Abstract
Poly(lactic acid) (PLA) fiber was developed more than a decade ago. It has been regarded as the most promising sustainable and biodegradable fiber to replace conventional polyethylene terephthalate (PET) polyester fiber in textile products. This paper reviews recent developments in PLA polymerization, PLA filament and fiber spinning, staple yarn spinning, fabric production, dyeing and finishing and aftercare procedures. The properties of PLA fiber are broadly similar to those of PET fiber; however, the properties of PLA fiber that differ, including thermal degradation and low hydrolytic resistance to strong alkaline, significantly affect the method selection and parameter setting of production and processing of PLA fibers and fabrics. PLA filaments are mainly produced by two-step melt spinning to get fibers with stable quality, but degradation at high temperature is still a problem. PLA staple yarns are normally spun using ring spinning. Currently existing knitting or weaving techniques can be used to produce PLA fabrics. PLA fabrics can be dyed with disperse dyes at 110°C, but their color fastness and shades are different from PET fabrics when using the same dyes. The scouring and dyeing of PLA/cotton blended fabrics and the reductive clearing after dyeing remain to be improved. As a new fiber, the entry of PLA fiber into the textile market faces difficult challenges as well as great opportunities in the future.
Keywords
Traditional synthetic fibers such as polyester, nylon and polypropylene have caused increasing environmental concerns due to the use of non-renewable petroleum-based raw materials and the production of scarcely recycled non-biodegradable wastes, 1 especially nowadays as fast fashion has sharply increased textile wastes. Poly(lactic acid) (PLA) has been considered as one of the solutions to alleviate the problems of plastics disposal. 2 It is produced from renewable resources and is fully biodegradable at the end of its useful life. Lactic acid is easily prepared in high yield by fermentation of molasses or potato starch or of dextrose from corn, 3 and PLA can then be polymerized from lactic acid by direct condensation, or by formation of the cyclic dimer intermediate (lactide). 4 According to NatureWorks, substitution of polyester used for 10,000 sports shirts by PLA fiber can help to save fossil fuels equating to 540 gallons of greenhouse gas emissions or 11,500 miles of driving a car. 5
PLA is the only biobased and biodegradable polymer which can be large-scale melt-spun to textile fibers with sufficient strength. Several aliphatic polyester fibers, including polycaprolactone (PCL), polyhydroxyalkanoates (PHAs) and poly(butylene succinate) (PBS) fibers, are also biodegradable, but they are made from unsustainable petrochemical sources. 5 Chitosan fiber is a kind of biodegradable fiber which is made from sustainable natural sources; however, its low degree of polymerization and poor strength limit its application in textile products.
PLA fiber has obvious advantages in textile application when compared with other fibers. Table 1 shows a property comparison between PLA fiber and other fibers. PLA fiber has much lower glass transition temperature and melting temperature than polyethylene terephthalate (PET) and nylon. 6 When compared with regenerated cellulose fibers (rayon, lyocell and modal), PLA fiber has lower moisture regain and faster moisture transportation, which are similar to those of polyester fibers. The manufacturing process of rayon fiber generates toxic wastes that can cause severe environmental pollution, whereas the manufacturing process of PLA fiber is nontoxic. In addition, PLA fibers still have inherent biological resistance, good anti-flame property and good UV resistance.
A comparison of PLA fiber and other fibers
With the development in the manufacturing technologies of the PLA polymer, the price of PLA has reduced over the last two decades. Jacobsen et al. 6 reported that the high price of PLA would be significantly reduced. The price of PLA was much higher than $4 USD/kg in 1999, but 10 years later, the price of PLA decreased to 1.8–4 Euro/kg in 2008. 7 Currently, the costs of PLA pellets are estimated to be around 250 USD/ton, but the market price of PLA pellets is much higher, at least 500 USD/ton or above. 8 A further decrease is expected with increasing demand and production scales. According to information from the e-commerce website Alibaba.com in October 2020, the current prices for most PLA staple fibers range from 2 to 5 USD/kg, whereas the prices for PET staple fibers are between 0.8 and 1.5 USD/kg. As the substitution of polyester used for 10,000 sports shirts (each shirt is estimated as 300 g) by PLA fiber can help to save fossil fuels equating to 540 gallons of greenhouse gas emissions, 5 it is speculated that the price for saving 1 gallon of greenhouse gas emissions by substituting PET fiber with PLA fiber is 13.06 USD.
Several reviews related to PLA fiber and fabric have been done by various researchers. Hussain et al. 9 reviewed the dyeing of PLA fabric in 2015. Avinc and Khoddami reviewed the synthesis, properties and applications of PLA10 and wet processing of PLA fabric in 2009. 11 Perepelkin’s 2002 review 12 mainly focused on polymerization and properties of PLA, while fiber and filament spinning was mentioned but with limited information. Dugan 13 summarized the properties of PLA fiber in 2001. Although the production of PLA fibers and fabrics has been further developed in recent years, a review on the recent development in PLA textile production and applications is still lacking. Figure 1 schematically shows the production and processing stages of PLA textiles. This paper will give a comprehensive review based on these production and processing stages. PLA filament spinning and yarn spinning, and the production of PLA fabrics are reviewed for the first time. Besides, wet processing of PLA fabrics, including pretreatment (pre-heat-setting, desizing, scouring and bleaching), dyeing, printing, finishing and laundry, is also reviewed in detail. In each section, the effects of different parameters and the pros and cons of different processing methods are discussed. It is expected that this review can provide useful information for the further development of PLA fibers and their textile products as well as manufacturing processes based on their unique features.

The production and processing stages of PLA textiles.
Manufacture of PLA polymer resin
PLA polymer manufacturing technologies have been well developed over the last two decades. Production of the PLA polymer resin starts from the extraction of starch or sugar from various annual renewable crops. 2 Different plants including corn, rice, wheat, rye, sweet potato, sugar beet and whey, etc., can be used as the source for making PLA. 5 , 14 , 15 To date, among all these sources, starch from corn is most widely commercially used for making PLA, as corn is one of the cheapest and most abundant sources of starch. 5 , 10 When synthesizing PLA from starch, the starches are first converted to fermentable sugars such as glucose and dextrose by enzymatic hydrolysis. Then these sugars are fermented with the help of microorganisms to generate lactic acid. 5 , 16 The conversion of starch to lactic acid is presented in Figure 2.

The conversion of starch to lactic acid.
There are two stereoisomers of lactic acid—dextro- (D-) lactic acid and levo- (L-) lactic acid (Figure 3 (a) and (b))—due to the chiral molecule structure of lactic acid. Generally, 50% of chemically synthesized lactic acid is D-lactic acid and the other 50% is L-lactic acid. Naturally fermented lactic acid consists of approximately 99.5% L-lactic acid and only 0.5% D-lactic acid. These two types of lactic acid differ in the spatial arrangement of the hydrogen atom and methyl group, and the physical properties of such isomers are almost the same.

Two stereoisomers of lactic acid.
Polycondensation of PLA
Lactic acid can be polymerized to form PLA using either direct polycondensation or ring-opening polymerization (ROP). These two methods have been studied for a long time, and various subdivided methods, catalysts and solutions, etc., have been developed to synthesize PLA. 5 , 10 , 15 , 17 , 18 The direct polycondensation of lactic acid was first developed by Carothers et al., who discovered PLA in 1932, and was conducted under high temperature and high vacuum. 18 The polycondensation reaction of lactic acid is shown in Figure 4. It can be seen that the condensation reaction process is reversible, and it will generate water which will severely affect the quality of the synthesized PLA. In this condensation process, it is essential to drive the dehydration equilibrium in the direction of esterification to obtain high-quality PLA with high weight-average molecular weight (Mw). To remove water from the reaction and drive the equilibrium toward esterification, some solvents, catalysts and branching agents have been used in the condensation reaction. In 1995, Ajioka et al. 19 developed azeotropic boiling using high-boiling solvent and catalyst to directly obtain PLA with Mw of 300,000. Takasu et al. 20 synthesized PLA using scandium trifluoromethanesulfonate and scandium trifluoromethanesulfonimide, and they found that these solvents were effective for the dehydration of the polycondensation process of lactic acid. In 2002 Kim and Woo 21 optimized solution polymerization conditions and designed experimental apparatus for removing water efficiently. Other solvents and branching agents, such as xylene, diphenyl ether and dipentaerythritol etc., also have been used for facilitating the polycondensation of lactic acid. 22 However, when these solvents are used, complicated control of the synthesis process is usually required, which increases the cost of PLA manufacturing. In addition, the solvents used during the reaction are difficult to fully remove from the end product, which limits the production of high Mw PLA.

Polycondensation of lactic acid to PLA.
To address the problems of using solvents, another polycondensation process, namely melt polycondensation, has been developed to obtain high Mw PLA with low cost. 22 The melt polycondensation process consists of oligomerization and polymerization. During the oligomerization, the lactic acid solution needs to be heated to remove water and kept under low pressure for reaction to obtain a transparent viscous oligomer gel. Catalysts are then added into the oligomer gel for polymerization. The oligomer and catalysts mixture is well stirred and kept under low pressure and high temperature for reaction for around 12 h. Following polymerization, the product is dissolved in chloroform and precipitated in diethyl ether for purification. After that, the purified PLA can be filtered out from the diethyl ether. Thus far, a number of studies have reported the use of the binary catalysts system consisting of stannous (Sn) (II)-based dihydrate and other co-catalysts for the polymerization process of making PLA. 22 Lee et al. 23 performed a similar series of experiments in 2005 to compare the catalytic effects between the SnCl2·2H2O and TSA catalysts system and Sn (II) octoate catalysts system. They found that the PLA produced using the SnCl2·2H2O and TSA catalysts system could reach higher molecular weight when the reaction time was the same. Moon et al. 24 used different proton acids to activate Sn(II) catalysts and found that the PLA synthesized with proton acid-activated Sn(II) catalysts reached a higher Mw with a shorter reaction time compared with those PLA synthesized with the simple Sn(II) catalysts system. In later work, to further enhance the polymerization of PLA, Moon and colleagues 25 , 26 mixed SnCl2·2H2O with several types of metal alkoxides including Al(OiPr)3, Ti(OiPr)4, Y(OiPr)3, Si(OEt)4 and Ge(OEt)4. They found that, among all types of metal alkoxides, Ge(OEt)4 was the most effective cocatalyst, and boosted PLA polymerization to reach high Mw within 15 h. In addition to these chemical methods for accelerating the polymerization reaction, microwave irradiation can also be used. A number of studies have assessed the impact of microwave irradiation on the polymerization of lactic acid.27–29 It was believed that the reaction speed is increased and the required pressure for reaction can be reduced with the help of microwave irradiation.
