DK178227B1 - A novel synthetic process of a block copolymer and a novel use - Google Patents

A novel synthetic process of a block copolymer and a novel use Download PDF

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DK178227B1
DK178227B1 DK201400240A DKPA201400240A DK178227B1 DK 178227 B1 DK178227 B1 DK 178227B1 DK 201400240 A DK201400240 A DK 201400240A DK PA201400240 A DKPA201400240 A DK PA201400240A DK 178227 B1 DK178227 B1 DK 178227B1
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Michael Stolzenburg
Christian Elbek
Søren Mentzel
Kent Høier Nielsen
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Aquaporin As
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G73/00Macromolecular compounds obtained by reactions forming a linkage containing nitrogen with or without oxygen or carbon in the main chain of the macromolecule, not provided for in groups C08G12/00 - C08G71/00
    • C08G73/02Polyamines
    • C08G73/0233Polyamines derived from (poly)oxazolines, (poly)oxazines or having pendant acyl groups
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D69/00Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/14Dynamic membranes
    • B01D69/141Heterogeneous membranes, e.g. containing dispersed material; Mixed matrix membranes
    • B01D69/142Heterogeneous membranes, e.g. containing dispersed material; Mixed matrix membranes with "carriers"
    • B01D69/144Heterogeneous membranes, e.g. containing dispersed material; Mixed matrix membranes with "carriers" containing embedded or bound biomolecules
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06Organic material
    • B01D71/70Polymers having silicon in the main chain, with or without sulfur, nitrogen, oxygen or carbon only
    • B01D71/702Polysilsesquioxanes or combination of silica with bridging organosilane groups
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06Organic material
    • B01D71/76Macromolecular material not specifically provided for in a single one of groups B01D71/08 - B01D71/74
    • B01D71/80Block polymers
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G77/00Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
    • C08G77/42Block-or graft-polymers containing polysiloxane sequences
    • C08G77/452Block-or graft-polymers containing polysiloxane sequences containing nitrogen-containing sequences
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06Organic material
    • B01D71/56Polyamides, e.g. polyester-amides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06Organic material
    • B01D71/58Other polymers having nitrogen in the main chain, with or without oxygen or carbon only

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Abstract

The present invention relates to a process for synthesizing amphiphilic block copolymers. The invention further relates to novel vesicles comprising said block copolymers having the structures according to Formulae (I) and (II) and novel uses of said block copolymers as a matrix forming material for incorporation of transmembrane molecules, such as aquaporins.

Description

A NOVEL SYNTHETIC PROCESS OF A BLOCK COPOLYMER AND A NOVEL USE FIELD OF THE INVENTION
The present invention relates to a novel process for synthesizing block copolymers, where said process may be performed in a reaction using a sterically hindered base, optionally using a solvent mixture, and where an increased degree of PDMS derivatization is obtained. The invention further relates to certain di- and triblock copolymers produced in higher degrees of purity as well as novel di- and triblock copolymer mixtures haying a controlled degree of molecular weight dispersity.
BACKGROUND OF THE INVENTION
Nardin et al. (Langmuir 2000, 1035-1041) describes the synthesis of a poiy(2-methyloxazoline)-block-poly(dimethylsiioxane)-biock-poly(2-methyloxazoline) (PMOXA-PDMS-PMOXA) triblock copolymer carrying polymerizable groups at both chain ends.
Isaacman et ai. (2012) describes a modular synthesis of poly(oxazoline)-poly(siloxane)-poly(oxazoline) block copolymers that have been clicked together using the copper catalyzed azide-alkyne cycloaddition reaction.
Chujo et al. (1992) describes the preparation of polyoxazoline-polysiloxane-polyoxazoline block copolymers having the formula
Figure DK178227B1D00031
The block copolymers are prepared by reacting amino-terminated telechelic poly (dime thylsiloxane)s (3) at the end of poly(2-methyl-2-oxazoline)s in CHCI3 at 60°C in the form of reactive oxazolinium (4) species using three different (4)/(3) reactant ratios: 20.6, 19,6, and 25.2 resulting in correspondingly increasing yields of 13.5, 23.8, and 29.0 %, respectively, WO 2013072378 Al (Byk-Chemie GMBH) discloses uses as additives in thermal hardening coating material compositions and molding materials of polysiloxane-polyoxazoline block copolymers having units of the general formulae
Figure DK178227B1D00041
wherein n is in the range of 1 to 400 preferably in the range of 5 to 100, and Rl and R2 represent alkyl moieties of various kinds having from 4 to 6 carbon atoms or they represent cyclic alkenyl, aryl, alkylaryl or arylalkyl moieties having up to 12 carbon atoms; m is in the range of 1 to 400 preferably in the range of 5 to 100, and R3 represents alkyl, alkenyl or aryl moieties of various kinds having from 3 to 12 carbon atoms. However, for the syntheses described in the preparation of said copolymers only single component solvents, such as toluol or acetonitrile, are used. For the reactants a large surplus of the polyoxazoline component is needed, cf. the synthesis of Chujo et al. (1992), and where the polyoxazoline-polysiloxane-copolymers are prepared in a one-pot reaction using methyl toluenesulfonate as initiator, PMOXA in excess amounts and as solvent toluene or acetonitrile.
