CN1690262A - Micro carbon roll, process for preparing same and use thereof - Google Patents
Micro carbon roll, process for preparing same and use thereof Download PDFInfo
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- CN1690262A CN1690262A CN 200410034061 CN200410034061A CN1690262A CN 1690262 A CN1690262 A CN 1690262A CN 200410034061 CN200410034061 CN 200410034061 CN 200410034061 A CN200410034061 A CN 200410034061A CN 1690262 A CN1690262 A CN 1690262A
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- carbon
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Abstract
The invention belongs to carbon fiber material, which particular relates to micro carbon roll and its preparation method and use. The invention reaches the realization by looking for the new accelerant to compound micro carbon roll. When use sulphide or phosphide of some transition metal and their composite as accelerant, the reaction, which has no, needs for sulfurous and phosphorus impure substance as accelerant gas, is friendly to environment. The structure of micro carbon roll is similar to DNA, formed by two carbon fiber which curling in same direction; the shape of micro carbon roll is regular and uniform; the radius is 1.5-1.8 mu m; the pitch is 0-6 mu m. It can be used as micro-machined element, micro-electrical element, additive of composite, and wave energy absorbent, which has wide prospect in military and civilian use.
Description
Technical field
The invention belongs to the carbon fibre material field, particularly micro carbon roll and its production and use.
Background technology
U.S. Pat 405480 just disclosed the synthetic of carbon fiber in 1889, and still, owing to lacked advanced technologies such as process control, test sign at that time, this material with carbon element never obtains excellent research.Up to the eighties in 20th century, along with carbon fiber is applied in fields such as polymeric additive, catalyst carriers, scientists just begins it has been carried out research extensively and profoundly.In order to adapt to different purposes, developed multiple synthetic method at present, obtain the carbon fiber of various different shapes, character and performance.Chinese patent publication number CN1078273C discloses the employing flow method and has prepared carbon fiber, specifically is with catalyst ferrocene or Ni (CO)
4Fully mix under gaseous state with carbon source, brought into reaction zone by carrier gas then, obtained diameter at 5～100nm, and have the carbon fiber of bigger serface, this carbon fiber is suitable as hydrogen storage material.Chinese patent publication number CN1077926C discloses employing boric acid activation method and has prepared activated carbon fiber; specific practice is at first cellulose fibre to be put into to soak certain hour in the boric acid; take out dry then; place the heating furnace carbonization again, the activated carbon fiber that adopts the method to obtain has good prospects for application in fields such as environmental protection.
The shimasuer of Japan discloses employing CVD method and has obtained spiral helicine carbon fiber in Chinese patent notification number CN1098941C, it is catalyst that the method briefly is exactly with some metal, and the heating and decomposition hydrocarbon gas obtains spiral helicine carbon fiber in the presence of sulfur-bearing or phosphorous impurity.Chinese patent notification number CN1120252C and patent announcement CN1113990C disclose and have adopted similar method to obtain spiral helicine carbon fiber.Yet one of defective of this method is exactly to need constantly to feed the impurity that contains sulphur or phosphorus in the process of preparation, and this just makes and also contain a certain amount of sulphur or phosphorus in the discharge tail gas, thereby brings pollution to environment.In addition, in the specific embodiment of patent announcement CN1098941C, disclose, for obtain rule, uniformly product must strict control synthesis condition, and the substrate that will place catalyst along with the growth needs of fiber moves down, these requirements are difficult to reach for industrial production; The technical scheme that patent announcement CN1120252C discloses then is to control course of reaction by a cover complicated apparatus, and operating process is very loaded down with trivial details, and this is unfavorable for realizing industrial production equally; The implementation process of the technical scheme that patent announcement CN1113990C is disclosed is simple relatively, convenient, but the micro carbon roll form that the method obtains is irregular, and product is inhomogeneous.
