Journal Pre-Proofs: Bioresource Technology
Journal Pre-Proofs: Bioresource Technology
PII: S0960-8524(19)31810-3
DOI: https://doi.org/10.1016/j.biortech.2019.122580
Reference: BITE 122580
Please cite this article as: Sharma, P., Gaur, V.K., Kim, S-H., Pandey, A., Microbial strategies for bio-transforming
food waste into resources, Bioresource Technology (2019), doi: https://doi.org/10.1016/j.biortech.2019.122580
This is a PDF file of an article that has undergone enhancements after acceptance, such as the addition of a cover
page and metadata, and formatting for readability, but it is not yet the definitive version of record. This version will
undergo additional copyediting, typesetting and review before it is published in its final form, but we are providing
this version to give early visibility of the article. Please note that, during the production process, errors may be
discovered which could affect the content, and all legal disclaimers that apply to the journal pertain.
Poonam Sharmaa¶, Vivek Kumar Gaurb,c¶, Sang-Hyoun Kimd and Ashok Pandeye,f*
a
Department of Bioengineering, Integral University, Lucknow, Uttar Pradesh, India
b
Environmental Biotechnology Division, Environmental Toxicology Group, CSIR-Indian
India.
d
School of Civil and Environmental Engineering, Yonsei University, Seoul, Republic of Korea
e
Centre for Innovation and Translational Research, CSIR-Indian Institute of Toxicology
1
Abstract
With the changing life-style and rapid urbanization of global population, there is increased
generation of food waste from various industrial, agricultural, and household sources. According
to Food and Agriculture Organization (FAO), almost one-third of the total food produced
annually is wasted. This poses serious concern as not only there is loss of rich resources; their
disposal in environment causes concern too. Food waste is rich in organic, thus traditional
approaches of land-filling and incineration could cause severe environmental and human health
hazard by generating toxic gases. Thus, employing biological methods for the treatment of such
waste offers a sustainable way for valorization. This review comprehensively discusses state-of-
art knowledge about various sources of food waste generation, their utilization, and valorization
could be a sustainable and eco-friendly solution for food waste management by generating
2
Introduction
Food is an essential component for the survival and existence of life. Organisms at different
evolutionary levels consume food in different form viz. micro-organisms ingest in the form of
contrastingly higher eukaryotes like humans feed upon a complex version of food i.e. in the form
of fruits, vegetables, cereals, pulses, meat, and dairy products. A major concern arise when this
indispensable commodity i.e. food is misused and mismanaged at any stage of the food life cycle
The leftover or precooked food which generates biodegradable organic waste is termed as food
waste (FW). As per the definition given by The Food and Agriculture Organization (FAO), FW
is “food losses of quality and quantity through the process of the supply chain taking place at
production, post-harvest, and processing stages”. Specifically FW corresponds to the loss of food
at the end of food life cycle (Tsang et al., 2019). Generation of FW also leads to considerable
loss of other resources like water, land, labour and energy. It was estimated by FAO that
annually 1.3 billion tonnes of wasted food is generated globally. This wasted food is one-third of
the total food produced globally, whose production corresponds from 28% of agricultural area
utilizing 1.4 billion hectare of the world’s fertile land (Karthikeyan et al., 2018; Paritosh et al.,
2017). It is projected that economic and population growth will lead to increased FW generation
in next 25 years in Asian countries. The urban FW is expected to rise 138 million tonnes by 2025
as compared to in 2005 (Paritosh et al., 2017). Out of the total waste generated globally, Asia
contributes to highest FW 278 million tonnes, whereas Vietnam produced approximately 11.55
million tonnes of FW (Kiran et al., 2014). This FW includes fresh fruits, vegetables, dairy
products, bakery products, and meat from diverse sources, including discharges from
3
households, hospitality sector, food processing industries, commercial kitchens, and agriculture
The disease control centers prevented the use of FW as animal feed, thus preferentially the
disposal of FW was done through fermentation, composting, and landfilling (Tsang et al., 2019).
high moisture content of FW leads to the generation of dioxins by incineration, whereas dumping
in open area causes environmental and health issues. FW is estimated to generate 3.3 billion
tonnes of CO2 per year, thereby contributing in the emission of greenhouse gases (Paritosh et al.,
valorization of FW for the production of value added products is an ideal approach attracting
has increased ≥90% during the last decade from 2009 to 2018 (Fig. 1). Therefore, this review is
to understand the sources and nature of FW that can be efficiently converted to value added
discarded/dumped FW.
On a global scale, significant proportion of the human diet is filled by cereal grains obtained
from seeds of Gramineae family such as wheat, rice, barley, maize, sorghum, millet, oat, and rye.