The direct polycondensation of lactic acid can also be performed in bulk state. The reaction in bulk state has a relatively shorter process compared with solution and melt polycondensation. In this process, the lactic acid is directly mixed with some catalysts in a sealed reactor under a vacuum environment. Kim et al. 30 used titanium butoxide as catalyst to make PLA with high Mw. The Mw of PLA synthesized in the bulk state can reach as high as 130,000.
Although PLA can be directly obtained from all three direct polycondensation methods, the Mw of such PLA is still low. These low Mw PLA can be further processed by various post-polycondensation methods including melt modification, radiation-induced cross-linking and solid-state polycondensation (SSP). 22 Among these post-polycondensation processing methods, melt modification and radiation including cross-linking are normally applied for adding polyfunctional monomers or branching to the PLA molecule to modify the mechanical, physical and chemical properties of the PLA, whereas the SSP is widely used for increasing the Mw of the PLA. 22 In the SSP of PLA, the PLA with relatively low molecular weight is heated up to a temperature between the glass transition temperature (Tg) and the melting temperature (Tm) for further polycondensation with the presence of proper catalysts.31–34 During the polycondensation, the byproduct of the reaction is continuously removed from the surface of the material either by evaporation under reduced pressure or by driving it away by a carrier gas. As the reaction temperature of the SSP is relatively lower compared with melt polycondensation and solution polycondensation, the mobility of the end groups is slow and restricted. Thus, SSP requires a much longer reaction period compared with other two polycondensation methods. 22
Ring-opening process of PLA
Because of the difficulties of removing water and impurities from the condensation reaction, the polycondensation method can only produce PLA resin with low to moderate Mw. Therefore, most studies in the industry have been focused on ROP.
ROP produces PLA from a cyclic intermediate dimer of lactic acid, namely lactide. This method is a better way to produce high Mw PLA under relatively milder reaction conditions. 5 , 10 , 22 The ROP of lactide is normally carried out under heat without solvent, and may produce different stereopolymers resulting from different starting lactides. As there are two types of lactic acid, the production of lactide from lactic acid can create three different stereoisomers, L-lactide, D-lactide and meso-lactide, as shown in Figure 5. 35 L-lactide and D-lactide are dimerized from pure L-lactic acid and D-lactic acid, respectively, and they are optically active. The meso-lactide is dimerized from both L-lactic acid and D-lactic acid, and it is optically inactive and has lower melting point compared with other lactides. Through controlling the production of the optical isomers of the lactic acid, the PLA can be polymerized with different and required characteristics. For example, PLA with different molecular weights can be obtained from controlling the purity of the lactide; by changing the ratio and the distribution of D-isomer and L-isomer along the PLA backbone, the Mw, crystallinity and properties including melt behavior, thermal properties, barrier properties and ductility of the PLA can be changed and designed. With a higher ratio of L-isomer in the polymer backbone, PLA can be produced with more crystalline regions and crystalline polymer can be produced. When the D-lactide content constitutes less than 2% of the material, highly crystalline polymer can be produced. When the D-lactide is more than 15% of the material, an amorphous polymer is achieved because the crystallinity of the PLA decreases with the increase of D-isomer content. The melting points of different PLA polymers vary from 130°C to 220°C. The melting points of pure poly(L-lactic acid) (PLLA), pure poly(D-lactic acid) (PDLA) and poly(D,L-lactic acid) (combination with highest melting point) are 180°C, 180°C and 220°C, respectively. 22

Lactide isomers.
Based on the ROP process, NatureWorks LLC developed and patented a low-cost continuous process for the production of lactic acid-based polymers. 2 The manufacturing process is shown in Figure 6. It can be seen that, in the first step of the manufacturing process, the low molecular weight PLA prepolymer is continuously produced from the condensation reaction of aqueous lactic acid. Then the PLA prepolymer is depolymerized to form the mixture of lactide stereoisomers with the help of stannous catalysis, which can facilitate the rate and selectivity of the intramolecular cyclization reaction. Next, the lactide mixture is purified through vacuum distillation. Finally, high molecular weight PLA is manufactured through the ROP of lactide in the melt state. Stannous catalysis is used in the ROP process as well. After the ROP, remaining monomers are removed from the end product and reused in the beginning of the process. This manufacturing process is cost effective and environmentally friendly, as the synthesis of PLA is carried out in melt state rather than in solution with the existence of toxic solvent. 2

Manufacturing process of the high molecular weight PLA.
Manufacturing of PLA fibers
Spinning of PLA filaments
The production of PLA filament from PLA polymer resin is now a well-established industry. Normally, PLLA polymer resin is used to produce PLA fiber. The PLA filament can be manufactured using melt-spinning technology similar to the production of other melt-spun fibers such as polypropylene fiber, or using solution spinning (both dry spinning and wet spinning). 4 , 10 , 36 , 37 Currently, almost all commercially available PLA fibers are manufactured through the melt-spinning process, as this process is possible in high-speed production. In addition, melt spinning is a solvent-free process, which is more economical and more eco-friendly. However, the PLA polymer easily degrades under the melt state. For some situations which require low degradation during the manufacturing process, solution spinning can be used. Both dry spinning and wet spinning require the use of certain solvents which are toxic and difficult to recycle. The solution-spun PLA fiber cannot be directly used for healthcare textiles and medical products, which are two important applications of PLA.
Wet spinning
In wet spinning, PLA is first dissolved in a suitable solvent (e.g. chloroform) to prepare the spinning solution. The concentration of the PLA ranges from 6 wt% to 12 wt%, and is decided by the solubility and molecular weight of PLA polymer used and solution spinning pressure limitations. The prepared solution is then extruded into a coagulation bath from a spinneret which is submerged in the coagulation bath. The coagulation bath contains a non-solvent solution such as toluene. There may be one or more coagulation baths used for the PLA spinning. When the filaments are in the coagulation bath, the appearance and structure of the PLA fibers are formed. After spinning, the filaments are dried and removed. The production speed of wet spinning can be around 25–35 cm/min at laboratory scale.
Tsuji et al. 38 reported the wet spinning of both PDLA and PLLA fiber and discussed the mechanical properties, appearance and cross-sectional structure of the PLA fibers. The PDLA and PLLA were dissolved in chloroform to make the spinning solution, respectively, with a concentration of 5–10 g/dL. Two coagulation baths were used. The first coagulation bath was carried out under 40°C, and the bath contained a mixture of ethanol and chloroform with a volume ratio of 10:3. Then the filaments were further coagulated in the second coagulation bath containing an ethanol/chloroform mixture with a volume ratio of 10:1 at 20°C. Finally, the filaments were wound up by a winder. Figure 7 presents the wet-spinning procedure and equipment used. The tensile property and appearance of the wet-spun PLA filaments were examined. It was found that the average diameter of the wet-spun PLA fibers was around 50 µm and the tensile strength was very low. It was also observed that the fiber surfaces were extremely irregular, and there were many pores of different diameters. The authors believed that the defective structure of the wet-spun PLA fiber was caused by the rapid desolvation of the PLA filament during coagulation.

Wet-spinning process and equipment. 38
Dry spinning
For the dry-spinning process, the PLA solution is extruded into a thermally insulated chamber with hot air, where the solvent is removed by evaporation to produce PLA fiber. Several studies have shown that, for dry spinning of PLA, both good solvents such as chloroform, and poor solvents (e.g. toluene) are available.39–42 The mixture of the good solvents and poor solvents can also be used for the production of PLA fiber, and the mixture even provides the PLA fiber with better tensile properties. In addition to the solvent used for dissolving PLA, the appearance, structure, properties of the dry-spun PLA fiber can be affected by many factors including extruding speed, winding speed, spinning temperature, hot-drawing and additives used, etc. Figure 8 shows the general manufacturing process of dry spinning and the equipment used.

Dry-spinning process and equipment. 43
Leenslag and Pennings 39 studied the manufacture of dry-spun PLA fiber using chloroform/toluene (40/60) solvent. The PLA was dissolved at 70°C, and then the solution was conditioned at the same temperature for 3 h before extrusion. The fibers were extruded through a stainless steel conical die and wound up to a bobbin with the extrusion speed of 3 m/min at 60°C. After the fiber collection, the whole bobbin was kept at 60°C for 10 min to completely solidify the fiber. Following this, the bobbin was dried at room temperature for 40 h until a constant weight of bobbin was reached. Then, the fibers were fully hot-drawn to the maximum draw ratio at 190°C.
Horáček and Kalíšek 40 manufactured PLA fibers through a continuous dry-spinning/hot-drawing process. A mixture of chloroform and cyclohexane was used as solvent. The PLA polymer was dissolved by continuous stirring for 16 h at 50°C. Then the solution was cooled for 2 h to 33°C, and it was spun at ambient temperature with an extrusion speed of 6.5 cm/min. The filament was then continuously led on to a steel drum in drawing tube with a drawing temperature between 110 and 190°C. After the drawing process, the fibers were collected on another drum. In another work by Horáček and Kalíšek, 41 the PLA solutions were prepared using non-solvent or chloroform for producing PLA fibers. It was found that the PLA fibers manufactured with non-solvent exhibited better tensile strength. In addition, these authors 42 manufactured PLA fibers using various non-solvents including methanol, ethanol or petroleum ether as vapor in the extrusion chamber rather than in the solution. Their work indicated that the tensile strength, structure and degradability of manufactured fibers were highly affected by the concentration of the non-solvent vapor.
The influence of spinning temperature on dry-spun fiber was studied by Postema et al. 44 They found that the tensile strength of the PLA fiber increased with the increase of ambient temperature up to 25°C. When the temperature is higher than 25°C, the tensile strength dramatically decreased with the increase of spinning temperature. The PLA fiber could obtain the highest tensile strength of 2.2 GPa when the spinning temperature was 25°C. Postema et al. 45 also studied the effect of extrusion speed and winding speed on the tensile strength of PLA fiber and indicated that the tensile strength of PLA fiber decreased with the increase of extrusion rate. It was also found that there was no correlation between the extrusion rate and the crystallinity of the PLA fiber. The flow instability could lead to voiding and cavitation on the PLA fiber, damaging fiber properties.
PLA fibers manufactured with additives were studied by Leenslag et al. 46 The PLA was dissolved in chloroform with different additives including toluene, camphor, poly(L-lactide)-polyurethane and commercial medical-grade polyurethane. After the fiber spinning, hot-drawing was carried out. The PLA fiber manufactured showed a loosened fibrillar structure.
Melt spinning
Melt spinning is the most studied and applied method for manufacturing PLA fibers. A number of researchers have studied the melt spinning of PLA fiber under various spinning conditions such as processing temperature, extruding speed, take-up speed and hot-drawing conditions, etc. 4 Figure 9 shows the schematic diagram of the manufacturing process of melt spinning.

