CN212335378U - Carbon fiber oxidation furnace - Google Patents
Carbon fiber oxidation furnace Download PDFInfo
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- CN212335378U CN212335378U CN202020773290.4U CN202020773290U CN212335378U CN 212335378 U CN212335378 U CN 212335378U CN 202020773290 U CN202020773290 U CN 202020773290U CN 212335378 U CN212335378 U CN 212335378U
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- furnace body
- carbon fiber
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- 229920000049 Carbon (fiber) Polymers 0.000 title claims abstract description 65
- 239000004917 carbon fiber Substances 0.000 title claims abstract description 65
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract description 65
- 230000003647 oxidation Effects 0.000 title claims abstract description 36
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 36
- 238000004891 communication Methods 0.000 claims abstract description 3
- 238000007789 sealing Methods 0.000 claims description 16
- 238000007689 inspection Methods 0.000 claims description 7
- 238000010438 heat treatment Methods 0.000 abstract description 12
- 230000006698 induction Effects 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 31
- 238000000034 method Methods 0.000 description 6
- 230000002349 favourable effect Effects 0.000 description 4
- 229920002239 polyacrylonitrile Polymers 0.000 description 4
- 230000001502 supplementing effect Effects 0.000 description 4
- 239000000835 fiber Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000009827 uniform distribution Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 238000003763 carbonization Methods 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005485 electric heating Methods 0.000 description 2
- 230000007774 longterm Effects 0.000 description 2
- 239000013589 supplement Substances 0.000 description 2
- 239000002912 waste gas Substances 0.000 description 2
- 229920000297 Rayon Polymers 0.000 description 1
- 238000002679 ablation Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007380 fibre production Methods 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 238000005087 graphitization Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000013081 microcrystal Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 238000003746 solid phase reaction Methods 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- 239000002341 toxic gas Substances 0.000 description 1
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Abstract
The utility model provides a pair of carbon fiber oxidation furnace, the induction cooker comprises a cooker bod, the furnace body is equipped with an entry, an export and a hot air circulating system, a serial communication port, a plurality of circulation wind channels have in the furnace body, and the multi-beam carbon fiber silk bundle draws through the outside roller and draws certainly the entry gets into the circulation wind channel of furnace body, hot air circulating system includes electric heater, circulating fan and gaseous uniform distributor, circulating fan is located the electric heater front end, circulating wind channel's air outlet sets up gaseous uniform distributor, hot-blast gets into under circulating fan's drive electric heater heating adjusts hot-blast through gaseous uniform distributor again for even unanimous horizontal hot-blast, and the horizontal hot-blast entering after the adjustment the circulation wind channel lasts to carbon fiber silk bundle thermal oxidation.
Description
Technical Field
The utility model relates to a carbon fiber production technical field especially relates to a formula carbon fiber oxidation furnace equipment of blowing horizontally.
Background
The carbon fiber is a new fiber material, has extremely high strength and rigidity, resists high temperature and high pressure and corrosion ablation, is widely applied to the fields of aerospace, military, sports and leisure and industry due to the excellent performance of the carbon fiber, and has a rapidly increasing trend in demand. The carbon fiber is a fibrous carbon material with carbon content over 90 percent, is prepared by carrying out high-temperature solid-phase reaction processes such as pre-oxidation, carbonization, graphitization and the like on protofilaments such as organic fiber-Polyacrylonitrile (PAN) fiber, viscose fiber, pitch fiber and the like, and consists of graphite microcrystals with preferred orientation, so that the carbon fiber has high strength and elastic modulus (rigidity). The specific gravity of the material is generally 1.70-1.80 g/cm3, the strength is 1200-7000 MPa, the elastic modulus is 200-400 GPa, and the thermal expansion coefficient is close to zero.
The production of high-quality PAN-based carbon fiber is a system engineering, and from the production of precursor to preoxidation, carbonization and subsequent surface treatment, the factors influencing the quality of the carbon fiber are numerous, wherein the preoxidation process is an important link and is a bottleneck restricting the production. At present, the pre-oxidation process of PAN needs 50-120 min, so the efficiency of the pre-oxidation furnace becomes the main factor for controlling the period of producing carbon fiber.
