L(+) LACTIC ACID POLYMERS AND COPOLYMERS : STRUCTURE PROPERTY RELATIONSHIPS Dr. S. Sivaram National Chemical Laboratory, Pune-411 008, INDIA Tel : 0091 20 2590 2600 2 nd Federation of Asian Polymer Fax : 0091 20 2590 2601 Societies Polymer Congress, Beijing, Email : s.sivaram@ncl.res.in China Visit us at : http://www.ncl-india.org May 11, 2011
PLLA : MAJOR PROPERTY DEFICITS Slow rate of crystallization Very brittle material ; Elongation : 3-4 %, Poor heat stability Poor chain entanglement in melt state leading to poor melt viscosities CSIR Proprietary
PLLA PROPERTY IMPROVEMENTS : APPROACHES Poor rate of crystallization Annealing and cold crystallization Nucleation Poor Elongation Plasticization Copolymerization Increase Tm Stereocomplexation Copolymerization Nanocomposites and blends Increase melt viscosity Crosslinking Branching
SYNTHESIS OF POLY (L+) LACTIC ACID)S FROM L(+) LACTIC ACID
POLY(L+) (LACTIC ACID)S (PLLA) : PREPARATION L-Lactic acid Dehydro-polycondensation Poly(L-Lactic acid) oligomers Poly(L-Lactic acid) s Ring opening polymerization Depolymerization & cyclization L-lactide 95% yield, mp =94 o C Optical purity 100%
CRUDE L(+) LACTIDE FORMATION SUGAR CANE FERMENTATION OF SUGAR CANE JUICE TO L(+) LA ROP L(+) LACTIDE CRYSTALS L(+) LACTIDE CRYSTALLIZATION
LABORATORY POLYMERIZATION SET -UP Polycondensation set up doubled up to do distillation. SS reactor of 200mL / 800 ml. Electrical heating and overhead stirring. Ability to purge, pull vacuum, add additives. Nozzle at bottom to extrude polymer melt coupled with a pelletizer.
PREPARATION OF L(+) LA OLIGOMER VIA DEHYDRO- POLYCONDENSATION O Lactic acid : 600 g (90% aqueous solution) Conditions : 150 o C/N 2 /2h, 150 o C/100 mm, Hg/1.5h, 150 o C/30 mm, Hg/1.5h, 150 o C/0.005 mm, Hg/1h H O n OH Source Yield (%) Mn* (g/mol) Mw* (g/mol) PDI PURAC 98 3100 7100 2.29 NCL-1 98 3000 7000 2.33 * Determined by GPC in chloroform Under these conditions only linear oligomers are obtained with no cyclic oligomers ( MALDI-TOF)
PREPARATION OF DILACTIDE VIA DEPOLYMERIZATION AND CYCLIZATION) O O Lactic acid oligomer : 493 g; Catalyst : Tin powder (<150 µm) Conditions : 160 o C/N 2 /1h, 180 o C/100 mm, Hg/1h, 190 o C/10 mm, Hg/1h, 200 o C/0.01 mm, Hg/2h O O Expt. No. Tin Powder (wt%) LactideYield Optical Purity (%) (L+)(%) 1 ( >150 µm) 6 (>150 µm) 0.5 70 95 0.5 99 100 L(+) LACTIDE AS FORMED UNSUITABLE FOR POLYMERIZATION: PURIFIED BY CRYSTALLIZATION FROM MELT :
PROTON NMR OF CRUDE L(+)LACTIDE PURIFICATION 4.34 4.37 4.40 4.43 4.46 2.022 1.981 1.36 1.301 5.19 5.11 5.01 4.14 5.05 5.08 1.45 1.48 1.55 1.59 1.66 1.69 1.74 O NCL O O O 4.42 4.40 4.31 1.67 1.70 5.22 5.11 4.35 3.77 5.15 5.18 1.47 1.50 1.56 1.60 PURAC O O O O 5.5 5.0 4.5 4.0 3.5 3.0 2.5 2.0 1.5
