Category Archives: GREEN BIORENEWABLE. BIOCOMPOSITES

DIFFERENTIAL SCANNING CALORIMETRY (DSC)

DSC is widely used to characterize the thermal properties of WPCs. DSC can mea­sure important thermoplastic properties, including the melting temperature (Tm), heat of melting, degree of crystallinity x(%), crystallization, and presence of recy- clates, nucleating agents, plasticizers, and polymer blends (the presence, composi­tion, and compatibility). Thermal analysis of the WPC samples was carried out on a differential scanning calorimeter (Perkin Elmer Instruments, Pyris Diamond DSC,

Shelton, Connecticut) with the temperature calibrated with indium. All DSC mea­surements were performed with samples of about (9.5 ± 0.1) mg under a nitrogen atmosphere with a flow rate of 20 mL/min. Three replicates were run for each speci­men. All samples were subjected to the same thermal history with the following thermal protocol, which was slightly modified from the one reported by Valentini et al.45.

1. First, the samples were heated from 40 to 180 °C at a heating rate of 20 °C/ min to remove any previous thermal history.

2. Second, the samples were cooled from 180 to 40.00 °C at a cooling rate of 10 °C/min to detect the crystallization temperature (Tc).

3.

Подпись: following equation: Xcor(%) Подпись: ДНт ДН Q. Xr Подпись: (1)

Finally, the samples were heated from 40 to 180 °C at a heating rate of 10 °C/min to determine Tm. Tm and the heat of fusion (днт) were calcu­lated from the thermograms obtained during the second heating. The heats of fusion were normalized on the basis of the weight fraction of PP present in the sample. The values of днт were used to estimate X, which was adjusted for each sample in XcOr (%) based on the percentage of polypro­pylene in the composite. Crystallinity (Xcor) was estimated according to the

ДНm and ДН0 are, respectively heats (J/g) of melting of composite and 100% crystalline PP, taken as 207.1 J/g,46 and Xpp is the PP fraction in the composite.

POL YMERIZA TION

Ethylene is a rather stable molecule that polymerizes only upon contact with cata­lysts. The conversion is highly exothermic, that is the process releases a lot of heat. Coordination polymerization is the most pervasive technology, which means that metal chlorides or metal oxides are used. The most common catalysts consist of titanium(III) chloride, the so-called Ziegler-Natta catalysts. Ethylene can be pro­duced through radical polymerization, but this route has only limited utility and typically requires high-pressure apparatus.

15.1.2.2. CLASSIFICATION

PE is classified into several different categories based mostly on its density and branching. Its mechanical properties depend significantly on variables such as the extent and type of branching, the crystal structure and the molecular weight. With regard to sold volumes, the most important polyethylene grades are HDPE, LLDPE and LDPE.

• Ultra-high-molecular-weight polyethylene (UHMWPE)

• High-density polyethylene (HDPE)

• Linear low-density polyethylene (LLDPE)

• Low-density polyethylene (LDPE)

(a) Ultra-high-molecular-weight polyethylene (UHMWPE)

These include can and bottle handling machine parts, moving parts on weaving machines, bearings, gears, artificial joints, edge protection on ice rinks and butch­ers’ chopping boards. It competes with aramid in bulletproof vests, under the trade names Spectra and Dyneema, and is commonly used for the construction of articular portions of implants used for hip and knee replacements.

(b) High-density polyethylene (HDPE)

HDPE is used in products and packaging such as milk jugs, detergent bottles, butter tubs, garbage containers and water pipes. One third of all toys are manufac­tured from HDPE. In 2007 the global HDPE consumption reached a volume of more than 30 million tons.

(c) Linear low-density polyethylene (LLDPE)

Lower thickness may be used compared to LDPE. Cable covering, toys, lids, buckets, containers and pipe. While other applications are available, LLDPE is used predominantly in film applications due to its toughness, flexibility and rela­tive transparency. Product examples range from agricultural films, saran wrap, and bubble wrap, to multilayer and composite films.

(d) Low-density polyethylene (LDPE)

LDPE is created by free radical polymerization. The high degree of branching with long chains gives molten LDPE unique and desirable flow properties. LDPE is used for both rigid containers and plastic film applications such as plastic bags and film wrap.

STARCH POLYMERS

Starch is one of the most exciting and promising raw materials for the production of biodegradable products. It is the major polysaccharide reserve material of photosyn­
thetic tissues and of many types of plant storage organs such as seeds and swollen stems. The primary crops used for its production consist of potatoes, corn, wheat and rice. In all of these sources, starch is produced in the form of granules, which vary in size and somewhat in composition based on the resources. Starch granule is composed of two main polysaccharides, amylose and amylopectin with some minor components such as lipids and proteins. Amylose is linear polymer of (1^4)-linked a-D-glucopyranosyl units with some slight branches by (1^-6)-a-linkages (Fig. 17.1). Amylose can have a molecular weight between 104 and 106 g mol-1, but it is soluble in boiling water.40,41 Amylopectin is a highly branched mol­ecule composed of chains of a-D-glucopyranosyl residues linked together mainly by (1^4)-linkages but with (1^6)-linkages at the branched points. Amylopectin consists of hundreds of short chains of (1^4)-linked a-D — glucopyranosyl interlinked by (1^6)-a-linkages (Fig. 17.2). It is an ex­tremely large and highly branched molecule with a molecular weights rang­ing from 106 to 108 g mol-1. Therefore, it is insoluble in boiling water, but in their use in foods, both fractions are readily hydrolyzed at the acetal link by enzymes. Amylases attack the a-(1-4)-link of starch while the a-(1-6)-link in amylopectin is by glucosidases. The crystallinity of the starch granules is attributed mainly to the amylopectin and not to amylose, which although linear, presents a conformation that hinders its regular association with other chains.42,43

image364 Подпись: CH2OH Подпись: CH2OH Подпись: O-

image276(Glucose-a(l -4 )-glucose)

image277

Starch has received significant interest during the past two decades as a biode­gradable thermoplastic polymer. Starch offers an attractive and cheap alternative in developing degradable materials. Starch is not truly thermoplastic as most synthetic polymers. However, it can be melted and made to flow at high temperatures under pressure and shear. It has been widely used as a raw material in film production be­cause of increasing prices and decreasing availability of conventional film-forming resins based on petroleum resources. Starch films possess low permeability and are thus attractive materials for food packaging. Starch is also useful for making ag­ricultural mulch films because it degrades into harmless products when placed in contact with soil microorganisms.44,45