Moreover, the block copolymers of the prior art exhibit a large variation in chain lengths of the blocks and may form different kinds of reaction by-products. In block copolymers polydispersity may be manifested through a molecular weight distribution. It has been shown by Meier et al. (2000) that amphiphilic block copolymers, such as PMOXA-PDMS-PMOXA, when forming biomimetic membranes, e.g. when self assembled into polymersomes, can incorporate transmembrane proteins in the amphiphilic lipid bilayer like wall (a polymeric bilayer). However, when incorporating transmembrane proteins and peptides in polymersome walls or membranes, the polydispersity of the block copolymer chains may result in a membrane thickness mismatch that could pose a problem for transmembrane protein incorporation. Pata & Dan (2003) found that the mechanism for the inhibition of protein incorporation in polymeric bilayers differs from that of their inclusion in lipid vesicles; because in polymersomes, the equilibrium concentration of transmembrane proteins decreases as a function of the thickness mismatch between the protein and the bilayer core. Thus, it is an additional object of the invention to provide a method of preparing block copolymers, such as PMOXA-PDMS-PMOXA triblock copolymers having a controlled, well defined and narrow molecular dispersity range making them useful for incorporation of various transmembrane molecules being proteins, such as aquaporin water channels, ion channel proteins, or being transmembrane peptide channels such as gramicidins, and the like according to the preferred incorporation requirements of said molecules.
A further object of the invention is the novel use of a triblock copolymer according to Formula I
Figure DK178227B1D00051
a diblock copolymer according to Formula ΪΙ
Figure DK178227B1D00052
or a mixture of said block copolymers: wherein R., R2, Li, L2, m, and n are defined as below; said novel use being as matrix forming material in vesicles being useful for having incorporated transmembrane proteins. In an exemplary embodiment of the invention said use comprises a mixture wherein the triblock copolymer comprises more than about 65 to 70 % (w/w), such as more than about 80 % (w/w). In another exemplary embodiment of the invention said use comprises a mixture wherein the triblock copolymer comprises about 25 to 40 % (w/w) or about one third, and the diblock copolymer comprises about 55 to 70 % (w/w) or about two thirds.
Other objects of the invention will be apparent to the person skilled in the art from the following detailed description and examples. A significant feature of the compounds of Formula I and II is that the PMOXA blocks exhibit a retro configuration of the repeat unit compared to PMOXA-PDMS-PMOXA block copolymers used in the relevant prior art cf. Isaacman et al. (2012), and another feature is that the Ri end groups are directly attached to the nitrogen atom of the repeat sequence, whereas end groups in prior art PMOXA-PDMS-PMOXA block copolymers, typically a hydroxyl group, is bound to the -(CH2)2- group of the repeat unit.
SUMMARY OF THE INVENTION
The present invention relates to a process for synthesizing a preferably amphiphilic block copolymer having at least one hydrophilic A block polymer and a hydrophobic B block polymer, the process comprising the step of reacting a terminally cationic reactive A block polymer (A+) with a terminally di- or mono functionalized B block in a reaction to obtain an A-B or an A-B-A block copolymer wherein said A block is selected from hydrophilic polymeric compounds, such as polyethyleneoxide (PEO/OEG) or polyalkyloxazoline (POXA) polymers, such as PMOX A polymers (poly(2-methyl-oxazoline)) and PEOXA (poly(2-ethyl-oxazoline)), and said B block is selected from hydrophobic polymeric compounds such as polybutadiene or silicone compounds, such as polyorganosiloxanes including polydimethylsiloxane (PDMS), polydiethylsiloxane (PDES) and polymethylphenylsiloxane (POPS) polymers. In particular the present invention relates to a process for synthesizing a block copolymer comprising reacting at least one hydrophilic and terminally cationic reactive polymer, A\ with a terminally di- or mono functionalized hydrophobic polymer, B, comprising polydimethylsiloxane (PDMS), to obtain an A-B block copolymer, an A-B-A block copolymer, or a mixture of said block copolymers; wherein said reaction is carried out in the presence of a sterically hindered base. In addition, said process preferably takes place in a reaction vessel using a solvent mixture where said mixture comprises a polar organic solvent and an apolar organic solvent where both are able to dissolve the hydrophilic as well as the hydrophobic reactants and reaction products. In addition, said process of preparing an amphiphilic block copolymer is terminated by quenching the reaction with water.
In particular, the invention relates to a process for synthesizing a block copolymer, wherein said terminally cationic reactive A block polymer (A A is formed by reacting 2-alkyloxazoline monomers with a nucleophilic reagent, such as having a lower alkyl substituent on the leaving group, e.g, methyl, to produce the desired length of polyalkyloxazoline (POXAH‘) polymer, such as PMQXA+ polymer (poly(2-methyl-oxazoline)), and reacting said POXA+ with said terminally di- or monoamine functionalized B block in the same reaction vessel without the need to exchange solvent (one-pot reaction), thus obtaining the desired A-B or A-B-A block copolymer. In addition, the method of polymerization of the invention can be used to incorporate functional end-groups. Such end-groups are normally added post-polymerization. However, functional end-groups including -NH2, -OH, -SH, -CHO, -C2H4OH, -COCH3, -COOH, methacrylate and epoxides may be introduced in the compounds of the invention via or as the Rj-group in Ts-O-Ri and thus be transferred to the POX Λ ends during the nucleophilic substitution reaction, cf. Scheme 1 below. If necessary, the functional end-groups can be protected. The block copolymers prepared using the method of the invention are useful as matrix materials in vesicles having incorporated transmembrane proteins, such as aquaporins including bacterial and yeast aquaporins and aquaporins from higher plants; ion channels including sodium, potassium, chloride, and calcium channels, ligand and voltage gated channels, stretch activated channels and constitutively open channels, such as porins; transporters including NaK atpase, F0F1 atp-synthase, calcium atpases and lithium transporters, taurine transporters and GLUT4.
DETAILED DESCRIPTION OF THE INVENTION
More specifically, the invention relates to a process wherein a mono or diamine end-functionalized silicone polymer, such as of Formula i): X1-L1-PDMS-L2-X2 or Formula ii): X.-L1-PDMS-L2, wherein X·, and X?, each represents a primary amine group (-NIL) or one of Xi and X2 represents a -NIL group and the other is absent; Lj and L2 each represents a hydrocarbon chain, such as alkylene, i.a. a ~(CH2)y- group where y is an integer selected from 1, 2, 3, and 4 and where y preferably is the same in Li and L2; or when one of the Ri groups is absent then the L{ or L2 group which is would be connected to said absent Rj group is also absent, and the number of repeating units of the PDMS is in the range of about 10 to about 100, such as about 35 to about 65, such as about 40.
