Conversion of starch from dry common beans (Phaseolus vulgaris L.) to ethanol

Dry common beans (Phaseolus vulgaris L.) were evaluated for potential conversion of starch to ethanol. Eight varieties of beans with average starch content of 46% (db) were assayed in a laboratory-scaled process based upon the commercial corn dry grind fermentation process. Ethanol yield was 0.43-0.51 g ethanol/g glucose (0.19-0.23 g ethanol/g beans). The average ethanol yield for the eight bean types was 92% of maximum theoretical yield, demonstrating that starch from beans could be efficiently converted to ethanol. Ethanol concentration obtained from 20% (w/w) solids loading was 3.5-4.4% (w/v). The residual fermentation solids contained, on a dry basis, 37.1-43.6% crude protein, 10.8-15.1% acid detergent fiber and 19.1-31.3% neutral detergent fiber.     

Process modeling of the Quick-germ/Quick-fiber process: Energy, water, and economics

A process simulation model was developed on the SuperPro Designer^® platform for a Quick-germ/Quick-fiber (QQ) modified dry grind ethanol fractionation facility. This paper compares energy and water demands, product quality, and economic performance between the QQ and the dry grind ethanol processes. Results showed that the QQ process reduces energy demand by 31.6% and water demand by 17.9%, produces more value-added coproducts, and improves the economic viability. The QQ process has a lower ethanol yield (0.405 vs. 0.414 L of ethanol per kg of corn) because of starch loss at the front-end separation. This model can be used to provide decision support for ethanol producers considering the new emerging technology.     

Effect of hammer mill retention screen size on fiber separation from corn flour using the Elusieve process

Corn is widely used as animal feed as well as for fuel ethanol production. Fiber present in corn is not digested well by non-ruminants such as chicken and swine. Also, this fiber does not participate in conversion of starch to ethanol. Fiber separation from ground corn flour using the Elusieve process, a combination of sieving and elutriation (air classification) results in high starch animal feed, and in increased ethanol productivity. The objective of this study was to understand the effect of retention screen size in the hammer mill on fiber separation from corn flour using the Elusieve process. Four different retention screen opening sizes were studied; 1.4 mm (3.5/64”), 2.0 mm (5/64”), 2.8 mm (7/64”) and 3.2 mm (8/64”). Ground corn flour was sieved into size fractions and the size fractions were subjected to air classification. As the retention screen size increased, fiber separation improved, and the difference in starch content between enhanced flour and original flour increased. The highest starch content of 64.1-65.2% was in the enhanced flour from Elusieve processing of corn flour obtained by using 3.2 mm (8/64”) retention screen in the hammer mill, while the starch content of the original corn flour was 62.5%. It is expected that at some threshold retention screen size, the fiber separation using the Elusieve process would be deteriorated. This threshold retention screen size was not reached in this study.     

Evaluation of a dry corn fractionation process for ethanol production with different hybrids

The effect of a specific dry fractionation process (FWS fractionation process) was evaluated on final ethanol and glucose concentration of 11 yellow dent corn hybrids in this dry grind corn process. In dry fractionation a dry de-germ de-bran process (similar to conventional corn dry milling) is used to separate germ and pericarp (bran) fiber prior to fermentation of the endosperm (grit) fraction. Fermentation results of grits produced from the FWS process were similar to whole corn samples and better than previously reported results on fermentation of grits from other dry fractionation processes. Further investigation showed that the amount of fat in FWS fractionated grits were 2–5 times more than grit samples from a commercial corn dry milling plant; suggesting reduced germ separation with more than 50% of germ not recovered and lost with the grits fraction. Final ethanol concentration for different corn hybrids varied from 12.7 to 13.8% (v/v) for whole corn and 13.4 to 14.7% (v/v) for grits samples. Dry fractionation (removal germ and bran) prior to dry grind processing, significantly affects the fermentation characteristics of corn hybrids. Corn dry fractionation can increase final ethanol concentration and recover germ and fiber as valuable coproducts.     

Oil extraction from coriander fruits by extrusion and comparison with solvent extraction processes

The aim of this work was to optimise a single-screw extruder dedicated to coriander production and to investigate the effects of screw configuration, nozzle diameter and nozzle/screw distance. On the other hand, the coriander fruit was extracted using soxhlet methods, the results were compared with mechanical screw press methods.Maximum yield was obtained with single screw extruder for a configuration allowing the strongest oil expression (nozzle/screw distance: 3 mm, nozzle diameter: 9 mm).Comparing with mechanical press, the maximum yield was obtained by the soxhlet extraction with 21.25%.The effect of the operating parameters on oil quality was not important. In all the experiments tested, the oil quality was very good. The acid value was below 1.8 mg of KOH/g of oil and iodine values were tolerable (44 mg of iodine/100 g of oil).Nine fatty acids were identified, with petroselinic acid accounting for 74-77% of the total fatty acids, followed by linoleic, oleic and palmitic acids, accounting for 12-13%, 4-6% and 3%, respectively, of the total fatty acids.β-Sitosterol was the major sterol in all oils with 28% of total sterols of all oils. The next major sterols in all oils were stigmasterol (24-27% of total sterols) and Δ⁷-stigmasterol (14-18% of total sterols).     