By itself, starch is a poor alternative for any commodity plastic because, it is mostly water soluble, difficult to process, and brittle. Therefore, research on starch includes exploration of its water adsorptive capacity, the chemical modification of the molecule, its behavior under agitation and high temperature, and its resistance to thermo mechanical shear. Although starch is a polymer, its stability under stress is not high. At temperatures higher than 150 °C, the glucoside links start to break, and above 250 °C the starch grain endothermally collapses. At low temperatures, a phe­nomenon known as retrogradation is observed. This is a reorganization of the hydro­gen bonds and an aligning of the molecular chains during cooling. In extreme cases under 10° C, precipitation is observed. Thus, though starch can be dispersed into hot water and cast as films, the above phenomenon causes brittleness in the film.46

Plasticized starch is essentially starch that has been modified by the addition of plasticizers to enable processing. Thermoplastic starch is plasticized to com­pletely destroy the crystalline structure of starch to form an amorphous thermoplas­tic starch. Thermoplastic starch processing involves an irreversible order-disorder transition termed gelatinization. Starch gelatinization is the disruption of molecu­lar organization within the starch macromolecules and this process is affected by starch-water interactions. Most starch processing involves heating in the presence of water and some other additives like sugar and salt to control the gelatinization in the food industry, or glycerol as a plasticizer for biodegradable plastics applications. Most of the commercial research on thermoplastic starches has involved modified starches and or blends with additives and other appropriate polymers for its applica­tion as biodegradable plastics.47 The starch molecule has two important functional groups, the — OH group that is susceptible to substitution reactions and the C-O-C bond that is susceptible to chain breakage. The hydroxyl group of glucose has a nucleophilic character. To obtain various properties starch can be modified through its — OH group. One example is the reaction with silane to improve its dispersion in polyethylene.48 Crosslinking or bridging of the — OH groups changes the structure into a network while increasing the viscosity, reducing water retention and increas­ing its resistance to thermo mechanical shear.

One of the approaches to modify this starch is by acetylation to from starch acetate. Acetylated starch does have several advantages as a structural fiber or film­forming polymer as compared to native starch. The acetylation of starch is a well — known reaction and is a relatively easy to synthesize. Starch acetate is considerably more hydrophobic than starch and has been shown to have better retention of tensile properties in aqueous environments. Another advantage is that starch acetate has an improved solubility compared to starch and is easily cast into films from simple solvents. The degree of acetylation is easily controlled by trans esterification, al­lowing polymers to be produced with a range of hydrophobicities. Starch has been acetylated [with a high content (70%) of linear amylose] and its enzymatic degrada­tion has been studied. Apart from acetylation and esterification, some other modifi­cation of starch such as carbonilation of starch with phenyl isocyanates, addition of inorganic esters to starch to produce phosphate or nitrate starch esters, production of starch ethers, and hydroxypropylation of starches via propylene oxide modifica­tion has been performed. Generally all these modifications involve hydroxyl group substitution on the starch that will lower gelatinization temperatures, reduce retro — degradation and improve flexibility of final product.42

Starch has been used for many years as an additive to plastic for various pur­poses. Starch was added as a filler49 to various resin systems to make films that were impermeable to water but permeable to water vapor. The use of starch as a biode­gradable filler in LDPE was reported.50 A starch-filled polyethylene film was pre­pared which became porous after the extraction of the starch. This porous film could be readily invaded by microorganisms and rapidly saturated with oxygen, thereby increasing polymer degradation by biological and oxidative pathways.51 Otey et al. in a study on starch-based films, found that a starch — polyvinyl alcohol film could be coated with a thin layer of water-resistant polymer to form a degradable agricultural mulching film.47 Starch-based polyethylene films were formulated and containing up to 40% starch, urea, ammonia and various portions of low density polyethylene (LDPE) and poly(ethylene-co-acrylic acid) (EAA). The EAA acted as a compatibil — izer, forming a complex between the starch and the PE in the presence of ammonia. The resulting blend could be cast or blown into films, and had physical properties approaching to those of LDPE.52,53

Additionally, crosslinked starch may be induced by the addition of organic/inor — ganic esters, hydroxyethers, aldehydes and irradiation. Kulicke et al. examined solu­tion phase crosslinking of starch with epichlorohydrin and trisodium trimetaphos- phate.54 Jane et al. examined the crosslinking of starch/zein cast films for improving water resistance.55 Iman et al. studied the crosslinking of starch/jute composite with glutaraldehyde to improve its performance characteristics such as mechanical properties, thermal properties, flame retardancy, etc.56 The possibility of chemically combining starch or starch-derived products with commercial resins in such a man­ner that the starch would serve as both filler and a crosslinking agent may provide a possible approach for incorporating starch into plastics.