Melt-spinning process and equipment. 43
Eling et al. 3 manufactured PLLA fiber with high degree of orientation and crystallinity from low Mw (below 300,000 Da) PLLA polymer. The PLLA polymer was molten and extruded to form filaments with a diameter of 1 mm at 185°C. The take-up speed was 25–35 cm/min. After the spinning process, the fibers were hot-drawn in an electric tube furnace with an input speed of 20 mm/min. The highest tensile strength of the fibers was found to be around 0.5 GPa. Fambri et al. 47 also reported the production of melt-spun PLLA fiber using polymer with a Mw of 330,000. To prevent the hydrolysis degradation, the PLLA polymer was dried at 50°C under vacuum condition for 48 h before the melting and extrusion process. A single-screw extruder with a diameter of 1 mm was used to spin PLLA monofilament under an inert atmosphere. A high take-up speed of 20 m/min was achieved. The monofilament was then drawn at 160°C using hot-plate drawing equipment with different drawing speeds and drawing cycles. It was found that the PLLA monofilament could reach the highest tensile strength of 0.87 GPa when it was drawn 10 times at 5 m/min.
A two-step method was used by Cicero et al. to spin PLA fibers. 48 , 49 Before production, textile-grade PLA pellets were dried at 82°C to reduce the water level of the polymer to around 100 ppm. A Killion KL-125 single-screw extruder was adopted to produce PLA monofilament. After the filament was extruded out of the extruder, it was quenched in a water bath. Then the fiber was cold-drawn with a constant draw ratio of 40. The take-up speed was between 7.5 and 60 ft/min. The PLA fiber manufactured by this method was found to have fibrillar morphology with microfibril diameters in nanoscale. Yuan et al. 50 also prepared PLA fibers using a two-step method. Pulverization and drying were carried out before the melt-spinning process. The PLA fibers were spun using a laboratory single-screw extruder which has three temperature zones with temperatures ranging from 200 to 240°C. A sandblasted glass drum was used to wind up the extruded filaments with a speed of 3.2 m/min. Following the extrusion, the filaments were drawn under a nitrogen environment at 120°C. The feed speed and take-up speed of the drawing process were 0.26 m/min and 1.09 m/min, respectively. After drawing, the filaments were kept under nitrogen at 120°C for another 10 min to produce the final hot-drawn fibers.
Ghosh and Vasanthan 51 studied the influence of spinning speed and drawing on fiber properties. PLA filaments were melt-spun at two spinning speeds of 500 mm−1 and 1850 mm−1, and the hot-drawing and heat-set processes were applied. The authors found that the PLA filaments produced at 500 mm−1 had almost no crystal region, whereas the PLA filaments produced at 1850 mm−1 had around 6% crystallinity. After drawing and heat-setting, the crystallinity of the PLA filaments was found to be further improved by around 60% compared with both 500 mm−1 and 1850 mm−1 as-spun filaments. The effects of draw ratio and temperature on the tensile and thermal properties and morphology of melt-spun PLA filaments were discussed by Persson et al. 52 Both monofilaments and multifilaments were manufactured and studied. These authors concluded that the melt draw ratio (ratio of extrusion speed and take-up speed during spinning), solid-state draw ratio (ratio of post-spinning drawing) and drawing temperature were the most important factors affecting the mechanical properties of PLA fibers. The orientation and crystallinity of the PLA fibers were found to be increased with the increase of solid-state draw ratio, which was dependent on the melt draw ratio. To manufacture PLA fibers with higher orientation, crystallinity and tenacity, a higher solid-state draw ratio was preferred, and the melt draw ratio should be lower accordingly. A drawing temperature of 90°C was proven to be suitable for manufacturing PLA fibers with the highest tenacity.
The degradation of PLA is one of the most critical problems of the melt-spinning method. It was observed that degradation could occur during the pulverization, spinning and post-spinning operations, which can cause 13.1–19.5%, 39–69% and around 9.1% degradation, respectively. 4 , 36 , 37 The degradation is believed to result from thermohydrolysis, depolymerization, intermolecular and cyclic oligomerization and transesterification. Specifically, the ester linkages of the PLA molecules are broken by water molecules and depolymerization processes due to hydrolytic cleavage. To minimize the degradation of PLA polymer during fiber spinning, dried PLA has to be used.
In addition to conventional PLA filament, PLA resin can be blended with other materials such as PBS and poly (hydroxybutyrate-co-hydroxyvalerate) (PHBV) to spin blended filament through the spinning process.53–55 Hassan et al. 55 fabricated PLA/PBS blended filaments with five different blending ratios for healthcare products. The proportions of PBS of the blended filaments were 0, 3%, 6%, 9% and 12%. PLA and PBS pellets were mixed according to the blending ratio in a container before being added into the extruder. The mixed polymer chips were then dried in a vacuum at 80°C for 2 days to remove moisture. A two-step melt-spinning/hot-drawing process was used to spin the blended filaments. The PLA/PBS blended filaments were found to have excellent miscibility and compatibility. The addition of PBS endowed the filament with improved melting temperature, crystallinity and elongation. Li et al. 53 manufactured PLA/PHBV blended filaments and studied the properties of these blended filaments. Four types of blended filaments containing 10, 20, 30 and 40 wt% PHBV were manufactured for comparison using a melt-spinning/hot-drawing process. The PLA and PHBV pellets were mixed according to the weight ratio and dried at 80°C for 16 h before the melt-spinning process. The spinneret temperatures for spinning blended filaments with 10%, 20%, 30% and 40% PHBV were 227°C, 223°C, 220°C and 218°C, respectively. After spinning, the as-spun fibers were hot-drawn immediately with a draw ratio of 1.6. It was observed that the addition of PHBV can result in a blended filament with superb softness. However, the increase of PHBV content could result in the deterioration of other properties including the melt-spinnability, tenacity, modulus and elongation at break, etc.
PLA filament with special functionality can also be manufactured using a melting–spinning technique. Antibacterial PLA/zinc oxide (ZnO) filament was developed by Doumbia et al. 56 The dried PLA pellets and nano ZnO were first mixed in a turbomixer. They were then added into a conventional co-rotating twin-screw extruder for further mixing and melt-compounding. The mixture was then extruded and pelletized for the melt-spinning process. The PLA filaments functionalized by nano ZnO were produced using a normal melt-spinning technique for PLA fiber. It was found that the nano ZnO-functionalized PLA had effective antibacterial performance, and also showed improved thermal and mechanical properties. In other research by Annandarajah et al., 57 the PLA fiber with insect-repellent functionality was manufactured using melt spinning. The manmade insect repellent (N,N-Diethyl-meta-toluamide (DEET)) and the natural insect repellent (pyrethrum) were added to PLA fibers through the extrusion process. After manufacture of the functionalized PLA fibers, the insect-repellent performance and the mechanical properties of these PLA fibers were measured. It was observed that the addition of DEET and pyrethrum in PLA fibers could repel mosquitoes effectively, but it also caused depolymerization and reduction of the mechanical properties of the PLA fibers. In addition, the authors indicated that the PLA fiber with natural pyrethrum showed higher efficacy than PLA fiber with DEET in repelling mosquitoes.
Texturing of PLA filament
Cayuela et al. 58 , 59 studied false-twist textured and stabilized PLA filaments. The PLA filaments were false-twist textured at various temperatures of 135°C, 150°C and 165°C and draw ratios of 1.30, 1.35 and 1.40, respectively. After texturing, the filaments were further stabilized by a continuous heat-setting process at 50 m/min and 100°C in a specially designed chamber. The dimensional stability, mechanical properties and crystallinity, etc., of these PLA fibers were examined. It was found that the textured fibers without setting process had extremely low stability, which exhibited more than 40% of wet and dry shrinkage. In addition, the stabilization process dramatically increased the crystallinity and orientation of the textured PLA filaments. The stabilization process also significantly enhanced the mechanical properties including initial modulus, tenacity and elongation of the PLA filaments.
Manufacturing of PLA yarns
The PLA fiber, as one type of manmade fiber, can be manufactured in the form of staple fiber to produce staple spun yarn using a conventional staple spun yarn manufacturing procedure as shown in Figure 10. Many studies have demonstrated that staple spun PLA yarn can be manufactured with both pure PLA fiber and blends of PLA with other fibers such as cotton, lyocell and rayon, etc. Both the ring spinning system and rotor spinning system can be used to manufacture staple spun PLA yarns. Some researchers have also shown the manufacture of fancy yarns using PLA staple fiber or filament.

Manufacturing process of the staple spun PLA yarn
In the staple fiber spinning system, the spinning process and parameters are strongly affected by the fiber properties. The spinnability of commercially available PLA fiber is similar to that of PET fiber. 60 The PLA fiber has low moisture regain and high mass specific resistance, leading to the easy accumulation of static electricity on its surface during the spinning process. Therefore, the environmental conditions (temperature and humidity), machine speed, roller material and roller pressure, and so on, need to be well controlled and designed. The PLA fiber has high tensile strength, low inter-fiber friction force and low cohesive force, which also influence the spinning process to a large extent.
Ring spinning of PLA yarn
Pure PLA yarn
The staple spun pure PLA yarn can have unique properties such as fluffy handle and moisture conductivity that the PLA filament cannot have. To date, a number of studies have reported manufacturing techniques for ring-spun pure PLA yarn and discussed the influences of manufacturing parameters and finishing on yarn properties.
Li et al. 61 manufactured carded staple spun PLA yarn with a thickness of 9.7 tex. In the opening and cleaning process, the machines were set to process fibers with more opening effect and less cleaning effect in order to prevent fiber adhesion and to reduce fiber damage. Then, in the carding process, the gauge between the cylinder and flats was set to be larger than that in cotton spinning, and the production speed was relatively low to guarantee sliver formation as PLA fibers have low cohesive force. Three draw-frames were used in the drawing process. A high twist level was used for roving to increase the cohesive force between fibers, which was able to reduce fiber slippage during the spinning process. The PLA yarn manufactured was found to have more thin-place faults than cotton yarns due to the fiber slippage and unexpected sliver drafting.
Zhao 60 produced carded staple spun pure PLA yarns with different thicknesses (9.8 tex, 11.5 tex, 14.7 tex, 19.7 tex, 27.8 tex) using a two draw-frames process. Anti-static agent and anti-lubricant was mixed with PLA fibers in the opening and cleaning process to prevent the accumulation of static electricity. The machine settings in all the processes from opening and cleaning to spinning followed the principle of large gauge, strong control of the fiber and low production speed.