Oil separation from wet-milled corn germ dispersions by aqueous oil extraction and aqueous enzymatic oil extraction

The many recent dry-grind plants that convert corn to ethanol are a potential source of substantial amounts of corn oil, if an economical method of separating it can be developed. Oil separation from corn germ by aqueous extraction (AE) was studied. Batches of 5–20% germ in a buffer solution were preheated in a pressure cooker, ground in a blender or colloid mill, churned in an incubator/shaker and centrifuged to separate a free oil fraction. The highest oil yields were obtained when the germ mass fraction was between 0.1 and 0.16. Addition of an enzyme solution to the ground germ suspension prior to churning, aqueous enzymatic extraction (AEE) gave an oil yield twice as high as the AE yield, carried out using similar conditions. Both types of extraction produced the most oil after a 122 °C cook followed by churning at 160 rpm and 70 °C. Oil yield increased linearly with dispersion loading, from 0.5 up to 1.0 g/cm² based on beaker cross-section (0.09–0.12 germ mass fraction). Over a several month period the germ used for the extractions became more difficult to extract, despite storage at 4 °C.     

Modification of aqueous enzymatic oil extraction to increase the yield of corn oil from dry fractionated corn germ

In previous aqueous enzymatic oil extraction (AEOE) experiments we reported a best free oil yield of 49% of the hexane extracted yield of dry fractionated corn germ. In the current experiments, a dispersion of 10% cooked, dry-fractionated germ in water was treated with α-amylase, glucoamylase and a cellulase complex. Free oil was collected by centrifuging a foam fraction of the dispersion. Several dispersion treatments were tried to evaluate their release of free oil and effect on the production of foam. The foam contained up to 8% free oil (dispersed from germ containing 26% oil) and fines oil (not centrifugally separable), protein and germ particles. Treatment with α-amylase and glucoamylase prior to treatment with the commercial cellulase used in previous AEOE studies increased the free oil yields about 25-61% of the hexane-extractable yield. A preliminary cost analysis indicates that oil separation with the amylase enhanced AEOE appears to be preferable to AEOE alone and profitable if crude corn oil cost exceeds $1.1/kg ($0.50/lb).     

Flaking as a corn preparation technique for dry-grind ethanol production using raw starch hydrolysis

A 2³ full-factorial study was designed to study the effect of corn preparation methods (flaking and grinding) on dry-grind ethanol performance using raw starch hydrolysis (RSH) process. Moisture content (15, 22%), flaker roller gapsetting (0.508 mm, 1.016 mm), and grinding were studied. Fifteen hundred g of corn samples were cracked, roller pressed, and were either ground further or retained, along with control ground corn. A bimodal size distribution was observed for ground corn, regardless of flaking. Moisture at 22% resulted in bigger-sized flakes with d₅₀ between ∼1.3 and 1.8 mm, compared to ∼138–169 μm for ground corn. Not all ground corn resulted in higher ethanol concentration in fermentation beer; the ethanol levels in beer did not reflect the starch hydrolysis trend that favored ground corn. In a related study, the beer ethanol concentration did not show a clear trend with rollermill gapsetting while fermenting the flakes produced at 0.203, 0.305, 0.406, and 0.508 mm gapsettings. Generally, flakes from corn at 22% moisture resulted in higher ethanol content in beer. Rollermill flaking was found comparable to hammermill grinding for dry-grind corn ethanol via raw starch hydrolysis and yeast fermentation.     

