Hazimah Abu Hassan

Mechanical, Thermal and Morphological Properties of Poly(lactic acid)/Epoxidized Palm Olein Blend

Poly(lactic acid) (PLA) is known to be a useful material in substituting the conventional petroleum-based polymer used in packaging, due to its biodegradability and high mechanical strength. Despite the excellent properties of PLA, low flexibility has limited the application of this material. Thus, epoxidized palm olein (EPO) was incorporated into PLA at different loadings (1, 2, 3, 4 and 5 wt%) through the melt blending technique and the product was characterized. The addition of EPO resulted in a decrease in glass transition temperature and an increase of elongation-at-break, which indicates an increase in the PLA chain mobility. PLA/EPO blends also exhibited higher thermal stability than neat PLA. Further, the PLA/1 wt% EPO blend showed enhancement in the tensile, flexural and impact properties. This is due to improved interaction in the blend producing good compatible morphologies, which can be revealed by Scanning Electron Microscopy (SEM) analysis. Therefore, PLA can be efficiently plasticized by EPO and the feasibility of its use as flexible film for food packaging should be considered.

An improved method for the preparations of nanostructured lipid carriers containing heat-sensitive bioactives.

Heat-sensitive bioactive compounds such as β-carotene and tocols, are widely used in the pharmaceutical and cosmetic fields. Their chemical stability in delivery systems is one of the major concerns in the production of nanostructured lipid carriers (NLCs). A previously established high-temperature high-pressure homogenisation technique involved in the preparation of NLCs can cause degradation of heat-sensitive compounds. Therefore, a novel preparation process needs to be developed to minimise the degradation of heat-sensitive active compounds during the preparation of NLCs. In this work, modified methods A and B were designed to minimise the degradation of β-carotene and tocols during the production of NLCs. These methods improved the chemical stability of heat-sensitive bioactive compounds (β-carotene and tocols) significantly compared to the previously established method. The physical stability of the formulation was maintained throughout study duration.

Development of Flexible Polyurethane Nanostructured Biocomposite Foams Derived from Palm Olein-Based Polyol

This study examined the effect of organoclay montmorillonite (OMMT) on the mechanical properties and morphology of flexible polyurethane/OMMT nanocomposite (PU/OMMT) foams prepared from petroleum- and palm olein-based polyols. Palm-based PU foams exhibited inferior mechanical strength as compared to neat petroleum PU foams. However, addition of OMMT significantly improved the foams strength of flexible polyurethane/OMMT nanocomposite foams prepared from palm olein-based polyol (PU bionanocomposite foam). The morphology analysed by scanning electron microscopy (SEM) showed that the cell size of the foam decreased with increasing OMMT content. PU bionanocomposite foam with 5 wt% of OMMT had the most improved tensile (63%) and tear (48%) strengths compared to its neat counterpart. Transmission electron microscopy (TEM) revealed the exfoliated structure of the respective foam. It was concluded that OMMT improved mechanical properties and morphology of PU foams.

Structure–property performance of natural palm olein polyol in the viscoelastic polyurethane foam:

Structure–property behavior of the palm olein-based natural oil polyol (E-135 NOP) was investigated in viscoelastic “memory” foams. In a model viscoelastic foam formulation, the E-135 NOP with pendant hydroxyls was used as a drop-in replacement for the well-defined model polyether polyol with terminal hydroxyls, Poly-G® 76-120. Both polyols have comparable equivalent weight and concentrations of primary and secondary hydroxyls. The data showed that replacing Poly-G® 76-120 polyether polyol with the E-135 NOP did not significantly impact the foaming reactivity. Increasing the E-135 NOP concentration in the VE foams increased the average foam cell size while maintaining the open cell structure. Aging properties of the VE foams were mostly unaffected by the replacement of the Poly-G® 76-120 with the E-135 NOP. Furthermore, addition of E-135 had no impact on foam density; however, it increased the support factor of the viscoelastic foams. Differential scanning calorimetry, dynamic mechanical analyzer, and Fourier transform infrared spectroscopy analyses indicate less defined morphological separation of hard and soft segments in the viscoelastic foams with higher concentration of E-135 NOP. Overall, the results demonstrated the feasibility that natural oil polyols can be used in viscoelastic polyurethane foams to replace a significant portion of the polyether polyols with comparable equivalent weights and concentrations of primary and secondary hydroxyls. In future, the feasibility study of E-135 NOP as a drop-in replacement of combination polyether polyols in viscoelastic foams formulation will be conducted. Furthermore, the effect of palm olein-based natural oil polyol in high resilience foam will be evaluated.