Wang et al. 62 studied the influence of the twist level on the yarn strength and found that the breaking strength of 15 tex carded PLA yarn increased from around 91 cN to 140 cN when the twist factor increased from 280 to 400, and then decreased with further twisting. This trend fits the general features of staple ring-spun yarn. The critical twist factor of the staple spun PLA yarn was 405.9. Jiang and Gu 63 illustrated the effect of heat finishing on the mechanical properties of PLA yarn. When the temperature of the heat finishing ranged from 60°C to 120°C, the breaking strength of the PLA yarn was found to increase with higher finishing temperature. However, the strength dropped dramatically once the temperature exceeded 120°C. This was because the molecular structure of the PLA was damaged under high temperature. In addition, the PLA yarn had higher elongation at yarn breakage when it was treated with higher temperature, as the higher temperature would reduce the intermolecular force and make it easier to create molecule displacement of PLA. These authors also demonstrated that the initial modulus of the PLA yarn decreased with the increase of heating temperature until 120°C.
The staple spun pure PLA yarn can also be manufactured by the Siro spinning technique. Li and Zhao 64 studied the influence of spinning parameters on the strength, hairiness and unevenness of 23.9 tex Siro-spun PLA yarn. They found that the roving twist factor, the gap between two rovings on the spinning frame and the draft of the back-drafting zone of the spinning frame were the most important parameters affecting the properties of the Siro-spun PLA yarn. The optimized twist factor, gap and draft were 96, 6 mm and 1.3, respectively. The experimental results showed that the use of the Siro spinning technique could improve the yarn quality. The Siro-spun PLA yarn was found to have higher strength at break, less hairiness and fewer yarn faults. In addition, the yarn unevenness of the Siro-spun PLA yarn was improved to a large extent due to the doubling effect of the Siro spinning technique.
Blended PLA yarn
To date, most research on PLA yarn has focused on blended PLA yarn, as blended yarn can have many benefits such as combining the advantages of different fibers and reducing production costs. Zhang et al. 65 manufactured 13 tex PLA/cotton blended yarn with a blend ratio of 65/35. In their method, the PLA fiber and cotton fiber were blended during the drawing process to reduce damage to the PLA fiber and to guarantee the right blending ratio. Before drawing, the cotton and PLA were processed separately. A combing process was applied to the cotton fiber to further reduce impurities, neps and short fibers. Three drawing processes were used to evenly blend the cotton fiber and PLA fiber. In the roving and spinning process, these authors used high twist level, low production speed and low tension.
The 14.7 tex carded PLA/cotton (50/50) blended yarn was manufactured by Cheng et al. 66 via a manufacturing process similar to the process Zhang et al. 65 used. They also manufactured polyester/cotton (50/50) blended yarn with the same thickness to examine differences between PLA/cotton blended yarn and polyester/cotton blended yarn. The PLA/cotton blended yarn was found to have more hairiness and higher extension than polyester/cotton blended yarn. In addition, the strength at breakage of PLA/cotton blended yarn was lower than that of polyester/cotton blended yarn.
In other research by Zhang et al., 67 PLA staple fiber was blended with alginate fiber and chitosan fiber to produce “green” yarn for medical applications. The linear density of the yarn was 14.8 tex. The blending ratio of the alginate/chitosan/PLA was 40/40/20, which could effectively combine the unique properties of each fiber. They also adopted a carding process and sliver blending and three drawing processes. In addition to the normal preparing and spinning processes mentioned before, pretreatment of fibers was applied in which the fibers were mixed with oil to prevent static accumulation during the spinning process. In the ring spinning process, the Siro-compact spinning technique was applied resulting in less hairiness, higher strength and lower unevenness of the yarn.
Manich et al. 68 used carded Siro-spun 55/45 PLA/wool blended yarn to make woven fabrics. The yarn had a thickness of 2 × 16.7 tex and a twist of 640 twist/meter. The PLA fiber used was specially designed for PLA/wool blended spinning. The length of the staple PLA fiber was 75 mm, and the fineness was 3 dtex. The wool was Australian wool with an average fineness of 19.5 µm.
The yarn quality and properties of blended PLA yarns have been widely discussed and studied. For the PLA/cotton blended yarn, Shan and Li 69 and Meng and Li 70 demonstrated that the yarn unevenness and hairiness were strongly affected by the blending ratio between PLA fiber and cotton fiber. Yarns with PLA contents of 0 (pure cotton yarn), 20%, 35%, 50%, 65%, 80% and 100% (pure PLA yarn) were tested. It was found that the yarn unevenness was reduced with the increase of PLA fiber content, and the pure PLA yarn was the most even yarn. The relationship between blending ratio and yarn hairiness was similar to that between blending ratio and yarn unevenness. It was found that the yarn hairiness could be largely reduced when the PLA content increased from 0 to 65%. However, if the PLA content was higher than 65%, the yarn hairiness would increase again. However, with a higher proportion of PLA fiber, the yarn hairiness will devolve again. The influence of blending ratio of PLA/cotton yarn on mechanical properties was further studied in several studies. 71 , 72 The breaking strength of the PLA/cotton yarn decreased with the increase of PLA content from 0 to 50%. When the PLA content was over 50%, the blended yarn was found to be stronger with the increase of PLA fibers. The breaking elongation of the PLA/cotton blended yarn was found to be stable when the PLA content was under 50%, and it dramatically increased with the increase of PLA fiber when PLA fibers exceeded 65%. The reason is that in the blended yarn, the fiber with lower breaking elongation would break first and cause breakage of the whole yarn. When the PLA content was under 50%, the cotton fiber dominated the breaking elongation, as the cotton fiber had much lower breaking elongation compared with PLA fiber. When the PLA fiber was over 65%, the breaking elongation of the blended yarn was decided by the PLA fiber, and thus the breaking elongation was greatly increased. In addition, Zhao et al. 73 proved that the blending ratio could also have huge effect on the specific work of breaking and initial modulus of the blended PLA yarn. It was found that the specific work of breaking of the PLA/cotton blended yarn increased with the increase of the PLA content and, on the contrary, the initial modulus of the yarn gradually decreased with the increase of PLA fiber. Tan et al. 74 measured the stress-relaxing property of PLA/cotton blended yarns with different blending ratios. They observed that when the PLA fiber content was around 60%, the blended yarn could have more stable inner stress, leading to better fabric stability.
Jabbar et al. 75 and Cao et al. 76 revealed the correlation between the blending ratio and the mechanical properties of PLA/lyocell blended yarn. The breaking strength and tenacity of the yarn were found to be increased with the increase of lyocell fiber proportion in the blended yarn, whereas the elongation at break decreased with the increase of lyocell fiber. These trends can be explained by two reasons. First, the lyocell fiber was more than three times stronger than the PLA fiber and had much lower elongation at break compared with PLA fiber, thus more lyocell fiber could lead to stronger blended yarn with lower elongation. The second reason was that the lyocell fiber was finer than PLA fiber, and as a result there were more fibers in the cross-section of yarn with given thickness, which contributed to the increase of overall strength of the blended yarn. In addition, the authors pointed out that, for any PLA/lyocell blended yarn, the lyocell fiber contributed more to the overall tensile strength of the yarn. This is because the elongation at break of lyocell fiber was only around 10% whereas that of PLA fiber was around 50%. Therefore, at the breaking elongation of lyocell fiber the tensile stress on PLA fiber was low, which resulted in a smaller contribution of PLA fiber to the overall strength of the blended yarn. In other research, Yang et al. 77 measured the initial moduli and specific works of breaking of PLA/lyocell blended yarns with various blending ratios. They showed that both initial moduli and specific works of the yarn at breaking increased with the increase of content of lyocell fiber.
The mechanical properties of PLA/modal blended yarn were studied by Yu et al. 78 They demonstrated that the breaking strength of the blended yarn decreased with the increasing proportion of PLA fiber until the proportion of PLA fiber reached 70%. When the PLA content was under 70% of the yarn, the breaking strength increased with higher proportion of PLA fiber. The breaking elongation of the blended yarn also increased with the increase of proportion of PLA fiber, as the breaking elongation of PLA fiber was larger than that of modal fiber, and more PLA fiber could contribute more to the overall breaking elongation of the blended yarn. In addition, the specific works of PLA/modal blended yarns at braking remained stable when the blending ratios were 30/70, 40/60 and 50/50, but surged when the PLA content exceeded 70%. The initial modulus of the yarn decreased with higher proportion of PLA fiber. Tan et al. 74 also studied the stress-relaxing property of the PLA/modal blended yarns. It was observed that, when the blending ratio of PLA/modal yarn was 70/30, the yarn could have smaller inner stress and better stability.
Rotor spinning of PLA yarn
Rotor-spun PLA yarn was reported by Zhang et al. 79 They manufactured rotor-spun PLA/cotton blended yarn with a thickness of 58.3 tex. In the opening and cleaning process, the combed cotton sliver was used to feed the opener with the PLA fibers, and thus the PLA and cotton fibers were blended in this process to ensure sufficient mixing of two types of fiber. The taker-in speed, cylinder speed and doffer speed were set with a relatively slow value to reduce fiber damage. Two-drawing processes were adopted to further mix the PLA and cotton fibers. In addition, for each drawing process, eight slivers were fed into the draw-frame, and small drafting and high-pressure technique were applied, resulting in strong control of fibers. In the rotor spinning process, the rotating speed of the opening roller was set to be higher than normal speed to increase the fiber transfer and opening effect. As the cohesive force between PLA fibers was low, the yarn was manufactured with a higher twist level. The twist factor was 10–20% higher than that of pure cotton yarn. In addition, a draw-off nozzle with relatively large diameter was used to increase the twist level on the yarn arm in the rotor. The rotor speed was set to be slower than the speed used for pure cotton yarn spinning. The rotor-spun PLA/cotton blended yarn was then measured by Zhang et al. It was found that the yarn manufactured had a breaking strength of 17.07 cN/tex and coefficient variation of unevenness of 11.88%, which met the quality requirements for making knitted fabric.
PLA fancy yarn
PLA fiber can be used to make core-spun yarn. Several researchers have manufactured PLA-based core-spun yarn using different techniques and materials. Zhang and Guo 80 developed one type of core-spun PLA/spandex yarn with the thickness of 40.13 tex on a modified conventional ring spinning frame. From fiber opening and cleaning to roving, the manufacturing parameters of the core-spun PLA/spandex yarn followed the same principles and requirements as staple spun pure PLA yarn. The spinning frame was installed with yarn guide and condenser on the front roller to feed the spandex filament into the spinning process. To balance the strength and elasticity of the yarn, the proportion of the spandex filament was chosen to be 5.658%. The core-spun PLA/spandex yarn with different twist levels and pre-drafts of the spandex filament was then produced. It was observed that, when the twist was 680 twists/m and the pre-drafts of the spandex filament was 3.91, the yarn produced could have optimized mechanical properties and appearance. The twist level of the core-spun yarn was too high, and consequently, the yarn shrinks easily after manufacturing. Therefore, after the spinning process, the heat-set of yarn twist was conducted. The yarn was immersed into hot water with temperature between 70 and 80°C and then dried at room temperature. The core-spun PLA/spandex yarn manufactured with this method was found to have high strength, good yarn evenness and few yarn faults.
