Production of macerating enzymes of mandarin orange peel by fungal cultures

Summary Thirty-nine fungal cultures belonging to the genera of Aspergillus, Podospora, Sordaria, Cbaetomium, Iodophanus, Scleotinia, Coniella, Pellicularia and others, were examined for the production of enzymes which macerate the mandarin orange peel using a wheat bran as substrate. An isolated strain of Aspergillus niger was an excellent producer of macerating enzymes compared to other organisms tested. The peel of the mandarin orange could be macerated by the crude enzymes produced by isolated A. niger. The maceration of 1 g of peel/24 h yielded 0.57 g of reducing sugars. Expressed differently, 83% of solid peel materials were released from the peel into the water/24 h under the following conditions: a peel concentration of 8 g peel/l, a crude enzyme concentration of 1 g protein/l, a temperature of 40°C, a pH of 5, a 24 h incubation time and 120 rpm reciprocal shaking. The test of the macerating activity of commercially available hydrolases on the orange peel showed that the two samples of pectinase originating from A. niger had about the same activity as isolated A. niger whereas the two samples of cellulase originating from Trichoderma viride had remarkably lower activities than A. niger.     

Bioflavour production from orange peel hydrolysate using immobilized Saccharomyces cerevisiae

The rising trend of bioflavour synthesis by microorganisms is hindered by the high manufacturing costs, partially attributed to the cost of the starting material. To overcome this limitation, in the present study, dilute-acid hydrolysate of orange peel was employed as a low-cost, rich in fermentable sugars substrate for the production of flavour-active compounds by Saccharomyces cerevisiae. With this purpose, the use of immobilized cell technology to protect cells against the various inhibitory compounds present in the hydrolysate was evaluated with regard to yeast viability, carbon and nitrogen consumption and cell ability to produce flavour active compounds. For cell immobilization the encapsulation in Ca alginate beads was used. The results were compared with those obtained using free-cell system. Based on the data obtained immobilized cells showed better growth performance and increased ability for de novo synthesis of volatile esters of "fruity" aroma (phenylethyl acetate, ethyl hexanoate, octanoate, decanoate and dodecanoate) than those of free cells. The potential for in situ production of new formulations containing flavour-active compounds derive from yeast cells and also from essential oil of orange peel (limonene, α-terpineol) was demonstrated by the fact that bioflavour mixture was found to accumulate within the beads. Furthermore, the ability of the immobilized yeast to perform efficiently repeated batch fermentations of orange peel hydrolysate for bioflavour production was successfully maintained after six consecutive cycles of a total period of 240 h.     

Single cell protein production from rayon pulp will waste by Paecilomyces variotii

Prehydrolysate liquor obtained from a rayon pulp mill was used as a substrate to produce single cell protein (SCP). Ten different strains of Paecilomyces variotii were locally isolated and screened for the production of SCP from following optimization creteria: rates and yield of biomass production, rates of substrate utilization, maximum specific growth rates and total biomass formation. The optimal SCP producer was found to be P. variotii TCRDC-M5 which gave a μmax of 0.11/h and a biomass yield of 96% of the theoretical, with 95% substrate utilization and 25 g dry wt. biomass/l in the Lab. fermentor. This resulted in a 70% reduction in the BOD of the prehydrolysate.     

Biorefinery of waste orange peel

Up to comparatively recently orange peel and the associated residual remnants of membranes resulting from juice extraction represented a significant disposal problem, especially in those regions where orange cultivation is a major industry. However, recent research has demonstrated that orange peel waste represents a potentially valuable resource that can be developed into high value products. These developments are critically reviewed in this article. This includes a summary of the chemical composition of the substrate and an assessment of the range of applications in which the peel is deployed. Utilization as a substrate to produce animal feed, fertilizer, essential oils, pectin, ethanol, methane, industrial enzymes, and single cell protein is discussed. The applications described together with those that will no doubt be developed in the future, represent great opportunities to harness the economical benefit of this agro-industrial waste and to develop even more efficient and sustainable systems. A scheme of integrated utilization of orange peel in a biorefinery approach is discussed together with some prediction of further necessary research.     

Cellulose extraction from orange peel using sulfite digestion reagents

Orange peel (OP) was used as raw material for cellulose extraction. Two different pulping reagents were used, sodium sulfite and sodium metabisulfite. The effect of the main process parameters, sulfite agent dosage and reaction duration, on cellulose yield was investigated. A central composite rotatable design involving two variables at five levels and response surface methodology were used for the optimization of cellulose recovery. Other two invariable parameters were reaction temperature and hydromodulus. The optimum yields, referred to the weight of double extracted OP, were 40.4% and 45.2% for sodium sulfite and sodium metabisulfite digestions, respectively. The crude celluloses were bleached with hypochlorite and oxygen. The physicochemical characterization data of these cellulose materials indicate good levels of purity, low crystallinities, good whitenesses, good water retention and moderate molecular weights. According to these specific properties the recovered celluloses could be used as fillers, water absorbents, or as raw materials for cellulose derivatives.     

