Next Article in Journal
Volatile Organic Compounds from Orchis Species Found in Basilicata (Southern Italy)
Previous Article in Journal
Convenient Access to Functionalized Non-Symmetrical Atropisomeric 4,4′-Bipyridines
 
 
Font Type:
Arial Georgia Verdana
Font Size:
Aa Aa Aa
Line Spacing:
Column Width:
Background:
Communication

Application of CO2-Assisted Polymer Compression to Polylactic Acid and the Relationship between Crystallinity and Plasticization

Research Institute for Chemical Process Technology, National Institute of Advanced Industrial Science and Technology, 4-2-1 Nigatake, Miyagino-ku, Sendai 983-8551, Japan
Compounds 2021, 1(2), 75-82; https://doi.org/10.3390/compounds1020007
Submission received: 7 June 2021 / Revised: 6 July 2021 / Accepted: 21 July 2021 / Published: 4 August 2021

Abstract

:
CO2-assisted polymer compression (CAPC) is an environmentally friendly processing method that uses CO2 to plasticize and crimp polymer fibers at room temperature, enabling low-energy processing within a short time. In this study, CAPC was applied to polylactic acid (PLA), a carbon-neutral polymer. To evaluate the relationships between CO2 plasticization and the crystallinity degree and plasticization of PLA, samples with different degrees of crystallinity were layered and simultaneously compressed to observe the most collapsed layer. The sample with lower crystallinity exhibited better crushing and higher plasticization than the crystallized samples. The PLA with high crystallinity developed cracks on the fiber surfaces with consequent loss of strength. Based on the results, CAPC is a potentially effective method for PLA with low crystallinity.

Graphical Abstract

1. Introduction

Reducing the use of fossil resources is an integral part of building a sustainable society, and has become a challenge in the twenty-first century. Indeed, fossil-fuel alternatives were declared as a sustainable development goal at the UN Summit in September 2015 [1]. Plastics, an indispensable material in our daily lives, must also be converted to plant-based plastics [2]. Polylactic acid (PLA) has the largest production volume among the current bioplastics [3]. As PLA is produced on commercial scales, its handling, processing, and applications have been extensively researched [4]. As an example of PLA application, active food packaging has been proposed [5,6].
The CO2-assisted polymer compression (CAPC) method fabricates plastic parts at low cost and low energy using CO2 [7]. In the CAPC method, polymer fibers are placed in a mold and compressed while CO2 is added. The polymer fibers plasticized by CO2 are pressed and bonded into porous materials. It can be regarded as a CO2 capture and utilization (CCU) method [8] because it uses CO2 as a plasticizer. The porous materials prepared by this new method have been studied in porosity control [9], adhesion strength [10], gas permeability [11], drug release [12], mass production [13], and multilayering [14,15] studies. Past studies of plasticization by CO2 have suggested that CO2 impregnates the amorphous part of resins [16,17,18], but the relationship between the crystallinity of raw materials and their suitability for CAPC processes remains unclear. The combination of CO2 and PLA has been considered as a suitable sustainable method [19,20].
The pores in a CAPC product are the gaps between the fibers. The CAPC proceeds at room temperature under vapor pressure CO2 and does not require heaters or pumps. Therefore, CAPC is a very energy-efficient process. In addition, as CO2 is lowly toxic, it can be applied to pharmaceutical manufacturing and as a food additive in the food industries [21]. The porous material produced by the CAPC method has already demonstrated its potential as a filter and drug-releasing tablet [11,12]. CAPC is a technology for molding porous resins with continuous pores, and it is expected that PLA will be used in many applications, such as filters, catalyst-loaded reactors, and drug capsules.
In previous work, the CAPC method was applied to polyethylene terephthalate [9,10,11,12,13,14,15]. In the present study, the CAPC method is newly applied to PLA as an environmentally friendly processing method on an environmentally friendly resin. The effect of the crystallinity of raw fibers on CAPC processes was discussed to determine if there are any restrictions on using raw materials from the viewpoint of crystallinity.

