CN1919429A - Graft phenylethene modified film and preparation method and application thereof - Google Patents
Graft phenylethene modified film and preparation method and application thereof Download PDFInfo
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- CN1919429A CN1919429A CN 200510093277 CN200510093277A CN1919429A CN 1919429 A CN1919429 A CN 1919429A CN 200510093277 CN200510093277 CN 200510093277 CN 200510093277 A CN200510093277 A CN 200510093277A CN 1919429 A CN1919429 A CN 1919429A
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Abstract
The invention discloses a grafted phenylethene modified diaphragm and preparing method and application, which comprises the following steps: adopting porous diaphragm as base film, grafting phenylethene monomer on the surface of base film to form porous layer or compact layer, irradiating hyperfilter film at low-temperature plasmid, generating active free base, contacting gas phenylethene monomer with film to graft. The porous base film is polyacrylonitile, polysulfone or polyethersulfone ultrafilter membrane or microfilter membrane.
Description
Technical field
The present invention relates to a kind of macromolecule pellicle separation process technique, particularly a kind of graft phenylethene modified film and preparation and application.
Background technology
The solvent dewaxing process method is mainly used in the dewaxing of modern lube base oil, promptly in the presence of a large amount of selective solvents, with oil plant solution carry out freezing, crystallization, wax separates with the machinery of oil.Technology is used a large amount of solvents, and therefore the about 80%-85% of solvent in the dewaxed oil need effectively recycle solvent.Main at present ketone benzene (butanone, the toluene) solvent that adopts in the triple effect evaporation method recovery dewaxed oil, solvent uses repeatedly through the circulation of dewaxing-evaporation recovery-liquid nitrogen condensation-dewaxing.The dewaxed solution temperature was subzero about 30 ℃ after wax separated with the machinery of oil in this process, reclaim solvent with the triple effect evaporation method, the solvent outlet temperature is about 90～200 ℃, recovered solvent is mixed with oil plant to the normal temperature with water quench, dewaxes to subzero 30 ℃ with liquid nitrogen condensation in the freezing and crystallizing system.Obviously, solvent has consumed lot of energy in the cyclic process of this heating-condensation.
Over nearly 20 years, succeed in developing the recovery that polymeric membrane for separation is used for dewaxing solvent in succession, adopt embrane method to hang down under temperature and directly from lubricating oil dewaxing filtrate, reclaim ketone-benzol solvent, can save fuel oil consumption in the evaporation removal process; Reduced the consumption of condensation process cooling water; Increased the output of lubricating oil; Organic steams such as the toluene that minimizing is volatilized because of heating, butanone have reduced environmental pollution, have excellent economic and social benefit.
Shell Co. Ltd has developed the technology of separating the lubricating oil dewaxing solvent by the modified silicon rubber film, and this film is basement membrane with the porous polyethylene, be dense layer surface with hydroxy-end capped poly-methyl-3 fluoropropyl siloxanes, prepares through coating is compound.At operating pressure is 5.5MPa, and temperature is under 30 ℃, and this film can reclaim 3/4 solvent (EP NO.0,220,753, Bitter, Johan George Albert) to the rejection of lubricating oil greater than 70%, three grade of commercial plant.
U.S. W.R.Grace ﹠amp; Co.-Conn. company has developed asymmetric polyimide film and has reclaimed the dewaxing solvent recovery system, and this film is prepared from by traditional inversion of phases method.At pressure is 4MPa, and under-10 ℃, this film is 96% to the rejection of lubricating oil, can reclaim 50% solvent, and operating cost is saved 2/3 (US4.5,264,166, White et al.).
The patent of U.S. Mobil oil company relates to polyimide film separation of methylbenzene butanone solvent (EP695337-A from dewaxed oil; WO9425543-A; US5360530-A; WO9425543-A1; Au9467113-A; EP695337-A4; JP8508762-W; AU675323-B; SG43673-A1; EP695337-B1; DE69419253-E, Spencer etal.).