Degradation of mikan (Japanese mandarin orange) peel by a novel Penicillium species with cellulolytic and pectinolytic activity

AIMS: The mikan, or Japanese mandarin orange, is a popular fruit in Japan, but its peel is one of the major agricultural wastes. The aims of this study were to screen, isolate, and characterize a mikan peel-degrading microbe. METHODS AND RESULTS: Several samples including activated sludge, sediment, compost and spoiled mikan peel were collected and cultured in a minimal salt medium containing mikan peel as the sole carbon source. Degradation activity was found in a culture of the spoiled mikan peel, and a fungal strain, designated OP1, with both cellulolytic and pectinolytic activity was isolated. No toxic metabolites, such as mycotoxins, were found in OP1 cultures, as evaluated by gas chromatography/mass spectrometry. A phylogenetic analysis strongly suggested that OP1 is a novel species of the genus Penicillium. CONCLUSIONS: Results suggest that Penicillium sp. OP1 plays an important role in aerobic microbial degradation of cellulose/pectin-rich biomasses in soil ecology, and further imply that this strain may be useful for both simultaneous cellulase/pectinase production and reduction of agricultural waste. SIGNIFICANCE AND IMPACT OF THE STUDY: The present results advance our understanding of microbial degradation of cellulose/pectin-rich biomasses in the natural environment, and offer a new tool for reduction of agricultural waste, which is important for sustaining circulatory societies.     

Production of biomass from untreated orange peel by Fusarium avenaceum

Summary The growth behaviour of Fusarium avenaceum (Sect. Roseum Wr.) in slurry fermentation systems using untreated orange peel as substrate was studied in a laboratory-fermenter scale to reproduce the results obtained in a shakenflask fermenter. The eventual effect of impeller speed on mechanical disruption of mycelial hyphae was then assessed by determining mycelial growth, total reducing sugars consumption, TOC reduction, carbon dioxide evolution and oxygen absorption rates. In particular, the main biomass yield coefficient, as well as the apparent specific growth rate, appeared to be independent of the impeller speed, at least within the experimental range of 450 and 900 min^–1 (equivalent to peripheral impeller speeds of 3.8–7.5 m sec^–1.     

Succinic acid production from orange peel and wheat straw by batch fermentations of Fibrobacter succinogenes S85

Succinic acid is a platform molecule that has recently generated considerable interests. Production of succinate from waste orange peel and wheat straw by consolidated bioprocessing that combines cellulose hydrolysis and sugar fermentation, using a cellulolytic bacterium, Fibrobacter succinogenes S85, was studied. Orange peel contains d-limonene, which is a well-known antibacterial agent. Its effects on batch cultures of F. succinogenes S85 were examined. The minimal concentrations of limonene found to inhibit succinate and acetate generation and bacterial growth were 0.01%, 0.1%, and 0.06% (v/v), respectively. Both pre-treated orange peel by steam distillation to remove d-limonene and intact wheat straw were used as feedstocks. Increasing the substrate concentrations of both feedstocks, from 5 to 60 g/L, elevated succinate concentration and productivity but lowered the yield. In addition, pre-treated orange peel generated greater succinate productivities than wheat straw but had similar resultant titres. The greatest succinate titres were 1.9 and 2.0 g/L for pre-treated orange peel and wheat straw, respectively. This work demonstrated that agricultural waste such as wheat straw and orange peel can be biotransformed to succinic acid by a one-step consolidated bioprocessing. Measures to increase fermentation efficiency are also discussed.     

Single cell protein production from bagasse pith pretreated with sodium hydroxide at room temperature

Summary Previous publications have revealed that a pretreatment of lignocellulosic wastes is necessary if they are to be employed as the hydrocarbon source of single cell protein production. A hot alkaline treatment is the most common.We have treated sugar cane bagasse pith with 1% NaOH solution at room temperature, at a NaOH/pith ratio of 10%. Different contact times were used in the experiments. The shortest contact period required for maximum protein production was 24 h at 25° C. A mixed culture of Cellulomonas sp. and Bacillus subtilis was used in the experiments. The values obtained for hemicellulose and cellulose in the treated pith did not differ greatly from those of untreated pith, in contrast the amount of lignin was 33% lower in the treated pith. The effect of reutilization of the alkaline liquor used for the pretreatment of pith upon protein production was also investigated. With four recyclings, there was a NaOH saving of 34.4 kg per 100 kg produced protein as compared to when the liquor was only used once.The quality of the resulting effluents, as measured by the chemical oxygen demand (COD), proved to be very similar for both types of treatment.     