Lavender and hyssop productivity, oil content, and bioactivity as a function of harvest time and drying

Field and laboratory experiments were conducted to evaluate the productivity and essential oil composition of lavender (Lavandula angustifolia Mill.) and hyssop (Hyssopus officinalis L.) as functions of year, harvest time, and drying. Lavender essential oil content ranged from 0.71 to 1.3% (overall average of 0.89%) and hyssop oil content ranged from 0.13 to 0.26% (overall average of 0.19%). Lavender and hyssop essential oil yields increased with time. Hyssop oil yields varied from 7.3 kg ha⁻¹ to 19.6 kg ha⁻¹, and lavender oil yields varied from 7.8 kg ha⁻¹ to 55.5 kg ha⁻¹. The major constituents of lavender oil were linalool (23.3-43.4%) and linalylacetate (20.2-39.6%), while the major constituents of hyssop oil were pinocamphene + isopinocamphene (57-75%) and β-pinene (5-15%). Lavender oil extracted from dry material had higher concentrations of linalyl acetate and caryophyllene but lower concentrations of myrcene than the oil from the fresh material. Delayed harvest of hyssop increased the concentrations of β-pinene, myrcene, and limonene + cineole but reduced pinocamphone + isopinocamphone. The chemical composition of the lavender and hyssop oil produced in Mississippi was similar to commercial oils from Bulgaria, Canada, France, and US. Lavender and hyssop can be established as essential oil crops in areas of the southeastern United States. Lavender and hyssop essential oils did not show significant antimicrobial, antileishmanial, antimalarial activity, and did not alter ruminal fermentation. However, commercial oil from L. latifolia reduced methane production in an in vitro digestibility study. The antioxidant activity of hyssop essential oil was 2039 μmol of TE L⁻¹, whereas the antioxidant activity of lavender essential oil was 328 μmol of TE L⁻¹.     

Characteristics, composition and thermal stability of Acacia senegal (L.) Willd. seed oil

The chemical composition, main physicochemical properties and thermal stability of oil extracted from Acacia senegal seeds were evaluated. The oil, moisture and the ash contents of the seeds were 9.80%, 6.92% and 3.82%, respectively. Physicochemical properties of the oil were iodine value, 106.56 g/100 g of oil; saponification value, 190.23 mg KOH/g of oil; refractive index (25 °C), 1.471; unsaponifiable matter, 0.93%; acidity, 6.41% and peroxide value, 5.43 meq. O₂/kg of oil. The main fatty acids in the oil were oleic acid (43.62%) followed by linoleic acid (30.66%) and palmitic acid (11.04%). The triacylglycerols (TAGs) with equivalent carbon number ECN 44 (34.90%) were dominant, followed by TAGs ECN 46 (28.19%), TAGs ECN 42 (16.48%) and TAGs ECN 48 (11.23%). The thermal stability analysed in a normal oxidizing atmosphere showed that the oil decomposition began at 268.6 °C and ended at 618.5 °C, with two stages of decomposition at 401.5 °C and 576.3 °C. According to these results, A. senegal seed oil has physicochemical properties, fatty acids composition and thermal characteristics that may become interesting for specific applications in several segments of food and non-food industries.     

Comparative seasonal variation and chemical composition of essential oils from the leaves and stems of Schefflera heptaphylla using microwave-assisted and conventional hydrodistillation

Two different isolation techniques, microwave-assisted hydrodistillation (MAHD) and conventional hydrodistillation (HD), were used to extract the volatile constituents from the leaves and stems of Schefflera heptaphylla (L.) Frodin harvested during four different seasons, which were subsequently analyzed via gas chromatography with flame ionization detection and gas chromatography with mass spectrometry. MAHD is more advantageous than HD in terms of energy savings and extraction time (60 min vs. 180 min for MAHD vs. HD). Large variations in the composition among the different oils were observed. The seasonal changes in the percentages of the main constituents of the oils were irregular; this affected the quantity and composition of the oil. Oil yield was affected by the method of extraction and seasonal changes. It ranged from 0.11% to 0.27%, with the maximum amount of oil extracted from the leaves using MAHD in winter and the minimum from the stem oil extraction using HD in spring. The essential oil content varied significantly with the season. Sesquiterpene hydrocarbons constituted the major portion of the essential oils. Sesquiterpene hydrocarbons were highest in the leaf oil extraction by HD during winter (88.6%) and lowest in the stem oil extraction by HD during spring (56.3%). Microwave irradiation did not adversely affect the composition of the essential oils. MAHD, indeed, is a modern, green, and fast technology.     

Improving the barrier and mechanical properties of corn starch-based edible films: Effect of citric acid and carboxymethyl cellulose

The films produced from pure starch are brittle and difficult to handle. Chemical modifications (e.g. cross-linking) and using a second biopolymer in the starch based composite have been studied as strategies to produce low water sensitive and relatively high strength starch based materials. A series of corn starch films with varying concentrations (0-20%, W/W) of citric acid (CA) and carboxymethyl cellulose (CMC) were produced by casting method. The effects of CA and CMC on the water vapor permeability (WVP), moisture absorption, solubility and tensile properties were investigated. The water vapor barrier property and the ultimate tensile strength (UTS) were improved significantly (p < 0.05) as the CA percentage increased from 0 to 10% (W/W). At the level of 15% (W/W) CMC, the starch films showed the lowest WVP values (2.34 × 10⁻⁷ g Pa⁻¹ h⁻¹ m⁻¹) and UTS increased from 6.57 MPa for the film without CMC to 16.11 MPa for that containing 20% CMC.     

