CN106955676A - A kind of temperature-responsive water-oil separating foam and preparation method thereof - Google Patents

A kind of temperature-responsive water-oil separating foam and preparation method thereof Download PDF

Info

Publication number
CN106955676A
CN106955676A CN201710162755.5A CN201710162755A CN106955676A CN 106955676 A CN106955676 A CN 106955676A CN 201710162755 A CN201710162755 A CN 201710162755A CN 106955676 A CN106955676 A CN 106955676A
Authority
CN
China
Prior art keywords
water
temperature
oil separating
foam
responsive
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.)
Pending
Application number
CN201710162755.5A
Other languages
Chinese (zh)
Inventor
王朝阳
雷志文
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.)
South China University of Technology SCUT
Original Assignee
South China University of Technology SCUT
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 South China University of Technology SCUT filed Critical South China University of Technology SCUT
Priority to CN201710162755.5A priority Critical patent/CN106955676A/en
Publication of CN106955676A publication Critical patent/CN106955676A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/26Synthetic macromolecular compounds
    • B01J20/265Synthetic macromolecular compounds modified or post-treated polymers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28014Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
    • B01J20/28042Shaped bodies; Monolithic structures
    • B01J20/28045Honeycomb or cellular structures; Solid foams or sponges
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/285Treatment of water, waste water, or sewage by sorption using synthetic organic sorbents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/16Regeneration of sorbents, filters

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Analytical Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Abstract

The invention discloses a kind of temperature-responsive water-oil separating foam and preparation method thereof.The water-oil separating foam is using melamine foams as carrier, the poly- N N-isopropylacrylamides of temperature-responsive are grafted on melamine foams surface, the regulatable surface of wettability is formed, changing water contact angle with temperature changes to 155 ° from 0 °, and inside is the loose structure of network interworking.Temperature-responsive water-oil separating foam of the present invention has temperature-responsive sexual function, and super hydrophilic property is can behave as at a lower temperature, superhydrophobic property is can behave as at relatively high temperatures;By regulating and controlling ambient temperature, the hydrophilic and hydrophobic of the water-oil separating foam is controlled, is discharged under water for the separation of oil water mixture and the intelligent pipeline switch control of absorption oil.Operating method of the present invention is simple, and preparation condition is gentle, environmentally friendly.

