WO2004085030A1 - 微粒子含有分散液の濃縮法および微粒子回収方法 - Google Patents
微粒子含有分散液の濃縮法および微粒子回収方法 Download PDFInfo
- Publication number
- WO2004085030A1 WO2004085030A1 PCT/JP2003/009875 JP0309875W WO2004085030A1 WO 2004085030 A1 WO2004085030 A1 WO 2004085030A1 JP 0309875 W JP0309875 W JP 0309875W WO 2004085030 A1 WO2004085030 A1 WO 2004085030A1
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- WO
- WIPO (PCT)
- Prior art keywords
- ionic liquid
- dispersion
- liquid
- fine particles
- concentrating
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D43/00—Separating particles from liquids, or liquids from solids, otherwise than by sedimentation or filtration
Definitions
- an ionic liquid that is not substantially dissolved in a dispersion medium of the dispersion liquid is added to a dilute dispersion liquid of the fine particles, and the fine particles are taken into the ionic liquid to form a high-concentration fine particle dispersion liquid.
- the present invention relates to a method for concentrating fine particles, and a method for collecting fine particles by filtration from the concentrated state of fine particles. Background art
- the liquid as the dispersion medium is subjected to normal pressure, reduced pressure, and freezing.
- an azeotropic component is added and the mixture is removed by evaporation, and a method in which the mixture is removed using a filtration membrane.
- the issue of environmental pollution has been raised in many fields, and the establishment of environmentally friendly methods in the field of chemistry has become so important as to affect the survival of companies.
- the environmental problems in addition to the problem that does not discharge harmful substances from a chemical reaction system, regulations on suppression of CO 2 generation is enhanced, reducing the how C o 2 generated in the entire production system It is necessary to consider this. Therefore, the method of removing the dispersing solvent by using a large amount of energy is, for example, a method of concentrating, separating and recovering fine particles from a dispersing medium that can be used instead of water because the latent heat of evaporation is large when the dispersing medium is water. Need to be developed.
- the solvent used not only controls the explosive progress of the reaction of the reagent, but also has the function of removing the heat of reaction, and further facilitates the handling of the reagent. It also has the function of
- after the chemical reaction it is necessary to separate and remove the used solvent from the reaction product and the like.
- the separation and removal of the solvent there is a problem similar to that of the concentration of the fine particle dispersion, that is, a problem of how to remove and discharge a large amount of the solvent without environmental pollution.
- organoionic liquids include various types of 1-alkylpyridinium salts, 1-alkyl-13-methylmidazolylium salts and ammonium salts of the following formulas 1a, b and c: It can be cited as one having a useful function in the reaction or having a useful functionality.
- R 3 is an alkyl group having 17 C atoms, especially a hexyl group
- R is an alkyl group having 17 C atoms, especially an ethyl group, a butyl group, a benzyl group
- An ionic liquid also referred to as a room temperature molten salt, has as a central element an ionic salt having N, 0, P, S, etc. as an organic cation.
- protons such as phosphonium, ammonium salt, 2-methyl-11-pyrroline, 1-methylvirazole, 1-ethylcarbazole and the like to produce cations. it can.
- ionic liquids also have difficult problems. This is because ionic liquids have a vapor pressure of almost zero and, like conventional organic solvents, separate substances that are dissolved in the ionic liquid when used in the reaction and then reused. There is a problem. Among them good UNA separation method combining supercritical C 0 2 and I O emissions liquids have attracted attention. Blanchard, Brennecke et al. Disclose supercritical C ⁇ 2 at 8 MPa in an imidazolium ionic liquid to 0.6 mol fraction in the ionic liquid, It is clear that adding more than that will separate it into two layers.
- An object of the present invention is to provide a method for concentrating a dilute dispersion of fine particles or collecting the fine particles, which eliminates the environmental problem and the energy problem in the concentration or recovery of the fine particles. Meanwhile, it is known that the fine particles dispersed in the liquid of the dispersion medium have a charge in the dispersion medium.
- the ionic liquid was developed as a substitute for water, which was used in large quantities as a reaction medium, but not only serves as a solvent for the reaction reagent in the reaction system, but also as a chemical structure of the cation.
- the solubility and action on the reaction reagents and reaction products are different depending on the counteranion etc. combined with this, the reaction sample and the reaction product can be easily separated and recovered after the reaction. May be significantly different.
- those insoluble in a dispersion liquid such as water can be selected.
- an ionic liquid that does not substantially dissolve the dispersion medium of the dispersion liquid is added to the dispersion liquid containing the fine particles, and the fine particles are taken into the ionic liquid from the dispersion liquid, and
- the ionic liquid to be added to the dispersion containing the fine particles is in an amount such that at least a / b becomes 0.05 with respect to the 1 OmL dispersion containing the fine particles in a concentration of a mM.
