CN103418159A - New method for preventing nano particles from re-agglomerating during rapid expansion of supercritical fluid - Google Patents
New method for preventing nano particles from re-agglomerating during rapid expansion of supercritical fluid Download PDFInfo
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- CN103418159A CN103418159A CN2013101908137A CN201310190813A CN103418159A CN 103418159 A CN103418159 A CN 103418159A CN 2013101908137 A CN2013101908137 A CN 2013101908137A CN 201310190813 A CN201310190813 A CN 201310190813A CN 103418159 A CN103418159 A CN 103418159A
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 4
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- MXOGJBKTZBIWOT-UHFFFAOYSA-N 2-phenoxycarbonylbenzoic acid Chemical compound OC(=O)C1=CC=CC=C1C(=O)OC1=CC=CC=C1 MXOGJBKTZBIWOT-UHFFFAOYSA-N 0.000 claims description 2
- QFOHBWFCKVYLES-UHFFFAOYSA-N Butylparaben Chemical compound CCCCOC(=O)C1=CC=C(O)C=C1 QFOHBWFCKVYLES-UHFFFAOYSA-N 0.000 claims description 2
- 229920000049 Carbon (fiber) Polymers 0.000 claims description 2
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- 229910052786 argon Inorganic materials 0.000 claims description 2
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Abstract
The invention provides a treatment method for preventing nano particles from re-agglomerating. The treatment method is characterized in that the RESS technology is adopted, and the suspending liquid containing both the nano particles and dissolved small organic molecules of supercritical fluid is directly sprayed to a container through spray microtubes and collected. Due to the instantaneous release of the supercritical fluid, the small organic molecules moving with the airflow are supersaturated to separate out solid particles, and the solid particles deposit and grow on the scattered nano particles to form a layer of film on each nano particle, so as to prevent the nano particles from re-agglomerating. The treatment method has the advantages that no volatile organic compound is needed, the operation is simple, the structures of the nano particles are not damaged, and industrialization is facilitated. The treatment method has a good effect and a high practical value in preventing nano particles from re-agglomerating.
Description
One, technical field
The invention provides a kind of moment discharged at supercritical fluid makes and separates out solia particle with the organic molecule of air motion because of supersaturation nano particle is wrapped up, thereby reach the processing method of reuniting again that prevents nano particle, belong to the technical field of nano particle.
Two, technical background
Nano particle with properties such as quantum size effect, small-size effect, skin effect and macro quanta tunnel effects, at aspects such as catalysis, optical filtering, light absorption, medicine, magnetizing mediums and new materials, huge scientific value and wide market prospects are arranged, caused worldwide great attention, various countries' researcher has carried out a large amount of research.
And the agglomeration traits again of nano particle is the crucial difficult problem of restriction nano particle application.In order to solve this difficult problem, people make a large amount of research work.As with organic matter washing, add dispersant etc. nano particle carried out to parcel, the absorption of physics, and then reach and stop reuniting again of nano particle.Carry out chemical modification by the surface to nano particle in addition, make the organic strand of nanoparticle surface polarization functional group or grafting, prevent reuniting again of nano particle.And these methods have defect in various degree at aspects such as the integrality of the removing of the consumption of washing agent, cost consumption, dispersant, nano particle, suitability for industrialized production, dissolvent residuals.The fast expanding supercritical fluid technique can improve the dispersion of nano particle effectively, but after rapid expanding, these nano particles are easy to reunite again.
In order to overcome above-mentioned the deficiencies in the prior art, the present invention adopts fast expanding supercritical fluid technique (RESS technology), by directly being sprayed onto in container and collecting through fine jet pipe containing the suspension of the supercritical fluid that is dissolved with organic molecule of nano particle.The abrupt release of supercritical fluid makes with the organic molecule of air motion and separates out solia particle because of supersaturation, in the nanoparticle surface deposition of being broken up, increases.Form thin film, thereby reach, prevent that it from reuniting again.The method do not need to use VOC, simple to operate, do not destroy the structure of nano particle and be easy to industrialization, preventing that nano particle from having very good effect and practical value aspect reuniting again.
