CN101704529B - Method for preparing amphiphilic nano silica powder and method for preparing Pickering emulsion using same - Google Patents

Method for preparing amphiphilic nano silica powder and method for preparing Pickering emulsion using same Download PDF

Info

Publication number
CN101704529B
CN101704529B CN2009102186771A CN200910218677A CN101704529B CN 101704529 B CN101704529 B CN 101704529B CN 2009102186771 A CN2009102186771 A CN 2009102186771A CN 200910218677 A CN200910218677 A CN 200910218677A CN 101704529 B CN101704529 B CN 101704529B
Authority
CN
China
Prior art keywords
powder
oil
water
amphiphilic nano
silica powder
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.)
Expired - Fee Related
Application number
CN2009102186771A
Other languages
Chinese (zh)
Other versions
CN101704529A (en
Inventor
范晓东
张卫红
田威
范伟伟
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Northwestern Polytechnical University
Original Assignee
Northwestern Polytechnical University
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Northwestern Polytechnical University filed Critical Northwestern Polytechnical University
Priority to CN2009102186771A priority Critical patent/CN101704529B/en
Publication of CN101704529A publication Critical patent/CN101704529A/en
Application granted granted Critical
Publication of CN101704529B publication Critical patent/CN101704529B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Silicon Compounds (AREA)
  • Colloid Chemistry (AREA)

Abstract

The invention discloses a method for preparing amphiphilic nano silica powder and is used for preparing nano silica powder with about 90 degrees of a tri-phase contact angle. The method uses ultrasonic preparation, thus having short preparation process; the invention adopts liquid phase modification, thus avoiding processing means such as grinding, calcining and the like which are easy to cause the powder to generate hard particle agglomeration; the invention can prepare better amphiphilic surface (about 90 degrees of tri-phase contact angle) nano silica powder. The invention also discloses a method for preparing Pickering emulsion by using the amphiphilic nano silica powder under the action of ultrasound or cutting, the nano silica powder stably exists in oil-water interface, thus preventing diffused oil (water) droplets to re-agglomerate into big droplets to split phase and stabilizing emulsion. The prepared emulsion can be stored at room temperature without occurrence of demulsification in three months.