Composite materials of thermoplastic starch and fibers from the ethanol-water fractionation of bagasse

The aim of this study was to evaluate the potential of the fibrous material obtained from ethanol-water fractionation of bagasse as reinforcement of thermoplastic starches in order to improve their mechanical properties. The composites were elaborated using matrices of corn and cassava starches plasticized with 30 wt% glycerin. The mixtures (0, 5, 10 and 15 wt% bagasse fiber) were elaborated in a rheometer at 150 °C. The mixtures obtained were pressed on a hot plate press at 155 °C. The test specimens were obtained according to ASTM D638. Tensile tests, moisture absorption tests for 24 days (20-23 °C and 53% RH, ASTM E104), and dynamic-mechanical analyses (DMA) in tensile mode were carried out. Images by scanning electron microscopy (SEM) and X-ray diffraction were obtained. Fibers (10 wt% bagasse fiber) increased tensile strength by 44% and 47% compared to corn and cassava starches, respectively. The reinforcement (15 wt% bagasse fiber) increased more than fourfold the elastic modulus on starch matrices. The storage modulus at 30 °C (E_30 °C′) increased as the bagasse fiber content increased, following the trend of tensile elastic modulus. The results indicate that these fibers have potential applications in the development of biodegradable composite materials.     

Increasing oxidative stability in corn oils through extraction of γ-oryzanol from heat treated rice bran

Corn oil was mixed with heated rice bran with different extraction periods and ratios of rice bran to corn oil to extract γ-oryzanol from rice bran. Selected corn oils based on the content of γ-oryzanol were heated at 180 °C for 100 min or 60 °C for 16 days, and oxidative stability was evaluated. Corn oils recovered from the mixture of rice bran showed higher oxidative stability at both 60 and 180 °C treatment compared to control corn oils. At 180 °C, corn oils of a 1:5 ratio of rice bran to corn oil (w/w) showed higher oxidative stability than did those of 1:3 and 1:7 (w/w), whereas at 60 °C, corn oils of 1:7 (w/w) showed higher oxidative stability than did others. γ-Oryzanol can be extracted through a corn-oil mixture at 80–90 mg/100 g oil, which is about 4.0% recovery of 2244 mg/100 g crude rice-bran oil. Oxidative stability of corn oils increased significantly, partly because of the extraction of γ-oryzanol under current experimental conditions.     

Quality characteristics of Canarium schweinfurthii Engl. oil

The oil content and quality characteristics of Canarium schweinfurthii Engl. oil are described. The oils were extracted from the mesocarp and endocarp using hexane to remove the free flowing lipid (FFL) and successive extraction with CHCl₃-MeOH followed by water saturated butanol to remove bound lipid (BL). On a dry matter basis, the mesocarp contained 68.3% FFL and 13.7% BL while the endocarp contained 67.0% FFL and 13.0% BL. The quality characteristics of the mesocarp oil extracts were 151.9–195.3 mg KOH/g fat saponification value (SV), 20–40 mEq peroxide/kg fat peroxide value (PV), 71.1–94.9 g iodine/100 g fat iodine value (IV) and 1.33–8.30 mg KOH acid value (AV). Characteristics for the endocarp oil extracts were 95.4–184.3 mg KOH/g fat SV, 4.0–8.0 mEq peroxide/kg fat PV, 100.1–118.3 g iodine/100 g fat IV, and AV of 0.48–8.70 mg KOH. The fatty acid composition of the first hexane extracts indicated that the oils were primarily C16 and C18s. The mesocarp contained 31.7% hexadecanoic acid, 30.0% 9-octadecenoic acid, 30.1% 6,9-octadecadienoic acid and 8.2% 9,12,15-octadecatrienoic acid, while the endocarp, contained 31.2% hexadecanoic acid, 28.9% 9-octadecenoic acid and 31.3% 6,9-octadecadienoic acid.     