Single cell protein from pineapple cannery effluent

Candida utilis was grown on pineapple cannery effluent as the sole carbon and energy source. These effluents are rich in microbially utilizable nutrients. The principal sugars in the effluent were glucose, fructose and sucrose, and when supplemented with diammonium hydrogen phosphate to prevent nitrogen limitation they supported good growth. The maximum specific growth rate (m=0.46h–1) and cell yield coefficient (Yc/s=0.30) were obtained with 23.2 g carbohydrate/l in the growth medium. The values of m and Yc/s varied with carbohydrate concentration: higher values of m and Yc/s were obtained with lower concentrations of carbohydrate, suggesting that a chemostat would be more suitable for single cell protein production. Freeze-dried yeast contained 55.3, 51.2, 1.45, 6.4 and 27.4% of crude protein, true protein, DNA, RNA and carbohydrate respectively. The yeast had a balanced amino acid profile, except for sulphur-containing amino acids. A 90–95% reduction in the chemical oxygen demand of the effluent was achieved during this process which suggests that yeast may be effectively used to treat this waste.     

Single cell oil production from rice hulls hydrolysate

Rice hull hydrolysate was used as feedstock for microbial lipids production using the oleaginous fungus Mortierella isabellina. Kinetic experiments were conducted in C/N ratios 35, 44 and 57 and the oil accumulation into fungal biomass was 36%, 51.2% and 64.3%, respectively. A detailed mathematical model was used in order to describe the lipid accumulation process. This model was able to predict reducing sugar and nitrogen consumption, fat-free biomass synthesis and lipid accumulation. Neutral lipids constitute the predominant lipid fraction, while the major fatty acids were oleic, palmitic and linoleic acid. Fatty acids of long aliphatic chain were not detected, thus the microbial oil produced is a promising feedstock for biodiesel production.     

β-Citraurin epoxide,a new carotenoid from valencia orange peel

A new minor carotenoid, β-citraurin epoxide (3-hydroxy-5,6-epoxy-5,6-dihydro-8′-apo-β-caroten-8′-al) and several isomers of violaxanthin (5,6,5′,6′-diepoxy-5,6,5′,6′-tetrahydro-β,β-caroten-3,3′-diol) have been identified in Valencia orange peel. The previously reported occurrence of apo-10′-violaxanthal (3-hydroxy- 5,6-epoxy-5,6-dihydro-10′-apo-β-caroten-10′-al) and apo-12′-violaxanthal (3-hydroxy-5,6-epoxy-5,6-dihydro- 12′-apo-β-caroten-12′-al) has been confirmed, and their syntheses are described. The quantitative determination of the carotenoids has also been performed.     

Dynamics of orange peel fermentation during ensilage

The dynamics of fermentation during ensilage were studied on orange peel (variety Shamouti) ensiled in 50 plastic containers, 10 kg in each, with an outlet for seepage. At predetermined intervals the containers were weighed and samples were taken from three of them for chemical and microbial analysis. Fermentation losses amounted to up to ca one-third of the fresh peel dry matter (DM) content. Most losses occurred within 10 d of commencement of fermentation, and were attributable to gas release. The major fermentation products were ethanol, lactic and acetic acids (16, 3 and 3% of DM, respectively). The dominant microbial populations were lactobacilli and yeasts. Tests are in progress to inhibit the yeasts and thereby reduce fermentation losses.     

Utilization of agro-industrial orange peel and sugar beet pulp wastes for fungal endo- polygalacturonase production

The pectinase enzymes are involved in several industrial applications, and industrial waste is one of the largest environmental pollutants, so this study aims to Endo-polygalacturonase (endo-PG) producing using Aspergillus niger AUMC 4156, Penicillium oxalicum AUMC 4153 and P. variotii AUMC 4149 by using some agro-industrial wastes (dried orange peel and sugar beet pulp) as a sole raw carbon source for degradation these waste in the process of urban wastes disposal. The fermentation process was carried out as a submerged culture technique under both shaken and static culture conditions. A. niger AUMC 4156 was the most promising producer of endo-PG under static conditions while P. oxalicum AUMC 4153 was the highest producer of endo-PG under shaken conditions. Sugar beet pulp proved to be the most preferable to orange peel as the only source of carbon in both shaken and static cultures. The medium that encompassing orange peel as a single carbon source afforded the highest protein content with all tested fungal strains in stirred and static cultures in comparison with sugar beet pulp. The highest activity of endo-polygalacuronase that produced using A. niger AUMC 4156 and P. oxalicum AUMC 4153 was achieved by using sugar beet pulp at 3% concentration under static cultures, meanwhile maximal enzyme activity produced by both fungal strains required 2% sugar beet pulp under shaken cultures. Sugar beet pulp showed promised potential as a good inducer for endo-polygalacturoase production, and enzymes production depended on fungal strains, culture medium, and submerged fermentation conditions.     

