CN206256205U - Carbon fiber low-temperature carbonization furnace - Google Patents
Carbon fiber low-temperature carbonization furnace Download PDFInfo
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- CN206256205U CN206256205U CN201621290444.4U CN201621290444U CN206256205U CN 206256205 U CN206256205 U CN 206256205U CN 201621290444 U CN201621290444 U CN 201621290444U CN 206256205 U CN206256205 U CN 206256205U
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- carbon fiber
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- inert gas
- heater
- waste discharge
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Abstract
A kind of carbon fiber low-temperature carbonization furnace, including body of heater, heating plate, heat-insulation layer, inert gas seal system, waste discharge system, heating plate uses banding adding thermal resistance, and heating part is divided into each warm area according to technological requirement, is isolated using warming plate between two adjacent warm areas;Waste discharge mouth is arranged at bottom of furnace body, and by temperature range subsection setup.The present apparatus substitutes electric furnace heating wire and partition heating mode using banding adding thermal resistance, substantially prolongs the service life of low-temperature carbonization furnace, thoroughly solves " string temperature " phenomenon between warm area, meets the thermograde requirement of production technology;Energy consumption is low, long service life, and inert gas consumption is low, and production waste gas can be discharged instantaneously;Temperature field in furnace, airflow field are evenly distributed, and reaction is uniform;The fracture of wire problem that the waste discharge of low-temperature carbonization furnace causes is solved, the yield and quality of carbon fiber product is improved, the production cost of carbon fiber is reduced, the problem that equipment life is short, maintenance cost is high, product yield is low, quality is unstable is solved.
Description
Technical field
The utility model is related to a kind of carbon fiber production low-temperature carbonization furnace.
Background technology
In carbon fiber production, polyacrylonitrile-radical(PAN)Fiber is combined with the oxygen in air to carry out pre-oxidation and is converted into ladder type
Structure;The carbon fiber of phosphorus content more than 93% is generated by charing operation again.It is low that low-temperature carbonization furnace in charing operation is used for fiber
The equipment of temperature carbonization, is processed fiber at a temperature of 300~900 DEG C.Belong to a kind of Muffle furnace, heat resisting steel in its structure
The rectangular seal furnace chamber that plate is made, oxidized fibre carries out carbonization reaction under inertia protection gas, and its molecular structure there occurs acutely
Change, there are about 43.3% quality and is pyrolyzed runaway with waste gas and tar mode.
At present, traditional low-temperature carbonization furnace is present:(1)Body of heater mode of heating is unreasonable, working service high cost:Easily make
Into " string temperature " phenomenon, i.e., thermograde is unsatisfactory for technological requirement between each warm area, and part warm area heating load is big, cause heater strip and
The furnace chamber life-span was greatly shortened to 1~2 year;(2)Carrier gas consumes high energy consumption:The high-temp waste gas produced in furnace chamber are taken away by carrier gas, together
Shi Zaiqi and waste gas have taken away substantial amounts of heat, not only increased the consumption of carrier gas, electric energy, and it is high to also result in indoor environment temperature,
It is unfavorable for enterprise employee health;(3)Waste discharge coke discharging is difficult;Byproduct of reaction is easily detained and after accumulation coking in Conventional cryogenic retort,
Under drip on the fiber of operation, can not only produce fracture of wire to influence the yield of carbon fiber product, moreover it is possible to cause carbon fiber Quality Down.
The content of the invention
Problem to be solved in the utility model is:For above-mentioned technical deficiency, there is provided a kind of carbon fiber low-temperature carbonization furnace,
So as to improve the stable operation level of equipment, the problem for overcoming above-mentioned prior art to exist.
Solve the problems, such as that the utility model is adopted the technical scheme that:It includes body of heater, heating plate, heat-insulation layer, indifferent gas
Body sealing system, waste discharge system, heating plate use banding adding thermal resistance, and heating plate is divided into each warm area according to technological requirement,
Isolated by warming plate between the adjacent warm area of each two;Waste discharge mouth is arranged at bottom of furnace body, and is set by temperature range segmentation
Put.
During inert gas duct is laid in the heat-insulation layer near heating plate, into the inert gas flows of body of heater outlet
Direction is identical with carbon fiber traffic direction in body of heater, into the inert gas flows direction of body of heater import and carbon fiber fortune in body of heater
Line direction is opposite.
Disturbance inert gas entrance is provided between two neighboring waste discharge mouth.
Bottom of furnace body residing for waste discharge mouth is pyramidal structure.
Good effect of the present utility model is:Traditional electric furnace heating wire and partition heating side is substituted using banding adding thermal resistance
Formula, substantially prolongs the service life of low-temperature carbonization furnace, thoroughly solve " string temperature " phenomenon between warm area, meet production technology
Thermograde requirement;Energy consumption is low, long service life, and inert gas consumption is low, and production waste gas can be excluded instantaneously, in-furnace temperature
Field, airflow field are evenly distributed, and reaction is uniform, solve the fracture of wire problem that the waste discharge of low-temperature carbonization furnace causes, and improve carbon fiber and produce
The yield and quality of product, reduce the production cost of carbon fiber;Can thoroughly solve that equipment life is short, maintenance cost is high, product yield
The unstable problem of low, quality, and the requirement of different strand specifications, such as 1K, 3K, 6K, 12K, 24K, 48K can be met.
Brief description of the drawings
Accompanying drawing 1 is structural representation of the present utility model;Accompanying drawing 2 is the vertical section structural representation of accompanying drawing 1;Accompanying drawing 3 is
Cross-sectional at the waste discharge mouth of accompanying drawing 1.
Specific embodiment
As shown in accompanying drawing 1,2, it includes body of heater 1, heating plate 6, heat-insulation layer 8, inert gas duct 5, row to the utility model
Useless mouth 2, heating plate 6 uses banding adding thermal resistance, and heating part is divided into each warm area according to technological requirement, and each warm area uses 50
The heating power of~200kW, is isolated between the adjacent warm area of each two using warming plate 7;Waste discharge mouth 2 is arranged at body of heater 1
Bottom, the bottom of furnace body residing for waste discharge mouth 2 is pyramidal structure(As shown in accompanying drawing 1,3), waste discharge mouth 2 is by temperature range subsection setup
Three, be respectively arranged at the maximum temperature range of fiber-reactive thing growing amount, i.e., 300~400 DEG C, 450~550 DEG C and 550~
700 DEG C, disturbance inert gas entrance 9 is provided between two neighboring waste discharge mouth 2, to prevent local generation dead band;By indifferent gas
During body pipeline 5 is laid on the heat-insulation layer 8 near heating plate 6 Nei, into the inert gas flows direction of body of heater outlet 10 and body of heater 1
The traffic direction of interior fiber 4 is identical, into the inert gas flows direction of body of heater import 11 and the traffic direction phase of fiber in body of heater 14
Instead, inert gas can make 100~150m of gas consumption reduction into being preheated to 200~350 DEG C before body of heater3/h。
Fiber 4 after oxidized from body of heater entrance 11 into low-temperature carbonization furnace body 1 inside carry out carbonization reaction, by each
After warm area reaction, subsequent processing is entered from body of heater outlet 10, heating plate 6 is heated to body of heater 1, it is ensured that the control temperature of each warm area
Degree;For the air for preventing interior enters body of heater, sealed using inert gas, inert gas warp in inert gas duct 5
After heating, body of heater 1 is entered through inert gas seal chamber 12.Oxidized fibre cracking reaction thing enters with inert gas through waste discharge mouth 2
Body of heater 1 is discharged in the road of waste pipe 3, finally enters emission-control equipment.
Claims (4)
1. a kind of carbon fiber low-temperature carbonization furnace, it includes body of heater, heating plate, heat-insulation layer, inert gas seal system, waste discharge system
System, it is characterised in that:Heating plate uses banding adding thermal resistance, and heating plate is divided into each warm area according to technological requirement, every two
Isolated by warming plate between individual adjacent warm area;Waste discharge mouth is arranged at bottom of furnace body, and by temperature range subsection setup.
2. carbon fiber low-temperature carbonization furnace according to claim 1, it is characterised in that:Inert gas duct is laid on heating
In in heat-insulation layer near plate, the inert gas flows direction into body of heater outlet is identical with carbon fiber traffic direction in body of heater,
It is opposite with carbon fiber traffic direction in body of heater into the inert gas flows direction of body of heater import.
3. carbon fiber low-temperature carbonization furnace according to claim 1, it is characterised in that:It is provided between two neighboring waste discharge mouth
Disturbance inert gas entrance.
4. carbon fiber low-temperature carbonization furnace according to claim 1, it is characterised in that:Bottom of furnace body residing for waste discharge mouth is cone
Shape structure.
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CN201621290444.4U CN206256205U (en) | 2016-11-29 | 2016-11-29 | Carbon fiber low-temperature carbonization furnace |
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CN201621290444.4U CN206256205U (en) | 2016-11-29 | 2016-11-29 | Carbon fiber low-temperature carbonization furnace |
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CN206256205U true CN206256205U (en) | 2017-06-16 |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106498566A (en) * | 2016-11-29 | 2017-03-15 | 河南永煤碳纤维有限公司 | Carbon fiber low-temperature carbonization furnace and controlling technical method |
CN108101047A (en) * | 2018-02-07 | 2018-06-01 | 安徽欣尔特新材料科技有限公司 | A kind of multi-temperature zone continous way superhigh temperature graphitizing furnace |
-
2016
- 2016-11-29 CN CN201621290444.4U patent/CN206256205U/en active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106498566A (en) * | 2016-11-29 | 2017-03-15 | 河南永煤碳纤维有限公司 | Carbon fiber low-temperature carbonization furnace and controlling technical method |
CN108101047A (en) * | 2018-02-07 | 2018-06-01 | 安徽欣尔特新材料科技有限公司 | A kind of multi-temperature zone continous way superhigh temperature graphitizing furnace |
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