Method for the production of polymers

Abstract

The present invention relates to a process for preparing polymers by polycondensation catalysed by transition metals. These polymers are of great importance in, in particular, the fast-growing field of organic semiconductors. The polymers obtained by the process of the invention can be prepared with greater reproducibility and in higher purity than polymers obtained according to the prior art.

1 - 29 . (canceled) 
     
     
         30 . A process for preparing polymers or oligomers comprising the step of polycondensing monomers by means of C—C or C—N coupling reactions in the presence of a solvent or solvent mixture and at least one transition metal catalyst, and optionally in the presence of at least one base and/or at least one additive, wherein said polymerization step is carried out in at least one continuous tube reactor,
 wherein said C—C or C—N coupling reaction is selected from the group consisting of Suzuki couplings, Yamamoto couplings, Hartwig-Buchwald couplings, Stille couplings, Heck couplings, Sonogashira couplings, Negishi couplings, Hiyama couplings, and Grignard cross-couplings and 
 the polycondensation proceeds according to the reaction shown in Scheme 1 or to the reaction shown in Scheme 2:
     n X—Ar-X+ n Y-M-Y→—[Ar-M] n -+X—Y  (Scheme 1)
 
     n X—Ar-(M) m -Y→—[Ar-(M) m ] n -  (Scheme 2)
 
 
 wherein 
 X identically or differently on each occurrence is chlorine, bromine, iodine, fluoroalkylsulphonate, or perfluoroalkylsulphonate; 
 Y identically or differently on each occurrence is X, B(OH) 2 , B(OR) 2 , BR 2 , SnR 3 , NR—H, NH 2 , MgCl, MgBr, MgI, SiR 2 F, SiRF 2 , ZnCl, ZnBr, or ZnI; or H if Y is bound directly to a vinylic or acetylenic bond of M; 
 Ar identically or differently on each occurrence is a divalent aromatic or heteroaromatic ring system having from 5 to 60 aromatic ring atoms, optionally substituted by one or more radicals R or OR; 
 M identically or differently on each occurrence is Ar or an organic group having from up to 60 carbon atoms, substituted by one or more vinyl or acetylene groups; 
 R identically or differently on each occurrence is H, a linear alkyl chain having up to 40 carbon atoms, or a branched or cyclic alkyl chain having from 3 to 40 carbon atoms, wherein one or more nonadjacent carbon atoms of said linear, branched, and cyclic alkyl chains is optionally replaced by N—R 1 , O, S, O—CO—O, CO—O, —CR 1 ═CR 1 —, or —C≡C—, and wherein one or more H atoms is optionally replaced by F, Cl, Br, I, CN, or an aromatic or heteroaromatic ring system having from 5 to 60 aromatic ring atoms, wherein said aromatic or heteroaromatic ring system is optionally substituted by one or more nonaromatic radicals R; and wherein two or more radicals R optionally define a ring system;
 R 1  identically or differently on each occurrence is H or an aliphatic or aromatic hydrocarbon radical having from up to 20 carbon atoms; 
 n is on each occurrence a number in the range of from 10 to 10 000; 
 m is on each occurrence either 0 or 1; and 
 
 wherein the broken lines indicate the linkage in the polymer chain. 
 
     
     
         31 . The process according to  claim 30 , wherein said continuous tube reactor has a volume of less than or equal to 20 ml. 
     
     
         32 . The process according to  claim 30 , wherein said continuous tube reactor comprises channels having a diameter of from 10 μm to 20 mm. 
     
     
         33 . The process according to  claim 30 , wherein said continuous tube reactor comprises microsystem apparatus having a volume of less than or equal to 1000 μl, and at least two inlets and at least one outlet, at least one mixing element in which the starting solutions are intensively mixed at least once, at least one reaction and potentially at least one analysis element and potentially at least one demixing element. 
     
     
         34 . The process according to  claim 30 , wherein said step comprises pumping reaction solution into said continuous tube reactor so that said reaction solution flows through said continuous tube reactor at a flow rate of from 0.01 μL/min to 100 mL/min. 
     
     
         35 . The process according to  claim 30 , wherein said step comprises conveying reaction solution through two or more continuous tube reactors connected in series. 
     
     
         36 . The process according to  claim 30 , wherein said step comprises conveying reaction solution through two or more continuous tube reactors connected in parallel. 
     
     
         37 . The process according to  claim 30 , wherein said step is carried out at a temperature of from −80° C. to 250° C. 
     
     
         38 . The process according to  claim 30 , wherein polycondensation progress is monitored and controlled by means of viscometry. 
     