Description

The preparation method of amphiphilic nano silica powder and the method that adopts this powder preparing Pickering emulsion
Technical field
The present invention relates to a kind of preparation method's of silicon-dioxide powdery, particularly amphiphilic nano silica powder preparation method.Also relate to the method that adopts this amphiphilic nano silica powder to prepare the Pickering emulsion.
Background technology
The Pickering emulsion often is called as solid (particle) stable form emulsion again, and the key that makes up such New Emulsion is the superfine powder that preparation has preferable amphipathic surface, nanometer SiO 2Powder is owing to nontoxic and have characteristics such as superior stability, reinforcement, thickening property and be fit to be used as stablizer and make up the Pickering emulsion.But general direct synthetic nano silicon contains great amount of hydroxy group and presents strongly hydrophilic owing to the surface, can not form stable Pickering emulsion.
Document 1 " K.Zhang, W.Wu, H.Meng et al.Pickering emulsion polymerization:Preparation ofpolystyrene/nano-SiO 2Composite microspheres with core-shell structure.Powder Technology 190 (2009) 393-400. " disclose a kind of with methyl allyl acyloxypropyl trimethoxysilane (KH570) modified Nano SiO 2Method, the contact angle of gained powder is 38.5 °, only can form the Pickering emulsion under the acidic conditions of pH=3, and stability is not good enough, storing 24h promptly has obvious demixing phenomenon to take place.
Document 2 " publication number is the Chinese invention patent of CN 1724352A " discloses a kind of preparation method of amphiphilic nano silicon dioxide, adopt amphipathic block polyether finishing to prepare amphiphilic nano silica, but need in the whole process of preparation through anion and cation exchange resin handle, repeatedly regulate the pH value, leave standstill, steps such as reaction and ultrafiltration and concentration, consuming time longer, operation easier is also bigger.
Summary of the invention
In order to overcome the nanometer SiO of prior art for preparing 2The deficiency that surface contact angle is little the invention provides a kind of amphiphilic nano SiO 2The preparation method of powder, adopt the liquid phase modification, can avoid grinding, calcining etc. easily makes powder produce the processing means of hard aggregation, by the pH value of control dispersion liquid and the add-on of silane coupling agent, can prepare nano silica powder with about 90 ° of preferable amphipathic surface contact angles.
In order to overcome prior art nanometer SiO 2The deficiency that the Pickering emulsion storage time of preparation is short, the present invention also provides and adopts aforementioned amphiphilic nano SiO 2The method of powder preparing Pickering emulsion, amphiphilic nano SiO 2Powder ultra-sonic dispersion in advance adds oil-based solvent (or water) then according to a certain volume in water (or oil phase), large power supersonic or high speed shear emulsification can make stable O/W (or W/O) type Pickering emulsion.
The technical solution adopted for the present invention to solve the technical problems: a kind of amphiphilic nano SiO 2The preparation method of powder is characterized in comprising the steps:
(a) tetraethoxy, ammoniacal liquor, methyl alcohol were mixed in 1: 2: 30 by volume, ultrasonic reaction 2~5h, ultrasound condition: frequency 30~60KHz, power 200~300W, temperature is controlled at 15 ℃~25 ℃ in the reaction process, obtains the nano silicon dispersion liquid;
(b) get the nano silicon dispersion liquid that step (a) prepares, under pH meter monitoring and magnetic agitation, dropwise add glacial acetic acid, regulating the pH value is 7~7.5, the chain alkyl Trimethoxy silane coupling agent that adds dispersion liquid volume fraction 0.09%~0.15% then, at 70 ℃~90 ℃ following back flow reaction 3~4h, 20000~25000r/min is centrifugal, back dehydrated alcohol ultrasonic cleaning, and then it is centrifugal, ultrasonic cleaning, this step repeats 3~5 times, with gained spawn vacuum-drying 8~10h under 20~40 ℃ of conditions, take out slightly grind amphiphilic nano SiO 2Powder.
The above-mentioned amphiphilic nano SiO of a kind of employing 2Powder is made the method for Pickering emulsion, it is characterized in that may further comprise the steps:
