# Patent

## Title
Catalytic process for polymerising cyclic carbonates issued from renewable resources

## Abstract

This invention relates to the polymerisation of five-, six- or seven-membered cyclic carbonates by ring-opening polymerisation in the presence of a system comprising a metal salt such as triflate, triflimidate, acetylacetonate or carboxylate and an alcohol.

## Background
This invention relates to the synthesis of polycarbonates prepared from cyclic monomers derived from the biomass in the presence of a system comprising a metal catalyst and a transfer agent. It also relates to the resulting polymers derived from these cyclic monomers.
Several methods have been developed to prepare polycarbonates. The starting material is selected either from a five- or from a six-membered carbonate monomer. There is an abundant literature describing the synthesis of these compounds. The synthesis of six-membered carbonates is described for example in Bhanage et al. (Bhanage B. M., Fujita S., Ikushima Y., Arai M., in Green Chemistry, 5, 429, 2003), or in Wang et al. (Wang X. L., Zhuo, R. X., Liu L. J., He F., Liu G., in J. Polym. Sci. Part A, 40, 70, 2002), or in Wolinsky et al. (Wolinsky J. B., Ray III W C., Colson Y. L., Grinstaff M. W., in Macromolecules, 40, 7065, 2007, or in Gasset et al (EP-A-0,955,298).
The synthesis of five-membered carbonates is described for example in Aresta and Dibenedetto (Aresta M., Dibenedetto A., J. Mol. Catal. A: Chem., 257, 149, 2006) or in Robicki et al. (Robicki G., Rakoczy P., Parzuchowski P., in Green Chem., 7, 529, 2005) or in Ubaghs et al. (Ubaghs L., Fricke N., Keul H., Hôcker H., in Macromol. Rapid Comm., 25, 517, 2004), or in Komura et al. (Komura H., Yoshino T., Ishido Y., in Bulletin of the chemical society of Japan, 46, 550, 1973) or in Matsumoto et al. (Matsumoto K., Fuwa S., Shimojo M., Kitajima H., in Bull. Chem. Soc. Jpn, 69, 2977, 1996).
Polymerisation of carbonates was typically carried out by ring-opening of the five- or six-membered carbonates either by organometallic catalysis or by organic catalysis. The advantage of organometallic catalysis was that it offers a controlled polymerisation. The most frequently used catalytic components were based on

    
    
        Sn(Oct)2 as described for example in Kricheldorf and Stricker (Kricheldorf H. R., Stricker A., in Macromol. Chem. Phys. 201, 2557, 2000)
        or biocompatible metals such as Mg, Ca, Fe or Zn as described for example in Darensbourg et al. (Darensbourg D., Wonsook C., Poulomi G., Casseday R., in Macromol. 37, 4374, 2006) or in Dobrzinsky et al. (Dobrzinsky P., Pastusiak M., Bero M., in J. Polym. Sci. Part A Polym. Chem., 43, 1913, 2004) or in Kuran et al. (Kuran W., Sobczak M., Listos T., Debek C., Florjanczyk Z., in Polymer. 41, 8531, 2000)
        or group 3 metal (including the lanthanide series) complexes such as described for example in Palard et al. (Palard I., Schappacher M., Belloncle B., Soum A., Guillaume S., in Chem. Eur. J. 13, 1511, 2007) or in Zhao et al. (Zhao B., Lu C., Shen Q., in J. Appl. Polym. Sci., 25, 517, 2004) or in Sheng et al. (Sheng H., Zhou L., Zhang Y., Yao Y., Shen Q., in J. Polym. Sci. Part A Polym. Chem., 45, 1210, 2007).
    
    


The advantage of organic catalysis was that it offered polymerisation under mild conditions with non-metal catalyst components. They were based on

    
    
        enzymes such as described for example in Bisht et al. (Bisht S. K., Svirkin Y. Y., Henderson L. A., Gross R. A., in Macromolecules, 30, 7735, 1997) or in Gross et al. (Gross R. A., Kumar A., Kalra B., in Chem. Rev., 101, 2109, 2001) or in Koboyashi et al. (Koboyashi S., Uyama H., Kimura S., in Chem. Rev., 101, 3793, 2001).
        organic compounds such as amines or guanidine as described for example in Nederberg et al. (Nederberg F., Lohmeijer G. B., Leibfarth F., Pratt R. C., Choi J., Dove A. P., Waymouth R. M., Heidrich J. L., in Biomacromolecules, 8, 153, 2007) or in Mindemark et al. (Mindemark J., Hilborn J., Bowden T., in Macromolecules, 40, 3515, 2007). They can also be based on strong Brönsted acids such as triflic acid as described for example in Kricheldorf, H. R. et al. (Kricheldorf, H. R. Weegen-Schulz, B. Jenssen, J. Macromolecular Symposia 1992, 60, 119-131) or in Endo T. et al (Endo T. Ariga, T. Takata, T. Macromolecules, 1997, 30, 737-744).
    
