CN1636868A - Polyolefin burning process of synthesizing carbon nanotube - Google Patents
Polyolefin burning process of synthesizing carbon nanotube Download PDFInfo
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- CN1636868A CN1636868A CN 200410011337 CN200410011337A CN1636868A CN 1636868 A CN1636868 A CN 1636868A CN 200410011337 CN200410011337 CN 200410011337 CN 200410011337 A CN200410011337 A CN 200410011337A CN 1636868 A CN1636868 A CN 1636868A
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- polyolefine
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- modified montmorillonoid
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Abstract
The present invention is polyolefin burning process of synthesizing carbon nanotube. Polyolefin, expander, organic matter modified montmorillonite and nickel-loading catalyst in certain proportion are mixed in n. banbury mixer or double-screw extruder, and mixture is set inside crucible and heated in gas flame to prepare carbon nanotube through combustion at 660-850 deg.c. The present invention uses cheap polyolefin as carbon source material and common equipment and has the advantages of low cost.
Description
Technical field
The present invention relates to a kind of method of the polyolefine synthesizing carbon nanotubes that burns, specifically, relate to and utilize polyolefine-montmorillonite composite material under the supported catalyst effect, by the method for combustion method synthesizing carbon nanotubes.
Background technology
The characteristics of carbon nanotube are that it typically has a diameter from several dusts to tens nanometers, and length-to-diameter ratio is tens to several thousand.Because carbon nanotube has excellent physical and mechanical performance and conductivity, is widely used.In recent years, people adopted the research of carbon nano-tube modification polymkeric substance more and more, and employed carbon nanotube and do not require that its structure is very perfect, but demand is big, and this just requires low and the carbon nanotube synthetic technology that output is big of preparation cost.
Usually, carbon nanotube adopts electric arc power generating method, laser evaporation method, electrochemical vapor deposition, catalysis synthesis process and the preparation of plasma synthesis method.The normally organic hydrocarbon small molecules of carbon source in these methods, as: methane, acetylene, ethene, CO or the like, the employing organic polymer is seldom arranged, particularly reclaim the carbon source material of polymkeric substance as made of carbon nanotubes.Adopt the fluidized bed cracking reactor as the ZL01118349.7 report; with CO and the following lower carbon number hydrocarbons of 7 carbon is carbon source; with hydrogen is reducing gas; all adopt protection of inert gas in the preparation process; reaction unit comprises main reactor, catalyst activator, gas distributor, gas-solid separator and product degassing stages, the equipment complexity that is adopted.
Summary of the invention
The method that the purpose of this invention is to provide a kind of polyolefine synthesizing carbon nanotubes that burns.
The present invention adopts olefin polymer and modified montmorillonoid mixture as carbon source, under the catalyst action, synthesizing carbon nanotubes in air, what is more important, along with polymer materials is widely used in industrial and agricultural production and the people's daily life, " white pollution " problem that waste or used plastics brought has produced serious threat to environment.Wherein, polyolefin polymers accounts for more than 50% of waste or used plastics.The olefin polymer that the present invention adopts is the carbon source of polyolefins waste or used plastics as synthesizing carbon nanotubes, opens up a new way for solving " white pollution ".Overcome the shortcoming of raw material costliness in the prior art and institute's using appts complexity simultaneously, and it has been used as filler in the existing technics of reclaim of plastic waste utilization and can not finally solve the problem of utilizing of waste or used plastics.
The present invention mixes polyolefine, expanding material with ni-loaded catalyst, organic modification montmonrillonite, prepare carbon nanotube by the incendiary method.Its basic step and processing condition are:
A) preparation of polyolefine-modified montmorillonoid-ni-loaded catalyst mixture
Ratio of components by weight, 65-85% polyolefine, 10% expanding material, 2.5-20% modified montmorillonoid and 2.5-5% ni-loaded catalyst are added in the Banbury mixer under 160-200 ℃, 70 rev/mins of melting mixing of rotating speed 10 minutes, make polypropylene miser, and modified montmorillonoid and closing of ni-loaded catalyst total amount are not less than 5%; Perhaps
Earlier with the pre-mixing at room temperature of polyolefine, expanding material and modified montmorillonoid, from main charging opening this mixture is entered that melting mixing prepares masterbatch the forcing machine, from the 2nd charging opening ni-loaded catalyst is added then and proceed melting mixing, each section of forcing machine temperature is in 160-200 ℃ of scope, the extruder screw rotating speed is 200-300 rev/min, gets polyolefin blend.