     
         39 . The process according to  claim 30 , wherein said transition metal catalyst comprises a transition metal or a transition metal compound selected from the group consisting of palladium, palladium compounds, nickel, nickel compounds, cobalt, cobalt compounds, iron, and iron compounds. 
     
     
         40 . The process according to  claim 45 , wherein each X is identical and each Y is identical. 
     
     
         41 . The process according to  claim 30 , wherein said at least one transition metal catalyst comprises or is prepared from at least one compound containing palladium having an oxidation state of 0. 
     
     
         42 . The process according to  claim 30 , wherein said at least one transition metal catalyst comprises or is prepared from at least one compound containing palladium having an oxidation state of +II. 
     
     
         43 . The process according to  claim 48 , wherein said at least one transition metal catalyst comprises at least one ligand selected from the group consisting of triarylphosphines; triheteroarylphosphines; diarylalkylphosphines; diheteroarylalkylphosphines; aryldialkylphosphines; heteroaryldialkylphosphines; trialkylphosphines; halophosphines; dihalophosphines; alkoxyphosphines; aryloxyphosphines; heteroaryloxyphosphines; dialkoxyphosphines; diaryloxyphosphines; and diheteroaryloxyphosphines; wherein the phosphorus substituents of said triarylphosphines, triheteroarylphosphines, diarylalkylphosphines, diheteroarylalkylphosphines, aryldialkylphosphines, heteroaryldialkylphosphines, and trialkylphosphines are optionally identical, different, chiral, or achiral, and wherein one or more of said phosphorus substituents optionally link the phosphorus substituents of a plurality of phosphines and these linkages can also occur via one or more metal atoms. 
     
     
         44 . The process according to  claim 30 , wherein said at least one transition metal catalyst is a heterogeneous or immobilized palladium catalysts. 
     
     
         45 . The process according to  claim 30 , wherein said at least one transition metal catalyst is nickel or a nickel compound. 
     
     
         46 . The process according to  claim 51 , wherein said nickel or nickel compound is selected from the group consisting of elemental nickel; disperse metallic nickel; colloidal metallic nickel; supported nickel; unsupported nickel; nickel sponge; nickel on kieselguhr; nickel on aluminium oxide; nickel on silica; nickel on carbon; nickel(II) carboxylates; nickel(II) ketoketonates; nickel(II) halides; nickel(II) carbonate; nickel(II) nitrate; nickel(II) sulphate; olefinnickel(II) halides; allylnickel(II) halides; addition compounds of the type NiL 2 (Hal) 2 , wherein Hal is chlorine, bromine, iodine and L is an uncharged ligand; bis(cyclooctadiene)nickel(0); and tetrakis(triphenylphosphine)nickel(0). 
     
     
         47 . The process according to  claim 30 , wherein said step is carried out in the presence of at least one base. 
     
     
         48 . The process according to claim  53 , wherein said at least one base is selected from the group consisting of alkali metal hydroxides; alkaline earth metal hydroxides; alkali metal oxides; alkaline earth metal oxides; alkali metal carboxylates; alkaline earth metal carboxylates; alkali metal carbonates; alkaline earth metal carbonates; alkali metal hydrogencarbonates; alkaline earth metal hydrogencarbonates; alkali metal phosphates; alkaline earth metal phosphates; alkali metal hydrogenphosphates; alkaline earth metal hydrogenphosphates; alkali metal fluorides; alkaline earth metal fluorides; metal alkoxides; organic hydroxides; organic amines; nitrogen-containing aromatic heterocycles; nitrogen-containing nonaromatic heterocycles; and mixtures thereof. 
     
     
         49 . The process according to  claim 30 , wherein said solvent is selected from the group consisting of aromatic solvents, straight-chain ethers, branched ethers, cyclic ethers, N-containing heterocyclic solvents, alcohols, dipolar aprotic solvents, organic esters, nitriles, sulphoxides, organic amides, organic carbonates, halogenated solvents, straight-chain hydrocarbons, branched hydrocarbons, cyclic hydrocarbons, and mixtures thereof. 
     
     
         50 . The process according to  claim 30 , wherein said at least one transition metal catalyst is present in an amount of from 0.00001 to 50 mol %, based on the number of C—C or C—N bonds to be formed. 
     
     
         51 . The process according to  claim 30 , further comprising the step of purifying said polymers or oligomers; wherein said purification is carried out by means of extraction, optionally using complexing agents; by means of ion exchangers, which are optionally bound to the wall of the continuous tube reactor; or by means of extraction with inorganic mineral acids, optionally performed at elevated temperature. 
     
     
         52 . The process according to  claim 30 , wherein said purification is carried out in one or more mixing and demixing steps in said continuous tube reactor.