Commercial starch polymer based products are provided in Table 17.1 given below:

TABLE 17.1 Starch Polymer Based Products and Suppliers.42,57

Base

Source

Advantages

Disadvan-

Potential

Manufacturer

Poly-

Type

tages

Applications

(Product name)

mer

Starch

Renewable

Low cost, Fast

Poor

Foams, Films

Novament (Mater-

biodegradation

mechanical

and bags,

biTM), Biotec (Bio-

properties,

Molded

plast®, Bioflex®,

Hydrophi-

items,

Biopur®), National

licity

Starch-based

Starch (ECO-

composite

FOAM), Buna Sow Leuna (Sconacell), Starch Tech (ST1, ST2, ST3), Novon (Poly NOVON®)

One of the first starch-based products was developed probably by the National Starch in the brand name ECO-FOAMTM and used as packaging material. ECO — FOAMTM materials are derived from maize or tapioca starch and include modified starches. This relatively short-term, protected-environment packaging use is ideal for thermoplastic starch polymers. National Starch now has additional thermoplas­tic starch materials, blends and specialty hydrophobic thermoplastic starches for a range of applications including injection molded toys, extruded sheet and blown film applications [http://www. ecofoam. com/loosefill. asp]. Novament has been de­veloping thermoplastic starch based polymers since 1990. Mater-BiTM polymers are based on starch-blend technologies and product applications include biodegradable mulch films and bags, thermoformed packaging products, injection molded items, personal hygiene products and packaging foam [http://www. novament. com]. Simi­larly, Biotech GmbH produces Bioplast™ based on starch for a wide range of ap­plications including accessories for flower arrangements, bags, boxes, cups, cutlery, edge protectors, golf tees, horticultural films, mantling for candles, nets, packag­ing films, packaging materials for mailing, planters, planting pots, sacks, shopping bags, straws, strings, tableware, tapes, technical films, trays and wrap films [http:// www. biotech. de/engl/index_engl. htm]. Recently, Plantic Technologies Ltd. pro­duced soluble Plantic™ thermoformed trays for confectionery packaging.42

OTHER FIBROUS MATERIALS PRODUCED ON AN INDUSTRIAL SCALE

DuPont® was one of the first companies to attempt to produce silk fibroins on an industrial scale70, but perfecting the large-scale production of spider silks has proved arduous and challenging relative to some other materials. DuPont® manufactures ap­proximately 2 million tons of Kevlar each year, requiring 15,800,000 to 18,750,000 pounds of sulfuric acid.71 The process also requires petroleum products, substantial pressure and temperatures that approach 1,400 degrees Fahrenheit. The U. S. Army uses about 10,000 pounds of Kevlar for composite materials. Manufacturing costs could be lowered by reducing the amount of hazardous waste material generated during the production of Kevlar. Additionally, over the past 70 years, DuPont® has also been manufacturing nylon. This material initially nicknamed the “miracle fi­ber.” One of first applications for nylon was socks, but other uses have expanded into clothing, carpeting, ropes, and the automobile industry. Despite the benefits of nylon’s use for a wide range of different applications, its production has a history of environmental concerns that include the reliance of large quantities of crude oil, adipic acid, and production of nitrous oxide, a greenhouse gas.

PROPERTIES OF SPE/TPG/WF BIOCOMPOSITES

The onset and peak temperatures of the exothermic curve on the first heating DSC thermogram for the SPE/TPG compound with a standard epoxy/hydroxy ratio of 1/1 were 142.3 and 192.9 °C, respectively. Based on the DSC data, the curing tem­perature of the SPE/TPG(1/1) was changed between 150 and 190 °C. The tan 5 peak temperature (43.0, 43.5 and 53.5 °C) measured by DMA increased with an increase of curing temperature (150, 170 and 190 °C). Also, the 5% weight loss temperature (344.3, 344.8 and 361.1 °C) increased with an increase of curing temperature. When the mixture was cured at a temperature higher than 190 °C, the cured material con­siderably colorized. The curing temperature was fixed to 190 °C, considering the stability of SPE/TPG and wood flour which is subsequently added.

Figure 4.31 shows DMA curves of the SPE/TPG(1/1)/WF biocomposites cured at 190 °C. The E’ at the rubbery plateau region over 50 °C for the composites was much higher than that of SPE/TPG, suggesting a superior reinforcement effect due to the wood fibers. The tan 5 peak temperature related to T for the composites (WF40:45.6 °C; WF50:45.7 °C; WF60:44.5 °C) was a little lower than that of the corresponding neat resins (53.5 °C). The reason is not clear, but it is thought that hydroxy groups of WF reacted with epoxy groups of SPE and the stoichiometry of epoxy and hydroxy is deviated. A similar decline of Tg by the addition of WF was also observed for the GPE/TA/WF biocomposites.22 Figure 4.32 shows TGA curves of WF, SPE/TPG(1/1) and SPE/TPG(1/1)/WF composites. Since the thermal de­composition temperature of WF was lower than that of SPE/PGT, the SPE/PGT/WF composite exhibited two-step thermo-degradation, and the 5% weight loss tempera­ture decreased with increasing WF content (0 wt.%: 361.1 °C, 40 wt.%: 294.7 °C, 50 wt.%: 286.3 °C, 60%: 279.6 °C).

image104

FIGURE 4.32 TGA curves of SPE/TPG(1/1), SPE/TPG(1/1)/WF biocomposites and WF.25

Figure 4.33 shows the tensile properties for SPE/TPG(1/1)/WF composites. The tensile modulus of SPE/TPG(1/1)/WF increased with increasing WF content in the range of 0-50 wt.%. However, the tensile modulus of SPE/TPG(1/1)/WF60 was lower than that of SPE/TPG(1/1)/WF50 in agreement with the influence of WF content on the E’ measured by DMA. Also, the tensile strength of the composites with WF content 40-50 wt.% was a little higher than the corresponding neat resin (SPE/TPG(1/1)). The fact that the improvement of tensile strength is not so high as that of tensile modulus is related to the decease of elongation at break for the WF biocomposites. In the previous our study on GPE/TA/WF and SPE/QC(1/1.2)/ WF biocomposites, the tensile strength considerably decreased by the addition of WF.22,25 When TPG was used as an epoxy-hardener, the tensile strength of the WF composite did not decrease.

image105

image106,image107

Figure 4.34 shows SEM images of WF and the fractured surfaces of SPE/ TPG(1/1) and SPE/TPG(1/1)/WF composites. The micrograph of SPE/TPG(1/1) showed no phase separation, indicating that SPE is homogeneously cured with TPG. The micrograph of WF shows that the fiber length and width of WF are ca. 0.2-0.4 mm and 40-200 mm, respectively. All the micrographs of SPE/TPG(1/1)/ WF biocomposites show that WF is tightly incorporated into the crosslinked epoxy resin and their interfacial adhesion is good. The fact that tensile strength did not decrease by the addition of WF is related to the good affinity of SPE/TPG(1/1) and WF. The good affinity is inferred from what TO is widely used as a coating material for woody surface and the structure of pyrogallol moieties of TPG resembles that of lignin of WF.