Description

A kind of temperature-responsive water-oil separating foam and preparation method thereof
Technical field
The invention belongs to perforated foams field, and in particular to a kind of temperature-responsive water-oil separating foam and its preparation Method.
Background technology
Because the wettability of material surface depends on surface chemical composition and surface roughness.Surface chemical composition is determined The hydrophilic and hydrophobic of material, surface roughness expands the performance of close and distant property, and then reaches super close and distant state.
The polymer of current a variety of responses can be covered in the hydrophobe material of material surface formation response.Such as temperature Response (Environ.Sci.Technol.2016,50,906-914), pH responses (ACS Appl.Mater.Interfaces 2016,8,5661-5667), optical Response (Langmuir 2015,31,5962-5969) Deng.
In the material of these hydrophobe responses, the application of temperature-responsive polymer poly NIPA is very Extensively, but the polymer be mainly used at present two dimension material in carry out response water-oil separating (Environ.Sci.Technol.2016,50,906-914)。
Melamine foams, it is cheap and easy to get as three-dimensional porous material, it is preferable modified template;Itself have excellent Elasticity, low-density, high porosity and anti-flammability.The present invention by poly-N-isopropyl acrylamide by being grafted to melamine foams table Face, has obtained the three-dimensional material of the water-oil separating of temperature-responsive.
The content of the invention
Present invention aims at a kind of temperature-responsive water-oil separating foam is provided, the water-oil separating foam is with melamine foams For carrier, surface is grafted poly-N-isopropyl acrylamide by ATRP, forms the regulatable table of wettability Face, changes water contact angle with temperature and 155 ° is changed to from 0 °, inside is the loose structure of network interworking;When temperature is less than 25 DEG C, It is 0 ° that the water-oil separating foam, which is in water contact angle in super hydrophilic state, air,;When temperature is higher than 40 DEG C, the water-oil separating foam Water contact angle is 150 ° in super-hydrophobic state, air;When temperature is higher than 45 DEG C, water contact angle is 155 ° in air.
When environment temperature is higher than 35 DEG C, the oil phase that the water-oil separating foam can be used in absorption effluent divides oil from water Separate out and;The foam of absorption oil is placed in water at low temperature (T<25 DEG C), by slight extruding, adsorbed oil is from foam Discharge;For the foam after oil-water separation processing, water-oil separating can be re-used for after over cleaning, drying.
The object of the invention also resides in a kind of preparation method of temperature-responsive water-oil separating foam described in providing, including such as Lower step:
(1) ultrasonic disperse in toluene by octadecyl trichlorosilane alkane and 3- TSL 8330s, is obtained Even mixed solution;
(2) aqueous melamine foams are added in the mixed solution that step (1) is obtained, impregnation;Take out, washing, Drying;
(3) under ice bath, 2- is added dropwise in the dichloromethane solution of pyridine in the foam impregnation after step (2) is dried dropwise Continue to be reacted under ice-water bath after bromine isobutyl acylbromide, completion of dropping, then normal-temperature reaction 10~12 hours;Take out, wash, do It is dry;
(4) step (3) dried foam is placed in the methanol/water mixed solvent containing NIPA monomer In, lead to nitrogen deoxygenation, add catalyst and complexant, lead to nitrogen deoxygenation, heating response;Foam is taken out, is cleaned, dries, obtains The temperature-responsive water-oil separating foam.
Further, in step (1), the time of the ultrasonic disperse is 1~10min.
Further, in step (1), in obtained mixed solution, the mass concentration of octadecyl trichlorosilane alkane for 0.2~ The mass concentration of 2%, 3- TSL 8330 is 0.2~2%.
Further, in step (2), in the aqueous melamine foams, the quality of water for melamine foams 10~ 100%.
Further, in step (2), the time of the impregnation is 0.5~5 hour.