Find that by analysis mainly there is the deficiency of following two aspects in existing preparation screw carbon fibre (being micro carbon roll) technology: (1) produces sulfur-bearing or phosphorous tail gas, and environment is polluted; (2) preparation efficiency, product form are to the synthesis condition sensitivity, and essential strict control synthesis condition is unfavorable for realizing industrial production.
Summary of the invention
One of purpose of the present invention is the defective that will solve two aspects of above-mentioned prior art, provide the form rule, evenly, micro carbon roll that product is single.
A further object of the present invention provides a kind of preparation method with simple, the easy to operate micro carbon roll of environmental friendliness, equipment.
Another object of the present invention provides the purposes of micro carbon roll.
The objective of the invention is to realize by the raw catelyst of seeking synthetic micro carbon roll material.When the sulfide that uses some transition metal or phosphide and their compound during as catalyst, reaction no longer needs to feed sulfur-bearing or phosphorous impurity as catalyst gas, and is environmentally friendly; And the micro carbon roll product form rule, single can obtained under the loose relatively synthesis condition, in the total overall reaction zone; In addition, this synthetic method equipment needed thereby device is simple, easy to operate.
Micro carbon roll of the present invention is characterised in that: the structure similar DNA of (1) micro carbon roll forms (micro carbon roll can left-handed or dextrorotation) by two equidirectional common helix-coils of carbon fiber; (2) shape of micro carbon roll rule, even.(3) cross section of carbon fiber can be circular or irregular polygon; (4) equivalent diameter of carbon fiber is 0.4～1.5 μ m; The coil diameter of micro carbon roll is 1.5～18 μ m; Pitch is 0～6 μ m; When reaction time during less than half an hour, the length of micro carbon roll is generally 0.1～3mm, if prolong the reaction time, can prepare longer micro carbon roll.
The preparation method of micro carbon roll of the present invention:
Pack into catalyst in the suitable containers or be applied on the substrate, then container or substrate are put into the crystal reaction tube of horizontal positioned; The air that vacuumizes or get rid of in the reaction system with inert gas feeds inert gas afterwards, flow is 80～120mL/ minute, begin heating simultaneously, adopt the CVD method to react, when being controlled at 600～800 ℃, temperature feeds hydrogen and carbon-source gas, hydrogen flowing quantity is 200～300mL/ minute, and the carbon-source gas flow is 80～120mL/ minute; React after 5～30 minutes, stop logical carbon-source gas and hydrogen, stop heating; In inert gas, can obtain the micro carbon roll product after the cooling.
Preparation method's principle of the present invention is such: because there is anisotropy in the different interplanars of catalyst, make that carbon-source gas cracking and speed of deposition or the speed that carbon atom is separated out from the different crystal faces of catalyst on the different crystal faces of catalyst is different, this has just directly caused the speed of growth of carbon fiber is uneven, and the velocity gradient here is exactly the driving force of carbon fiber generation helical buckling; On the other hand, each catalyst granules can grow two carbon fibers from two opposite directions, and these two carbon fibers have just become micro carbon roll with the common spiral of same direction.
Described catalyst is sulfide, phosphide or their compound of transition metal; Described sulfide is CoS, NiS
2, Sb
2S
3, Ni
3S
2, FeS, TiS
2Or their any mixture etc.; Described phosphide is Co
2P, Ni
2P, CrP, Mo
4P
3, Rh
4P
3, ZrP
2, TiP or their any mixture etc.