DENSITY

The density of biocomposite plays a significant role in weight reduction. For en­ergy savings, designer are striving to manufacture light weight and high strength components. However it is to be noted that the density of the biocomposite have a significant influence on their noise reduction capabilities. Jute fibers are heavier than water and have a density in the range of 1200 to 1400 kg/m3.

THE FLAX WOVEN FABRICS

The flax fabric (Fig. 7.4.a) used in this study, is a plain weave fabric with an areal weight of 280±19 g/m2, manufactured by GroupeDepestele (France)68. The fabric is not balanced, as the space between the weft tows (1.59± 0.09 mm) is different to the one between the warp tows (0.26± 0.03 mm). The width of the warp and the weft tows are, respectively 2.53±0.12 mm and 3.25±0.04 mm. As a consequence, there are 360 warp tows and 206 weft tows per meter of fabric. The linear mass of the warp and the weft tows is the same and is equal to 494±17 g/km. The tows are constituted by globally aligned groups of fibers. The length of these groups of fibers varies between 40 to 600 mm with a maximum occurrence-taking place at 80 mm. This fabric is constituted of continuous tows (Fig. 4.b). Generally, when natural fibers are considered, twisted yarns are elaborated to increase its tensile properties. Indeed, as discussed by Goutianos et al.69 sufficient tensile properties of the yarns are necessary for these ones to be considered for textile manufacturing or for pro­cesses such as pultrusion or filament winding. In this study, the flax tows used to elaborate the plain weave fabric are un-twisted and exhibit a rectangular shape. The fibers or groups of fibers are slightly entangled to provide a minimum rigidity to the tows. This geometry has been chosen as it generates low bending stiffness tows, therefore limiting the crimp effect in the fabric and therefore limiting empty zones between tows. It has also been chosen because fabric manufactured from highly twisted yarns exhibit low yarn permeability preventing or partially preventing the use of processes from the LCM (Liquid Composite Moulding) family. Un-twisted tows have also been chosen because manufactured composites display better me­chanical properties than composites made with twisted yarns70. However, this rein­forcement was originally developed to manufacture large panels with low curvature and was therefore not optimized for complex shape forming.

image166

FIGURE 7.4 Reinforcement 1: (a) Flax fabric; (b) flax tow.

A second flax woven reinforcement has also been used. This reinforcement 2 is a 4/4 flax woven hopsack construction with an areal weight of 508 ± 11 g/m2 manu­factured by the Composites Evolution Company, UK71. The hopsack is presented in Fig. 7.5. The cylindrical yarns are manufactured from aligned fibers held together by a polyester yarn going in a spiral manner along the flax yarn. The linear density of the flax yarns is 250 ± 9 tex (g/km). The lineic mass of the yarn holding the flax fibers is 20 ± 3 tex. The reinforcement used in this work is not balanced. A differ­ence of 20% in the number of flax yarns has been measured between warp and weft directions.

image167

FIGURE 7.5 Reinforcement 2: (a) flax fabric; (b) 4 aligned yarns; (c) individual yarn.

7.2 RESULTS

SUGAR PALM FIBERS

Sugar palm fiber is black in color, with diameter up to 0.50 mm.70 According to Siregar,68 sugar palm fiber has heat resistant of up to 150°C and the flash point is around 200°C. It has been reported that the fiber length of sugar palm fiber is up to 1.19 m and density is 1.26 kg/m3.71,72 Traditionally, sugar palm fiber was used as ropes, filters, broom, roof and handicraft application such as for making ‘ko — piah.’72,73 Tomlinson74 reported that the ropes made from sugar palm fiber have bet­ter performance than the ropes made from rattan fiber (Calamus sp.). The main advantages of sugar palm fiber are durable and good resistant to seawater. It is also not affected by heat and moisture compared to coir fiber. Unlike other natural fibers, sugar palm fiber can directly be obtained from the trees which do not need second­ary processes to yield the fibers.3 Due to these advantages, sugar palm fiber should be a good material in the development of new ‘green’ materials.

Sugar palm fiber locally known as ijuk is one of the most popular fiber among the researcher over the last decade. The fiber is originally wrapped along the sugar palm trunk.75 The tree can grow up to 12.3 m tall and has a thick, black/brown hairy fibrous trunk, with the dense crown of leaves, which are white on the outside. The tree begins to produce black sugar palm fiber after about 5 years, before flowering and the type of its fibers are depending to age and altitude of sugar palm tree.71 The fibers that are taken after flowering will produce fiber approximately 1.4 m long. It can yield about 15 kg for each tree and around 3 kg is very best and stiffest. In Malaysia, black sugar palm fiber started used since 1416 during Malacca Sultanate History. In 1800, the sugar palm tree was planted by British East India Company in Penang to yield its high durability of rope made from black sugar palm fiber.