Used polyolefine is polypropylene, polyethylene or polystyrene; Used expanding material is acid anhydrides polypropylene, acid anhydrides polyethylene, and maleic anhydride content is 1-2.5% weight ratio or styrene-maleic anhydride copolymer, and maleic anhydride content is 12.5% weight ratio; The particle diameter of used modified montmorillonoid is at the 10-50 micron; Catalyst system therefor is that nickel particles loads on the micron-sized aluminium oxide-silicon oxide hybrid of 20-50, and nickel content is 50% weight ratio in the supported catalyst.
B) preparation of carbon nanotube
The polyolefin blend of step a) preparation is placed ceramic crucible and add a cover, being heated to the interior temperature of container is 660-850 ℃, be polymkeric substance the no flame generation to container top that takes fire heat-up time, is cooled to room temperature, obtains the black mixture of carbon nanotube and ni-loaded catalyst and polynite.
C) purification of carbon nanotube
Hydrofluoric acid with 10-30% joins in the black mixture of step b) preparation, stirs down and places 25-30 hour, separates obtaining black carbon powder; Additional proportion is 1: 1 the vitriol oil and the mixture of concentrated nitric acid, refluxes 2-4 hour, separates the carbon nanotube that obtains purifying.
The advantage of the inventive method:
The carbon source material that adopts among the present invention is polyolefine or reclaims polyolefine, cheap, the source is abundant, the ni-loaded catalyst and the modified montmorillonoid that adopt are easy to get, employed mixing equipment is the common process equipment of polymer materials, and the equipment of employed synthesize nano carbon tube material is ceramic crucible and common flame.The cost that adopts method of the present invention to prepare carbon nano-tube material has advantage than other method, can solve the problem that technics of reclaim of plastic waste is utilized simultaneously.
Embodiment
Embodiment 1
With polypropylene, maleic anhydride content are the acid anhydrides polypropylene of 1% weight ratio and modified montmorillonoid that particle diameter is 10 microns, particle diameter is 30 microns ni-loaded catalyst by 80: 10: 5: 5 weight ratios enter in the Banbury mixer simultaneously, under 200 ℃ and 70 rev/mins, carry out melting mixing 10 minutes, and obtained polypropylene miser.
Get said mixture 1 gram and be put in 15 milliliters of crucibles, and add and be placed on the crucible.With combustion gas lamp flame envelope heating crucible bottom.After several seconds, polymkeric substance takes fire.The interior temperature of crucible this moment is 660 ℃.Polymkeric substance behind the reignition, does not take off crucible, is put in shady and cool place and is cooled to room temperature.Obtain this moment is the black mixture of carbon nanotube and nickel catalyzator and polynite.
Hydrofluoric acid with 30% joins in the above-mentioned black mixture, and places 25 hours under magnetic agitation.Obtain black carbon powder after the centrifugation.Adding volume ratio then is 1: 1 the vitriol oil and the mixture of concentrated nitric acid, refluxes after 4 hours, takes out and carries out centrifugation.Obtain carbon nanotube 0.21 gram of purifying this moment.
Embodiment 2
Be that the acid anhydrides polypropylene of 2.5% weight ratio and the modified montmorillonoid that 2.5% particle diameter is 30 microns, the ni-loaded catalyst that 2.5% particle diameter is 20 microns enter in the Banbury mixer simultaneously with 85% recovery polypropylene, 10% maleic anhydride content by weight, under 200 ℃ and 70 rev/mins, carry out melting mixing 10 minutes, and obtained polypropylene miser.
Get said mixture 3 gram and be put in 15 milliliters of crucibles, and add and be placed on the crucible. with combustion gas lamp flame envelope heating crucible bottom.After several seconds, polymkeric substance takes fire.The interior temperature of crucible this moment is 700 ℃.Polymkeric substance behind the reignition, does not take off crucible, is put in shady and cool place and is cooled to room temperature.Obtain this moment is the black mixture of carbon nanotube and ni-loaded catalyst.
Hydrofluoric acid with 10% joins in the above-mentioned black mixture, and places 30 hours under magnetic agitation.Centrifugation then obtains black carbon powder.Add volume ratio then and be the mixture of 1: 1 vitriol oil and concentrated nitric acid, reflux after 2 hours, take out and carry out centrifugation.Obtain carbon nanotube 0.15 gram of purifying this moment.
Embodiment 3
By weight the ni-loaded catalyst and 70% recovery polypropylene, 10% maleic anhydride content that with 5% particle diameter are 50 microns is that the acid anhydrides polypropylene and 15% particle diameter of 2% weight ratio is that 40 microns modified montmorillonoids add in the Banbury mixer simultaneously, under 200 ℃ and 70 rev/mins, carry out melting mixing 10 minutes, and obtained polypropylene miser.
