Patent Application
20220106440
This patent application claims priority from Italian patent application no. 102019000002891 filed on 28 Feb. 2019, the entire disclosure of which is incorporated herein by reference.
The present invention relates to a method to prepare branched polymers of lactic acid having a low melt viscosity.
For some time now polylactic acid (PLA) has been attracting a great deal of industrial interest due to the fact it comes from renewable sources and to its easy degradation both in the human organism (useful as suture thread) and during composting. In this regard, a part of research concentrates on improving the features of PLA to be able to use it advantageously in packaging. In particular, attempts are made to improve its rheological properties, thermal stability and barrier effect.
To date, modifications to PLA above all concern the use of nanofillers, or the use of particular comonomers. In particular, nano composites obtained by mixing PLA with graphite, montmorillonite or other silicates are known; instead, generally known branched PLAs generally have a dendrimer structure with synthesis strictly controlled and with polydispersity of the molecular weights of approximately 1.
One of the limits of PLA for a correct industrial application thereof also concerns its high melt viscosity, necessary to achieve adequate mechanical properties. As can be immediately understood by those skilled in the art, this limit affects the possibility of processing the PLA-based polymer by means of injection moulding and, consequently, the possibility of producing a large variety of products.
Therefore, there was a need to provide a solution that allowed the preparation of structurally modified PLA and that, at the same time, lowered its viscosity so that it could be processed by means of injection moulding.
The inventors of the present invention have provided a solution that allows PLA to be modified bestowing thereon both the features belonging to materials to be used in the packaging sector and, at the same time, a lower viscosity than that of the initial PLA and that allows it to undergo injection moulding.
The subject matter of the present invention is a method to prepare a polylactic acid-based polymer and having a molecular weight (Mn) greater than 25,000 g/mol; said method comprising
(i) a first compound with general formula I
wherein n ranges from 1 to 20
(ii) a second compound chosen among citric acid, malic acid and derivatives thereof with the carboxylic groups partially or completely in the form of ester or anhydride and with the hydroxyl groups partially or completely in the form of ester.
The (mean) molecular weight values indicated in the present description and in the claims were calculated with the standard international method ASTM D4001-13.
The polylactic acid-based polymers according to the present invention are produced starting from lactide and not from lactic acid, as they are structural polymers with high mechanical properties which must be processed by injection moulding. To reach the required molecular weight (Mn>25,000 g/mol) it is necessary to start from lactide and not from lactic acid. In fact, it has been experimentally proven that the synthesis of polylactic acid-based polymers starting from lactic acid gives rise to polymers with low molecular weight, due to the impossibility of completely removing the water from the reaction medium, thus resulting in a composition having a balance that cannot be modified in the melt polymerization conditions. The maximum molecular weight that can be achieved with the use of lactic acid is Mn<1,500 g/mol and only with some synthesis techniques was it possible to achieve Mn<6,500 g/mol. Preferably, said first and said second compounds are present according to a molar ratio ranging from 0.05 to 2, more preferably ranging from 0.075 to 1, even more preferably ranging from 0.1 to 0.75.
Preferably, said first and said second compounds are present in a quantity ranging from 0.1% to 25% by weight, more preferably from 1% to 10% by weight, even more preferably from 1.5% to 5% by weight, relative to the weight of the lactide monomer.
Preferably, said polymerization catalyst is used in a quantity ranging from 0.0001% to 1% by weight, more preferably from 0.01% to 0.5% by weight, even more preferably from 0.015% to 0.25% by weight, relative to the weight of the lactide monomer.
Preferably, the compound with general formula I has a n ranging from 1 to 15, even more preferably ranging from 1 to 10.
Preferably, the second compound is chosen among citric acid, malic acid, trimethyl citrate, triethyl citrate, tripropyl citrate, triisopropyl citrate, tributyl citrate, triisobutyl citrate, tritertbutil citrate, trimethyl acetyl citrate, triethyl acetyl citrate, tripropyl acetyl citrate, triisopropyl acetyl citrate, tributyl acetyl citrate, triisobutyl acetyl citrate, tritertbutyl acetyl citrate, dimethyl malate, diethyl malate, dipropyl malate, diisopropyl malate, dibutyl malate, diisobutyl malate, ditertbutyl malate, dimethyl acetyl malate, diethyl acetyl malate, dipropyl acetyl malate, diisopropyl acetyl malate, dibutyl acetyl malate, diisobutyl acetyl malate, ditertbutyl acetyl malate.