Previously, the characterization (tensile and chemical properties) of single fibers from different morphological parts of sugar palm tree, that is, sugar palm frond (SPF), sugar palm bunch (SPB), ijuk and sugar palm trunk (SPT).76 From the in­vestigation, it was found that the tensile strength of ijuk was 276.64 MPa and the tensile modulus was5.86 GPa. The elongation at break of ijuk was 22.3% which was approximately the same with oil palm and coir fibers in term of physical and me­chanical properties because they were from same palmae family.77 For the chemical analysis, it was shown that ijuk has a high cellulose content which is 52.29%. This proved that mechanical properties of sugar palm fiber are strongly influenced by the cellulose content.78 Cellulose was the main structural component that provides strength and stability to the plant cell walls and the fibers.49Generally, ijuk can be used as reinforcement in composites due to higher tensile strength and cellulose content in comparison with other established natural fibers such as kenaf, pineapple leaf, coir and oil palm bunch.

WATER ABSORPTION, THICKNESS CHANGES AND SPECTROPHOTOMETRIC RESPONSES

Water absorption is due to the hydrogen bonding of water molecules to the hydroxyl groups on the cells walls of the wood or lignocellulosic fibers.4870 The long-term water absorption as a function of time for the various LPCs at room temperature is shown in Fig. 13.5. All composites tested absorbed water during the incubation peri­od and no distinct saturation levels were achieved after 872 h of soaking (Fig. 13.5). The HDPE and HDPE-MAPE samples exhibited inconsequential weight gains (i. e., less than a 1% increase) after the immersion incubation time (872 h) compared to the biocomposites (Table 13.4; Fig. 13.5). Absorption of water by composites is a crucial factor in evaluating the ability of biocomposite to be commercially used.87172 To improve the resistance to water absorption inclusion of MAPE into the compos­ite formulation is routinely conducted.7172 However, we did not confirm this situa­tion for the composites used in this study. In fact, in some cases inclusion of MAPE in the formulation actually resulted in greater water absorption than that from com­posites without MAPE. For example, HDPE-25DDGS and HDPE-25DDGS-MAPE exhibited weight gains of 1.1 and 1.8%, respectively. This trend was observed for several STDDGS, PW and STPW formulations (Table 13.4; Fig. 13.5). These re­sults are somewhat surprising, since several other investigators have reported that inclusion of maleate olefins with the composite blend considerably reduces wa­ter absorption when using bio-fillers such as with Paulownia wood, loblolly wood, pine wood, sisal fiber, and wheat.437173 Practically no difference in water absorp­tion rates occurred between the HDPE-PW and HDPE-PW-MAPE formulations or the HDPE-STPW and HDPE-STPW-MAPE formulations (Table 13.4; Fig. 13.5). This observation seems counterintuitive and contrary to prior observations yet it is clearly demonstrated in this study with the PW formulations employed.437173 One explanation for the discrepancy between this study and others could be the thick­ness of the tensile bar formulations, method of processing and/or injection molding procedures employed in various studies.

TABLE 13.4 Tensile Properties of Original and Soaked Type I Tensile Bars*

Composition

su

(MPa)

E

(MPa)

EI%

(%)

Wt. Gain (%)

HDPE

35.3, 36.4*

361,376*

57.7, 55.1

0.0

HDPE-MAPE

33.0, 33.9*

362, 343

58.9, 58.0

0.0

HDPE-25DDGS

25.2, 26.4

432, 469

46.6, 43.4

1.1

HDPE-25DDGS-MAPE

29.1, 28.2*

524, 546*

28.4, 35.2*

1.8

HDPE-25STDDGS

25.6, 26.2*

435, 504*

34.5, 29.0*

0.9

HDPE-25STDDGS-MAPE

32.1, 31.1

562, 552

21.2, 19.8

1.3

HDPE-25STDDGS/A

28.1, 27.7*

590, 578

20.7, 17.7*

0.9

HDPE-25STDDGS/A-MAPE

32.2, 32.7

570, 622*

20.8, 17.5*

0.9

HDPE-25STDDGS/AM

30.4, 30.9

573, 581

17.7, 17.8

0.9

HDPE-25STDDGS/AM-MAPE

30.6, 31.0

566, 587

20.4, 17.8*

0.9

HDPE-25PINEW

32.0, 32.8

871, 870

14.9, 15.2

1.0

HDPE-25PINEW-MAPE

38.1, 38.8

714,745

20.0, 18.9

0.8

HDPE-12.5STDDGS/12.5PINEW

26.9, 28.8*

719, 779*

17.8, 16.4*

1.2

HDPE-12.5STDDGS/12.5PINEW-

MAPE

29.6, 31.0*

503, 549*

25.0, 18.5*

1.2

HDPE-10STDDGS/30PINEW

31.0, 30.1

853, 859*

11.1, 10.3*

1.7

HDPE-40PINEW

25.0, 26.8*

962, 987

6.9, 7.9

2.5

HDPE-25PW

35.2, 35.4

881,913*

13.4, 10.9*

0.9

HDPE-25PW-MAPE

40.7, 41.5

930, 923

14.2, 13.6

0.8

HDPE-25STPW

33.7, 34.0

911,926

11.8, 9.7*

0.9

HDPE-25STPW-MAPE

41.6, 41.3

931,955

12.8, 11.6

0.9

HDPE-25STPW/A

35.3, 35.2

840, 856*

9.8, 10.0

0.8

HDPE-25STPW/A-MAPE

41.2, 40.9

836, 822*

14.8, 12.3*

0.7

HDPE-25STPW/AM

39.2, 38.8

850, 865*

15.8, 14.0

0.7

HDPE-25STPW/AM-MAPE

38.8, 39.6*

817, 804

16.9, 14.3*

0.6

‘Properties are given as “original” or un-soaked, “soaked” treatments and the presence of the asterisk “*” after a value indicates significant difference between treatments (p £ 0.05).

image243

FIGURE 13.5 Comparative water absorption plots for various PW/DDGS/PINEW composites over 872 h of soaking.