Synthesis and characterization of polyurethanes made from copolymers of epoxidized natural oil and tetrahydrofuran.

Polyols were synthesized from epoxidized natural oils and tetrahydrofuran through ring opening copolymerization catalyzed by Lewis acid. The properties of these polyols depend on the type of natural oils as well as the reaction conditions (monomer concentration, catalyst amount, reaction temperature and reaction time). These polyols were evaluated as a raw material for making polyurethane (PU) in order to understand the structure-property relationship between a natural oil and PU made from it. The tensile test analysis shows that the incorporation of natural oil moiety into the PU polymer network improves the elasticity of these PU samples when compared to a benchmark PU sample. In addition, the PU samples made from palm oil and soybean oil based polyols exhibit better tensile strength than benchmark PU. These polyols samples are suitable for making elastomeric PU, where high flexibility (high elongation at break) of PU is a common requirement.

Palm Oleochemicals in Non-food Applications

Publisher Summary Palm oil is currently one of the most sustainable and important key base stocks for “Modern” or “Green” industry due to its high productivity rate as compared to other crops. The main feedstocks for oleochemicals are coconut oil and tallow, resulting in oleochemicals having fatty acid moiety of even numbered saturated carbon chain lengths. However, between 1985 and 1995, the significance of tallow was greatly reduced because of the BSE disease outbreak. Palm stearin has since replaced tallow in many applications and now becomes the major feed stock for oleochemicals. However, only about 10%–15% of palm oil is used for non-food application. Out of this, about 70% is used as surfactant either in food or non-food application. Palm oil is first converted into basic oleochemicals such as fatty acid, glycerol, methyl esters, fatty alcohols, and fatty amines. These basic oleochemicals will serve as building blocks for many other chemicals.

Preliminary investigation on the effects of primary airflow to coal particle distribution in coal-fired boilers

This paper presents an investigation on the effects of primary airflow to coal fineness in coal-fired boilers. In coal fired power plant, coal is pulverized in a pulverizer, and it is then transferred to boiler for combustion. Coal need to be ground to its desired size to obtain maximum combustion efficiency. Coarse coal particle size may lead to many performance problems such as formation of clinker. In this study, the effects of primary airflow to coal particles size and coal flow distribution were investigated by using isokinetic coal sampling and computational fluid dynamic (CFD) modelling. Four different primary airflows were tested and the effects to resulting coal fineness were recorded. Results show that the optimum coal fineness distribution is obtained at design primary airflow. Any reduction or increase of air flow rate results in undesirable coal fineness distribution.

Reaction Parameters for the Synthesis of N , N -Dimethyl Fatty Hydrazides from Oil

Hydrazide derivatives have been synthesized from methyl esters, hydrazones and vegetable oils. They are important due to their diverse applications in pharmaceutical products, detergents as well as in oil and gas industries. The chemical synthesis of fatty hydrazides is well-established; however, only a few publications described the synthesis of fatty hydrazide derivatives, particularly, when produced from refined, bleached and deodorized palm olein. Here, the synthesis and characterization of N,N-dimethyl fatty hydrazides are reported. The N,N-dimethyl fatty hydrazides was successfully synthesized from fatty hydrazides and dimethyl sulfate in the presence of potassium hydroxide with the molar ratio of 1:1:1, 6 hours reaction time and 80℃ reaction temperature in ethanol. The product yield and purity were 22% and 89%, respectively. The fatty hydrazides used were synthesized from refined, bleached and deodorized palm olein with hydrazine monohydrate at pH 12 by enzymatic route. Fourier transform infrared, gas chromatography and nuclear magnetic resonance (NMR) spectroscopy techniques were used to determine the chemical composition of N,N-dimethyl fatty hydrazides. Proton NMR confirmed the product obtained were N,N-dimethyl fatty hydrazides.

1,3-Bis{[(4-methyl-phen-yl)sulfon-yl]-oxy}propan-2-yl 4-methyl-benzene-sulfonate.

In the title sulfonate derivative, C24H26O9S3, all atoms apart from those of one of the 4-methylbenzenesulfonate residues lie approximately in a disc; the dihedral angles between the approximately orthogonal benzene ring and those in the plane are 74.53 (9) and 67.79 (11)°. In the crystal, molecules are consolidated into the three-dimensional architecture by C—H⋯O interactions. One of the 4-methylbenzenesulfonate residues is disordered over two almost parallel positions; the major component refined to a site-occupancy factor of 0.918 (2).