SUMMERY OF THE UTILITY MODEL
The utility model discloses a main purpose, lie in providing a carbon fiber oxidation furnace, the induction cooker comprises a cooker bod, the furnace body is equipped with an entry, an export and a hot air circulating system, a serial communication port, a plurality of circulation wind channels have in the furnace body, and the multi-beam carbon fiber silk bundle pulls through outside traction roller certainly the entry gets into the circulation wind channel of furnace body, hot air circulating system includes electric heater, circulating fan and gaseous uniform distributor, circulating fan is located the electric heater front end, circulating wind channel's air outlet sets up gaseous uniform distributor, hot-blast entering under circulating fan's drive electric heater heating is again through gaseous uniform distributor with hot-blast adjustment for even unanimous horizontal hot-blast, the horizontal hot-blast entering after the adjustment the circulation wind channel lasts to carbon fiber silk bundle thermal oxidation.
In one embodiment, the furnace body is provided with a new steam replenishing pipeline for injecting fresh hot air, and the fresh hot air is injected into the circulating air duct through the new steam replenishing pipeline.
In one embodiment, the furnace body is divided into an upper furnace body and a lower furnace body which are divided into two layers, each layer of the furnace body is provided with a front furnace body and a rear furnace body, the upper furnace body and the lower furnace body are identical in arrangement structure and are not communicated, and the front furnace body and the rear furnace body are communicated.
In one embodiment, the hot air circulating system is respectively positioned in the front furnace body and the rear furnace body of the upper furnace body and the front furnace body and the rear furnace body of the lower furnace body.
In one embodiment, a plurality of carbon fiber tows are drawn by an external drawing roller and enter an upper furnace body of the furnace body from an inlet, are repeatedly circulated in the upper furnace body under the drawing of the external drawing roller and then enter a lower furnace body of the furnace body, the carbon fiber tows are pre-oxidized by hot air from the hot air circulation system, and the pre-oxidized carbon fiber tows leave the furnace body from an outlet.
In one embodiment, a sealed flow passage is arranged in the furnace body, and the sealed flow passage is located at the inlet and the outlet of the furnace body and is communicated with the inlet and the outlet of the furnace body.
In one embodiment, the furnace body is connected with a gas collecting pipeline, and the gas collecting pipeline is communicated with the sealed flow passage outlet.
In one embodiment, the furnace body is provided with an inspection door, and the inspection door is positioned in the middle of the furnace body.
In one embodiment, the furnace body is provided with a furnace body exhaust line.
In one embodiment, the inlet and the outlet of the furnace body are provided with inlet and outlet sealing gas pipelines, and the inlet and outlet sealing gas pipelines are arranged close to the sealing flow channel.
The application provides a carbon fiber oxidation furnace, hot air circulating system, electric heating control can realize that temperature control is accurate, and the temperature difference is undulant little, can satisfy the carbon fiber silk bundle and react the temperature demand in the oxidation furnace, are favorable to equipment long-term steady operation. The air duct flow field trace form in the carbon fiber tow oxidation furnace body is favorable for improving the pre-oxidation effect of the carbon fiber tow and improving the quality of the carbon fiber tow, and in addition, the temperature of the whole carbon fiber tow heating oxidation process is controllable, and the heating efficiency is high.
Drawings
FIG. 1 is a schematic structural view of a carbon fiber oxidation furnace.
Fig. 2 is a schematic view of the wind direction and the wind channel of the hot wind in the furnace body.
Fig. 3 is the air channel flow field trace of the hot air in the furnace body.