In one aspect of the process of the invention, i.a. the synthesis of an A-B copolymer and/or an A-B-A copolymer, the synthetic route to POXA-HN-(CH2)y-PDMS-(CH2)yH and POXA-HN-(CH2)y-PDMS-(CH2)y-NH-POXA comprises the steps of: a) providing the reactant ΡΟΧΛ'. e.g. through polymerization of the monomer alkyl-2-oxazoline using an initiator such as tosylate, both in a suitable polar organic solvent; b) reacting the POXA+ with H2N-(CH2)y-PDMS-(CH2)y-NH2 in the presence of a proton scavenger, preferably a stericaliy hindered base, in a suitable apolar organic solvent; c) quenching the polymerization reaction in water.
In a further aspect of the process of the invention formula i) represents FLN-CCFLL-PDMS-(CH2)3-NH2 which is reacted with a terminally cationic reactive PMOXAT where the number of repeating units of the PMGXA is in the range of about 3 to about 50, such as about 5 to about 20, and the molar ratio of said PMOXA+ to the amine groups in the compound i) is about 1, such as about 1.1 or such as 0.5, to obtain the desired PMOXA-HN-(CH2)3-PDMS-(CH2)3-NH-PMOXA.
In a further aspect of the process of the invention formula ii) represents H2N-(CH2)3-PDMS-(('H2 )dl which is reacted with a terminally cationic reactive P.V10XA' where the number of repeating units of the PMOXA is in the range of about 3 to about 50, such as about 5 to about 20, and the molar ratio of said PMOXA+ to the amine groups in the compound i) is about 1, such as about LI or such as 0,5, to obtain the desired PMOXA-HN-tCHiL-PDMS-iCTLh-NH-PMOXA.
In the process of the invention the compounds of formulae i) and ii), such as H2N-(CH2)3-PDMS-(CH2)3-NH2 or H2N-(CH2)3-PDMS-(CH2)4H, is preferably dissolved in an organic solvent, such as dichloromethane, chloroform, or the like, and added to the POXA+ reagent,, in the reaction vessel, and the A-B or A-B-A reaction may be performed at a temperature of between 20 and 70°C lasting for a period of between 2 hours and up to 30 hours. An example of said coupling reaction is shown in scheme 1 below where a terminal -NI L group in the presence of a proton scavenger, such as a Hiinig's base, e.g. DIPEA, participates in a ring opening of a terminal oxazoline moiety and resulting addition reaction with the release of protons from said -NH2 group.
Furthermore, prior to reacting terminally cationic reactive POXAH‘ with H2N-(CH2)3-PDMS-(CH2)3-NH2 or H2N-(CH2)3-PDMS, the process of the invention may comprise the step of polymerizing 2-alkyl oxazoline monomers, preferably 2-methyl-2-oxazoline, to obtain said cationic reactive PQXAL
In the process of the invention the polymerization of the A block monomer (e.g. 2-methyl-2-oxazoiine) is preferably performed with a nucleophilic reagent initiator capable of initiating an Sn2 reaction (also known as bimolecular nucleophilic substitution), such as alkyl p-toluene sulfonate Ri-O-Ts (e.g, methyl tosylate), alkyl trifluoromethane sulfonate (e.g. methyl inflate) or alkyl methanesulfonate (e.g, methyl mesylate), preferably methyl p-toluenesulfonate (methyl tosylate) in a nucleophilic substitution reaction leading to alkyl end capped PMOXA, i.e. methyl end capped PMOXA, ef. Formula II below'. When using 2-dimethylammoniumethyl methacrylate tosylate as the initiator the final block copolymer would possess methacrylate end-groups suitable for crosslinking by UV light. The initiator is used at a molar ratio dependent of the desired chain length, and said polymerization of 2-methyl-2-oxazoline monomers is preferably conducted in a solvent such as acetonitrile or DMSO both solvents being compatible wdth solvents such as dichloromethane or chloroform.
In a further embodiment of the invention the mono functionalized B block is a compound of Formula i), i): Xj-Li-PDMS-L2-X2, wherein Xj, Lj, L2 and X2 are as defined below.
In a preferred embodiment of the process of the invention the compound of Formula i) is H2N-(CH2)3-PDMS-(CH2)3-NH2, such as a compound, wherein the average number of repeating units of the PDMS is in the range of about 10 to about 100, such as about 25 to about 55, such as about 35. In other preferred embodiments of the invention the compound of Formula ii) is H2N-(CH2)3-PDMS-(CH2)4H, such as a compound wherein the average number of repeating units of the PDMS is in the range of about 10 to about 100, such as about 20 to about 30. Examples of amino functionalized PDMS polymers useful in the process of the invention preferably have a number average molecular weight, Mn, of from about 2000 Da to about 4500 Da, e.g. such as about 2500 to about 3000 Da.
In a further embodiment of the invention the polymer, B, is a terminally mono functionalized block polymer and the block copolymer obtained is predominantly an A-B block copolymer. In a further embodiment the polymer, B, is a terminally difunctionalized polymer and the block copolymer obtained is a mixture of A-B-A and A-B block copolymers. In a further embodiment the polymer, B, is a terminally difunctionalized polymer and the block copolymer obtained is predominantly an A-B-A block copolymer.
In a further embodiment of the invention, the process is being conducted in a solvent mixture which dissolves all of the A+, B, A-B, and A-B-A polymers which are present in the reaction mixture. In a further embodiment said solvent mixture a comprises * a polar aprotic solvent selected from acetonitrile or DMSO; ® and an apolar solvent selected from dichloromethane, trichloromethane, or trichloroethylene.
In a special embodiment, solvent mixture comprises acetonitrile and methylene chloride, preferably in the ratio ranges of from 1:3 to 3:1.
