Keywords
Kitchen waste; Saccharomyces cerevisiae; Fermentation; Bioethanol
Kitchen waste; Saccharomyces cerevisiae; Fermentation; Bioethanol
Kitchen waste is a raw material available in large volumes. The term applies to organic solids, which are discarded during food preparation. Kitchen waste is mostly composed of lignocelluloses and starch, and is degradable through microbial infestation. An outstanding resource for biotechnology is present in kitchen waste as carbohydrate polymer fraction1. The usage of lignocelluloses as feedstock would prompt novel challenges for biotechnology, for example, the product diversification2,3.
Kitchen waste extracted bioethanol is an alluring and sustainable energy source for vehicle fuel, as a gasoline alternative. Present ethanol production (so-called ‘first generation’), utilizing harvests such as sugar cane and corn, has become conventional method, whereas second-generation ethanol generation uses less expensive, non-sustenance feedstocks, for example, lignocelluloses or municipal solid waste, which could make ethanol more competitive alternative to petroleum4,5.
Plant cell walls are mostly composed of lignocellulosic biomass. Among its main components is cellulose, a linear polymer of cellobiose consisting of two D-glucose molecules connected by β-1, 4 bonds6. The more organized or crystalline cellulose is, the less soluble and less degradable it is. Cellulose degradation techniques include the use of effective enzymes, concentrated acid or alkaline and high temperatures for both nebulous and crystalline cellulose in the transformation procedure. Cellulose would be an ideal carbohydrate source for the fermentation due to the uniform hydrolyzable glucose building blocks7.
Hemicellulose is another important hetero-polysaccharide present in the plant cell wall. Hemicellulose differs from cellulose by the organization of several sugar units, by the presence of shorter chains and by a ramified central chain. Hemicellulose removal from the plant cell wall is easier than lignin and cellulose, owing to the bonds between cellulose, hemicellulose and lignin. A wide variety of enzymes, including endoxylanase, exoxylanase, mannanase, arabinosidase, acetylesterase, and glucoronisidase, are essential due to its structural diversity8. Alkaline pretreatments were also found to be successful at degrading hemicellulose9.
Lignin provides additional strength and protection to prevent enzymatic activity of fungi and insect attack by linking cellulose and hemicellulose10. Substantial moisture and rigidity resistance also added to biomass11 and known as a cellulase inhibitor12. As a result, exogenous proteins, such as bovine serum albumin, and surfactants, such as MgSO4, and CaCl213, are added before microbial or enzyme loading. Moreover, many pretreatment processes have been established to moderate the lignin hindrance.
Functional groups of lignin, including phenolic hydroxyl, benzyl hydroxyl, methoxyl, carbonyl and a minor amount of terminal aldehyde groups, are factors that influence its decomposition14. The lignin carbohydrate complexes (syringyl, guaiacyl and p-hydroxyphenyl units) formed by crosslink interactions, are also counted as a fermentation-restricting factor.
Starch (α-D-glucose monomer) degradation is complex than the sugar fermentation process. It initially broke down into glucose, through amylase or diastase and maltase hydrolysis. Then, ethanol and carbon dioxide are fermented from sugars through enzyme activity.
Alongside a mainstream project15,16, in this study, tentative fermentation was carried out in kitchen waste medium to find out if a wild-type microorganism has the ability to ferment cellulose efficiently17.
Yeast samples (Saccharomyces cerevisiae) were isolated and identified from date-juice using previously described methods15,18 in YEPD medium (106–107 cells/ml; 0.3% yeast extract #Y1625, 1% peptone #P7750, 2% dextrose #G8270, 1.5% agar #A1296, pH: 5; Sigma-Aldrich, St Louis, MO, USA). Discarded solid kitchen waste was collected from different households. This included peels from potatoes, pumpkin, papaya, cucumber, okra, green banana, balsan apple, carrot and basil. After chopping, pulverizing and blending with 1 L water, 250 g solid waste was taken as raw medium. Concentrated HCl (2 ml) was added to convert the calcium present (a fermentation inhibitor) to calcium sulfate salt19. HCl also regulates the pH of the medium to control for bacterial contamination and facilitate chemical hydrolysis of plant residues, which were boiled for 1.5 h, giving carbohydrate units of cellulose and starch. Monomers of amylose, amylopectin and glucose arose from further degradation. Urea (0.1 g) was also supplemented prior to boiling as a nitrogen source nutrient. The final pH was adjusted to 6.0 by dropwise addition of NaOH or HCl (measured using a pH meter; Mettler Toledo, Switzerland).
The 250 ml fermentation medium was transferred into 500 ml Erlenmeyer flasks and a homogenous suspension of yeast (10 ml YEPD broth) was inoculated in aseptic conditions. The flask was incubated in a rotary incubator (120 rpm) at 30°C for 48 h. Two separate experiments were conducted and ethanol production was recorded at 24 and 48 h intervals, and the average were calculated. The ethanol in this experiment was analyzed using the Conway method20. Downstream processing is required before isolation of usable ethanol.
Previous investigations15,16,18 indicated that ethanol is produced more readily under shaking than non-shaking conditions. After 48 h of fermentation at room temperature in a rotary incubator (120 rpm), a maximum of 7.3% (v/v) ethanol production was recorded (Table 1). The rate of alcohol production showed a cumulatively increasing trend, which was mirrored by a continued rise in pH throughout incubation, recorded as pH 6.52 at 48 h. The results also indicated that the full potential of kitchen waste fermentation will be revealed through longer durations of fermentation.
The kitchen waste medium contained plant organelles and was a rich source of cellulose, starch and glucose monomers. Comparison with previous studies15,16,18 showed the achieved production efficiency is below the level required for profitable commercial production. In this study, production of 7.3% (v/v) ethanol was recorded (Table 1). Further optimization of the process and co-fermentation (e.g. ethanol–butanol co-fermentation) is among the future goals of researchers21.
Most of the kitchen waste was similar feedstock to lignocellulosic raw materials, which is considered to be an excellent substrate22. Previous works delineated the pathway of converting plant-based waste biomass to bioethanol, in which enzyme pretreatment was conducted before yeast fermentation23–26. Gnansounou & Dauriat produced 30.9 g bioethanol and 65.2 L biogas using 1 kg of kitchen waste27. Velasquez & Ruiz fermented 346.5–388.7 l/ton bioethanol in a similar study using banana pulp and skin28. Industrial waste has also been used in fermentation technology29. A planned facility in East London will produce 16 million gallons of jet fuel per annum from 500,000 tons of waste for British Airways (the Green Sky project). A combination of plasma arc gasification with the Fischer-Tropsch method, known as Solena's Plasma Gasification (SPG) technology, will be used. In China’s Jiangsu province, a new waste-to-energy facility with a processing capacity of 900 metric tons, will be constructed.
Results were derived from limited parameters and only a single isolate of microorganism was employed. Future studies should be directed towards elaborate characterization and compare different criteria of kitchen waste fermentation. Optimization of the media and physicochemical parameters, and longer-duration fermentation will also be performed in future. This study was aimed towards fermentation only. A cheap, efficacious downstream processing method of the ethanol generated in this process also requires development.
All data underlying the results are available as part of the article and no additional source data are required.
When the research was carried out, SSR was a MSc student at Biotechnology program, Department of Mathematics and Natural Sciences, BRAC University and NC was the Coordinator of Biotechnology and Microbiology programmes at the Department of Mathematics and Natural Sciences, BRAC University.
Authors are grateful to the late Prof. Dr. AAZ Ahmad, former Chairperson of Department of MNS, BRAC University, Dhaka, for allowing the research work. Their sincere appreciation goes to Armanul Nasir, Arif, Forkan and Shamim Akhter Chowdhury for their graceful help and support.
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Is the work clearly and accurately presented and does it cite the current literature?
No
Is the study design appropriate and is the work technically sound?
No
Are sufficient details of methods and analysis provided to allow replication by others?
Partly
If applicable, is the statistical analysis and its interpretation appropriate?
No
Are all the source data underlying the results available to ensure full reproducibility?
Partly
Are the conclusions drawn adequately supported by the results?
No
Competing Interests: No competing interests were disclosed.
Is the work clearly and accurately presented and does it cite the current literature?
No
Is the study design appropriate and is the work technically sound?
No
Are sufficient details of methods and analysis provided to allow replication by others?
No
If applicable, is the statistical analysis and its interpretation appropriate?
No
Are all the source data underlying the results available to ensure full reproducibility?
No
Are the conclusions drawn adequately supported by the results?
No
Competing Interests: No competing interests were disclosed.
Alongside their report, reviewers assign a status to the article:
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