The various composites exhibited distinctly different tensile bar thickness. Gen­erally, the gate section of the tensile bar is slightly thicker than the neck, which in turn is thicker than the end section (Table 13.5). This is due to the method the plastic resin and composite blend is injected into the mold; the gate portion is subjected to more injection time than the end portion and therefore contains more plastic resin than the other portions of the tensile bar. For example, the HDPE-25DDGS com­posite tensile bar exhibits an initial gate, neck and end section thickness of 3.18, 3.13 and 3.11 mm, respectively (Table 13.5). No significant increase in thickness for the tensile bar sections (gate, neck or end) of the neat HDPE and HDPE-MAPE were observed. However, increases in thickness could occur in the various com­posite formulations tested when given a soaking treatment (Table 13.5). Signifi­cant increases in thickness for the tensile bar gate, neck and end sections occurred in the HDPE-DDGS composites (e. g., HDPE-25DDGS and HDPE-25STDDGS, HDPE-25DDGS-MAPE and HDPE-25STDDGS-MAPE (Table 13.5). In contrast, the HDPE-PW composites (HDPE-25PW, HDPE-25PW-MAPE, HDPE-25STPW, and HDPE-25STPW-MAPE) only exhibited significant increases in the end section of the tensile bar. We attribute this occurrence to the presence of more PWF and less HDPE in the end portion of the tensile bar compared to that occurring in the gate and neck sections. Bio-fillers are hydrophilic in nature due to the presence of the abundant hydroxyl groups on the cellulose, lignin and hemicellulose which readily interacts with water molecules by hydrogen bonding.43 DDGS composites were ini­tially thicker than PW composites and when soaked for 872 h exhibited higher per­centages in thickness increases than PW composites (Table 13.5). We can conclude that DDGS composites are less dimensionally stable than PW composites. Inclusion of MAPE into the DDGS or PW composites did not notably alter the thickness measurements of the initial tensile bars compared to formulation without MAPE. Soaked composites containing MAPE exhibited slightly less thickness increases in terms of percent thickness increases than composites without MAPE (Table 13.5). Similarly this trend was also observed for “combination” composite mixtures (HDPE-12.5STDDGS/12.5PINEW and HDPE-12.5STDDGS/12.5PINEW-MAPE) where the inclusion of MAPE in the formulation reduced the thickness increase compared to the formulation without MAPE. This observation conforms to previous observations where inclusion of a maleate polyolefin in the formulation increases dimensional stability of the resulting composites through the binding of the cou­pling agent with the hydroxyl groups of the filler thereby preventing fillers binding to water molecules.43

TABLE 13.5 Influence of Soaking on the Thickness Swelling% of Tensile Bars of PW/ DDGS/Pine Composites

Gate

Neck

End

Composition

mm, mm (%)a

mm, mm (%)

mm, mm (%)

HDPE

3.10, 3.11 (0.24)

3.08, 3.10 (0.48)

3.09, 3.09 (-0.01)

HDPE-MAPE

3.12, 3.12 (0.07)

3.10, 3.10 (-0.09)

3.09, 3.10 (0.20)

HDPE-25DDGS

3.18, 3.21

3.13, 3.17

3.11, 3.016

(1.02)*

(1.38)*

(1.51)*

HDPE-25DDGS-MAPE

3.15, 3.19 (1.19)*

3.12, 3.15 (0.88)*

3.11, 3.15 (1.39)*

HDPE-25STDDGS

3.15, 3.18 (0.89)*

3.11, 3.14

(0.96)*

3.10, 3.13 (0.87)*

TABLE 13.5 (Continued)

HDPE-25STDDGS-MAPE

3.15, 3.17 (0.76)

3.08, 3.12 (1.27)*

3.09, 3.11 (0.77)*

HDPE-25STDDGS/A

3.13, 3.16 (0.83)*

3.09, 3.12 (1.09)*

3.06, 3.10 (1.25)*

HDPE-25STDDGS/A-MAPE

3.13, 3.16 (1.00)*

3.07, 3.10 (0.93)*

3.06, 3.09 (1.09)*

HDPE-25STDDGS/AM

—, 3.17 (—)

—, 3.13 (—)

—, 3.11 (—)

HDPE-25STDDGS/AM-

MAPE

3.14, 3.17 (1.01)*

3.08, 3.12 (1.17)*

3.08, 3.10 (0.80)*

HDPE-25PINEW

3.11, 3.14 (1.00)

3.05, 3.07 (0.53)

3.02, 3.05 (0.89)

HDPE-25PINEW-MAPE

3.10, 3.14 (1.38)*

3.05, 3.09 (1.42)*

3.01, 3.05 (1.20)*

HDPE-

12.5STDDGS/12.5PINEW

3.13, 3.15 (0.63)

3.06, 3.10 (1.15)*

3.05, 3.09 (1.34)*

HDPE-

12.5STDDGS/12.5PINEW-

MAPE

3.12, 3.14 (0.69)*

3.07, 3.11 (1.15)*

3.05, 3.08 (0.83)

HDPE-

10STDDGS/30PINEW

-, 3.16 (-)

-, 3.10 (-)

-, 3.10 (-)

HDPE-40PINEW

-, 3.14 (-)

-, 3.08 (-)

-, 3.12 (-)

HDPE-25PW

3.12, 3.14 (0.66)

3.06, 3.07 (0.48)

3.02, 3.04 (0.71)*

HDPE-25PW-MAPE

3.11, 3.12 (0.52)

3.05, 3.06 (0.36)

3.02, 3.04 (0.77)*

HDPE-25STPW

3.11, 3.12 (0.49)

3.06, 3.05 (-0.18)

3.01, 3.04 (0.98)*

HDPE-25STPW-MAPE

3.11, 3.13 (0.48)

3.06, 3.07 (0.62)

3.03, 3.04 (0.29)

HDPE-25STPW/A

-, 3.11 (-)

-, 3.05 (-)

-, 3.02 (-)

HDPE-25STPW/A-MAPE

3.11, 3.12 (0.43)

3.04, 3.07 (1.11)*

3.02, 3.03 (0.23)

HDPE-25STPW/AM

3.11, 3.12 (0.17)

3.05, 3.07 (0.71)

3.02, 3.04 (0.56)*

HDPE-25STPW/AM-MAPE

3.11, 3.12 (0.29)

3.07, 3.07 (0.08)

3.04, 3.05 (0.47)*

“Thickness properties are given as “original” or un-soaked, “soaked” treatments and percent change in parenthesis. The presence of the asterisk “*” indicates significant difference between soaking treatments (p £ 0.05).