    


On the other hand, Lewis acids based on metal groups 2, 3, 4, 12, 13 such as magnesium, calcium, scandium, yttrium, cerium, samarium, ytterbium, zirconium, zinc, aluminum and tin triflates or triflimidates are known to be effective catalysts, in combination with a protic source such as an alcohol or a carboxylic acid, for the ring-opening polymerisation of cyclic esters such ε-caprolactone and lactide, as described for example in Moller et al. (Moller M., Kange R., Hedrick J. L., in J. Polym. Sci. A: Polym. Chem., Vol. 38, 2067-2074 (2000)), in Nomura et al. (Nomura N., Taira A., Nakase A., Tomioka T., Okada M., in Tetrahedron, Vol. 63, 8478-8484 (2007)), in Nomura et al. (Nomura N., Taira A., Tomioka T., Okada M., in Macromolecules, Vol. 33, 1497-1499 (2000)), in Wang et al. (Wang Y., Kunioka M., in Macromol. Symp. Vol. 224, 193-205 (2005)), in Kunioka et al. (Kunioka M., Wang Y., Onozawa S. Y., in Macromol. Symp. Vol. 224, 167-179 (2005)), in Gorczynski et al. (Gorczynski J. L., Chen J., Fraser C. L., in JACS, Vol. 127, 14 956-14 957 (2005)), in Dobrzynski et al. (Dobrzynski P., Pastusiak M., Bero M., in J. Polym. Sci. A: Polym. Chem., Vol. 43, 1913-1922 (2005)), in Funasabi et al. (Funasabi M., Kunioka M; in Macromol. Symp. 2005, 224, 309.32.
It is an aim of the present invention to provide a method for polymerising cyclic carbonate compounds using small amounts of a metal catalyst.
It is another aim of the present invention to use, in combination with the small amounts of the metal catalyst, large amounts of a transfer agent to achieve so-called “immortal” polymerisation of cyclic carbonate compounds.
It is a further aim of the present invention to control and tune the characteristics and properties of the resulting polycarbonates.
In particular, it is another aim to prepare functionalised polycarbonates selectively end-capped by a group originating from the transfer agent.
It is yet another aim of the present invention to apply the method of the immortal ring-opening polymerisation to new cyclic carbonates derived from glycerol.
It is yet a further aim of the present invention to develop a catalyst system operative on technical grade carbonate monomers, without specific preliminary purification.
Any one of those aims is, at least partially, fulfilled by the present invention.



LIST OF FIGURES
FIG. 1 represents the 1H NMR spectrum of the precipitated polymer prepared in example 1.



