Abstract
The rising population and industrialisation produce a huge amount of waste, in particular from agro-industries, thus inducing environmental pollution. Therefore, waste should be better recycled into materials and energy, e.g. by incineration, gasification, and pyrolysis. Valuable by-products include enzymes, pigments, biofertilizers and edibles. Here we review the conversion of agro-waste, with focus on fermentation, composting, anaerobic digestion, enzymes, bioethanol, biofertilizers, microbial treatment and greenhouse gases.
Access provided by Autonomous University of Puebla. Download chapter PDF
Similar content being viewed by others
Keywords
1.1 Introduction
The rapid growth of the population generated significant investment in the food and agricultural industries. Every year, approximately 1.3 billion tonnes of agro-industrial food waste is produced worldwide. Fruits, vegetables, roots, and tubers account for the bulk of this (40–50%), making for 520–650 million tonnes (Ravindran et al. 2018), and destined for landfills or uncontrolled disposal, resulting in damage to the environment and financial loss. Therefore, sustainable management of them must be established. Population rise also calls for increased global energy demand, currently supported by fossil-fuels, which prevents long-term sustainability. The biggest and most often used source of renewable energy globally is biomass, which is increasingly used. The world biomass production is expected to 1500 Exajoules in 2050 and can be used sustainably from 200 to 500 Exajoules, accounting for 40–50% of the estimated primary energy demand (Popp et al. 2014). The energy demand is expected to rise by about 48 percent between 2012 and 2040 (Avcıoğlu et al. 2019). Government assistance is a pillar in accessing funding and technology and reducing the cost of producing green energy to promote the application of biomass-based energy technologies (Gutiérrez et al. 2020).
High-strength residues like livestock slurry, manure, crop remains, by-products of the agri-food such as coffee dregs, bagasse, degummed fruit, legumes, milk serum, sludge from wool, cellulose generated from agricultural and industrial sectors may be used to produce electricity, composting, biogas, biofuels and many other by-products by the action of microbes. (Yusuf 2017). For this purpose, advanced biorefinery becomes a promising option with several outputs (biofuels, biomaterials). The circular economy is based on a biorefining concept and approach to reducing, reusing, and recycling waste to recover waste products considered renewable resources (Peng and Pivato 2017).
This chapter discussed various kinds of waste generated from the agro-industrial sectors, such as agricultural residues, industrial residues, and different forms of wastewaters generated from agro-food industries. Well-established methods such as solid-state fermentation, Anaerobic digestion, and the composting process can be used to treat these various organic wastes. The action of different microbial communities can result in the production of various value-added products such as enzymes (alpha and beta-amylase, β-glucanase, cellulase, hemicellulase, xylanase, mannase, pectinase, inulinase, laccase, phytase, invertase, protease, pullulanase, and lipase), bioethanol, biodiesel, biogas and microbial biofertilizers with their potential applications in industrial or agricultural sectors. Increased industrialization and improper agro-waste management lead to greenhouse gas generation at a high rate, which has a toxic effect on the atmosphere and the human race. So, proper management practices can be helpful in the reduction of greenhouse gases and also dependency on fossil fuels.
1.2 Generation and Utilization of Agro-Industrial Biomass
A vast amount of waste is generated from agriculture-based industries in the form of agriculture and industrial residues, and wastewaters. Poor and unorganized disposal of these wastes adversely affects the environment and human health. These agro-based wastes have great potential to generate various kinds of value-added products such as biofuels, enzymes, and biofertilizers. Different type of biomass wastes generated from these industries are discussed below.
1.2.1 Agricultural Residues
Agriculture residues can be classified into field residues and process residues. Field residues are residues present in the field during the crop harvesting process, such as seed pods, stems, leaves, and stalks. Process residues are present till the crop has been turned into a profitable replacement commodity. These residues consist of husks, nuts, straw, leaves, shells, peel, pulp, roots, molasses, bagasse, and other waste biomass. They are used for animal feed, soil enhancement, fertilizers production, and various other uses (Sadh et al. 2018). Five million metric tons of agricultural biomass are generated annually from agro-based industries (Bharathiraja et al. 2017), which is underutilized, and their controlled use will improve irrigation abilities and erosion management. Barley and wheat are the main crops in the Middle East region. Moreover, many other crops are also produced worldwide, such as Fruits, vegetables, rice, corn, lentils, and chickpeas. The availability and characteristics of agricultural residues distinguished them from other solid fuels such as charcoal, char briquette, and wood.
1.2.2 Industrial Wastes
An immense quantity of organic waste and associated effluents are produced annually by food processing industries such as fruits, chips, garments, juices, and meat. These organic residues may be used as multiple sources of energy. The continually increasing population has raised the demand for food and its uses. Thus, in most of the nations, numerous food and beverage industries in this region have greatly expanded to satisfy food needs. These food and fruit industries lost around 20–40% of fruit and vegetable production annually (Dora et al. 2020). These agro-food-based waste materials show different compositions of lignin, ash, moisture, carbon, nitrogen, cellulose, and hemicellulose, which are useful for biogas production, biofuels, and some other valuable products by biochemical conversion. With increasing production by food industries, the percentage of waste generated also increased with a high value of chemical oxygen demand (COD), biological oxygen demand (BOD), and other suspended solids in it. Many of these wastes are discarded or untreated, resulting in harmful natural, human, and animal health effects, but their composition involves many organic compounds providing a range of value-added goods and reducing the manufacturing costs (Madureira et al. 2020).
After extracting oil from the seeds, enormous quantities of refined residues are made in oil industries called oil-cakes. Different varieties of oil cakes are generated after processing, such as coconut oil cake, mustard oil cake, soybean cake, cottonseed cake, rapeseed cake, palm kernel cake, olive oil cake, groundnut oil cake, sunflower oil cake, sesame oil cake, and canola oil cake. (Ramachandran et al. 2007). These industries pollute water, air, and other solid waste because these residues have vast amounts of grease, oil, suspended solids, fat, and dissolved solids. These agro-industrial residues are comparatively inexpensive, containing vast quantities of components, and can be used as substitute substrates for fermentation in an infinite prospect.
1.2.3 Drainage from Agro-Food Industries
In India, roughly 65–70% of organic contaminants are released into water bodies by food and agricultural sectors, such as distilleries, sugar mills, milk, fruit canning, and pulp and paper milling industries. The production of wine has also reached prominence in other parts of the world and is one of the leading food-processing industries in Mediterranean countries such as Australia, South Africa, Chile, China, and The US with its rising economic impact (Ganesh et al. 2010). According to the international organization of vine and wine (OIV), in 2020, global wine production was estimated at approximately 258 million hectoliters. Wine produces large amounts of wastewaters primarily from various washing procedures, e.g., when the grapes were crushed and squeezed, fermentation tanks, barrels, other machinery, and the surfaces were washed (Badshah et al. 2012). Moreover, for many Mediterranean countries, the olive oil industry has become of fundamental economic value. Malaysia currently represents 28% of the world’s palm oil production and 33% of world exports (MPOC 2020). Because of its surplus production, a large amount of contaminated wastewater is generated, commonly referred to as palm oil mill effluent (POME). An estimated 1750 million metric tons of olive oil are produced worldwide annually, with Portugal, Greece, Italy, Tunisia, and Spain are the leading producers. About 30 million cubic meters of waste oils are produced annually in the Mediterranean region in seasonal olive oil extraction (Meksi et al. 2012). The final effluent produced after the processing of coffee industries in the regions such as Colombia, Brazil, and Vietnam has created a huge environmental impact, which requires low-cost and efficient techniques for treating wastewater generated (Fia et al. 2012). Also, some agro-food wastes such as yogurt waste, milled apple waste, beverages waste, fat and oil from dairy wastewater treatment, and cattle manure have great potential for the production of methane and other biofuels.
1.3 Different Methods Used for Bioconversion of Agro-Industrial Waste
Various microbial treatments such as solid-state fermentation, composting, anaerobic digestion may employ to manage waste generated from the agro-industries. These treatment technologies are eco-friendly, cost-effective, and produce many value-added products to overcome future demand. Some of the treatment methods are discussed below:
1.3.1 Solid-State Fermentation
When non-soluble or solid organic wastes are processed in biotechnological ways in the absence or lack of water by microorganisms, it is called solid-state fermentation (Soccol et al. 2017). Residues of rice bran, rice straw, wheat bran, wheat straw, barley straw, corn, legume seeds, sawdust, wood shavings, fruits and vegetable peels, and other plant and animal products constitute the substrate for the solid-state fermentation (Singhania et al. 2009). Though these substrates are polymeric and barely soluble in water or barely soluble, they are available easily and cheaply. The process of solid-state fermentation has been given in Fig. 1.1.
Both at the lab and pilot scale, the solid-state fermentation process can occur, which results in bioconversion of organic agro-industrial waste leading to the production of active biological metabolites. The bio-products produced by the solid-state fermentation method are organic acids, aromatic compounds, enzymes, biosurfactants, bio-pesticides, bio-fertilizers, feed for animals, vitamins, antibiotics, and pigments (Thomas et al. 2013). Different industries like agriculture, paper, beer and wine, detergent, textile, food, animal feed generate large substrates for solid-state fermentation. Though the substrates used in solid-state fermentation are solids, the moisture level is low. The low-level moisture is sufficient for the fermentation process. Because of their high-water absorbing capacity, many agro-industrial wastes are being used as carriers in solid-state fermentation that help in the immobilization of fungus (Orzua et al. 2009). This helps in the efficacious growth of required microorganisms.
Through the process of solid-state fermentation, from the cheap substrates of agro-industrial solid wastes, many varieties of value-added products like tempeh, oncom, animal feed, biofuels, biogas are being prepared and sold for economic benefits (Fig. 1.2).
1.3.2 Composting
It is a managed process of converting organic matter into nutrient-rich and pathogen-free end product, i.e., compost (Fig. 1.3) (Onwosi et al. 2017). The end product is dark brown with a humus-like substance that may be stored and used as a beneficial soil amendment for agricultural applications (Onwosi et al. 2017). To carry out an efficient composting process, the temperature is the main parameter that regulates the overall composting process. According to Kulikowska (2016), the substrate’s ambient temperature and nature decide the composting process’s effectiveness and the final compost’s quality. Based on temperature gradient, there are four stages of the composting process viz.; mesophilic phase, thermophilic phase, cooling phase, and the maturation phase (Fig. 1.4) (Onwosi et al. 2017). In each phase, the microbial biomass varies within the composting pile (Hou et al. 2017).
Such temperature variation during the composting process defines the benefits of microbial populations involved in transforming available substrates into value-added products. In the initial phase, i.e., mesophilic phase, the complex organic matters get converted into simpler ones by the synergistic action of different microbial populations, which further accelerates the compost temperature and drives the composting process into the thermophilic phase (Van der Wurff et al. 2016). In the composting process, the thermophilic stage plays an important role because it eliminates pathogens, weeds, and parasites from the compost pile (Zhang et al. 2012; Hou et al. 2017). Thus, it results in pathogen-free compost (Varma and Kalamdhad 2014). Due to the limited bioavailability of substrate, the microbial population’s activity slows down in the cooling phase. As a result, this takes the composting temperature to a declining stage. Now at this phase, the microbial community, for their survival, they will compete with each other by developing strategies such as antibiotic productions (Van der Wurff et al. 2016). In the last stage, i.e., the maturation phase, there is a slow transformation in the composting pile’s microbial population. In this stage, the compost gets colonized by the microorganisms that readily depend on the available substrate (Van der Wurff et al. 2016).
1.3.2.1 Composting of Agro-Industrial Waste
Urbanization and rapid industrialization have led to increased exploitation of resources and the generation of waste in bulky volumes (Gonzalez-Salazar et al. 2016). The huge amount of nutrients rich biomass waste generated from agro-industries is disposed of and underutilized (Abdel-Shafy and Mansour 2018). With the advancement in technology and increased global research standards, scientific tools have taken place. The emerging interest in research is to control agro-industrial waste by proposing green value-added technologies focused on traditional approaches, including harsh and hazardous chemicals at high processing and waste treatment costs (Chen and Lee 2018). The biological processing of agro-industrial wastes is exciting green biotechnology with minimal harmful effects on the environment while balancing it (Zakaria et al. 2020). Microorganisms, primarily from bacterial and fungal species, are used for biological treatments to fix those problems. Bran and cereal straw (Hart et al. 2003); horticultural wastes (Lu et al. 2004; Lopez et al. 2006); Cotton, lemon tree prunings, and brewery wastes (García-Gómez et al. 2005); Grapes, olive, and palm wastes (Arvanitoyannis and Kassaveti 2007) are ideal substrates for the processing of humus-rich compost.
1.3.2.2 Various Microbial Community Involved in Carrying out the Composting Process
Conventional chemical methods for agro-industrial waste treatment have led to increased environmental pollution hampering human and animal life. Therefore, there is a demand for eco-friendly approaches to tackle such waste. In such conditions, microorganisms’ function can’t be ignored as they play a vital role in the biological method of composting to treat agro-industrial wastes into value-added products. Various microorganisms are reported to yield better compost products under improved composting conditions. These microorganisms possess various enzymatic activities directly involved in decomposing organic materials into a valuable product (Eida et al. 2009). These microbes have great potential to rapidly convert cellulosic and lignocellulosic compositions of wastes into nutrient-rich biological matter (de Souza 2013). This nutrient-rich decomposed organic matter is fruitful to enhance the activity of native important microorganisms in the soil (Meena et al. 2014; Rashid et al. 2016).
The mixture of bacterial communities, i.e., Ureibacillus thermosphaericus, Streptomyces thermovulgaris, and Bacillus shackletonni are proved to enhance the process of composting (Vargas-García et al. 2007). The inoculum of lignocellulolytic fungi (e.g., Trichurus spiralis) can be used before composting process, which will help reduce the resistance to biodegradation substrates (Hart et al. 2003; Vargas-García et al. 2007).
A decomposed product by the action of earthworm Eisenia fetida, i.e., vermicompost, is also considered to increase indigenous soil microbial diversity and encourage plant growth (Lim et al. 2015). The mixture of sawdust, guar gum waste, and cow dung in the substrate has been reported to humify by a new strain of earthworm Perionyx sansibaricus (Suthar 2007). Composting may also be viewed as a cheap technology for transforming agro-industrial waste into a value-added commodity.
1.3.3 Anaerobic Digestion
Anaerobic digestion is a method of decomposition of organic waste under anaerobic conditions with low energy requirements. It produces biogas and leftover digestate as the by-products used as renewable energy sources and fertilizer for agricultural lands. The application of anaerobes in waste management has been identified for more than hundreds of years (McCarty 2001). Generally, the waste disposal methods are employed to avoid contamination of the environment; however, anaerobic processes are used for the treatment of high organic waste content for the generation of energy in the form of biogas or biofuels. The current scenario of global greenhouse gas emission and energy disasters is encouraging green energy and advances in biotechnology to generate a new economy based on environmental and energetic factors (Holm-Nielsen et al. 2009). In this regard, principles like biorefining and energy extraction are introduced based on the biotechnological transformation of biomass. From this point of view, anaerobic digestion plays a vital role in these situations, as it generates various by-products such as methane and hydrogen at the different metabolic stage, which can be used as power sources, i.e., either in boilers, internal combustion engines, or fuel cells.
The fermentation of methane is a dynamic mechanism separated into four stages: hydrolysis, acidogenesis, acetogenesis, and methanogenesis (Pereda Reyes and Sárvári Horváth 2015) (Fig. 1.5). Diverse microorganisms execute the degradation steps, which are partially interrelated syntrophically and have different environmental requirements. Hydrolytic bacteria were the first group of microorganisms. These species hydrolyze polymeric compounds by extracellular hydrolytic enzymes (cellulase, xylanase, amylase, protease, lipase) into monomers such as glucose and amino acids (Weiland 2010). These microbial communities include some strict anaerobes such as Clostridia, Bifidobacteria, Bacteriocides, and some facultative anaerobes also take parts, such as Streptococci and Enterobacteriaceae. The acidogenic bacteria are the second category of microorganisms that transform carbon dioxide, hydrogen, ammonium, and other organic acids from sugars and amino acids. The third type of bacterial species involved is hydrogen-producing acetogenic bacteria, such as Clostridium acetium, Acetobacterium woodii, which converts volatile fatty acids into acetate and hydrogen. Two different groups of strictly anaerobic bacteria produce methane as a final product from acetate (Acetotrophic pathway) or hydrogen and carbon dioxide (hydrogenotrophic pathway) at the end of the degradation process. Very few microorganisms, i.e., Methanotrix soehngenii, Methanosarcina barkeri, and Methanococcus mazei can degrade acetate into methane and carbon dioxide, whereas hydrogen can be used to form methane by all methanogenic bacteria such as Methanobacteriales and Methanomicrobiales (Batstone et al. 2002).
Anaerobic digestion occurs at three different temperatures depending on the climate conditions, thermophilic (55–60 °C), mesophilic (35–37 °C), and psychrophilic (below 20 °C). Thermophilic and mesophilic temperatures are often used for industrial applications due to higher process stability, methane yields, and fewer energy requirements (Alatriste-Mondragón et al. 2006). The proper implementation of anaerobic digestion relies heavily on how the composition of waste to be digested (Murto et al. 2004). Solid waste treatment varies from liquid waste treatment, as solubilization and hydrolysis of particle material may be the limiting step in the process. To enhance mass transfer phenomena and ensure the proper interaction between the biomass and the substrate, waste mixing must be carried out correctly. If the microorganisms involved in the process are not separated from the solid wastes to be decayed, the retention time is generally 50–60 days in the digester; otherwise, microorganisms may wash out from it. On the other hand, in the wastewater bioreactor system, microorganisms’ retention time will be decoupled from liquid retention results into reduced hydraulic retention time to a few hours. The microbial treatments of agro-industrial waste generally remove pathogens and other organic compounds from the effluent, but due to high particulate and fat contents, anaerobic digestion is complicated in slaughterhouse industries (Batstone et al. 1997). Still, anaerobic digestion remains a viable alternative for the treatment of these kinds of waste materials, as they have a high potential to generate biogas only because of their high protein and fat content.
On the other hand, agro wastes are composed of major biodegradable components, i.e., cellulose and hemicellulose linked with lignin. Compared to carbohydrates, these organic compounds produce low amounts of methane (up to 50% methane) under anaerobic conditions due to the low biodegradability and sheltering effect of lignin. But several agro wastes are favorable for anaerobic digestion as they can degrade 80% of their fiber content, such as paper and rice residues (Esposito et al. 2011) (Contreras et al. 2012). For the anaerobic treatment of agro-industrial drainages, several reactor configurations are used:
1.3.3.1 Completely Stirred Anaerobic Digester
The continuous stirred tank reactor is the earliest and basic high-rate system for the anaerobic treatment of wastewater with a high amount of suspended solids and organic industrial waste. It a stable and reliable anaerobic treatment system with an equally solid retention time and hydraulic retention time of 15–40 days for the proper treatment and process (Del Real Olvera and Lopez-Lopez 2012). In this system, alternate and continuous mixing is helpful to suspend the microorganism in the digester, which results in better substrate-sludge contact, but it requires a significant amount of energy and is labor-intensive (Mao et al. 2015). Another drawback of this method is that only high volumetric waste sources with a biodegradable COD content range between 8.000 and 50.000 mg/L attain a high loading rate, but many waste sources are diluted considerably. A single continuous stirred tank reactor system is easy to operate but produces poor quality effluent. So, a two-phase treatment system is employed and is most common these days. The two-stage continuous stirred tank reactor system is comparatively simple in design and cost-effective for the treatment of wet digesters. However, the system’s sensitivity to substrates with high organic loads and the complicated operation leads to fewer alternatives to increase the two-phase system’s digestive efficiency (Boe and Angelidaki 2009). Different variants of continuous stirred tank reactors are currently constructed to enhance the reactor’s performance by optimizing the reactor volume. To increase the reactor’s microbial load, gravity sedimentation tanks or membrane bioreactors are used in series with continuous stirred tank reactors for a more effective digestion process. For the treatment of dairy wastewater, a two-phase anaerobic system of continuous stirred tank reactor and up-flow anaerobic filters are used under various operating conditions, but a high concentration of suspended solids affects treatment efficiency (Mao et al. 2015).
1.3.3.2 Upflow Anaerobic Sludge Blanket Reactor
Upflow anaerobic sludge blanket reactor is a compact system that requires a small area to operate with low maintenance and expenditure costs, low energy usage, and low production of sludge continuously feeding the up-flow anaerobic sludge blanket reactor from the bottom, creating an up-flow stream towards the upper outlet through the sludge bed consisting of aggregated microbes and granular biomass. With the upward movement of effluent, its velocity decreases, providing greater area and enhancing the process’s solid retention time and efficiency. Upflow anaerobic sludge blanket reactor systems can achieve better settlement ability, high biomass concentrations, short retention time, strong solids/liquid isolation, cost removal of packaging content, and very high loading rate operations. The removal efficacy of chemical oxygen demand is about 65%, and biochemical oxygen demand is 75% in up-flow anaerobic sludge blanket reactor type reactor system. Also, highly concentrated sludge is produced with better dehydration capacity. Although the sludge acclimation is vital for start-up only, after long periods of disrupted functioning, reactor output can be resumed. This method is generally restricted by the high solid suspended content in wastewater to be treated, which prevents the production of dense granular sludge, and sometimes foul smell occurs due to the inappropriate nature or installation of the gas collection system and low tolerance of toxic charge.
1.3.3.3 Fluidized and Expanded Bed Reactors
In an anaerobic fluidized bed reactor, bacteria are grown and attached on small granular particles such as alumina or sand and activated carbon. These particles are suspended by a fast-upward flow of wastewater, allowing resistance to inhibitors and a higher organic loading rate level. Organic loading rate of 10–20 kg COD/m3d−1 can be used in an anaerobic fluidized bed reactor (Siqueira et al. 2013). The high rate of flow around the particles covered with a thin biofilm layer of methanogens results in good mass transfer. Less clogging of the latter allows the short-circuiting and larger surface to volume ratio of the carrier in the reactor, making the anaerobic fluidized bed reactor more efficient than up-flow anaerobic sludge blanket reactors. Also, an anaerobic fluidized bed reactor is cheaper due to the reduced volume of the reactor, and it is better than an up-flow anaerobic sludge blanket in terms of removing the suspended solid particles from wastewater (Mao et al. 2015). However, the key disadvantages of this method are the difficulties of producing a tightly attached biofilm containing the right mix of methanogens, the risk of detachment of microorganisms, the harmful consequences of dilution near the inlet due to high recycling rates more cost of energy. The expanded granular sludge bed reactor is a variant of the anaerobic fluidized bed reactor with a variation in the fluid’s upward flow rate (Del Real Olvera and Lopez-Lopez 2012).
1.3.3.4 Anaerobic Filters Reactors
The Anaerobic Filters are designed to support the intimate interaction between the waste and bacterial population, thereby providing a longer retention time for biomass than hydraulic retention time. They are used to treat various wastewaters produced from dairy, beverages, chemical, and food processing industries. Anaerobic filters are a widely used anaerobic digestion process due to the high organic loading rate. The anaerobic filter is generally made up of different materials such as ceramic, charcoal, plastic materials, sintered glasses, seashells, limestones, and pumice clay (Karadag et al. 2015). These are designed with at least two filtration compartments arranged in a manner. At the anaerobic filters, biomass can degrade the organic material found in wastewater and then bind outside the filter material. Furthermore, these anaerobic filters are commonly used as an optional treatment to increase solid elimination. The anaerobic filters need to be able to use sufficient packaging media because the media’s chemical and physical properties have a crucial influence on biomass and its reactor efficiency. The anaerobic filter is generally packed with various packaging materials to contain the bacteria in the voids. The ideal packaging media increases the surface area and extends anaerobic filters’ porosity, increasing the biomass link, decreasing the reactor’s volume, and restricting channel obstruction. Some researches show that anaerobic filters remove 80% of chemical oxygen demand with a maximum organic loading rate capacity of 19 and 17 g COD L−1d−1 of wastewater generated from cheese, dairy, and fruit canning industries (Rajagopal et al. 2013). These days, researchers concentrate on using industrial by-products for the natural application of anaerobic filters, as it is more efficient for the treatment of wastewaters with a low level of suspended solids. Also, anaerobic filters have some advantages like minimum nutrients reduction and require further treatment of effluents.
1.4 Recycled Value-Added Products from the Microbial Treatment of Agro-Industrial Waste
The scientific community uses various agro-industrial wastes and effluents through green and recycling technologies to overcome the existing global environmental health. The agro-industrial wastes are used for the production of many value-added products such as biofuels, enzymes, and biofertilizers based on their composition, i.e., lignocellulose, proteins, polyphenols, and carbohydrates. Some of the products are discussed below:
1.4.1 Some Important Enzymes from Agro-Industrial Waste
1.4.1.1 Alpha and Beta-Amylase
Alpha-amylases (E.C 3.2.1.1) cleave α-D-(1,4) glycosidic linkages between the glucose subunits in starch, glycogen, and other related polysaccharides. They have a wide variety of applications in food, detergent, textile, paper, pulp, distilleries, and pharmaceutical industries (Ramachandran et al. 2004). They are derived from many organisms, such as plants, animals, and microorganisms (Far et al. 2020). At the industrial level, they are produced by both submerged fermentation and solid-state fermentation using genetically improved microorganisms such as Bacillus and Aspergillus species (Sundarram and Murthy 2014). Agro-industrial residues act as a favorable substrate for the production of α-amylases, mainly due to their high lignocellulosic content and low economic cost. In literature, the production of this enzyme is primarily emphasized by solid-state fermentation. In some of the earlier studies, banana waste, rice husk, coconut oil cake, sugarcane bagasse, corn cob, and spent brewer’s grain has been used for the production of amylase (Ramachandran et al. 2004; Anto et al. 2006; Aliyah et al. 2017).
β-amylases (E.C. 3.1.2.3), also known as glucoamylases, cleave the α-1,4linkages found in starch and other carbohydrates to release glucose molecules. It also hydrolyses α-1,6 glycosidic bonds at slower rates. Thus, an exoamylase releases glucose moieties from the non-reducing end of the carbohydrates (Espinosa-Ramírez et al. 2014). They are very useful in the bakery and brewery industry (Diler et al. 2015). They are produced by several bacterial and fungal species like Aspergillus, Bacillus, Saccharomyces, and Rhizopus (Singh and Soni 2001; Shin et al. 2000). Vegetable waste such as cassava, yam, and banana peels has been used as a carbon source for glucoamylase production (Adeniran et al. 2010).
1.4.1.2 β-Glucanase
β-glucans are polysaccharides made of D-glucose monomers linked through β-1,3 and β-1,4 glycosidic linkages. They form a major part of the cell wall polysaccharide of cereal endosperm and comprise approximately 5.5% of the dry weight of grains (Dais and Perlin 1982). Besides cereal endosperm, they can also be found in natural products like mushrooms, yeast, oats, and algae (Zhu et al. 2016). Fungi produce glucans with β-1,3, β-1,4, and β-1,6 bonds, which also exhibit antitumor activity (Latgé 2010). Based on the cleavage of glycosidic bond, β-glucanases are classified as β-1,4-glucanase (EC 3.2.1.4), β-1,3(4)-glucanase (EC 3.2.1.6), β-1,3-glucanase (EC 3.2.1.39), and β-1,3-1,4-glucanase (EC 3.2.1.73) (Ueda et al. 2014). Microorganisms like Fusarium oxysporum, Bacillus subtilis, and Penicillium echinulatum have been reported to produce high endo and exoglucanase levels when grown on biomass sources (Ravindran et al. 2018). They have applications in brewing, detergent, and animal feed industries (Chaari and Chaabouni 2019).
1.4.1.3 Cellulase
Cellulases are a group of enzymes involved in the depolymerization of cellulose. They comprise three enzymes endoglucanase (E.C. 3.2.1.4), exoglucanase or cellobiohydrolase (E.C. 3.2.1.176) (E.C. 3.2.1.91), and β-glucosidase (E.C. 3.2.1.21). They play a very important role in biofuel production using different lignocellulosic materials (Castro and Pereira Jr 2010). Besides bioethanol, they have applications in food, detergent, paper, pulp, and textile sectors (Ferreira et al. 2014). They are secreted by several microorganisms like bacteria, fungi and actinomycetes (Zverlov et al. 2015). Clostridium thermocellum, Proteus vulgaris, Bacillus circulans, Escherichia coli, Klebsiella pneumonia, and Cellulomonas are the bacteria involved in the production of Cellulases (Ravindran et al. 2018). Simultaneously, fungal species such as Melanocarpus, Schizophyllum, Penicillium, Aspergillus, Trichoderma and Fusarium produce these enzymes (Juturu and Wu 2014). Studies have been conducted in the literature to use fruit peels and spent brewer’s grain to be used as a substrate for cellulase production by Trichoderma sp. (Sim and Oh 1990; Nadar and Rathod 2019).
1.4.1.4 Hemicellulase
Hemicellulose is a branched heteropolysaccharide consisting of different hexoses and pentoses, including glucose, fructose, galactose, arabinose, xylose, mannose, glucuronic acid, and galacturonic acid. It accounts for 20–30% of the total wood (Collins et al. 2005) and is generally amorphous in nature. Hemicellulases are the enzymes that break β-1,4-glycosidic bonds present in the backbone of hemicellulose. They are produced both by bacterial and fungal strains, namely Clostridium, Bacillus, Geobacillus, Trichoderma, and Aspergillus (Shallom and Shoham 2003). The most common hemicellulases are xylanases, mannanases, glucuronidases, galactosidases, and arabinofuranosidases (Obeng et al. 2017). They also play a crucial role in the paper, pulp, biofuel, food, and pharmaceutical industries. Studies have been conducted on using corn cobs, apple pomace, and palm oil effluents as a substrate for hemicellulases production (Zainudin et al. 2013; Dhillon et al. 2012; Kheiralla et al. 2018).
1.4.1.5 Xylanase
Xylan is a complex polysaccharide made of β-1,4-linked xylose residues. It is the most abundant type of hemicellulose present in nature (Beg et al. 2001). The backbone made of xylan residues have the side branches of d-glucuronic acid and d-glucuronic acid (4-O-methyl α-1,2 linked) or d-arabinofuranose (α-1,2 or α-1,3 linked), and O-acetyl groups (Bastawde 1992). The branches play an important role in the cross-linking of cellulose microfibrils and lignin through ferulic acid residues. The extent of branching depends on the source of xylan. Because of its heterogenous nature and complex structure, xylan requires several enzymes, namely endoxylanases, β-xylosidases, ferulic acid esterase, p-coumaric acid esterase, acetyl xylan esterase, and α-glucuronidase (Bhardwaj et al. 2019). They all form a class of xylan degrading enzymes called xylanases (E. C. 3.2.1.8). Xylanases have been isolated from different microorganisms, such as Aspergillus Chytridiomyces, Streptomyces, Trichoderma, Phanerochaete, Clostridium, Fibrobacter, Bacillus, and Pichia (Collins et al. 2005). Several agro-industrial wastes such as wheat straw, wheat bran, rice husk, and sugarcane bran have been used to produce xylanases at very low cost (Pandya and Gupte 2012; Membrillo Venegas et al. 2013).
1.4.1.6 Mannase
Mannan is the second most abundant hemicellulose in nature. It comprises linear mannan, glucomannan, galactomannan, and glactoglucomannan. The enzymes involved in the depolymerization of linear mannan are β-mannanase (EC 3.2.178), β-mannosidase (EC 3.2.1.25), β-glucosidase (EC 3.2.1.21), acetyl mannan esterase (EC 3.1.1.6), and α-galactosidase (EC 3.2.1.22) (Moreira 2008). β-mannanases cleave the internal glycosidic bonds and release short-chain manno-oligosaccharides, whereas β-mannosidases hydrolyze mannan from the non-reducing end releasing individual mannose unit (McCleary and Matheson 1983; Gomes et al. 2007). They are produced by several bacterial and fungal species: Bacillus circulans, Clostridium cellulolytic, Trichoderma reesei, Agaricus bisporus, Aspergillus aculeatus (Moreira 2008). They have applications in paper, pulp, food, and textile industries (Clarke et al. 2000; Naganagouda et al. 2009). Abdeshahian et al. has used palm kernel to produce β-mannanases using the fungi Aspergillus niger (Abdeshahian et al. 2010). Apple pomace, cottonseed powder, and locust bean have also been observed as excellent substrates for the production of mannases (Gomes et al. 2007; Yin et al. 2013).
1.4.1.7 Pectinase
Pectin is a widely distributed carbohydrate polymer in plants. It is a complex polysaccharide made of galacturonic acid residues linked by α-1,4 linkage. The acid groups along the chain are largely esterified with methoxy groups in the natural product. There can also be acetyl groups present on the free hydroxy groups. Pectinases are a group of enzymes that degrade pectic substances and release comparatively simpler compounds based on their mode of action. The linear pectin chain is generally cleaved by endo-polygalacturonases (EC 3.2.1.15) and exo-polygalacturonases (EC 3.2.1.67) from inside and at the terminal, respectively (Rytioja et al. 2014). Pectinlyases (EC 4.2.2.10) and pectate lyases (EC 4.2.2.2) also cleave the pectin backbone. Whereas the branched region is degraded by rhamnogalacturonan acetylesterase (EC 3.1.1), pectin acetyl esterase (EC 3.1.1), and pectin methylesterase (EC 3.1.1.11) (De Vries and Visser 2001). Pectinases are produced by bacterial, fungal, and yeast strains, namely Bacillus, Paenibacillus, Chryseobacterium, Pectobacterium, Aspergillus, Fusarium, Penicillium, Rhizopus, Botrytis, Fusarium, Trichoderma, Rhodotorula (Singh et al. 2019). They have applications in the fruit, paper, pulp, textile, and animal feed industries. They have also been used in coffee and tea fermentation (Sharma et al. 2013).
1.4.1.8 Inulinase
Inulin is produced by several plants such as banana, garlic, chicory, onion, garlic, barley, wheat, barley, and rye (Kaur and Gupta 2002). It is classified as an oligo or polysaccharide, depending upon its chain length. It consists of D-fructosyl moieties linked by β-2,1 glycosidic bond terminating with α-1,2 bonded D-glucosyl group (Ronkart et al. 2007). Inulinases are defined as a group of enzymes involved in the degradation of inulin. They mainly consist of exo-inulinases (β-D-fructanfructohydrolase, EC 3.2.1.80) and endo-inulinases (2,1-β- D -fructanfructohydrolase, EC 3.2.1.7) based on their mode of activity (Vijayaraghavan et al. 2009). They are shown to produce by Streptococcus, Pseudomonas, Xanthomonas, Chrysosporium, Actinomyces, Penicillium, Aspergillus, Kluyveromyces species. They have applications in lactic acid production, 2,3 butanediols, biofuel, sugar alcohols, fructose syrup, and inuloorligosaccharides (Liu et al. 2013; Chi et al. 2009). Recently, coconut oil cake, sugarcane baggase, and rice bran have been used for the synthesis of inulinases (Onilude et al. 2012; Singh and Chauhan 2018; Mazutti et al. 2006).
1.4.1.9 Laccase
Laccases (E.C. 1.10.3.2) are aromatic compounds oxidizing enzyme which belong to a multi-copper oxidase family. They oxidize a wide variety of phenols, heterocyclic compounds, and aromatic amines. They catalyze the oxidation of their substrates with the help of molecular oxygen. They play a crucial role in dye, bleaching, pulp, and industrial effluent treatment. They have also been explored for the degradation of lignin, herbicides, and pesticides (Ravindran et al. 2018). They are produced by bacteria, fungi, plants, and insects. The bacterial and fungal species involved in the production of laccases are Bacillus subtilis, Streptomyces lavendulae, Azospirillum lipoferum, Pleurotus ostreatus, Trametes versicolor. (Kiiskinen et al. 2004). They can be produced using groundnut, banana peel, rice straw, orange peel, and wheat bran from agro-industries as substrate (Singh and Gupta 2020).