Get said mixture 2 gram and be put in 15 milliliters of crucibles, and add and be placed on the crucible.With combustion gas lamp flame envelope heating crucible bottom.After several seconds, polymkeric substance takes fire.The interior temperature of crucible this moment is 850 ℃.Polymkeric substance behind the reignition, does not take off crucible, is put in shady and cool place and is cooled to room temperature.Obtain this moment is the black mixture of carbon nanotube and ni-loaded catalyst and polynite.
Hydrofluoric acid with 20% joins in the above-mentioned black mixture, and under magnetic agitation, placed 28 hours. centrifugation then, obtain black carbon powder. add volume ratio then and be the mixture of 1: 1 vitriol oil and concentrated nitric acid, reflux after 3 hours, take out and carry out centrifugation.Obtain carbon nanotube 0.49 gram of purifying this moment.
Embodiment 4
Add in the Banbury mixer simultaneously by weight the modified montmorillonoid that with ni-loaded catalyst and 75% polystyrene, 10% styrene-maleic anhydride copolymer and 10% particle diameter in 5% example 2 is 50 microns, under 180 ℃ and 70 rev/mins, carry out melting mixing 10 minutes, and obtained polystyrene blends.
Get said mixture 2 gram and be put in 15 milliliters of crucibles, and add and be placed on the crucible.With combustion gas lamp flame envelope heating crucible bottom.After several seconds, polymkeric substance takes fire.The interior temperature of crucible this moment is 800 ℃.Polymkeric substance behind the reignition, does not take off crucible, is put in shady and cool place and is cooled to room temperature.Obtain this moment is the black mixture of carbon nanotube and ni-loaded catalyst and polynite.
Hydrofluoric acid with 25% joins in the above-mentioned black mixture, and under magnetic agitation, placed 30 hours. centrifugation then, obtain black carbon powder. add volume ratio then and be the mixture of 1: 1 vitriol oil and concentrated nitric acid, reflux after 4 hours, take out and carry out centrifugation.Obtain carbon nanotube 0.19 gram of purifying this moment.
Embodiment 5
By weight being that used modified montmorillonoid adds in the Banbury mixer simultaneously in the acid anhydrides polyethylene of 2.5% weight ratio and 20% example 3 with ni-loaded catalyst used in 5% example 2 and 65% polyethylene, 10% maleic anhydride content, under 160 ℃ and 70 rev/mins, carry out melting mixing 10 minutes, and obtained polyethylene mixture.
Get said mixture 2 gram and be put in 15 milliliters of crucibles, and add and be placed on the crucible.With combustion gas lamp flame envelope heating crucible bottom.After several seconds, polymkeric substance takes fire.The interior temperature of crucible this moment is about about 750 ℃.Polymkeric substance behind the reignition, does not take off crucible, is put in shady and cool place and is cooled to room temperature.Obtain this moment is the black mixture of carbon nanotube and ni-loaded catalyst and polynite.
Hydrofluoric acid with 20% joins in the above-mentioned black mixture, and places 30 hours under magnetic agitation.Centrifugation then obtains black carbon powder. and add volume ratio then and be the mixture of 1: 1 vitriol oil and concentrated nitric acid, reflux after 3 hours, take out and carry out centrifugation.Obtain carbon nanotube 0.29 gram of purifying this moment.
Embodiment 6
Adopting ni-loaded catalyst used in modified montmorillonoid used in the example 3 of weight ratio 10%, 4% example 2 and 76% polyethylene and 10% maleic anhydride content is that the acid anhydrides polyethylene of 1% weight ratio carries out two and goes on foot melting mixing in twin screw extruder, screw speed is 200 rev/mins, and four sections temperature are respectively 160 ℃, 170 ℃, 170 ℃ and 170 ℃.In twin screw extruder, will contain polyethylene and modified montmorillonoid earlier and add, at the 2nd charging opening ni-loaded catalyst be added again at the 1st charging opening.
Get said mixture 1 gram and be put in 15 milliliters of crucibles, and add and be placed on the crucible.With combustion gas lamp flame envelope heating crucible bottom.After several seconds, polymkeric substance takes fire.The interior temperature of crucible this moment is about about 800 ℃.Polymkeric substance behind the reignition, does not take off crucible, is put in shady and cool place and is cooled to room temperature.Obtain this moment is the black mixture of carbon nanotube and ni-loaded catalyst and polynite.