Chemical modification treatments (A and AM) performed on the HDPE-STD — DGS formulations (HDPE-25STDDGS/A, HDPE-25 STDDGS/A-MAPE, HDPE — 25STDDGS/AM, and HDPE-STDDGS/AM-MAPE) did not improve absorption rates (% weight gain) compared to untreated controls (HDPE-25STDDGS) (Table 13.4). Thickness of DDGS formulations that were chemically modified (A and AM) were less initially than the untreated formulation. However, both formulations in­creased significantly following soaking (Table 13.5). In contrast, chemical modifi­cation treatments (A and A/M) of HDPE-STPW formulations (HDPE-25STPW/A, HDPE-25STPW/A-MAPE, HDPE-25STPW/AM, and HDPE-STPW/AM-MAPE) exhibited less weight gain compared to un-modified controls (HDPE-25STPW and HDPE-25STPW-MAPE) (Table 13.4). Thickness of STPW formulations that were chemically modified (A and AM) were initially comparable to untreated controls (HDPW-25STPW). However, all soaked STPW composites whether chemically modified or not exhibited significant increases in the end section of the tensile bar only but not in the gate or neck sections, which were much less affected (Table 13.5). One explanation for the difference in responses between the two filler for­mulations was the abundance of protein content in the DDGS formulations which contains more hydroxyl groups that can interact with water molecules during the soaking process than present in the PW formulations.

An important attribute of WPC is their ability to retain their original color and this characteristic greatly contributes toward its commercial value.7197475 Weather­ing causes color changes in WPC which is both undesirable and irreversible.71974 Water soaking is an important weathering test and is useful in determining the du­rable nature of a thermoplastic composite.764’7176 Weathering (e. g., water soaking) causes HDPE-composites to undergo chemical reactions such as breakdown of lig­nins into water soluble products which form chromophoric functional groups such as carboxylic acids, quinones, and hydroperoxy radicals.74

Figure 13.6 compares color values (L*, a* and b*) of the original composites to the soaked composites. Almost all of the composites exhibited lightness (L*) following the soaking treatment. This trend has been observed in other immersion studies employing WPC.7 Coupling agents are included in the biocomposites to im­prove bio-filler binding to the thermoplastic resin and they may combat lightness (L* value) changes.197778 Similarly, in this study, composites containing MAPE are darker than the corresponding composites without MAPE and retained their L* val­ues to a greater extent following the soaking process (Table 13.6; Fig. 13.6). For example, following soaking the HDPE-25DDGS formulation exhibited a 16% light­ening response; while HDPE-DDGS-MAPE exhibited a 6% lightening response. Overall, DDGS formulations exhibited much higher color change values (L*, a* and b*) following soaking than PW formulations. This may be attributed to water induced chemical reactions in the DDGS; suggesting that DDGS are less chemically stable than PWF. Chemical modification of DDGS resulted in less change in color values compared to that occurring in the nonchemically modified DDGS formula­tions. Changes in redness (a*) and yellowness (b*) values generally followed the L* trends, but not always (Table 13.6). Changes in the C*ab (chromaticity, color qual­ity), and H*ab (hue) values also occurred when comparing the original and soaked composites. Notable changes in color values even occurred in the neat HDPE and HDPE-MAPE polymers (Table 13.6; Fig. 13.6).

TABLE 13.6 Color Value Properties Comparison Between Original and Soaked Composites1

Composition

L*

a*

b*

/"4*

ab

H*

HDPE

62.48,

63.32*

-0.79,

-1.11*

4.02,

3.85*

4.10,

4.01*

-1.38,

-1.29*

HDPE-MAPE

60.53,

61.55*

-0.92,

-1.02

4.65,

4.42

4.74, 4.54

-1.38,

-1.34*

HDPE-25DDGS

25.62,

29.61*

0.41,

0.57*

1.56,

2.36*

1.62,

2.43*

1.31, 1.34

HDPE-25DDGS-MAPE

25.74,

27.16*

0.24,

0.35*

1.10,

1.46*

1.13,

1.50*

1.35, 1.34

HDPE-25STDDGS

30.41,

34.14*

0.71,

0.97*

2.83,

3.89*

2.92,

4.01*

1.32, 1.33

HDPE-25STDDGS-MAPE

27.50,

29.34

0.31, 0.43

1.68,

2.09

1.72, 2.14

1.37, 1.36

HDPE-25STDDGS/A

32.97,

34.95*

1.54,

1.39*

3.68,

4.41*

3.99,

4.63*

1.17,

1.27*

HDPE-25STDDGS/A-

MAPE

30.52,

31.18

0.74, 0.76

2.47,

2.87*

2.58,

2.97*

1.28, 1.31

HDPE-25STDDGS/AM

32.02,

33.60

1.28, 1.20

3.33,

3.54

3.57, 3.74

1.20, 1.24

HDPE-25STDDGS/AM-

MAPE

27.74,

29.79*

0.64, 0.78

1.98,

2.72*

2.08,

2.83*

1.25, 1.29

HDPE-25PINEW

43.08,

46.12

5.62, 5.11

13.19,

11.92*

14.34,

12.98*

1.17, 1.17

HDPE-25PINEW-MAPE

36.53,

36.40

4.35, 4.33

8.93,

8.14*

9.94,

9.22*

1.12,

1.08*

HDPE-

12.5STDDGS/12.5PINEW

36.90,

42.84*

2.02, 2.02

7.05,

8.35

7.34, 8.59

1.28,

1.33*

HDPE-

12.5STDDGS/12.5PINEW-

MAPE

40.39,

42.44

2.07,

1.68*

7.02,

7.18

7.33, 7.38

1.28, 1.34

HDPE-

10STDDGS/30PINEW

46.74,

50.63*

3.31, 3.30

11.39,

12.93

11.86,

13.34

1.29,

1.32*

HDPE-40PINEW

62.03,

63.02

4.36, 4.23

17.57,

17.18

18.11,

17.69

1.33, 1.33

HDPE-25PW

38.33,

38.19

3.22, 3.52

7.98,

8.07

8.61, 8.81

1.19, 1.16

HDPE-25PW-MAPE

31.44,

32.30

3.24, 3.35

6.60,

6.55

7.36, 7.36

1.11, 1.10

Подпись:
presence of the asterisk “*” indicates significant difference between soaking treatments (p £ 0.05).

