CN208390637U - A kind of energy-efficient oil-containing equipment for treating materials - Google Patents
A kind of energy-efficient oil-containing equipment for treating materials Download PDFInfo
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- CN208390637U CN208390637U CN201820512021.5U CN201820512021U CN208390637U CN 208390637 U CN208390637 U CN 208390637U CN 201820512021 U CN201820512021 U CN 201820512021U CN 208390637 U CN208390637 U CN 208390637U
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- energy
- cooling
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- 239000000463 material Substances 0.000 title claims abstract description 80
- 238000004064 recycling Methods 0.000 claims abstract description 51
- 238000001816 cooling Methods 0.000 claims abstract description 47
- 238000000197 pyrolysis Methods 0.000 claims abstract description 47
- 239000007789 gas Substances 0.000 claims abstract description 37
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 30
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 26
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 15
- 238000003860 storage Methods 0.000 claims abstract description 13
- 238000007084 catalytic combustion reaction Methods 0.000 claims abstract description 11
- 238000006555 catalytic reaction Methods 0.000 claims abstract description 11
- 238000009833 condensation Methods 0.000 claims abstract description 4
- 230000005494 condensation Effects 0.000 claims abstract description 4
- 238000001704 evaporation Methods 0.000 claims abstract 2
- 238000012546 transfer Methods 0.000 claims description 13
- 238000010438 heat treatment Methods 0.000 claims description 10
- 238000005086 pumping Methods 0.000 claims description 8
- 239000000498 cooling water Substances 0.000 claims description 7
- 238000009413 insulation Methods 0.000 claims description 6
- 230000007246 mechanism Effects 0.000 claims description 4
- 230000005540 biological transmission Effects 0.000 claims description 2
- 238000002485 combustion reaction Methods 0.000 claims 1
- 235000019628 coolness Nutrition 0.000 claims 1
- 238000012545 processing Methods 0.000 abstract description 8
- 230000000694 effects Effects 0.000 abstract description 5
- 239000010802 sludge Substances 0.000 abstract description 4
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 239000003921 oil Substances 0.000 description 73
- 238000000034 method Methods 0.000 description 12
- 239000010410 layer Substances 0.000 description 6
- 230000008569 process Effects 0.000 description 5
- 230000008901 benefit Effects 0.000 description 3
- 239000003054 catalyst Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000004939 coking Methods 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 2
- 239000012774 insulation material Substances 0.000 description 2
- 239000011229 interlayer Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- 239000005995 Aluminium silicate Substances 0.000 description 1
- 229910000975 Carbon steel Inorganic materials 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- PZZYQPZGQPZBDN-UHFFFAOYSA-N aluminium silicate Chemical compound O=[Al]O[Si](=O)O[Al]=O PZZYQPZGQPZBDN-UHFFFAOYSA-N 0.000 description 1
- 229910000323 aluminium silicate Inorganic materials 0.000 description 1
- 235000012211 aluminium silicate Nutrition 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000037237 body shape Effects 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 239000010962 carbon steel Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 210000002268 wool Anatomy 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/20—Waste processing or separation
Landscapes
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The utility model discloses a kind of energy-efficient oil-containing equipment for treating materials, including horizontal thermal energy recycling pyrolysis oven, nitrogen generation device, catalytic combustion system, oil storage tank and the oil water separator for evaporating vapour cooling unit, the fixed gas that burns；The thermal energy, which recycles, is equipped with calandria, heat-energy recycling system and upper and lower arranged for interval upper conveyor belt and lower conveyor belt in pyrolysis oven.If upper and lower two conveyer belt, the material of two conveyer belts can be carried out heat exchange, slips vapour and generate oil slick and fixed gas after cooling condensation, thermal energy is reused after fixed gas catalysis burning, oil slick is through water-oil separating at oil, on the one hand, reduces energy consumption, avoid pollution environment, energy recycling is used again, on the other hand, solves the conveying of oil-containing material, therefore it can have the following technical effects: reduce operation cost, have huge social and economic significance for processing oily sludge.
Description
Technical field
The utility model relates to a kind of Environmental-protecting treater more particularly to a kind of energy-efficient oil-containing equipment for treating materials.