Three, summary of the invention
In order to solve the agglomeration traits again of nano particle, the invention provides a kind of making and separate out solia particle with the organic molecule of air motion because of supersaturation nano particle is wrapped up when the abrupt release of supercritical fluid, thereby reach the processing method of reuniting again that prevents nano particle.
Concrete experimental procedure is:
A) taking a certain amount of nano particle and organic molecule puts in 1~500ml reactor.
B) connect reaction unit, check air-tightness, by the gas component in supercritical system, get rid of the air in reactor, then temperature is transferred to 0~600 ℃ of even higher temperature.
C) by being passed in reactor of shooting flow system, be pressurized to 0~30MPa even higher, mix 0~300min even longer.
D) supercritical system mixed is injected in container and collects fast through minute nozzle.
E), after cooling, take out sample.
In above-mentioned test method, nano particle can be carbon black, active carbon, carbon fiber, CNT, Graphene, aluminium oxide, any nano particle or the mix nanoparticles such as titanium dioxide, silica, imvite.
In above-mentioned test method, the system components of supercritical fluid is under carbon dioxide, methyl alcohol, ethanol, methane, ethane, propane or other normal temperature, to be one or more of gas or volatile liquid substance.
In above-mentioned test method, organic molecule is under phthalic acid phenyl ester, butyl p-hydroxybenzoate, DMIP or other normal temperature, to be one or more of material solid and that can be dissolved in supercritical system.
In above-mentioned test method, while in supercritical system, there is no gas component, with nitrogen, argon gas or other inert gas, discharge the air in reactor, and for pressurized operation.
In above-mentioned test method, the internal diameter of minute nozzle is 1~500 μ m.
The electron scanning micrograph that is not wrapped nano particle that the nano particle wrapped up by organic molecule of processing by RESS and RESS process contrasts, we find that fluorescence probe is by the nano particle parcel, and agglomeration does not have wrapped nano particle that obvious improvement has been arranged again.
That the present invention has is simple to operate, do not need to use VOC, do not destroy the structure of nano particle and be easy to industrialized advantage.The present invention is by directly being sprayed onto in container and collecting through fine jet pipe containing the suspension of the supercritical fluid that is dissolved with organic molecule of nano particle.The abrupt release of supercritical fluid makes to separate out solia particle with the organic molecule of air motion because of supersaturation, in the nanoparticle surface deposition of being broken up, increases.Form thin film, thereby reach, prevent that it from reuniting again.This kind of method preventing that nano particle from having very good effect and practical value aspect reuniting again.
Four, accompanying drawing explanation
Fig. 1 contains the electron scanning micrograph of the multi-walled carbon nano-tubes of DMIP while being the RESS processing.
Fig. 2 does not contain the electron scanning micrograph of the multi-walled carbon nano-tubes of DMIP while being the RESS processing.
Fig. 3 contains the electron scanning micrograph of the SWCN of DMIP while being the RESS processing.
Fig. 4 does not contain the electron scanning micrograph of the SWCN of DMIP while being the RESS processing.
Five, the specific embodiment
Below introduce embodiments of the invention.
Embodiment mono-:
Taking a certain amount of multi-walled carbon nano-tubes and DMIP puts in 1~500ml reactor.Connect reaction unit, check air-tightness, use CO
2Get rid of the air in reactor, then temperature is transferred to 0~600 ℃ of even higher temperature.By CO
2Be passed in reactor, be pressurized to 0~30MPa even higher, mix 0~300min even longer.The supercritical system that mixes is injected in container and collects fast through minute nozzle, cooling after, take out sample.
The deployment conditions of two kinds of multi-walled carbon nano-tubes is observed by electron scanning micrograph.Fig. 1, Fig. 2 are respectively that RESS does not contain the electron scanning micrograph that does not contain the multi-walled carbon nano-tubes of DMIP when the multi-walled carbon nano-tubes of DMIP and RESS process while processing.By contrast, we find that DMIP is by the multi-walled carbon nano-tubes parcel, and agglomeration does not have wrapped multi-walled carbon nano-tubes that obvious improvement has been arranged again.