Accordingly, the present invention discloses a process for polymerising five- or six- or seven-membered cyclic carbonates by ring-opening polymerisation in the presence of a system comprising a metal salt such as triflate, triflimidate, acetylacetonate or carboxylate and an alcohol, characterised in that the number average molecular weight Mn of the final polymer is controlled by the monomer/alcohol ratio.
The alcohol is acting as co-activator and as transfer agent.
The metallic salt can be selected from metallic complexes of formula M(OSO2CF3)n, hereafter referred to as triflates or OTf or M(N(OSO2CF3)2)n, hereafter referred to as triflimidates or NTf2 or M(RC(O)CR2C(O)R)n, hereafter referred to as acetylacetonates or acac or (R′′CO2)nM, hereafter referred to as carboxylates, wherein M is a metal Group 2, 3, including the lanthanide series, hereafter referred as Ln, 4, 12, 13, 14 or 15 of the periodic Table, wherein each R is selected independently from a linear or branched hydrocarbyl radical having from 1 to 12 carbon atoms, substituted or not by for instance an halogen or heteroatom, wherein each R′′ is selected independently from a perfluorinated alkyl or aryl residue having from 1 to 12 carbon atoms, and wherein n is the valence of M.
Preferably, M is Mg(II), Ca(II), Sc(III), Y(III), Sm(III), Yb(III), Zr(IV), Fe(II), Fe(III), Zn(II), Al(III) Sn(IV) or Bi(III). More preferably, it is Al, Zn or Sc, Al being the most efficient metal.
Preferably each R is selected independently from a alkyl group such as CH3 or a substituted alkyl group such as CF3, More preferably, they are all the same and they are CF3.
Preferably, R′′ is (C6F5) or (CF3), or CF3(CF2)m wherein m is an integer from 1 to 6.
The alcohol can be represented by formula R′OH wherein R′ is an hydrocarbyl, linear or branched, having from 1 to 20 carbon atoms. Preferably R′ is a secondary alkyl residue or benzylic group, more preferably it is isopropyl (iPr) or benzyl (Bn). It can also be a poly-ol such as diol, triol or higher functionality polyhydridic alcohol. Typically it can be selected from propanediol or trimethylolpropane, possibly derived from biomass such as glycerol or any other sugar-based alcohol such as for example erythritol or cyclodextrine. All alcohols can be used individually or in combination.
Among the preferred catalytic compounds according to the present invention, one can cite Al(OTf)3, Al(NTf2)3, Mg(OTf)2, Ca(OTf)2, Zn(OTf)2, Sc(OTf)3, Bi(OTf)3, Fe(acac)3, Al(OCOCF3)3, ZN(OCOCF3)2, Zn(acac)2,
In these embodiments, the catalyst system also comprises an alcohol. In the present invention, the catalyst system operates via a so-called “activated monomer pathway”. That means that the metal centre of the metal salt behaves as a Lewis acid onto which the carbonyl function of the monomer coordinates in the course of catalysis. This results eventually in an increase of the electrophilicity at the carbon atom of the monomer carbonyl group, which is therefore prone to being attacked by an external nucleophile such as the alcohol co-catalyst, or any other protic source such as for example water or carboxylic acid.
The present mechanism differs from the so-called “coordination-insertion” mechanism. In the present mechanism, the nucleophile is external in that it is not sigma-bonded to the metal center in the pre-catalyst, while in the coordination-insertion mechanism, the nucleophile is included in the pre-catalyst and active catalyst as a sigma-bonded ligand of the metal complex, under the form of an alkoxide, amide or borohydride group.
In the current “activated monomer pathway”, the alcohol plays two roles:

    
    
        as an external nucleophile for initiating the polymerisation via the ring-opening of the activated monomer; 1 equivalent of alcohol per metal centre is used in the process;
        as a transfer agent, by generating multiple polymer chains; all excess alcohol molecules are used in this second process, and the final molecular weight of the polymer is a function of the alcohol-to-monomer ratio.
    
    


It can be represented schematically as follows:
1. Initiation mechanism by ring opening (ROP) of the activated monomer




2. Propagation and Transfer mechanism




In the “coordination-insertion” mechanism, the alcohol also plays two roles but in a different manner:

    
    
        the alcohol transforms the pre-catalyst, that has little or no activity, into an active alkoxide-metal species, via an alcoholysis process;
        as a transfer agent like in the other mechanism.
    
    


Excess alcohol acts as transfer agent, transferring propagating polycarbonate chains from the active metal center to dormant hydroxy-end capped polycarbonate chains. Accordingly, it is observed that the number average molecular weight increases when the monomer/alcohol ratio increases. The ratio monomer/alcohol is of from 5 to 1000, preferably it is of from 10 to 500.
Optionally, the alcohol can contain a functional group which will be selectively capping the terminus of each polycarbonate chain. This functional group can be used for various purposes. As non-limitating examples, one can cite:

    a) vinyl end-groups which can (i) promote further copolymerisation with other olefin-type monomers; or (ii) be transformed into other functional groups such as for instance epoxide, alcohol, or 1,2-diol.
    b) nitroxide or alkoxyamine end-groups which can promote controlled radical polymerisation and/or ring-opening polymerisations,
    c) fluorinated pony-tails.