Get amphiphilic nano SiO 2Powder, by powder: the mass/volume ratio of water=1: 100~1: 150 adds in the entry, ultra-sonic dispersion 20~30min, ultrasound condition: frequency 30~60KHz, power 200~300W, again to wherein by oil: the volume ratio of water=1: 10~1: 15 adds oil-based solvent, is that 75~85% ultrasonic cell pulverization machine is pulverized through amplitude, be high speed shear emulsification instrument processing 2~3min of 18000~23000r/min perhaps, promptly get oil-in-water-type Pickering emulsion through rotating speed;
Perhaps get amphiphilic nano SiO 2Powder, press powder: the mass/volume of oil=1: 100~1: 50 is than adding in the oil-based solvent, ultra-sonic dispersion 20~30min, ultrasound condition: frequency 30~60KHz, power 200~300W, again to wherein by water: the volume ratio of oil=1: 7.5~1: 10 adds entry, is that 75~85% ultrasonic cell pulverization machine is pulverized through amplitude, be high speed shear emulsification instrument processing 2~3min of 18000~23000r/min perhaps, promptly get water-in-oil-type Pickering emulsion through rotating speed.
Described oil-based solvent is any of normal heptane, benzene, toluene, propyl carbinol, isopropylcarbinol or ethyl acetate.
The invention has the beneficial effects as follows: adopt ultrasonic preparation nano silica powder, preparation process is short; Adopt the liquid phase modification, avoided grinding, calcining etc. easily to make powder produce the processing means of hard aggregation, only just prepared nano silicon with preferable amphipathic surface (about 90 ° of three-phase contact angles) by the pH value of control dispersion liquid and the add-on of silane coupling agent, gained powder hard aggregation-free reaches nano level easily and disperses under ultrasonication.
Owing to adopt the amphiphilic nano silica powder of contact angle about 90 °, preparation O/W or w/o type Pickering emulsion under ultrasonic or shearing action, nano silica powder is stable is present in water-oil interface, stop dispersive oil (water) droplet to condense once more and be big drop phase-splitting, make emulsion keep stable, deposit under the made emulsion room temperature and do not occur obvious demulsifying phenomenon in 3 months.
Below in conjunction with drawings and Examples the present invention is elaborated.
Description of drawings
Fig. 1 is the prepared nanometer SiO of embodiment 1 2The nanometer SiO of powder and background technology preparation 2Granularity and size-grade distribution laser particle analyzer detect figure.
Fig. 2 is the prepared nanometer SiO of embodiment 2 2The nanometer SiO of powder and background technology preparation 2The laser particle size detected result.
Fig. 3 is the prepared nanometer SiO of embodiment 2 2The nanometer SiO of powder and background technology preparation 2Infrared contrast collection of illustrative plates.
Fig. 4 is the prepared nanometer SiO of embodiment 3 2The nanometer SiO of powder and background technology preparation 2The laser particle size detected result.
Fig. 5 is the prepared nanometer SiO of embodiment 4 2The nanometer SiO of powder and background technology preparation 2The laser particle size detected result.
Embodiment
Embodiment 1: get 20mL tetraethoxy and 200mL methyl alcohol, at frequency 40KHz, shake 5min in the power 250W ultrasonic cleaner; Getting 40mL concentration and be 25% ammoniacal liquor joins in the 400mL methyl alcohol, just be poured into after stirring ultrasonic concussion the methanol solution of tetraethoxy in, at the ultrasonic reaction 3h that continues down, whole process adopts the recirculated water cooling, keep water temperature at 15 ℃, finally can obtain nattier blue nanometer SiO 2Dispersion liquid.Detect through laser particle analyzer, Z-Average (d.nm): 42.8nm, granularity heterogeneity index (PDI) is 0.149, detected result is seen Fig. 1.This dispersion liquid stable in properties deposits at room temperature that particle diameter does not change substantially more than 3 months.
Get above-mentioned nanometer SiO 2Dispersion liquid 100mL, under pH meter monitoring and magnetic agitation, drip glacial acetic acid, regulating dispersion liquid pH value is 7.0, add 0.12mL chain alkyl Trimethoxy silane (WD-10) behind the ultra-sonic dispersion 10min, ultra-sonic dispersion 5min again, then with dispersion liquid at 80 ℃ of following back flow reaction 4h, through 20000r/min high speed centrifugation 15min, remove supernatant liquor and obtain pale blue transparent gel-form modification SiO 2, adding the ultrasonic rinsing 10min of 10mL dehydrated alcohol, recentrifuge and ultrasonic rinsing 3~5 times repeatedly, place vacuum drying oven dry 10h under 20 ℃ to get amphiphilic nano SiO final centrifugal product 2Take out slightly grind amphiphilic nano SiO 2Powder.Granularity and size-grade distribution result are after testing: Z-Average (d.nm): 86.4nm; PDI:0.197 sees Fig. 1.