Preferably, the method forming the subject matter of the present invention comprises a solid state polycondensation (SSP) step, during which the polymer mass obtained from the cooling step is heated at a temperature ranging from 100 to 160° C. and at a pressure ranging from 10−3 to 1 torr.
Preferably, said solid state polycondensation step comprises a preliminary operation of granulation of the polymer, during which the polymer mass obtained from the cooling step is granulated.
Examples of embodiment of the present invention are provided hereunder purely by way of non-limiting illustration.
The examples set forth below provide for the synthesis of some polymers representative of the invention starting from LL-lactide, as main reactant monomer, by means of ring-opening polymerization.
In general, the use of reactants with free carboxylic acids requires the use of a larger amount of catalysts capable of promoting ring-opening polymerization and/or higher molten state reaction times to obtain a high conversion of the lactide monomer.
In general, the use of reactants with ester derivatives of carboxylic acids requires the use of catalysts capable of promoting transesterification reactions.
The polymers indicated in the examples were obtained by means of ring-opening polymerization in the presence of suitable catalysts, described in said examples.
As already indicated, the choice of the catalyst is not selective for the purposes of the final properties of the polymer.
The method used for the examples is as follows:
Before heating the reaction flask loaded with the reactants in the oven, the reaction atmosphere is purged to eliminate the oxygen present with suitable vacuum-inert gas (N2) cycles to then keep the reaction environment under a continuous flow of inert gas at around 50 ml/min.
The reaction is conducted by means of heating to 190° C. for the time indicated in the examples.
At the end of the reaction, the polymer is left to cool to room temperature, maintaining the nitrogen flow and is subsequently recovered as solid material at room temperature.
The polymers thus recovered are subjected to a further solid state polycondensation (SSP) step.
The solid state polycondensation step is conducted using the following methodology: the polymer is broken down into small granules (from 1 to 8 mm) and is placed in a 250 ml single-neck flask equipped with a single-neck cylindrical joint, in turn equipped with a stopcock to which a mechanical vacuum pump is connected.
The SSP is conducted at a temperature of 150° C. in vacuum conditions of 10−1 Torr for 15 hours.
During the SSP step most of the residual lactide not reacted during the ring-opening polymerization step and any volatile reaction products are also eliminated.
By convention in the examples below the polymers obtained will be called:
In each of the examples below, the related polymer (TQ) obtained in the ring-opening polymerization step is partly analyzed as is and partly subjected to the SSP process to be analyzed subsequently.
The results of the analyses are set forth in Tables I and II below.
With the ring-opening polymerization methodology described above we obtain a polymer from the following formulations and utilizing the following reaction conditions:
25 g of LL-lactide
106.5 mg of glycerine
625.2 mg of tributyl citrate
7.7 mg of Sn octanoate (catalyst)
The reaction is conducted for 3 hours at 190° C.
25 g of LL-lactide
106.5 mg of glycerine
552.1 mg of triethyl-acetyl-citrate
7.7 mg of Sn octanoate (catalyst)
The reaction is conducted for 3 hours at 190° C.
25 g of LL-lactide
53.2 mg of glycerine
232.6 mg of malic acid
7.6 mg of Sn octanoate (catalyst)
The reaction is conducted for 6 hours at 190° C.
25 g of LL-lactide
416.7 mg of polyglycerol-3,
1.56 g of tributyl citrate
8 mg of Sn octanoate (catalyst)
The reaction is conducted for 4 hours at 180° C.
25 g of LL-lactide
416.7 mg of polyglycerol-3
1.56 g of tributyl citrate
8 mg of Sn octanoate (catalyst)
8 mg of Mn acetate tetrahydrate (catalyst)
8 mg of Co acetate tetrahydrate (catalyst)
The reaction is conducted for 4 hours at 190° C.
