CN107760352A - A kind of anaerobic low temperature pyrolyzer technical equipment - Google Patents
A kind of anaerobic low temperature pyrolyzer technical equipment Download PDFInfo
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- CN107760352A CN107760352A CN201711303578.4A CN201711303578A CN107760352A CN 107760352 A CN107760352 A CN 107760352A CN 201711303578 A CN201711303578 A CN 201711303578A CN 107760352 A CN107760352 A CN 107760352A
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- pipeline
- cracking reaction
- low temperature
- reaction stove
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention discloses a kind of anaerobic low temperature pyrolyzer technical equipment of low temperature pyrolyzer technical field,Including cracking reaction stove,The cracking reaction stove includes body of heater,The intracavity bottom of the body of heater is provided with three groups of cracking gas burners and three groups of neat gas burners,Gas burner is cracked described in three groups and three groups of neat gas burners are alternately installed,The right side of the cracking reaction stove is connected with feeding mechanism by pipeline,The feeding mechanism includes transmission cylinder,The left end of the transmission cylinder is connected with the charging aperture of cracking reaction stove,Material pushing box is connected with the right side of the transmission cylinder,The top connection charge door of the material pushing box,The inner chamber of the material pushing box is provided with guide pad,The right side wall of the material pushing box has been connected by screw hydraulic cylinder,The anaerobic low temperature pyrolyzer technical equipment,Globality is preferable,Improve oil gas lysis efficiency,Increase the structural strength between structure,Pass through the control to discharge gas,Reduce the influence to environment.
Description
Technical field
The present invention relates to low temperature pyrolyzer technical field, specially a kind of anaerobic low temperature pyrolyzer technical equipment.
Background technology
In petrochemical production process, commonly usePetroleum fractionatingProduct（Including oil gas）Make raw material, using than cracking more
High temperature（700~800 DEG C, sometimes even up to more than 1000 DEG C）, make to haveLong-chainThe breakdown of hydrocarbon of molecule is into variousShort chain
Gaseous hydrocarbon and a small amount of liquid hydrocarbon, to provide Organic Chemicals.This method is industrially called oilCracking.Thus
Cracking is exactly drastic cracking, to obtain short chainUnsaturated hydrocarbonsFor the petroleum refining process of main component, it isChemical change, it is original
Cracking apparatus can produce substantial amounts of waste gas, and air is caused to have a strong impact on, globality is inadequate, influences overall processing efficiency, therefore,
We have proposed a kind of anaerobic low temperature pyrolyzer technical equipment.
The content of the invention
It is an object of the invention to provide a kind of anaerobic low temperature pyrolyzer technical equipment, to solve to propose in above-mentioned background technology
Original cracking apparatus can produce substantial amounts of waste gas, air is caused to have a strong impact on, globality is inadequate, influence overall processing effect
The problem of rate.
To achieve the above object, the present invention provides following technical scheme：A kind of anaerobic low temperature pyrolyzer technical equipment, including split
Solve reacting furnace, the cracking reaction stove includes body of heater, the intracavity bottom of the body of heater be provided with three groups of cracking gas burners with
Three groups of neat gas burners, crack gas burner described in three groups and three groups of neat gas burners are alternately installed, and the cracking is anti-
The right side of stove is answered to be connected with feeding mechanism by pipeline, the feeding mechanism includes transmission cylinder, the left end of the transmission cylinder
It is connected with the charging aperture of cracking reaction stove, material pushing box, the top connection of the material pushing box is connected with the right side of the transmission cylinder
Charge door, the inner chamber of the material pushing box are provided with guide pad, and the right side wall of the material pushing box has been connected by screw hydraulic cylinder, institute
State the output end of hydraulic cylinder and the right side wall of guide pad connects, the top right side of the cracking reaction stove is connected with breast by pipeline
Change machine, the lower right side of the cracking reaction stove are connected with scraper type slag extractor structure, the bottom of the cracking reaction stove by pipeline
Atomisation tower is connected with by pipeline, the bottom of the atomisation tower is connected with industrial waste gas purifying equipment, the cracking by pipeline
The pipeline that passes on left of reacting furnace is connected with a point gas bag, and the bottom for dividing gas bag is connected with Residual Oil Tank by pipeline, described point
The left side wall of gas bag is connected with cooling system by pipeline, and the cooling system includes cooling tube, the cooling tube upper right side
Entrance is connected with big collector, and the exit of the cooling tube lower right side is connected with small collector, the big collector with it is small
The bottom of collector is mounted on temperature detector, and the cooling system is arranged on the top of spray system, the spray system
Including pond, the left side wall in the pond is connected with water pump by pipeline, and the pipeline that passes on left of the water pump is connected with spray
Pipe, the shower are horizontally installed on the upside of cooling tube, and the right wall in the pond is provided with support, the shower, big receipts
Storage and small collector are fixed by support, and the pipeline that passes on left of the small collector is connected with tank for gaseous or liquid substances.