2. Materials and Methods

The raw materials were PLA pellets (Luminy L105, Melt flow index 70 g/10 min (210 °C, 2.16 kg), Total Corbion PLA, Rayong, Thailand), and the nonwoven fabric (fiber diameter = 8 μm) was manufactured by Nippon Nozzle Co., Ltd. (Kobe, Japan) using the melt blowing method [22] with a 0.3-mm nozzle.
To control the crystallization degree of the nonwoven fabrics, the prepared nonwoven fabrics were heated at 62 °C for different times (1, 3, and 10 h). The heating temperature was only slightly higher than the glass transition point (60 °C in the data sheet).
To clarify the order of plasticization in the presence of CO2, an experiment was conducted in which two samples were stacked, set in a high-pressure vessel, and then pressed. In single experiment, the order of plasticization of the two samples in the same environment could be determined, and the order of plasticization of all samples could be determined by experimenting with different combinations of samples. The untreated, 1-h-treated, 3-h-treated, and 10-h-treated nonwoven fabrics were punched with a Φ-18-mm punch. The experimental setup is shown in Figure 1. CO2 lines were connected to the piston, and a pressure vessel was placed below the piston. Valves V1 to V3 are ball valves, and valve V4 is a metering valve. Stacked 32 circular sheets (18-mm diameter, 0.253 g) were prepared on the upper and lower sides of the separator and placed in a high-pressure vessel (20-mm inner diameter). After lowering the piston to the CO2 introduction position (where the total of the upper and lower layers was 3.6 mm), the entry–exhaust cycle of CO2 was performed three times through valves V1 and V2 to drive out the air in the vessel. After replacing air with CO2, valve V1 was opened to introduce gaseous CO2 at vapor pressure (~6 MPa), and the piston was lowered to the press position (where the total of the upper and lower layers was 2.4 mm), where it was held for 10 s. Next, exhaust valve V3 was opened and exhausted for 30 s through the flow-limiting valve V4. Finally, V2 valve was opened to release CO2 to the atmosphere, and the piston was raised to remove the samples. The experiment was conducted at room temperature (~22 °C) and no heating manipulation was used. The thickness of the center of each sample was measured with a micrometer caliper.
To determine the crystallinity degree of each sample, the heat of crystallization was evaluated from differential scanning calorimetry (DSC) measurements conducted on a Thermo Plus Evo DSC 8230 (Rigaku Corporation, Akishima, Japan). The thermograms were recorded under the atmosphere. The heating rate was 5 °C/min. The sample mass was in the range of 7.5–9.1 mg. Melting and crystallization characteristics were evaluated from the first heating run. X-ray diffraction (XRD) patterns were obtained using a SmartLab diffractometer (Rigaku Corporation, Akishima, Japan). The degree of crystallinity was calculated from the cold crystallization and melting enthalpy.
The surface of the CAPC products was observed in a TM-1000 scanning electron microscope (SEM) system (Hitachi High-Technologies Co., Minato-ku, Japan).