The PLA/cotton composite yarn was manufactured and studied by Liu et al. 81 They modified the conventional spinning frame with Sirofil spinning equipment and spun the composite yarn using the Sirofil technique. The PLA filament was fed into the front roller of the spinning frame to form a Sirofil-spun composite yarn. Composite yarns with different blending ratios were manufactured and the properties of the composite yarns were then measured. With a higher proportion of PLA filament, the composite yarn was found to have larger breaking strength, as more PLA filament can provide more efficient covering of the yarn, and the cohesive force between the PLA filament and cotton fibers was increased. The elongation at break of the composite yarn also increased with the increase of PLA filament content, as the elongation at break of PLA filament was much higher than cotton fiber and the contribution of PLA filament to the overall elongation of the yarn increased with higher proportion of PLA filament.
Du et al. 82 studied the influence of pretention on cotton/PLA/modal/polyester composite yarn. The composite yarn was manufactured using the Sirofil technique. The linear density of the composite yarn was 36 tex. The polyester filament was used as the core and the staple cotton, PLA and modal fibers were used as the wrap of the composite yarn. Different pretensions (5 cN, 15 cN, 25 cN, 35 cN and 45 cN) were applied on the polyester filament before the filament was fed into the spinning frame. It was observed that when the pretension was 25 cN, the composite yarn had the highest breaking strength and lowest hairiness.
Production of PLA fabrics
The most commonly used fabric-producing techniques are knitting and weaving. Like other synthetic fiber yarns, PLA staple fiber yarns and filaments could be knitted or woven into fabrics using currently existing knitting or weaving machines. Blended fabrics have been developed using blended yarns or combining PLA staple yarns or filaments with other yarns such as natural cotton, wool, silk yarns, as well as manmade Tencel and lyocell yarns. The machine parameters for PLA fabric knitting and weaving are often set referring to PET fabrics, but the properties of PLA yarns and filaments should be considered, such as higher elongation, relatively lower strength and instability (becoming less elastic) after long-term storage in air.
Knitted PLA fabrics
Both weft and warp-knitted PLA fabrics could be produced with various knitting structures including jersey, pique, interlock and plating stitches. The knitting parameters are similar to those of PET fabric knitting; however, tension and stitch length should be adjusted according to the resiliency and elongation of PLA yarns and filaments.
Weft-knitted single-jersey fabrics with stitch lengths of 0.26 and 0.30 were produced using 100% PLA yarn or PLA/lyocell blended yarns with blend ratio 75/25, 50/50 and 25/75. The bursting strength of 100% PLA yarn fabric was the lowest around 300 kPa, and it rose with the increasing proportion of lyocell fibers, but was still lower than that of 50/50 PET/cotton blended fabric. Fabrics with a high proportion of PLA fibers were stiffer than fabrics with a low proportion of PLA fibers, whereas PLA-containing fabrics appeared softer than 50/50 PET/cotton blended fabric. In addition, the PLA/lyocell blended yarn fabrics had much better pilling resistance and water vapor permeability than 50/50 PET/cotton blended fabric. 75 40s cotton-rich/PLA blended yarns containing 20% or 35% PLA fibers were knitted into single-jersey fabrics. The smoothness and softness of the blended fabrics were enhanced by the addition of PLA fibers with total hand value between 3.2 and 3.5. 83
Socks and gloves were knitted using draw-textured PLA multifilaments. Socks were knitted on a 9-gauge single cylinder socks-knitting machine having 120 needles with 4 inches diameter of the cylinder. Gloves were produced on a 13-gauge glove-knitting machine. Knitting structures including single-jersey and rib were fabricated with loop length and stitch density of 0.4 cm and 56–64 stitches/cm2 for socks and 0.5 cm and 70–80 stitches/cm2 for gloves. 84 , 85
Warp-knitted PLA fabrics of velveteen structure were fabricated on a 28-gauge warp-knitting machine, having fabric density of 11.2 wales/cm and 17 courses/cm. The tensile breaking strength and elongation at break of the warp-knitted PLA fabric were 254.4cN and 83.19%, respectively. The anti-pilling level of the produced fabric was 4.5 and the drape coefficient in static and dynamic state was 46.06% and 47.05%, respectively. 86
Woven PLA fabrics
It is noteworthy that a sizing process is carried out before weaving to minimize tensions and abrasions caused by the high elongation and relatively low strength of PLA yarns. However, the poor resistance of PLA to alkaline should be considered when choosing suitable sizes. The selection of sizes and the desizing process will be discussed in the wet processing section. In comparison to PET fabric, woven filament PLA fabrics have softer hand feel and better drapability. 5
Woven PLA fabrics can made in different weaves, such as plain weave, basket weave, 1/3 twill and 2/2 twill. 87 2/2 twill woven fabrics have been made with PTT/PLA/Rayon blended yarns, having warp and weft density of 440/10cm and 390/10cm, respectively. 88 A silk/PLA blended woven fabric was manufactured using silk as warp yarn and PLA as weft yarn, with mass ratio of the two fibers about 1:1. 89 In another study, PLA filaments (50dtex/36f and 75dtex/48f) and silk (3/22.2/24.4dtex 2.5T) were used as warp or weft yarns to weave plain satin fabrics with warp density of 720/10 cm and weft density of 500/10 cm. Before weaving, PLA filaments were sized at 55°C using modified starch and polyvinyl alcohol (PVA) as sizing agent. The introduction of the PLA filament enhanced the moisture penetrability and anti-pilling resistance, but reduced air permeability and wrinkle recovery, and using PLA filaments as weft maximized the advantages of silk and PLA. 90 PLA/wool blended fabrics were woven with plain weave and twill weave structures using blended PLA/wool (55/45) Siro-spun yarns. Compared with PET/wool blended fabrics, the felting effect of PLA/wool blended fabrics was hardly developed because of the lower hydrolysis resistance and thermal stability of PLA. 68
Wet processing of PLA fabrics
After PLA fabrics have been made, they are still unattractive to consumers because of their appearance, hand feel, and lack of stability and durability. Wet processing, which involves pretreatments, coloration (dyeing or printing), finishing, and aftercare procedures, is carried out to improve fabric properties. As PLA fiber is a kind of synthetic fiber and has broadly similar properties as PET fiber, PLA fabrics have been conventionally treated with the same dyes and chemicals as for PET fabrics in wet processing. On the other hand, PLA has much lower glass transition temperature (55–60°C) and crystalline melting point (165–180°C) than PET, and hydrolytic degradation easily occurs under high temperature and strong alkaline conditions, and thus the wet processing condition should be adjusted accordingly. For instance, PLA fabrics are normally dyed with disperse dyes as for PET fabrics, but in lower temperature at 120°C. NatureWorks suggests to treat PLA fabric following this process flow: pre-heat-setting (depending on yarn type), pretreatment (desizing and scouring), dyeing, reductive clearing, post-heat-setting, finishing. 91
Pretreatments of PLA fabrics
The pretreatment processes remove impurities, make fabrics white and soft, and improve wicking properties, so that fabrics are able to accept dyes and chemicals in the later stages of textile wet processing. As a new type of textile material, PLA fabrics have been pretreated with steps referring to the processes for most commonly used cotton and PET fabrics. Typical continuous processing sequences for the pretreatment of cotton fabric and PET fabric are given as follows: cotton fabric pretreatment: gray inspection, singeing, desizing, scouring, bleaching, mercerization; PET fabric pretreatment: gray inspection, heat-setting, scouring, (bleaching).
Like PET and other synthetic fibers, PLA fiber contains far fewer impurities than natural fibers, and requires fewer treatment steps and milder conditions. The main steps for PLA fabrics are heat-setting and scouring. Normally, singeing is carried out for cotton fabrics to burn off loose surface fibers to form a smooth and uniform fabric surface. In fabrics of polyester and cellulosic fiber blends, singeing is the best method to control pilling. However, it is not suitable for PLA-containing fabrics, due to the low melting temperature (165–180°C) of PLA fibers. For PLA/cotton blended fabrics, a biopolishing enzyme has been used to remove unwanted surface hairs, and a calendering process has been used to increase the smoothness of the fabric surface. 92 In addition, some PLA yarns should be sized before weaving because of their relatively low yarn strength, so the desizing pretreatment is needed to remove sizes in a similar manner used for natural fibers. PLA fibers are sufficiently white for many purposes without bleaching. However, if they are to be used as white goods or need to be used for brilliant shades, or for those materials that have yellowed, PLA fibers can be bleached. Besides, the pretreatment for PLA/cotton blended fabrics should take cotton fiber pretreatment into consideration. Therefore, the processing sequence for the pretreatment of PLA fabric could be: gray inspection, heat-setting, (desizing), scouring, (bleaching).
Pre-heat-setting of PLA fabrics
A pre-heat-setting step prior to any wet processing is necessary when PLA filaments, especially friction-twist textured PLA filaments, are used in the fabric because of their high shrinkage potential. It is not a must for fabrics containing only PLA spun yarns to be pre-heat set. 91 The pre-heat-setting can improve the dimension stability and crease resistance, and avoid stiff and harsh fabric. The optimum heat-setting condition for spun and false-twist textured PLA yarns was reported as 30–45 s at 130°C. The false-twist textured PLA yarns exhibited much higher shrinkage than spun PLA yarns after heat-setting, scouring and dyeing. 93
The PLA fabrics were recommended to be set to a width 6–10% less than the “off loom” fabric width, and with 6–10% overfeed. 91 For PLA knitted pique fabric, the optimal pre-heat-setting process is the same as above-mentioned to treat the fabric at 130°C for 30–45 s to achieve dimensional stability with good tensile extension and formability. 94 A study showed that tension is the most important factor in heat-setting of PLA knitted fabrics. It was found that the PLA fabric’s dimensional change increased with the increase of tension applied, because of the stress relaxation in the subsequent wet processes. Thus, 0% tension was suggested for PLA fabric heat-setting. The study also showed that heat-setting made the PLA fabric stiffer and more resistant to shearing movement, resulting in worse drape and worse bending recovery ability. 95 Idumah et al. 96 , 97 compared the effects of heat-setting time on shearing properties of knitted PLA and PET fabrics. Shear rigidity and shear hysteresis of PLA fabric were significantly changed with the increasing time of heat-setting, whereas the PET fabric had little change in shear properties. PET fabric had higher shear hysteresis than PLA fabric before heat-setting and wet processing, whereas PLA fabric had higher shear hysteresis than PET fabric after the treatments. Liu et al. 98 investigated the effect of heat-setting on thermal properties of PLA fiber. The melting temperature of PLA fiber increased when heat-setting temperature was raised from 120 to 150°C due to the increased orientation of PLA molecule chains. Thermal degradation of PLA was significantly increased when the heat-setting temperature is higher than 160°C.