Gelation of sugarbeet and citrus pectins using enzymes extracted from orange peel

Sugarbeet pectin is shown to form gels in the presence of calcium using an enzyme preparation extracted from orange peel. The gels were transparent and exhibited no syneresis. The mechanism of gelation is chain association arising from both lowered pectin solubility and from formation of a limited network of calcium-linked junction zones. The gelation reaction involves limited pectin demethoxylation, the release of acetate presumably from C-2 or C-3 of galacturonyl residues, and a decrease in pH. The enzymes responsible are pectinesterase (EC 3.1.1.11) and pectin acetylesterase. We suggest that the latter is a novel activity associated with triacetin acetylesterase (EC 3.1.1.6). The gels are compared to citrus pectin gels made in the same way.     

Citric acid production by Aspergillus niger grown on orange peel medium fortified with cane molasses

Citric acid production (CAP) by Aspergillus niger was obtained following culture on an orange peel medium (OPM) fortified with cane molasses. The key physico-chemical parameters influencing CAP, such as bed loading, moisture levels, volume and age of inoculum, initial pH, incubation temperature and duration, agitation rate, sugar concentration, addition of nitrogen and phosphorus sources, treatment of molasses and the addition of different low levels of alcohols, were assessed. The suitability of molasses to increase the concentration of sugar in the fermentation medium without previous treatments with EDTA or ferro-cyanide was indicated. Maximum amounts of CA (640 g/kg orange peel) were obtained after 72 h of incubation on an OPM moisturized to 65 %?w/v, with bed loading of 20 %, an initial pH of 5, a temperature of 30 °C, an agitation rate of 250 rpm, with fortification of the medium with molasses at a final sugar concentration of 14 % in the presence of 3.5 % methanol.     

Modelling of cyclic fed-batch plus batch polygalacturonase production by Aureobasidium pullulans on raw orange peel

Summary Cyclic fed-batch plus batch polygalacturonase production by Aureobasidium pullulans in slurry fermentation systems using raw orange peel as substrate was studied in a 3-dm³ stirred fermentor by setting the main operating variables (T=297°K; pH₀=3.2; OP₀=3% w/v; n=700 rpm) to optimal values determined previously. In this way, it was possible to stabilize enzyme excretion at 130–140 VU cm^–3. The time course of this fermentation process in terms of cell growth, substrate consumption and enzyme synthesis was reconstructed with a mean standard error less than 10%, by applying an unstructured model set up in a batch run and further refined in a series of cyclic fed-batch plus batch operations. In particular, the enzyme formation rate was related to the effect of reducing sugars as inhibitors at higher concentrations and as activators at lower levels by using an exponential equation. Moreover, the consumption rate of reducing sugars was found to be linearly related to the cell growth rate, its specific date being of pseudo-first order with respect to the reducing sugar concentration.Offprint requests to: M. Moresi     

Galactolipids and phospholipids of orange peel and juice chromoplasts

Chromoplasts from yellow orange (Citrus sinensis) fruit peel contain monogalactosyl diglycerides (MGDG), digalactosyl diglycerides (DGDG) and phosphatidyl glycerol (PG) in amounts similar to those found in chloroplasts from green fruit peel. Juice chromoplasts contain relatively little MGDG and no DGDG with high levels of phosphatidyl choline and phosphatidyl ethanolamine but no PG.     

Hydrolysis of orange peel with pectinase and cellulase enzymes

Summary Hydrolysis of polysaccharides in comminuted orange peel by commercial cellulase and pectinase enzymes has been investigated. High levels of conversion to monomeric sugars were observed after treatment with pectinase enzyme, but cellulase enzyme achieved only limited solubilization. The combination of cellulase and pectinase enzymes appears to be a most efficient system for enzymatic hydrolysis of polysaccharides in orange peel.     

Optimization of isolation of cellulose from orange peel using sodium hydroxide and chelating agents

Response surface methodology was used to optimize cellulose recovery from orange peel using sodium hydroxide (NaOH) as isolation reagent, and to minimize its ash content using ethylenediaminetetraacetic acid (EDTA) as chelating agent. The independent variables were NaOH charge, EDTA charge and cooking time. Other two constant parameters were cooking temperature (98 °C) and liquid-to-solid ratio (7.5). The dependent variables were cellulose yield and ash content. A second-order polynomial model was used for plotting response surfaces and for determining optimum cooking conditions. The analysis of coefficient values for independent variables in the regression equation showed that NaOH and EDTA charges were major factors influencing the cellulose yield and ash content, respectively. Optimum conditions were defined by: NaOH charge 38.2%, EDTA charge 9.56%, and cooking time 317 min. The predicted cellulose yield was 24.06% and ash content 0.69%. A good agreement between the experimental values and the predicted was observed.