3. Results and Discussion

First, I checked whether PLA fibers could adhere using CAPC. The experiments were conducted on untreated sheets. Sixteen sheets with punch diameters of 30 mm were CAPC-treated to form 0.6-mm-thick sheet-like samples. Figure 2 displays photographs of raw nonwoven fabric sheets, the sample after cutting with scissors, and the sample after cutting and bending. The samples were firmly bonded without peeling, indicating the effectiveness of PLA processing by CAPC. In an attempted T-type tensile test, configured by inserting a central sheet to create a non-adhesive area, the sheet sample exhibited higher adhesive strength than the raw fiber; accordingly, the sheet was torn and could not be tested (Figure 3). Therefore, the adhesive strength of the fiber sheets was very high.
Next, the degree of plasticization was evaluated in the presence of CO2 and was related to the degree of crystallinity. Figure 4 shows the DSC data for each sample; the DSC chart shows the peaks of cold crystallization 1, cold crystallization 2, and fusion at ~93 °C, ~157 °C, and ~174 °C, respectively, similar to an existing study [23]. The enthalpies of cold crystallization 1, cold crystallization 2, and fusion are ΔHc1, ΔHc2, and ΔHm, respectively, and considering their signs, the degree of crystallinity is given by the following equation [24]:
Degree   of   Crystallinity = Δ H c 1 + Δ H c 2 + Δ H m Δ H 0
where ΔH0 is the heat of fusion when the crystallinity degree of PLA is 100%, which is −93.1 J/g [25]. Because an overlap exists between the cold crystallization 2 and melting peaks, the integrated values of both were evaluated and analyzed by transforming Equation (1) into the following equation:
Degree   of   Crystallinity = Δ H c 1 + Δ H c + m 2 Δ H 0
Derived crystallinities were 0.02 (unheated), 0.07 (1-h heating), 0.15 (3-h heating), and 0.17 (10-h heating).
XRD data of unheated nonwoven fabric is shown in Figure 5. The degree of crystallinity is calculated as the area ratio of the broad halo due to the amorphous part and the sharp peak due to the crystalline part in the XRD data [26]. The XRD chart in Figure 5 shows no sharp peaks, and the degree of crystallinity was almost zero, which agreed with the value calculated from DSC data (0.02).
To analyze the hardness of the samples impregnated with CO2, a separator was placed between the two samples, and the entire sample was compressed to a certain thickness. The raw material comprises stacked nonwoven fabrics, and the product is a uniform porous material with a certain thickness. The thicknesses of the CAPC products above and below the separator were measured to determine their relative hardness.
First, untreated samples were set at both the top and bottom, and they were then compressed to a total of 2.4 mm. The experiments were performed four times. CAPC products were formed at the top and bottom through the separator. The top and bottom CAPC products were of the same thickness (1.200 ± 0.002 mm), confirming that the samples were compressed in the same manner regardless of their position. Next, experiments with six different sample combinations were performed; the experiments were performed four times in each combination. Two experiments were conducted with sample A on the top and sample B on the bottom, and the other two were conducted with sample A on the bottom and sample B on the top. Then, the results of these experiments were averaged and demonstrated, as shown in Table 1. The sample name indicates the experiment number (samples A and B in each experiment). For example, experiment number 1 is a combination of an untreated sample and a 1-h-heated sample, where the untreated sample is 1A and the 1-h-heated one is 1B. Comparing the untreated and 1-h-heated samples, the untreated sample was more crushed, indicating that the sample without heat treatment was more plasticized by CO2. The untreated sample crumbled more as its counterpart was heated for longer times, indicating that it hardened after heating for 3 h and further hardened after 10 h. This result indicates that the degree of crystallization increased with heating time, inhibiting the plasticization effect of CO2. In fact, the 1-h-heated sample was more compressed than the 3-h-heated sample, and the 3-h-heated sample was more compressed than the 10-h-heated sample. In summary, the hardening increased in the following order: untreated <1-h heating <3-h heating <10-h heating. CO2 plasticizes polymers by dissolving in the amorphous part of the polymers [27,28]. The results in this study show that the hardness of the polymer in CO2 increases as the amorphous part decreases, which is consistent with previous studies.
The untreated samples bonded very well, but the 10-h-heated sample appeared brittle. Therefore, the microscopic surface morphologies of the samples were compared. Figure 6 compares the SEM images of the sample surfaces after the CAPC process. In the untreated CAPC product, the fibers were crushed and spread horizontally by the plasticization and pressing processes, but this crushing was increasingly reduced as the heat treatment progressed. In addition, the fibers in the 10-h-heated product were cracked and fiber damage was confirmed. The flexural strength and maximum strain of PLA, whose crystallinity is increased through annealing, decreases owing to the rigidity effects of the crystalline domains [4,23]. These effects must have appeared in the cracks in the 10-h-heated product. Therefore, the CAPC method should be limited to PLA fibers with low crystallinity.