Getting above-mentioned pressed by powder diameter is
Figure G2009102186771D00031
The thin slice of the about 2mm of thickness, ironed of institute is placed in the transparent vessel, add the whiteruss submergence, about the high 1cm of submergence liquid level, drip water on the subsurface thin slice of paraffin with dropper, treat that drop takes pictures with digital camera immediately after stable on the thin slice, test its three-phase contact angle subsequently, the result is 85 °-90 °.
Get 0.3g amphiphilic nano SiO 2Powder adds in the 30mL water, and (30KHz, 300W) 20min to wherein adding 2mL toluene, pulverize 2min through ultrasonic cell pulverization machine (500W, 85% amplitude) to ultra-sonic dispersion again, can form stable oil-in-water (O/W) type Pickering emulsion.This emulsion property is stable, and demulsifying phenomenon did not appear in 3 months in airtight placement under the room temperature.
Embodiment 2: get 10mL tetraethoxy and 100mL methyl alcohol, at frequency 30KHz, shake 6min in the power 300W ultrasonic cleaner; Getting 20mL concentration and be 26% ammoniacal liquor joins in the 200mL methyl alcohol, just be poured into after stirring ultrasonic concussion the methanol solution of tetraethoxy in, at the ultrasonic reaction 2h that continues down, whole process adopts the recirculated water cooling, keep water temperature at 18 ℃, finally can obtain nattier blue nanometer SiO 2Dispersion liquid.Detect through laser particle analyzer, Z-Average (d.nm): 44.1nm, granularity heterogeneity index (PDI) is 0.157, sees Fig. 2.
Get above-mentioned nanometer SiO 2Dispersion liquid 100mL, under pH meter monitoring and magnetic agitation, drip glacial acetic acid, regulating dispersion liquid pH value is 7.3, add 0.15mL chain alkyl Trimethoxy silane (WD-10) behind the ultra-sonic dispersion 10min, ultra-sonic dispersion 5min again, then with dispersion liquid at 70 ℃ of following back flow reaction 3h, through 25000r/min high speed centrifugation 16min, remove supernatant liquor and obtain pale blue transparent gel-form modification SiO 2, adding the ultrasonic rinsing 10min of 10mL dehydrated alcohol, recentrifuge and ultrasonic rinsing 3~5 times repeatedly, place vacuum drying oven dry 9h under 25 ℃ to get amphiphilic nano SiO final centrifugal product 2Take out slightly grind amphiphilic nano SiO 2Powder.Granularity and size-grade distribution result are after testing: Z-Average (d.nm): 84.6nm; PDI:0.160 sees Fig. 2.SiO before modified powder and the modification 2Carry out infrared spectra respectively and detect, as shown in Figure 3,3400cm -1The place is the hydroxyl peak of planar water and powder surface, 1100cm -1, 800cm -1And 470cm -1Adhere to Si-O-Si skeletal vibration, asymmetric and symmetrical stretching vibration peak separately, be SiO 2Characteristic peak; Different is that after the modification of chain alkyl Trimethoxy silane, modified powder is at 2927cm -1And 2855cm -1Absorption peak has to a certain degree appearred in the place, these two peak correspondences be methylene radical (CH 2) C-H unsymmetrically and symmetrical stretching vibration peak, this shows has alkyl to be attached to powder surface with the form of chemical bond.
Getting above-mentioned pressed by powder diameter is
Figure G2009102186771D00041
The thin slice of the about 2mm of thickness, ironed of institute is placed in the transparent vessel, add the whiteruss submergence, about the high 1cm of submergence liquid level, drip water on the subsurface thin slice of paraffin with dropper, treat that drop takes pictures with digital camera immediately after stable on the thin slice, test its three-phase contact angle subsequently, the result is 90 °-95 °.
Get 0.3g amphiphilic nano SiO 2Powder adds in the 30mL ethyl acetate, and (40KHz, 260W) 24min to wherein adding the 2mL pure water, handle 2min through high speed shear emulsification instrument (23000r/min) to ultra-sonic dispersion again, can form stable water-in-oil (W/O) type Pickering emulsion.