25 g of LL-lactide
416.7 mg of polyglycerol-3
581.5 mg of malic acid
78 mg of Sn octanoate (catalyst)
The reaction is conducted for 6 hours at 200° C.
25 g of LL-lactide
416.7 mg of polyglycerol-3
833.1 mg of citric acid
79 mg of Sn octanoate (catalyst)
The reaction is conducted for 6 hours at 190° C.
25 g of LL-lactide
1.32 g of polyglycerol-10
2.00 g of citric acid
85 mg of Sn octanoate (catalyst)
The reaction is conducted for 6 hours at 190° C.
25 g of LL-lactide
1.32 g of polyglycerol-10
2.79 g of malic acid
87 mg of Sn octanoate (catalyst)
The reaction is conducted for 6 hours at 190° C.
25 g of LL-lactide
1.32 g of polyglycerol-10
3.75 g of tributyl citrate
9 mg of Sn octanoate (catalyst)
The reaction is conducted for 3 hours at 190° C.
25 g of LL-lactide
7.5 mg of Sn octanoate (catalyst)
The reaction is conducted for 3 hours at 190° C.
The polymers obtained in the examples described were analyzed to assess their properties by means of:
The amount of residual monomer was also determined.
The analysis techniques used are described below.
DSC Analysis:
DSC analyses were conducted using 40 μl aluminium crucibles weighing around 5-10 mg of sample. The heat cycle used to conduct the analyses is the following:
The following were considered as thermal properties of the synthesized polymers:
TGA Analysis:
TGA analyses were conducted using an alumina crucible weighing around 5-10 mg of sample. The heat cycle used to conduct the analyses is the following:
The temperatures at which the loss of 5% by weight (T5%), of 10% by weight (T10%) and of 50% by weight (T50%) occurred were considered as properties of the synthesized polymers.
Rheological Analysis:
Rheological analyses were conducted, after accurate drying of the samples analyzed, by means of a rotational rheometer equipped with a 25 mm parallel plate measuring instrument at 190° C. in “frequency sweep” with variation of the oscillation frequency from 100 Hz to 0.1 Hz and with constant oscillation amplitude at 5%.
The zero shear rate complex viscosity ([η0]) extrapolated from the rheological curves obtained was considered as property of the synthesized polymers.
SEC Analysis:
SEC analyses were conducted using the following chromatographic system:
Calibration of the SEC system was carried out with polystyrene standards in the molecular mass range from 106 to 2,000,000 Dalton.
The number mean molecular weight (Mn) in terms of polystyrene equivalent (system calibration) and distribution of the molecular masses (D) equivalent to the ratio between the weighted mean molecular weight (Mw) and the number mean molecular weight (Mn) both in terms of polystyrene equivalent were considered as properties of the synthesized polymers.
Two tables summarizing the properties measured for the synthesized polymers are set forth below. Where not indicated the properties were not measured.
The polymers of examples 1 to 10 all have lower melt viscosity relative to the comparison polymers. The semi-crystalline polymers (i.e., those with a Tcc and Tm value in Table I), due to the low viscosity relative to the comparison polymers, can be more easily injection moulded. The wide distribution of molecular weights (D in Table II) although in the presence of a lower Mn relative to the comparison polymers, implies that, among polymer chains, there are species with high molecular weight essential to ensure adequate mechanical properties of the polymer. Therefore, the combination of these two factors (low viscosity and wide distribution of the molecular weights) allows to obtain polymers that are easily injection moulded (i.e., possibility of filling the moulds more quickly or of filling more complex moulds with thin parts) with adequate mechanical properties.
Amorphous polymers (those without Tm and Tcc in Table I), due to the low viscosity and to their amorphous nature, can be used as plasticizers to facilitate processing during injection moulding of PLA.
| Number | Date | Country | Kind |
|---|---|---|---|
| 102019000002891 | Feb 2019 | IT | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/IB2020/051267 | 2/14/2020 | WO | 00 |