Described metal sulfide or phosphide can directly obtain from market, also can synthesize by the following method to obtain: with alloy powder and vulcanizing agent or bonderite reaction under 500～800 ℃ of transition metal or transition metal.Here said vulcanizing agent can be sulphur-containing substances such as elemental sulfur, carbon disulfide, thioether, mercaptan, thiophene or hydrogen sulfide; Said bonderite refers to phosphorus containg substances such as red phosphorus, phosphorus trichloride or phosphorus pentachloride; If use phosphorus pentasulfide etc. not only to contain sulphur but also contain the material of phosphorus then can obtain the compound of metal sulfide and metal phosphide.There is any need to prove, when adopting these methods to prepare catalyst, according to may containing elements such as a spot of carbon, oxygen, chlorine in the selected reagent different catalysts, but do not influence catalytic effect.The granular size of preparation micro carbon roll catalyst system therefor is 0.5～8.0 μ m, and catalyst amount is advisable at 0.001～0.1mm evenly to spread out back thickness.Catalyst adds howly, and product is just how, and too much certainly catalyst is also of no use!
Container described in the micro carbon roll preparation technology can be porcelain boat or quartz boat etc.; Described substrate can graphite flake, silicon chip or quartz plate etc.; Operable inert gas has argon gas, nitrogen, helium or their any mixture etc.; What can be used for carbon-source gas has acetylene, methane, ethane, ethene, propylene, benzene carbon containing micromolecule or their any mixture such as (through gasifications).
The micro carbon roll structure degree of graphitization of the present invention's preparation is lower, has scalability.Can be used for preparing the material of micromechanical component (as mechanical spring), microelectronic component (as the inductance coupling coil), the additive of composite is with mechanical property of reinforcing material etc., go back fields such as useful as catalysts carrier, chiral template, hydrogen storage material, electrode material in addition, particularly the absorber as electromagnetic energy has excellent performance.Therefore, military or civilian aspect all have broad application prospects.
Description of drawings
Fig. 1. the SEM photo of micro carbon roll of the present invention.
The specific embodiment
Embodiment 1:
5.8g nickel powder (5 μ m) and 3.5g sulphur powder mixed be placed on porcelain boat, the crystal reaction tube that the level that is placed into is again put (in 40 * 1200mm), is heated to 600 ℃ and kept 1 hour under the nitrogen protection.Get the nickel sulfide catalyst, quality percentage composition: nickel 73.3%, sulphur 26.7% after cooling and the grinding.
Embodiment 2:
Get 6.0g cobalt-nickel alloy powder (0.5 μ m) and 2.3g phosphorus pentasulfide and mix and be placed on quartz boat, the crystal reaction tube that puts it to horizontal positioned then (in 40 * 1200mm), is heated to 700 ℃ and kept 0.5 hour under the argon shield.Get the composite catalyst of nickel sulfide and nickel phosphide after cooling and the grinding, quality percentage composition: cobalt 7.2%, nickel 54.5%, sulphur 25.4%, phosphorus 12.9%.
Embodiment 3:
Take by weighing the 0.1g titanium disulfide, evenly be applied to 3.5 * 18cm
2Graphite substrate on, this graphite substrate is put into the crystal reaction tube (40 * 1200mm) of horizontal positioned; Charge into nitrogen and repetitive operation three times after vacuumizing; Feed nitrogen then constantly, flow is 100mL/ minute; The heating of employing horizontal electric resistance furnace feeds hydrogen and ethene when temperature reaches 680 ℃, flow was respectively 300mL/ minute and 120mL/ minute; React after 20 minutes, stop logical ethene and hydrogen, stop heating; Graphite substrate is taken out in the cooling back, overgrows with fine hair shape atrament on the graphite substrate, i.e. micro carbon roll.Output is 0.46g.The carbon fiber cross section of this micro carbon roll is irregular polygon, and the diameter of carbon fiber is 1.0～1.2 μ m, and the coil diameter of micro carbon roll is 12～16 μ m, and pitch is 2～6 μ m, and the length of micro carbon roll is 0.5～1.5mm.The retractility of this micro carbon roll is bigger, is suitable as elasticity and the toughness of the additive of micromechanical component (as mechanical spring), composite with reinforcing material, also can be used as the absorber of electromagnetic energy in addition.