Embodiment 3: get 30mL tetraethoxy and 300mL methyl alcohol, at frequency 60KHz, shake 8min in the power 200W ultrasonic cleaner; Getting 60mL concentration and be 27% ammoniacal liquor joins in the 600mL methyl alcohol, just be poured into after stirring ultrasonic concussion the methanol solution of tetraethoxy in, at the ultrasonic reaction 5h that continues down, whole process adopts the recirculated water cooling, keep water temperature at 21 ℃, finally can obtain nattier blue nanometer SiO 2Dispersion liquid.Detect through laser particle analyzer, Z-Average (d.nm): 43.2nm, granularity heterogeneity index (PDI) is 0.173, sees Fig. 4.
Get above-mentioned nanometer SiO 2Dispersion liquid 100mL, under pH meter monitoring and magnetic agitation, drip glacial acetic acid, regulating dispersion liquid pH value is 7.5, add 0.09mL chain alkyl Trimethoxy silane (WD-10) behind the ultra-sonic dispersion 10min, ultra-sonic dispersion 5min again, then with dispersion liquid at 80 ℃ of following back flow reaction 3.5h, through 21000r/min high speed centrifugation 18min, remove supernatant liquor and obtain pale blue transparent gel-form modification SiO 2, adding the ultrasonic rinsing 10min of 10mL dehydrated alcohol, recentrifuge and ultrasonic rinsing 3~5 times repeatedly, place vacuum drying oven dry 8h under 30 ℃ to get amphiphilic nano SiO final centrifugal product 2Take out slightly grind amphiphilic nano SiO 2Powder.Granularity and size-grade distribution result are after testing: Z-Average (d.nm): 86.6nm; PDI:0.205 sees Fig. 4.
Getting above-mentioned pressed by powder diameter is
Figure G2009102186771D00042
The thin slice of the about 2mm of thickness, ironed of institute is placed in the transparent vessel, add the whiteruss submergence, about the high 1cm of submergence liquid level, drip water on the subsurface thin slice of paraffin with dropper, treat that drop takes pictures with digital camera immediately after stable on the thin slice, test its three-phase contact angle subsequently, the result is 85 °-88 °.
Get 0.1g amphiphilic nano SiO 2Powder adds in the 15mL water, and (50KHz, 220W) 27min to wherein adding the 1.5mL normal heptane, pulverize 3min through ultrasonic cell pulverization machine (500W, 75% amplitude) to ultra-sonic dispersion again, can form stable oil-in-water (O/W) type Pickering emulsion.
Embodiment 4: get 20mL tetraethoxy and 200mL methyl alcohol, at frequency 40KHz, shake 10min in the power 250W ultrasonic cleaner; Getting 40mL concentration and be 28% ammoniacal liquor joins in the 400mL methyl alcohol, just be poured into after stirring ultrasonic concussion the methanol solution of tetraethoxy in, at the ultrasonic reaction 4h that continues down, whole process adopts the recirculated water cooling, keep water temperature at 25 ℃, finally can obtain nattier blue nanometer SiO 2Dispersion liquid.Detect through laser particle analyzer, Z-Average (d.nm): 36.2nm, granularity heterogeneity index (PDI) is 0.162, sees Fig. 5.
Get above-mentioned nanometer SiO 2Dispersion liquid 100mL, under pH meter monitoring and magnetic agitation, drip glacial acetic acid, regulating dispersion liquid pH value is 7.4, add 0.11mL chain alkyl Trimethoxy silane (WD-10) behind the ultra-sonic dispersion 10min, ultra-sonic dispersion 5min again, then with dispersion liquid at 75 ℃ of following back flow reaction 4h, through 23000r/min high speed centrifugation 15min, remove supernatant liquor and obtain pale blue transparent gel-form modification SiO 2, adding the ultrasonic rinsing 10min of 10mL dehydrated alcohol, recentrifuge and ultrasonic rinsing 3~5 times repeatedly, place vacuum drying oven dry 8h under 40 ℃ to get amphiphilic nano SiO final centrifugal product 2Take out slightly grind amphiphilic nano SiO 2Powder.Granularity and size-grade distribution result are after testing: Z-Average (d.nm): 80.4nm; PDI:0.137 sees Fig. 5.
Getting above-mentioned pressed by powder diameter is
Figure G2009102186771D00051
The thin slice of the about 2mm of thickness, ironed of institute is placed in the transparent vessel, add the whiteruss submergence, about the high 1cm of submergence liquid level, drip water on the subsurface thin slice of paraffin with dropper, treat that drop takes pictures with digital camera immediately after stable on the thin slice, test its three-phase contact angle subsequently, the result is 90 °-95 °.
Get 0.3g amphiphilic nano SiO 2Powder adds in the 15mL isopropylcarbinol, and (60KHz, 200W) 30min to wherein adding the 2mL pure water, handle 3min through high speed shear emulsification instrument 23000r/min to ultra-sonic dispersion again, can form stable water-in-oil (W/O) type Pickering emulsion.
In addition, also test with oil-based solvents such as benzene, propyl carbinols respectively, all obtained good effect.