PROTON NMR OF CRYSTALLIZED L(+) LACTIDE 5.10 5.00 5.04 5.07 1.66 1.69 NCL O O O O 5.04 4.94 4.97 5.00 1.59 1.62 PURAC O O O O 5.0 4.5 4.0 3.5 3.0 2.5 2.0 1.5
PREPARATION OF POLY(LACTIC ACID)S via RING OPENING POLYMERIZATION Catalyst concentration: 0.03% to 0.05 wt% Chain stopper : Lauryl alcohol Temperature: 180 o C Expt. No. Chain Stopper (wt%) Time Mn a Mw a (min) (g/mol) (g/mol) PDI 1 0 35 176000 412000 2.34 2 0.50 40 55100 92000 1.67 3 0.25 40 102000 156000 1.53
ISOSORBIDE AS A COMONOMER
ISOSORBIDE MONOMER Dihydrohexitols - byproducts of biomass - prepared from starch, chiral in nature - thermally stable Monomer for biodegradable polymers - improved accessibility of two -OH groups - exo substituent increases ring thermal stability Polymers presented promising properties - high glass transitions - excellent thermal stabilities - interesting physical properties Isosorbide copolyesters - relatively high Tg s - cholesteric phase formation HO O H H O OH
ISOSORBIDE: A PLATFORM CHEMICAL
L(+) LA- ISOSORBIDE COPOLYMER Incorporation of isosorbide into PLLA by melt/solution disproportionation followed by solid state polymerization
L(+) LA-ISOSORBIDE COPOLYMER VIA MELT DISPROPORTIONATION PLLA : 10 g (IV : 1.6 dl/g; Mw: 160,000 g/mol) Catalyst : Titanium isopropoxide Catalyst conc.: 0.5 wt% (based on PLA) PLLA (wt%) Isosorbide (wt%) Temp. ( o C) Time (h) IV* (dl/g) 98 2 200 1 0.38 94 6 200 1 0.25 90 10 200 1 0.16 * Determined in chloroform at 30 o C by Ubbelhode viscometer.
DISPROPORTIONATED L(+)LA-ISOSORBIDE COPOLYMER Sample ID PLA:ISB Ratio IV (dl/g) T m (ºC) T c (ºC) T g (ºC) H f (J/g) H c (J/g) PLAISB1 98:02 0.38 161 100 52 42 35 PLAISB2 94:06 0.25 168 99 59 41 28 PLAISB3 90:10 0.16 174 85 64 36 21 IV was determined in Chloroform at 30 o C by Ubbelhode viscometer Tg, Tm, Tc were determined by Q10 DSC (TA Instruments).
L(+) LA-ISOSORBIDE COPOLYMER VIA SOLUTION DISPROPORTIONATION PLLA : 10 g (IV : 1.6 dl/g; Mw: 160, 000 g/mol) Solvent : Chloroform Catalyst : Titanium isopropoxide Catalyst conc.: 0.5 wt% (based on PLA) PLLA (wt%) ISB (wt%) Temp. ( o C) Time (h) Incorp. (%) Yield (%) IV* (dl/g) 90 10 65 1 6 97 1.12 90 10 65 5 8 96 1.03 80 20 65 5 13 97 0.98 70 30 65 5 15 94 0.81 * Determined in chloroform at 30 o C by Ubbelhode viscometer.
DISPROPORTIONATED L(+)LA-ISOSORBIDE COPOLYMER Sample ID PLA:ISB Ratio IV (dl/g) T m (ºC) T c (ºC) T g (ºC) H f (J/g) PLAISB4 90:10 1.03 152 100 48 31 PLAISB6 70:30 0.81 141 101 40 17 IV was determined in Chloroform at 30 o C by Ubbelhode viscometer Tg, Tm, Tc were determined by Q10 DSC (TA Instruments).