1.4.1.10 Phytase
Phytates are defined as naturally occurring phosphate-rich compounds found in cereals, oilseeds, and legumes. The enzyme that catalyzes the release of phosphates from phytates is known as phytase (EC 3.1.3.8) (Hussin et al. 2007). Phytases are classified based on their stereospecificity of hydrolysis. The enzymes that cleave at the C3 and C6 positions of phytic acid are classified as 3-phytases (EC 3.1.3.8) and 6-phytases (EC 3.1.3.26), respectively. Mostly, 3-phytases are produced by the microorganisms; on the other hand, 6-phytases by plants. They are produced by different bacterial, fungal, and yeast genera, namely Klebsiella, Bacillus, Shigella, Selenomonas, Rhodotorula, Aspergillus (Pandey et al. 2001). Ruminants produce phytases for the proper digestion of phytate-rich food, whereas monogastric animals do not produce this enzyme. Treatment of animal feed with phytases increases the bioavailability of minerals, thus improving its nutritional value. The phytases are important for poultry, pig, baking, and bioethanol industries. They can be produced using residues from agricultural industries and fruit peels as substrate, thus pointing towards their low-cost synthesis (Bajaj and Wani 2011).
1.4.1.11 Invertase
Invertase (EC.3.2.1.26) is a glycoprotein that catalyzes the hydrolysis of sucrose into glucose and fructose. They mainly hydrolyze β-1,2 linkage present between the glucose and sucrose units. They are also known as β-D-fructofuranosidase because of their ability to release fructose from the non-reducing terminal of β-D-fructofuranoside substrates (Linde et al. 2009). Sucrose hydrolysis is generally carried out using hydrochloric acid with only 50–60% efficiency, whereas the employment of invertase enzyme improves the efficiency of this reaction up to 100% and without yielding any impurities (Ravindran et al. 2018). Invertase is shown to be present in Bacillus cereus, Lactobacillus reuteri, Brevibacterium sp., Arthrobacter sp., Streptomyces sp., Zymomonas mobilis, Saccharomyces cerevisae, Candida utilis, Aspergillus niger, and Penicillium chrisogenum (Lincoln and More 2017). Recently, wheat bran, fruit waste, and bagasse waste have been observed as excellent carbon sources for the low-cost production of invertase (Ravindran et al. 2018).
1.4.1.12 Protease
Proteases (EC 3.4.21.62) are a group of enzymes that perform the hydrolysis of peptide bonds and release small peptides or free amino acids. They are also known as proteinases. They are a crucial industrial enzyme that accounts for approximately 70% of the total enzymes produced worldwide (Meena et al. 2013). They are widely distributed in living organisms as they are crucial for various physiological processes. They can be classified as acidic, alkaline, and neutral proteases. The alkaline (EC.3.4.21–24.99) and acidic proteases cleave proteins between pH range 9–11 and 3–4, respectively (Razzaq et al. 2019). They are found in plants, animals, and microorganisms. Among microbes, they are produced by Bacillus licheniformis, Bacillus stearothermophilus, Pseudomonas aeruginosa, Lactobacillus acidophilus, Aspergillus oryzae, Penicillium, Rhizopus (Singh et al. 2019; Razzaq et al. 2019). They are important in the food, feed, leather, silk, and textile industries. Alcalase, Neutrase, and protease are some of the commercially available proteases. Tomato pomace, soybeans, and jatropha seed cakes have been used as a substrate for protease production (Ravindran et al. 2018).
1.4.1.13 Pullulanase
Pullulan is a maltotriose trimer made up of α-1-4 and α-1-6-linked triglucosides. Due to the existence of both α-1-4 and α-1-6 in this compound, it is seen as an intermediate between the amylose and dextran structure. Pullulan is insoluble in non-polar compounds but is soluble in water. It has high mechanical strength thus can be used for a gelling agent, capsule, and thin-film formation (Farris et al. 2014). The enzymes used to depolymerize pullulan are mainly classified as pullulanase (EC. 3.2.1.41), isopullulanase (EC.3.2.1.57), and neopullulanase (EC.3.2.1.35). The pullulanase is further divided into type-I and type-II, which cleave only α-1,6-glycosidic linkage and α-1,4 & α-1,6-glycosidic linkages, respectively. They are essential for the baking and starch industries (Hii et al. 2012). They are synthesized by Klebsiella pneumoniae, Bacillus cereus, Bacillus macerans, Streptomyces mitis, Clostridium sp.., Thermus aquaticus, Thermoanaerobacter sp., Saccharomyces sp., Aspergillus sp., Cladosporium sp. (Saha and Zeikus 1989; Tomasik and Horton 2012). Agricultural waste materials such as wheat, rice, and corn bran can be used for its cheap production (Zhang et al. 2020; Reddy et al. 2000).
1.4.1.14 Lipase
Lipases (EC 3.1.1.3) are a group of hydrolases that catalyze the breakdown of triglycerides to glycerol and fatty acids. They also carry out hydrolysis, transesterification, alcoholysis, aminolysis, acidolysis, and esterification, which are important industrial processes (Ravindran et al. 2018). They are crucial in the cosmetic, food, detergent, and pharmaceutical industries. They are well distributed in plants, animals, and microorganisms. Among microbes, they are produced by bacterial, yeast, and fungal strains such as Bacillus, Serratia, Burkholderia, Candida, Rhodotorula, Aspergillus, and Penicillium (Treichel et al. 2010). They are extracellular enzymes and are greatly influenced by physicochemical factors like pH and temperature. They are inducible enzymes and are synthesized when an inducer such as fatty acid, oil, and triglycerols are present in the medium. Agricultural residues like oil cake, fruit peels, and bean waste have been used for the cheap production of lipase (Godoy et al. 2011; Pereira et al. 2019).
1.4.2 Bioethanol Production
Due to the rise in population and rapid industrialization, energy demands have increased worldwide. The excessive consumption of fossil fuels, such as natural gas, oil, coal, and petroleum, has resulted in higher pollution levels. The increased pollution, especially due to the accumulation of large amounts of greenhouse gases, causes a change in the earth’s climate. It has also been suggested that petroleum-based fuels will deplete in the near future; thus, due to their harmful effects and limited supply, these non-renewable sources should be replaced with better environment-friendly energy resources. Biofuels are the most feasible alternate for traditional fuels as they reduce our dependency on fossil fuels and do not disturb the balance of the earth’s atmosphere. Both bioethanol and biodiesel have been seen as a supplement of gasoline and diesel, respectively. The global bioethanol production was approximately 66.77 billion liters in 2008, which was increased to 90.38 billion liters in 2014 (Gupta and Verma 2015).
The countries like the USA and Brazil produce bioethanol using corn and sugarcane, respectively, which account for 62% of the total global production (Kim and Dale 2004). The utilization of sugars and starch is not widespread in bioethanol generation, mainly due to their high food value. Recently, it has been observed that lignocellulosic biomass and agricultural crop waste can be used for bioethanol production. They are cheap sources and present in large amounts, so their employment for bioethanol production provides a route for their effective utilization. Agro-residues like wheat straw, rice straw, corn straw, fruit peels, sugarcane bagasse, and oil cakes now have significant interests. Rice straw is the highest agricultural waste and can produce 205 billion liters of bioethanol per year (Sarkar et al. 2012). Physical, chemical, and biological pre-treatments are required to generate bioethanol from agricultural waste materials.
Lignocellulosic material consists of cellulose and lignin linked with hemicellulose chains. A pre-treatment process is required for the breakdown and release of these components. It makes lignocellulose susceptible to hydrolysis and makes the release of monomer sugars easy (Mosier et al. 2005). There are three types of pre-treatment processes, i.e., physical, chemical, and biological treatments. The physical pre-treatment process for bioethanol production involves mechanical methods such as milling, grinding, and chipping. The amount of power used to crush the material mainly depends on the particle size, nature, and moisture content of the waste (Buaban et al. 2010). The mechanical processes disrupt the structure of lignocellulose and decrease its particle size to increase the surface area for enzymatic hydrolysis (Kumar et al. 2008). Besides mechanical processes, physical pre-treatment also includes uncatalyzed steam-explosion, high-energy radiation, and liquid hot water treatment (Fig. 1.6). The steam explosion aids in the loosening of lignocellulosic structure and releases pentose, but it has a disadvantage of generating cellulase inhibitory compounds, which later interfere with enzymatic hydrolysis of this substrate (Gupta and Verma 2015). The high-energy treatment is provided by heating in a microwave oven or electron beam irradiation. The microwave irradiation leads to the vibrations in the bonds present in the exposed biomass and heats it from inside. It leads to the explosion effect, thus disrupting the recalcitrant structures of lignocellulose (Hu and Wen 2008). The liquid hot water treatment employs compressed hot water to hydrolyze the lignocellulosic biomass and release sugar monomers (Sarkar et al. 2012).
Chemical pre-treatment methods make use of dilute acids, alkali, organic solvents, and ammonia. This process utilizes a chemical impact to access the lignocellulosic matrix. However, this method produces certain inhibitors that later interfere with enzymatic activity in downstream processing and affect the entire economy of bioethanol production. On the other hand, the biological treatment uses microorganisms like brown rot, white rot, and soft rot fungi. White and soft rot fungi degrade both cellulose and lignin, whereas brown rot fungi only attack cellulosic material. The hydrolysis rate is lower in biological treatment, but it requires low energy and mild environmental conditions. Most of the sugar released after biological treatment are still in the form of oligomers and still needs to be hydrolyzed by specific microbes before fermentation (Prasad et al. 2007). Enzyme hydrolysis is also necessary to convert sugars to simple monomers. The cellulases and hemicellulases producing microorganisms such as Clostridium, Cellulomonas, Thermonospora, Bacillus, Streptomycetes, Bacteriodes, Acetovibrio, Ruminococcus, Erwinia, Microbispora, Trichoderma, Penicillium, Fusarium, Phanerochaete, Humicola, Schizophillum, release hexoses and pentoses upon acting on lignocellulosic substrate materials (Gupta and Verma 2015). The cellulases which are involved in the degradation are endoglucanase (E.C. 3.2.1.4), degrading the low crystallinity regions, exoglucanase (E.C. 3.2.1.91) removing the cellobiase units from the free chain terminal, and finally, βglucosidase (E.C. 3.2.1.21), which cleave cellobiose units into glucose (Castro and Pereira Jr 2010). The hemicellulases consist of a mixture of enzymes, namely xylanases, mannases, glucuronidases, galactosidases, and arabinofuranosidases (Obeng et al. 2017). Fermentation and distillation are the final steps for the production of bioethanol. For industrial purposes, microbes with a broad substrate range, higher temperature tolerance, and high ethanol yields are essential. As such microbes’ recognition becomes difficult, genetically modified microorganisms are employed to utilize the sugars spent for efficient bioethanol production. It has been reported that Saccharomyces can theoretically yield around 90% ethanol from glucose (Spindler et al. 1992).
The most common fermentation processes are simultaneous saccharification and fermentation and separate hydrolysis and fermentation. Other agricultural remains like bagasse, fruit peels, wheat straw, almond shells, rice straw, sorghum, and corn cobs can be used to efficiently produce bioethanol (Quintero et al. 2011; Gupta and Verma 2015).
1.4.3 Biofertilizers
Targeting agro-industrial waste represents a possible source for developing biofertilizers that can be used as a soil conditioner in agro-ecosystem to yield high crop productivity (Sadh et al. 2018). The term biofertilizer is defined as the preparations which contain living microorganisms that play a crucial role in providing nutrients to the plants. These biofertilizers accelerate specific microbial processes such as nitrogen fixation, ammonia production, indole acetic acid production, siderophore production, phosphate solubilization, and potassium mobilization into the soil and boost up the nutrient availability for easy assimilation by the plants (Devi and Sumathy 2017). Hence biofertilizer plays a vital role in nutrients management (Devi and Sumathy 2017). To develop biofertilizers, several microbial populations and their close association with plant hosts are being exploited.
1.4.3.1 Diversity of Microbial Biofertilizers
The biodiversity of microbial biofertilizers includes nitrogen fixers, phosphate mobilizers, phosphate solubilizers, phosphate mobilizers (Devi and Sumathy 2017), potassium solubilizers, potassium mobilizers (Parmar and Sindhu 2013; Yadav 2018), and plant growth-promoting rhizobacteria (Devi and Sumathy 2017) (Table 1.1).
1.4.3.2 Production of Biofertilizers Using Agro-Industrial Waste
The generation of agro-industrial waste is a huge problem, and at the same time, its maintenance is a major concern. The agro-industrial wastes can be an alternative source to derive biofertilizers for agro-ecosystem and sustainable development (Sadh et al. 2018). solid-state fermentation and submerged fermentation are substrate-based fermentations processes, which are extensively used for producing biofertilizers at a large scale. Agro-industrial waste like soluble sugars, liquid synthetic media, extracts of fruit and vegetable, and dairy by-products are used in biofertilizer production (Suthar et al. 2017). Such waste contains high nutritional components in the form of proteins, sugars, and minerals, which offers a hostile environment for the growth of several microorganisms (Sadh et al. 2018). The agro-industrial waste such as corn steep liquor, molasses, deproteinized leaf extracts, jaggery, wastewater sludge is utilized as a substrate for the cultivation of Rhizobium species (Suthar et al. 2017). Moreover, agricultural waste such as bagasse, paper pulp, wheat bran, vegetable, watermelon, papaya, pineapple, custard apple, guava, rice straw is also being used routinely as a source for biofertilizer production using the fermentation process (Devi and Sumathy 2017; Suthar et al. 2017; Sadh et al. 2018).
1.5 Potential Outcomes from Microbial Treatment of Agro-Industrial Waste
Improper management of high-value waste from agro-industries will lead to many environmental and health-related issues. Proper treatment of these waste residues can be helpful in many aspects, such as reducing greenhouse gases, being used as a renewable energy source, and improving environmental and human health.
1.5.1 Greenhouse Gases Emission Reduction
Greenhouse gases that consist of CO2, CH4, NOx, SOx, H2O are natural temperature regulators for the Earth by trapping solar radiation’s heat. In the lacuna of these gases, the earth would be a cold planet. But excess of these gases along with synthetic gases like CFCs, HFCs, PFCs, SF6, and NF3 (Department of Environment and Energy 2018). These greenhouse gases are increasing at an alarming rate due to massive industrialization and improper agricultural practices. As it is aptly said, excess of anything is toxic or has a catastrophic effect. This is the reason the earth and earthlings are suffering from global warming.
Currently, the agro-industrial waste with a very high potential energy recovery is being dumped in landfills or left on the fields. These methods of waste disposal lead to an incessant generation of GHGs, mainly CO2 and CH4. Anaerobic decomposition is the prevailing process through which the anaerobic microorganisms generate methane. The crop leftovers release nitrous oxide (N2O) by the microbial action, which involves nitrifying and denitrifying microorganisms (Portugal-Pereira et al. 2015). One of the mains sources of greenhouse gases in milk production industries comprises enteric fermentation (CH4), feed purchased (N2O, CO2, CH4), manure management (N2O), manure fertilizers, and energy (fuels and electricity). Instead of utilizing the agro-industrial waste for animal feed, it is more effective if it is put to energy production because the milch animals, when fed with the waste, will generate more greenhouse gases. The waste, when used as biofuel, will be carbon neutral (Fig. 1.7). There is a drastic decrease in enteric methane production through the feed involving tomato waste (Pardo et al. 2016).
There is an immediate need for abatement to reduce the emission of greenhouse gases. One of the eminent steps to do so is through bioprocessing of agro-industrial waste. Fossil fuels are the greatest source of greenhouse gases. The combustion of fossil fuels emits massive CO2. Moreover, fossil fuels are diminishing at a very proliferating rate. To curb this burden, bioenergy from agro-industrial waste helps in dual ways.
Firstly, it reduces the dependency on fossil fuels. Secondly, it reduces the emission of greenhouse gases. The trash from crops like sugarcane, maize, and soybean is a readily available substrate for bioenergy production in Brazil, where it was estimated that around 141 TWh/year of environmentally sustainable potential is achieved in different regions, mainly the South, Southeast, and Midwest regions of Brazil (Portugal-Pereira et al. 2015).
1.5.2 Renewable Source of Energy
Today’s global economy relies mainly on a range of fossil fuels such as oil, natural gases, and coal used to manufacture fuel, electricity, and other uses. A sustainable alternative needs to be sought for the world’s increased energy demand due to population growth. As fossil fuel stocks are limited, world annual petroleum production will start to decrease in the coming future, leading to the use of renewable sources as alternative options. As the energy industries rely on solar, water, wind, and geothermal heat as renewable sources of energy, biomass generated from agro-industries can be an alternative source for fuel production and chemical industries (Sarkar et al. 2012). These fossil fuels may be replaced by bioethanol production as a renewable source through waste generated from agro-industries. In 2004, Kim and Dale reported that lignocellulosic biomass would generate 442 billion liters of bioethanol, and 491 billion liters can be generated from total waste crop residues every year, 16-folds greater than the current world bioethanol supply. This can be accomplished through different processes, such as enzymatic decomposition, physio-chemical treatments, pyrolysis, and solid-state fermentation (Yusuf 2017). The use of agro-industrial biomass for electricity generation appears to be an energy option and mitigates carbon dioxide emissions as fossil fuels are minimal and non-renewable. The Inexpensive agricultural biomass wastes such as oil residues, energy crops, and other organic materials generated from agro and food-based industries may be utilized to produce renewable energy (Guldhe et al. 2017).
1.5.3 Improvement in the Environment and Human Health
A massive amount of agro-industrial wastes are dumped in landfills, left on the fields, or drained into rivers and other water bodies, which pollute the soil, air, and water. Improper management of waste in the landfills will lead to various health problems such as asthma, cancer, bacterial infections, increased cardiovascular risk, some vector-borne diseases, i.e., dengue and cholera, improper reproductive disorders, and other diseases due to exposure to carcinogenic and non-carcinogenic pollutants (Giusti 2009). Microbial degradation of some organic compounds in the landfills results in the emission of greenhouse gases such as methane and carbon dioxide, carbon monoxide, and nitrogen. Greenhouse gas emitted through landfills has great potential for global warming, whereas the pollutants released in the lower soil and groundwater in the form of leachate cause soil and water pollution. So, the leachate, greenhouse and toxic gases, and other toxic substances released from the unorganized landfills are adversely affecting humans and environmental health (Swati et al. 2018).
To overcome these problems, a proper system should be established for the treatment of waste biomass. The bulk of garbage is dumped freely and is now turned into an enormous mountain of waste, leading to significant environmental pollution and depletion of natural resources. The health and ecological resources, including groundwater, soil fertility, and air quality, can be covered by building properly engineered sanitary landfills (Kumar et al. 2009). Additional issues such as pollution pollutants, smelling, litter, fire hazards, and pest breeding can also be eliminated where waste is disposed of at appropriately built landfill sites. Sanitary landfills can also be used to store methane by installing vertical wells on the top, which can generate heat and electricity and eliminate the exponential harm to the atmosphere and public health. Instead of dumping the waste in the ground, it can be transferred to waste-to-energy plants where a high calorific fraction of the waste can be utilized as a resource with present technologies. Generally, heat and power can be generated by the combustion of waste in waste-to-energy plants. These waste-to-energy plants use waste material as a resource collected in the dumping ground. For energy recovery, the waste composition is of considerable significance as present technologies use a high calorific fraction of the wastes that provide heat and power upon combustion. In the future, waste-to-energy technologies are crucial in treating various industrial wastes (Swati et al. 2018). New waste management technologies will play an essential role in future waste treatment, positively affecting the environment and human health.
1.6 Conclusion
In the current scenario, the global view for agro-industrial waste changes quickly to protect the environment and human health. Various kinds of wastes generated in the form of agricultural residues or wastewaters have been utilized to produce value-added products. These waste residues have enormous potential for the production of various important products such as biofuels, enzymes, biofertilizers, and many other bioactive compounds by using different microbial treatments. As these products are profitable, eco-friendly with an optional alternate for fossil fuels, and have potential applications in new sectors, it is important to establish more regulatory systems and investments to commercialize these products in the market. Transforming agro-industrial waste residues into efficacious compounds provides researchers a new way of sustainability for the next generation and eliminates established environmental risks.
References
Abdel-Shafy HI, Mansour MS (2018) Solid waste issue: sources, composition, disposal, recycling, and valorization. Egypt J Pet 27(4):1275–1290. https://doi.org/10.1016/j.ejpe.2018.07.003
Abdeshahian P, Samat N, Hamid AA, Yusoff WMW (2010) Utilization of palm kernel cake for production of β-mannanase by Aspergillus niger FTCC 5003 in solid substrate fermentation using an aerated column bioreactor. J Ind Microbiol Biotechnol 37(1):103. https://doi.org/10.1007/s10295-009-0658-0
Adeniran HA, Abiose SH, Ogunsua AO (2010) Production of fungal β-amylase and amyloglucosidase on some Nigerian agricultural residues. Food Bioprocess Technol 3(5):693–698. https://doi.org/10.1007/s11947-008-0141-3
Alatriste-Mondragón F, Samar P, Cox HH, Ahring BK, Iranpour R (2006) Anaerobic codigestion of municipal, farm, and industrial organic wastes: a survey of recent literature. Water Environ Res 78(6):607–636. https://doi.org/10.2175/106143006X111673
Aliyah A, Alamsyah G, Ramadhani R, Hermansyah H (2017) Production of α-Amylase and β-Glucosidase from Aspergillus niger by solid state fermentation method on biomass waste substrates from rice husk, bagasse and corn cob. Energy Procedia 136:418–423. https://doi.org/10.1016/j.egypro.2017.10.269
Alsanius BW, Blok C, Cuijpers WJ, França SC, Fuchs JG, Janmaat L, van der Wurff AW (2016) Handbook for composting and compost use in organic horticulture. BioGreenhouse COST Action FA. 1105. https://doi.org/10.18174/375218
Anto H, Trivedi UB, Patel KC (2006) Glucoamylase production by solid-state fermentation using rice flake manufacturing waste products as substrate. Bioresour Technol 97(10):1161–1166. https://doi.org/10.1016/j.biortech.2005.05.007
Arvanitoyannis IS, Kassaveti A (2007) Current and potential uses of composted olive oil waste. Int J Food Sci Technol 42(3):281–295. https://doi.org/10.1111/j.1365-2621.2006.01211.x
Avcıoğlu AO, Dayıoğlu MA, Türker U (2019) Assessment of the energy potential of agricultural biomass residues in Turkey. Renew Energy 138:610–619. https://doi.org/10.1016/j.renene.2019.01.053
Badshah M, Parawira W, Mattiasson B (2012) Anaerobic treatment of methanol condensate from pulp mill compared with anaerobic treatment of methanol using mesophilic UASB reactors. Bioresour Technol 125:318–327. https://doi.org/10.1016/j.biortech.2012.08.109
Bajaj BK, Wani MA (2011) Enhanced phytase production from Nocardia sp. MB 36 using agro-residues as substrates: potential application for animal feed production. Eng Life Sci 11(6):620–628. https://doi.org/10.1002/elsc.201100039
Bastawde KB (1992) Xylan structure, microbial xylanases, and their mode of action. World J Microbiol Biotechnol 8(4):353–368. https://doi.org/10.1007/bf01198746
Batstone D, Keller J, Newell B, Newland M (1997) Model development and full-scale validation for anaerobic treatment of protein and fat based wastewater. Water Sci Technol 36(6–7):423–431. https://doi.org/10.1016/S0273-1223(97)00551-9
Batstone DJ, Keller J, Angelidaki I, Kalyuzhnyi SV, Pavlostathis SG, Rozzi A, Sanders WTM, Siegrist HA, Vavilin VA (2002) The IWA anaerobic digestion model no 1 (ADM1). Water Sci Technol 45(10):65–73. https://doi.org/10.2166/wst.2002.0292
Beg Q, Kapoor M, Mahajan L, Hoondal GS (2001) Microbial xylanases and their industrial applications: a review. Appl Microbiol Biotechnol 56(3–4):326–338. https://doi.org/10.1007/s002530100704
Bharathiraja S, Suriya J, Krishnan M, Manivasagan P, Kim SK (2017) Production of enzymes from agricultural wastes and their potential industrial applications. In: Advances in food and nutrition research, vol 80. Academic, pp 125–148. https://doi.org/10.1016/bs.afnr.2016.11.003
Bhardwaj N, Kumar B, Verma P (2019) A detailed overview of xylanases: an emerging biomolecule for current and future prospective. Bioresour Bioprocess 6(1):1–36. https://doi.org/10.1186/s40643-019-0276-2
Boe K, Angelidaki I (2009) Serial CSTR digester configuration for improving biogas production from manure. Water Res 43(1):166–172. https://doi.org/10.1016/j.watres.2008.09.041
Buaban B, Inoue H, Yano S, Tanapongpipat S, Ruanglek V, Champreda V, Pichyangkura R, Rengpipat S, Eurwilaichitr L (2010) Bioethanol production from ball milled bagasse using an on-site produced fungal enzyme cocktail and xylose-fermenting Pichia stipitis. J Biosci Bioeng 110(1):18–25. https://doi.org/10.1016/j.jbiosc.2009.12.003
Castro AMD, Pereira N Jr (2010) Production, properties and application of cellulases in the hydrolysis of agro-industrial residues. Quim Nova 33(1):181–188. https://doi.org/10.1590/S0100-40422010000100031
Chaari F, Chaabouni SE (2019) Fungal β-1, 3-1, 4-glucanases: production, proprieties and biotechnological applications. J Sci Food Agric 99(6):2657–2664. https://doi.org/10.1002/jsfa.9491
Chen YW, Lee HV (2018) Revalorization of selected municipal solid wastes as new precursors of “green” nanocellulose via a novel one-pot isolation system: a source perspective. Int J Biol Macromol 107:78–92. https://doi.org/10.1016/j.ijbiomac.2017.08.143
Chi Z, Chi Z, Zhang T, Liu G, Yue L (2009) Inulinase-expressing microorganisms and applications of inulinases. Appl Microbiol Biotechnol 82(2):211–220. https://doi.org/10.1007/s00253-008-1827-1
Clarke JH, Davidson K, Rixon JE, Halstead JR, Fransen MP, Gilbert HJ, Hazlewood GP (2000) A comparison of enzyme-aided bleaching of softwood paper pulp using combinations of xylanase, mannanase and α-galactosidase. Appl Microbiol Biotechnol 53(6):661–667. https://doi.org/10.1007/s002530000344
Collins T, Gerday C, Feller G (2005) Xylanases, xylanase families and extremophilic xylanases. FEMS Microbiol Rev 29(1):3–23. https://doi.org/10.1016/j.femsre.2004.06.005
Contreras LM, Schelle H, Sebrango CR, Pereda I (2012) Methane potential and biodegradability of rice straw, rice husk and rice residues from the drying process. Water Sci Technol 65(6):1142–1149. https://doi.org/10.2166/wst.2012.951
Dais P, Perlin AS (1982) High-field, 13C-NMR spectroscopy of β-d-glucans, amylopectin, and glycogen. Carbohydr Res 100(1):103–116. https://doi.org/10.1016/S0008-6215(00)81029-0
de Souza WR (2013) Microbial degradation of lignocellulosic biomass. In: Sustainable degradation of lignocellulosic biomass-techniques, applications and commercialization. InTech, Rijeka, pp 207–247. https://doi.org/10.5772/54325
De Vries RP, Visser JAAP (2001) Aspergillus enzymes involved in degradation of plant cell wall polysaccharides. Microbiol Mol Biol Rev 65(4):497–522. https://doi.org/10.1128/MMBR.65.4.497-522.2001
Del Real Olvera J, Lopez-Lopez A (2012) Biogas production from anaerobic treatment of agro-industrial wastewater. In: Biogas. InTech, Rijeka, pp 91–112. https://doi.org/10.5772/31906
Department of the Environment and Energy, 2018. Synthetic Greenhouse Gases [WWW Document]. Dep. Agric. Water Environ. URL http://www.environment.gov.au/. Accessed 27.10.20
Devi V, Sumathy VJH (2017) Biofertilizer production from agro-wastes. https://doi.org/10.20959/wjpr20179-9323
Dhillon GS, Kaur S, Brar SK, Verma M (2012) Potential of apple pomace as a solid substrate for fungal cellulase and hemicellulase bioproduction through solid-state fermentation. Ind Crop Prod 38:6–13. https://doi.org/10.1016/j.indcrop.2011.12.036
Diler G, Chevallier S, Pöhlmann I, Guyon C, Guilloux M, Le-Bail A (2015) Assessment of amyloglucosidase activity during production and storage of laminated pie dough. Impact on raw dough properties and sweetness after baking. J Cereal Sci 61:63–70. https://doi.org/10.1016/j.jcs.2014.10.003
Dora M, Wesana J, Gellynck X, Seth N, Dey B, De Steur H (2020) Importance of sustainable operations in food loss: evidence from the Belgian food processing industry. Ann Oper Res 290(1):47–72. https://doi.org/10.1007/s10479-019-03134-0
Eida MF, Nagaoka T, Wasaki J, Kouno K (2009) Isolation and characterization of cellulose-decomposing bacteria inhabiting sawdust and coffee residue composts. Microbes Environ:1202170356–1202170356. https://doi.org/10.1264/jsme2.ME11299
Espinosa-Ramírez J, Pérez-Carrillo E, Serna-Saldívar SO (2014) Maltose and glucose utilization during fermentation of barley and sorghum lager beers as affected by β-amylase or amyloglucosidase addition. J Cereal Sci 60(3):602–609. https://doi.org/10.1016/j.jcs.2014.07.008
Esposito G, Frunzo L, Panico A, Pirozzi F (2011) Model calibration and validation for OFMSW and sewage sludge co-digestion reactors. Waste Manag 31(12):2527–2535. https://doi.org/10.1016/j.wasman.2011.07.024
Far BE, Ahmadi Y, Khosroshahi AY, Dilmaghani A (2020) Microbial alpha-amylase production: progress, challenges and perspectives. Adv Pharm Bull 10(3):350. https://doi.org/10.34172/apb.2020.043
Farris S, Unalan IU, Introzzi L, Fuentes-Alventosa JM, Cozzolino CA (2014) Pullulan-based films and coatings for food packaging: present applications, emerging opportunities, and future challenges. J Appl Polym Sci 131(13). https://doi.org/10.1002/app.40539
Ferreira NL, Margeot A, Blanquet S, Berrin JG (2014) Use of cellulases from Trichoderma reesei in the twenty-first century—part I: current industrial uses and future applications in the production of second ethanol generation. In: Biotechnology and biology of Trichoderma. Elsevier, pp 245–261. https://doi.org/10.1016/B978-0-444-59576-8.00017-5
Fia FR, Matos AT, Borges AC, Fia R, Cecon PR (2012) Treatment of wastewater from coffee bean processing in anaerobic fixed bed reactors with different support materials: performance and kinetic modeling. J Environ Manag 108:14–21. https://doi.org/10.1016/j.jenvman.2012.04.033
Ganesh R, Rajinikanth R, Thanikal JV, Ramanujam RA, Torrijos M (2010) Anaerobic treatment of winery wastewater in fixed bed reactors. Bioprocess Biosyst Eng 33(5):619–628. https://doi.org/10.1007/s00449-009-0387-9
García-Gómez A, Bernal MP, Roig A (2005) Organic matter fractions involved in degradation and humification processes during composting. Compos Sci Util 13(2):127–135. https://doi.org/10.1080/1065657X.2005.10702229
Giusti L (2009) A review of waste management practices and their impact on human health. Waste Manag 29(8):2227–2239. https://doi.org/10.1016/j.wasman.2009.03.028
Godoy MG, Gutarra ML, Castro AM, Machado OL, Freire DM (2011) Adding value to a toxic residue from the biodiesel industry: production of two distinct pool of lipases from Penicillium simplicissimum in castor bean waste. J Ind Microbiol Biotechnol 38(8):945–953. https://doi.org/10.1007/s10295-010-0865-8
Gomes J, Terler K, Kratzer R, Kainz E, Steiner W (2007) Production of thermostable β-mannosidase by a strain of Thermoascus aurantiacus: isolation, partial purification and characterization of the enzyme. Enzym Microb Technol 40(4):969–975. https://doi.org/10.1016/j.enzmictec.2006.08.011
Gonzalez-Salazar MA, Venturini M, Poganietz WR, Finkenrath M, Kirsten T, Acevedo H, Spina PR (2016) Development of a technology roadmap for bioenergy exploitation including biofuels, waste-to-energy and power generation & CHP. Appl Energy 180:338–352. https://doi.org/10.1016/j.apenergy.2016.07.120
Guldhe A, Singh B, Renuka N, Singh P, Misra R, Bux F (2017) Bioenergy: a sustainable approach for cleaner environment. In: Phytoremediation potential of bioenergy plants. Springer, Singapore, pp 47–62. https://doi.org/10.1007/978-981-10-3084-0_2
Gupta A, Verma JP (2015) Sustainable bio-ethanol production from agro-residues: a review. Renew Sust Energ Rev 41:550–567. https://doi.org/10.1016/j.rser.2014.08.032
Gutiérrez AS, Eras JJC, Hens L, Vandecasteele C (2020) The energy potential of agriculture, agroindustrial, livestock, and slaughterhouse biomass wastes through direct combustion and anaerobic digestion. The case of Colombia. J Clean Prod 269:122317. https://doi.org/10.1016/j.jclepro.2020.122317
Hart TD, Lynch JM, De Leij FAAM (2003) Production of Trichurus spiralis to enhance the composting of cellulose-containing waste. Enzym Microb Technol 32(6):745–750. https://doi.org/10.1016/S0141-0229(03)00049-8
Hii SL, Tan JS, Ling TC, Ariff AB (2012) Pullulanase: role in starch hydrolysis and potential industrial applications. Enzyme Res 2012. https://doi.org/10.1155/2012/921362
Holm-Nielsen JB, Al Seadi T, Oleskowicz-Popiel P (2009) The future of anaerobic digestion and biogas utilization. Bioresour Technol 100(22):5478–5484. https://doi.org/10.1016/j.biortech.2008.12.046
Hou N, Wen L, Cao H, Liu K, An X, Li D, Wang H, Du X, Li C (2017) Role of psychrotrophic bacteria in organic domestic waste composting in cold regions of China. Bioresour Technol 236:20–28. https://doi.org/10.1016/j.biortech.2017.03.166
Hu Z, Wen Z (2008) Enhancing enzymatic digestibility of switchgrass by microwave-assisted alkali pretreatment. Biochem Eng J 38(3):369–378. https://doi.org/10.1016/j.bej.2007.08.001
Hussin ASM, Farouk AE, Greiner R, Salleh HM, Ismail AF (2007) Phytate-degrading enzyme production by bacteria isolated from Malaysian soil. World J Microbiol Biotechnol 23(12):1653–1660. https://doi.org/10.1007/s11274-007-9412-9
Juturu V, Wu JC (2014) Microbial cellulases: engineering, production and applications. Renew Sust Energ Rev 33:188–203. https://doi.org/10.1016/j.rser.2014.01.077
Karadag D, Köroğlu OE, Ozkaya B, Cakmakci M (2015) A review on anaerobic biofilm reactors for the treatment of dairy industry wastewater. Process Biochem 50(2):262–271. https://doi.org/10.1016/j.procbio.2014.11.005
Kaur N, Gupta AK (2002) Applications of inulin and oligofructose in health and nutrition. J Biosci 27(7):703–714. https://doi.org/10.1007/bf02708379
Kheiralla ZH, El-Gendy NS, Ahmed HA, Shaltout TH, Hussein MM (2018) One-factor-at-a-time (OFAT) optimization of hemicellulases production from Fusarium moniliforme in submerged fermentation. Energy Source Part A Recovery Util Environ Eff 40(15):1877–1885. https://doi.org/10.1080/15567036.2018.1487485
Kiiskinen LL, Rättö M, Kruus K (2004) Screening for novel laccase-producing microbes. J Appl Microbiol 97(3):640–646. https://doi.org/10.1111/j.1365-2672.2004.02348.x
Kim S, Dale BE (2004) Global potential bioethanol production from wasted crops and crop residues. Biomass Bioenergy 26(4):361–375. https://doi.org/10.1016/j.biombioe.2003.08.002
Kulikowska D (2016) Kinetics of organic matter removal and humification progress during sewage sludge composting. Waste Manag 49:196–203. https://doi.org/10.1016/j.wasman.2016.01.005
Kumar R, Singh S, Singh OV (2008) Bioconversion of lignocellulosic biomass: biochemical and molecular perspectives. J Ind Microbiol Biotechnol 35(5):377–391. https://doi.org/10.1007/s10295-008-0327-8
Kumar S, Bhattacharyya JK, Vaidya AN, Chakrabarti T, Devotta S, Akolkar AB (2009) Assessment of the status of municipal solid waste management in metro cities, state capitals, class I cities, and class II towns in India: An insight. Waste Manag 29(2):883–895. https://doi.org/10.1016/j.wasman.2008.04.011
Latgé JP (2010) Tasting the fungal cell wall. Cell Microbiol 12(7):863–872. https://doi.org/10.1111/j.1462-5822.2010.01474.x
Lian B, Wang B, Pan M, Liu C, Teng HH (2008) Microbial release of potassium from K-bearing minerals by thermophilic fungus Aspergillus fumigatus. Geochim Cosmochim Acta 72(1):87–98. https://doi.org/10.1016/j.gca.2007.10.005
Lim SL, Wu TY, Lim PN, Shak KPY (2015) The use of vermicompost in organic farming: overview, effects on soil and economics. J Sci Food Agric 95(6):1143–1156. https://doi.org/10.1002/jsfa.6849
Lincoln L, More SS (2017) Bacterial invertases: occurrence, production, biochemical characterization, and significance of transfructosylation. J Basic Microbiol 57(10):803–813. https://doi.org/10.1002/jobm.201700269
Linde D, Macias I, Fernández-Arrojo L, Plou FJ, Jiménez A, Fernández-Lobato M (2009) Molecular and biochemical characterization of a β-fructofuranosidase from Xanthophyllomyces dendrorhous. Appl Environ Microbiol 75(4):1065–1073. https://doi.org/10.1128/AEM.02061-08
Liu D, Lian B, Dong H (2012) Isolation of Paenibacillus sp. and assessment of its potential for enhancing mineral weathering. Geomicrobiol J 29(5):413–421. https://doi.org/10.1080/01490451.2011.576602
Liu GL, Chi Z, Chi ZM (2013) Molecular characterization and expression of microbial inulinase genes. Crit Rev Microbiol 39(2):152–165. https://doi.org/10.3109/1040841X.2012.694411
Lopez MJ, del Carmen Vargas-García M, Suárez-Estrella F, Moreno J (2006) Biodelignification and humification of horticultural plant residues by fungi. Int Biodeterior Biodegradation 57(1):24–30. https://doi.org/10.1016/j.ibiod.2005.10.005
Lu WJ, Wang HT, Nie YF, Wang ZC, Huang DY, Qiu XY, Chen JC (2004) Effect of inoculating flower stalks and vegetable waste with ligno-cellulolytic microorganisms on the composting process. J Environ Sci Health B 39(5–6):871–887. https://doi.org/10.1081/lesb-200030896
Ma Y, Rajkumar M, Zhang C, Freitas H (2016) Beneficial role of bacterial endophytes in heavy metal phytoremediation. J Environ Manag 174:14–25. https://doi.org/10.1016/j.jenvman.2016.02.047
Madureira J, Barros L, Cabo Verde S, Margaça FM, Santos-Buelga C, Ferreira IC (2020) Ionizing radiation technologies to increase the extraction of bioactive compounds from agro-industrial residues: a review. J Agric Food Chem 68(40):11054–11067. https://doi.org/10.1021/acs.jafc.0c04984
Mao C, Feng Y, Wang X, Ren G (2015) Review on research achievements of biogas from anaerobic digestion. Renew Sust Energ Rev 45:540–555. https://doi.org/10.1016/j.rser.2015.02.032
Mazutti M, Bender JP, Treichel H, Di Luccio M (2006) Optimization of inulinase production by solid-state fermentation using sugarcane bagasse as substrate. Enzym Microb Technol 39(1):56–59. https://doi.org/10.1016/j.enzmictec.2005.09.008
McCarty PL (2001) The development of anaerobic treatment and its future. Water Sci Technol 44(8):149–156. https://doi.org/10.2166/wst.2001.0487
McCleary BV, Matheson NK (1983) Action patterns and substrate-binding requirements of β-D-mannanase with mannosaccharides and mannan-type polysaccharides. Carbohydr Res 119:191–219. https://doi.org/10.1016/0008-6215(83)84056-7
Meena P, Tripathi AD, Srivastava SK, Jha A (2013) Utilization of agro-industrial waste (wheat bran) for alkaline protease production by Pseudomonas aeruginosa in SSF using Taguchi (DOE) methodology. Biocatal Agric Biotechnol 2(3):210–216. https://doi.org/10.1016/j.bcab.2013.05.003
Meena VS, Maurya BR, Verma JP (2014) Does a rhizospheric microorganism enhance K+ availability in agricultural soils? Microbiol Res 169(5–6):337–347. https://doi.org/10.1016/j.micres.2013.09.003
Meena VS, Meena SK, Verma JP, Kumar A, Aeron A, Mishra PK, Bisht JK, Pattanayak A, Naveed M, Dotaniya ML (2017) Plant beneficial rhizospheric microorganism (PBRM) strategies to improve nutrients use efficiency: a review. Ecol Eng 107:8–32. https://doi.org/10.1016/j.ecoleng.2017.06.058
Meksi N, Haddar W, Hammami S, Mhenni MF (2012) Olive mill wastewater: a potential source of natural dyes for textile dyeing. Ind Crop Prod 40:103–109. https://doi.org/10.1016/j.indcrop.2012.03.011
Membrillo Venegas I, Fuentes-Hernández J, García-Rivero M, Martínez-Trujillo A (2013) Characteristics of Aspergillus niger xylanases produced on rice husk and wheat bran in submerged culture and solid-state fermentation for an applicability proposal. Int J Food Sci Technol 48(9):1798–1807. https://doi.org/10.1111/ijfs.12153
Moreira LRS (2008) An overview of mannan structure and mannan-degrading enzyme systems. Appl Microbiol Biotechnol 79(2):165. https://doi.org/10.1007/s00253-008-1423-4
Mosier N, Wyman C, Dale B, Elander R, Lee YY, Holtzapple M, Ladisch M (2005) Features of promising technologies for pretreatment of lignocellulosic biomass. Bioresour Technol 96(6):673–686. https://doi.org/10.1016/j.biortech.2004.06.025
MPOC (Malaysian Palm Oil Council). Available online: http://mpoc.org.my/malaysian-palm-oil-industry/. Accessed on 05 Nov 2020
Murto M, Björnsson L, Mattiasson B (2004) Impact of food industrial waste on anaerobic co-digestion of sewage sludge and pig manure. J Environ Manag 70(2):101–107. https://doi.org/10.1016/j.jenvman.2003.11.001
Nadar SS, Rathod VK (2019) A co-immobilization of pectinase and cellulase onto magnetic nanoparticles for antioxidant extraction from waste fruit peels. Biocatal Agric Biotechnol 17:470–479. https://doi.org/10.1016/j.bcab.2018.12.015
Naganagouda K, Salimath PV, Mulimani VH (2009) Purification and characterization of endo-β-1, 4 mannanase from Aspergillus niger gr for application in food processing industry. J Microbiol Biotechnol 19(10):1184–1190. https://doi.org/10.4014/jmb.0901.029
Nath D, Maurya BR, Meena VS (2017) Documentation of five potassium-and phosphorus-solubilizing bacteria for their K and P-solubilization ability from various minerals. Biocatal Agric Biotechnol 10:174–181. https://doi.org/10.1016/j.bcab.2017.03.007
Obeng EM, Adam SNN, Budiman C, Ongkudon CM, Maas R, Jose J (2017) Lignocellulases: a review of emerging and developing enzymes, systems, and practices. Bioresour Bioprocess 4(1):16. https://doi.org/10.1186/s40643-017-0146-8
OIV (International Organisation of Vine and Wine). WINE PRODUCTION – OIV FIRST ESTIMATES 2020. Available online: http://www.oiv.int/js/lib/pdfjs/web/viewer.html?file=/public/medias/7541/en-oiv-2020-world-wine-production-first-estimates.pdf. Accessed on 05 Nov 2020
Onilude AA, Fadaunsi IF, Garuba EO (2012) Inulinase production by Saccharomyces sp. in solid-state fermentation using wheat bran as substrate. Ann Microbiol 62(2):843–848. https://doi.org/10.1007/s13213-011-0325-3
Onwosi CO, Igbokwe VC, Odimba JN, Eke IE, Nwankwoala MO, Iroh IN, Ezeogu LI (2017) Composting technology in waste stabilization: on the methods, challenges and future prospects. J Environ Manag 190:140–157. https://doi.org/10.1016/j.jenvman.2016.12.051
Orzua MC, Mussatto SI, Contreras-Esquivel JC, Rodriguez R, de la Garza H, Teixeira JA, Aguilar CN (2009) Exploitation of agro-industrial wastes as immobilization carrier for solid-state fermentation. Ind Crop Prod 30(1):24–27. https://doi.org/10.1016/j.indcrop.2009.02.001
Pandey A, Szakacs G, Soccol CR, Rodriguez-Leon JA, Soccol VT (2001) Production, purification and properties of microbial phytases. Bioresour Technol 77(3):203–214. https://doi.org/10.1016/S0960-8524(00)00139-5
Pandya JJ, Gupte A (2012) Production of xylanase under solid-state fermentation by Aspergillus tubingensis JP-1 and its application. Bioprocess Biosyst Eng 35(5):769–779. https://doi.org/10.1007/s00449-011-0657-1
Pardo G, Martin-Garcia I, Arco A, Yañez-Ruiz DR, Moral R, Del Prado A (2016) Greenhouse-gas mitigation potential of agro-industrial by-products in the diet of dairy goats in Spain: a life-cycle perspective. Anim Prod Sci 56(3):646–654. https://doi.org/10.1071/AN15620
Parmar P, Sindhu SS (2013) Potassium solubilization by rhizosphere bacteria: influence of nutritional and environmental conditions. J Microbiol Res 3(1):25–31. https://doi.org/10.5923/j.microbiology.20130301.04
Peng W, Pivato A (2017) Sustainable management of digestate from the organic fraction of municipal solid waste and food waste under the concepts of back to earth alternatives and circular economy. Waste Biomass Valoriz 10:465–481. https://doi.org/10.1007/s12649-017-0071-2
Pereda Reyes I, Sárvári Horváth I (2015) Anaerobic biodegradation of solid substrates from agro-industrial activities—slaughterhouse wastes and agrowastes. https://doi.org/10.5772/60907
Pereira ADS, Fontes-Sant’Ana GC, Amaral PF (2019) Mango agro-industrial wastes for lipase production from Yarrowia lipolytica and the potential of the fermented solid as a biocatalyst. Food Bioprod Process 115:68–77. https://doi.org/10.1016/j.fbp.2019.02.002
Popp J, Lakner Z, Rákos MH, Fári M (2014) The effect of bioenergy expansion: food, energy, and environment. Renew Sust Energ Rev 32:559–578. https://doi.org/10.1016/j.rser.2014.01.056
Portugal-Pereira J, Soria R, Rathmann R, Schaeffer R, Szklo A (2015) Agricultural and agro-industrial residues-to-energy: techno-economic and environmental assessment in Brazil. Biomass Bioenergy 81:521–533. https://doi.org/10.1016/j.biombioe.2015.08.010
Prasad S, Singh A, Joshi HC (2007) Ethanol as an alternative fuel from agricultural, industrial and urban residues. Resour Conserv Recycl 50(1):1–39. https://doi.org/10.1016/j.resconrec.2006.05.007
Quintero JA, Rincón LE, Cardona CA (2011) Production of bioethanol from agro-industrial residues as feedstocks. In: Biofuels. Academic, pp 251–285. https://doi.org/10.1016/B978-0-12-385099-7.00011-5
Rajagopal R, Torrijos M, Kumar P, Mehrotra I (2013) Substrate removal kinetics in high-rate upflow anaerobic filters packed with low-density polyethylene media treating high-strength agro-food wastewaters. J Environ Manag 116:101–106. https://doi.org/10.1016/j.jenvman.2012.11.032
Ramachandran S, Patel AK, Nampoothiri KM, Francis F, Nagy V, Szakacs G, Pandey A (2004) Coconut oil cake––a potential raw material for the production of α-amylase. Bioresour Technol 93(2):169–174. https://doi.org/10.1016/j.biortech.2003.10.021
Ramachandran S, Singh SK, Larroche C, Soccol CR, Pandey A (2007) Oil cakes and their biotechnological applications–a review. Bioresour Technol 98(10):2000–2009. https://doi.org/10.1016/j.biortech.2006.08.002
Rashid MI, Mujawar LH, Shahzad T, Almeelbi T, Ismail IM, Oves M (2016) Bacteria and fungi can contribute to nutrients bioavailability and aggregate formation in degraded soils. Microbiol Res 183:26–41. https://doi.org/10.1016/j.micres.2015.11.007
Ravindran R, Hassan SS, Williams GA, Jaiswal AK (2018) A review on bioconversion of agro-industrial wastes to industrially important enzymes. Bioengineering 5(4):93. https://doi.org/10.3390/bioengineering5040093
Razzaq A, Shamsi S, Ali A, Ali Q, Sajjad M, Malik A, Ashraf M (2019) Microbial proteases applications. Front Bioeng Biotechnol 7:110. https://doi.org/10.3389/fbioe.2019.00110
Reddy PRM, Mrudula S, Ramesh B, Reddy G, Seenayya G (2000) Production of thermostable pullulanase by Clostridium thermosulfurogenes SV2 in solid-state fermentation: optimization of enzyme leaching conditions using response surface methodology. Bioprocess Eng 23(2):107–112. https://doi.org/10.1007/pl00009116
Ronkart SN, Blecker CS, Fourmanoir H, Fougnies C, Deroanne C, Van Herck JC, Paquot M (2007) Isolation and identification of inulooligosaccharides resulting from inulin hydrolysis. Anal Chim Acta 604(1):81–87. https://doi.org/10.1016/j.aca.2007.07.073
Rytioja J, Hildén K, Yuzon J, Hatakka A, de Vries RP, Mäkelä MR (2014) Plant-polysaccharide-degrading enzymes from basidiomycetes. Microbiol Mol Biol Rev 78(4):614–649. https://doi.org/10.1128/MMBR.00035-14
Sadh PK, Duhan S, Duhan JS (2018) Agro-industrial wastes and their utilization using solid-state fermentation: a review. Bioresour Bioproces 5(1):1. https://doi.org/10.1186/s40643-017-0187-z
Saha BC, Zeikus JG (1989) Novel highly thermostable pullulanase from thermophiles. Trends Biotechnol 7(9):234–239. https://doi.org/10.1016/0167-7799(89)90013-9
Sarkar N, Ghosh SK, Bannerjee S, Aikat K (2012) Bioethanol production from agricultural wastes: an overview. Renew Energy 37(1):19–27. https://doi.org/10.1016/j.renene.2011.06.045
Shallom D, Shoham Y (2003) Microbial hemicellulases. Curr Opin Microbiol 6(3):219–228. https://doi.org/10.1016/S1369-5274(03)00056-0
Sharma N, Rathore M, Sharma M (2013) Microbial pectinase: sources, characterization and applications. Rev Environ Sci Biotechnol 12(1):45–60. https://doi.org/10.1007/s11157-012-9276-9
Shin HK, Kong JY, Lee JD, Lee TH (2000) Syntheses of hydroxybenzyl-α-glucosides by amyloglucosidase-catalyzed transglycosylation. Biotechnol Lett 22(4):321–325. https://doi.org/10.1023/A:1005699104814
Sim TS, Oh JCS (1990) Spent brewery grains as substrate for the production of cellulases by Trichoderma reesei QM9414. J Ind Microbiol 5(2–3):153–158. https://doi.org/10.1007/BF01573865
Singh RS, Chauhan K (2018) Production, purification, characterization and applications of fungal inulinases. Curr Biotechnol 7(3):242–260. https://doi.org/10.2174/2211550105666160512142330
Singh D, Gupta N (2020) Microbial laccase: a robust enzyme and its industrial applications. Biologia:1–11. https://doi.org/10.2478/s11756-019-00414-9
Singh H, Soni SK (2001) Production of starch-gel digesting amyloglucosidase by aspergillus oryzae HS-3 in solid-state fermentation. Process Biochem 37(5):453–459. https://doi.org/10.1016/S0032-9592(01)00238-2
Singh M, Dotaniya ML, Mishra A, Dotaniya CK, Regar KL, Lata M (2016) Role of biofertilizers in conservation agriculture. In: Conservation agriculture. Springer, Singapore, pp 113–134. https://doi.org/10.1007/978-981-10-2558-7_4
Singh RS, Singh T, Pandey A (2019) Microbial enzymes-an overview. In: Advances in enzyme technology. Elsevier, Amsterdam, pp 1–40. https://doi.org/10.1016/B978-0-444-64114-4.00001-7
Singhania RR, Patel AK, Soccol CR, Pandey A (2009) Recent advances in solid-state fermentation. Biochem Eng J 44:13–18. https://doi.org/10.1016/j.bej.2008.10.019
Siqueira LM, Damiano ES, Silva EL (2013) Influence of organic loading rate on the anaerobic treatment of sugarcane vinasse and biogas production in fluidized bed reactor. J Environ Sci Health A 48(13):1707–1716. https://doi.org/10.1080/10934529.2013.815535
Soccol CR, da Costa ESF, Letti LAJ, Karp SG, Woiciechowski AL, de Souza Vandenberghe LP (2017) Recent developments and innovations in solid state fermentation. Biotechnol Res Innov 1(1):52–71. https://doi.org/10.1016/j.biori.2017.01.002
Spindler DD, Wyman CE, Grohmann K, Philippidis GP (1992) Evaluation of the cellobiose-fermenting yeast Brettanomyces custersii in the simultaneous saccharification and fermentation of cellulose. Biotechnol Lett 14(5):403–407. https://doi.org/10.1007/BF01021255
Sundarram A, Murthy TPK (2014) α-Amylase production and applications: a review. J Appl Environmen Microbiol 2(4):166–175. https://doi.org/10.12691/jaem-2-4-10
Suthar S (2007) Production of vermifertilizer from guar gum industrial wastes by using composting earthworm Perionyx sansibaricus (Perrier). Environmentalist 27(3):329–335. https://doi.org/10.1007/s10669-007-9032-9
Suthar H, Hingurao K, Vaghashiya J, Parmar J (2017) Fermentation: a process for biofertilizer production. In: Microorganisms for green revolution. Springer, Singapore, pp 229–252. https://doi.org/10.1007/978-981-10-6241-4_12
Swati TI, Vijay VK, Ghosh P (2018) Scenario of landfilling in India: problems, challenges, and recommendations. In: Handbook of environmental materials management. Springer, Cham, pp 1–16. https://doi.org/10.1007/978-3-319-58538-3_167-1
Thomas L, Larroche C, Pandey A (2013) Current developments in solid-state fermentation. Biochem Eng J 81:146–161. https://doi.org/10.1016/j.bej.2013.10.013
Tomasik P, Horton D (2012) Enzymatic conversions of starch. In: Advances in carbohydrate chemistry and biochemistry, vol 68. Academic, New York, pp 59–436. https://doi.org/10.1016/B978-0-12-396523-3.00001-4
Treichel H, de Oliveira D, Mazutti MA, Di Luccio M, Oliveira JV (2010) A review on microbial lipases production. Food Bioprocess Technol 3(2):182–196. https://doi.org/10.1007/s11947-009-0202-2
Ueda M, Ito A, Nakazawa M, Miyatake K, Sakaguchi M, Inouye K (2014) Cloning and expression of the cold-adapted endo-1, 4-β-glucanase gene from Eisenia fetida. Carbohydr Polym 101:511–516. https://doi.org/10.1016/j.carbpol.2013.09.057
Van der Wurff AW, Fuchs JG, Raviv M, Termorshuizen A (2016) Handbook for composting and compost use in organic horticulture. BioGreenhouse, Rotterdam. https://doi.org/10.18174/375218
Vargas-García MC, Suárez-Estrella F, López MJ, Moreno J (2007) Effect of inoculation in composting processes: modifications in lignocellulosic fraction. Waste Manag 27(9):1099–1107. https://doi.org/10.1016/j.wasman.2006.06.013
Varma VS, Kalamdhad AS (2014) Stability and microbial community analysis during rotary drum composting of vegetable waste. Int J Recycl Organic Waste Agri 3(2):52. https://doi.org/10.1007/S40093-014-0052-4
Verma JP, Yadav J, Tiwari KN, Jaiswal DK (2014) Evaluation of plant growth promoting activities of microbial strains and their effect on growth and yield of chickpea (Cicer arietinum L.) in India. Soil Biol Biochem 70:33–37. https://doi.org/10.1016/j.soilbio.2013.12.001
Vijayaraghavan K, Yamini D, Ambika V, Sravya Sowdamini N (2009) Trends in inulinase production–a review. Crit Rev Biotechnol 29(1):67–77. https://doi.org/10.1080/07388550802685389
Weiland P (2010) Biogas production: current state and perspectives. Appl Microbiol Biotechnol 85(4):849–860. https://doi.org/10.1007/s00253-009-2246-7
Yadav A (2018) Microbial Inoculants for Sustainable Agriculture. Int J Curr Microbiol App Sci 7(5):800–804. https://doi.org/10.20546/ijcmas.2018.705.097
Yin JS, Liang QL, Li DM, Sun ZT (2013) Optimization of production conditions for β-mannanase using apple pomace as raw material in solid-state fermentation. Ann Microbiol 63(1):101–108. https://doi.org/10.1007/s13213-012-0449-0
Yusuf M (2017) Agro-industrial waste materials and their recycled value-added applications. In: Handbook of Ecomaterials. Springer, Cham, pp 1–11. https://doi.org/10.1007/978-3-319-48281-1_48-1
Zainudin MHM, Hassan MA, Tokura M, Shirai Y (2013) Indigenous cellulolytic and hemicellulolytic bacteria enhanced rapid co-composting of lignocellulose oil palm empty fruit bunch with palm oil mill effluent anaerobic sludge. Bioresour Technol 147:632–635. https://doi.org/10.1016/j.biortech.2013.08.061
Zakaria ZA, Boopathy R, Dib JR (eds) (2020) Valorisation of agro-industrial residues-volume I: biological approaches. Springer, Cham. https://doi.org/10.1007/978-3-030-39208-6
Zhang H, Li C, Li G, Zang B, Yang Q (2012) Effect of spent air reusing (SAR) on maturity and greenhouse gas emissions during municipal solid waste (MSW) composting-with different pile height. Procedia Environ Sci 16:59–69. https://doi.org/10.1016/j.proenv.2012.10.009
Zhang Y, Nie Y, Zhou X, Bi J, Xu Y (2020) Enhancement of pullulanase production from recombinant Bacillus subtilis by optimization of feeding strategy and fermentation conditions. AMB Express 10(1):1–9. https://doi.org/10.1186/s13568-020-0948-5
Zhu F, Du B, Xu B (2016) A critical review on production and industrial applications of beta-glucans. Food Hydrocoll 52:275–288. https://doi.org/10.1016/j.foodhyd.2015.07.003
Zverlov VV, Köck DE, Schwarz WH (2015) The role of cellulose-hydrolyzing bacteria in the production of biogas from plant biomass. In: Microorganisms in biorefineries. Springer, Berlin/Heidelberg, pp 335–361. https://doi.org/10.1007/978-3-662-45209-7_12
Acknowledgment
RK is thankful to DST, Govt. of India for financial assistance under the DST INSPIRE Faculty Scheme [DST/INSPIRE/04/2014/001280], Science and Engineering Research Board Start-up research grant no. SRG/2019/001071, NMHS project of MoEF&CC grant no. GBPNI/NMHS-2018-19/SG/178, and DST-TDT project no. DST/TDT/WM/2019/43. KD is thankful to CSIR, Govt. of India for ‘Research Fellowship’ Grant [CSIR-NET JRF award no: 31/054(0139)/2019-EMR-I/CSIR-NET JRF JUNE 2017]. Authors also acknowledge financial support from CSIR MLP 0137, MLP 0143, and MLP 0201.
Author information
Authors and Affiliations
Corresponding author
Editor information
Editors and Affiliations
Rights and permissions
Copyright information
© 2021 The Author(s), under exclusive license to Springer Nature Switzerland AG
About this chapter
Cite this chapter
Kumar, A., Kumari, S., Dindhoria, K., Manyapu, V., Kumar, R. (2021). Efficient Utilization and Bioprocessing of Agro-Industrial Waste. In: Rana, A., Saneja, A., Kumar, S., Lichtfouse, E. (eds) Sustainable Agriculture Reviews 56. Sustainable Agriculture Reviews, vol 56. Springer, Cham. https://doi.org/10.1007/978-3-030-84405-9_1
Download citation
DOI: https://doi.org/10.1007/978-3-030-84405-9_1
Published:
Publisher Name: Springer, Cham
Print ISBN: 978-3-030-84404-2
Online ISBN: 978-3-030-84405-9
eBook Packages: Biomedical and Life SciencesBiomedical and Life Sciences (R0)