In a further embodiment, the hydrophobic polymer, B, is dissolved in the apolar solvent prior to addition to the reaction pot.
In a further embodiment of the process of the invention POXA+ is PMOXA+, and the molar ratio of PMOXA+ to functionalized groups is at least 1:1, such as equal to or larger than 1.1:1, such as larger than 1.2:1. In a further embodiment, POXA+ is PMOXA+, and the molar ratio of PMOXA+ to functionalized groups is at least 0.5:1, such as equal to or larger than 0.55:1, such as larger than 0.6:1.
In a further embodiment of the invention the process comprises the step prior to reacting the terminally cationic reactive POXA+ with said terminally di- or monoamine functionalized B block, of: polymerization of 2-alkyl oxazoline monomers, such as 2-methyl oxazoline, to obtain said cationic reactive POXA+. In a further embodiment the polymerization of 2-alkyl oxazoline monomers, such as 2-methyl oxazoline, is performed with a nucleophilic reagent or initiator, such as methyl p-toluenesulfonate, being capable of initiating an SN2 reaction. In a special embodiment the polymerization is conducted in a polar aprotic solvent, such as acetonitrile.
The invention further relates to a vesicle comprising a triblock copolymer according to Formula I,
Figure DK178227B1D00101
a diblock copolymer according to Formula II,
Figure DK178227B1D00102
and a transmembrane molecule selected from the group consisting of aquaporin water channel molecules.
In a special embodiment of the above use both Ri groups are the same and selected from straight or branched Ci to C3 lower alkyl groups, such as methyl and ethyl; Li and L2 are the same and selected from -(CFFk- and -(CFbri-; m is an integer between 60 and 100; and n is an integer between 7 and 19, such as 9 to 11.
In a further embodiment of the above use the triblock copolymer has the structure of Formula III:
Figure DK178227B1D00111
The invention further relates to a block copolymer composition comprising a compound according to Formula I and a compound according to Formula II, said composition being prepared according to the process as disclosed herein, and wherein each of said compounds has a degree of PDMS derivatization of more than about 30 to 40 %, such as more than or equal to 50%.
An exemplary synthetic route of preparing an A-B-A type compound of Formula I is shown below in Scheme 1 where Ts-O-Rt represents a tosylate, Ts representing the leaving group, and Ri is a group, such as alkyl (eg. methyl) and H2N-L1-PDMS-L2-NH2 represents the diamine functionalized PDMS, cf. also formula i) above.
Figure DK178227B1D00112
Scheme 1: Synthesis reaction scheme. Hiinig's base is shown here while other sterieahy hindered bases also may be useful as proton scavengers.
Definitions and Terms
The term amine functionalized PDMS as used herein refers to mono- or diamine functionalized polydimethyl siloxane polymers, e.g. such as aminomethyl, aminoethyl, aminopropyl, or aminobutyl terminated polydimethylsiloxane (CAS: 106214-84-0 ), Example of a diamine functionalized PDMS is the cheap commercial oligomer DMS A21 (bis(3-aminopropyl)-polydimethylsiloxane, calculated Mn app, 6400 Da) trom Gelest or polydimethylsiloxane, aminopropyl terminated (Mw 3000,00 g/mol from abcr specialty chemicals, Karlsruhe, Germany). Or PDMS diamine can be synthesized if needed to tailor the PDMS portion in Mw. Example of synthesis of oligomers with targeted number average molecular weights (Mn) of 1000, 2000, 5000, and 11000 g/mol is disclosed in Bowens, A.D. Synthesis and Characterization of Polyisiioxane irnide) Block Copolymers and End-Functional Polyimides for Interphase Applications (Ph. D. dissertation 1999-11-29) cf. url> hlip:// wh· Tir.iih.vi vGiiAiwsoDawuk-MoA.k!· i 20?vv·: 5 1523/ retrieved from the internet on 28-04-2014. Alternatively as disclosed in Baranauskas, V.V. url> hUpF/sdn-kir kk \ kodu/kH: ws/uvniiahD/elu -04272=)05 · i 9·'·-48/ retrieved from the internet on 28-04-2014.
The term PMOXA as used herein refers to the polyoxazoline poly(2-methyloxazoline) or poly(2-methyl-2-oxazoline) being prepared by polymerizing 2-methyloxazoline CAS No. 1120-64-5: 2-methyl-2-oxazoiine. Other similar oxazolines may be useful in the method of the invention, e.g. oxazoline and 2-ethyl-2-oxazoline.
The term PDMS as used herein refers to polydimethylsiloxane. However, in general other polyorganosiloxanes including polydiethylsiloxane (PDES) and polymethylphenylsiloxane (PDFS) polymers may be useful in synthesizing block copolymers according to the methods described herein.
Sterically hindered base A sterically hindered base is an organic base that has the ability to abstract an acidic hydrogen atom from a compound without otherwise chemically reacting with the compound, that is without displacing a functional group within the compound (i.e. nucleophilic substitution). Tertiary amines are good examples of non-nucleophilic bases because they have the ability to abstract an acidic proton from a compound but because of their steric hindrance, they cannot otherwise react with the compound. Other non-limiting illustrative examples of non-nucleophilic bases include lithium diisopropylamide (LDA), lithium 2,2,6,6-tetramethylpiperdine (LIMP), lithium hexamethyldisilazide (LHMDS), and the like.
Specifical examples of sterically hindered bases for use in the present invention include: Ν,Ν-Diisopropylethylamine (DIPEA, or Hunig's Base), l,5-Diazabicyclo[4.3.0]non-5-ene (DBN), 1,4-Diazabicyclo[2.2.2]octan (TED), tert-butylamine, l,8-diazabicyclo[5.4.0]undec-7-ene (DBU), l,4-diazabicyclo(2.2.2)octane (DABCO), N,N-dicyclohexylmethylamine, 2,6-di-tert-butyI-4-methylpyridine, quinuclidine, 1,2,2,6,6-pentamethylpiperidine (PMP), 7-methyl-l,5,7-triazabicyclo(4.4.0)dee-5-ene (MTBD), triphenylphosphine, tri-tert-butylphosphine an d trie y c I oh ex y I ph o sph ine.