Further, in step (2), the washing is successively with toluene and dichloromethane cyclic washing 5 times.
Further, in step (2), the drying is in 60 DEG C of drying.
Further, in step (3), the mass concentration of the dichloromethane solution of the pyridine is 2%.
Further, in step (3), the mass ratio of the 2- bromine isobutyl acylbromides and melamine foams is 1:1~5:1.
Further, in step (3), drip after 2- bromine isobutyl acylbromides, the time for continuing to react under ice-water bath is small for 1 When.
Further, in step (3), the washing is successively with dichloromethane and acetone cyclic washing 5 times.
Further, in step (3), the drying is dry in a nitrogen atmosphere.
Further, in step (4), in the methanol/water mixed solvent, the volume ratio of methanol and water is 1:1, N- isopropyl The concentration of base acrylamide monomer is 0.02~0.05g/mL.
Further, in step (4), the mass ratio of the NIPA monomer and melamine foams is 10:1~ 15:1。
Further, in step (4), the catalyst is CuBr, and catalyst CuBr quality is N- isopropyl acrylamides The 2~6% of amine monomers.
Further, in step (4), the complexant is PMDETA, complexant pentamethyl divinyl The quality of base triamine is the 30~40% of NIPA monomer.
Further, in step (4), the heating response is reacted 1~10 hour at 60 DEG C.
Further, in step (4), the cleaning is cleaned with deionized water.
Further, in step (4), the drying is dry in a nitrogen atmosphere.
Compared with prior art, the invention has the advantages that and beneficial effect:
(1) temperature-responsive water-oil separating foam of the present invention has temperature-responsive sexual function, (is less than 25 in lower temperature DEG C) under can behave as super hydrophilic property, can behave as superhydrophobic property under higher temperature (be higher than 40 DEG C);It is extraneous by regulating and controlling Temperature, controls the hydrophilic and hydrophobic of the water-oil separating foam, is opened for the separation of oil water mixture and the intelligent pipeline of absorption oil Control is closed to discharge under water;
(2) temperature-responsive water-oil separating foam surface of the present invention has been grafted temperature-responsive polymer N- isopropyl propylene Acid amides, forms the regulatable surface of wettability, and changing with temperature can realize water contact angle in 0~155 ° of range;
(3) temperature-responsive water-oil separating foam of the present invention, carries out water-oil separating and oil by way of temperature-responsive Reclaim, can not only reduce energy consumption using ambient temperature well, and can effectively improve the rate of recovery for being adsorbed oil, And the foam handled for water-oil separating can be re-used for water-oil separating after over cleaning, drying;
(4) preparation method of the present invention is simple, and preparation condition is gentle, environmentally friendly.
Brief description of the drawings
Fig. 1 is the scanning electron microscope (SEM) photograph of temperature-responsive water-oil separating foam prepared by embodiment 1.
Embodiment
With reference to embodiment and accompanying drawing, the present invention is described in further detail, but embodiments of the present invention are not limited In this.Other it is any without departing from Spirit Essences and the change made under principle of the present invention, modification, replacement, combine, simplification, Equivalent substitute mode is should be, is included within protection scope of the present invention.
Embodiment 1
A kind of preparation of temperature-responsive water-oil separating melamine base foam, comprises the following steps:
(1) by octadecyl trichlorosilane alkane (30 μ L) and 3- TSL 8330s (20 μ L) at toluene (10mL) In organic solvent, ultrasonic disperse 2min forms uniform mixed solution;
(2) by melamine foams and mass fraction containing 16mg be its 20% water into the mixed solution of step (1), react After 1h, foam is taken out, is cleaned repeatedly with toluene and dichloromethane solvent successively 5 times, 60 DEG C of drying;