Preferably, the radius of the transmission cylinder is 1200mm.
Preferably, it is described divide forcing press and thermometer are installed on gas bag.
Preferably, it is described to divide gas bag to be heat-insulated point of gas bag of vacuum double.
Preferably, water seal flame-retardant device is installed on the tank for gaseous or liquid substances.
Compared with prior art, the beneficial effects of the invention are as follows：The anaerobic low temperature pyrolyzer technical equipment, globality is preferable,
Oil gas lysis efficiency is improved, increases the structural strength between structure, by the control to discharge gas, reduces the shadow to environment
Ring.
Brief description of the drawings
Fig. 1 is schematic structural view of the invention；
Fig. 2 is the sectional view of cracking reaction stove of the present invention；
Fig. 3 is the sectional view of feeding mechanism of the present invention；
The upward view that Fig. 4 is connected between cooling system of the present invention and spray system.
In figure：1 cracking reaction stove, 11 bodies of heater, 12 cracking gas burners, 13 neat gas burners, 2 feeding mechanisms, 21
Transmit cylinder, 22 material pushing boxes, 23 charge doors, 24 hydraulic cylinders, 25 guide pads, 3 mulsers, 4 scraper type slag extractor structures, 5 atomisation towers,
6 industrial waste gas purifying equipment, 7 points of gas bags, 8 Residual Oil Tanks, 9 cooling systems, 91 cooling tubes, 92 big collectors, 93 small collectors, 94
Temperature detector, 10 spray systems, 101 ponds, 102 water pumps, 103 showers, 104 supports, 11 tank for gaseous or liquid substances.
Embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation describes, it is clear that described embodiment is only part of the embodiment of the present invention, rather than whole embodiments.It is based on
Embodiment in the present invention, those of ordinary skill in the art are obtained every other under the premise of creative work is not made
Embodiment, belong to the scope of protection of the invention.
Fig. 1-4 are referred to, the present invention provides a kind of technical scheme：A kind of anaerobic low temperature pyrolyzer technical equipment, including cracking
Reacting furnace 1, cracking reaction stove 1 include body of heater 11, and the intracavity bottom of body of heater 11 is provided with three groups of cracking gas burners 12 and three
Group neat gas burner 13, three groups of cracking gas burners 12 and three groups of neat gas burners 13 are alternately installed, cracking reaction stove 1
Right side feeding mechanism 2 is connected with by pipeline, feeding mechanism 2 includes transmission cylinder 21, transmits left end and the cracking of cylinder 21
The charging aperture connection of reacting furnace 1, the right side of transmission cylinder 21 are connected with material pushing box 22, the top connection charge door of material pushing box 22
23, the inner chamber of material pushing box 22 is provided with guide pad 25, and the right side wall of material pushing box 22 has been connected by screw hydraulic cylinder 24, hydraulic cylinder
24 output end is connected with the right side wall of guide pad 25, and the top right side of cracking reaction stove 1 is connected with mulser 3 by pipeline,
The lower right side of cracking reaction stove 1 is connected with scraper type slag extractor structure 4 by pipeline, and the bottom of cracking reaction stove 1 is connected by pipeline
Atomisation tower 5 is connected to, the bottom of atomisation tower 5 is connected with industrial waste gas purifying equipment 6 by pipeline, and the left side of cracking reaction stove 1 leads to
Piping is connected with point gas bag 7, divides the bottom of gas bag 7 to be connected with Residual Oil Tank 8 by pipeline, divides the left side wall of gas bag 7 to pass through pipe
Road is connected with cooling system 9, and cooling system 9 includes cooling tube 91, and the entrance of the upper right side of cooling tube 91 is connected with big collector
92, the exit of the lower right side of cooling tube 91 is connected with small collector 93, and the bottom of big collector 92 and small collector 93 is respectively mounted
There is temperature detector 94, cooling system 9 is arranged on the top of spray system 10, and spray system 10 includes pond 101, pond 101
Left side wall water pump 102 is connected with by pipeline, the pipeline that passes on left of water pump 102 is connected with shower 103, shower 103
It is horizontally installed on the upside of cooling tube 91, the right wall in pond 101 is provided with support 104, shower 103, big collector 92 and small
Collector 93 is fixed by support 104, and the pipeline that passes on left of small collector 93 is connected with tank for gaseous or liquid substances 11.