Background technique
Exploitation of oil-gas field can generate a large amount of oil-containing materials (such as oil patch and oily sludge), which can be serious dirty
Environment is contaminated, therefore harmless treatment must be carried out.The method of processing oil-containing material has very much, and various methods have respective advantage and disadvantage.Mesh
Before, mostly use national oil recommended industry standard SY/T7300-2016 " at land oil natural gas extraction disposal of oily sludge greatly
Set and pollution control technology specification " in the pyrolytic technique method introduced of 7.1.3.Pyrolytic technique is as the innoxious place of oil-containing material
Reason technology, comparative maturity and perfect, also gets the nod in the disposition of numerous oil fields, but because of pyrolytic process specified conditions, make
There are following deficiencies for pyrolysis plant:
First is that pyrolytic process maximum temperature is more than 500 degrees Celsius, oil-containing material is caused to be easy to produce in pyrolysis reactor furnace
Coking and sintering effect.The coking and sinter are easy to attach in reacting furnace, are difficult to clean up removal, this will be greatly reduced equipment
Production efficiency can also greatly improve maintenance of equipment expense, furthermore, which is difficult after temperature-rise period or pyrolytic reaction defeated
It send and is conveyed and moved on device, cause many difficulties for the continuous pyrolysis of the oil-containing material.
Second is that pyrolytic process maximum temperature is more than 500 degrees Celsius, causes material after processing also to keep higher temperature, contain
More thermal energy directly excludes that cooling treatment must be carried out.It contains the heating energy consumption that thermal energy is equal to the pyrolysis processing oil-containing material, directly
Run in put and extremely waste, if can recycle will substantially reduce processing oil-containing material operation cost.
Utility model content
The utility model provides a kind of energy-efficient oil-containing equipment for treating materials, and which overcome oil contents in background technique
Expect deficiency present in processing equipment.
The technical solution adopted by the utility model to solve the technical problem is that:
A kind of energy-efficient oil-containing equipment for treating materials including horizontal thermal energy recycling pyrolysis oven, nitrogen generation device, evaporates
Catalytic combustion system, oil storage tank and the oil water separator of vapour cooling unit, the fixed gas that burns；
The thermal energy recycle pyrolysis oven in be equipped with calandria, heat-energy recycling system and upper and lower arranged for interval upper conveyor belt and under
Conveyer belt, set at the top of thermal energy recycling pyrolysis oven it is inside and outside it is perforative slip vapor outlet, thermal energy recycling pyrolysis oven front side wall sets opening,
The upper conveyor belt front end and lower conveyor belt front end are respectively material input and material outlet, and the upper conveyor belt conveying direction is certainly
After going to and lower conveyor belt conveying direction after forward, the rear end of the lower conveyor belt is stretched out after upper conveyor belt rear end so as to upload
Send the material taken that can fall on lower conveyor belt from rear end, the material on the material and lower conveyor belt on upper conveyor belt carries out heat
Exchange；
The nitrogen generation device connects thermal energy recycling pyrolysis oven and provides nitrogen can recycle pyrolysis oven to thermal energy；
This evaporates the connection of vapour cooling unit and slips vapor outlet will slip vapour and be divided into oil slick and fixed gas through being cooled into；The oil storage
Tank connection evaporates vapour cooling unit to collect oil slick, which connects oil storage tank to separate oil slick into oil and water；The catalysis
Burner connection evaporates vapour cooling unit to be catalyzed burning fixed gas, which connects heat-energy recycling system with benefit
The material in energy heats thermal energy recycling pyrolysis oven is generated with burning.
Among one embodiment: thermal energy recycling pyrolysis oven includes the insulating layer of furnace shell and connection furnace shell；Thermal energy recycling heat
It solves in furnace and is equipped between front and back arrangement and the temperature warm area that temperature is arranged from low to high from front to back, adjacent warm area equipped with multiple
What material and lower conveyor belt for upper conveyor belt and thereon and material thereon passed through passes through mouth.