Desizing of PLA fabrics
As PLA yarns may have insufficient strength in weaving, sizes are usually applied to improve PLA yarn strength and resilience, and abrasion resistance. Desizing is a process to remove the sizes to avoid uneven dyeing and finishing. Sizes for synthetic fibers are normally composed of starches or synthetic chemical agents, such as PVA, carboxylcellulose, and polyacrylic acids. 99 As PLA fiber is sensitive to strong alkaline and high temperature, traditional chemical desizing including alkali steeping, acid steeping and oxidative treatment will cause high strength loss in PLA fabrics. Thus, PLA yarns are commonly sized with water-soluble PVA or polyester sizes, 9 which can be removed by hot water. In addition, biochemical enzymes are often used to decompose the starch-based sizes on PLA fabric.
Desizing conditions are recommended as chemical bath pH less than 7.5, and applied temperature below 90°C. 91 Different desizing methods for PLA woven fabrics with PVA–acrylic size have been studied. 100 The results showed that PLA fabrics had some fiber damage when treated with hydrogen peroxide with sodium hydroxide and sodium carbonate, causing 7.0% and 3.8% strength loss, respectively. Desizing with warm water, hot water, non-ionic surfactant, and anionic surfactant resulted in little fiber damage with strength loss less than 1.0%. Desizing would be completed using warm water without any chemical, which removed size effectively and retained strength. The application of ultrasonic technology in enzyme desizing of PLA/cotton blended fabric has been investigated. 101 , 102 The results showed that compared with conventional enzyme desizing, ultrasonic enzyme desizing achieved a higher desizing rate and whiteness, but reduced the fabric breaking strength. Furthermore, the desizing process could be combined with scouring, removing sizes during aqueous scouring.
Scouring and bleaching of PLA fabrics
The impurities of PLA fabrics are mainly removed in the scouring process. The main impurities of PLA fabric include lubricants or anti-static agents added to assist in spinning the yarn or knitting a fabric, dirt and stains acquired during manufacturing, and wax applied on spun yarns. As mentioned above, PLA fibers are sufficiently white for many purposes, but bleaching is still needed for extra whiteness or for the cotton component of PLA/cotton blended fabrics. The key point for PLA fabric pretreatment is that alkaline-oxidative conditions are deleterious to the integrity of PLA polymer at high temperature, although there is little damage at low temperature. The acidic-oxidative conditions do not significantly affect bulk or surface properties of PLA fiber even at high temperature. 103 To minimize the risk of hydrolysis of PLA fibers, strong alkaline conditions at high temperature for scouring and bleaching should be avoided.
According to the suggestion from NatureWorks, 91 scouring for PLA fabrics can be carried out with non-ionic scouring agents at 60°C for 10 min, using soda ash and mono sodium phosphate to adjust the pH in a range of 4.5–7.5. PLA fabric was not damaged during scouring by sodium carbonate up to 5 g/l at 60°C. 103 However, alkaline treatment with sodium hydroxide is not a suitable process for PLA fabric pretreatment, due to high strength loss at low treatment temperature. Enzyme scouring can effectively prepare PLA fabrics for dyeing. Lipase and esterase were used in pH 8 at 40°C, which improved the moisture regain and dyeing ability of PLA fabrics with little strength loss. 100 , 104
For PLA/cotton blended fabrics, cotton fiber requires intense scouring and bleaching conditions, which cause damage to the PLA fiber. The bleaching process has a greater effect on reducing the strength of the PLA/cotton fabric than simple scouring. 105 A study showed that the molecular weight of PLA and ball burst strength of PLA/cotton fabric reduced slightly after alkaline scouring in a bath containing 2 g/l soda ash and non-ionic surfactant at 60°C for 20 min, but the bursting strength of fabric was significantly reduced after hydrogen peroxide bleaching in strong alkaline condition at 95°C for 30 min. 106
The pretreatment conditions for the PLA/cotton blended fabric were optimized to avoid fiber damage. Enzyme scouring (10% owf pectinase, 60°C, 60 min) was also recommended for PLA/cotton blended fabrics which would go through deep-shade dyeing to obtain satisfactory water absorbency without causing any adverse effect on the fabric strength. However, for pale-shade fabrics, bleaching was required to achieve the correct shade on the fabrics in the dyeing process. A one-bath scouring/bleaching process with 7% owf hydrogen peroxide (100°C, 60 min) was found to be a suitable pretreatment for pale-shade PLA/cotton blended fabrics to obtain adequate absorbency and whiteness and maintain the fabric strength. 107 The cold pad batch technique has been applied to hydrogen peroxide bleaching, resulting in little PLA fiber damage, whereas the exhaust technique caused holes and slit formation in the fiber structure. Sodium chlorite and sodium hypochlorite also caused less damage to the mechanical properties of PLA in the bleaching process when compared with hydrogen peroxide. 103 , 108 An ozone treatment was carried out on PLA fabric at room temperature. A 6% increase in whiteness was observed after 10 min of treatment, which caused no surface damage to the PLA fiber. 109 UV/ozone irradiation could also modify the PLA hydrophilicity and dyeability. 110 The color depth of the PLA fabric was increased by pretreatment with UV/ozone irradiation. 111
Overall, the temperature of PLA fabric scouring has been controlled at 60°C around its glass transition temperature, and enzyme scouring is recommended to provide a mild condition. Although bleaching needs to be carried out at high temperature, a one-bath scouring/bleaching process, and cold pad batch technique has been used to reduce fiber damage.
Dyeing
As a hydrophobic polymer, PLA can readily be dyed with disperse dyes at 110°C, which is 20°C lower than the dyeing temperature of PET fiber (Figure 11). The dyeing process generally produces similar depth of shades, but inferior fastness of PET. The color fastness is greatly affected by dye exhaustion, and the shade depth is determined by the color yield based on a certain amount of dye sorption. The impact factors including disperse dye structures, polymer properties, dyeing, clearing and heat-setting conditions and their influences on dye exhaustion, color yield, and color fastness are discussed below.

Disperse dyeing of PLA and PET fabrics.
The risk of hydrolysis of PLA in alkali and high temperature condition should also be considered in dyeing. The disperse dyeing of PLA is normally carried out in acidic condition at around pH 5. However, reductive clearing after dyeing is carried out in alkali condition. Besides, reactive dyeing for the cotton fiber in PLA/cotton blended fabric is usually conducted in a strong alkali condition.
Disperse dye structures
The structures of disperse dyes affect the dyeability of PLA fiber, as shown in Table 2. The majority of disperse dyes are azo dyes, and they are often applied to PLA fabric. The dyeing and spectroscopic properties of azo disperse dyes with different substituents on PLA fabric have been studied and compared with those of PET fabric. Most of the dyes exhausted well into both PLA and PET fabrics (exhaustion >90%), except those having the -C2H4OH group. The shade of a given dye on PLA was deeper (higher K/S values), yellower (lower λmax) and slightly brighter than that on PET, when applying the same dye concentration. 112 Azo disperse dyes containing β-sulfatoethylsulfonyl group have been applied in PLA fabric dyeing, and were temporarily solubilized and applied without dispersant. The dyes showed higher color yield and lower chemical oxygen demand levels when compared with commercial disperse dyes. However, the dyeing properties of these azo disperse dyes containing β-sulfatoethylsulfonyl group and formed with different structures were different. Some should be used in acid condition and could obtain good to very good wash fastness, whereas others should be used in alkaline condition with very poor to poor wash fastness. 113 , 114 In addition to azo disperse dyes, aminoanthraquinone dyes with strong hydrophobicity have been applied in PLA dyeing. Good exhaustion (higher than 85%) and wash fastness between 4 and 5 were obtained. The dyes with aromatic amino or cyclo-fatty amino groups had higher light fastness than dyes with fatty amino groups, while the substitution had little effect on wash fastness. 115
The effects of disperse dye structures and substituents on PLA dyeing
New disperse dyes have been developed as dyestuffs for PLA fiber coloration. Novel disazo pyrazole disperse dyes with two pyrazole rings were synthesized by diazotizing and coupling reactions. The absorption ability of these dyes substituted with electron-withdrawing and electron-donating groups at their o-, m- and p-positions was examined in detail. 116 These synthesized yellow-red dyes were applied to PLA, PET, and polyamide (PA) 6.6 fibers, resulting in quite high color yield on PLA and PET fabrics with high K/S values leading to medium to heavy depth of shades at only 2% dye concentration. PLA and PET fabrics presented higher color strength and darker shades than PA 6.6 fabrics, while the light fastness of PET fabric was better than PLA and PA 6.6 fabrics. The dyed PLA fabrics displayed better sublimation fastness than dyed PET and PA 6.6 fabrics. 117 Novel phenylazopyrazolone-containing acylamide disperse yellow dyes were designed and synthesized for PLA, based on the prediction that some polar groups build stronger force between dyes and PLA macromolecular chain. The dye sorptions changed depending on the types of acylamide dyes. The highest dye sorption of 96.8% was achieved by acylamide dye with two –(CH2)3CH3 groups. All the dyes exhibited good build-up properties, with color strength reaching saturation at 3.0% owf, and good wash and rub fastness of level 4–5 and 5. 118 A series of phenylazo-β-naphthol-containing sulfonamide disperse dyes were designed and synthesized for PLA fabric dyeing. The introduction of the tertiary sulfonamide groups gave suitable water solubility to the disperse dyes, so that the dyes had high affinity on PLA, improving dye exhaustion (98.6% was achieved) and fastness properties of PLA fabric. 119
Fundamental research on dyeing kinetics and prediction of dye sorption on PLA fiber brought better understanding of the dyeing process. The diffusion coefficient of the disperse dyes on PLA fabric was calculated, and the kinetic dyeing model was established, which was proved by the dyeing results obtained from three different disperse dyes. This model set a theoretical basis for the dyeing process of disperse dyes on PLA fabric, which guided the optimization of parameters in PLA fabric dyeing and color matching. 120 A linear equation was developed to predict the percentage sorption of disperse dyes with different structures onto PLA based on the interaction energies, which were calculated using molecular modeling. The prediction between various disperse dyes and PLA has been shown to agree with the actual percentage sorption. Dyes with stronger interactions had higher sorption on PLA fiber. The results showed that the substituents that form the strongest interactions with PLA are –N(C2H4OCOCH3)2, –(CO)2NC3H6OCH3, –SO2NHC6H5, –NO2, –CN(NH)C6H4, and –CH(CO)2C6H4, and the substituents that form the weakest interactions with PLA are –Br and –Cl. 121
Another explanation for disperse dye sorption on PLA has been made through solubility parameters. Disperse dyes with solubility parameters close to that of PLA tend to give better sorption on PLA in dyeing at 100–110°C. The chemical structure of these dyes gives low cohesive energy and high molar volume. They are mainly azo dyes and other dyes that contain more –NHR, –NR2, –NHCOR, –COR, –OR, or –COOR groups than –NO2, –NH2, –OH, –CN and halide groups, and the R groups are –CH3, –(CH2)nCH3, or a phenyl. Most anthraquinone dyes do not have similar solubility parameters with PLA, except these with large –(CH2)nCH3 groups. 122
Polymer properties
In addition to dye structures, the dye exhaustion is affected by the polymer properties of PLA (Table 3). PLA fiber generally has a moderate affinity with disperse dyes. PLA fiber with high crystallinity (50%) was found to have lower exhaustion than PLA fiber with low crystallinity (21%). The fiber with high crystallinity had a lower degree of amorphous and fewer interstices that dye molecules could penetrate, which limited the dye saturation capacities. The dyes with multiple carbonyl groups did not exhaust well on the high-crystallinity PLA, whereas their exhaustion on low-crystallinity PLA was high. 123
The effects of polymer properties on PLA dyeing
The concentration of D-isomer in PLA affects its crystallinity, and further influences its dyeability. PLA fibers with higher D-isomer concentration have greater fiber entropy, more amorphous and less crystalline regions in the polymer, with respect to low D-isomer fibers. Therefore, high D-isomer fibers presented greater dye exhaustion and color strength for all kinds of dyes and concentrations. Beside, high D-isomer fibers could be dyed to an excellent black shade, whereas low D-isomer fibers appeared very brown. The wash fastness of both fibers was very similar. 124
Nanoparticles were added in PLA fiber to improve its dyeability. The addition of N-Phenylaminopropyl polyhedral oligomeric silsesquioxane (AP-POSS) during melt spinning is effective for increasing the dyeability of PLA fiber regardless of the type of disperse dye. The effectiveness of AP-POSS rose with the increase of the amount added, and it was more effective in disperse dyes with low dye exhaustion. The main reason for the dyeability enhancement is the huge surface area of AP-POSS, which is essential for good sorbent. The polar (secondary amine structure) and aromatic (benzene ring) functional groups of AP-POSS also improved the attractions between PLA fiber and dye molecules. 125 The improvement of dyeability on PLA fiber was also investigated by addition of octa (aminophenyl) polyhedral oligomeric silsesquioxane (OAP-POSS) 126 and octaammonium polyhedral oligomeric silsesquioxane (OA-POSS) (dyeing with anionic dyes) 127 nanoparticles during the melt spinning.