(3) foam for drying step (2) is placed in 10mL anhydrous methylene chlorides (anhydrous pyridine containing 0.2mL), in 0 DEG C of bar Under part, it is added dropwise dropwise after 50mg 2- bromine isobutyl acylbromides, completion of dropping and continues to react after 1h under ice-water bath, be placed under normal temperature anti- Answer 12h;Foam is taken out, cleaned repeatedly 5 times with dichloromethane and acetone successively, is dried in nitrogen atmosphere;
(4) foam for obtaining step (3) is placed in the methanol/water (first containing monomer NIPA (0.2g) Alcohol:Water=1:1v/v) (5mL) in solution, lead to nitrogen degasification, add catalyst CuBr (8mg) and complexant pentamethyl divinyl Base triamine (70mg), leads at nitrogen degasification, 60 DEG C and reacts after 1.5h, cleaned by deionized water, dry, obtain under nitrogen atmosphere The temperature-responsive water-oil separating foam.
The scanning electron microscope (SEM) photograph of obtained temperature-responsive water-oil separating foam is as shown in figure 1, as shown in Figure 1, melamine foams Surface by a tunic in addition to being covered, and also part surface is covered by the polymerized segment of nano-scale, and these segments are temperature Spend responsive polymer poly-N-isopropyl acrylamide.
Embodiment 2
A kind of preparation of temperature-responsive water-oil separating melamine base foam, comprises the following steps:
(1) by octadecyl trichlorosilane alkane (30 μ L) and 3- TSL 8330s (30 μ L) at toluene (10mL) In organic solvent, ultrasonic disperse 1min forms uniform mixed solution;
(2) melamine foams and mass fraction containing 16mg are added in the mixed solution of step (1) for its 30% water, React after 1.5h, foam is taken out, cleaned repeatedly with toluene and dichloromethane solvent successively 5 times, 60 DEG C of drying;
(3) foam for drying step (2) is placed in 10mL anhydrous methylene chlorides (anhydrous pyridine containing 0.2mL), in 0 DEG C of bar Under part, it is added dropwise dropwise after 16mg 2- bromine isobutyl acylbromides, completion of dropping and continues to react after 1h under ice-water bath, be placed under normal temperature anti- Answer 10h;Foam is taken out, cleaned repeatedly 5 times with dichloromethane and acetone, is dried in nitrogen atmosphere;
(4) foam for obtaining step (3) is placed in the methanol/water (first containing monomer NIPA (0.16g) Alcohol:Water=1:1v/v) (5mL) in solution, lead to nitrogen degasification, add catalyst CuBr (4mg) and complexant pentamethyl divinyl Base triamine (60mg), leads at nitrogen degasification, 60 DEG C and reacts after 2h, cleaned by deionized water, dried under nitrogen atmosphere, obtain institute State temperature-responsive water-oil separating foam.
Obtained temperature-responsive water-oil separating foam surface is reference can be made to Fig. 1.
Embodiment 3
A kind of preparation of temperature-responsive water-oil separating melamine base foam, comprises the following steps:
(1) by octadecyl trichlorosilane alkane (50 μ L) and 3- TSL 8330s (20 μ L) at toluene (10mL) In organic solvent, ultrasonic disperse 3min forms uniform mixed solution;
(2) it is the mixed solution that its 15% water is added to step (1) by the melamine foams containing 16mg and its mass fraction, React after 3h, foam is taken out, cleaned repeatedly with toluene and dichloromethane solvent successively 5 times, 60 DEG C of drying;
(3) foam for drying step (2) is placed in 10mL anhydrous methylene chlorides (anhydrous pyridine containing 0.2mL), in 0 DEG C of bar Under part, it is added dropwise dropwise after 90mg 2- bromine isobutyl acylbromides, completion of dropping and continues to react after 1h under ice-water bath, be placed under normal temperature anti- Answer 11h;Foam is taken out, cleaned repeatedly 5 times with dichloromethane and acetone successively, is dried in nitrogen atmosphere;
(4) foam for obtaining step (3) is placed in the methanol/water (first containing monomer NIPA (0.24g) Alcohol:Water=1:1v/v) (8mL) in solution, lead to nitrogen degasification, add catalyst CuBr (12mg) and complexant pentamethyl divinyl Base triamine (90mg), leads at nitrogen degasification, 60 DEG C and reacts after 4h, cleaned by deionized water, dried under nitrogen atmosphere, obtain institute State temperature-responsive water-oil separating foam.
Obtained temperature-responsive water-oil separating foam surface is reference can be made to Fig. 1.
Embodiment 4