Подпись: Ш eE 2* a a 2a 1 і 1 1 Original ^2, и / / і Soaked a a a s safe E E "/////,*. a. :rh w E E ъ 2з Подпись: HDPE-25STDDGS/AM-MAPE HDPE-25STDDGS/AM HDPE-25STDDGS/A-MAPE HDPE-25STDDGS/A HDPE-25STDDGS-MAPE HDPE-25STDDGS HDPE-25DDGS-MAPE HDPE-25DDGS HDPE-MAPE HDPE Подпись: HDPE-25STPW/AM-MAPE HDPE-25STPW/AM HDPE-25STPW/A-MAPE HDPE-25STPW/A Н DPE-25STPW-M АРЕ HDPE-25STPW HDPE-25PW-MAPE HDPE-25PW HDPE-MAPE HDPEПодпись: HDPE-40PINEW HDPE-10STDDGS/30PINEW HDPE-12.5STDDGS/12.5PINEW-MAPE HDPE-12.5STDDGS/12.5PINEW HDPE-25PINEW-MAPE HDPE-25PINEW HDPE-25STDDGS-MAPE HDPE-25STDDGS HDPE-MAPE HDPEПодпись: 0 20 40 60 L* Values </>

Ф

’35

о

Q.

E

о

о

о

ш

2 4 6 0 5 10 15 20

a* Values b* Values

FIGURE 13.6 Influence of soaking on color analysis of various PW/DDGS/PINEW composites.

Environmental stresses such as water soaking may cause changes in the me­chanical properties to occur which needs to be determined in order to assess the po­tential commercial value of a composite.7,64,70,73,76,79 For example, flexural properties have been reported to decrease when LPC are weathered.7,71,72 The response of the mechanical properties of composites as well as neat HDPE and HDPE-MAPE by water soaking are presented in Table 13.4. The neat HDPE and HDPE-MAPE blends exhibited significant changes in their oU and E values when given a soaking treat­ment (Table 13.4). Soaking caused oU values increased 3 and 3% for neat HDPE and HDPE-MAPE, respectively while %El values decreased 5 and 2% for neat HDPE and HDPE-MAPP, respectively. Soaking caused neat HDPE and HDPE-MAPE E values to change +4 and -5%, respectively. Changes in the mechanical properties for the composites varied considerably depending on the composition of the filler and MAPP concentration employed (Table 13.4). It is difficult to discern trends for the mechanical properties in the soaked and un-soaked formulations. Chemical modification of the PW and DDGS resulted in composites that when soaked main­tained their oU values (Table 13.4). However, several of these chemically modified formulations exhibited significant changes occurred for the E and %El values fol­lowing soaking. Absorption was found to be somewhat related to the variation of the mechanical properties of the composites. Formulations that maintained their me­chanical properties after prolonged soaking generally exhibited low absorption rates (Table 13.4). Even when significant differences occurred, less than a 5% change in values occurred (Table 13.4). Further work needs to be conducted to address how water absorbance affects the long-term mechanical properties of composites.

STRUCTURAL PARAMETERS

The optimized structural parameters were used in the vibrational wavenumber calculation with AM1 method to characterize all stationary points as minima. The structural parameters were calculated select the Constrain bond and length options of Build menu for two method of analysis.

15.2.2 FTIR

The energy of each peak in an absorption spectrum corresponds to the frequency of the vibration of a molecule part, thus allowing qualitative identification of certain bond types in the sample.

The FTIR was obtained by first selecting menu Compute, vibrational, rotational option, once completed this analysis, using the option vibrational spectrum of FTIR spectrum pattern is obtained for two methods of analysis. The analysis of the struc­ture of LDPE, benzophenone and WG husk with AM1 method was show in Tables 15.2-15.4, respectively.

TABLE 15.2 FTIR Results of LDPE

Assignment

Frequency (cm-1)

CH2 scissoring stretching

4341-4318

CH stretching

3418

CH2 symmetric stretching

3224

CH2-CH2 symmetric stretching

3173-3109

CH symmetric

2567

C-C

2168, 2017, 1888, 1825, 1531, 910, 894

CH2-CH2 balanced

1415, 1170, 1101

TABLE 15.3 FTIR Results of Benzophenone

Assignment

Frequency (cm-1)

CH stretching (1° ring)

3221, 3081

CH stretching (2° ring)

3159, 2944

C=O stretching

2010

C=C (2° ring)

1760

C-C (1° ring)

1550

C-C

1436, 1401

CH (1° ring)

1339,1140,1011

CH (2° ring)

1176

CH

875-861, 819

CH (2° ring)

754

TABLE 15.4 FTIR Results of WG Husk

Assignment

Frequency (cm-1)

NH

5741

CH2 stretching

4279-4029

CH asymmetric stretching

4190,3868

OH groups

3695,3319

C=C

3588, 3291

C=O, C=C

3555, 3366, 3024

C=O

2971

NH stretching

2875, 2438

C-C, C-N, C-O

2619

C-N, C-C

2226

NH

1454

C-H, C-N, C-O

1289, 1096