The dyeing efficiency on PLA could also be enhanced by plasma treatment and coating with polyethylene glycol, because the surface roughness and hydrophilicity of PLA fiber were increased. 128
Dyeing conditions
The effects of dyeing temperature, time and pH on dye exhaustion, shade depth and color fastness have been studied in a great number of research works. Scheyer and Chiweshe 123 studied nine disperse dyes on PLA fabric, and four of them had exhaustion values greater than 60% at 2% owf dye concentration and 100°C. The dye exhaustion percentages for disperse dyes increased dramatically, while the temperature rose from 70°C to 100°C. Maximum dye exhaustion occurred within 30 min for most dyes. The dyed PLA fabrics had acceptable wash fastness with ratings higher than 4, but low staining fastness with ratings lower than 3. Another study 129 showed that two out of the 10 disperse dyes had exhaustion higher than 80% on PLA with 2% owf dye at 110°C and pH 5, while all 10 dyes had more than 90% exhaustion on PET at 130°C. Although PLA had lower disperse dye exhaustion than PET, it had 30% higher color yield, which was attributed to the lower reflectance of PLA. A similar apparent shade depth could be achieved on PLA as for PET. The dyed PLA fabrics had lower washing and crocking fastness, and similar light fastness compared with PET. An energy-saving dyeing process was developed in which the PLA fabric was kept in dye bath at 60°C for 10 min and then dyed at 110°C for 10 min. The same color fastness was achieved by this two-stage dyeing process when compared with a conventional dyeing process at 110°C for 30 min. 130 In terms of the shades, Choi and colleagues 131 , 132 found that the yellow and blue dyes were greener and orange/red dyes were yellower in hue on PLA than on PET, while PLA has brighter shades and greater values for hue angle (h) than PET for the same dye.
Ultrasound was applied to enhance the color strength of disperse dyeing on PLA, which was attributed to dye disaggregation. The color strength of three (out of six) disperse dyes was improved by ultrasound when dyeing at 70°C, but dyeing at 80°C in the presence of ultrasound resulted in pale, dull shades because of the breakdown of the dye dispersions at this particular temperature. 133
Non-aqueous dyeing was developed for disperse dyeing on PLA fiber to reduce the hydrolytic degradation of PLA fibers under the conventional aqueous dyeing conditions. PLA fabric was dyed with disperse dye in supercritical carbon dioxide (SC-CO2) at pressure of 17 MPa and 120°C for 60 min. The breaking strength loss of SC-CO2-dyed PLA fabric was 9.22%, which was much improved compared with the 44.66% loss of fabric dyed in aqueous condition. The dye sorption of PLA in SC-CO2 increased faster and reached dyeing equilibrium in 10 min, whereas it took 40 min in water. The wash fastness and light fastness of SC-CO2-dyed PLA fabric and aqueous dyed fabric were comparable. 134 Solvent disperse dyeing using liquid paraffin without water and auxiliaries at 130°C achieved high-quality dyed PLA fabrics. The solvent dyed fabrics had color fastness comparable to aqueously dyed fabrics. After post-heat-setting, the degree of orientation increased from 80.6% to 85.6%, and the breaking strength loss decreased from 59.1% to 16.7%. The solvent dyeing did not require high-pressure equipment as for SC-CO2 dyeing. 135
Clearing
In the disperse dyeing process, dye molecules are deposited on PLA fibers. The unfixed dye molecules should be removed to improve color fastness and shade by a clearing step using a detergent or reductive agent. The azo disperse dyes can be decomposed by a reductive agent (sodium dithionite) in alkaline condition. Reductive clearing of dyed PET fibers is usually carried out using 2–3 g/L sodium dithionite and 1–3 g/L sodium hydroxide, at 70–80°C for 10–20 min. However, PLA is sensitive to alkaline condition, and the milder alkali sodium carbonate is used to substitute sodium hydroxide for clearing. Preferred conditions for PLA fabric were clearing with 2 g/L sodium carbonate and 2 g/L sodium dithionite at 60°C for 15 min. The effect of reductive clearing on wash fastness depends on the chemical structures of the dyes. A high level of wash fastness was achieved by alkali-sensitive disperse dyes. 136 It could also be achieved by lower air content in the sealed reduction-clearing equipment and a greater amount of sodium dithionite in the clearing bath. 137 Clearing of dyed PLA fabric under acid condition was also carried out. Reductive agents including zinc formaldehyde sulphoxylate, a sodium salt of a sulphinic acid derivative, and a sulphinic acid derivative were applied at pH 5.0 and pH 4.0, respectively, which obtained commercially acceptable high levels of wash, alkaline perspiration and wet rubbing fastness. 138
ECE detergent clearing on disperse-dyed PLA fabric had comparable effectiveness in terms of fastness and color in comparison to the traditional reduction clearing with sodium carbonate and sodium dithionite. This alternative after-clearing reduced the risk of hydrolytic damage of PLA fibers and chemical consumption. 139 Water clearing on disperse-dyed PLA fabric showed little improvement on fastness and little effect on color. 140 , 141 Both wash and rub fastness were improved when clearing temperature rose from 50°C to 60°C, but little improvement on clearing effectiveness could be made when the temperature was further increased to above 60°C. 139 , 141
Ultrasound was also applied to assist the clearing of disperse-dyed PLA fabric, resulting in an enhancement of the rub fastness of both reduction clearing and ECE detergent clearing, but with little change on color. 140 , 141
Post-heat-setting
As a type of synthetic fiber fabric, after dyeing PLA fabrics are heat-set at 125°C for 25–45 s. Many factors should be considered when dealing with the post-heat-setting conditions including the desired width, density, smoothness, drape, hand feel and bulk of PLA fabrics. Experiments were suggested to be carried out to set the final condition for each type of fabric. 91
Dyeing properties are also affected by the post-heat-setting through thermal migration. A dyed PLA fabric was reported to exhibit 0.5–1.0 levels lower in wash fastness (particularly the stain on a nylon adjacent) compared with PET fabric, because of the higher degree of thermal migration of the disperse dyes to the surface of the PLA fiber. There was no loss of disperse dye due to sublimation after heat-setting at 130°C for 30 s. 142
Natural dyes, vat dyes and cationic dyes
In addition to disperse dyes, the application of natural dyes, vat dyes, and cationic dyes on PLA fabrics has been investigated. Many natural dyes have been used to dye PLA fiber including curcumin, emodin, indigo, and so on. The application of natural dyes on PLA has environmental advantages. It is suggested that natural dyes that have similar solubility parameter to the fiber could have good dyeing properties. As most natural dyes are soluble in water, they can readily dye on hydrophilic textile fibers. 143 As curcumin is hydrophobic in nature, it was found to be dyeable on PLA fiber. It was applied on PLA at 110°C, providing a bright yellow color. It had higher build-up and color yield on PLA than on PET. 144 Natural emodin dye was also used on PLA fabric at 100°C and gave the fabric a brilliant yellow color and excellent soaping and crocking fastness at levels 4–5 and 5. 145 Other natural yellow dyes from turmeric and cassumunar had good dyeing properties and exhibited medium-deep shade and fluorescence emission on PLA fabric. 143 Natural indigo dye was applied on PLA fabrics by exhaustion in the presence of 5 g/L sodium dithionite and 0.2 g/L sodium hydroxide at 80°C for 60 min to obtain the maximum color strength. 146 Many other natural dyes were compared including marigold petals, rhubarb rhizomes, garcinia barks, turmeric rhizomes, sappan barks and catechu barks. The results showed that only the turmeric dye performed well on PLA. 147 Like disperse dyes, the addition of POSS nanoparticles enhanced the dyeability of natural dyes. 148
PLA fabrics have also been dyed with vat dyes. Three indigoid vat dyes were applied, showing increasing color strength and fastness with the rise of dyeing temperature from 60°C to 110°C. The vat-dyed PLA fabrics had inferior wash fastness to dispersed-dyed PLA and vat-dyed PA fabrics, mainly because no clearing process had been carried out to remove surplus dyes on vat-dyed PLA fabrics. 149 , 150
Cationic dyes were used to dye modified PLA films which were irradiated by UV/O3. The UV/O3 irradiation increased the hydrophilicity of PLA and introduced anionic and dipolar sites to electrostatically interact with the cationic dye. The modified PLA films were successfully dyed with 2% owf cationic dye at 60°C and pH 5.5 for 1 h. 110
Dyeing of blended PLA fabrics
As PLA/cotton blended fabric involves hydrophobic polyester PLA fiber and hydrophilic cellulose cotton fiber, like PET/cotton blended fabric, it should be dyed with a two-bath, two-stage process in which the PLA component is dyed using disperse dyes, followed by the cotton component being dyed with reactive dyes. However, reactive dyeing for cotton fiber is normally carried out in strong alkaline condition, which may cause high hydrolysis of PLA. To avoid severe strength loss of PLA, low temperature (lower than 60°C) and low alkali concentration (less than 3 g/L) were applied in reactive dyeing for the cotton component in PLA/cotton blended fabric, while the PLA component was first dyed with disperse dyes at 110°C with pH 5 for 20 min. The fixation rate, which refers to the percentage of dyes forming covalent bonds with cotton fiber, was investigated in terms of reactive dye structures. The results showed that, in this low-temperature and low-alkali dyeing system, the reactive dyes containing monofluorotriazine and monofluorotriazine/sulphatoethylsulphone groups gave higher total fixation rate than conventional monochlorotriazine and monochlorotrizaine/sulphatoethylsulphone groups-based dyes. 151 A reactive-disperse dye was synthesized to dye the PLA/cotton blended fabric in one bath. Its dyeability for PLA and cotton was studied separately. The findings indicated that synthesized dye performed better on PLA than on cotton. Using this synthesized dye, the optimal dyeing condition for PLA was at pH 6 and 110°C, while for cotton it was at 80°C with high alkali concentration. 152