The abbreviation Mn means number average molecular weight. It means the total weight of polymer divided by the number of polymer molecules. Thus, M„ is the molecular weight weighted according to number fractions.
The abbreviation Mw means weight average molecular weight. The molecular weight weighted according to weight fractions.
The term PDI means the polydispersity index. The polydispersity index is calculated as the ratio of Mw to M„.
The term ''transmembrane molecule" as used herein means in particular membrane proteins haying at least one transmembrane domain such as aquaporin water channels including bacterial aquaporins, yeast aquaporins, plant aquaporins, mammalian aquaporins, and other euc ary otic aquaporins. In addition, "transmembrane molecule" means membrane bound peptides, such as gramicidin peptides, having transmembrane spanning properties as well as other transmembrane molecules having sufficient amphiphilic features to enable transmembrane binding or localization.
The process according to the invention exhibits several advantages compared with the prior art, such as the use of a single solvent mixture that abolishes the need to exchange solvent during the reactions and enables the reaction to be performed in one reaction vessel, i.e. as a one-pot reaction. The use of functional tosylates or triflates for the cationic ring-opening polymerization of 2-methyl- 1,3-oxazoline is described in Einzmann & Binder (2001), and the polymerization of 2-methyl oxazoline is well described in literature (e.g. Matyjazewski & Hrkach 1992).
In addition the following synthesis examples show that:
The process is highly reproducible.
The process is scalable due to one-pot reaction in one or two steps without a need to exchange solvents.
The POXA polymerization is fast as compared to literature.
It is possible to control the polydispersity of the end product through control of the POXA+ polymerisation step.
It is possible to obtain a consistently low polydispersity matching the lowest found in literature yielding a very defined product.
The synthesis of the invention provides a simple way of generating a relatively well-defined di-or triblock copolymer which would exhibit a lower polydispersity compared to similar block copolymers synthesized according to the prior art.
EXAMPLES
The present invention is further illustrated by the following examples should not be construed as further limiting the general scope of the invention.
Experimental section
General procedere
The reaction according to the invention for the synthesis of PMOXAn-PDMSm-PMOXAn (poly(2-methyl oxazolin) block polydimethylsiloxan block poly(2-methyl oxazolin)) in general is as shown in Scheme 1 above.
Example 1. Preparation of PMOXA-PDMS-PMOXA/PMOXA-PDMS block copolymers in a two step reaction, cf. Formulae III and IV below:
Prior to reaction the solvent (acetonitrile) and the monomer (2-methyl-2-oxazoline) are both dried, such as using molecular sieve 4. 130 g acetonitrile is charged into a 500 ml glass reactor with stirrer. 50 g 2-methyl-2-oxazoline monomer is added by means of a dried (such as Ar flushed) syringe. The monomer reaction solution is heated to 40 °C, 50 g on initiator solution (methyl-p-toluenesulfonate in acetonitrile with a concentration of 1.0 mol/L) is added with a dried syringe. The reaction solution is heated to 100 °C. After 3 hours at 100 °C the reaction solution is cooled to room temperature, 113 g Dichloromethane is added to the resulting PMOXA+ reaction solution.
10 g Aminopropyl terminated polydimethylsiloxane, symmetric (PDMS difunctional amine, CAS No. 106214-84-0, molecular weight around 3000 kDa, obtained from Gelest DMS A15), 33 g acetonitrile and 3 g Ν,Ν-Diisopropylethylamine (DIPEA) are added to a 250 ml reaction flask. 50 g of the previously prepared PMOXA+ reaction solution are added. The reaction is kept at 60 °C for 64 hours. The copolymerization reaction is quenched in water. The resulting copolymer is purified by ultrafiltration. Derivation of amines from PDMS: 92%, as determined by NMR. We infer from this finding using binominal distribution modelling that a high percentage of the final copolymer is a triblock copolymer, such as about > 70% or about > 80%, and a low percentage of the final copolymer is a diblock copolymer with a negligible amount of unreacted PDMS.
Example 2. Preparation of PMOXA-PDMS and PMOXA-PDMS-PMOXA block copolymers according to Formulae III and IV below in a two step reaction: a) 130 g acetonitrile is charged into a 500 ml glass reactor with stirrer. 50 g 2-methyl-2-oxazoline is added by means of a dried syringe. The monomer reaction solution is heated to 40 °C. 50 g initiator solution (methyl-p-toluenesulfonate in acetonitrile with a concentration of 1.0 moi/L) is added with a dried syringe. The reaction solution is heated to 100 °C. After 3 hours at 100 °C the reaction solution comprising the resulting PMOXA+ polymer is cooled to room temperature, 10 g Aminopropyl terminated polydimethylsiloxane, symmetric (PDMS difunctional amine, CAS No. 106214-84-0, obtained from Gelest DMS A15), 17 g dichloromethane and 3 g Ν,Ν-Diisopropylethylamine are added to a 250 ml reaction flask. 47 g of acetonitrile and 15 g of the previously prepared PMOXA+ reaction solution are added. The reaction is kept at 60 °C for 64 hours. The copolymerization reaction is quenched in water. The resulting copolymer is purified by ultrafiltration. Derivation of amines from PDMS: 56%, as determined by NMR. We infer from this finding using binominal distribution modelling that about two thirds of the final copolymer is a diblock copolymer and about one third is a tribloek copolymer.