A kind of preparation of temperature-responsive water-oil separating melamine base foam, comprises the following steps:
(1) by octadecyl trichlorosilane alkane (200 μ L) and 3- TSL 8330s (200 μ L) in toluene In (10mL) organic solvent, ultrasonic disperse 10min forms uniform mixed solution;
(2) it is the melamine foams containing 16mg and its mass fraction are molten for the mixing that its 100% water is added to step (1) After liquid, reaction 5h, foam is taken out, cleaned repeatedly with toluene and dichloromethane solvent successively 5 times, 60 DEG C of drying;
(3) foam for drying step (2) is placed in 10mL anhydrous methylene chlorides (anhydrous pyridine containing 0.2mL), in 0 DEG C of bar Under part, it is added dropwise dropwise after 60mg 2- bromine isobutyl acylbromides, completion of dropping and continues to react after 1h under ice-water bath, be placed under normal temperature anti- Answer 12h;Foam is taken out, cleaned repeatedly 5 times with dichloromethane and acetone successively, is dried in nitrogen atmosphere;
(4) foam for obtaining step (3) is placed in the methanol/water (first containing monomer NIPA (0.2g) Alcohol:Water=1:1v/v) (10mL) in solution, lead to nitrogen degasification, add catalyst CuBr (8mg) and complexant pentamethyl divinyl Base triamine (70mg), leads at nitrogen degasification, 60 DEG C and reacts after 10h, cleaned by deionized water, dry, obtain under nitrogen atmosphere The temperature-responsive water-oil separating foam.
Obtained temperature-responsive water-oil separating foam surface is reference can be made to Fig. 1.
Embodiment 5
A kind of preparation of temperature-responsive water-oil separating melamine base foam, comprises the following steps:
(1) by octadecyl trichlorosilane alkane (20 μ L) and 3- TSL 8330s (20 μ L) at toluene (10mL) In organic solvent, ultrasonic disperse 1min forms uniform mixed solution;
(2) it is the mixed solution that its 10% water is added to step (1) by the melamine foams containing 16mg and its mass fraction, React after 0.5h, foam is taken out, cleaned repeatedly with toluene and dichloromethane solvent successively 5 times, 60 DEG C of drying;
(3) foam for drying step (2) is placed in 10mL anhydrous methylene chlorides (anhydrous pyridine containing 0.2mL), in 0 DEG C of bar Under part, it is added dropwise dropwise after 30mg 2- bromine isobutyl acylbromides, completion of dropping and continues to react after 1h under ice-water bath, be placed under normal temperature anti- Answer 12h;Foam is taken out, cleaned repeatedly 5 times with dichloromethane and acetone successively, is dried in nitrogen atmosphere;
(4) foam for obtaining step (3) is placed in the methanol/water (first containing monomer NIPA (0.2g) Alcohol:Water=1:1v/v) (4mL) in solution, lead to nitrogen degasification, add catalyst CuBr (8mg) and complexant pentamethyl divinyl Base triamine (70mg), leads at nitrogen degasification, 60 DEG C and reacts after 1h, cleaned by deionized water, dried under nitrogen atmosphere, obtain institute State temperature-responsive water-oil separating foam.
Obtained temperature-responsive water-oil separating foam surface is reference can be made to Fig. 1.
The performance of the temperature-responsive water-oil separating foam of the gained of embodiment 1~5:When environment temperature is less than 25 DEG C, foam In super hydrophilic state (water contact angle is 0 ° in its air);When environment temperature is higher than 40 DEG C, foam is in super-hydrophobic state (water contact angle is 150 ° in its air);When temperature is higher than 45 DEG C, water contact angle is 155 ° in air.When environment temperature is higher than 35 DEG C, prepare the oil phase that foam can be used in absorption effluent and be separated from the water out by oil;The foam for adsorbing oil is placed in low temperature (T in water<25 DEG C), by slight extruding, adsorbed oily almost all is discharged from foam.After water-oil separating Foam through over cleaning, can be re-used for water-oil separating after drying.It is this carried out by way of temperature-responsive water-oil separating and The recovery of oil can not only reduce energy consumption using ambient temperature well, and can effectively improve the recovery for being adsorbed oil Rate.