4. Conclusions

The CAPC method is an energy-saving resin bonding technology that belongs to the CCU category of production methods. CAPC method effectively processing fibers of a bioplastic material (PLA) was demonstrated. Fibers with different degrees of crystallinity were prepared by heat treatment at the same temperature for different times, and their compression ratios after CO2 exposure were compared. The fibers with a shorter heat-treatment time were more compressed than those with a long heat-treatment time and were more plasticized by CO2. After 10 h of treatment at 62 °C, the fibers had a crystallinity of 0.17 and were cracked by the CAPC treatment; therefore, they were not suitable for this method. In contrast, the PLA fibers with low crystallinity were successfully processed using the CAPC method. Thus, it was strongly suggested that the CAPC process should be applied to fibers with low crystallinity. In some cases, PLA products are shipped after annealing to improve their thermal stability. However, unannealed PLA nonwoven fabrics with low crystallinity should be used as raw materials for CAPC.

Funding

This research received no external funding.

Data Availability Statement

All data generated or analyzed during this study are included in this published article.

Conflicts of Interest

The author declares no conflict of interest.

References

  1. UN OWG. Introduction to the Proposal of the Open Working Group for the Sustainable Development Goals. Outcome Document as of 19.6.2014 (Online). 2014. Available online: https://sdgs.un.org/ (accessed on 13 April 2021).
  2. Shogren, R.; Wood, D.; Orts, W.; Glenn, G. Plant-based materials and transitioning to a circular economy. Sustain. Prod. Consum. 2019, 19, 194–215. [Google Scholar] [CrossRef]
  3. Inamuddin. Green Polymer Composites Technology: Properties and Applications; CRC Press: Boca Raton, FL, USA, 2019; ISBN 978-0367872557. [Google Scholar]
  4. Sin, L.T.; Tueen, B.S. Polylactic Acid: A Practical Guide for the Processing, Manufacturing, and Applications of PLA, 2nd ed.; William Andrew: Oxford, UK, 2019; ISBN 978-0128144725. [Google Scholar]
  5. Rojas, A.; Velásquez, E.; Garrido, L.; Galotto, M.J.; de Dicastillo, C.L. Design of active electrospun mats with single and core-shell structures to achieve different curcumin release kinetics. J. Food Eng. 2020, 273, 109900. [Google Scholar] [CrossRef]
  6. Velásquez, E.; Vidal, C.P.; Rojas, A.; Guarda, A.; Galotto, M.J.; de Dicastillo, C.L. Natural antimicrobials and antioxidants added to polylactic acid packaging films. Part I: Polymer processing techniques. Compr. Rev. Food Sci. Food Saf. 16. [CrossRef]
  7. Aizawa, T. A new method for producing porous polymer materials using carbon dioxide and a piston. J. Supercrit. Fluids 2018, 133, 38–41. [Google Scholar] [CrossRef]
  8. Koytsoumpa, E.K.; Bergins, C.; Kakaras, E. The CO2 economy: Review of CO2 capture and reuse technologies. J. Supercrit. Fluids 2018, 132, 3–16. [Google Scholar] [CrossRef]
  9. Aizawa, T. Fabrication of porosity-controlled polyethylene terephthalate porous materials using a CO2-assisted polymer compression method. RSC Adv. 2018, 8, 3061–3068. [Google Scholar] [CrossRef] [Green Version]
  10. Aizawa, T. Peel and penetration resistance of porous polyethylene terephthalate material produced by CO2-assisted polymer compression. Molecules 2019, 24, 1384. [Google Scholar] [CrossRef] [Green Version]