According to the FAO, globally total crop production during 2016 reached 2577.85 million tons.
In contrast, the production of coarse grains (cereal grains other than wheat and rice used
4
primarily for animal feed or brewing) was 1330.02 million tons (FAO-AMIS, 2017). The
production ranking in the year 2014 was corn 1253.6, rice paddy 949.7, wheat 854.9, barley
146.3, oat 23.2, and rye 15.8 tonnes (Papageorgiou and Skendi, 2018). The cereal and pulses
processing industry produce a large quantity of by-products like bran and germ, during
processing (Anal, 2017). India is the worlds’ largest producer of pulses producing a considerable
amount of husk as a by-product during processing (Parate and Talib, 2015). Husk is recycled in
many ways to produce high-end products. There are many crops which generate husk as a by-
product of processing. Apart from utilization as animal feed the straw, husk and dried leaves of
crops like wheat, corn, rice, and barley is utilized in traditional way for making thatching roofs,
baskets, broom, hand fans, handbags and in preparation of decorative items. It is used as cleaning
and polishing agent in metal and machine industries. Rice husk can be used as pet feed fiber,
fertilizer and substrate for vermicomposting technique, and in the production of construction
material like light weight bricks (Kumar et al., 2013). Husk obtained after cocoa pod processing
was utilized for pectin extraction and production of vermicompost, oyster mushrooms, livestock
feed, and other value-added products (Dede et al., 2018). Furthermore, coconut husk has multiple
household applications like rope, broom, mat, tiles, fishing net, and mattresses. It is also
employed for the production of second generation bio-ethanol (Bolivar-Telleria et al., 2018).
These by-products are rich in nutrients, generally consists of dietary fibers, proteins, lipids, fatty
acids, vitamins, minerals and phenolic compounds but still they arrive finally as animal feed,
fuel, and biorefinery substrate. For production of refined flour, bran and germ, a proportion of
grain is removed as they adversely affect the processing properties (Verni et al., 2019). The by-
product of barley pearling process serves as a rich source of bioactive compounds like phytates,
insoluble dietary fiber, phenolics and it contains 2.7 times more vitamin E than in whole barley
5
grain (Papageorgiou and Skendi, 2018). Rice husk is used in fermentation process to adjust
moisture, maintain the porosity of fermentative material for gaseous exchange during distillation
Fruits and vegetables are energy rich food items with high moisture content having rich nutritive
polyphenols and other bioactive compounds (Schieber, 2017). Fruit and vegetable wastes were
generated during different steps of food supply chain starting from farm to fork, including
production, processing, packaging, handling, storage and transportation (Ji et al., 2017). Fruits
and vegetables are classified to waste category only when a consumer disqualifies it from degree
of acceptance. This may arise due to several factors such as discoloration, wounding or chilling,
treatment, microbial attack (rotting, softening and surface growth), and degree of ripening. India
is the second largest producer of vegetables and fruits in the world sharing 10% and 14% of
global production, respectively. It leads to economic loss worth of US $483.9 million per year
due to wastage of about 50 million tons, accounting for 30-40% of total production in India
(Panda et al., 2016). Central de Abasto, the second largest fruit and vegetable market in the
world, at Mexico City, produced 895 tonnes of waste/day. China produces approximately 1.3
million tonnes of this waste per day (Ji et al., 2017). According to a report of FAO in 2014, UK
alone produced 5.5 million tonnes of potatoes; around 3 % to 13 % of harvested crop never
reaches to customer and is wasted due to “grading losses” in supermarkets. This generated waste
methods give rise to serious environmental concern such as toxic and greenhouse gas emission,
6
microbial proliferation due to high content of moisture and landfill leachate (Ji et al., 2017;
Reduction of fruits and vegetable waste is warranted to alleviate the increasing demand for food
production and improving the overall efficiency of food supply chain (Matharu et al., 2016).
Growing public concerns about hunger, fruits and vegetable losses, food security reasons,
conserving the environment from pollution, socio-economic factors have accelerated research
into FW domain towards finding better ways of using this natural and renewable resource. The
starch, cellulose and/or hemicelluloses of fruit and vegetable waste is hydrolyzed to soluble
sugars and further fermented to produce ethanol and hydrogen (Diaz et al., 2017). Microbial
processing of fruits and vegetable waste has opened new horizons for value addition to rejected
fruits and vegetables. Several high-end commodities was reported to be produced by utilizing
Candida utilis, Endomycopsis fibuligera and Pichia burtonii), single-cell oils, polysaccharides,
oils, biopesticides, plant growth regulators, enzymes (cellulase, amylase, protease, phytase, etc),
biohydrogen, bioethanol and biogas (Panda et al., 2016; Schieber 2017; Sabu et al., 2002; Bogar
et al., 2003a; Pandey and Soccol, 2000; Benjamin and Pandey, 1997). Acidogenic fermentation
of fruit and vegetable wastes produces lactic acid (Wu et al., 2015) whereas in solid state
fermentation they are hydrolysed using crude enzyme mixtures to produce succinic acid (Dessie
et al., 2018).