PLA/silk blended fabric was dyed with Everzil ED reactive dyes in weak alkali condition using sodium bicarbonate at 80°C. The reactive dyes exhibited a good dyeability on the PLA/silk blended fabric, showing quick fixation, good build-up properties and wash and rub fastness between 4 to 5. 89
For PLA/wool blends, the wool fibers are usually dyed with acid dyes in acidic condition, which conforms with the sensitivity of PLA to alkali treatments. 5
Recently, PLA has been spun with PHBV and PBS into textile fibers. The dyeing of PLA/PHBV fabric was optimized using C.I. Disperse Orange 30, Red 74, and Blue 79 at 100°C with pH 5 for 10 min. Satisfactory build-up properties could be obtained using 1% owf dye concentration. The color fastness to laundry and rubbing of the dyed PLA/PHBV fabrics reached the commercially acceptable levels of 5 or 4–5. 153 The dyeability of PLA/PBS fabric was also investigated, which provided evidence that the addition of PBS to PLA improved the dye exhaustion and shade depth of PLA, with good wash and rubbing fastness rating 5 or 4–5. 55
Printing
Pigment printing is one of the most commonly used printing techniques for textiles. The pigments are normally cured at high temperature for a relatively long time. As PLA is sensitive to high temperature, inkjet printing on PLA fabric using UV-curable inks at room temperature was investigated. The UV-curable inks on PLA fabric were compared with thermal inks which were dried at 90°C for 5 min and then cured at 150°C for 5 min. The results obtained suggested that UV-curable inks exhibited higher color strength and better color fastness. The UV-cured fabrics had no significant changes in bursting strength, whereas the bursting strength of thermally cured fabrics decreased a lot. In addition, the effect of room-temperature UV curing on fabric handle was much less than that of thermal curing. 154 The printing of PLA nonwoven fabrics was improved by surface coating with polyacrylamide. The apparent color depth and pattern sharpness of printed PLA nonwoven fabrics were enhanced. 155
Finishing
As PLA fiber has good moisture transmission, flame retardancy, UV resistance, biocompatibility and biological resistance, 5 PLA fabrics are mainly finished to improve these properties. PLA nonwovens have been treated with chemicals or plasma to improve their performance as medical products or filters, which could also be considered as finishing processes for knitted or woven PLA fabrics to improve their properties in apparel and home textiles end-uses.
Water-repellent finishing has been carried out on PLA fabrics. Fluorocarbon finishing was applied on knitted PLA fabrics by low-temperature plasma polymerization. A perfluoroalkyl acrylate, 1H,1H,2H,2H-heptadecafluorodecylacrylate was used as the feed monomer in plasma reactor. The plasma treatment resulted in better repellency and less impact on fabric handle compared with pad-dry-cure method. The plasma-treated PLA fabric kept its repellency after washing without hot pressing. 156 The needle-punched and spunbonded PLA nonwovens were treated with C6F14 vapor plasma, which significantly reduced water and aqueous salt solutions transmission into the nonwoven structure, while maintaining its air permeability. 157 The spunlaced PLA nonwovens were finished with organic fluorin FG-910, which achieved good resistance to water, alcohol and blood with little effect on fabric strength, air and moisture permeability. 158 Superhydrophobic PLA fabrics with water contact angle around 150° were obtained by UV photo-grafting of hydrophobic spherical silica particles possessing vinyl functional groups on fabric surfaces. This one-step method gave the PLA fabric surface roughness as well as hydrophobicity simultaneously. 159
The hydrophilicity of PLA fabric has been improved by coating, enzyme treatment and plasma treatment. Hydrophilic coating on PLA fabric was studied using polyethylene glycol–dimethyloldihydroxyethyleneurea (PEG-DMDHEU) with a conventional pad-dry-cure process at relatively low curing temperature of 120°C. Highly cross-linked PEG was obtained and fixed on PLA fiber, imparting thermal adaptability and anti-static properties as permanent durable coating finishing properties. 160 Enzymatic finishing was used to improve hydrophilicity of PLA fabric. A proteolytic enzyme, alcalase from Bacillus licheniformis was applied on PLA fabric at 60°C, pH 9.5 with enzyme concentration 50%. PLA fabrics were hydrolyzed effectively, which enhanced moisture regain and dyeing properties without damage of tensile strength. 161 The treatment of Radio Frequency (RF) air plasma on PLA nonwoven modified its sorption property without reducing fabric air permeability. 157 Oxygen plasma treatment introduced new polar groups into the PLA fabric surface. 162 Knitted PLA fabrics were treated with pulsed plasma polymerization of heptylamine, giving PLA fabric excellent hydrophilicity of less than 1 s of absorption time of water drop. It gave the PLA fabric a sufficient level of primary amine functionality (3.5%) for bio-application, which could be controlled by the duty cycle and the average RF power. 163 Atmospheric dielectric barrier discharge plasma was applied on PLA nonwovens, which significantly reduced the water contact angle to nearly 0° when the treatment time is longer than 90 s, and the hydrophilicity was maintained for more than 90 days. 164
Controllable wettability of PLA nonwovens was developed by treating nonwovens with Ti(OBu)4-HFA (heptadecafluorononanoic acid) emulsion to separate oil/water mixtures. The wettability of PLA fabric could be controlled by varying the mass proportions of Ti(OBu)4 and HFA. The treated PLA nonwovens exhibited high absorption capacity and high selectivity in oil/water separation, as well as excellent photocatalysis degradation of soluble organic pollutants under UV irradiation. 165
A bifunctional PLA fabric with hydrophilicity and hydrophobicity on different sides was generated. Both sides of the PLA fabric were subjected to a plasma treatment with oxygen and methane, separately. The side treated with oxygen plasma showed micropittings in morphological analysis with high wettability and fast water absorption, while the side treated with methane had a smooth surface without wicking. 166
PLA fiber has a higher limiting oxygen index (LOI) than most fibers, which means it is more difficult to ignite. It has better self-extinguishing characteristics, burning for 2 min after a flame is removed, and it generates less smoke. However, PLA fiber is still flammable, and it melts and burns with a white flame. Flame retardant (a mixture of cyclic phosphonate esters, Afflamit PE) finish on PLA fabric was carried out by pad-dry-cure process with drying at 110°C and thermofixation curing at 135°C for 90 s. The flame retardancy of the treated PLA fabric was durable to 50 washing cycles, meeting the requirements of flame-retardant standard. The flame retardancy of the treated PLA fabric was better than treated PET fabric after repeated laundering. 167 PLA nonwovens were also treated with cyclic phosphonate ester flame retardant by a pad-dry-cure technique, which improved the LOI from 26.3% to 35%. 168
Aftercare—laundry and ironing
The low glass transition temperature and poor resistance to hydrolysis limit the aftercare temperature and pH of PLA fabrics. Ironing at high temperature should be avoided as fiber damage could be caused and, more importantly, the PLA fabric will harden and its softness, and hand feel will significantly decrease. Therefore, knitted fabrics are recommended for PLA instead of woven fabrics, to avoid wrinkles and ironing problems. 169
The laundry conditions for PLA fabrics have been investigated via 50 home laundry cycles. The pH levels (8 or 10), washing temperatures (35°C or 55°C), and drying conditions (line dry at 21°C/65% relative humidity or tumble dry at 50°C or 70°C) were compared. An appropriate laundry condition maintaining better mechanical properties was recommended using mild detergents with relatively low pH (pH 8), cold machine wash (35°C), and line dry. 170 , 171 Tumble drying should be avoided, or if it is desired, the fabric should be dried at low temperature (50°C).170–172 The mechanical properties of the laundered PLA fabric were tested by KES-F evaluation. During laundry cycles, the shear stiffness and shear hysteresis decreased, and the bending stiffness and bending hysteresis were reduced too. The compression energy of laundered PLA fabric decreased whereas the compression resilience increased. The extensibility and tensile energy of PLA fabric increased and tensile resilience decreased after laundry. 173 The load-extension behavior of PLA and cotton fabric had little change after 10 laundry cycles, whereas PET fabric retained its load-extension behavior beyond 50 laundry cycles. In terms of the constituent of fibers, laundering had greater impacts on cotton than PLA. There was no impact on PET. The life expectancy of PLA fabric was 35 washes, lower than that of PET and cotton fabrics with 42 and 43 washes, respectively. 172 Ultrasonic laundering of PLA fabrics was performed and significantly lowered fabric thermal resistance as compared with conventionally washed fabrics. 174
Conclusion
This review summarized PLA polymerization, PLA filament and fiber spinning, staple yarn spinning, fabric knitting and weaving, and wet processing. The properties of PLA fiber are broadly similar to those of PET fiber; however, differences such as low melting and glass transmission temperature, poor degradation resistance to high temperature and poor hydrolytic resistance to strong alkaline, high elongation and relatively poor storage stability, should be considered in production and processing methods. Based on this review, conclusions and future research suggestions are given as follows.
The production of the
Footnotes
Declaration of conflicting interests
The authors declared no potential conflicts of interest with respect to the research, authorship and/or publication of this article.
Funding
The authors disclosed receipt of the following financial support for the research, authorship, and/or publication of this article: This work was supported by the Innovation and Technology Commission of The Government of the Hong Kong Special Administrative Region of China in the form of an ITF project (Ref. No. ITP/061/18TP).