Alternatively, b) 130 g acetonitrile is charged into a 500 ml glass reactor with stirrer, 50 g 2-methyl-2-oxazoline is added by means of a dried syringe. The monomer reaction solution is heated to 40 °C. 50 g initiator solution (methyl-p-toluenesulfonate in acetonitrile with a concentration of 1.0 moI/L) is added with a dried syringe. The reaction solution is heated to 100 °C. After 3 hours at 100 °C the reaction solution comprising the resulting PMOXA+ polymer is cooled to room temperature.
10 g Aminopropyl terminated polydimethylsiloxane, symmetric (PDMS difunctional amine, CAS NR 106214-84-0, obtained trom Gelest DMS A15), 17 g dichloromethane and 3 g N,N-Diisopropylethylamine are added to a 250 ml reaction flask. 13 g of acetonitri le and 15 g of the previously prepared PMOXA reaction solution are added. The reaction is kept at 60 °C for 64 hours. The copolymerization reaction is quenched in water. The resulting copolymer is purified by ultrafiltration. Derivation of amines from PDMS: 53%, as determined by NMR. We infer from this finding using binominal distribution modelling that about two thirds of the final copolymer is a diblock copolymer and about one third is a triblock copolymer.
Example 3: Preparation of diblock copolymer PMOXA-PDMS of Formula IV below.
130 g acetonitrile is charged into a 500 ml glass reactor with stirrer. 50 g 2-methyl-2-oxazoline is added by means of a dried syringe. The monomer reaction solution is heated to 40 °C. 50 g initiator solution (methyl-p-toluenesulfonate in acetonitrile with a concentration of 1,0 mol/L) is added with a dried syringe. The reaction solution is heated to 100 °C. After 3 hours at 100 °C the reaction solution comprising the resulting PMOXA+ polymer is cooled to room temperature, 10 g Monoaminopropyl terminated polydimethylsiloxane, asymmetric, cf. Formula ii) where n is approximately 24 (mean value) (PDMS monofunctional amine, molecular weight around 2000 kDa, obtained from Gelest MCR A12), 17 g dichloromethane, and 2 g N,N-diisopropylethylamine are added to a 250 ml reaction flask. 8 g of acetonitrile and 21 g of the previously prepared PMOXA+ reaction solution are added. The reaction is kept at 60 °C for 64 hours. The copolymerization reaction is quenched in water. The resulting copolymer is purified by ultrafiltration. Derivation of amines from PDMS: 50%, as determined by NMR. We infer from this finding using binominal distribution modelling that about two thirds of the final copolymer is a diblock copolymer and about one third is a triblock copolymer.
Figure DK178227B1D00171
Formula ii), n » 24
Table i) mol amounts and mol ratios used in the above examples
Figure DK178227B1D00172
Table i) clearly shows that the PM OX A reactant is used in approximately equimolar amount relative to the amino functionality.
Figure DK178227B1D00173
Formula III; n * 9 and m » 35-40
Figure DK178227B1D00174
Formula IV; n » 9 and m = 25
Example 4. Protocol for lmg/ml proteo-polymersomes, protein to polymer ratio (PQPR) 50
Materials:
Polyoxazoline Based Di- and Triblock Copolymers prepared and purified as described in the examples above, having an average molecular weight of between approximately 1500 (diblock copolymers) and approximately 6000 (triblock copolymers).
Protein: Aquaporin Z (AqpZ), Mw 27233.
Preparation: 1) Fill a 50 mi glass evaporation vial with 5mi of a 2 mg/ml stock solution of copolymers (either in pure diblock or pure triblock form or as mixtures of di- and tribloek copolymers) in CHCI3.
2) Evaporate the CHCE using a rotation evaporator for at least 2h to complete dryness.
3) Add 3.0 mL of buffer solution (1.3% O.G.; 2Q0mM Sucrose; lOmM Tris pH 8; 50mM Nad) to rehydrate the film obtained in the evaporation vial in step 2.
4) Shake the vial at 200 rpm on a platform shaker (Heidolph orbital platform shaker Unimax 2010 or equivalent) for 3 hours to obtain dissolution of the copolymer.
5) Add 1,55mg μ L of AqpZ in a protein buffer containing Tris, glucose and OG, and rotate vial over night at 200rpm and 4°C.
6) Add 6.88 ml buffer (lOmM Tris pH 8; 50mM NaCl) slowly while mixing up and down with pipette.
7) Add 180mg hydrated Biobeads and rotate for Ih at 200rpm.
8) Add 210mg hydrated Biobeads and rotate for lh at 200rpm.
9) Add 240mg hydrated Biobeads and rotate O.N. at 200rpm 4°C.
10) Add 240mg hydrated Biobeads and rotate O.N. at 200rpm 4°C.
11) The Biobeads with adsorbed OG are then removed by pipetting off the suspension.
12) Extrude the suspension for about 21 times through a 200nm track etched polycarbonate filter using an extruder, such as from at least l time and up to about 22 times to obtain a uniform proteopolymersome suspension (vesicles) suspension.
References
Veena Pata and Nily Dan, Biophysical Journal Volume 85 October 2003 2111-2118]
Einzmann & Binder, Journal of Polymer Science Part A: Polymer Chemistry, Volume 39, Issue 16, pages 2821-2831, 15 August 2001.
T, Saegusa, H. Ikeda, H, Fujii; Macromolecules 1972, 5, 359-362; Isomerization Polymerization of 2-Oxazoline IV. Kinetic study of 2-MethyI-2-oxazoIine Polymerization, B. Brissault, C. Guis, H. Cheradame; European Polymer Journal 2002, 38, 219-228; Kinetic study of poly(ethylene oxide-b-2-methyl-2-oxazoline) diblocks synthesis from poly(ethylene oxide) maeroinitia tor s, R, Hoogenboom, M.W.M. Fijten, U.S.Schubert; journal of Polymer Science Part A: Polymer Chemistry 2004, 42, 1830-1840: Parallel kinetic Investigation of 2-Oxazoline Polymerizations with Different Initiators as Basis for Designed Copolymer Synthesis, R. Hoogenboom, M.W.M. Fijten, R.M. Paulus, H.M.L. Thijs, S. Hoeppener, G, Kickelbiek, U.S. Schubert; Polymer 2006, 47, 75-84; Accelerated pressure synthesis and characterization of 2-oxazoline block copolymers.