Embodiment bis-:
Taking a certain amount of SWCN and DMIP puts in 1~500ml reactor.Connect reaction unit, check air-tightness, use CO
2Get rid of the air in reactor, then temperature is transferred to 0~600 ℃ of even higher temperature.By CO
2Be passed in reactor, be pressurized to 0~30MPa even higher, mix 0~300min even longer.The supercritical system that mixes is injected in container and collects fast through minute nozzle, cooling after, take out sample.
The deployment conditions of two kinds of SWCNs is observed by electron scanning micrograph.Fig. 1, Fig. 2 are respectively that RESS does not contain the electron scanning micrograph that does not contain the SWCN of DMIP when the SWCN of DMIP and RESS process while processing.By contrast, we find that DMIP is by the SWCN parcel, and agglomeration does not have wrapped SWCN that obvious improvement has been arranged again.
Claims (6)
1. the invention provides a kind of abrupt release at supercritical fluid and make to separate out solia particle with the organic molecule of air motion because of supersaturation nano particle is wrapped up, thereby reach the processing method of reuniting again that prevents nano particle, concrete experimental procedure is:
A) taking a certain amount of nano particle and organic molecule puts in 1~500ml reactor.
B) connect reaction unit, check air-tightness, by the gas component in supercritical system, get rid of the air in reactor, then temperature is transferred to 0~600 ℃ of even higher temperature.
C) by being passed in reactor of shooting flow system, be pressurized to 0~30MPa even higher, mix 0~300min even longer.
D) supercritical system mixed is injected in container and collects fast through minute nozzle.
E), after cooling, take out sample.
2. the described method of claim 1, wherein said nano particle can be carbon black, active carbon, carbon fiber, CNT, Graphene, aluminium oxide, any nano particle or the mix nanoparticles such as titanium dioxide, silica, imvite.
3. the described method of claim 1, the system components of wherein said supercritical fluid is under carbon dioxide, methyl alcohol, ethanol, methane, ethane, propane or other normal temperature, to be one or more of gas or volatile liquid substance.
4. the described method of claim 1, wherein said organic molecule is under phthalic acid phenyl ester, butyl p-hydroxybenzoate, DMIP or other normal temperature, to be one or more of material solid and that can be dissolved in supercritical system.
5. the described method of claim 1, while in wherein said supercritical system, there is no gas component, discharge the air in reactor with nitrogen, argon gas or other inert gas, and for pressurized operation.
6. the described method of claim 1, the internal diameter of wherein said described minute nozzle is 1~500 μ m.
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104722219A (en) * | 2014-09-03 | 2015-06-24 | 青岛科技大学 | Carbon nano tube dispersion method |
CN106430113A (en) * | 2016-10-31 | 2017-02-22 | 重庆市南川区庆岩福利碱厂 | Production process capable of lowering sodium sulfide oxidation degree |
CN107973292A (en) * | 2016-10-24 | 2018-05-01 | 林逸樵 | A kind of devices and methods therefor for producing graphene |
CN113831762A (en) * | 2020-11-04 | 2021-12-24 | 东华理工大学 | Preparation method of coated titanium dioxide |
-
2013
- 2013-05-09 CN CN2013101908137A patent/CN103418159A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104722219A (en) * | 2014-09-03 | 2015-06-24 | 青岛科技大学 | Carbon nano tube dispersion method |
CN104722219B (en) * | 2014-09-03 | 2017-11-14 | 青岛科技大学 | A kind of carbon nano tube dispersion method |
CN107973292A (en) * | 2016-10-24 | 2018-05-01 | 林逸樵 | A kind of devices and methods therefor for producing graphene |
CN106430113A (en) * | 2016-10-31 | 2017-02-22 | 重庆市南川区庆岩福利碱厂 | Production process capable of lowering sodium sulfide oxidation degree |
CN106430113B (en) * | 2016-10-31 | 2018-07-13 | 重庆市南川区庆岩福利碱厂 | A kind of manufacture craft reducing oxidizing sodium sulphide degree |
CN113831762A (en) * | 2020-11-04 | 2021-12-24 | 东华理工大学 | Preparation method of coated titanium dioxide |
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Application publication date: 20131204 |