CN207552252U - 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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- CN207552252U CN207552252U CN201721702984.3U CN201721702984U CN207552252U CN 207552252 U CN207552252 U CN 207552252U CN 201721702984 U CN201721702984 U CN 201721702984U CN 207552252 U CN207552252 U CN 207552252U
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Abstract
The utility model 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 furnace body,The intracavity bottom of the furnace body is equipped 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 connect with the feed inlet of cracking reaction stove,Material pushing box is connected on the right side of the transmission cylinder,The top connection charge door of the material pushing box,The inner cavity 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 utility model is related 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 1000 DEG C or more）, 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 hydrocarbonsPetroleum refining process as main component isChemical change, it is original
Cracking apparatus can generate a large amount of exhaust gas, and air is caused to seriously affect, and globality is inadequate, influences overall processing efficiency, for this purpose,
We have proposed a kind of anaerobic low temperature pyrolyzer technical equipment.
Utility model content
The purpose of this utility model is to provide a kind of anaerobic low temperature pyrolyzer technical equipment, to solve in above-mentioned background technology
The original cracking apparatus proposed can generate a large amount of exhaust gas, and air is caused to seriously affect, and globality is inadequate, influence whole add
The problem of work efficiency rate.
To achieve the above object, the utility model provides following technical solution：A kind of anaerobic low temperature pyrolyzer technical equipment, packet
Cracking reaction stove is included, the cracking reaction stove includes furnace body, and the intracavity bottom of the furnace body is equipped with three groups of cracking fuel gas burings
Device and three groups of neat gas burners, crack gas burner described in three groups and three groups of neat gas burners are alternately installed, described to split
The right side for solving reacting furnace is connected with feeding mechanism by pipeline, and the feeding mechanism includes transmission cylinder, the transmission cylinder
Left end is connect with the feed inlet of cracking reaction stove, and material pushing box, the top of the material pushing box are connected on the right side of the transmission cylinder
Charge door is connected, the inner cavity of the material pushing box is provided with guide pad, and the right side wall of the material pushing box has been connected by screw hydraulic pressure
Cylinder, the output terminal of the hydraulic cylinder and the right side wall of guide pad connect, and the top right side of the cracking reaction stove is connected by pipeline
Mulser is connected to, the lower right side of the cracking reaction stove is connected with scraper type slag extractor structure, the cracking reaction stove by pipeline
Bottom atomisation tower is connected with by pipeline, the bottom of the atomisation tower is connected with industrial waste gas purifying equipment, institute by pipeline
The pipeline that passes on left for stating cracking reaction stove is connected with a point gas bag, and the bottom for dividing gas bag is connected with Residual Oil Tank by pipeline,
The left side wall of described point of gas bag is connected with cooling system by pipeline, and the cooling system includes cooling tube, and the cooling tube is right
The entrance of upside is connected with big collector, and the exit of the cooling tube lower right side is connected with small collector, the big collection
The bottom of device and small collector is mounted on temperature detector, and the cooling system is mounted on the top of spray system, the spray
Leaching system includes pond, and the left side wall in the pond is connected with water pump by pipeline, and the water pump passes on left pipeline connection
There is spray tube, the spray tube is horizontally installed on the upside of cooling tube, and the right wall in the pond is equipped with stent, the spray
Pipe, big collector and small collector are fixed by the bracket, 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 that gas bag is divided 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 utility model are：The anaerobic low temperature pyrolyzer technical equipment, globality compared with
It is good, oil gas lysis efficiency is improved, increases the structural strength between structure, by the control to discharge gas, reduces to environment
It influences.
Description of the drawings
FIG. 1 is a schematic structural view of the utility model；
Fig. 2 is the sectional view of the utility model cracking reaction stove；
Fig. 3 is the sectional view of the utility model feeding mechanism；
The bottom view that Fig. 4 is connected between the utility model cooling system and spray system.
In figure：1 cracking reaction stove, 11 furnace bodies, 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 spray tubes, 104 stents, 11 tank for gaseous or liquid substances.
Specific embodiment
The following is a combination of the drawings in the embodiments of the present utility model, and the technical scheme in the embodiment of the utility model is carried out
It clearly and completely describes, it is clear that the described embodiments are only a part of the embodiments of the utility model rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are without making creative work
All other embodiments obtained shall fall within the protection scope of the present invention.