The system described in the present invention allows transforming very large amounts of monomer with minute amounts of metal catalyst. The ratio monomer to metal is of from 100 to 1,000,000, preferably it is of from 10,000 to 500,000.
Polymerisation can be carried out in bulk or in solution. Usual aromatic and aliphatic hydrocarbons can be used for that purpose.
Polymerisation can be carried out on technical, unpurified monomer since the Lewis acids based metal catalysts are rather prone to withstand umpurity traces.
Polymerisation is conducted at a temperature ranging from 20° C. to 180° C., preferably between 100 and 150° C. The pressure ranges from 0.5 to 20 atm, preferably it is 1 atm.
The polycarbonates thus prepared show typically a unimodal molecular weight distribution that ranges from 1.1 to 5.0, more typically from 1.5 to 1.8.
The number average molecular weight Mn can be tuned by the monomer-to-alcohol ratio and ranges from 1 000 to 1 000 000 g/mol, more typically from 10 000 to 250 000 g/mol.
This polymerisation process is operative for 5- to 7-membered cyclic carbonates. Preferably, this polymerisation process is operative for 6-membered cyclic carbonates.
The polycarbonates that can be used in the present invention are selected for example from trimethylenecarbonate (TMC), 2-benzyloxy-trimethylenecarbonate (BTMC), 2-hydroxy-trimethylenecarbonate (TMCOH), 4-(benzyloxymethyl)-1,3-dioxolan-2-one (BDMC), 4-(hydroxymethyl)-1,3-dioxolan-2-one (DMCOH),
In particular, one can cite new cyclic carbonates such as 2-oxy-trimethylenecarbonate (OTMC), and dehydrotrimethylenecarbonate (DHTMC).




Copolymers resulting from any combinations of these monomers are also included in the present invention.
One of the main advantages of the present invention is that the cyclic carbonate monomer does not need to be purified. By unpurified is meant the technical grade taken off the shelf without any further treatment and thus containing water and free acid. The catalyst system of the present invention is very robust and does not have fragile covalent bonds as disclosed in the prior art Zn-based catalyst systems.
EXAMPLES
The polymerisation of trimethylenecarbonate (TMC) has been carried out with various catalyst components, alcohol initiators and polymerisation conditions.
Example 1
TMC, purified by drying over calcium hydride and finally recrystallised, was polymerised in the presence of a metal catalyst and an alcohol initiator R′OH.




BnOH was selected as the alcohol and the ratio TMC/Metal salt/ROH was set at 500:1:5. The polymerisation temperature and the polymerisation time were varied as indicated in Table I.
The conversion rate expressed in %, the theoretical and experimental number average molecular weight and the polydispersity index Pl, represented by Mw/Mn, are disclosed in Table 1.
The theoretical number average molecular weight was calculated as

Mntheo=[TMC]/[BnOH]×MTMC×conversion+MBnOH 

with MTMC=102.09 g/mol, MBnOH=108.14 g/mol

















TABLE I







Time

Conv
Mntheo
MnNMR
MnSEC

TON


Entry
cat.
(min)
T ° C.
(%)
(g · mol−1)
(g · mol−1)
(g · mol−1)
Mw/Mn
(mol/mol/h)
























1
Fe(acac)3
160
110
90
9300
10500
12050
1.56
169


2
Sc(OTf)3
150
60
19
nd
nd
nd
nd
38


3
Sc(OTf)3
120
110
78
8070
 9380
10100
1.47
195


4
Al(OTf)3
30
110
88
9090
Nd
13500
1.57
880


5
Al(OTf)3
60
110
96
9900
nd
13800
1.62
480


6
Zn(OTf)2
180
110
30
3170
 2920
nd
nd
50


7
Zn(OTf)2
30
150
97
10010 
 9790
11340
1.62
970


8
Ca(OTf)2
120
110
<10
nd
nd
nd
nd
<25


9
Ca(OTf)2
30
150
95
9806
11330
11680
1.64
950


10
Bi(OTf)3
60
110
99
10200 
11500
11900
1.45
495


11
Bi(OTf)3
30
150
99
10200 
10950
11400
1.51
990









The number and weight average molecular weights Mn and Mw, and polydispersity (Mw/Mn)index were determined by Size Exclusion Chromatography (SEC) in THF versus PS standards and corrected with a Mark-Houwink factor of 0.73.
The 1H NMR spectrum of a typical precipitated polymer prepared according to the above procedure can be seen in FIG. 1
It can be seen that Al is one of the most efficient metal at 110° C. It is speculated that the Lewis acidity of the metal plays an important role, the efficiency of the metal increasing with increasing acidity. Aluminum(III) trifalte is very active. High activities are also obtained with bismuth (III), calcium (II) and zinc(II) triflates.
Example 2
The polymerisation of unpurified trimethylene carbonate was carried out with Al(OTf)3 or Sc(OTf)3 and BnOH. By unpurified is meant the technical grade taken off the shelf without any further treatment and thus containing water and free acid. The ratio TMC/Metal triflate/BnOH was set at 10 000:1:10




Temp modifiee 110-150
The experimental conditions and results are displayed in Table II.