Claims (2)

1. amphiphilic nano SiO 2The preparation method of powder is characterized in that may further comprise the steps:
(a) tetraethoxy, ammoniacal liquor, methyl alcohol were mixed in 1: 2: 30 by volume, ultrasonic reaction 2~5h, ultrasound condition: frequency 30~60KHz, power 200~300W, temperature is controlled at 15 ℃~25 ℃ in the reaction process, obtains the nano silicon dispersion liquid;
(b) get the nano silicon dispersion liquid that step (a) prepares, under pH meter monitoring and magnetic agitation, dropwise add glacial acetic acid, regulating the pH value is 7~7.5, the chain alkyl Trimethoxy silane coupling agent that adds dispersion liquid volume fraction 0.09%~0.15% then, at 70 ℃~90 ℃ following back flow reaction 3~4h, 20000~25000r/min is centrifugal, back dehydrated alcohol ultrasonic cleaning, and then it is centrifugal, ultrasonic cleaning, this step repeats 3~5 times, with gained spawn vacuum-drying 8~10h under 20~40 ℃ of conditions, take out slightly grind amphiphilic nano SiO 2Powder.
2. one kind is adopted the described amphiphilic nano SiO of claim 1 2The prepared amphiphilic nano SiO of the preparation method of powder 2Powder is made the method for Pickering emulsion, it is characterized in that may further comprise the steps:
Get amphiphilic nano SiO 2Powder, by powder: the mass/volume ratio of water=1: 100~1: 150 adds in the entry, ultra-sonic dispersion 20~30min, ultrasound condition: frequency 30~60KHz, power 200~300W, again to wherein by oil: the volume ratio of water=1: 10~1: 15 adds oil-based solvent, is that 75~85% ultrasonic cell pulverization machine is pulverized through amplitude, be high speed shear emulsification instrument processing 2~3min of 18000~23000r/min perhaps, promptly get oil-in-water-type Pickering emulsion through rotating speed;
Perhaps get amphiphilic nano SiO 2Powder, press powder: the mass/volume of oil=1: 100~1: 50 is than adding in the oil-based solvent, ultra-sonic dispersion 20~30min, ultrasound condition: frequency 30~60KHz, power 200~300W, again to wherein by water: the volume ratio of oil=1: 7.5~1: 10 adds entry, is that 75~85% ultrasonic cell pulverization machine is pulverized through amplitude, be high speed shear emulsification instrument processing 2~3min of 18000~23000r/min perhaps, promptly get water-in-oil-type Pickering emulsion through rotating speed;
Described oil-based solvent is any of normal heptane, benzene, toluene, propyl carbinol, isopropylcarbinol or ethyl acetate.
CN2009102186771A 2009-11-05 2009-11-05 Method for preparing amphiphilic nano silica powder and method for preparing Pickering emulsion using same Expired - Fee Related CN101704529B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2009102186771A CN101704529B (en) 2009-11-05 2009-11-05 Method for preparing amphiphilic nano silica powder and method for preparing Pickering emulsion using same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2009102186771A CN101704529B (en) 2009-11-05 2009-11-05 Method for preparing amphiphilic nano silica powder and method for preparing Pickering emulsion using same