- a method for concentrating the fine particle-containing dispersion (4) more preferably the method for concentrating the fine particle-containing dispersion according to (3) above, wherein the ionic liquid is an organic ionizable liquid, and still more preferably (4) The method for concentrating a fine particle-containing dispersion according to the above (4), wherein the organic ionizable liquid is selected from the group of compounds represented by the following formula 1. [Dish 4 n H 4 _ n ] +1
- R 3 and R 4 are a C 17 alkyl group, n is an integer of 13 and is a C 1-7 alkyl group which may have a substituent,
- a known ionic liquid can be basically used. Among them, considering the problem of energy consumption, it is a liquid at room temperature, and it can be considered to recover fine particles after concentration. If the viscosity is as low as possible, or if the viscosity is high, add a solvent such as ether to make it less viscous and filter.
- ionic liquids those described in the above formula 1 can be mentioned, and most preferably, the imidazolium-based organic ionic liquid represented by b in the above formula 1 is used. Liquids may be mentioned.
- the amount b (m L) of the ionic liquid to be added depends on the ratio a / to the concentration a (mM) of the fine particles in the fine particle dispersion medium.
- concentration is slightly affected by the concentration of the microparticles, the concentration of fine particles can be concentrated if the concentration of the dispersion is from 0.01 mM or more at room temperature to less than 100 ° C and 0.067 or more. Is acceptable And preferably 1 or less. However, this is not the case if it is not an aqueous dispersion.
- the ionic liquid is separated, and the ionic liquid is separated using a known filtration membrane, for example, JP-A-10-57784. Just do it.
- the fine particles to be concentrated according to the present invention refer to particles having a particle size in the order of nanometers to several tens of micrometers, for example, 20 micrometers.
- it can be applied to pigments, metals, semiconductors, polymers, etc., and can also be applied to the case where the fine particles have a composite structure or the case of a system having a plurality of components.
- this method cannot be applied to materials containing a material that is soluble in ionic liquids as a constituent material of fine particles.
- a filtration method such as using a filtration membrane for the fine particles can be considered.
- the ionic liquid has a low viscosity, for example, it is conceivable that the viscosity is reduced by adding an appropriate organic solvent or the like, followed by filtration and separation.
- DCHD 1,6-Gee (N-force rubazoyl)-2,4-Hexazine
- 1,6-Di- (N-caproluvazoyl)-2,4-hexazine (abbreviated as DCHD) using a reprecipitation method followed by concentration / dilution operations to obtain a poly (100 nm).
- Aqueous blue dispersions containing acetylene microparticles in various concentrations (0.0 mM, 0.1 mM, 0.5 mM) were prepared.
- 10 mL of the dispersion is collected in a sample bottle, and 5 to 10 drops (approximately 0.01 mL) of an ionic liquid are added thereto as an aggregation promoter. The operation of mixing vigorously was repeated.
- Perylene nanoparticles (approximately 150 nm in size, several micrometer fibers) in 0.1 mM by reprecipitation
- An aqueous dispersion was prepared. After collecting 10 mL of the dispersion in a sample bottle and setting it to different temperature conditions (5 ° C, 18 ° C, and 80 ° C), the ionic liquid was used as an aggregation promoter in the sample. 5-10 drops (approximately 1 drop of O.O lm L) were added, and the operation of intense mixing was repeated. The amount of ionic liquid droplets colored yellow appeared at the bottom of the bottle, and the amount required for confirming phase separation was different. At high temperatures, the amount tended to increase.
- the ionic liquid is used as an aggregation promoter in 1 O mL of cyclohexane dispersion containing 2.0% by weight of polyimide (size: about 250 nm) particles.
- 0.15 mL or more of the ionic liquid is added, phase separation occurs, and colored ionic liquid droplets appear at the bottom of the bottle.
- the addition amount of the ionic liquid necessary for complete recovery was larger than that of the aqueous system, and was about 1.5 mL. Before and after this operation, no change was observed in the shape and light absorption characteristics of the fine particles.