1.1.3. Dairy
Around 29 million tonnes of dairy products are wasted in Europe every year. This dairy waste is
derived from the processing industry, spoilage of the dairy products due to microbial attack, and
7
inappropriate handling (Mahboubi et al., 2017). Dairy waste consists of complex organic
constituents like fat, protein, sugar, traces of food additives, and detergents that are used for
maintaining proper hygiene and clean in place (CIP). Dairy products are the most perishable
commodities due to their rich composition and absorbability. Fungal contamination in milk
India is reported as the largest milk producing nation and simultaneously produces 1 to 3 times
of effluent for every volume of processed milk, thus generating 3.739 - 11.217 million m3 of
waste per year. While manufacturing of cheese, a considerable amount of whey is produced as a
al., 2016). Another constituent of dairy produce i.e. raw milk, contaminates groundwater due to
the presence of ammonia, nitrogen, and nitrate that is converted to nitrite thereby causing
methemoglobinemia. During processing of raw milk around 2.5- 3.0 litres of wastewater is
generated per litre of processed milk (Singh et al., 2014), carrying about 14–830 mg/l of total
nutrients, like carbohydrates, lipids, proteins. Milk proteins dissociates and gives rise to organic
and inorganic forms of nitrogen such as nucleic acids, urea, proteins, and NO− 2, NO− 3, NH+ 4
respectively (Kushwaha et al., 2011). It was found that elevated concentration of NO3 > 40 mg/L
This raises serious environmental concerns and demands the employment of microbial assisted
method of waste conversion including activated sludge, sequencing batch reactor, tickling filter,
anaerobic sludge blanket, and aerated lagoons (Dias et al., 2014). Dairy waste is rich in organic
matter, facilitating the growth of microorganisms hence a large number of value-added products
can be obtained by utilizing dairy industry waste like lactose and protein (Lapppa et al., 2019). It
8
is a suitable substrate for ethanol production using Saccharomyces cerevisiae via enzymatic
hydrolysis of fermentable sugar (Parashar et al., 2016). Filamentous fungi produce a variety of
enzymes capable of hydrolyzing complex carbohydrates to simple sugar hence aids in high
quality biomass production that can be used as animal / fish feed and even for human
consumption as single cell protein with a GRAS status (Mahboubi et al., 2017).
Edible oil industry generate waste during various steps of refining process like degumming,
rancidity is caused due to the oxidation of lipids, aging, moisture, presence of oxygen and
effluent coming out of industry laden with lots of fatty acids, carbohydrates and protein (Okino-
Delgado et al., 2017). Waste cooking oil is an oil-based substance that resulted from multiple
deep fat frying process which makes fat unsuitable for human consumption due to the formation
of polar compounds like free short-chain fatty acids, mono- and di-glycerides, aldehydes,
ketones, polymers, cyclic and aromatic compounds. It was reported that edible oil industry
annually produces 350.9 million tonnes of de-oiled cake and oil meal as a by-product, which is a
concentrated source of protein. After pretreatment, this waste is further utilized for preparing
human nutrition products, animal feed and fertilizer (Chang et al., 2018).
Traditionally, effluents from oil processing industry were released directly into the soil and
groundwater which leads to oily film formation on aquatic surface causing a serious threat to
survival of aquatic animals, blockage of sewage and drains due to emulsification of organic
matter, oil methanization worsening greenhouse effect (Okino-Delgado et al., 2017). Advance
methods employ microbial cells for biodegradation of organic matter from effluents, thereby
9
aeruginosa synthesized biosurfactants such as rhamnolipids and glycolipids, biodiesel
production using lipase, liquid hydrocarbon biofuels (Henkel et al., 2012; Chen et al., 2018).
Edible oil industry waste was reported to be a cheap source for health constructive products such
as tocopherols, sterols, squalene, which were used in different industries as raw material, e.g.,
food for SCP production (Diwan et al., 2018), pharmaceutical formulations and cosmetics in the
Meat poultry and egg processing industry is a huge segment of food chain system. European
Union annually accounts for approximately 11 million tonnes of production. About 3.5 billion
pounds of beef was produced by Canada in 2006, contributing $26 billion to its economy.
generated (Ning et al., 2018). This comprises 49% from cattle, 47% from sheep and lambs, 44%
from pigs and 37% from chicken 37%, which is inedible in nature, thereby generating a huge
Major wastes material generated in industry include feathers, hairs, skin, horn, hooves, soft meat,
deboning residues, bones, etc. In addition to this, the slaughter house wastewater consists of
blood residue, protein, animal fat (lard and tallow), detergent residues and high organic matter
(carbon, nitrogen and phosphorous). Rendering of perishable animal waste extends a possible
alternative way to eradicate the environmental issue along with revenue generation. Rendering
industries produces meat and bone meal, hydrolyzed feather meal, blood meal, fish meal, animal
fats (lard and tallow) (Yaakob et al., 2019). Lactic acid fermentation of slaughterhouse waste is a
promising approach to utilize slaughterhouse waste for the production of lactic acid bacteria that
can be used as a probiotic product (Ashayerizadeh et al., 2017). Due to high nutritional
10
composition slaughterhouse waste can be utilized for various value-added product generation
like biomass (Scenedesmus sp.) as fish feed (Yakoob et al., 2019), a clean energy substitute i.e.
methane produced by anaerobic digestion of wastewater (Ning et al., 2018), biogas production
from poultry litter, blood in food applications (blood sausage, blood cake, blood pudding, blood
curd) and non-food application (fertilizer, binder) (Adhikari et al., 2018). Biodiesel has been
produced from chicken manure biochar by pseudo catalytic transesterification reaction, from
pork fatty waste by fermentation employing Staphylococcus xylosus and from eggshells by
industry.
Marine ecosystem supplies around 20% of the world’s food to humans, therefore plays a vital
role in feeding a significant population of the world. It is estimated that around 183 million
tonnes of seafood would be needed by 2030 for feeding. Generally, 50-70 % of seafood raw
material is wasted every year (Kumar et al., 2018). Globally producing about 6-8 million tonnes
of waste in the form of crabs, shrimp and lobster shells, where Southeast Asia contributes 1.5
million tonnes in totality. In seafood’s the utilizable mass of marine animal is less, crabs yield
40% meat of whole mass, in tuna fishes only 75 % of fillets is available. This generates a huge
amount of waste, including inedible parts like shrimp shells, crab shell, prawn waste, fish scales
and endoskeleton shell of crustacean. Shells and scales of aquatic animals such as shrimps,
lobsters and fishes harbor useful chemicals such as protein, chitin and calcium carbonate. Dried
shrimps and crabs contain about 50% of chitin on dried basis, generating a revenue of around
$100-120 per tonne (Yan and Chen, 2015), and is used as animal feed supplement, bait or
11
fertilizer. Seafood waste is chitinaceous in nature, harbouring pathogenic microbes, carcinogens,
aflatoxins and other health risks it can cause due to bioaccumulation of these contaminants.
The conventional method for seafood waste disposal includes ocean dumping, incineration,
landfilling, and wastewater discharge of seafood processing industry. It contains high organic
material load that potentially causes euthrophication and oxygen depletion of receiving water
bodies (Yan and Chen, 2015). Chitin, the major component of seafood waste is insoluble in
water and inert to most of chemical agents hence leads to environmental pollution and bio-
fouling, thus stipulating biological processing of this waste material as a step toward
Indian shrimp processing industries produces more than 0.15 million tonnes of shrimp waste
annually. Waste of shrimp processing industries was used to produce nutraceutical compound
in crustacean waste that was extracted through oxidative transformations of ingested β-carotene
extracted from exoskeletons of crustaceans waste. It was reported to exhibit antibacterial activity
against Enterococcus faecalis, Escherichia coli, Staphylococcus aureus, and Candida albicans
(Hussein et al., 2012). Glycosaminoglycans (GAGs) extracted from marine animal waste is of
better quality to that of terrestrial organisms (Valcarcel et al., 2017). Waste of Seafood
processing industries is a potential source for functional and bioactive compounds produced
12
Urbanization, rapid economic development and uncontrolled population growth has increased
the consumption of food leading to many folds increase in the generation of kitchen waste
annually (Zhao et al., 2017). In 2011, rural areas of China produced 200,000 kg of domestic
waste. Presently China is producing more than 30 million tonnes of kitchen waste every year. It
has been estimated that annually 2.5 billion tonnes of FW is produced by European Union out of
Kitchen waste (KW) is a kind of anthropogenic organic waste, usually discharged from public
catering rooms, restaurants, households, canteens of school and factory etc. (Li et al., 2017; Zhao
et al., 2017; Liu et al., 2019). The waste generated by restaurants, commercial and institutional
kitchens is different from municipal solid waste and is referred to as kitchen waste (KW). KW
includes fruits, vegetables, cooked food wastes, meat, used fat, oil and grease. On wet basis KW
broadly comprises of fruits 38.2%, vegetables 41.5%, staple food 7.6%, egg shell bones 7.2%,
shells and pits 2.5%, and meat 2.3% (Zhao et al., 2017). Chemically it comprises of carbohydrate
polymers (cellulose, hemicellulose, pectin and starch), protein, lignin, fats, organic acids,
inorganic salts and others (Chen et al., 2017; Zhao et al., 2017). KW is generated during various
food processing operations such as handling, processing, production, storage, transportation and
activities like washing and rinsing foodstuffs, cooking, cleaning dishes, cooking utensils, and
general housekeeping.
incineration and direct or indirect discharge of wastewater into the environmental system is
detrimental to the ecosystem and human health (Chen et al., 2019). Kitchen waste is
biodegradable biomass with higher moisture content and a pool of nutrients facilitating the
13
growth of pathogenic microorganisms causing rotting and breeding of flies and mosquitoes in
shorter span of time. It emits toxic substances, greenhouse gases, a huge amount of leachate in
water bodies and foul smell of ammonia and hydrothion. Ammonia produced during
decomposition of kitchen waste has strong, pungent order which can cause serious irritation in
the respiratory tract, redness of eyes and skin, while hydrothion is highly toxic to humans (Zhao
et al., 2017). The uncontrolled generation and improper management could produce lethal and
life-threatening consequences on the environment. It was reported that kitchen waste could be
used as a substrate for generation of numerous high value products viz. biosurfactant production
using Pseudomonas aeruginosa (Chen et al., 2018), butanol production by enzymatic hydrolysis
(Chen et al., 2017), lactic acid production by Lactobacillus amylophilus, volatile fatty acids and
hydrogen from mixed culture (Liu et al., 2019), cellulose production via Aspergillus niger in
can be used to harness energy liberating products like biogas, bioelectricity, biodiesel, etc.
Nano-composites, biopolymers and edible film like materials can be synthesized using FW as
pigment, nutraceuticals, dietary fiber, organic acids, high fructose syrup, single-cell protein,
Waste framework directive 2008/98/EC laws defines waste as “any substance or object which
substance involving straw, bagasse, molasses, spent grains, husk (rice, maize, and wheat), shell
14
(walnut, coconut, and groundnut), skin (banana, avocado), crop stalks (cotton), plant waste,
livestock and poultry manure (Dai et al., 2018). In 2013, FAO reported that about 250 million
tonnes of non-edible plant waste from different crop processing is generated as agro-industrial
waste (Heredia-Guerrero et al., 2017). Being world’s largest grain producer, China produced
1.75×109 tons of agriculture waste, of which 9.93×108 tonnes was contributed by crop straw,
4.52×108 tonnes from livestock and poultry manure, and 3.03×108 tonnes from forest residues in
2013 (Dai et al., 2018). Asia alone generates 4.4 billion tonnes of solid wastes annually. Agro-
industrial waste generation from different sources in India is more than 350 million tonnes per
Traditionally, agricultural waste is either incinerated/burnt off or allowed to rot in fields, thereby
causing serious air pollution and is also exacerbating soil pollution, water pollution and food
contamination. These traditional approaches liberate toxic gases (such as N2O, SO2, CH4,),
smoke, greenhouse gases into thfe air, and other carcinogenic chemicals such as dioxins, furans
and polycyclic aromatic hydrocarbons, which are detrimental to the environment as well as for
human health. Exposure to these chemicals causes severe development damage in fetuses,
infants, children, and adults (Cheng and Hu, 2010). Agricultural waste is biodegradable and
hemicellulose), proteins, lignins, fibers, minerals, vitamins, and others (Madurwar et al., 2013).
Agriculture waste is porous and loose in constitution containing carboxyl, hydroxyl, and other
reactive groups, so agricultural biomass can be used for wastewater remediation as an adsorption
material, hence “reducing waste by waste” (Dai et al., 2018). Apart this, the chemical
15
a number of products such as bioplastic from cuticles present on the outer layer of plants parts
Agriculture waste can be a cheap and natural substitute for production of multiple high valued
products. Microbes can readily feed upon agriculture waste to generate an array of high end
glucosidase, amylase, glucoamylase) by utilizing peels, seeds, oil cakes, field residues, and bran
(Bogar et al., 2003b; Selvakumar et al., 1998; Singh et al., 2006). Xanthan is a type of
exopolysaccharide that acts as food additive in food industry and is reported to be produced by
Food additives play a significant role in enhancing the technological properties of food.
Mushroom is ecology and economy balancing crop derived of lignocellulosic agro waste (wheat
paddy, rice paddy, banana leaves, cotton stalks) by mushroom fungi Lentinula edodes and
Pleurotus sp. (Philippoussis, 2009). Agro-industrial waste is reported to be a good carrier for
Agricultural material can be utilized to produce suitable substitutes of construction material with
improved qualities like light weight, biodegradable and eco-friendly material. It can be used to
develop several construction items like fiber-board made from cotton stalk with no chemical
additives, thermal insulating walls and roofs, waste-create bricks made from recycled paper mills
waste and cotton waste. Cement replacer is manufactured from sugar industries waste (bagasse
ash) and oil palm shell as a coarse aggregate for structural concrete production (Madurwar et al.,
2013).
16
The current strategies of landfilling or incinerating FW do not eliminate the environmental and
economic stress thus valorization is gaining much interest. FW can be converted to different
forms of energy molecules or biofuels, viz. biogas, hydrogen, ethanol and biodiesel, butanol and
2.1.1. Biodiesel
Increasing environmental pollution, fuel demand, and depletion of fossil fuels have intensified
the requirement of alternative fuels. Biodiesel emerges as an alternative fuel that can be acquired
from oils and fats. It is a green fuel whose production is expensive because of the high cost of
feedstock, thus in order to reduce the cost, possibility to utilize FW as lost cost feedstock have
oleaginous microorganisms (Kiran et al., 2014). Microbial oils have similar fatty acid
composition as plant oil thus microbial oils can be used as raw material for production of
biodiesel. FW hydrolyzate can be used as nutrient source and culture medium for the cultivation
of microalgae for biodiesel production. Aspergillus oryzae and Aspergillus awamori was used to
pyrenoidosa and Schizochytrium mangrovei yielding 10-20 g biomass. The fatty acids produced
by C. pyrenoidosa and S. mangrovei were suitable for the production of biodiesel (Pleissner et
al., 2013). Waste cooking olive oil was reported to serve as a substrate by Penicillium expansum
and five different strains of Aspergillus sp. for the production of biomass rich in lipid. Among
these, Aspergillus sp. ATHUM 3482 yielded highest amount of lipid 0.64 g/g dry cell weight
(Papanikolaou et al., 2011). Biodiesel production from vegetable oils, animal fats and butter was
17
reported to globally yield 24.5 GJ energy per year (Kiran et al., 2014). Cubas et al., (2016)
reported biodiesel production employing corona discharge plasma reactor technology (CDPT).
This technique offers several advantages such as increased esterification, easy biodiesel
separation, and no co-product generation. CDPT has been efficiently used for biodiesel
2.1.2. Ethanol
Wide industrial application of ethanol has increased its demand globally. It is prominently used
as a feedstock chemical for synthesis of ethylene (Kiran et al., 2014) and an essential raw
material for production of polyethylene. Traditionally cellulose and starchy crops, e.g. sugar
cane, rice, and potato were used for production of bio based ethanol (Thomsen et al., 2003).
Commercial enzymes are available to convert starch to glucose which is further fermented to
2014). Thus FW with low cellulosic content serves as a better alternative for the production of
bioethanol. To improve the purity and yield of ethanol, FW is autoclaved prior to fermentation,
as harsh or thermal treatment may cause partial degradation of nutritional components and sugars
(Sakai and Ezaki 2006). Dried FW has reduced surface area which results in decreased reaction
efficiency between substrate and enzyme, thus fresh and wet FW was reported to be an efficient
source for ethanol production. Furthermore as cellulose or starch cannot be directly converted to
(Kiran et al., 2014). For this a mixture of enzymes namely glucoamylase, α-amylase, β-amylase
and pullulanase etc. will be added for high molecular weight substrates. Hong and Yoon, (2011)
utilizing 100 g of FW. Kitchen garbage and non-diluted FW was reported to yield 17.7 g/L/h and
18
0.49 g ethanol per g sugar by simultaneous saccharification and fermentation process (Ma et al.,
2009). Several countries including Japan, Finland and Spain had developed pilot scale plants to
2.1.3. Biohydrogen
Hydrogen is a potential renewable energy source with high energy yield of 142 MJ/kg
(Jarunglumlert et al., 2018). In nature, hydrogen is not readily available but can be produced
from primary energy source. Hydrogen being carbon free with the highest energy output and
yielding water on combustion is globally used as a substitute to fossil fuels (Nikolaidis and
Poullikkas, 2017). Biohydrogen is hydrogen gas produced employing biological processes. The
simultaneously recycles the waste generated, thus it has become the most favored method.