  11. Aizawa, T.; Wakui, Y. Correlation between the porosity and permeability of a polymer filter fabricated via CO2-assisted polymer compression. Membranes 2020, 10, 391. [Google Scholar] [CrossRef]
  12. Wakui, Y.; Aizawa, T. Analysis of sustained release behavior of drug-containing tablet prepared by CO2-assisted polymer compression. Polymers 2018, 10, 1405. [Google Scholar] [CrossRef] [Green Version]
  13. Aizawa, T. Process development of CO2-assisted polymer compression for high productivity: Improving equipment and the challenge of numbering-up. Technologies 2019, 7, 39. [Google Scholar] [CrossRef] [Green Version]
  14. Aizawa, T. Novel strategy for fabricating multi-layer porous membranes with varying porosity. ACS Omega 2020, 5, 24461–24466. [Google Scholar] [CrossRef] [PubMed]
  15. Aizawa, T. New design method for fabricating multilayer membranes using CO2-assisted polymer compression process. Molecules 2020, 25, 5786. [Google Scholar] [CrossRef]
  16. Kemmere, M.F.; Meyer, T. Supercritical Carbon Dioxide in Polymer Reaction Engineering; Wiley-VCH: Weinheim, Germany, 2005; ISBN 978-3527607051. [Google Scholar]
  17. Li, M.; Zhang, J.; Zou, Y.; Wang, F.; Chen, B.; Guan, L.; Wu, Y. Models for the solubility calculation of a CO2/polymer system: A review. Mater. Today Commun. 2020, 25, 1012772. [Google Scholar] [CrossRef]
  18. Lee, J.K.; Yao, S.X.; Li, G.M.; Jun, M.B.G.; Lee, P.C. Measurement methods for solubility and diffusivity of gases and supercritical fluids in polymers and its applications. Polym. Rev. 2017, 57, 695–747. [Google Scholar] [CrossRef]
  19. Gangapurwala, G.; Vollrath, A.; De San Luis, A.; Schubert, U.S. PLA/PLGA-based drug delivery systems produced with supercritical CO2-A green future for particle formulation? Pharmaceutics 2020, 12, 1118. [Google Scholar] [CrossRef] [PubMed]
  20. Villamil Jiménez, J.A.; Le Moigne, N.; Bénézet, J.-C.; Sauceau, M.; Sescousse, R.; Fages, J. Foaming of PLA composites by supercritical fluid-assisted processes: A review. Molecules 2020, 25, 3408. [Google Scholar] [CrossRef] [PubMed]
  21. Balaban, M.O.; Ferrentino, G. Dense Phase Carbon Dioxide: Food and Pharmaceutical Applications; Wiley-Blackwell: Ames, IA, USA, 2012; ISBN 978-0813806495. [Google Scholar]
  22. Drabek, J.; Zatloukal, M. Meltblown technology for production of polymeric microfibers/nanofibers: A review. Phys. Fluids 2019, 31, 091301. [Google Scholar] [CrossRef]
  23. Bruckmoser, K.; Resch, K. Effect of processing conditions on crystallization behavior and mechanical properties of poly(lactic acid) staple fibers. J. Appl. Polym. Sci. 2015, 132, 42432. [Google Scholar] [CrossRef]
  24. Fried, J.R. Polymer Science and Technology, 3rd ed.; Prentice Hall: Upper Saddle River, NJ, USA, 2014; ISBN 978-0137039555. [Google Scholar]
  25. Lim, L.-T.; Auras, R.; Rubino, M. Processing technologies for poly(lactic acid). Prog. Polym. Sci. 2008, 33, 820–852. [Google Scholar] [CrossRef]
  26. Young, R.J.; Lovell, P.A. Introduction to Polymers, 3rd ed.; CRC Press: Boca Raton, FL, USA, 2011; ISBN 978-0849339295. [Google Scholar]
  27. Tomasko, D.L.; Li, H.; Liu, D.; Han, X.; Wingert, M.J.; Lee, L.J.; Koelling, K.W. A review of CO2 applications in the processing of polymers. Ind. Eng. Chem. Res. 2003, 42, 6431–6456. [Google Scholar] [CrossRef]
