis quality increasing system and process
CN205635485U (en) Developments serialization is coproduction gas carbon oil device useless admittedly organically
CN108787694B (en) High-efficiency energy-saving oil-containing material treatment equipment
CN105157399B (en) The segmentation dehydration drying system of high humidity coal and using method thereof
CN106746462A (en) A kind of oily sludge carbonization treatment apparatus
CN206843308U (en) A kind of low-power consumption sludge drying device
CN207944062U (en) Industrial continuous oil sludge pyrolysis device
CN106673395A (en) Oily sludge carbonization treatment and heat recovery device and method
CN100592014C (en) Waste drying method and its system device
CN109810718A (en) Industrial continuous oil sludge pyrolysis device
CN207646040U (en) Industrial continuous oil sludge thermally decomposes skid mounted equipment
CN202532903U (en) Pyrite acid making slag discharge heat recovery equipment system
CN106838916A (en) Integrated flammable solid discarded object dry thermal cracking kettle
CN207646039U (en) Electrothermic industry serialization oil sludge thermally decomposes skid mounted equipment
CN205633898U (en) Chain scraper mechanism of serialization domestic waste combustible substance production fuel oil device
CN109337696A (en) Rotary carbonizing furnace

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant