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Article

Characterization of Orange Peel Waste and Valorization to Obtain Reducing Sugars

by
José R. Ayala
*,
Gisela Montero
,
Marcos A. Coronado
,
Conrado García
,
Mario A. Curiel-Alvarez
,
José A. León
,
Carlos A. Sagaste
and
Daniela G. Montes
Instituto de Ingeniería, Universidad Autónoma de Baja California, Blvd. Benito Juárez y Calle de la Normal S/N, Col. Insurgentes Este, Mexicali 21280, Baja California, Mexico
*
Author to whom correspondence should be addressed.
Molecules 2021, 26(5), 1348; https://doi.org/10.3390/molecules26051348
Submission received: 3 February 2021 / Revised: 20 February 2021 / Accepted: 26 February 2021 / Published: 3 March 2021
(This article belongs to the Special Issue Food-Waste as a Sustainable Source of Chemicals and Materials)
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Versions Notes

Abstract

Annually, millions of tons of foods are generated with the purpose to feed the growing world population. One particular eatable is orange, the production of which in 2018 was 75.54 Mt. One way to valorize the orange residue is to produce bioethanol by fermenting the reducing sugars generated from orange peel. Hence, the objective of the present work was to determine the experimental conditions to obtain the maximum yield of reducing sugars from orange peel using a diluted acid hydrolysis process. A proximate and chemical analysis of the orange peel were conducted. For the hydrolysis, two factorial designs were prepared to measure the glucose and fructose concentration with the 3,5-DNS acid method and UV-Visible spectroscopy. The factors were acid concentration, temperature and hydrolysis time. After the hydrolysis, the orange peel samples were subjected to an elemental SEM-EDS analysis. The results for the orange peel were 73.530% of moisture, 99.261% of volatiles, 0.052% of ash, 0.687% of fixed carbon, 19.801% of lignin, 69.096% of cellulose and 9.015% of hemicellulose. The highest concentration of glucose and fructose were 24.585 and 9.709 g/L, respectively. The results highlight that sugar production is increased by decreasing the acid concentration.

1. Introduction

In 2018, the United Nations Food and Agriculture Organization (F.A.O.) [1] estimated a world citrus production of 104.15 Mt, with 75.54 Mt corresponding to orange. During 2018, the largest orange producers worldwide were Brazil, China, India, USA and Mexico, achieving 58.10% of the total orange production. In the same year Mexico produced 4.74 Mt of orange, which represents 6.3% of the world total production [2]. Figure 1 presents the orange production of these countries compared to the world production from 2000 to 2018 [1]. In general, orange production is increasing year over year. The wastes that are generated from the orange industry include seeds, pulp, albedo and peel. Some processes take advantage of the greater amount of the fruit and used the rest in different subprocess—cattle feed, essential oil and/or limonene extraction, as well as pectin’s extraction are some of the trends applied to the orange residues. However, not all waste is used, resulting in non-hazardous waste with revalorization potential.
The orange peel is the waste with the highest volume and ease of use in the orange industry. It is estimated that around 20% of the orange is orange peel. Therefore, there is an estimation of 15.10 Mt of orange peel generation in 2018. However, before proposing a valorization route for orange peel, the physicochemical characteristics of this waste must be known. The literature indicates that the orange peel contains 23% sugar, 22% cellulose, 25% pectins and 11% hemicellulose [3,4,5]. With these values, biochemical transformations are feasible options, such as the production of bioethanol or biogas [6,7,8]. These processes require several stages of biomass treatment, so its full implementation must be studied extensively, in addition, each stage may generate a by-product [9].
In recent years, food waste valorization acquired significantly importance, whether animal or vegetable. In the case of agro-industrial waste, olive leaves have been proven to be precursors of value-added chemical compounds such as phenols [10]. Regarding organic food waste, chemical–biological treatments are used to produce hydrogen, biogas and reagents in the form of acetic acid, propionic acid and butyric acid [11]. In the case of sea biomass waste, shrimp waste is subjected to enzymatic hydrolysis to produce nitrogen compounds [12].
Essential oil extraction is one of the most common applications of orange peel waste. This process does not significantly transform the orange peel, it only allows the removal of the compounds that make up the essential oil such as limonene, alpha pinene, camphene, among others [13]. Normally, this type of extraction is carried out in presence of water around 100 °C. However, not taking advantage of this by-product implies two problems—the loss of a valuable material in different industries and the possibility of inhibiting microbial activity in later operations. The processes for bioethanol and biogas production include a microbial operation and different studies have shown the ability of orange essential oil to inhibit similar processes [5].
Some biomass residues that have been used as precursors of reducing sugars for bioethanol production are rice straw, rice husk, macaranga, bamboo, agave leaves, palm oil, wheat bran, sorghum stalk, sugarcane leaves and citronella residues, to mention a few [14,15,16,17,18,19,20]. To achieve the presence of reducing sugar, it is necessary to apply an integral process that can convert the hemicellulosic material of the biomass into sugars that are easily accessible to the microorganisms for fermentation. During the polymer’s degradation, important monomers such as glucose, fructose, xylose and galactose can be obtained, which by fermentation generate bioethanol. These processes can range from acid hydrolysis, enzymatic hydrolysis and simultaneous hydrolysis and fermentation [8,21,22,23,24]. The case of orange peel has been studied, where it has been reported that hydrolysis with diluted acid is one of the best options for cellulose and hemicellulose degradation [25].
Although it has been reported that diluted acid hydrolysis is the most appropriate for similar wastes, each author uses different temperature, time, and acid concentration values under 6% (w/w) [15,26]. Likewise, the scale of production of both reducing sugars and bioethanol affects the operating parameters, since high concentrations of acid deteriorate the reactors, increase the plant maintenance cost and adds costs in the form of raw materials and waste disposal [27,28]. Therefore, the objective of the present work was to determine the experimental conditions to obtain the maximum reducing sugars yield from orange peel using a diluted acid hydrolysis process once essential oil was extracted. Proximate and chemical analysis of orange peel before the hydrolysis was performed. Before and after hydrolysis, a Scanning Electron Microscopy with Energy-dispersive X-ray spectroscopy analysis (SEM-EDS) was applied to the orange peel surface.

2. Results

2.1. Results for the Proximate and Chemical Analysis of Orange Peel

Table 1 describes the proximate and chemical analysis results of the orange peel. The proximate analysis results indicate that the orange peel residue is not susceptible to its use in a thermochemical process since its primary composition is water. The volatility of various compounds in orange peel is also noticeable—the terpenes that conform the essential oils are usually volatile compounds whose phase change begins around 60 °C. In the case of solvent extractables, the orange peel shows an affinity of 40.399% for the extraction of these compounds in hot water. It is one of the reasons why the extracts prepared based on this residue are aqueous [5].
The chemical composition of the orange peel is mainly made up of cellulose, followed by lignin and then hemicellulose. Cellulose is the simplest natural polymer to convert into its monomers, which helps to improve the fermentation process [18].

2.2. Design of Experiments of the Dilute Acid Hydrolysis

Table 2 depicts the results obtained in the factorial designs for the concentration of glucose and fructose obtained by dilute acid hydrolysis.
The combination of factors that produces the greatest amount of glucose and fructose was 0.5% v/v of H2SO4, 125 °C and 120 min of operation. The previous combination forms up to 24.585 g/L of glucose and up to 9.709 g/L of fructose. It is important to note that at lower factors levels, it is possible to obtain a concentration of glucose and fructose above 10 g/L. At a pilot plant level, low levels of acid concentration are beneficial, since it prolongs the duration of the installations, and saves on reagent costs like H2SO4. Due to the above, the combination of factors at low levels is attractive [29]. At the maximum temperature level, sugar production increases. However, these increases do not follow the same trend if the H2SO4 concentration increases. Other biomass residues show increases in the concentration of reducing sugars while increasing the concentration of H2SO4 [29], where the orange peel shows a contrary behavior if this factor is analyzed individually.
In Minitab, two ANOVA tables were created, one with glucose concentration as a response variable and the other with fructose concentration as a response variable. The results of both analyses are shown in Table 3.
The individual factors that turned out to be significant were the acid concentration (A) and the temperature (B) for both designs of experiments, while for glucose the operating time (C) was also an important factor. Regarding the binary interactions, the combination of acid–concentration–temperature and temperature–time was significant for both designs of experiments. Figure 2 shows the contour plots for these combinations. For the acid–concentration–temperature factors, the areas with the highest production are in the strong blue region (Figure 2a,c), which begins with a temperature of at least 112 °C and is limited to acid concentration less than 1% v/v. By increasing the temperature and decreasing the acid concentration, a clear increase in the glucose and fructose concentration can be observed. In the interaction between the temperature and the hydrolysis time (Figure 2b,d) a similar behavior is observed; the longer the time and the higher temperature, the higher the reducing sugars concentration. However, these areas are different compared with the ones in Figure 2a,c.
The contour diagram is useful because it provides factor ranges in which a response variable is similar to the ones in the design of experiments. When combining both contour diagrams for glucose and fructose, it is observed that the region with a glucose production between 15–20 g/L will occur in the ranges of 0.5–0.75% of H2SO4, 123–125 °C and 1.95–2 h. For fructose, the ranges in which a concentration between 6–8 g/L can be produced are 0.5–0.95% H2SO4, temperature of 119–125 °C and 1.7–2 h.

2.3. SEM-EDS Analyses

The image in Figure 3 shows the surface of orange peel before the addition of H2SO4. It can be seen that there is an absence of acid and NaOH. The percentage of O and C in the image was obtained without chemical modifications to the surface of the orange peel, so they are considered basal values. These values can increase or decrease depending on the type of reaction that occurs with H2SO4 and NaOH.
The images presented in Figure 4 were taken based on the results of the design of experiments. For this, the combinations of temperature–time at low level and high level were chosen. It can be seen that the surfaces deteriorate due to the hydrolysis, which increases from top to bottom and from left to right. As the H2SO4 concentration increases in the hydrolysis, the surface contracts and becomes irregular.
The operation conditions for Figure 5a were 60 min and 100 °C, and for Figure 5b were 120 min and 125 °C. The elemental analysis indicates that S was not enough to be deposited on the surface of Figure 5a. In the case of Figure 5b, an average of 1.97% of S appears on the surface. Because the neutralizations were carried out with NaOH, the presence of Na is remarkable in both cases, being 5.6 times higher for Figure 5b. The results for Figure 5b are capable of producing on average 21.887 g/L of glucose and 9.286 g/L of fructose. If these values are compared with those in Figure 5a, which were 10.659 g/L of glucose and 4.872 g/L of fructose, the decrease of C in Figure 5b can be explained, since when the H2SO4 reacts under these conditions it generated a greater quantity of reducing sugars, as a result of a greater consumption of C. In some cases, the equipment detects Al in the samples, which is attributed to parts of the orange peel that had direct contact with the container where they were placed. With respect to the surface, Figure 5a is more uniform compared to Figure 5b. In addition, in the latter, rougher areas can be seen.
The operating conditions of the sample in Figure 6a were 60 min and 120 °C, and for Figure 6b, the conditions were 120 min and 125 °C. For both cases of Figure 6a, the concentration of S at the surface is appreciable, with a similar average at the points shown. There is an average concentration below 1.20% of Al in the two figures, which is attributed to the lid of the container where the hydrolysate reaction occurs. The concentration of O increases from Figure 6a to Figure 6b—since both NaOH and H2SO4 contain O, there is an addition of these materials to the surface of the orange peel. In the case of C, a decrease occurs in Figure 6b, which is attributed to its consumption for the generation of glucose and fructose. On average, Figure 6a generates 8.105 g/L of glucose and 3.708 g/L fructose, in contrast to the 16.277 g/L of glucose and 7.356 g/L of fructose that are generated in Figure 6b. The generation of both sugars in Figure 6b is doubled compared to Figure 6a, even though the elemental compositions of S and Na remain similar. Visually, both samples present surfaces worn by hydrolysis.
The operating conditions of Figure 7a were 60 min and 100 °C and for Figure 7b 120 min and 125 °C. For the two cases the concentration of H2SO4 used was 1.5% v/v. For this EDS, it is important highlight that the average glucose and fructose productions in both hydrolysis reactions were similar at 6.560 g/L of glucose and 3.129 g/L of fructose for Figure 7a, while for Figure 7b it was 8.657 g/L of glucose and 3.652 g/L of fructose. With the above, a similar behavior was expected in the element’s percentage compositions, an effect that occurs for both Na and S. In addition, C now has a higher percentage composition in Figure 7b than in Figure 7a. The operating conditions of the sample in Figure 7b indicate that the hydrolysis is not as satisfactory as in the other EDS. Visually, Figure 7b shows a lower surface uniformity if compared to its counterpart Figure 7a.

3. Discussion

According to proximate analysis results, thermochemical applications such as direct combustion of orange peel are not recommended due to the high moisture content. Biological applications must be carefully studied, since the amount of volatile compounds such as limonene will prevent the growth of certain microorganisms. The presence of volatile compounds is evident. Regardless of the revalorization procedure for orange peel, these compounds that comprise orange peel essential oil must be considered. As an industrial process that seeks the use of orange peel for the production of reducing sugars and bioethanol, it must consider the essential oil as a by-product to help the profitability of the process. The results of orange peel chemical composition are linked to the quantification of glucose and fructose, since cellulose degrades into these monomers when is hydrolyzed.
Regarding the results from the design of experiments, the conditions under which the greatest amount of reducing sugars in the form of glucose and fructose are produced were—H2SO4 concentration 0.5% v/v, temperature of 125 °C and hydrolysis time 120 min. The above combination gives an average glucose and fructose concentration of 21.887 and 9.286 g/L, respectively. When increasing the H2SO4 concentration, a decrease in the sugars produced was observed. Presenting on average, at the highest levels of the factors, a production of 8.657 g/L of glucose and 3.652 g/L of fructose, up to three times lower compared to the conditions of maximum production. The glucose and fructose concentrations achieved according to the design of experiments may vary even under strict operating conditions. This is due to the fact that orange peel waste can have a different composition according to the geographical position, soil type where orange was grown and weather conditions. However, working with orange peel waste, the tendency set by the parameters of the design of experiments must be maintained, at low acid concentration, 125 °C for 2 h.
The results of the SEM-EDS analysis yield morphological and elemental information of the surface that confirm the information obtained by the design of experiments. An important aspect to highlight is that, unlike other biomass materials such as corn, the concentration must remain at low levels, which is favorable.
Both the percentage of O and Na in the sample increase with increasing H2SO4 concentration, due to the greater need for NaOH to maintain the pH of the hydrolysate between 4.8 and 5.2. Likewise, if the concentration of H2SO4 increases, the % of C decreases in the mixture, which reacts to form the sugars dissolved in the hydrolysate. The previous behavior is not fulfilled in the hydrolysate with the maximum factor levels, since the temperature–time interaction causes a low reaction yield in the generation of reducing sugars, and that the SEM-EDS detects a % of C that was lower that its counterparts.

4. Materials and Methods

4.1. Proximate and Chemical Analysis of Orange Peel

For the orange peel proximate analysis, 1 g of freshly peeled sample was weighed, which included both albedo and peel and placed inside a crucible of known mass. The crucible and the sample were placed in a muffle at 45 °C for 48 h [30]. Once it reached the desired time in the muffle, the sample was cooled to room temperature in a desiccator and the mass of the crucible was measured. The moisture percentage was calculated by weight difference. To calculate the volatiles percentage, the moisture-free sample was brought to a temperature of 950 °C in the absence of air for 7 min, then it was cooled on a ceramic surface in a desiccator at room temperature and the mass of the crucible was measured. The difference in mass was calculated as the volatile percentage [31]. For the ash analysis, the sample resulting from the determination of volatiles was subjected to 580 °C for 4 h, cooled in a desiccator with ceramic surface and the mass of the crucible was measured, the difference in percentage was recorded as ash content [32]. Finally, the remaining residue in the crucible was quantified and considered as the fixed carbon percentage. The moisture, volatiles, ash and fixed carbon analyses were carried out in triplicate.
The chemical analysis of the orange peel began by measuring 4 g of moisture-free sample and then placing it in a thimble of known mass. Subsequently, the thimble was placed inside soxhlet extraction equipment with 200 mL of acetone as solvent and boiled for 8 h [33]. At the end of the extraction, the thimble was dried in a muffle at 105 °C for 3 h, cooled to room temperature in a desiccator and then the mass of the thimble with sample was measured. The acetone extractables percentage was calculated by weight difference.
For the determination of hot water extractables, 3 g of moisture-free sample of orange peel and free from acetone extractables was used. The sample was placed in a 250 mL ball flask, 200 mL of hot water was added and it was boiled in a water bath with condensation refluxed for 3 h [34]. At the end of the extraction, a filter paper was weighed and used in a büchner funnel to separate the sample from the hot water. The filter paper was brought to 105 °C for 4 h in a muffle, dried at room temperature in a desiccator and the mass of the filter paper with the orange peel was measured. The hot water extractables percentage was determined by weight difference. The resulting orange peel was considered free of total extractables.
The lignin content determination was carried out using 1 g of orange peel free of moisture and free of total extractables, which was mixed with 15 mL of H2SO4 at 72%, stirred for 1 min at 400 rpm and for 2 h at 200 rpm. Then, the solution was placed in a 1 L Erlenmeyer flask with 560 mL of distilled water and it was boiled with condensation reflux for 4 h [35]. To filter the sample, a filter paper was weighed and used with a bücher funnel. The filter paper was heated to 105 °C and 4 h, then cooled to room temperature in a desiccator and the mass of the paper was measured. The lignin percentage was calculated by weight difference.
For the holocellulose content, 2 g of moisture-free orange peel that was free of total extractables was added inside an Erlenmeyer flask. Also, 150 mL of distilled water, 0.2 mL of acetic acid and 1 g of sodium chlorite were used to complete the mixture [36]. The flask was sealed and placed in a water bath at 75 °C for 5 h. Every hour, 0.2 mL of acetic acid and 1 g of sodium chlorite were added, until reaching a total of 1 mL of acetic acid and 5 g of sodium chlorite. The procedure ended at the fifth hour and the sample was removed from the water bath. A filter paper with known mass was used in a büchner funnel to filter the sample. During the filtration, 500 mL of distilled water was used as a wash until the yellow coloration of the sample was removed. The content of the paper was brought to 105 °C for 4 h, then it was cooled in a desiccator to finally measure its mass on a balance. The holocellulose content was measured by weight difference.
The cellulose content determination used 2 g of sample resulting from the holocellulose determination, which was added to an Erlenmeyer flask with 10 mL of 17.5% NaOH, and allowed to rest for 5 min at 20 °C [37]. A total of 5 mL of 17.5% NaOH was added every 5 min until reaching 25 mL of NaOH. Then, the last 5 mL of NaOH the sample was allowed to rest for 30 min. Then, 33 mL of distilled water was added and the mixture was left to rest for 60 min. The content of the flask was neutralized with 15 mL of acetic acid and NaOH at 8.3% until pH of 7 was reached, then it was filtered using a filter paper of known mass. After the filtration, the filter paper and its content were dried at 105 °C for 4 h and allowed to cool in a desiccator. Finally, the filter paper was weighed and the cellulose content was measured by weight difference. The hemicellulose content was determined by percentage difference between the holocellulose and cellulose content.

4.2. Design of Experiments for the Orange Peel Diluted Acid Hydrolysis

A design of experiments of the factorial design type applied to the diluted acid hydrolysis of orange peel was developed to contrast the obtained reduced sugars [38,39]. The purpose of a design of experiment is to identify the variables that significantly affect a process from a statistical point of view, adjusting the operation parameters to achieve the best result according to the desired application [26].
The selected factors were—(A) H2SO4 concentration, (B) temperature, (C) hydrolysis time. A total of 3 levels were specified for factor (A) and 2 levels for factors (B) and (C), with 2 replicates per combination of variables. The amount of hydrolysis performed for this design of experiment was 24 experiments. The levels for the factors were concentration of H2SO4 0.5%, 1.0% and 1.5% all in volume percent, for the temperature 100 °C and 125 °C and for the hydrolysis time 1 and 2 h. The purpose of the factorial design is to identify which individual factors and combinations thereof are capable of significantly affecting the production of sugars. The results of the sugar production were analyzed in Minitab® where the important process variables were identified.
Orange peel needs a pretreatment before the hydrolysis, a series of orange peel hydrodistillations were carried out to remove the essential oil. The essential oil was stored in amber vials and refrigerated at 4 °C [13]. The orange peel without essential oil was heated 24 h at 65 °C [22,40,41]. The previous procedure was repeated, until 100 g of dried orange peel was obtained, then its size was reduced in a mortar and placed in a desiccator, until later use.
A furnace was preheated for 30 min to a temperature set in the design of experiments. At the same time, 2 g of dried orange peel was placed in a 100 mL flask, adding 60 mL of the H2SO4 solution (1:30 ratio). The flask was placed in the furnace by the time of hydrolysis, and once finished, it was removed and cooled to a temperature of 30 °C. The acid pH of the hydrolysate was brought to 4.8–5.2 with NaOH 0.5 N, then it was filtered and stored at 4 °C [42]. The filtered orange peel was dried at 65 °C for 24 h and placed in a desiccator for further analysis by SEM.
For the reducing sugars identification, the 3,5-DNS method was chosen [43,44]. This method has proved its validation for reducing sugars identification by using known standard solutions [45,46,47]. Two calibration curves were prepared, one with glucose and the second with fructose. In both curves, 10 points were used, whose concentration ranges ranged from 0.2 to 2.0 g/L. Once the calibration curve was ready, each hydrolysate sample was diluted 10 times and 3 mL of it was taken. Subsequently, 3 mL of the prepared DNS reagent was added to each dilution, to a total of 6 mL, in a 1:1 ratio (sample—DNS). Each of the preparations was heated for 5 min at 100 °C, to generate the chemical reaction that gives the color to the sample and then cooled to 25 °C. Also, a DNS solution blank was prepared. The quantification of reducing sugars was achieved by a Perkin Elmer Lambda 25 UV-Vis Spectrometer (Waltham, MA, USA), and the method worked at 575 nm. All the hydrolysate samples treated were contrasted with the 2 calibration curves and their readings were recorded.

4.3. SEM-EDS

The samples for SEM were placed on a conductive plate with carbon tape without metallic coating. A total of 6 samples were taken from 24 of the design of experiments, which had the highest amount of sugar produced. The equipment used was a JEOL JSM-6010LA analytical scanning electron microscope (Tokyo, Japan), with a working distance of 11 mm, acceleration voltage of 10 kV and under vacuum of 50 Pa [48].
The general procedure of this work can be seen in Table 4. This scheme includes the analysis of reducing sugars and the SEM-EDS of the samples after hydrolysate.

5. Conclusions

Under the selected parameters of the design of experiments, the maximum concentration of glucose and fructose was achieved with an acid concentration of 0.5%, at 125 °C for 2 h. However, this does not mean that they are the best conditions to operate a hydrolysis process applied to orange peel waste. Future research could study the effect of reducing the concentration of H2SO4 to find the turning point, where the reducing sugars concentration starts to decrease. In addition, the effect of the volume ratio of H2SO4 and orange peel waste can be addressed, since in all the experiments it remained constant. While this methodology allows essential oil extraction from orange peel, other value-added products such as pectins can be explored before this waste is subjected to fermentation processes to obtain alcohols.
Although it is possible to modify the pretreatment of the orange peel to improve the production of sugars, the revaluation of a waste must be an integral process, which follows the principles of the biorefinery concept. That is, not just looking for punctual application for the given waste, but obtaining multiple products from the same source in such a way that can be scalable to a commercial level. Depending on the desired production scale, either at the laboratory or pilot plant level, this work provides the concentration of reducing sugars in the form of glucose and fructose, according to the 12 combinations proposed in the design of experiments.

Author Contributions

Conceptualization, J.R.A. and G.M.; methodology, G.M. and M.A.C.; software, D.G.M.; validation, C.G. and M.A.C.-A.; formal analysis, C.A.S.; investigation, J.A.L.; resources, M.A.C.-A.; data curation, J.A.L. and C.A.S.; writing—original draft preparation, J.R.A. and M.A.C.; writing—review and editing, C.G.; visualization, D.G.M.; supervision, M.A.C.; project administration, J.R.A. All authors have read and agreed to the published version of the manuscript.

Funding

This research received no external funding.

Data Availability Statement

The data that support the findings of this study are available from the corresponding authors upon reasonable request.

Acknowledgments

The authors thank the National Council on Science and Technology (CONACYT) and the Engineering Institute of the Universidad Autónoma de Baja California for its support in the development of this work.

Conflicts of Interest

The authors declare no conflict of interest.

Sample Availability

Not available.

References

  1. Food and Agriculture Organization FAOSTAT. Food Production. 2020. Available online: http://www.fao.org/faostat/en/#data/QC (accessed on 24 June 2020).
  2. Sistema de Información Agroalimentaria y Pesquera (SIAP). Cierre de la Producción por Estado. 2020. Available online: http://infosiap.siap.gob.mx:8080/agricola_siap_gobmx/AvanceNacionalCultivo.do (accessed on 24 June 2020).
  3. Gaind, S. Exploitation of orange peel for fungal solubilization of rock phosphate by solid state fermentation. Waste Biomass Valor. 2016, 8, 1351–1360. [Google Scholar] [CrossRef]
  4. Dávila, J.A.; Rosenberg, M.; Cardona, C.A. Techno-economic and environmental assessment of p-Cymene and pectin production from orange peel. Waste Biomass Valor. 2015, 6, 253–261. [Google Scholar] [CrossRef]
  5. Siles, J.A.; Li, Q.; Thompson, I.P. Biorefinery of waste orange peel. Crit. Rev. Biotechnol. 2010, 30, 63–69. [Google Scholar] [CrossRef]
  6. Aboagye, D.; Banadda, N.; Kiggundu, N.; Kabenge, I. Assessment of orange peel waste availability in Ghana and potential bio-oil yield using fast pyrolysis. Renew. Sust. Energ. Rev. 2017, 70, 814–821. [Google Scholar] [CrossRef]
  7. Maschke, R.W.; Geipel, K.; Bley, T. Modeling of plant in vitro cultures: Overview and estimation of biotechnological processes. Biotechno. Bioeng. 2015, 112, 1–12. [Google Scholar] [CrossRef] [PubMed]
  8. Santi, G.; Crognale, S.; Annibale, A.D.; Petruccioli, M.; Ruzzi, M.; Valentini, R.; Moresi, M. Orange peel pretreatment in a novel lab-scale direct steam-injection apparatus for ethanol production. Biomass Bioenerg. 2014, 61, 146–156. [Google Scholar] [CrossRef]
  9. Molina-Calle, M.; Priego-Capote, F.; Luque de Castro, M.D. Development and application of a quantitative method for determination of flavonoids in orange peel: Influence of sample pretreatment on composition. Talanta 2015, 144, 349–355. [Google Scholar] [CrossRef]
  10. Voros, V.; Drioli, E.; Fonte, C.; Szekely, G.; Fonte, C.; Szekely, G. Process Intensification via Continuous and Simultaneous Isolation of Antioxidants: An Upcycling Approach for Olive Leaf Waste. ACS Sustain. Chem. Eng. 2019, 7, 18444–18452. [Google Scholar] [CrossRef]
  11. Sarkar, O.; Katakojwala, R.; Mohan, S.V. Low Carbon Hydrogen production from waste based Biorefinery System and Environmental Sustainability Assessment. Green Chem. 2021, 23, 561–574. [Google Scholar] [CrossRef]
  12. Deng, J.-J.; Zhang, M.-S.; Li, Z.-W.; Lu, D.L.; Mao, H.-H.; Zhu, M.-J.; Li, J.-Z.; Luo, X.-C. One-step processing of shrimp shell waste with a chitinase fused to a carbohydrate-binding module. Green Chem. 2020, 22, 6862–6873. [Google Scholar] [CrossRef]
  13. Ayala, J.R.; Montero, G.; Campbell, H.E.; García, C.; Coronado, M.A.; León, J.A.; Sagaste, C.A.; Pérez, L.J. Extraction and Characterization of Orange Peel Essential Oil from Mexico and United States of America. J. Essent. Oil. Bear. Plants 2017, 20, 897–914. [Google Scholar] [CrossRef]
  14. Chen, W.-H.; Jang, M.-F.; Jheng, S.-L.; Lo, C.-J.; Wang, W. Cellulosic sugars from biomass: Effect of acid presoaking on pretreatment efficiency and operating cost estimation for sugar production. Bioresour. Technol. Rep. 2019, 7, 100259. [Google Scholar] [CrossRef]
  15. Cheng, Y.-S.; Wu, Z.-Y.; Sriariyanun, M. Evaluation of Macaranga tanarius as a biomass feedstock for fermentable sugars production. Bioresour. Technol. 2019, 294, 122195. [Google Scholar] [CrossRef] [PubMed]
  16. Kassaye, S.; Pant, K.K.; Jain, S. Hydrolysis of cellulosic bamboo biomass into reducing sugars via a combined alkaline solution and ionic liquid pretreatment steps. Renew. Energ. 2017, 104, 177–184. [Google Scholar] [CrossRef]
  17. Khamis, N.A.; Shamsudin, S.; Rahman, N.S.A.; Kasim, K.F. Effects of autohydrolysis on rice biomass for reducing sugars production. Mater. Today Proc. 2019, 16, 2078–2087. [Google Scholar] [CrossRef]
  18. Láinez, M.; Héctor, A.; Ruiz, H.A.; Castro-Luna, A.A.; Martínez-Hernández, S. Release of simple sugars from lignocellulosic biomass of Agave salmiana leaves subject to sequential pretreatment and enzymatic saccharification. Biomass Bioenerg. 2018, 118, 133–140. [Google Scholar] [CrossRef]
  19. Martínez, C.M.; Adamovic, T.; Cantero, D.A.; Cocero, M.J. Scaling up the production of sugars from agricultural biomass by ultrafast hydrolysis in supercritical water. J. Supercrit. Fluid. 2019, 143, 242–250. [Google Scholar] [CrossRef]
  20. Timung, R.; Goud, V.V. Subcritical water hydrolysis of spent Java Citronella biomass for production of reducing sugar. Mater. Today Proc. 2018, 5, 23128–23135. [Google Scholar] [CrossRef]
  21. Elliston, A.; Collins, S.R.A.; Faulds, C.B.; Roberts, I.N.; Waldron, K.W. Biorefining of waste paper biomass: Increasing the concentration of glucose by optimizing enzymatic hydrolysis. Appl. Biochem. Biotechnol. 2014, 172, 3621–3634. [Google Scholar] [CrossRef]
  22. Modenbach, A.A.; Nokes, S.E. The use of high-solids loadings in biomass pretreatment-a review. Biotechnol. Bioeng. 2012, 6, 1430–1442. [Google Scholar] [CrossRef]
  23. Murthy, G.S.; Johnston, D.B.; Rausch, K.D.; Tumbleson, M.E.; Singh, V. Design and Evaluation of an Optimal Controller for Simultaneous Saccharification and Fermentation Process. Appl. Biochem. Biotechnol. 2012, 166, 87–111. [Google Scholar] [CrossRef] [PubMed]
  24. Nerurkar, M.; Joshi, M.; Adivarekar, R. Bioscouring of cotton using lipase from marine bacteria bacillus sonorensis. Appl. Biochem. Biotechnol. 2015, 175, 253–265. [Google Scholar] [CrossRef] [PubMed]
  25. Buyukkileci, A.O.; Fernandez, M.M.L.; Tari, C. Utilization of orange peel, a food industrial waste, in the production of exo-polygalacturonase by pellet forming Aspergillus sojae. Bioprocess. Biosyst. Eng. 2015, 38, 749–760. [Google Scholar] [CrossRef]
  26. Tai, C.; Keshwani, D. Impact of pretreatment with dilute sulfuric acid under moderate temperature on hydrolysis of corn stover with two enzyme systems. Appl. Biochem. Biotechnol. 2014, 172, 2628–2639. [Google Scholar] [CrossRef]
  27. Chaiprapat, S.; Wongchana, S.; Loykulnant, S.; Kongkaew, C.; Charnnok, B. Evaluating sulfuric acid reduction, substitution, and recovery to improve environmental performance and biogas productivity in rubber latex industry. Process. Saf. Environ. 2015, 94, 420–429. [Google Scholar] [CrossRef]
  28. Lindgren, M.; Siljander, S.; Suihkonen, R.; Pohjanne, P.; Vuorinen, J. Erosion-corrosion resistance of various stainless steel grades in high-temperature sulfuric acid solution. Wear 2016, 364–365, 10–21. [Google Scholar] [CrossRef]
  29. Jin, M.; Sarks, C.; Bals, B.D.; Posawatz, N.; Gunawan, C.; Dale, B.E.; Balan, V. Toward high solids loading process for lignocellulosic biofuel production at a low cost. Biotechnol. Bioeng. 2016, 5, 980–988. [Google Scholar] [CrossRef]
  30. Determination of Total Solids in Biomass and Total Dissolved Solids in Liquid Process Samples. Available online: https://www.nrel.gov/docs/gen/fy08/42621.pdf (accessed on 20 August 2018).
  31. ASTM International. ASTM E872-82–Standard Test Method for Volatile Matter in the Analysis of Particulate Wood Fuels; ASTM International: West Conshohocken, PA, USA, 2006. [Google Scholar]
  32. ASTM International. ASTM E830-87–Standard Test Method for Ash in the Analysis Sample of Refuse Derived Fuel; ASTM International: West Conshohocken, PA, USA, 2004. [Google Scholar]
  33. TAPPI. Preparation of Wood for Chemical Analysis Test Method T264 cm-07 (TAPPI); TAPPI: Peachtree Corners, GA, USA, 2007. [Google Scholar]
  34. TAPPI. Water Solubility of Wood and Pulp Test Method T207 cm-99 (TAPPI); TAPPI: Peachtree Corners, GA, USA, 1999. [Google Scholar]
  35. ASTM International. ASTM D1106-96–Standard Test Method for Acid-Insoluble Lignin in Wood; ASTM International: West Conshohocken, PA, USA, 2001. [Google Scholar]
  36. ASTM International. ASTM D1104-56–Method of Test for Hollocelulose in Wood; ASTM International: West Conshohocken, PA, USA, 1985. [Google Scholar]
  37. Rowell, R.M.; Pettersen, R.; Tshabalala, M.A. Handbook of Wood Chemistry and Wood Composites, 1st ed.; Taylor & Francis Group: Boca Raton, FL, USA, 2013; pp. 33–74. [Google Scholar]
  38. Chong, Y.; Yan, A.; Yang, X.; Cai, Y.; Chen, J. An optimum fermentation model established by genetic algorithm for biotransformation from crude polydatin to resveratrol. Appl. Biochem. Biotechnol. 2012, 166, 446–457. [Google Scholar] [CrossRef]
  39. Dai, J.-Y.; Zhao, P.; Cheng, X.-L.; Xiu, Z.-L. Enhanced production of 2,3-Butanediol from sugarcane molasses. Appl. Biochem. Biotechnol. 2015, 175, 3014–3024. [Google Scholar] [CrossRef]
  40. Bustamante, J.; Stempvoort, S.; García-Gallarreta, M.; Houghton, J.A.; Briers, H.K.; Budarin, V.L.; Matharu, A.S.; Clark, J.H. Microwave assisted hydro-distillation of essential oils from wet citrus peel waste. J. Clean. Prod. 2016, 137, 598–605. [Google Scholar] [CrossRef]
  41. Njoroge, S.M.; Koaze, H.; Karanja, P.N.; Sawamura, M. Essential oil constituents of three varieties of Kenyan sweet oranges (Citrus sinensis). Flavour Fragr. J. 2004, 20, 80–85. [Google Scholar] [CrossRef]
  42. Ji, W.; Shen, Z.; Wen, Y. Hydrolysis of wheat straw by dilute sulfuric acid in a continuous mode. Chem. Eng. J. 2015, 260, 20–27. [Google Scholar] [CrossRef]
  43. García, J.F.M.; Sánchez, S.; Cuevas, M. Evaluation of the effect of the dilute acid hydrolysis on sugars release from olive prunings. Renew. Energ. 2013, 51, 382–387. [Google Scholar] [CrossRef]
  44. Miller, G.L. Use of dinitrosalicylic acid reagent for determination of reducing sugar. Anal. Chem. 1959, 31, 426–428. [Google Scholar] [CrossRef]
  45. Julio-Altamiranda, Y.T.; Mercado-Pacheco, J.D.; Sánchez-Tuirán, E.L.; González-Delgado, A.D. Evaluation of mechanical-green solvent pretreatment of oil palm wastes for reducing sugars production in North-Colombia. Sustain. Chem. Pharm. 2020, 16, 100256. [Google Scholar] [CrossRef]
  46. Manmai, N.; Unpaprom, Y.; Ponnusamy, V.K.; Ramaraj, R. Bioethanol production from the comparison between optimization of sorghum stalk and sugarcane leaf for sugar production by chemical pretreatment and enzymatic degradation. Fuel 2020, 278, 118262. [Google Scholar] [CrossRef]
  47. Martins, E.H.; Ratuchne, A.; Machado, G.O.; Knob, A. Canola meal as a promising source of fermentable sugars: Potential of the Penicillium glabrum crude extract for biomass hydrolysis. Biocatal. Agric. Biotechnol. 2020, 27, 101713. [Google Scholar] [CrossRef]
  48. Wang, H.; Srinivasan, R.; Yu, F.; Steele, P.; Li, Q.; Mitchell, B.; Samala, A. Effect of acid, steam explosion, and size reduction pretreatments on Bio-oil production from sweetgum, switchgrass, and corn stover. Appl. Biochem. Biotechnol. 2012, 167, 285–287. [Google Scholar] [CrossRef] [PubMed]
Molecules 26 01348 g001
Figure 1. World and various countries orange production (Elaborated with data from the United Nations Food and Agriculture Organization).
Figure 1. World and various countries orange production (Elaborated with data from the United Nations Food and Agriculture Organization).
Molecules 26 01348 g001
Molecules 26 01348 g002
Figure 2. Binary interactions. (a) Glucose acid concentration vs. temperature; (b) glucose temperature vs. time; (c) fructose acid concentration vs temperature; and (d) fructose temperature vs. time.
Figure 2. Binary interactions. (a) Glucose acid concentration vs. temperature; (b) glucose temperature vs. time; (c) fructose acid concentration vs temperature; and (d) fructose temperature vs. time.
Molecules 26 01348 g002
Molecules 26 01348 g003
Figure 3. SEM-EDS analysis of orange peel before the dilute acid hydrolysis.
Figure 3. SEM-EDS analysis of orange peel before the dilute acid hydrolysis.
Molecules 26 01348 g003
Molecules 26 01348 g004
Figure 4. Surface comparison of the hydrolyzed orange peel samples, (a) H2SO4 0.5% v/v, 100 °C and 60 min, (b) H2SO4 1.0% v/v, 100 °C and 60 min, (c) H2SO4 1.5% v/v, 100 °C and 60 min, (d) H2SO4 0.5% v/v, 125 °C and 120 min, (e) H2SO4 1.0% v/v, 125 °C and 120 min, (f) H2SO4 1.5% v/v, 125 °C and 120 min.
Figure 4. Surface comparison of the hydrolyzed orange peel samples, (a) H2SO4 0.5% v/v, 100 °C and 60 min, (b) H2SO4 1.0% v/v, 100 °C and 60 min, (c) H2SO4 1.5% v/v, 100 °C and 60 min, (d) H2SO4 0.5% v/v, 125 °C and 120 min, (e) H2SO4 1.0% v/v, 125 °C and 120 min, (f) H2SO4 1.5% v/v, 125 °C and 120 min.
Molecules 26 01348 g004
Molecules 26 01348 g005
Figure 5. EDS analyses for orange peel treated with H2SO4 at 0.5 % v/v. (a) for 100 °C and 60 min. (b) for 125 °C and 120 min.
Figure 5. EDS analyses for orange peel treated with H2SO4 at 0.5 % v/v. (a) for 100 °C and 60 min. (b) for 125 °C and 120 min.
Molecules 26 01348 g005
Molecules 26 01348 g006
Figure 6. EDS analyses for orange peel treated with H2SO4 at 1.0 % v/v. (a) for 100 °C and 60 min. (b) for 125 °C and 120 min.
Figure 6. EDS analyses for orange peel treated with H2SO4 at 1.0 % v/v. (a) for 100 °C and 60 min. (b) for 125 °C and 120 min.
Molecules 26 01348 g006
Molecules 26 01348 g007
Figure 7. EDS analyses for orange peel treated with H2SO4 at 1.5 % v/v. (a) for 100 °C and 60 min. (b) for 125 °C and 120 min.
Figure 7. EDS analyses for orange peel treated with H2SO4 at 1.5 % v/v. (a) for 100 °C and 60 min. (b) for 125 °C and 120 min.
Molecules 26 01348 g007
Table 1. Proximate and chemical analysis of orange peel.
Table 1. Proximate and chemical analysis of orange peel.
AnalysisComposition (% in Weight)Standard Deviation
ProximateMoisture73.530%0.477%
Volatiles99.261%0.074%
Ash0.052%0.004%
Fixed carbon0.687%0.078%
ChemicalAcetone extractables6.821%0.604%
Hot water extractables40.399%2.595%
Lignin determination19.801%3.595%
Holocellulose determination78.110%4.404%
Cellulose determination69.096%9.015%
Hemicellulose determination5.433%5.433%
Table 2. Glucose and fructose concentration results for the factorial design.
Table 2. Glucose and fructose concentration results for the factorial design.
RunH2SO4 Concentration (%v/v) (A)Temperature (°C) (B)Time (h) (C)Glucose (g/L)Average Glucose (g/L)Standard Deviation (Glucose)Fructose (g/L)Average Fructose (g/L)Standard Deviation (Fructose)
1,20.5100111.302 10.01610.6590.9094.651 5.0924.8710.312
3,40.510027.940 8.8218.3800.6233.367 3.4993.4330.093
5,60.5125113.843
17.009		15.4262.2395.242
8.936		7.0892.612
7,80.5125224.585 19.18921.8873.8169.709
8.862		9.2850.599
9,10110018.212
7.998		8.1050.1514.231 3.1843.7070.740
11,12110029.500 10.3099.9040.5723.580
5.600		4.591.428
13,14112519.686
11.373		10.5291.1934.049 5.0904.5690.736
15,161125216.727
15.826		16.2760.6376.803 7.9087.3550.781
17,181.510017.080 6.0396.5590.7363.880
2.377		3.1281.063
19,201.510023.397 4.1923.7940.5621.768 1.7421.7550.018
21,221.512513.064
4.274		3.6690.8561.829
2.015		1.9220.132
23,241.512528.604 8.7098.6560.0743.600
3.704		3.6520.074
Table 3. ANOVA data for glucose and fructose.
Table 3. ANOVA data for glucose and fructose.
Variation SourceGlucoseFructose
Square SumFreedom DegreesMean SquareF0F CriticSquare SumFreedom DegreesMean SquareF0F
Critic
Acid concentration (A)292.8292146.41571.543.8952.911226.45626.063.89
Temperature (B)140.5681140.56868.684.7525.911125.57725.204.75
Time (C)32.441132.44115.854.753.81313.8133.764.75
AB67.025233.51216.373.8913.80326.9026.803.89
AC7.25123.6251.773.893.26721.6341.613.89
BC69.629169.62934.024.7512.447112.44812.264.75
ABC6.40323.2011.563.890.78720.3930.393.89
Error24.560122.047 12.181121.015
Total640.70523 124.78623
Table 4. Procedure of the presented work.
Table 4. Procedure of the presented work.
SampleStageAnalysisConditions and EquipmentReference
Orange peelProximate analysisMoisture45 °C for 48 h inside a muffle[30]
Volatiles950 °C for 7 min without air[31]
Ash580 °C for 4 h inside a muffle[32]
Fixed carbonThe difference in % of the sample, moisture, volatiles and ash analysis[32]
Chemical analysisAcetone extractable8 h Soxhlet extraction with acetone[33]
Water extractable3 h boiling water with condenser reflux[34]
Lignin %4 h, 15 mL of H2SO4, stirring and 560 mL of distilled water[35]
Holocellulose %150 mL water, 0.2 mL of acetic acid and 1 g of sodium chlorite per hour for 4 h. [36]
Cellulose %25 mL of NaOH at 17.5 %, 100 mL of NaOH at 8.3%, 10 mL of acetic acid and water for 105 min.[37]
Essential oil extractionHydrodistillation65 g of orange peel, 90 min, orange peel grinding of 1 min, 500 mL of water[13]
HydrolysisDiluted acid hydrolysisH2SO4 concentration, time and temperature according to the factorial design[38,39]
pH stabilizationNaOH at 0.5 N until a pH of 4.8–5.2 was reached[42]
Orange peel drying65 °C for 24 h
SEM-EDSSEM micrographyJEOL JSM-6010LA SEM, working distance 11 mm, 10 kV, 50 Pa, 300x, 500x[48]
EDS analysis
HydrosylateReducing sugars determination3,5 DNS reagent2.5 g of 3,5-Dinitric salicylic acid, 7.5 g of mixed potassium sodium tartrate, 4 g of NaOH in 250 mL of water[44,45,47]
Calibration curveGlucose and fructose calibration curves prepared from 0.2 g/L to 2 g/L with water[43,44]
Sample preparation1:10 dilution of the hydrosylate in distillated water and 1:1 diluted hydrosylate with DNS reagent
Reducing sugars quantificationPerkin-Elmer Lambda 25 UV-Vis Spectrometer at 575 nm measured in quartz cell[43,44,47]
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Ayala, J.R.; Montero, G.; Coronado, M.A.; García, C.; Curiel-Alvarez, M.A.; León, J.A.; Sagaste, C.A.; Montes, D.G. Characterization of Orange Peel Waste and Valorization to Obtain Reducing Sugars. Molecules 2021, 26, 1348. https://doi.org/10.3390/molecules26051348

AMA Style

Ayala JR, Montero G, Coronado MA, García C, Curiel-Alvarez MA, León JA, Sagaste CA, Montes DG. Characterization of Orange Peel Waste and Valorization to Obtain Reducing Sugars. Molecules. 2021; 26(5):1348. https://doi.org/10.3390/molecules26051348

Chicago/Turabian Style

Ayala, José R., Gisela Montero, Marcos A. Coronado, Conrado García, Mario A. Curiel-Alvarez, José A. León, Carlos A. Sagaste, and Daniela G. Montes. 2021. "Characterization of Orange Peel Waste and Valorization to Obtain Reducing Sugars" Molecules 26, no. 5: 1348. https://doi.org/10.3390/molecules26051348

APA Style

Ayala, J. R., Montero, G., Coronado, M. A., García, C., Curiel-Alvarez, M. A., León, J. A., Sagaste, C. A., & Montes, D. G. (2021). Characterization of Orange Peel Waste and Valorization to Obtain Reducing Sugars. Molecules, 26(5), 1348. https://doi.org/10.3390/molecules26051348

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