Claims (9)

1. a kind of temperature-responsive water-oil separating foam, it is characterised in that using melamine foams as carrier, surface grafting temperature sound Answering property polymer NIPA, forms the regulatable surface of wettability, and water contact angle is changed from 0 ° of change with temperature To 155 °, inside is the loose structure of network interworking.
2. a kind of temperature-responsive water-oil separating foam according to claim 1, it is characterised in that temperature is less than 25 DEG C When, it is 0 ° that the water-oil separating foam, which is in water contact angle in super hydrophilic state, air,;When temperature is higher than 40 DEG C, the water-oil separating It is 150 ° that foam, which is in water contact angle in super-hydrophobic state, air,;When temperature is higher than 45 DEG C, water contact angle is 155 ° in air.
3. a kind of preparation method of temperature-responsive water-oil separating foam described in claim 1 or 2, it is characterised in that including Following steps:
(1) ultrasonic disperse in toluene by octadecyl trichlorosilane alkane and 3- TSL 8330s, obtains uniform Mixed solution;
(2) aqueous melamine foams are added in the mixed solution that step (1) is obtained, impregnation;Take out, wash, drying;
(3) foam impregnation after step (2) is dried is in the dichloromethane solution of pyridine, under ice bath, 2- bromines is added dropwise dropwise different Continue to be reacted under ice-water bath after butyryl bromide, completion of dropping, then normal-temperature reaction 10~12 hours;Take out, wash, dry;
(4) step (3) dried foam is placed in the methanol/water mixed solvent containing NIPA monomer, Logical nitrogen deoxygenation, adds catalyst and complexant, leads to nitrogen deoxygenation, heating response;Foam is taken out, is cleaned, is dried, obtains described Temperature-responsive water-oil separating foam.
4. a kind of preparation method of temperature-responsive water-oil separating foam according to claim 3, it is characterised in that step (1) in, the time of the ultrasonic disperse is 1~10min;In obtained mixed solution, the quality of octadecyl trichlorosilane alkane is dense The mass concentration spent for 0.2~2%, 3- TSL 8330s is 0.2~2%.
5. a kind of preparation method of temperature-responsive water-oil separating foam according to claim 3, it is characterised in that step (2) in, in the aqueous melamine foams, the quality of water is the 10~100% of melamine foams;The time of the impregnation is 0.5~5 hour;The washing is successively with toluene and dichloromethane cyclic washing 5 times;The drying is in 60 DEG C of drying.
6. a kind of preparation method of temperature-responsive water-oil separating foam according to claim 3, it is characterised in that step (3) in, the mass concentration of the dichloromethane solution of the pyridine is 2%;The quality of the 2- bromine isobutyl acylbromides and melamine foams Than for 1:1~5:1;Drip after 2- bromine isobutyl acylbromides, the time for continuing to react under ice-water bath is 1 hour;The washing is Successively with dichloromethane and acetone cyclic washing 5 times;The drying is dry in a nitrogen atmosphere.
7. a kind of preparation method of temperature-responsive water-oil separating foam according to claim 3, it is characterised in that step (4) in, in the methanol/water mixed solvent, the volume ratio of methanol and water is 1:1, the concentration of NIPA monomer For 0.02~0.05g/mL;The mass ratio of the NIPA monomer and melamine foams is 10:1~15:1.
8. a kind of preparation method of temperature-responsive water-oil separating foam according to claim 3, it is characterised in that step (4) in, the catalyst is CuBr, and catalyst CuBr quality is the 2~6% of NIPA monomer;It is described to match somebody with somebody Position agent is PMDETA, and the quality of complexant PMDETA is NIPA monomer 30~40%.
9. a kind of preparation method of temperature-responsive water-oil separating foam according to claim 3, it is characterised in that step (4) in, the heating response is reacted 1~10 hour at 60 DEG C;The cleaning is cleaned with deionized water;The drying is Dry in a nitrogen atmosphere.
CN201710162755.5A 2017-03-18 2017-03-18 A kind of temperature-responsive water-oil separating foam and preparation method thereof Pending CN106955676A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710162755.5A CN106955676A (en) 2017-03-18 2017-03-18 A kind of temperature-responsive water-oil separating foam and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710162755.5A CN106955676A (en) 2017-03-18 2017-03-18 A kind of temperature-responsive water-oil separating foam and preparation method thereof