TABLE II







T
Time
Conv
Mntheo
MnSEC

TON


entry
cat.
(° C.)
(min)
(%)
(g · mol−1)
(g · mol−1)
Mw/Mn
(mol/mol/h)























1
Sc(OTf)3
110
900
76
77580
58900
1.76
 507


2
Sc(OTf)3
150
150
85
86880
20200
1.30
3400


3
Al(OTf)3
110
120
75
76680
54200
1.53
3750


4
Al(OTf)3
150
20
92
104960 
61200
1.42
27600 









It can be seen that very high conversions can be reached with small amounts of metal catalysts, as low as 100 ppm, leading to polycarbonates with high molecular weights and narrow polydispersities.
Example 3
The polymerisation of technical-grade unpurified trimethylene carbonate was carried out with Al(OTf)3 and the nature of the alcohol was varied. The ratio [TMC]/[Metal trifiate]/[R′OH] was set at 10 000:1:10 and the ratio [TMC]/[Metal triflate]/[n-OH] was set at 500:1:5.




The experimental conditions and results are displayed in Table III.















TABLE III







T
Time
Conv
Mntheo
MnSEC

TON


entry
[R′OH]
(° C.)
(min)
(%)
(g · mol−1)
(g · mol−1)
Mw/Mn
(mol/mol/h)























1
PhCH2OH
110
120
75
76680
54200
1.53
3750


2
PhCH2OH
150
20
92
104970 
61200
1.42
27600 


3
iPrOH
110
150
68
69480
44600
1.48
2720


4
iPrOH
150
40
77
78650
26100
1.42
11550 


5
2-butanol
110
120
64
65410
43200
1.52
3200


6
2-butanol
150
20
84
85830
50200
1.44
25200 


7
3buten-2-ol
110
150
59
60850
51560
1.59
2360


8
3-buten-2-ol
150
30
91
93800
64900
1.58
18200 


9
4-bromophenol
110
150
80
81844
61280
1.46
3200


10
4-bromophenol
150
30
90
91970
59320
1.52
18000 


11
propanediol
110
60
98
10100
17300
1.50
 490


12
1,4-benzenedimethanol
110
60
94
 9730
12190
1.49
 470


13
glycerol
110
20
98
10100
 8490
1.71
1470









It can be seen that the nature of the alcohol can be varied while maintaining the catalyst performance. The alcohol, however, does affect the catalyst activity, and the best activities are observed with benzyl alcohol (BnOH).
Example 4
The polymerisation of technical-grade unpurified trimethylene carbonate was carried out with Al(OTf)3 and iPrOH or BnOH as the alcohol. The ratio TMC/Metal triflate/R′OH was largely increased and varied as shown in Table IV.

Mntheo=[TMC]/[R′OH]×MTMC×conversion+MR′OH 

with MTMC=102.09 g/mol, MBnOH=108.14 and MiPrOH=60.10 g/mol
X=amount of chain transfer agent arising from the monomer and calculated from

MnSEC=[TMC]/{X×([TMC]/[Al])+([R′nOH]/[Al])}×MTMC×conversion

Mn′theo=[TMC]/{Xav+[BnOH]}×MTMC×conversion, with Xav=average of all 7 X values=0.0056





The experimental conditions and results are displayed in Table IV.

















TABLE IV







[TMC]/[Al]/
Time
Conv
Mntheo
MnSEC

TON
X
Mn′theo


entry
ROH
[BnOH]
(min)
(%)
(g · mol−1)
(g · mol−1)
Mw/Mn
(mol/mol/h)
(%)
(g · mol−1)

