Carbohydrate-rich FW is preferred for the production of biohydrogen gas as it has 20 time higher
potential than protein or fat-based FW. Hydrogen production from FW had been reported
multiple stages (Kiran et al., 2014). Upflow anaerobic sludge blanket (UASB) and anaerobic
sequencing batch (ASBR) reactors have been used with high hydrogen producing rates because
of their high biomass concentration in the reactor (Karthikeyan et al., 2018). For these processes,
solid retention time (SRT), hydraulic retention time (HRT), and organic loading rate (OLR)
affect the production of hydrogen. An optimized SRT with low HRT enhanced the technical
feasibility and productivity of biohydrogen production. However, the role of a higher OLR is yet
debatable as it affects the process in both ways, suggesting an optimal OLR for maximum
19
As in anaerobic digestion, the process of dark fermentation is set at low HRT with high acidic
condition to inhibit methanogenic activity. The dark fermentation process for the production of
biohydrogen from glucose follows two major pathways, viz. butyrate and acetate pathways that
utilize one mole of glucose, yielding two and four moles of biohydrogen, respectively
(Karthikeyan et al., 2018). Mixed cultures of Enterobacter and Clostridium produce hydrogen
from waste, which is readily utilized by hydrogenotrophic bacteria (Li and Fang 2007). Seed
acid bacteria whereas pretreated FW is dominated by biohydrogen producers (Kiran et al., 2014).
2.1.4. Methane
Anaerobic production of methane is favored because of its renewable energy source utilization,
low residual waste production and low cost. The waste produced through this process is nutrient
rich that can be used as soil conditioner or fertilizer (Kiran et al., 2014). The energy content of
methane is 55.5 MJ/kg. Anaerobic digestion produces methane through biodegrading and
reducing organic waste. The production of methane by this process is affected by several
parameters such as alkalinity, pH, organic loading rate, nutrients, reactor type, volatile fatty
characteristics (Park et al., 2018). A decrease in pH and volatile fatty acids accumulation
minimizes the production of methane gas during anaerobic digestion (Chen et al., 2008). Park et
al., (2018) reported that the use of microbial electrolysis cell (MEC) with anaerobic digestion
reactor enhances the methane production rate by 1.7 times as compared to the anaerobic
digestion reactor alone. MEC increases the rate of degradation of volatile fatty acids,
concentrated organic wastes and non-degradable organic matter thereby improving methane
20
production. During this process, methane is formed at cathode by electrons released from
reducing acidification rate, altering biological and physico-chemical properties, thus avoiding
process inhibition and improving the recovery of methane. The pretreatment process commonly
includes physical (grinding), thermal, acid and alkali treatment, high-pressure treatment, pulse
(Karthikeyan et al., 2018). Thermal treatment followed by alkali treatment is the best
pretreatment strategies for anaerobic digestion of FW. Alkali pretreatment enhanced the yield of
methane by 25%, whereas when combined with thermal treatment, the yield further enhanced to
32% (Naran et al., 2016). FW of 54 different fruits and vegetables produced 180–732 mL
methane per g volatile solid. Furthermore fruits and vegetables waste in a two stage anaerobic
digester yielded 530 mL per g volatile solid by utilizing 95.1% volatile solids (Kiran et al.,
2014). Zhao et al., (2017) reported the effect of presence of varying salt (NaCl) concentrations in
FW. They observed that low salt concentration increased the acidification and hydrolysis
2.1.5. Biobutanol
Butanol, a four carbon alcohol is considered more advanced biofuel compared to ethanol as it
offers several advantages such as improved combustion efficiency, higher energy density, lower
vapour pressure and property to dissolve in vegetable oils in order to reduce their viscosity
(Girotto et al., 2015). Traditionally, cane molasses and starch (corn, potato, and wheat) are used
for the production of biobutanol through fermentation process. Economic viability of biobutanol
21
production via fermentation process is mainly influenced by the substrate cost, which accounts
for about 50% of the cost of production (Ujor et al., 2014). Several studies have reported the
(Girotto et al., 2015; Huang et al., 2015; Ujor et al., 2014). Clostridium acetobutylicum produced
biobutanol through fermentation process by utilizing FW. Lactose-rich waste whey yielded 0.3 g
of butanol per g of carbohydrates (Girotto et al., 2015). Similar yields of biobutanol were
observed from starch-rich industrial FW such as bread liquid, batter liquid and inedible dough
(Ujor et al., 2014). Clostridium beijerinckii strain P260 utilized 81 g/L of FW procured from
retail store in Illinois, USA containing white bread, sweet corn, and mashed potatoes to produce
biobutanol with a yield of 0.38 g/g and a high productivity of 0.46 g/L/h (Huang et al., 2015).
beijerinckii strain BA101 upon action on different FW types, viz. agricultural waste yields 20.3
g/L and starch-rich packing peanuts 21.7 g/L whereas control starch yielded 24.7 g/L ABE. This
difference in production could be attributed to the difference in the nature of the waste material.
biobutanol production can be an efficient strategy for waste management, promoting economic
viability.