- the dilute dispersion has the excellent effect of allowing fine particles to be concentrated in an ionic liquid very efficiently, making it a promising commercial concentration technology.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
- Colloid Chemistry (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
Description
Claims
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US10/548,407 US7732494B2 (en) | 2003-03-27 | 2003-08-04 | Method of concentrating fine particle dispersion and method of recovering fine particle |
| EP03816457A EP1623751A4 (en) | 2003-03-27 | 2003-08-04 | METHOD FOR CONCENTRATING DISPERSITION OF FINE PARTICLES AND METHOD FOR RECOVERING FINE PARTICLES |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2003086924A JP4275976B2 (ja) | 2003-03-27 | 2003-03-27 | 微粒子含有分散液の濃縮法および微粒子回収方法 |
| JP2003-86924 | 2003-03-27 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2004085030A1 true WO2004085030A1 (ja) | 2004-10-07 |
Family
ID=33095082
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP2003/009875 Ceased WO2004085030A1 (ja) | 2003-03-27 | 2003-08-04 | 微粒子含有分散液の濃縮法および微粒子回収方法 |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US7732494B2 (ja) |
| EP (1) | EP1623751A4 (ja) |
| JP (1) | JP4275976B2 (ja) |
| CN (1) | CN100415342C (ja) |
| WO (1) | WO2004085030A1 (ja) |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102004024000A1 (de) * | 2004-05-14 | 2005-12-08 | Clariant Gmbh | Nachbehandlung von Pigmenten in ionischen Flüssigkeiten |
| JP4669754B2 (ja) * | 2005-03-09 | 2011-04-13 | 富士フイルム株式会社 | 色素組成物、および染色方法 |
| WO2006103946A1 (ja) * | 2005-03-25 | 2006-10-05 | Sharp Kabushiki Kaisha | イオン性着色液体及びこれを用いた画像表示装置 |
| JP4870383B2 (ja) * | 2005-05-06 | 2012-02-08 | 富士フイルム株式会社 | ナノ粒子の濃縮方法 |
| JP4993875B2 (ja) * | 2005-05-06 | 2012-08-08 | 富士フイルム株式会社 | 凝集ナノ粒子の分散方法 |
| US8679341B2 (en) | 2005-05-06 | 2014-03-25 | Fujifilm Corporation | Method of concentrating nanoparticles and method of deaggregating aggregated nanoparticles |
| US8283395B2 (en) | 2005-05-09 | 2012-10-09 | Fujifilm Corporation | Method of producing organic-particles-dispersion liquid |
| WO2006132308A1 (ja) * | 2005-06-10 | 2006-12-14 | Bridgestone Corporation | 超微粒子又は超微粒子集合体の製造方法 |
| WO2007083431A1 (ja) | 2006-01-23 | 2007-07-26 | Fujifilm Corporation | 有機ナノ粒子の製造方法、それにより得られる有機ナノ粒子、それを含むカラーフィルタ用インクジェットインク、着色感光性樹脂組成物、および感光性樹脂転写材料、ならびにそれらを用いたカラーフィルタ、液晶表示装置、およびccdデバイス |
| JP5180007B2 (ja) * | 2007-08-31 | 2013-04-10 | 国立大学法人東北大学 | イオン性液体を用いた機能性ポリマー微粒子の製造方法 |
| CA2754117C (en) | 2009-03-20 | 2015-09-15 | Bomi P. Framroze | Improving the recovery of precious metals from recalcitrant refractory ore |
| US8784663B2 (en) * | 2009-11-20 | 2014-07-22 | Nokia Corporation | Trapping nanostructures |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH1057784A (ja) | 1996-08-16 | 1998-03-03 | Noritake Co Ltd | ゼオライト分離膜及びその製造方法 |
| JPH11349316A (ja) * | 1998-06-04 | 1999-12-21 | Ishizuka Kenkyusho:Kk | 水性媒質から懸濁ダイヤモンド微細粒子を回収する方法 |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB9407920D0 (en) * | 1994-04-21 | 1994-06-15 | British Nuclear Fuels Plc | Solvent extraction |
| US5683574A (en) * | 1994-08-08 | 1997-11-04 | Chevron U.S.A. Inc. | Method for the extraction of low molecular weight mercaptans from petroleum and gas condensates |
| US6339182B1 (en) * | 2000-06-20 | 2002-01-15 | Chevron U.S.A. Inc. | Separation of olefins from paraffins using ionic liquid solutions |
| CA2426770A1 (en) * | 2000-10-26 | 2002-05-02 | Laura C. Boudreau | Removal of mercaptans from hydrocarbon streams using ionic liquids |
-
2003
- 2003-03-27 JP JP2003086924A patent/JP4275976B2/ja not_active Expired - Fee Related
- 2003-08-04 WO PCT/JP2003/009875 patent/WO2004085030A1/ja not_active Ceased
- 2003-08-04 EP EP03816457A patent/EP1623751A4/en not_active Withdrawn
- 2003-08-04 CN CNB038262274A patent/CN100415342C/zh not_active Expired - Fee Related
- 2003-08-04 US US10/548,407 patent/US7732494B2/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH1057784A (ja) | 1996-08-16 | 1998-03-03 | Noritake Co Ltd | ゼオライト分離膜及びその製造方法 |
| JPH11349316A (ja) * | 1998-06-04 | 1999-12-21 | Ishizuka Kenkyusho:Kk | 水性媒質から懸濁ダイヤモンド微細粒子を回収する方法 |
Non-Patent Citations (4)
| Title |
|---|
| BLANCHARD, L.A.; GU, Z.; BRENNECKE, J.F., J.PHHYS. CHEM. B, vol. 105, 2001, pages 2437 - 2444 |
| HIROAKI SASAKI, CHEMICAL, vol. 55, no. 3, 2000, pages 66 - 67 |
| See also references of EP1623751A4 |
| THOMAS WELTON, CHEM. REV., vol. 99, 1999, pages 2071 - 2083 |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2004292632A (ja) | 2004-10-21 |
| EP1623751A4 (en) | 2008-07-23 |
| EP1623751A1 (en) | 2006-02-08 |
| US7732494B2 (en) | 2010-06-08 |
| CN100415342C (zh) | 2008-09-03 |
| US20060107793A1 (en) | 2006-05-25 |
| JP4275976B2 (ja) | 2009-06-10 |
| CN1758945A (zh) | 2006-04-12 |
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