EXXON company has also developed the technology of separating dewaxing solvent from dewaxed oil with embrane method, and used film is the asymmetric polyimide film (EP125907 for preparing by phase inversion; JP60035091; EP125907; DE3468432; CA1262880, Wight).
The Pasternak of Texaco Inc. etc. has reported the technology of separating dewaxed oil and dewaxing solvent, the film that adopts is by be coated with the composite membrane that the active layer of building centrifugation prepares on polyacrylonitrile ultrafiltration film, the composite bed that plays centrifugation is respectively synthetic rubber, as polybutadiene (US5240591), polyureas US5146038), cross linking polysiloxane (US5102551) and crosslinked polyimide (US4935138).
Retrieval is the lubricating oil dewaxing ketone-benzol solvent reclamation film document of research and development both at home and abroad, and the film of being reported all belongs to the NF membrane that is prepared by inversion of phases or coating composite algorithm.In the last few years, some research work were modified the film surface by the surface grafting technology, can form new active layer on the film surface, thereby can improve the separating property of film.Ulbricht etc., are exposed in the air, to improve the hydrophilicity of film by helium, the irradiation of water low temperature plasma then to the polyacrylonitrile ultrafiltration film surface; Or after polyacrylonitrile ultrafiltration film and the helium low temperature plasma irradiation of polysulphone super-filter membrane surface, grafting 2-hydroxyl-ethyl-methyl acrylate, acrylic acid, methacrylic acid monomer, make the hydrophily of film strengthen (Journal of Applied Polymer Science, 1995,56 (3): 325-343), the main purpose of modification is to improve the antifouling property of film in water solution system.Employing gas ions modification technologies such as Bryjak have formed film (Environ.Prot.Eng., 1993,19 (1～4), 113-19 (Eng)) as polytetrafluoroethylene (PTFE) at polyacrylonitrile ultrafiltration film surface deposition perfluoro-n-hexane.Weigel etc. have carried out the argon plasma processing to asymmetric polypropylene screen, but do not carry out monomer-grafted (ActPolym.1988,39 (4), 174-7 (Ger)).Wang Ying top grade utilization response type gas oxygen low temperature plasma (Shanxi chemical industry, 2000,20 (4), 1～3), the non-response type gas argon low temperature plasma of utilization such as poplar Niu Zhen (Xibei Textile Engineering College's journal, 2000,14 (3), 314～317) respectively polyacrylonitrile commodity milipore filter is carried out surface treatment, but do not carried out graft modification.
Summary of the invention
The objective of the invention is to adopt the low temperature plasma surface modification technology, polymerization milipore filter or micro-filtration membrane surface are carried out the styrene monomer grafting, when introducing hydrophobic group, the film surface adjusts membrane pore structure, its hydrophobicity is strengthened, the aperture reduces, pore size distribution is more even, realizes that other changes from ultrafiltration to the nanofiltration level, and film is used for removing of lubricating oil and dewaxing solvent system toluene and butanone.
The invention provides a kind of graft modification film, it is characterized in that with the perforated membrane being base film, at its surface grafting styrene monomer, the surface forms porous layer or compacted zone, and porous base film is polyacrylonitrile, polysulfones or poly (ether-sulfone) ultrafiltration membrane or micro-filtration membrane.
The present invention realizes by following process program:
The preparation method of Modified Membrane is characterized in that:
The first step: the preliminary treatment of base film
To base film extracting 0.5～6 hour, obtain pretreated base film with ethanol or acetone soln;
Second step: the activation of base film
Pretreated matrix body film is inserted in the glass reaction chamber, adopt the pretreated base film of argon or helium low temperature plasma irradiation, plasma pressure is 0.5～100Pa, and power is 5～120 watts, and irradiation time is 10～200 seconds;
The 3rd step: monomer-grafted polymerization
With liquid nitrogen styrene monomer is carried out freezing-circulation deaeration of vacuumizing-thawing, the temperature of styrene monomer is controlled at 10～80 ℃, then monomer vapours was imported in the reaction chamber graft reaction 10～210 minutes with water bath with thermostatic control;
The 4th step: the post processing of film
To base film extracting 0.5～6 hour, obtain the graft modification film with ethanol or acetone soln.