S. Ji, T.T. Hoye, C.W. Macosko: Macromolecules 2005, 38, 4679-4686, Primary Amine (-NH2) Quantification in Polymers: Functionality by 19F NMR Spectroscopy.
Corinne Nardin, Thomas Hirt, Jorg Leukel and Wolfgang Meier, Polymerized ABA tribloek Copolymer Vesicles, Langmuir 2000, 1035 - 1041Michael J. Isaacman, Kathryn A. Barron and Michael J. Isaacman, Kathryn A, Barron and Luke S. Theogarajan, Clickable Amphiphilic Triblock Copolymers, Polymer Chemistry 2012, 50, 2319 -- 2329.
Corinne Nardin, Sandra Thoeni, Jorg Widmer, Mathias Winterhalter and Wolfgang Meier, Nanoreactors based on (polymerized) ABA-triblock copolymer vesicles, ('hem. Commun., 2000, 1433 -- 1434.
Matyjaszewski, Krzysztof & Jeffrey S. Hrkach. Cationic ring opening polymerization of oxazolines initiated by trimethylsilyl derivatives. Technical Report, Carnegie Mellon University, Department of Chemistry, May 25, 1992.
W. Meier, C. Nardin, M. Winterhalter, Reconstitution of channel proteins in (polymerised) ABA tribloek copolymer membranes. Angew. Chem. Ini. Ed. 39(24) (2000) 4599 Mirko Einzmann & W olfgang H. Binder (2001) Novel functional initiators for oxazoline polymerization. Journal of Polymer Science Part A: Polymer Chemistry,Volume 39, Issue 16, pages 2821-2831, 15 August 2001 Y. Chujo, E. Ihara & T. Saegusa, Synthesis of Polyoxazoline-polysiloxane block copolymers. Kobunshi ronbunshu, 1992, vol 49, no. 11, pages 943-946.

Claims (13)

1. En fremgangsmåde til syntese af en blokcopolymer, hvilken fremgangsmåde omfatter omsætning af mindst en hydrofil og terminalt kationisk reaktiv polymer, A+, med en terminalt di- eller monofunktionaliseret hydrofob polymer, B, omfattende polydimethylsiloxan (PDMS), til opnåelse af en A-B blokcopolymer, en A-B-A blokcopolymer eller en blanding af disse blokcopolymerer, hvori omsætningen udføres i nærvær af en sterisk begrænset base.A process for the synthesis of a block copolymer comprising the reaction of at least one hydrophilic and terminally cationic reactive polymer, A +, with a terminal di- or monofunctionalized hydrophobic polymer, B, comprising polydimethylsiloxane (PDMS), to obtain an AB block copolymer , an ABA block copolymer or a mixture of these block copolymers wherein the reaction is carried out in the presence of a sterically restricted base. 2. Fremgangsmåden ifølge krav 1 hvori den sterisk begrænsede base er udvalgt fra gruppen DIPEA (Hiinigs base), DBN og TED.The method of claim 1 wherein the sterically restricted base is selected from the group DIPEA (Hiinig's base), DBN and TED. 3. Fremgangsmåden ifølge krav 1 eller 2 hvori den hydrofile og terminalt kationisk reaktive polymer, AH’, omfatter POXA+ (polyalkyloxazolin), såsom PMOXA+ (poly(2-methyl-oxazolin)).The process of claim 1 or 2 wherein the hydrophilic and terminally cationic reactive polymer, AH ', comprises POXA + (polyalkyloxazoline) such as PMOXA + (poly (2-methyl-oxazoline)). 4. Fremgangsmåden ifølge et hvilket som helst af kravene 1 til 3 hvori den hydrofobe polymer B er terminalt di- eller monofunktionaliseret med en eller to reaktive grupper, der er i stand til at udføre koblingsreaktionen med den hydrofile og terminalt kationisk reaktive polymer A+, hvor den reaktive gruppe er uafhængigt udvalgt fra gruppen bestående af amin, thiol, piperidyl, piperazinyl og acyl.The process of any one of claims 1 to 3 wherein the hydrophobic polymer B is terminally di- or monofunctionalized with one or two reactive groups capable of carrying out the coupling reaction with the hydrophilic and terminally cationic reactive polymer A +, wherein the reactive group is independently selected from the group consisting of amine, thiol, piperidyl, piperazinyl and acyl. 5. Fremgangsmåden ifølge et hvilket som helst af kravene l til 4 hvori den terminalt di- eller monofunktionaliserede B blok er en forbindelse ifølge Formel i) i): X1-L1-PDMS-L2-X2, hvori Xi og X2 hver betegner en primær amingruppe (-NH2) eller den ene af X. og X2 betegner en -NH2 gruppe og den anden mangler; Li og 1.2 betegner hver en binding eller en kulbrintekæde, såsom alkylen, f. elcs. en -(CILV gruppe hvor y er et heltal udvalgt fra 1, 2, 3, og 4 og hvor y fortrinsvist er den samme i Li og L2; og det gennemsnitlige antal af repetitive enheder af PDMSen ligger i intervallet fra cirka 10 til cirka 100, såsom cirka 25 til cirka 55, såsom cirka 35.The method of any one of claims 1 to 4 wherein the terminally di- or monofunctionalized B block is a compound of Formula i) i): X1-L1-PDMS-L2-X2, wherein Xi and X2 each represent a primary amine group (-NH 2) or one of X. and X 2 represents an -NH 2 group and the other is missing; Li and 1.2 each represent a bond or a hydrocarbon chain, such as alkylene, f. Elcs. a - (CILV group where y is an integer selected from 1, 2, 3, and 4 and where y is preferably the same in Li and L2; and the average number of repetitive units of the PDMS ranges from about 10 to about 100 , such as about 25 to about 55, such as about 35. 