Wherein, the radius for transmitting cylinder 21 is 1200mm, divides on gas bag 7 and is provided with forcing press and thermometer, divides the gas bag 7 to be
Heat-insulated point of gas bag of vacuum double, water seal flame-retardant device is installed on tank for gaseous or liquid substances 11.
During use：Feeding mechanism 2 is the machine for being specifically used to promote fritter organic hazardous waste, passes through hydraulic drive former material
Material enters reacting furnace to realize automatic feed, feeding mechanism 2 can quick feeding, charging capacity is big, is be easily moved, and organizes installation and dismantling
Unload, split the raw material fallen out of charge door 23 by transmitting cylinder 21 and importing by way of hydraulic cylinder 24 promotes guide pad 25
Solve in reacting furnace 1, cracking reaction stove 1 uses Dual welding technology and automatic welding machine, is welded, and cracks gas burner 12
It is that one kind realizes clean-burning instrument, its performance influences the combustion heating efficiency of stove, therefore can influence energy resource consumption
And environmental protection, neat gas burner 13 use GS20 burners, meet 90/396/EEC standards, using NE676 standards, it is complete
The heating condition needed during cracking reaction is met entirely, major function is heavy oil separation, while high-temperature oil gas will be by dividing gas bag 7
And enter cooling system 9, so it needs Sealing Technology and the air temperature and air pressure monitoring of high standard, divide on gas bag 7 that installs to have one
Individual forcing press, a thermometer, they can monitor temperature and pressure in real time, understand production process, and Residual Oil Tank 8 is placed in a point gas
By bag 7, connected by pipeline, Residual Oil Tank 8, which is not less than, divides gas bag 7 to avoid any combustible from occurring, not entail dangers to oil storage tank, waste
Crack cause：Because dividing gas bag 7 of a relatively high, the heavier part of oil gas can not rise it is too high, so walking downwards；On the other hand,
Impurity is assembled herein, does not interfere with the quality of following oil product, and residual oil can be sent back to cracking reaction stove 1 and carry out secondary fissure again
Solution, because may be complete without cracking.By cracking again, still can obtain some oil, can put it into mulser 3, oil and
Water can not be fused, but can be stirred for into cream colored fuel by mulser 3, and they are sent into heating system to heat cracking
It uses natural water evaporation principle for reacting furnace 1, cooling system 9 and spray system 10, and the water in pond 101 can be pressed into top
In shower 103, allow water to fall naturally, parcel cooling, 91, water can form calabash shaped, while water cooling, can also by air and
Air cooling influences, and has temperature detector 94 on big collector 92 and small collector 93, and first shows access into temperature, second
Show that exhaust temperature, oil gas can be liquefied as oil after entering spraying cooling and be collected by tank for gaseous or liquid substances 11, oil will but be as cold as normal temperature, will not
It is burned, and the time that oil pressure is entered to final tank for gaseous or liquid substances 11 can be reduced, product oil can be collected in this tank for gaseous or liquid substances 11,
In its side, there is liquid level meter to see oil mass, tank for gaseous or liquid substances 11 is the oil yield of temporary transient oil tank, capacity and raw material
Match somebody with somebody, oil is preferably pumped into final oil tank after the end of the product run, in order to next round processing, whole low temperature oxygen-free cracking production
All it is under conditions of atmospheric pressure either tiny structure, is gravity by the power that oil brings tank for gaseous or liquid substances 11 into, liquid utilizes toward lower stream
This activity pattern of liquid, the energy can be saved, ensure safety, atomisation tower 5 is specially designed to carry out cracked gas discharge
, it effectively removes sulphur and dust in fuel gas.
Although an embodiment of the present invention has been shown and described, for the ordinary skill in the art, can be with
A variety of changes, modification can be carried out to these embodiments, replace without departing from the principles and spirit of the present invention by understanding
And modification, the scope of the present invention is defined by the appended.