4.62 4.59 4.57 4.244 3.94 3.76 3.79 3.47 3.52 2.91 3.84 2.88 4.34 3.89 1.0 0.9 0.8 0.7 0.6 0.5 0.4 0.3 0.2 0.1 0.0 1 H NMR SPECTRA OF ISOSORBIDE IN CDCL3 2.02 2.11 2.21 7.21 1.53 1.50 1.23 1.18 4.21 3.44 0.10 0.27 0.28 0.11 0.16 0.00 8.5 8.0 7.5 7.0 6.5 6.0 5.5 5.0 4.5 4.0 3.5 3.0 2.5 2.0 1.5 1.0 0.5 Fig. 2
1 H NMR SPECTRA OF PLA-ISOSORBIDE COPOLYMER IN CDCL 3 5.25 5.22 5.15 5.18 1.60 1.64 2 1 3.80 3.83 4.34 4.07 3.94 3.85 3.88 3.90 4.44 4.46 4.41 3.97 3.99 4.01 3.92 4.38 6,5 3,8 7,4 4.83 4.49 4.86 4.88 6,5 3,8 7,4 0.20 0.01 0.02 0.03 0.67 5.0 4.5 4.0 3.5 3.0 2.5 2.0 1.5 1.0 δ ppm
1 H NMR SPECTRA OF PLA-ISOSORBIDE COPOLYMER IN CDCL 3 7.27 5.14 5.18 1.57 1.60 0.30 0.25 0.20 0.15 0.10 3.83 3.86 3.88 3.91 3.94 3.98 4.30 4.42 4.66 4.68 4.71 0.05 3.49 3.58 3.61 2.18 1.93 1.25 5.21 5.11 1.68 0.00 0.04 0.17 0.01 0.01 0.02 0.01 0.130.54 0.01 8.0 7.5 7.0 6.5 6.0 5.5 5.0 4.5 4.0 3.5 3.0 2.5 2.0 1.5 1.0
SOLID STATE POLYMERIZATION OF DISPROPORTIONATED L(+) LA-ISOSORBIDE COPOLYMER Polymn Steps Sample ID IV (dl/g) T g ( C) T m ( C) T c ( C) H f (W/g) H c (W/g) 1 PLAISB6 0.81 40 141 101 17 22 2 3 4 5 6 BSSP 100 C/1h ASSP 120 C/2h ASSP 135 C/3h ASSP 145 C/2h ASSP 155 C/2h - - 165 - - - - 61 174 106 48 36-59 173 107 54 45-61 183 109 78 37 0.96 60 185 110 85 40 IV was determined in Chloroform at 30 o C by Ubbelhode viscometer Tg, Tm, Tc were determined by Q10 DSC (TA Instruments).
:DSC THERMOGRAMS OF PLA-ISOSORBIDE COPOLYMER DURING SSP 0.5 0.0 Step-6 /g) Heat flow (W/ -0.5-1.0-1.5 Step-5 Step-1 S tep-3 S tep-4-2.0-2.5 40 60 80 100 120 140 160 180 200 220 Tem perature ( o C ) Fig. 9
12-HYDROXY STEARIC ACID AS COMONOMER
HO CH 3 O CH C OH + HO CH (CH 2 ) 11 COOH ( CH 2 ) 5 CH 3 O H O CH C O m CH 3 Sn Catalyst CH (CH 2 ) 11 ( CH 2 ) 5 O C OH n COPOLYMERS OF L (+) - LACTIC ACID WITH 12-HYDROXY STEARIC ACID CH 3
PROPERTIES OF L(+) LA 12- HSA COPOLYMERS mol% PLA mol% 12-HSA Feed Product T g ( C) T m ( C) M n (VPO) 99 1 0.99 38 147 8,800 97 3 3.01 28 143 7,600 95 5 4.92 22 133 8,100 100 NIL 48 142 4,320
BRANCHING/CROSSLINKING USING STYRENE GMA COPOLYMER
SYNTHESIS OF STYRENE-GMA COPOLYMER Sty (%) GMA (%) IV a (dl/g) Mn b (g/mol) Mw b (g/mol) PDI Copolymer Comp c Sty (%) GMA (%) Epoxy eq d (g/mol) 30 70 0.14 6620 25820 3.90 40 60 203 40 60 0.12 5020 17550 3.50 35 65 226 20 80 0.13 5240 20290 3.80 35 65 259 50 50 0.17 4570 16900 3.69 20 80 186 a Determined by Ubbelhode viscometer in chloroform at 30 o C. b Determined by gel permeation chromatography using chloroform solvent. c Determined by 1 H NMR spectroscopy. d Determined by titrimetry.