- 4 are please referred to Fig.1, the utility model provides a kind of technical solution：A kind of anaerobic low temperature pyrolyzer technical equipment, including
Cracking reaction stove 1, cracking reaction stove 1 include furnace body 11, and the intracavity bottom of furnace body 11 is equipped with three groups of cracking gas burners 12
With three groups of neat gas burners 13, three groups of cracking gas burners 12 and three groups of neat gas burners 13 are alternately installed, and cracking is anti-
The right side of stove 1 is answered to be connected with feeding mechanism 2 by pipeline, feeding mechanism 2 includes transmission cylinder 21, transmit the left end of cylinder 21 with
The feed inlet connection of cracking reaction stove 1, the right side of transmission cylinder 21 are connected with material pushing box 22, the top connection charging of material pushing box 22
Mouth 23, the inner cavity 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 pressure
The output terminal of cylinder 24 is connect with the right side wall of guide pad 25, and the top right side of cracking reaction stove 1 is connected with mulser by pipeline
3, 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 passes through pipeline
Atomisation tower 5 is connected with, the bottom of atomisation tower 5 is connected with industrial waste gas purifying equipment 6, the left side of cracking reaction stove 1 by pipeline
Point gas bag 7 is connected with by pipeline, the bottom of gas bag 7 is divided to be connected with Residual Oil Tank 8 by pipeline, the left side wall of gas bag 7 is divided to pass through
Pipeline is connected with cooling system 9, and cooling system 9 includes cooling tube 91, and the entrance of 91 upper right side of cooling tube is connected with big collection
Device 92, the exit of 91 lower right side of cooling tube are connected with small collector 93, and the bottom of big collector 92 and small collector 93 is pacified
Equipped with temperature detector 94, cooling system 9 is mounted on the top of spray system 10, and spray system 10 includes pond 101, pond
101 left side wall is connected with water pump 102 by pipeline, and the pipeline that passes on left of water pump 102 is connected with spray tube 103, spray tube
103 are horizontally installed on the upside of cooling tube 91, and the right wall in pond 101 is equipped with stent 104, spray tube 103,92 and of big collector
Small collector 93 is fixed by stent 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 of transmission cylinder 21 divides on gas bag 7 and is equipped with forcing press and thermometer for 1200mm, divides the gas bag 7 to be
Heat-insulated point of gas bag of vacuum double is equipped with water seal flame-retardant device 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 realizes automatic feed into reacting furnace, feeding mechanism 2 can quick feeding, charging capacity is big, is be easily moved, and organizes installation and dismantling
It unloads, splits the raw material fallen out of charge door 23 by transmitting the importing of cylinder 21 in a manner that hydraulic cylinder 24 pushes guide pad 25
It solves 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 a kind of clean-burning tool of realization, its performance influences the combustion heating efficiency of stove, therefore can influence energy 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 the sealing technique of high standard and air temperature and air pressure monitoring, divide that is installed on gas bag 7 to have one
A 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
It by packet 7, is connected by pipeline, Residual Oil Tank 8, which is not less than, divides gas bag 7 to occur to avoid any combustible, not entail dangers to oil storage tank, waste
Crack cause：Because dividing gas bag 7 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 cannot fuse, but can be stirred for into cream colored fuel by mulser 3, they are sent into heating system to heat cracking
Reacting furnace 1, cooling system 9 and spray system 10 it using natural water evaporation principle, the water in pond 101 can be pressed into top
In spray tube 103, water is allowed to fall naturally, package 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 exhaust temperature, oil gas can be liquefied as oil after entering spraying cooling and be collected by tank for gaseous or liquid substances 11, and oil will but be as cold as room temperature, will not
It being 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 that can see oil mass, tank for gaseous or liquid substances 11 is the oil yield of temporary oil tank, capacity and raw material
Match, oil is preferably pumped into final oil tank after the end of the product run, in order to next round processing, entire 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 is utilized toward lower stream
This activity pattern of liquid, can be energy saving, ensures safety, and atomisation tower 5 is specially designed to carry out cracked gas discharge
, it effectively removes sulphur and dust in fuel gas.
While there has been shown and described that the embodiment of the utility model, for the ordinary skill in the art,
It is appreciated that can these embodiments be carried out with a variety of variations in the case of the principle and spirit for not departing from the utility model, repaiied
Change, replace and modification, the scope of the utility model are defined by the appended claims and the equivalents thereof.
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 furnace body（11）, the furnace body（11）Intracavity bottom three groups of cracking gas burners are installed（12）It is 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）It alternately installs, 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）Feed inlet 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 cavity 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 terminal 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）Mounted on spray system（10）Top, the spray system（10）Packet
Include pond（101）, the pond（101）Left side wall water pump is connected with by pipeline（102）, the water pump（102）Left side
Spray tube is connected with by pipeline（103）, the spray tube（103）It is horizontally installed on cooling tube（91）Upside, the pond
（101）Right wall stent is installed（104）, the spray tube（103）, big collector（92）With small collector（93）Pass through stent
（104）It is fixed, the small collector（93）The pipeline that passes on left be connected with tank for gaseous or liquid substances（11）.
2. a kind of anaerobic low temperature pyrolyzer technical equipment according to claim 1, it is characterised in that：The transmission cylinder（21）
Radius be 1200mm.
3. a kind of 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.
4. a kind of 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.
5. a kind of 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 |
|---|---|---|---|
| CN201721702984.3U CN207552252U (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 |
|---|---|---|---|
| CN201721702984.3U CN207552252U (en) | 2017-12-11 | 2017-12-11 | A kind of anaerobic low temperature pyrolyzer technical equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207552252U true CN207552252U (en) | 2018-06-29 |
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ID=62666329
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721702984.3U Active CN207552252U (en) | 2017-12-11 | 2017-12-11 | A kind of anaerobic low temperature pyrolyzer technical equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207552252U (en) |
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2017
- 2017-12-11 CN CN201721702984.3U patent/CN207552252U/en active Active
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