Publications (2)

Publication Number Publication Date
CN101704529A CN101704529A (en) 2010-05-12
CN101704529B true CN101704529B (en) 2011-06-22

Family

ID=42374800

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2009102186771A Expired - Fee Related CN101704529B (en) 2009-11-05 2009-11-05 Method for preparing amphiphilic nano silica powder and method for preparing Pickering emulsion using same

Country Status (1)

Country Link
CN (1) CN101704529B (en)

Families Citing this family (28)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102874822B (en) * 2012-10-24 2015-09-23 河南安彩高科股份有限公司 A kind of silicon dioxide gel, its method for making and application
JP5778873B2 (en) * 2012-12-07 2015-09-16 富士フイルム株式会社 Image processing apparatus, image processing method and program, and recording medium
US20140242016A1 (en) * 2013-02-22 2014-08-28 Stiefel Laboratories, Inc. Non-aqueous solid stabilized emulsions
CN106103393A (en) * 2013-04-12 2016-11-09 罗地亚经营管理公司 The hydrolysis of ester compounds
CN103529068B (en) * 2013-10-11 2016-08-17 西北工业大学 The dynamic monitoring method that environment-responsive macromolecule hydrophobe is changed by low field nuclear-magnetism technology
CN103721584B (en) * 2013-12-16 2015-08-19 三棵树涂料股份有限公司 A kind of preparation method of silicone oil pickering emulsion
CN104016361B (en) * 2014-05-16 2017-06-23 三棵树涂料股份有限公司 The preparation method of amphiphilic nanoparticles and its application in Pickering emulsions are prepared
CN104525061B (en) * 2014-11-07 2016-08-24 陕西师范大学 Based on ionic liquid and the magnetic responsiveness pickering emulsion of amphipathic Fe3O4 nano particle
CN104801213B (en) * 2015-03-07 2018-05-29 中石化石油工程技术服务有限公司 A kind of Pickering emulsion preparation methods of high viscous high stable
CN104947229B (en) * 2015-07-02 2017-05-03 武汉工程大学 Method for preparing medicine-carrying nanofibers of core-shell structure by virtue of Pickering emulsion electrospinning
CN105086556A (en) * 2015-08-11 2015-11-25 陈曦 Preparation method of nanometer particles used for anti-corrosion coating
CN105802465B (en) * 2016-03-31 2018-05-11 武汉理工大学 A kind of super-hydrophobic coating material and preparation method thereof
CN107412193A (en) * 2017-03-29 2017-12-01 华南理工大学 Nano hybridization pharmaceutical carrier and its preparation method prepared by the Pickering emulsion template methods using magadiite as emulsifying agent
CN107417922B (en) * 2017-05-08 2020-07-14 苏州科技大学 Polymer mixed graft modified magnetic nano-silica and application thereof
US11225613B2 (en) * 2017-05-08 2022-01-18 Solvay Sa Process for removing sulfur compounds from a liquid composition
CN107140651B (en) * 2017-05-25 2020-01-14 海南大学 High-viscoelasticity Pickering emulsion and preparation method and application thereof
CN107130428B (en) * 2017-06-15 2019-02-01 东华大学 A kind of superhydrophobic fabric and preparation method thereof
CN107287181B (en) * 2017-07-25 2020-11-10 山西大学 Method for applying Pickering emulsion immobilized enzyme to fixed bed continuous reaction
CN107399740B (en) * 2017-09-01 2020-03-24 东北石油大学 Fluorinated amphiphilic nano-particles and application thereof
CN107970230B (en) * 2017-11-10 2020-04-28 华南理工大学 Pickering emulsion capable of collapsing and inhibiting generation of bacterial biofilm and preparation and application thereof
CN107868258B (en) * 2017-12-13 2020-04-28 齐鲁工业大学 Method for separating and extracting lignin in wood chip prehydrolysis liquid through temperature-sensitive emulsion membrane
CN108070368B (en) * 2018-01-18 2020-09-29 中国石油大学(华东) Self-emulsifying emulsion and preparation method thereof
CN109666455A (en) * 2019-01-16 2019-04-23 中国海洋大学 The preparation method of amphipathic silica solid particle base marine oil spill dispersing agent
CN111440533B (en) * 2020-04-22 2021-06-22 复旦大学 Pickering emulsification preparation method of high-performance single-component invisible skin coating liquid
CN111632405B (en) * 2020-05-28 2021-10-22 清华大学 Oil-water separation method based on magnetic Janus particles
CN112662256B (en) * 2020-12-18 2022-09-09 上海奇想青晨新材料科技股份有限公司 Nano-modified water-based acrylic resin and preparation method thereof
CN114316916A (en) * 2021-12-15 2022-04-12 西安建筑科技大学 Double-layer nano oxide coated inorganic hydrous salt phase change material and preparation method thereof
CN115318335A (en) * 2022-08-22 2022-11-11 中节能工程技术研究院有限公司 Magnetic TiO 2 Preparation method of Pickering photocatalyst