Claims (5)
1. a kind of anaerobic low temperature pyrolyzer technical equipment, including cracking reaction stove（1）, it is characterised in that：The cracking reaction stove（1）
Including body of heater（11）, the body of heater（11）Intracavity bottom three groups of cracking gas burners are installed（12）Fired with three groups of natural gases
Burner（13）, gas burner is cracked described in three groups（12）With three groups of neat gas burners（13）Alternately install, the cracking is anti-
Answer stove（1）Right side feeding mechanism is connected with by pipeline（2）, the feeding mechanism（2）Including transmitting cylinder（21）, the biography
Defeated cylinder（21）Left end and cracking reaction stove（1）Charging aperture connection, the transmission cylinder（21）Right side be connected with pusher
Case（22）, the material pushing box（22）Top connection charge door（23）, the material pushing box（22）Inner chamber be provided with guide pad
（25）, the material pushing box（22）Right side wall be connected by screw hydraulic cylinder（24）, the hydraulic cylinder（24）Output end with
Guide pad（25）Right side wall connection, the cracking reaction stove（1）Top right side mulser is connected with by pipeline（3）, institute
State cracking reaction stove（1）Lower right side scraper type slag extractor structure is connected with by pipeline（4）, the cracking reaction stove（1）Bottom
Portion is connected with atomisation tower by pipeline（5）, the atomisation tower（5）Bottom industrial waste gas purifying equipment is connected with by pipeline
（6）, the cracking reaction stove（1）The pipeline that passes on left be connected with a point gas bag（7）, it is described to divide gas bag（7）Bottom pass through pipe
Road is connected with Residual Oil Tank（8）, it is described to divide gas bag（7）Left side wall cooling system is connected with by pipeline（9）, the cooling system
（9）Including cooling tube（91）, the cooling tube（91）The entrance of upper right side is connected with big collector（92）, the cooling tube
（91）The exit of lower right side is connected with small collector（93）, the big collector（92）With small collector（93）Bottom pacify
Equipped with temperature detector（94）, the cooling system（9）Installed in spray system（10）Top, the spray system（10）Bag
Include pond（101）, the pond（101）Left side wall water pump is connected with by pipeline（102）, the water pump（102）Left side
Shower is connected with by pipeline（103）, the shower（103）It is horizontally installed on cooling tube（91）Upside, the pond
（101）Right wall support is installed（104）, the shower（103）, big collector（92）With small collector（93）Pass through support
（104）It is fixed, the small collector（93）The pipeline that passes on left be connected with tank for gaseous or liquid substances（11）.
A kind of 2. anaerobic low temperature pyrolyzer technical equipment according to claim 1, it is characterised in that：The transmission cylinder（21）
Radius be 1200mm.
A kind of 3. anaerobic low temperature pyrolyzer technical equipment according to claim 1, it is characterised in that：Described point of gas bag（7）On
Forcing press and thermometer are installed.
A kind of 4. anaerobic low temperature pyrolyzer technical equipment according to claim 1, it is characterised in that：Described point of gas bag（7）For
Heat-insulated point of gas bag of vacuum double.
A kind of 5. anaerobic low temperature pyrolyzer technical equipment according to claim 1, it is characterised in that：The tank for gaseous or liquid substances（11）On
Water seal flame-retardant device is installed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711303578.4A CN107760352A (en) | 2017-12-11 | 2017-12-11 | A kind of anaerobic low temperature pyrolyzer technical equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711303578.4A CN107760352A (en) | 2017-12-11 | 2017-12-11 | A kind of anaerobic low temperature pyrolyzer technical equipment |
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| Publication Number | Publication Date |
|---|---|
| CN107760352A true CN107760352A (en) | 2018-03-06 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711303578.4A Withdrawn CN107760352A (en) | 2017-12-11 | 2017-12-11 | A kind of anaerobic low temperature pyrolyzer technical equipment |
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| Country | Link |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109504403A (en) * | 2018-09-14 | 2019-03-22 | 广州叶林环保科技有限公司 | A kind of organic solid dangerous waste anaerobic carbonization treatment process |
-
2017
- 2017-12-11 CN CN201711303578.4A patent/CN107760352A/en not_active Withdrawn
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109504403A (en) * | 2018-09-14 | 2019-03-22 | 广州叶林环保科技有限公司 | A kind of organic solid dangerous waste anaerobic carbonization treatment process |
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Application publication date: 20180306 |