Among one embodiment: setting transfer roller and two lower transfer rollers, the upper conveyor belt solderless wrapped connection two on two in thermal energy recycling pyrolysis oven
Upper transfer roller, the lower transfer roller of the lower conveyor belt solderless wrapped connection two；Thermal insulation portion is designed between every adjacent two warm area in thermal energy recycling pyrolysis oven
Point, the thermal insulation part include the first thermal insulative board being located in upper conveyor belt, the second thermal insulative board being located in lower conveyor belt and between
Third thermal insulative board between upper conveyor belt and lower conveyor belt.
Among one embodiment: the calandria includes multiple heating tubes, and multiple heating tube is arranged in upper conveyor belt.
Among one embodiment: the heat-energy recycling system includes heat-dissipating pipe, which is arranged in thermal energy recycling pyrolysis oven
Bottom wall, the heat-dissipating pipe connect catalytic combustion system.
Among one embodiment: further including feeding part, splicing container and lifting device, on the feeding part and splicing container
Lower to arrange and respectively correspond material input and material outlet, which connects feeding part to convey oil-containing material
To feeding part.
Among one embodiment: further including temperature control unit and temperature sensor, which is located at thermal energy recycling
Pyrolysis oven roof, the temperature control unit signal connect temperature sensor and calandria.
Among one embodiment: further including extractor fan, extractor fan connection slips vapor outlet and slips vapour to extract out.
Among one embodiment: each warm area, which is equipped, slips vapor outlet；This evaporates vapour cooling unit
And it is provided with the cooling drainer of cooling water, which condenses pot bottom and is equipped with air inlet, is equipped with outlet at the top of cooling drainer
Mouthful, cooling condensation pot sidewall offers the oil pumping mouth of the corresponding cooling water water surface；Multiple cooling drainer air inlets and multiple warm areas
The vapor outlet that slips correspond and connect, the gas outlet of multiple cooling drainers all connects catalytic combustion system, which passes through
The mechanism that pumps connects oil pumping mouth.
Among one embodiment: it further include water treatment facilities, which connects cooling drainer and oil water separator,
Cooling drainer is supplied to handle water and recycle.
The technical program compared with the background art, it has the following advantages:
If upper and lower two conveyer belt, the material of two conveyer belts can be carried out heat exchange, slip vapour generated after cooling condensation oil slick and
Fixed gas, thermal energy is reused after fixed gas catalysis burning, and oil slick is through water-oil separating at oil, on the one hand, reduces energy consumption, avoids dirt
Environment is contaminated, energy recycling is used again, on the other hand, is solved the conveying of oil-containing material, therefore can have the following technical effects: being reduced
Operation cost has a huge social and economic significance for processing oily sludge.
Detailed description of the invention
The utility model is described in further detail with reference to the accompanying drawings and detailed description.
Fig. 1 is the structural schematic diagram of the energy-efficient oil-containing equipment for treating materials of present embodiment.
Fig. 2 is the structural schematic diagram of the thermal energy recycling pyrolysis oven of present embodiment.
Specific embodiment
A kind of energy-efficient oil-containing equipment for treating materials, please refers to Fig. 1 and Fig. 2, recycles pyrolysis oven including horizontal thermal energy
10, feeding part, splicing container 20, lifting device, nitrogen generation device 30, evaporate vapour cooling unit 40, burning fixed gas is urged
Change burner 50, oil storage tank 60, oil water separator 70 and water treatment facilities 80.
It includes furnace shell and the insulating layer for connecting furnace shell that the thermal energy, which recycles pyrolysis oven 10,；In specific structure: thermal energy recycling pyrolysis
Furnace 10 is rectangle cavity furnace shell, and furnace shell has furnace shell outer wall and furnace shell inner wall, is formed between the furnace shell outer wall and furnace shell inner wall
Interlayer sets insulating layer in interlayer；The furnace shell outer wall such as uses ordinary carbon steel, and furnace shell inner wall such as uses high-temperature steel, high temperature resistant silicon
Sour aluminium or refractory brick marshalling are constructed, and the thermal insulation material that insulating layer uses such as uses the aluminium silicate wool insulation board of fire resisting, moreover,
The selection of thermal insulation material and thickness should be lower than 50 with the refractory heat-insulating thermal requirements suitable for 900 degrees Celsius, furnace shell surface temperature
Degree is to reduce the lost thermal energy in furnace shell surface to the greatest extent.