  28. Lian, Z.; Epstein, S.A.; Blenk, C.W.; Shine, A.D. Carbon dioxide-induced melting point depression of biodegradable semicrystalline polymers. J. Supercrit. Fluids 2006, 39, 107–117. [Google Scholar] [CrossRef]
Figure 1. Setup of the experiment for comparing the hardness values of the two layers (V1: CO2 introduction valve, V2: fast exhaust valve, V3: slow exhaust valve, V4: metering valve).
Figure 1. Setup of the experiment for comparing the hardness values of the two layers (V1: CO2 introduction valve, V2: fast exhaust valve, V3: slow exhaust valve, V4: metering valve).
Compounds 01 00007 g001
Figure 2. Raw nonwoven fabric sheets (left), a cut and bent CAPC product (middle), and a cut CAPC product (right).
Figure 2. Raw nonwoven fabric sheets (left), a cut and bent CAPC product (middle), and a cut CAPC product (right).
Compounds 01 00007 g002
Figure 3. Sample after the T-type tensile test.
Figure 3. Sample after the T-type tensile test.
Compounds 01 00007 g003
Figure 4. Differential scanning calorimetry data of (a) a raw fabric sheet and the sheet after heating at 62 °C for different times: (b) 1 h, (c) 3 h, and (d) 10 h. Indicated values are enthalpies of Δ H c 1 and Δ H c + m 2 in Equation (2).
Figure 4. Differential scanning calorimetry data of (a) a raw fabric sheet and the sheet after heating at 62 °C for different times: (b) 1 h, (c) 3 h, and (d) 10 h. Indicated values are enthalpies of Δ H c 1 and Δ H c + m 2 in Equation (2).
Compounds 01 00007 g004
Figure 5. XRD data of a raw fabric sheet.
Figure 5. XRD data of a raw fabric sheet.
Compounds 01 00007 g005
Figure 6. Scanning electron microscope images of the surfaces of CAPC products formed from (a) raw fabric, and fabric treated at 62 °C for different times: (b) 1 h, (c) 3 h, and (d) 10 h.
Figure 6. Scanning electron microscope images of the surfaces of CAPC products formed from (a) raw fabric, and fabric treated at 62 °C for different times: (b) 1 h, (c) 3 h, and (d) 10 h.
Compounds 01 00007 g006
Table 1. Compression results for the hardness comparison.
Table 1. Compression results for the hardness comparison.
SampleHeat-Treatment Time [h]Thickness [mm]Standard Deviation [mm]
1A01.1970.003
1B11.2060.003
2A01.1520.018
2B31.2490.019
3A01.1140.006
3B101.2850.005
4A11.1570.004
4B31.2460.009
5A11.1400.009
5B101.2610.009
6A31.1730.010
6B101.2290.006
Publisher’s Note: MDPI stays neutral with regard to jurisdictional claims in published maps and institutional affiliations.

Share and Cite

MDPI and ACS Style

Aizawa, T. Application of CO2-Assisted Polymer Compression to Polylactic Acid and the Relationship between Crystallinity and Plasticization. Compounds 2021, 1, 75-82. https://doi.org/10.3390/compounds1020007

AMA Style

Aizawa T. Application of CO2-Assisted Polymer Compression to Polylactic Acid and the Relationship between Crystallinity and Plasticization. Compounds. 2021; 1(2):75-82. https://doi.org/10.3390/compounds1020007

Chicago/Turabian Style

Aizawa, Takafumi. 2021. "Application of CO2-Assisted Polymer Compression to Polylactic Acid and the Relationship between Crystallinity and Plasticization" Compounds 1, no. 2: 75-82. https://doi.org/10.3390/compounds1020007

APA Style

Aizawa, T. (2021). Application of CO2-Assisted Polymer Compression to Polylactic Acid and the Relationship between Crystallinity and Plasticization. Compounds, 1(2), 75-82. https://doi.org/10.3390/compounds1020007

Article Metrics

Back to TopTop