Embodiment 4:
Take by weighing the catalyst 0.2g of embodiment 1 preparation, be laid on equably in the quartz boat, this quartz boat is pushed in the crystal reaction tube of horizontal positioned (40 * 1200mm); Logical argon gas (flow is 500mL/ minute) 5 minutes is to get rid of the air in the reaction system; Feed nitrogen and argon gas then constantly, flow is respectively 40mL/ minute, 40mL/ minute; The heating of employing horizontal electric resistance furnace feeds hydrogen and acetylene when temperature reaches 760 ℃, flow was respectively 250mL/ minute and 80mL/ minute; React after 30 minutes, stop logical acetylene and hydrogen, stop heating; Quartz boat is taken out in the cooling back, overgrows with fine hair shape atrament in the quartz boat, i.e. micro carbon roll.Output is 0.59g.The carbon fiber cross section of this micro carbon roll is circular, and the diameter of carbon fiber is 0.4～0.5 μ m, and the coil diameter of micro carbon roll is 2～5 μ m, and pitch is 0 (closely spiral), and the length of micro carbon roll is 1～3mm.This micro carbon roll form homogeneous, specific area are big, be suitable as fields such as chiral template, hydrogen storage material, microelectronic component (as the inductance coupling coil), catalyst carrier, electrode material, can reach-40dB as absorber absorption maximum in 8～18GHz scope of electromagnetic energy.
Embodiment 5:
Take by weighing the catalyst 0.1g of embodiment 2 preparations, be applied to 3.5 * 18cm equably
2Quartz plate on, this quartz plate is placed into the crystal reaction tube of horizontal positioned (in 40 * 1200mm); Helium injection gas 5 minutes is to get rid of the air in the reaction system; Feed helium then constantly, flow is 120mL/ minute; Employing horizontal electric resistance furnace heating feeds hydrogen, methane and acetylene when temperature reaches 700 ℃, flow was respectively 220mL/ minute, 50mL/ minute, 70mL/ minute; React after 25 minutes, stop ventilating methane, acetylene and hydrogen, stop heating; Quartz plate is taken out in the cooling back, overgrows with fine hair shape atrament on the quartz plate, i.e. micro carbon roll.Output is 0.67g.The carbon fiber cross section of this micro carbon roll is circular, and the diameter of carbon fiber is 0.5～0.7 μ m, and the coil diameter of micro carbon roll is 4～8 μ m, and pitch is 0～1 μ m, and the length of micro carbon roll is 0.5～2mm.This micro carbon roll coil diameter and pitch are moderate, can be used as the additive of electromagnetic energy absorption body, microelectronic component, micromechanical component, composite, go back fields such as useful as catalysts carrier, chiral template, electrode material, hydrogen storage material in addition.
Claims (9)
1. micro carbon roll, it is characterized in that: described micro carbon roll is formed by two equidirectional common helix-coils of carbon fiber; Shape of micro carbon roll rule, even; The cross section of carbon fiber can be circular or irregular polygon; The equivalent diameter of carbon fiber is 0.4～1.5 μ m; The coil diameter of micro carbon roll is 1.5～18 μ m; Pitch is 0～6 μ m.
2. the preparation method of a micro carbon roll as claimed in claim 1 is characterized in that:
Pack into catalyst in the container or be applied on the substrate, then container or substrate are put into the crystal reaction tube of horizontal positioned; The air that vacuumizes or get rid of in the reaction system with inert gas feeds inert gas afterwards, flow is 80～120mL/ minute, begin heating simultaneously, when being controlled at 600～800 ℃, temperature feeds hydrogen and carbon-source gas, hydrogen flowing quantity is 200～300mL/ minute, and the carbon-source gas flow is 80～120mL/ minute; Stop logical carbon-source gas and hydrogen after reaction a period of time, stop heating, in inert gas, obtain the micro carbon roll product after the cooling.
3. method as claimed in claim 2 is characterized in that: the granular size of described catalyst is 0.5～8.0 μ m, and catalyst amount is evenly to spread out back thickness at 0.001～0.1mm.