Publications (1)

Publication Number Publication Date
CN106955676A true CN106955676A (en) 2017-07-18

Family

ID=59470233

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710162755.5A Pending CN106955676A (en) 2017-03-18 2017-03-18 A kind of temperature-responsive water-oil separating foam and preparation method thereof

Country Status (1)

Country Link
CN (1) CN106955676A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111196620A (en) * 2020-01-20 2020-05-26 重庆科技学院 Oil-water separation device and method for treating wastewater in metallurgical industrial process
CN111196621A (en) * 2020-01-20 2020-05-26 重庆科技学院 Foam for treating metallurgical oily wastewater and preparation method thereof
JP2021525880A (en) * 2018-06-06 2021-09-27 ブリンク アーゲー Device for fractionating suspension samples
CN114196066A (en) * 2021-12-06 2022-03-18 南京林业大学 Thermal response type intelligent sponge and preparation method and application thereof

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
ZHIWEN LEI等: "Thermoresponsive Melamine Sponges with Switchable Wettability by Interface-Initiated Atom Transfer Radical Polymerization for Oil/Water Separation", 《ACS APPL. MATER. INTERFACES》 *

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2021525880A (en) * 2018-06-06 2021-09-27 ブリンク アーゲー Device for fractionating suspension samples
CN111196620A (en) * 2020-01-20 2020-05-26 重庆科技学院 Oil-water separation device and method for treating wastewater in metallurgical industrial process
CN111196621A (en) * 2020-01-20 2020-05-26 重庆科技学院 Foam for treating metallurgical oily wastewater and preparation method thereof
CN111196620B (en) * 2020-01-20 2022-04-22 重庆科技学院 Oil-water separation device and method for treating wastewater in metallurgical industrial process
CN114196066A (en) * 2021-12-06 2022-03-18 南京林业大学 Thermal response type intelligent sponge and preparation method and application thereof

Similar Documents

Publication Publication Date Title
CN106955676A (en) A kind of temperature-responsive water-oil separating foam and preparation method thereof
CN104772048B (en) Inorganic-organic hybrid film that a kind of inorganic filler is combined with dopamine and its production and use
CN105621420B (en) A kind of method that aerosil is prepared by foaming
CN105647159B (en) A kind of polymer-base foam material and the preparation method and application thereof of graphene ribbon modification
CN109225121A (en) The preparation method and brine of compound adsorbent propose lithium method
CN110124616B (en) Modified biochar and modification method and application thereof
Huang et al. 2-Methylol-12-crown-4 ether immobilized PolyHIPEs toward recovery of lithium (i)
CN107913677B (en) Nano heavy metal wastewater ion adsorption microspheres and preparation method thereof
CN109776744B (en) Preparation method of amidoxime-silicon dioxide resin for adsorbing gallium
Xiao et al. Electrospinning preparation of β-cyclodextrin/glutaraldehyde crosslinked PVP nanofibrous membranes to adsorb dye in aqueous solution
CN105032203A (en) Preparation method of membrane adsorbent for removing ammonia nitrogen in wastewater
CN104190264B (en) Preparation method for hollow fiber ultrafiltration membrane with chelation function
CN105384832A (en) Preparation technology of crosslinked starch capable of preventing shearing force
Wang et al. Facile synthesis of hierarchical porous solid catalysts with acid–base bifunctional active sites for the conversion of cellulose to 5-hydroxymethylfurfural
CN106824097A (en) The preparation of the mercaptopyrimidine modified magnetic activated carbon sponge material of 4 amino 2
RU2446876C1 (en) Method of producing moulded sorbent
CN103894080B (en) Fill hybridized film and Synthesis and applications that hydrogel microsphere regulates water content in film
CN105418773A (en) Preparation process for crosslinking starch
CN107827108A (en) A kind of pole micro-pore carbon material and preparation method thereof
Yang et al. Dense and superhydrophobic biopolymer-coated large tablet produced with energy efficient UV-curing for controlled-release fertilizer
CN106809835B (en) A method of preparing super-hydrophobic active carbon
CN105418774A (en) Method for preparing crosslinked starch by utilizing sodium trimetaphosphate crosslinking agent
CN116920792A (en) Modified fly ash-based molecular sieve, preparation method and application thereof in gas targeted adsorption
CN110256624A (en) A kind of hypercrosslinked polymeric resin and its application in adsorbing separation 5 hydroxymethyl furfural
CN104445224B (en) A kind of preparation method of fine silicon dioxide aerogel powder

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20170718

RJ01 Rejection of invention patent application after publication