Also Published As

Publication number Publication date
CN101704529A (en) 2010-05-12

Similar Documents

Publication Publication Date Title
CN101704529B (en) Method for preparing amphiphilic nano silica powder and method for preparing Pickering emulsion using same
CN105944581B (en) A kind of anion responsiveness Pickering lotion and its preparation method and application
CN104525174B (en) A kind of method preparing graphene-based composite based on graphene oxide self assembly
CN107236150B (en) A kind of graphene-supported SiO 2 hybrid filler and preparation method thereof, application
US20080311398A1 (en) Aerogel Particles and Methods Of Making Same
CN105879719B (en) A kind of silicon rubber based on emulsion film forming/silica infiltrating and vaporizing membrane environment-friendly preparation method thereof
CN105579566A (en) Oil extraction aids in grain processing
CN105819432B (en) A kind of method for preparing high-quality graphene material
CN108070368B (en) Self-emulsifying emulsion and preparation method thereof
CN103964448A (en) Method for preparing monodisperse silicon dioxide nanoparticle sol for paint
CN105819497B (en) Preparation method of tin dioxide nanoparticles
CN102795630B (en) Method for preparing silicon dioxide by using reverse micro-emulsion method
CN107879348A (en) A kind of preparation method of the monodisperse silica nanosphere of novel green
CN110371992B (en) Method for synthesizing monodisperse silicon dioxide spheres by regulating microemulsion, and product and application thereof
CN106861450B (en) A kind of preparation of biomass emulsion seperation film and the application in the separation of selective lotion
CN101857699B (en) Method for preparing organic-inorganic composite microspheres with eccentric structure
CN114574184A (en) Nano oil displacement agent based on oil-rock interaction destruction and preparation method and application thereof
CN107501853A (en) A kind of functionalization redox graphene phenol-formaldehyde resin modified and preparation method thereof
CN105038753B (en) A kind of foaming agent and preparation method and application
Hajduchova et al. Adsorption of dodecylbenzenesulfonic acid on the alumina particles in the preparation of alumina foam
CN104138733B (en) A kind of surface has SiO 2 hollow microsphere running through macropore and preparation method thereof
CN103111208B (en) A kind of solid suspension list distribution emulsion and emulsification method thereof
CN115261003B (en) Amphiphilic Janus sheet material and preparation method and application thereof
Wang et al. Polymerizable allyl anionic and nonionic emulsifier: synthesis and properties of its emulsion for architectural coating
RU61709U1 (en) DEVICE FOR OBTAINING WATER-OIL AND EMULSION BY MECHANICAL MIXING OF OIL, WATER AND EMULSIFIER

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20110622

Termination date: 20131105