6. Fremgangsmåden ifølge et hvilket som helst af kravene 1 til 4 hvori den terminalt di- eller monofunktionaliserede B-blok er en forbindelse ifølge Formel ii) ii): Xi-L}-PDMS-L2, hvori Xi betegner en primær amingruppe (-NFL·); Li betegner en binding eller en kulbrintekæde, såsom en alkylen, f. eks. en -(CFLjy- gruppe hvori y er et heltal udvalgt fra 1, 2, 3, og 4; Lj2 mangler eller betegner en kulbrintekæde, såsom alkylen, f. eks, en -(CFLjy- gruppe hvor y er et heltal udvalgt fra 1, 2, 3, og 4; og det gennemsnitlige antal af repetitive enheder of PDMSen ligger i intervallet fra cirka 10 til cirka 100, såsom cirka 20 til cirka 30.The method of any of claims 1 to 4 wherein the terminally di- or monofunctionalized B block is a compound of Formula ii) ii): X 1 -L} -PDMS-L 2, wherein X 1 represents a primary amine group (- NFL ·); Li represents a bond or a hydrocarbon chain, such as an alkylene, e.g., a - (CFLjy group wherein y is an integer selected from 1, 2, 3, and 4; Lj2 is missing or represents a hydrocarbon chain such as alkylene, f. example, one - (CFLjy group where y is an integer selected from 1, 2, 3, and 4; and the average number of repetitive units of the PDMS ranges from about 10 to about 100, such as about 20 to about 30. 7. Fremgangsmåden ifølge et hvilket som helst af kravene 1 til 4 og 6 hvori polymeren, B, er en terminalt monofunktionaliseret blokpolymer, og den opnåede blokcopolymer er overvejende en A-B blokcopolymer.The process of any one of claims 1 to 4 and 6 wherein the polymer, B, is a terminal monofunctionalized block polymer and the obtained block copolymer is predominantly an A-B block copolymer. 8. Fremgangsmåden ifølge et hvilket som helst af kravene 1 til 5 hvori polymeren, B, er en terminalt difunktionaliseret polymer, og den opnåede blokcopolymer er en blanding af A-B-A og A-B blokcopolymerer,The process of any one of claims 1 to 5 wherein the polymer, B, is a terminally difunctionalized polymer and the block copolymer obtained is a mixture of A-B-A and A-B block copolymers, 9. Fremgangsmåden ifølge et hvilket som helst af kravene 1 til 8 hvori fremgangsmåden udføres i en opløsningsmiddelblanding, der opløser alle af A+, B, A-B, og A-B-Å polymerer, der er til stede i reaktionsblandingen.The process of any one of claims 1 to 8 wherein the process is carried out in a solvent mixture which dissolves all of the A +, B, A-B, and A-B-Å polymers present in the reaction mixture. 10. Fremgangsmåden ifølge krav 9 hvori opløsningsmiddelblandingen omfatter acetonitril og methylenchlorid, fortrinsvist i forholdsintervaller fra 1:3 til 3:1.The process of claim 9 wherein the solvent mixture comprises acetonitrile and methylene chloride, preferably in ratio ranges of 1: 3 to 3: 1. 11. Fremgangsmåden ifølge krav 10 hvori den hydrofobe polymer, B, er opløst i det apolære opløsningsmiddel forud for tilsætning til reaktionsbeholderen,The process of claim 10 wherein the hydrophobic polymer, B, is dissolved in the apolar solvent prior to addition to the reaction vessel. 12 En vesikel omfattende - en triblokcopolymer ifølge Formel I,A vesicle comprising - a triblock copolymer of Formula I, - en diblokcopolymer ifølge Formel II,- a diblock copolymer of Formula II, (II); og et transmembrant molekyle udvalgt fra gruppen bestående af aquaporin-vandkanalmolekyler; hvori i Formlerne I og II Ri og R2 er uafhængigt udvalgt fra gruppen bestående af ligekædet eller forgrenet Cj til Ce alkyl, sekundær eller tertiær amin, -Oil, SH, -CHO, -C2H4OH, -COCII3, -COOH, methacrylat og epoxider; R3 er ligekædet eller forgrenet lavere alkyl; Li og L2 er uafhængigt af hinanden -(CFFjy-, hvori y er et heltal udvalgt fra 1, 2, 3, og 4; eller Li er -(CH2)y-, og L2 mangler; m er et heltal mellem 10 og 100; og n er et heltal mellem 3 og 50; og i Formel II kan R2 valgfrit betegne hydrogen.(II); and a transmembrane molecule selected from the group consisting of aquaporin-water channel molecules; wherein in Formulas I and II R 1 and R 2 are independently selected from the group consisting of straight or branched C 1 to C 6 alkyl, secondary or tertiary amine, -O 1, SH, -CHO, -C 2 H 4 OH, -COCII 3, -COOH, methacrylate and epoxides; R 3 is straight or branched lower alkyl; Li and L2 are independent of each other - (CFFjy-, wherein y is an integer selected from 1, 2, 3, and 4; or Li is - (CH2) y-, and L2 is missing; m is an integer between 10 and 100 and n is an integer between 3 and 50, and in Formula II R2 can optionally represent hydrogen. 13. En blokcopolymersammensætning omfattende en forbindelse ifølge Formel I og en forbindelse ifølge Formel II, hvor sammensætningen fremstilles ifølge fremgangsmåden ifølge krav 1, og hvori hver af forbindelserne har en PDMS-derivatiseringsgrad på mere end cirka 30 til 40%, såsom mere end eller lig med 50¾).A block copolymer composition comprising a compound of Formula I and a compound of Formula II, wherein the composition is prepared according to the method of claim 1, wherein each of the compounds has a degree of PDMS derivatization of more than about 30 to 40%, such as more than or equal to with 50¾).
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