MELT COMPOUNDING AND RHEOLOGICAL MEASUREMENTS Temp. : 180 o C, Residence Time : 3 min in nitrogen Speed : 100 rpm ARES RHEOMETER DSM MICROCOMPOUNDER
MELT COMPOUNDING OF STYRENE- GMA COPOLYMER WITH PLLA Polymer Code Sty:GMA (Comp.) PLA (%) St-GMA (%) Mn a (g/mol) Mw a (g/mol) PLLA - 100-46800 108000 2.50 PLLA1 99 1 41100 93100 2.26 50:50 PLLA2 98 2 39200 91400 2.33 PLLA3 40:60 99 1 53500 159000 2.96 PLLA4 98 2 56000 133000 2.36 PLLA5 30:70 99 1 44700 121000 2.71 PLLA6 98 2 54200 118000 2.18 PLLA7 20:80 99 1 43200 92900 2.33 PLLA8 98 2 49600 91900 1.85 a Determined by gel permeation chromatography using chloroform solvent. PDI
STORAGE MODULUS AND COMPLEX VISCOSITY OF PLLA- GMA BLENDS Addition of 2 % GMA enhances melt viscosity of PLLA
SUMMARY Tm improved using isosorbide as comonomer Tg decreased using 12- hydroxystearic acid as comonomer Branching and crosslinking with S-GMA copolymer improves melt viscosity of PLLA
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SYNTHESIS OF PLLA OLIGOMERS CONTROLLED END GROUPS Controlled ROP of purified LL-dilactide performed 120 C/ 12 h H Oct 2 Sn O R O O O ROCO(CH 3 )OCOCH(CH H 3 )O SnOct 2 O R = H, WATER used as initiator to get carboxylic acid end groups M n = ([M] / [I]) x M Lactide x conversion % and DP n = ([M] / [I]) x conversion %
MOLECULAR WEIGHT DETERMIATION OF PLLA SAMPLES Number average molecular weights of the PLA oligomers synthesized by ROP of L-lactide with water as co-initiator and Sn(Oct) 2 as initiator. PLA sample [Lactide]/ [Sn(Oct) 2 ] [Lactide]/ [H 2 O] Conv. (%) DP n, Calc DP n, NMR M n, NMR M n, VPO 3.1 200 32 86 55 60 4320 4400 3.2 400 45 87 79 77 5544 5692 Fig. 3.1: 13C-NMR spectrum (500 MHz) of PLLA oligomer3.1 synthesized by ROP : Inset showing ester carbonyl region (ester as well as carboxylic acid)
DSC OF PLA OLIGOMERS HAVING HYDROXYLA AND CARBOXY END GROUPS PLA samples T g ( C) T m ( C) H melt ing (J.g -1 ) % Crystallinity from powder XRD 3.1 48 141 53.4 85 3.2 51 162 59.7 85 Fig. 3.2: Thermal characterization(dsc) first and second heating showing Tm and Tg, respectively of PLA oligomers: (a) 3.1, first heating; (b) 3.2, first heating; (c) 3.1, second heating and (d) 3.2, second heating