Base film used in the present invention can be polyacrylonitrile, polysulfones or poly (ether-sulfone) ultrafiltration membrane or micro-filtration membrane.
At first with acetone or alcohol base film being carried out extracting cleans, then by argon low temperature plasma irradiation film surface, make the film surface produce free radical with reactivity, and then the styrene gaseous monomer is contacted with film and carry out graft reaction, with acetone or alcohol film is carried out extracting more at last and handle, can obtain described graft modification NF membrane or milipore filter.Characteristics of the present invention are, under the situation that does not change the base film agent structure, at film or the surperficial active layer of having introduced centrifugation of fenestra, combine with chemical bond between this active layer and the base film surface, thereby the improvement of film surface nature does not decay in time, improve the separating property of original polymeric membrane, also widened the range of application of membrane material.The resulting NF membrane of the present invention is specially adapted to the separation of ketone-benzol solvent in the lubricating oil dewaxing filtrate and reclaims.
Measure the contact angle of film, the results are shown in Table 1.Contact angle increases, and the film surface hydrophobic strengthens.
The graft phenylethene modified polyacrylonitrile film surface contact angle of table 1
| t Reaction | 0 | 10 | 20 | 30 | 35 | 40 |
| Contact angle θ Water (°) | 49.2 | 59.4 | 57.7 | 58.9 | 60 | 75.3 |
Film is used for the lubricating oil system removes dewaxing solvent (toluene, butanone), The performance test results is as shown in table 2.
Table 2 grafted monomers temperature is to the influence of membrane separating property
| The grafted monomers temperature (℃) | 15 | 20 | 25 | 30 |
| Toluene+butanone C Feed liquid(%) toluene+butanone C See through side(%) flux J (Kgm -2h -1) rejection (%) | 85.0 91.9 9.6 45.8 | 81.0 90.3 8.4 49.0 | 84.0 93.7 11.9 60.2 | 84.4 96.5 22.2 77.5 |
Annotate: operating pressure 2MPa, 20 ℃ of operating temperatures
The film for preparing is lubricated the separation of ketone-benzol solvent in the oil dewaxing filtrate and reclaims, and separating property is as shown in table 3 with the variation of feed temperature, along with feed temperature reduces, film improves the rejection of lubricating oil, flux descends, and in the time of-15 ℃, rejection is up to 88.0%.
Temperature is to the influence of membrane separating property during table 3 2MPa
| Operating temperature, ℃ | 20 | 15 | 5 | 0 | -5 | -15 |
| Rejection, % flux, kg/m -2.h -1 | 77.5 22.2 | 74.7 13.7 | 72.5 9.2 | 70.9 7.9 | 77.1 6.7 | 88.0 5.4 |
The specific embodiment
Embodiment 1
With acetone to polyacrylonitrile ultrafiltration film extracting 0.5 hour, with vavuum pump system is evacuated to absolute pressure 0.5Pa after placing film in the glass tube reaction chamber, under the power of 5W, shone film 200 seconds with argon plasma, with liquid nitrogen styrene monomer is carried out simultaneously freezing-vacuumize-thaw cycles deaeration three times, then, to import in the reaction chamber by 10 ℃ of gaseous state styrene monomers of water bath with thermostatic control constant temperature and carry out grafting 10 minutes, again with acetone to grafting polyacrylonitrile film extracting 0.5 hour, promptly obtain described graft modification film.
Embodiment 2
With ethanol to polyacrylonitrile ultrafiltration film extracting 1 hour, with vavuum pump system is evacuated to absolute pressure 15Pa after placing film in the glass tube reaction chamber, under the power of 80W, shone film 150 seconds with argon plasma, with liquid nitrogen styrene monomer is carried out simultaneously freezing-vacuumize-thaw cycles deaeration three times, to import in the reaction chamber by 30 ℃ of gaseous state styrene monomers of water bath with thermostatic control constant temperature then and carry out grafting 60 minutes, again with ethanol to grafting polyacrylonitrile film extracting 1 hour, promptly obtain described graft modification film.