It is equipped in calandria 11, heat-energy recycling system 12 and upper and lower arranged for interval and transmits in thermal energy recycling pyrolysis oven 10
Band 13 and lower conveyor belt 14, set at the top of thermal energy recycling pyrolysis oven 10 it is inside and outside it is perforative slip vapor outlet 15, thermal energy recycling pyrolysis
10 front side wall of furnace sets opening, and 13 front end of upper conveyor belt and 14 front end of lower conveyor belt are respectively material input and material output
Mouthful, 13 conveying direction of upper conveyor belt after go to and 14 conveying direction of lower conveyor belt after forward, after the lower conveyor belt 14
End stretch out after 13 rear end of upper conveyor belt so that: material conveys after go to through upper conveyor belt 13, the material on upper conveyor belt 13
It can fall in from rear end on lower conveyor belt 14, then be conveyed forward by lower conveyor belt 14 after, the material on upper conveyor belt 13 is under
Material on conveyer belt 14 carries out heat exchange, on the one hand, the material on preheating upper conveyor belt 13, recycling preheating avoid thermal energy from disappearing
Consumption, on the other hand, without cooling discharging material.Wherein: upper conveyor belt is pyrolytic process reacting furnace conveyer belt, cascading conveyors fortune
Scanning frequency degree is calculated according to material handling capacity and exchange rate.In one specific structure: the thermal energy recycles in pyrolysis oven 10
If transfer roller 131 and two lower transfer rollers 141 on two, transfer roller 131 in 13 solderless wrapped connection two of upper conveyor belt, two lower turns of 14 solderless wrapped connection of lower conveyor belt
Roller 141, to drive conveyer belt activity to realize conveying by transfer roller；Transfer roller passes through the decelerating motor transmission shaft outside shaft coupling and furnace shell
Connection.
The thermal energy recycle pyrolysis oven 10 in be equipped with it is multiple along front and back arrangement and temperature temperature is arranged from low to high from front to back
Warm area, the step temperature difference is formed between adjacent warm area, be equipped between adjacent warm area material for upper conveyor belt 13 and thereon and under
What conveyer belt 14 and material thereon passed through passes through mouth.In thermal energy recycling pyrolysis oven 10 per be designed between adjacent two warm area every
Isothermal segment, that is, realized by thermal insulation part and divide warm area, which includes the first thermal insulative board being located in upper conveyor belt 13
161, the second thermal insulative board 162 being located in lower conveyor belt 14 and the third thermal insulation between upper conveyor belt 13 and lower conveyor belt 14
Plate 163 can also set the 4th thermal insulative board 164 as needed between lower conveyor belt and furnace bottom.In specific structure: warm area is with 5 to 10
It is a best, big subregion follow pyrolysis oil and gas disjunction rule be 170 degrees Celsius or less, 170-250 degrees Celsius, 250-350 degrees Celsius,
350-500 degrees Celsius and 500 degrees Celsius or more 5 warm areas；As needed, it is (big that small subregion can be also segmented again in big subregion
Divide multiple small warm areas in warm area again).Rule is exchanged according to the step of temperature recycling, segments the exchange of the more recycling thermal energy of small subregion
Effect is better, and general 50 degree the above are a subregion or small subregion, when maximum temperature is 550 degree, can be divided into 10 subregions.This tool
Among body is implemented: each warm area, which is equipped, slips vapor outlet 15, and the corresponding furnace roof portion of each warm area is arranged to dome knot
Structure.
The calandria 11 includes multiple heating tubes, and multiple 11 uniform intervals of heating tube are arranged in upper conveyor belt 13.It should
Heat-energy recycling system 12 includes heat-dissipating pipe, which is arranged in thermal energy recycling 10 bottom wall of pyrolysis oven.
Material input and material outlet are arranged and respectively corresponded to the feeding part and about 20 splicing container, the promotion
Device connects feeding part so that oil-containing material is delivered to feeding part, and oil-containing material is spread in upper conveyor belt 13 by feeding part
On, the material heated object 11 on upper conveyor belt 13 heats, and, heat exchange (temperature of charge quilt of upper and lower level conveyer belt material
The material on upper layer realizes that heat exchange is recycled by heat radiation and nitrogen free convection) preheating, it is anti-to generate pyrolysis
It answers, slips vapour to generate；It falls on lower conveyor belt 14, is fed forward by lower conveyor belt 14 later, go to front end and overturn nature
Fall into splicing container 20 (such as in material storage tank).