Hydrofluoric acid with 20% joins in the above-mentioned black mixture, and places 27 hours under magnetic agitation.Centrifugation then obtains black carbon powder.Add volume ratio then and be the mixture of 1: 1 vitriol oil and concentrated nitric acid, reflux after 2 hours, take out and carry out centrifugation.Obtain carbon nanotube 0.10 gram of purifying this moment.
Embodiment 7
Adopting ni-loaded catalyst used in modified montmorillonoid used in the example 1 of weight ratio 10%, 5% example 1 and 75% polypropylene and 10% maleic anhydride content is that the acid anhydrides polypropylene of 1.5% weight ratio carries out two and goes on foot melting mixing in twin screw extruder, screw speed is 300 rev/mins, and four sections temperature are respectively 180 ℃, 190 ℃, 200 ℃ and 200 ℃.In twin screw extruder, will contain polypropylene and modified montmorillonoid earlier and add, at the 2nd charging opening ni-loaded catalyst be added again at the 1st charging opening.
Get said mixture 1 gram and be put in 15 milliliters of crucibles, and add and be placed on the crucible.With combustion gas lamp flame envelope heating crucible bottom.After several seconds, polymkeric substance takes fire.The interior temperature of crucible this moment is about about 850 ℃.Polymkeric substance behind the reignition, does not take off crucible, is put in shady and cool place and is cooled to room temperature.Obtain this moment is the black mixture of carbon nanotube and ni-loaded catalyst and polynite.
Hydrofluoric acid with 30% joins in the above-mentioned black mixture, and places 25 hours under magnetic agitation.Centrifugation then obtains black carbon powder.Add volume ratio then and be the mixture of 1: 1 vitriol oil and concentrated nitric acid, reflux after 3 hours, take out and carry out centrifugation.Obtain carbon nanotube 0.35 gram of purifying this moment.
Embodiment 8
Adopting ni-loaded catalyst used in modified montmorillonoid used in the example 2 of weight ratio 10%, 5% example 3 and 75% polypropylene and 10% maleic anhydride content is that the acid anhydrides polypropylene of 1.5% weight ratio carries out two and goes on foot melting mixing in twin screw extruder, screw speed is 250 rev/mins, and four sections temperature are respectively 180 ℃, 190 ℃, 200 ℃ and 200 ℃.In twin screw extruder, will contain polypropylene and modified montmorillonoid earlier and add, at the 2nd charging opening ni-loaded catalyst be added again at the 1st charging opening.
Get said mixture 1 gram and be put in 15 milliliters of crucibles, and add and be placed on the crucible.With combustion gas lamp flame envelope heating crucible bottom.After several seconds, polymkeric substance takes fire.The interior temperature of crucible this moment is about about 750 ℃.Polymkeric substance behind the reignition, does not take off crucible, is put in shady and cool place and is cooled to room temperature.Obtain this moment is the black mixture of carbon nanotube and ni-loaded catalyst and polynite.
Hydrofluoric acid with 20% joins in the above-mentioned black mixture, and places 28 hours under magnetic agitation.Centrifugation then obtains black carbon powder.Add volume ratio then and be the mixture of 1: 1 vitriol oil and concentrated nitric acid, reflux after 4 hours, take out and carry out centrifugation.Obtain carbon nanotube 0.41 gram of purifying this moment.
Claims (6)
1, a kind of method of the polyolefine synthesizing carbon nanotubes that burns, its key step is:
A) preparation of polyolefine-modified montmorillonoid-ni-loaded catalyst mixture
Ratio of components by weight, 65-85% polyolefine, 10% expanding material, 2.5-20% modified montmorillonoid and 2.5-5% ni-loaded catalyst are added in the Banbury mixer under 160-200 ℃, 70 rev/mins of melting mixing of rotating speed 10 minutes, make polypropylene miser, and modified montmorillonoid and closing of ni-loaded catalyst total amount are not less than 5%;
B) preparation of carbon nanotube
The polyolefin blend of step a) preparation is placed ceramic crucible and add a cover, being heated to the interior temperature of container is 660-850 ℃, be polymkeric substance the no flame generation to container top that takes fire heat-up time, is cooled to room temperature, obtains the black mixture of carbon nanotube and ni-loaded catalyst and polynite;
C) purification of carbon nanotube
Hydrofluoric acid with 10-30% joins in the black mixture of step b) preparation, stirs down and places 25-30 hour, separates obtaining black carbon powder; Additional proportion is 1: 1 the vitriol oil and the mixture of concentrated nitric acid, refluxes 2-4 hour, separates the carbon nanotube that obtains purifying.