Wherein the reference numerals are:
inlet 1
Gas collecting line 2
Furnace body 3
Circulating fan 5
Furnace exhaust line 6
Fresh steam make-up line 7
Inlet and outlet sealed gas pipeline 8
An outlet 9
Inspection door 10
Sealed flow passage 11
Arched hot air a
Horizontal hot wind a1
Arc hot wind a2
Detailed Description
The detailed description and technical contents related to the present invention are described below with reference to the accompanying drawings:
the utility model provides a carbon fiber oxidation furnace, and figure 1 is a schematic structural diagram of the carbon fiber oxidation furnace. Fig. 2 is a schematic view of the wind direction and the wind channel of the hot wind in the furnace body. Fig. 3 is the air channel flow field trace of the hot air in the furnace body. This carbon fiber oxidation furnace includes furnace body 3 and other accessory parts and constitutes, furnace body 3 is equipped with an entry 1, an export 9 be equipped with drive and heated circulation wind's heated air circulation system in the furnace body, be the circulation wind channel in the furnace body, heated air circulation system includes electric heater 4, circulating fan 5 and gaseous uniform distribution ware (not marked), circulating fan is located electric heater 4 front end, the air outlet installation in circulation wind channel are provided with gaseous uniform distribution ware, hot-blast entering under circulating fan 5's drive electric heater 4 heating is again through gaseous uniform distribution ware with hot-blast adjustment for even unanimous horizontal hot-blast, and horizontal hot-blast entering circulation wind channel after the adjustment lasts to carbon fiber tow thermal oxidation.
Hot air heated by the hot air circulating system is horizontally blown to the carbon fiber tows for pre-oxidation, and the running track of the carbon fiber tows in the furnace body is as follows: a plurality of carbon fiber tows are drawn by an external drawing roller and enter an upper furnace body of the furnace body 3 from an inlet 1, in the embodiment, the wind direction of hot wind for heating the plurality of carbon fiber tows is a horizontal direction, the wind direction is perpendicular to the direction of the carbon fiber tows, the carbon fiber tows are prevented from being blown away, the hot wind is firstly repeatedly circulated in the upper furnace body under the drawing of the external drawing roller and then enters a lower furnace body of the furnace body 3 for repeated circulation, the hot wind from the hot wind circulation system heats and oxidizes the carbon fiber tows, and the oxidized carbon fiber tows leave the furnace body 3 from an outlet 9.
Referring to fig. 1, the furnace body 3 is divided into an upper furnace body and a lower furnace body, which are two layers, each layer of the furnace body is provided with a front furnace body and a rear furnace body, the upper furnace body and the lower furnace body are the same in arrangement structure, the upper furnace body and the lower furnace body are not communicated, and the front furnace body and the rear furnace body are communicated. All the accessory parts of the upper furnace body and the lower furnace body are arranged in the same way, and the front furnace body and the rear furnace body are arranged symmetrically. The accessory components comprise a gas collecting pipeline 2, an electric heater 4, a circulating fan 5, a gas uniform distributor, a furnace body exhaust pipeline 6, a new steam supplementing pipeline 7, an inlet and outlet sealing gas pipeline 8 and an inspection door 10.
In this embodiment, referring to fig. 3, it can be seen from fig. 3 that hot air in the furnace body flows in an arcuate circulation manner, the arcuate hot air is formed by horizontal hot air and arc-shaped hot air at two opposite ends of the horizontal hot air, the horizontal hot air is mainly used for heating and oxidizing carbon fiber tows, an outlet of the circulation air channel is located at the arc-shaped hot air, the furnace body is provided with a new steam supplement pipeline 7 into which new hot air is injected, and the new hot air enters the hot air circulation system through the new steam supplement pipeline 7.
In this embodiment, the hot air circulation system includes the electric heater 4, the circulating fan 5 and the gas uniform distributor, and the hot air circulation system is respectively located in the front furnace body and the rear furnace body of the upper furnace body and the front furnace body and the rear furnace body of the lower furnace body. The definition of preceding, back in this application is based on the motion of carbon fiber silk bundle, and the position that the entrance side was located is preceding furnace body, and the exit side position is back furnace body, refer to fig. 1, in fig. 1, circulating fan is located electric heater 4 front end, and the air outlet in circulation wind channel sets up gaseous uniform distributor. The new steam supplementing pipeline 7 is communicated with the upper furnace body and the lower furnace body, fresh hot air of the new steam supplementing pipeline 7 enters the circulating fan 5, enters the electric heater 4 under the action of the circulating fan 5 for heating, and participates in hot air circulation, the hot air circulation means that hot air enters the electric heater 4 under the driving of the circulating fan for heating, and the heated hot air heats and oxidizes the carbon fiber tows.
Referring to fig. 2, fig. 2 is a schematic view of the wind direction and the wind channel in the furnace body, and as shown in fig. 2, in the present embodiment, the circulating wind channel of the hot wind for heating the plurality of carbon fiber tows is horizontal, and the wind direction is horizontal. In the process, the hot air heats and oxidizes the carbon fiber tows all the time in a horizontal blowing mode, and fresh hot air enters a hot air circulating system through a new steam supplementing pipeline 7.
Referring to fig. 1 again, in the embodiment, a sealed flow channel 11 is disposed in the furnace body, the sealed flow channel is located at the inlet and the outlet of the furnace body and is communicated with the inlet and the outlet, the sealed flow channel 11 is used to prevent harmful gas from overflowing the inlet and the outlet of the furnace body, the sealed flow channel 11 is connected to a gas collecting pipeline 2, and in the specific embodiment, the gas collecting pipeline 2 is used to guide out the harmful gas overflowing from the furnace body and prevent the harmful gas from entering the atmosphere.
Referring again to fig. 1, the inlet 1 and the outlet 9 of the furnace body 3 are provided with inlet and outlet sealing gas lines 8, and the inlet and outlet sealing gas lines 8 are disposed near the sealing flow passage 11. The sealing gas continuously impacts the sealing flow channel 11 at the inlet and the outlet in a gas pressure mode through the inlet and outlet sealing gas pipeline, the sealing gas pressure entering the furnace body is higher than the furnace body pressure, harmful gas from the furnace body is prevented from overflowing the sealing flow channel 11, if part of the harmful gas overflows the sealing flow channel 11, the harmful gas enters the gas collecting pipeline 2 to be discharged, the tail end of the gas collecting pipeline 2 can be connected with a waste gas processor, specifically can be a combustor or a gas cleaning device, and the harmful gas meets the discharge condition after being processed.
Referring to fig. 1 again, the furnace body 3 is provided with an inspection door 10 and a furnace body exhaust line 6, the inspection door 10 is opened to adjust the gas injection angle of the sealed flow channel 11, the furnace body exhaust port is arranged above the middle of the furnace body, toxic gas in the furnace body is exhausted from the furnace body exhaust line, the tail end of the furnace body exhaust line is connected with a waste gas processor, specifically a burner or a gas cleaning device, and harmful gas meets the emission condition after being processed.
To sum up, the carbon fiber oxidation furnace that this application provided, hot air circulating system, electric heating control can realize that temperature control is accurate, and the temperature difference is undulant little, can satisfy the carbon fiber silk bundle and react the temperature demand in the oxidation furnace, are favorable to equipment long-term steady operation. The air duct flow field trace form in the carbon fiber tow oxidation furnace body is favorable for improving the pre-oxidation effect of the carbon fiber tow and improving the quality of the carbon fiber tow, and in addition, the temperature of the whole carbon fiber tow heating oxidation process is controllable, and the heating efficiency is high.
Claims (10)
1. A carbon fiber oxidation furnace comprises a furnace body (3), wherein the furnace body (3) is provided with an inlet (1), an outlet (9) and a hot air circulating system, it is characterized in that a plurality of circulating air ducts are arranged in the furnace body, a plurality of carbon fiber tows are drawn by an external drawing roller to enter the circulating air ducts of the furnace body from the inlet, the hot air circulation system comprises an electric heater (4), a circulating fan (5) and an air uniform distributor, the circulating fan is positioned at the front end of the electric heater, the air outlet of the circulating air duct is provided with an air uniform distributor, the hot air enters the electric heater to be heated under the driving of the circulating fan (5), then the hot air is adjusted into uniform horizontal hot air through the air uniform distributor, and the adjusted horizontal hot air enters the circulating air duct to continuously heat and oxidize the carbon fiber tows.
2. The carbon fiber oxidation furnace according to claim 1, wherein the furnace body is provided with a fresh steam supply line (7) through which fresh hot air is injected, and fresh hot air is injected into the circulation duct through the fresh steam supply line (7).
3. The carbon fiber oxidation furnace according to claim 1, wherein the furnace body is divided into an upper furnace body and a lower furnace body, which are two layers, each layer of the furnace body has a front furnace body and a rear furnace body, the upper furnace body and the lower furnace body are arranged in the same structure, the upper furnace body and the lower furnace body are not communicated, and the front furnace body and the rear furnace body are communicated.
4. The carbon fiber oxidation furnace according to claim 3, wherein the hot air circulation systems are respectively located at the front furnace body and the rear furnace body of the upper furnace body and the front furnace body and the rear furnace body of the lower furnace body.
5. The carbon fiber oxidation furnace according to claim 3, wherein a plurality of carbon fiber tows are drawn by an external drawing roller and enter an upper furnace body of the furnace body (3) from the inlet (1), and are repeatedly circulated in the upper furnace body under the drawing of the external drawing roller and then enter a lower furnace body of the furnace body (3), the carbon fiber tows are pre-oxidized by hot air from the hot air circulation system, and the pre-oxidized carbon fiber tows leave the furnace body (3) from the outlet (9).
6. The carbon fiber oxidation furnace according to claim 1, wherein a sealed flow channel is provided in the furnace body, and the sealed flow channel is located at and communicates with the inlet and the outlet of the furnace body.
7. The carbon fiber oxidation furnace according to claim 6, wherein the furnace body is connected to a gas collection line, the gas collection line being in communication with the sealed flow channel outlet.
8. The carbon fiber oxidation furnace according to claim 1, wherein the furnace body (3) is provided with an inspection door located throughout the middle of the furnace body.
9. The carbon fiber oxidation furnace according to claim 1, wherein the furnace body is provided with a furnace body exhaust line (6).
10. The carbon fiber oxidation furnace according to claim 6, wherein the inlet (1) and the outlet (9) of the furnace body (3) are provided with inlet and outlet sealing air pipelines (8), and the inlet and outlet sealing air pipelines (8) are arranged close to the sealing flow passage.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020773290.4U CN212335378U (en) | 2020-05-12 | 2020-05-12 | Carbon fiber oxidation furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020773290.4U CN212335378U (en) | 2020-05-12 | 2020-05-12 | Carbon fiber oxidation furnace |
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| Publication Number | Publication Date |
|---|---|
| CN212335378U true CN212335378U (en) | 2021-01-12 |
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| CN202020773290.4U Active CN212335378U (en) | 2020-05-12 | 2020-05-12 | Carbon fiber oxidation furnace |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114540986A (en) * | 2022-02-28 | 2022-05-27 | 新创碳谷控股有限公司 | Carbon fiber pre-oxidation furnace with airflow rectification function |
-
2020
- 2020-05-12 CN CN202020773290.4U patent/CN212335378U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114540986A (en) * | 2022-02-28 | 2022-05-27 | 新创碳谷控股有限公司 | Carbon fiber pre-oxidation furnace with airflow rectification function |
| CN114540986B (en) * | 2022-02-28 | 2022-08-16 | 新创碳谷控股有限公司 | Carbon fiber pre-oxidation furnace with airflow rectification function |
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Effective date of registration: 20240119 Address after: 100728 No. 22 North Main Street, Chaoyang District, Beijing, Chaoyangmen Patentee after: CHINA PETROLEUM & CHEMICAL Corp. Patentee after: Sinopec Shangai Petrochemical Co.,Ltd. Address before: 730060 Gansu city of Lanzhou province Xigu District Heshui Road No. 3 Patentee before: TIANHUA INSTITUTE OF CHEMICAL MACHINERY AND AUTOMATION Co.,Ltd. |