It is as needed: to may also include temperature control unit and temperature sensor, which is located at thermal energy recycling heat
10 roof of furnace is solved, which connects temperature sensor and calandria, to control the heating of calandria 11, temperature control
Unit processed such as PLC.It further include extractor fan, extractor fan connection slips vapor outlet and slips vapour to extract out, slips vapour with raising and goes out gas velocity
Degree, will slip vapour be evacuated to evaporate vapour cooling unit carry out condensing recovery.
The nitrogen generation device 30 connects thermal energy recycling pyrolysis oven 10 and provides nitrogen, the furnace can recycle pyrolysis oven to thermal energy
Nitrogen is full of in inner chamber body, which is micro-positive pressure.The nitrogen production device 30, such as nitrogen is filtered out from air with molecular sieve
Device, which can directly buy from market.The nitrogen, on the one hand, for filling, purging air or space in furnace, make
Anaerobic state is in furnace as far as possible, prevents the oxidation and burning of crude oil, on the other hand, realizes heat exchange for realizing thermal convection,
Improve utilization rate of waste heat.
This evaporates vapour cooling unit 40 and slips vapor outlet 15 by the connection of oil and gas offtake piping system and be divided into that will slip vapour through cooling
The oil slick and fixed gas of formation.Among present embodiment: it includes counting and being provided with warm area etc. that this, which evaporates vapour cooling unit 40,
The cooling drainer of cooling water, the cooling condense pot bottom and are equipped with air inlet, gas outlet are equipped at the top of cooling drainer, cooling is cold
Solidifying pot sidewall offers the oil pumping mouth of the corresponding cooling water water surface；Multiple cooling drainer air inlets and multiple warm areas slip vapor outlet
It corresponds and connects, catalytic combustion system is all connected in the gas outlet of multiple cooling drainers, which is connect by the mechanism that pumps
Logical oil pumping mouth.This slips vapour and enters from cooling drainer bottom, is cooled into oil slick through supercooled water and floats on water surface and accumulate into
Layer, fixed gas are exported from the gas outlet at top, and oil slick is pumped in oil storage tank 60 by oil pumping mechanism to be saved.In specific structure: setting
There are 5 tank bodies, 5 tank bodies accept 170 degree or less oil and gas, 175-250 degree oil and gas, 250-350 degree oil and gas, 350-500 degree respectively
Oil and gas, 500 or more oil and gas.The for example up-narrow and down-wide cone of the tank body shape.
The oil water separator 70 connects oil storage tank 60 to separate oil slick into oil and water, stays the quality for collecting oil to improve, should
Oil water separator 70 such as CN201720538596.X.
The catalytic combustion system 50 connection evaporates vapour cooling unit 40 to be catalyzed burning fixed gas, which connects
The heat-dissipating pipe of heat-energy recycling system 12 is to utilize the material generated in energy heats thermal energy recycling pyrolysis oven 10 that burns.
The catalytic combustion system 50 includes catalysis burning bed and catalysis heater, and fixed gas enters catalysis burning bed and heating
Completely catalysis burning is warming up to after 600 degree under body and catalyst action, and hot gas is recycled through piping dispatch to above-mentioned thermal energy is
The heat-dissipating pipe of system 12 is discharged after carrying out thermal energy recycling.The catalyst of the catalytic combustion system is by the heterogeneity of each oil gas from market
Upper selection, such as metal oxide containing precious metals.
The water treatment facilities 80 connects cooling drainer and oil water separator, is supplied to cooling with harmless processing water and circulation
Drainer, on the one hand, on the other hand pollution caused by prevent water from discharging and saving water resource reduce water consumption.
As needed, it may also include electric-control system, electric-control system is made of power control cabinet and automatic control system, by temperature
Feeding back to control the speed of service and other operating statuses of machine column for degree, is programmed to automation control with PLC.