2, the method for burning polyolefine synthesizing carbon nanotubes as claimed in claim 1, it is characterized in that, step a) can also be earlier with the pre-mixing at room temperature of polyolefine, expanding material and modified montmorillonoid, from main charging opening this mixture is entered that melting mixing prepares masterbatch the forcing machine, from the 2nd charging opening ni-loaded catalyst is added then and proceed melting mixing, each section of forcing machine temperature is in 160-200 ℃ of scope, and the extruder screw rotating speed is 200-300 rev/min.
3. the method for burning polyolefine synthesizing carbon nanotubes as claimed in claim 1 is characterized in that, described modified montmorillonoid is a micron order, and particle diameter is at the 10-50 micron.
4. the method for burning polyolefine synthesizing carbon nanotubes as claimed in claim 1 is characterized in that, described ni-loaded catalyst is that nickel particles loads on the micron-sized aluminium oxide-silicon oxide hybrid of 20-50, and nickel content is 50% weight ratio in the supported catalyst.
5. the method for burning polyolefine synthesizing carbon nanotubes as claimed in claim 1 is characterized in that, used polyolefine is polypropylene, polyethylene and polystyrene.
6. the method for burning polyolefine synthesizing carbon nanotubes as claimed in claim 1, it is characterized in that, used expanding material is acid anhydrides polypropylene, acid anhydrides polyethylene, and maleic anhydride content is 1-2.5% weight ratio or styrene-maleic anhydride copolymer, and maleic anhydride content is 12.5% weight ratio.
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100434360C (en) * | 2005-12-09 | 2008-11-19 | 中国科学院理化技术研究所 | Method for preparing multi-wall carbon hano tube, chestnut-like carbon nano tube aggregator and carbon nano tube ball |
| CN100519408C (en) * | 2005-08-10 | 2009-07-29 | 中国科学院长春应用化学研究所 | Preparing hydrogen and Nano carbon tube through catalytic cracking polyolefine |
| CN1775671B (en) * | 2005-12-16 | 2010-05-05 | 中国科学院长春应用化学研究所 | Method for preparing carbon nano tube by nickel compound catalytic combustion of polyolefin |
| CN102987559A (en) * | 2012-12-27 | 2013-03-27 | 安徽中烟工业有限责任公司 | Composite filter stick capable of selectively reducing releasing amount of harmful phenol in main stream smoke of cigarettes |
| CN102741161B (en) * | 2008-04-16 | 2014-06-25 | 日本瑞翁株式会社 | Equipment and method for producing orientated carbon nano-tube aggregates |
| CN114572967A (en) * | 2022-04-07 | 2022-06-03 | 暨南大学 | System for solid polyolefin second-order firing carbon nano tube |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AU783464B2 (en) * | 2000-12-04 | 2005-10-27 | Kubota Corporation | Air diffuser and flushing method thereof |
| CN1141250C (en) * | 2001-05-25 | 2004-03-10 | 清华大学 | Process and reactor for continuously preparing nm carbon tubes with fluidized bed |
| CN1294076C (en) * | 2001-12-28 | 2007-01-10 | 南京师范大学 | Carbon atom wire and process for preparing carbon nanotube and carbon atom wire by pyrolyzing solid-state carbon source |
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2004
- 2004-12-10 CN CNB2004100113379A patent/CN1323029C/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100519408C (en) * | 2005-08-10 | 2009-07-29 | 中国科学院长春应用化学研究所 | Preparing hydrogen and Nano carbon tube through catalytic cracking polyolefine |
| CN100434360C (en) * | 2005-12-09 | 2008-11-19 | 中国科学院理化技术研究所 | Method for preparing multi-wall carbon hano tube, chestnut-like carbon nano tube aggregator and carbon nano tube ball |
| CN1775671B (en) * | 2005-12-16 | 2010-05-05 | 中国科学院长春应用化学研究所 | Method for preparing carbon nano tube by nickel compound catalytic combustion of polyolefin |
| CN102741161B (en) * | 2008-04-16 | 2014-06-25 | 日本瑞翁株式会社 | Equipment and method for producing orientated carbon nano-tube aggregates |
| CN102987559A (en) * | 2012-12-27 | 2013-03-27 | 安徽中烟工业有限责任公司 | Composite filter stick capable of selectively reducing releasing amount of harmful phenol in main stream smoke of cigarettes |
| CN114572967A (en) * | 2022-04-07 | 2022-06-03 | 暨南大学 | System for solid polyolefin second-order firing carbon nano tube |
| CN114572967B (en) * | 2022-04-07 | 2023-10-20 | 暨南大学 | System for second order firing of carbon nano tube by solid polyolefin |
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