Embodiment 3
With ethanol to polysulphone super-filter membrane extracting 6 hours, with vavuum pump system is evacuated to absolute pressure 100Pa after placing film in the glass tube reaction chamber, under the power of 120W, shone film 10 seconds with helium plasma, with liquid nitrogen styrene monomer is carried out simultaneously freezing-vacuumize-thaw cycles deaeration three times, to import in the reaction chamber by 80 ℃ of gaseous state styrene monomers of water bath with thermostatic control constant temperature then and carry out grafting 210 minutes, again with acetone to grafting PS membrane extracting 6 hours, promptly obtain described graft modification film.
Embodiment 4
With acetone to polysulfones micro-filtration membrane extracting 4 hours, with vavuum pump system is evacuated to absolute pressure 50Pa after placing film in the glass tube reaction chamber, under the power of 50W, shone film 100 seconds with helium plasma, with liquid nitrogen styrene monomer is carried out simultaneously freezing-vacuumize-thaw cycles deaeration three times, to import in the reaction chamber by 40 ℃ of gaseous state styrene monomers of water bath with thermostatic control constant temperature then and carry out grafting 180 minutes, again with ethanol to grafting PS membrane extracting 1 hour, promptly obtain described graft modification film.
Embodiment 5
With acetone to poly (ether-sulfone) ultrafiltration membrane extracting 2 hours, with vavuum pump system is evacuated to absolute pressure 20Pa after placing film in the glass tube reaction chamber, under the power of 90W, shone film 50 seconds with argon plasma, with liquid nitrogen styrene monomer is carried out simultaneously freezing-vacuumize-thaw cycles deaeration three times, to import in the reaction chamber by 20 ℃ of gaseous state styrene monomers of water bath with thermostatic control constant temperature then and carry out grafting 100 minutes, again with acetone to grafting poly (ether sulfone) film extracting 3 hours, promptly obtain described graft modification film.
Embodiment 6
With acetone to polyether sulfone micro-filtration membrane extracting 5 hours, with vavuum pump system is evacuated to absolute pressure 90Pa after placing film in the glass tube reaction chamber, under the power of 20W, shone film 100 seconds with helium plasma, with liquid nitrogen styrene monomer is carried out simultaneously freezing-vacuumize-thaw cycles deaeration three times, to import in the reaction chamber by 60 ℃ of gaseous state styrene monomers of water bath with thermostatic control constant temperature then and carry out grafting 60 minutes, again with acetone to grafting poly (ether sulfone) film extracting 5 hours, promptly obtain described graft modification film.
Claims (3)
1. graft phenylethene modified film, it is characterized in that: it is as base film with perforated membrane, at its surface grafting styrene monomer, the surface forms the NF membrane of porous layer or compacted zone, and porous base film is polyacrylonitrile, polysulfones or poly (ether-sulfone) ultrafiltration membrane or micro-filtration membrane.
2. the preparation method of a kind of graft phenylethene modified film according to claim 1 is characterized in that:
The first step: the preliminary treatment of base film
To base film extracting 0.5～6 hour, obtain pretreated base film with ethanol or acetone soln;
Second step: the activation of base film
Pretreated base film is inserted in the glass reaction chamber, adopt the pretreated base film of argon or helium low temperature plasma irradiation, plasma pressure is 0.5～100Pa, and power is 5～120 watts, and irradiation time is 10～200 seconds;
The 3rd step: monomer-grafted
With liquid nitrogen styrene monomer is carried out freezing-circulation deaeration of vacuumizing-thawing, the temperature of styrene monomer is controlled at 10～80 ℃, then monomer vapours was imported in the reaction chamber graft reaction 10～210 minutes with water bath with thermostatic control;
The 4th step: the post processing of film
To base film extracting 0.5～6 hour, obtain the graft modification film with ethanol or acetone soln.