The workflow of the equipment describes:
Oil-containing material is delivered to 13 entrance of upper conveyor belt via lifting device promotion, and is equably spread in oil-containing material
On upper conveyor belt 13, oil-containing material is evenly transmitted to 10 other end of reacting furnace, calandria in transmit process by upper conveyor belt 13
11 heating, heat-energy recycling system 12 heat, cascading conveyors 13,14 carry out heat exchange, with heat oil-containing material to be pyrolyzed steam
Evaporate reaction；And by each warm area workshop section, and pyrolysis distillation is completed in each workshop section.Overturning nature is fallen on down after being delivered to another end
On conveyer belt 14.The lower conveyor belt goes in the same direction with upper conveyor belt, is sent to low-temperature space by high-temperature region, the high-temperature material respectively according to
It is secondary to pass through high-temperature region, secondary high-temperature region, until low-temperature space.And radiation and advection heat are carried out in the oil-containing material of each warm area and upper conveyor belt
Exchange exchanges the heat of itself by each warm area and is absorbed and utilized.After the oil-containing material heat is utilized by exchange, it is sent to outlet
It holds and overturns and fall into the container 20 (such as storage mud groove) being set under it.The oil and gas that pyrolysis oil-containing material generates then passes through reacting furnace
Top dome Fractional Collections simultaneously pass through the pipeline being disposed thereon to vapour cooling unit 40 is evaporated, after recycling condenses grease, no
Solidifying gas is left to catalytic combustion system 50 through tank group top duct and carries out catalysis burning harmless treatment.Tail gas after catalysis burning contains
Have a large amount of thermal energy (about 600), after tail gas passes through heat-energy recycling system recovery waste heat, discharge, the oil product for condensing collection is drawn
It takes out oil storage tank to be collected and store, and periodically further progress water-oil separating operation is used to improve the oil quality of recycling
Water treatment facilities, which is recycled to, in the cooling water for slipping vapour carries out harmless treatment and recycling after cooling.
The above, only the utility model preferred embodiment, therefore, it cannot be limited according to, and the utility model is implemented
It is practical new to should still belong to this for range, i.e., equivalent changes and modifications made according to the scope of the patent of the utility model and the content of the manual
In the range of type covers.
Claims (10)
1. a kind of energy-efficient oil-containing equipment for treating materials, it is characterised in that:
Including horizontal thermal energy recycling pyrolysis oven, nitrogen generation device, the catalysis burning dress for evaporating vapour cooling unit, the fixed gas that burns
It sets, oil storage tank and oil water separator；
The thermal energy, which recycles, is equipped with calandria, heat-energy recycling system and upper and lower arranged for interval upper conveyor belt and lower transmission in pyrolysis oven
Band, set at the top of thermal energy recycling pyrolysis oven it is inside and outside it is perforative slip vapor outlet, thermal energy recycling pyrolysis oven front side wall sets opening, on this
Conveyor front end and lower conveyor belt front end are respectively material input and material outlet, which goes to certainly
Afterwards and lower conveyor belt conveying direction after forward, the rear end of the lower conveyor belt is stretched out after upper conveyor belt rear end so that upper conveyor belt
On material can be fallen on lower conveyor belt from rear end, material on the material and lower conveyor belt on upper conveyor belt carries out hot friendship
It changes；
The nitrogen generation device connects thermal energy recycling pyrolysis oven and provides nitrogen can recycle pyrolysis oven to thermal energy；
This evaporates the connection of vapour cooling unit and slips vapor outlet will slip vapour and be divided into oil slick and fixed gas through being cooled into；The oil storage tank connects
Logical to evaporate vapour cooling unit to collect oil slick, which connects oil storage tank to separate oil slick into oil and water；Catalysis burning
Device connection evaporates vapour cooling unit to be catalyzed burning fixed gas, which connects heat-energy recycling system to utilize combustion
Burn the material generated in energy heats thermal energy recycling pyrolysis oven.
2. a kind of energy-efficient oil-containing equipment for treating materials according to claim 1, it is characterised in that: thermal energy recycling heat
Solution furnace includes the insulating layer of furnace shell and connection furnace shell；The thermal energy recycle pyrolysis oven in be equipped with it is multiple along front and back arrangement and temperature by preceding
The warm area arranged from low to high to rear temperature, be equipped between adjacent warm area material for upper conveyor belt and thereon and lower conveyor belt and
What material thereon passed through passes through mouth.