4. method as claimed in claim 1 or 2 is characterized in that: described catalyst is sulfide, phosphide or their any compound of transition metal.
5. method as claimed in claim 4 is characterized in that: described sulfide is CoS, NiS
2, Sb
2S
3, Ni
3S
2, FeS, TiS
2Or their mixture; Described phosphide is Co
2P, Ni
2P, CrP, Mo
4P
3, Rh
4P
3, ZrP
2, TiP or their any mixture.
6. method as claimed in claim 2 is characterized in that: described substrate comprises graphite flake, silicon chip or quartz plate.
7. method as claimed in claim 2 is characterized in that: described inert gas comprises argon gas, nitrogen, helium or their any mixture.
8. method as claimed in claim 2 is characterized in that: described carbon-source gas comprises acetylene, methane, ethane, ethene, propylene, benzene or their any mixture.
9. the purposes of a micro carbon roll as claimed in claim 1 is characterized in that: the material that is used to prepare micromechanical component, microelectronic component; The absorber of the additive of composite, catalyst carrier, chiral template, hydrogen storage material, electrode material, electromagnetic energy.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100340616A CN1328424C (en) | 2004-04-23 | 2004-04-23 | Micro carbon roll, process for preparing same and use thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100340616A CN1328424C (en) | 2004-04-23 | 2004-04-23 | Micro carbon roll, process for preparing same and use thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1690262A true CN1690262A (en) | 2005-11-02 |
| CN1328424C CN1328424C (en) | 2007-07-25 |
Family
ID=35346008
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2004100340616A Expired - Fee Related CN1328424C (en) | 2004-04-23 | 2004-04-23 | Micro carbon roll, process for preparing same and use thereof |
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|---|---|
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101774564B (en) * | 2009-01-12 | 2012-04-25 | 中国科学院理化技术研究所 | Method for preparing composite material of coiled carbon fibers filled with nano-magnetic micro-powder |
| CN106410214A (en) * | 2016-09-12 | 2017-02-15 | 天津工业大学 | Preparation method of NiS2 catalyst with high specific surface area |
| CN108998861A (en) * | 2018-06-08 | 2018-12-14 | 四川理工学院 | A kind of helical form carbon nano-fiber and preparation method thereof |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3844564B2 (en) * | 1997-07-18 | 2006-11-15 | 独立行政法人科学技術振興機構 | Hollow microfiber and method for producing the same |
| JPH11247030A (en) * | 1998-02-27 | 1999-09-14 | Seiji Motojima | Vapor phase production of coil-like carbon fiber |
| CN1113990C (en) * | 2000-06-07 | 2003-07-09 | 华侨大学 | High elastic screw carbon fibre and its preparing method |
| JP2004105827A (en) * | 2002-09-17 | 2004-04-08 | Gifu Univ | Catalyst for manufacturing coil shaped carbon fiber, and method of manufacturing the same |
-
2004
- 2004-04-23 CN CNB2004100340616A patent/CN1328424C/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101774564B (en) * | 2009-01-12 | 2012-04-25 | 中国科学院理化技术研究所 | Method for preparing composite material of coiled carbon fibers filled with nano-magnetic micro-powder |
| CN106410214A (en) * | 2016-09-12 | 2017-02-15 | 天津工业大学 | Preparation method of NiS2 catalyst with high specific surface area |
| CN108998861A (en) * | 2018-06-08 | 2018-12-14 | 四川理工学院 | A kind of helical form carbon nano-fiber and preparation method thereof |
| CN108998861B (en) * | 2018-06-08 | 2020-09-01 | 四川理工学院 | Preparation method of spiral carbon nanofiber |
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| Publication number | Publication date |
|---|---|
| CN1328424C (en) | 2007-07-25 |
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Granted publication date: 20070725 Termination date: 20200423 |
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