3. the purposes of a kind of graft phenylethene modified film according to claim 1 is characterized in that: be used for the separation recovery of lubricating oil dewaxing filtrate ketone-benzol solvent.
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| CN101270202B (en) * | 2007-03-23 | 2010-08-11 | 中国科学院化学研究所 | Polymethyl methacrylate with superhydrophobic surface and preparation method thereof |
| CN102120829A (en) * | 2010-12-30 | 2011-07-13 | 中国科学院等离子体物理研究所 | Preparation method of polymer alkaline anion-exchange membrane |
| CN101831079B (en) * | 2009-03-13 | 2011-11-30 | 中国纺织科学研究院 | Method and device for modifying surface of polymer material |
| CN102139187B (en) * | 2010-01-28 | 2013-04-10 | 中国科学院化学研究所 | Hyperfiltration membrane or nanofiltration membrane with multi-layered composite structure and preparation method thereof |
| CN105688687A (en) * | 2016-02-29 | 2016-06-22 | 江苏久朗高科技股份有限公司 | Preparation technology of hydrophobic and oleophobic film |
| CN109694724A (en) * | 2017-10-24 | 2019-04-30 | 中国石油化工股份有限公司 | The method of the recovery method and crude lube stock oil dewaxing of crude lube stock oil dewaxing solvent |
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| IL99498A0 (en) * | 1990-10-05 | 1992-08-18 | Himont Inc | Blends of graft copolymers of propylene polymer material and of olefinic rubber material |
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| DE10051910A1 (en) * | 2000-10-19 | 2002-05-02 | Membrana Mundi Gmbh | Flexible, porous membranes and adsorbents, and processes for their manufacture |
| US6688477B2 (en) * | 2001-05-03 | 2004-02-10 | Air Products And Chemicals, Inc. | Composite membranes |
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| CN101831079B (en) * | 2009-03-13 | 2011-11-30 | 中国纺织科学研究院 | Method and device for modifying surface of polymer material |
| CN102139187B (en) * | 2010-01-28 | 2013-04-10 | 中国科学院化学研究所 | Hyperfiltration membrane or nanofiltration membrane with multi-layered composite structure and preparation method thereof |
| CN102120829A (en) * | 2010-12-30 | 2011-07-13 | 中国科学院等离子体物理研究所 | Preparation method of polymer alkaline anion-exchange membrane |
| CN102120829B (en) * | 2010-12-30 | 2012-07-25 | 中国科学院等离子体物理研究所 | Preparation method of polymer alkaline anion-exchange membrane |
| CN105688687A (en) * | 2016-02-29 | 2016-06-22 | 江苏久朗高科技股份有限公司 | Preparation technology of hydrophobic and oleophobic film |
| CN105688687B (en) * | 2016-02-29 | 2018-09-04 | 江苏久朗高科技股份有限公司 | The preparation process of double-hydropholic film |
| CN109694724A (en) * | 2017-10-24 | 2019-04-30 | 中国石油化工股份有限公司 | The method of the recovery method and crude lube stock oil dewaxing of crude lube stock oil dewaxing solvent |
| CN109694744A (en) * | 2017-10-24 | 2019-04-30 | 中国石油化工股份有限公司 | The method of the recovery method and crude lube stock oil dewaxing of crude lube stock oil dewaxing solvent |
| CN109694744B (en) * | 2017-10-24 | 2022-03-15 | 中国石油化工股份有限公司 | Method for recovering dewaxing solvent for lube-oil feedstock and method for dewaxing lube-oil feedstock |
| CN112403282A (en) * | 2019-08-23 | 2021-02-26 | 中国石油化工股份有限公司 | Amphiphilic polypropylene porous membrane and preparation method and application thereof |
| CN112403282B (en) * | 2019-08-23 | 2022-06-03 | 中国石油化工股份有限公司 | Amphiphilic polypropylene porous membrane and preparation method and application thereof |
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