3. a kind of energy-efficient oil-containing equipment for treating materials according to claim 2, it is characterised in that: thermal energy recycling heat
Transfer roller and two lower transfer rollers on two, transfer roller in the upper conveyor belt solderless wrapped connection two, the lower transfer roller of the lower conveyor belt solderless wrapped connection two are set in solution furnace；The heat
It can recycle in pyrolysis oven per being designed with thermal insulation part between adjacent two warm area, which includes the be located in upper conveyor belt
One thermal insulative board, the second thermal insulative board being located in lower conveyor belt and the third thermal insulative board between upper conveyor belt and lower conveyor belt.
4. a kind of energy-efficient oil-containing equipment for treating materials according to claim 3, it is characterised in that: the calandria includes
Multiple heating tubes, multiple heating tube are arranged in upper conveyor belt.
5. a kind of energy-efficient oil-containing equipment for treating materials according to claim 1, it is characterised in that: the thermal energy recycles
System includes heat-dissipating pipe, which is arranged in thermal energy recycling pyrolysis furnace hearth wall, which connects catalytic combustion system.
6. a kind of energy-efficient oil-containing equipment for treating materials according to claim 1, it is characterised in that: further include feeder
Divide, splicing container and lifting device, the feeding part and splicing container are arranged up and down and respectively correspond material input and material
Delivery outlet, the lifting device connect feeding part so that oil-containing material is delivered to feeding part.
7. a kind of energy-efficient oil-containing equipment for treating materials according to claim 1, it is characterised in that: further include temperature control
Unit and temperature sensor processed, the temperature sensor are located at thermal energy recycling pyrolysis oven roof, temperature control unit signal connection
Temperature sensor and calandria.
8. a kind of energy-efficient oil-containing equipment for treating materials according to claim 1, it is characterised in that: further include exhausting dress
It sets, extractor fan connection slips vapor outlet and slips vapour to extract out.
9. a kind of energy-efficient oil-containing equipment for treating materials according to claim 2, it is characterised in that: each warm area
It is equipped with and slips vapor outlet；It includes the cooling drainer for counting and being provided with cooling water with warm area etc., the cooling that this, which evaporates vapour cooling unit,
It condenses pot bottom and is equipped with air inlet, gas outlet is equipped at the top of cooling drainer, cooling condensation pot sidewall offers corresponding cooling water
The oil pumping mouth of the water surface；Multiple cooling drainer air inlets are connected with the vapor outlet one-to-one correspondence that slips of multiple warm areas, and multiple coolings are cold
Catalytic combustion system is all connected in the gas outlet of solidifying tank, which connects oil pumping mouth by oil pumping mechanism.
10. a kind of energy-efficient oil-containing equipment for treating materials according to claim 9, it is characterised in that: further include at water
Device is managed, which connects cooling drainer and oil water separator, is supplied to cooling drainer to handle water and recycle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820512021.5U CN208390637U (en) | 2018-04-11 | 2018-04-11 | A kind of energy-efficient oil-containing equipment for treating materials |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820512021.5U CN208390637U (en) | 2018-04-11 | 2018-04-11 | A kind of energy-efficient oil-containing equipment for treating materials |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208390637U true CN208390637U (en) | 2019-01-18 |
Family
ID=65063986
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820512021.5U Withdrawn - After Issue CN208390637U (en) | 2018-04-11 | 2018-04-11 | A kind of energy-efficient oil-containing equipment for treating materials |
Country Status (1)
| Country | Link |
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| CN (1) | CN208390637U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108787694A (en) * | 2018-04-11 | 2018-11-13 | 方明环保科技(漳州)有限公司 | Energy-efficient oil-containing equipment for treating materials |
-
2018
- 2018-04-11 CN CN201820512021.5U patent/CN208390637U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108787694A (en) * | 2018-04-11 | 2018-11-13 | 方明环保科技(漳州)有限公司 | Energy-efficient oil-containing equipment for treating materials |
| CN108787694B (en) * | 2018-04-11 | 2024-02-09 | 方明环保科技(漳州)有限公司 | High-efficiency energy-saving oil-containing material treatment equipment |
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