Formation,characterization, and glucose response in mice to rice starch with low digestibility produced by citric acid treatment

The optimum conditions for producing rice starch enriched in slowly digestible and resistant fractions by citric acid treatment determined by a response surface methodology (RSM) model equation, were: reaction temperature, 128.4 °C; reaction time, 13.8 h; and citric acid, 2.62 mmol/20 g starch. The slowly digestible and resistant starch fractions of the optimally acid-treated rice starch totalled 54.1%, which was 28.1% higher than the control. The slowly digestible and resistant fractions of the acid-treated rice starch did not differ significantly after heat treatment, whereas those of raw rice starch decreased by 49.6–63.8%, depending on the type of heat treatment (cooking at 100 °C or autoclaving). The slowly digestible fraction of the acid-treated starch increased by 8.9–14.2%. After autoclaving, the glucose response of the acid-treated starch was lower than untreated starch, but similar to that of Novelose 330. After heat treatment, the rate of blood glucose decrease was slower for the acid-treated starch than for Novelose 330. Compared to raw rice starch, the acid-treated starch exhibited increases in apparent amylose content, blue value, dextrose equivalent, cold-water solubility and transmittance, and decreases in wavelength of maximum absorbance, viscosity, and gel-forming ability.     

Effect of ageing on quality of jojoba oil from Indian locations

Jojoba oil is a source of specialty chemicals and its uses for industrial application are gaining in adaptability and importance. For prolong use of jojoba oil, the details of its storage behaviour are required. This information is scarce for the products obtained from Indian locations. In this study, the ageing effect on the quality of oils was studied for oils from five locations of Rajasthan (India). The oils were extracted/expelled from the seeds that contained 2.5–3.9 wt.% moisture and 42–50 wt.% oil.Physico-chemical properties were determined by standard analytical test methods. Effect of storage time on quality of solvent extracted oil samples with respect to acid value, iodine value, saponification value and peroxide value were determined. The samples were stored for 18 months in the laboratory under climatic condition prevailing in Dehradun (India) during study period. The analysis of samples was done at an interval of 3 months. The properties of jojoba oils compare well with the International Jojoba Expert Council (IJEC) specifications. During storage, acid values, iodine values and peroxide values of the oil increase with time while saponification values remain almost unchanged.     

Characteristics, chemical composition and utilisation of Albizia julibrissin seed oil

The physicochemical characteristics, fatty acid and triacylglycerol compositions, DSC profile and UV/vis spectrum of oil extracted from Albizia julibrissin seeds were determined in this study. The oil content and the moisture of the seeds were 10.50% and 1.56%. The free fatty acid, the peroxide value, the p-anisidine value, the saponification value, the iodine value were 2.54%, 6.61 mequiv. O₂/kg of oil, 1.98, 190.63 (mg KOH/g) and 111.33 (g/100 g of oil), respectively. The specific extinction coefficients K₂₃₂, K₂₆₈ were 7.55 and 0.96, respectively. Linoleic acid (C_18:2, 58.58%), palmitic acid (C₁₆, 13.86%) and oleic acid (C_18:1, 10.47%) were the dominant fatty acids in the A. julibrissin seed oil. LLL (36.87%), OLL (21.62%), PLL (16.69%) and PLO + SLL (8.59%) were the abundant triacylglycerol representing > 83% of the seed oil (L: linoleic, O: oleic, P: palmitic, S: stearic). The DSC melting curves reveal that: melting point = −14.70° C and melting enthalpy = 54.34 J/g. A. julibrissin seed oil showed some absorbance in the UV-B and UV-C ranges. The results of the present analytical study show that A. julibrissin is a promising oilseed crop, which can be used for making soap, hair shampoo and UV protectors. Furthermore, the high level of unsaturated fatty acids makes it desirable in terms of nutrition.     

The addition of corn fiber gum improves the long-term stability and retrogradation properties of corn starch

This study was designed to test the hypothesis that the stability and physical properties of starch gels could be improved by adding small amounts of corn fiber gum (CFG). In the differential scanning calorimeter measurement, the enthalpy of retrogradation was 7.30 J/g for starch without CFG and 4.30 J/g for starch composite gel with 1.0% CFG. The addition of 1.0% CFG to starch significantly (p < 0.05) decreased the degree of retrogradation during the long-term storage from 61.6% to 36.5%. The addition of CFG retarded the syneresis of the starch system from 17.97% and 34.93%–6.15% and 26.57% after storage for 7 and 14 days respectively. The crystallization peak of starch containing 0.5–1.0% CFG was quite diminished. When compared with the starch gel alone, the addition of CFG significantly lowered the hardness of the composite starch gel from 60.92 to 45.81 N after 14 days storage. The starch gel without CFG showed the lowest rapidly digestible starch content and the highest resistant starch content in comparison to starch/CFG composite gels after 7 and 14 days storage. Over all, the addition of CFG considerably inhibits the retrogradation of corn starch gels during long-term storage.