1
BnOH
10000/1/10
90
92
94030
53200
1.56
6130
0.076
60262


2
iPrOH
10000/1/10
90
94
96025
61230
1.55
6270
0.057
61522


3
BnOH
25000/1/10
240
88
224700 
83860
1.56
5500
0.067
93608


4
BnOH
25000/1/20
240
96
122616 
70120
1.54
6000
0.060
72108


5
BnOH
25000/1/50
240
84
42990
35770
1.56
5250
0.040
33580


6
BnOH
50000/1/20
480
90
229810 
102270 
1.53
5625
0.050
95730


7
BnOH
50000/1/50
480
75
76610
53730
1.59
4690
0.043
49150









It can be seen that, for a given [BnOH]/[Al] ratio (e.g. 10, 20 or 50), increasing the monomer loading from 10 000 up to 50 000, results in an increase of the molecular weight of the final polymer recovered. Also, for a given monomer loading (e.g. [TMC]/[Al]=10 000, 25 000 or 50 000), increasing the [BnOH]/[Al] ratio from 10 to 50, results in a decrease of the molecular weight of the final polymer recovered. This indicates that the molecular weight of the polycarbonate can be controlled by tuning the [TMC]/[Al]/[BnOH] ratio. One can note that the experimental molecular weights are always lower than the values (Mntheo) calculated from the [TMC]/[Al]/[BnOH] ratio. This indicates that some impurities contained in the technical-grade monomer also act as transfer agents. The amount of impurities (X) can be evaluated, and is found to be constant for a given batch of monomer. As expected, the Mn′theo values calculated by taking into account X content of impurities fit very well with the MnSEC values determined experimentally by SEC. This approach allows thus the <<at will>> preparation of polymers with predetermined molecular weights, based on the [TMC]/[Al]/[BnOH] ratio and the X content of <<transfer active>> impurities contained in the technical grade monomer.

## Claims

1. A process for polymerizing five-, six- or seven-membered cyclic carbonates by ring-opening polymerization in the presence of a system comprising:
a metal salt selected from the group consisting of triflate, triflimidate, acetylacetonate and carboxylate; and
an alcohol, wherein the alcohol is represented by the formula R′OH, a poly-ol selected from the group consisting of diol, triol and a polyhydridic alcohol represented by the form R′(OH)n, or a combination thereof, wherein R′ is an hydrocarbyl, linear or branched having from 1 to 20 carbon atoms, wherein the number average molecular weight Mn of the final polymer is controlled by the ratio monomer/alcohol, and wherein the ratio monomer/alcohol is of from 5 to 1000 and the ratio monomer to metal is of from 100 to 1,000,000,
and wherein the metal salt is a metallic complex of formula M(OSO2CF3)n (OTf) or M(N(OSO2CF3)2)n (NTf2) or M(RC(O)CR2C(O)R)n (acac) or (R′′CO2)nM (carboxylates), wherein M is a metal Group 2, 3, including the lanthanide series Ln, 4, 12, 13, 14 or 15 of the periodic Table, wherein each R is selected independently from a linear or branched hydrocarbyl radical having from 1 to 12 carbon atoms, wherein each R′′ is selected independently from a perfluorinated alkyl or aryl residue having from 1 to 12 carbon atoms, and wherein n is the valence of M.

2. The process of claim 1 wherein the metal is Mg(II), Ca(II), Sc(III), Y(III), Sm(III), Yb(III), Zr(IV), Fe(II), Fe(III), Zn(II), Al(III), Sn(IV) or Bi(III).

3. The process of claim 1 wherein the metal salt is Al(OTf)3, Al(NTf2)3, Mg(OTf)2, Ca(OTf)2, Zn(OTf)2, Sc(OTf)3, Fe(acac)3, Al(OCOCF3)3, ZN(OCOCF3)2, or Zn(acac)2.

4. The process of claim 1 wherein in alcohol R′OH or poly-ol R′(OH)n, R′ is a primary or secondary alkyl residue or a benzylic group_or combinations thereof.

5. The process of claim 4 wherein the alcohol is isopropyl (iPr) or benzyl (Bn) alcohol.

6. The process of claim 1 wherein the ratio monomer/alcohol is of from 10 to 500.

7. The process of claim 4 wherein the polyol is propanediol, 1,4-benzenedimethanol or glycerol.

8. The process of claim 1 wherein the alcohol additionally contains a functional group that is capping the end of each polycarbonate chain.

9. The process of claim 1 wherein the ratio monomer/metal is of from 10,000 to 500,000.

10. The process of claim 1 wherein the carbonate is a 5-, 6- or 7-membered cyclic carbonate selected from the group consisting of trimethylenecarbonate (TMC), 2-benzyloxy-trimethylenecarbonate (BTMC), 2-hydroxy-trimethylenecarbonate (TMCOH), 4-(benzyloxymethyl)-1,3-dioxolan-2-one (BDMC), 4-(hydroxymethyl)-1,3-dioxolan-2-one (DMCOH), 2-oxy-trimethylenecarbonate (OTMC), dehydrotrimethylenecarbonate (DHTMC), or a combination thereof.

11. The process of claim 10 wherein the five-, six- or seven-membered carbonates are OTMC or DHTMC.

12. The process of claim 10 wherein the five-, six- or seven-membered carbonate is an unpurified technical-grade product.

13. Homo- or co-polymers of carbonates obtained by the process of claim 1.

14. Homo- or co-polymers of carbonates obtained by the process of claim 10.