Since most of the FW generated was disposed through conventional methods like incineration,
compost, and landfill, which were uneconomical and unsustainable processes, leading to toxic
gas emission or ground water contamination (Paritosh et al., 2017). Thus, recovering energy or
sustainable approach. This can be achieved by anaerobically treating the FW in specific devices
22
such as microbial fuel cell (MFC) (Li et al., 2016). MFC utilizes microorganisms as catalyst for
domestic wastewater and excess sludge (Li et al., 2016; Cercado-Quezada et al., 2010). Briefly
in MFC, microorganisms oxidize organic matter transferring electrons to anode and at cathode
the oxidized compounds or oxygen get reduced microbially or by abiotic process (Cercado-
Quezada et al., 2010). Organic matter rich FW serves as energy source for electricigens in MFC,
hydrolysis of this organic fraction is the rate limiting step in electricity production (Li et al.,
2016). Pretreatment of FW employing microwave and sonication was reported to further enhance
substrate hydrolysis, which in turn increases the efficiency of electricity generation (Yusoff et
al., 2013). MFC containing FW leachate at a concentration of 5000 mg/L produced maximum
power 15.14 W/m3 and open circuit voltage of 1.12 V. Power output reduced with increasing
substrate concentration 20,000 mg/L; this reduction was attributed to anode chamber microbial
inhibition (Rikame et al., 2012). MFC performance was significantly decreased by the deposition
of cations and microorganisms on fouled membranes. Jia et al., (2013) reported the microbial
community structure in MFC loaded with FW collected from canteen of Harbin Institute of
Technology. They have reported a maximum 18 W/m3 power density at a chemical oxygen
demand (COD) of 3200 ± 400 mg/L. The 454 pyrosequencing of the amplified 16S rRNA gene
revealed the presence of different genera in anode biofilm of which fermentative Bacteroide and
exoelectrogenic Geobacter were the dominant ones. Food industry wastes such as wine lees,
yogurt waste and fermented apple juice in combination with two inoculums sources garden
compost and anaerobic sludge was evaluated for electricity production by MFC (Cercado-
Quezada et al., 2010). Of these, only yogurt waste inoculated with compost leachate exhibited
the generation of stable power density of 44 mW/m2. Organic fraction rich composite FW from
23
canteen of CSIR- Indian Institute of Chemical Technology (IICT), India generated electricity
upon action of anaerobic consortia as anodic biocatalyst in MFC. It was shown that OLR
significantly affected the production of electricity from FW. OLR at 1.01, 1.74, and 2.61 kg
COD/m3-day generated 188, 295, and 250 mV electricity, respectively (Goud et al., 2011).
3.1. Biosurfactants
diverse microorganisms including bacteria, fungi, and yeast (Gaur et al., 2019a; Gaur et al.,
2019b). Globally, they are estimated to generate a revenue of over 18 Billion USD with a market
of 30.64 Billion USD in 2016 (Singh et al., 2019). The compound annual growth rate of
biosurfactant market is estimated to be 5.6 % from 2017 to 2022. This increasing demand
impulse to explore cheap waste material as substrates thus reducing the production cost while
obligating waste management. Thus, FW from house-holds and various food industries can be
employed as substrate for biosurfactant production aiding in curtailing the production cost while
diminishing the pollution. One of the prominent FW produced from house-holds and commercial
kitchens is used waste oil. Kitchen waste oil (KWO) is rich in protein and moisture content, thus
utilized KWO over glucose, glycerol, molasses, and rapeseed oil as a fermentation substrate for
biosurfactant production (Chen et al., 2018). Another major waste from Indian food (dairy)
industry is from paneer production. With the annual production of 0.15 million tonnes of paneer
generated two million tonnes of waste whey, which is often released in the environment without
any pretreatment that leads to soil and water pollution (Parashar et al., 2016; Patowary et al.,
24
whey to yield 2.7 g/L of biosurfactant (Table. 2). The production further enhanced to 4.8 g/L by
additionally supplementing it with mineral salts and glucose (Patowary et al., 2016). Another
strain of Pseudomonas aeruginosa ATCC 10145 utilized soy molasses as sole carbon source for
biosurfactant which showed potential application as laundry detergent additives (Sajna et al.,
2013). Soy molasses is generated during soyabean processing having low commercial value,
although rich in proteins, carbohydrates, and lipids. Pseudomonas aeruginosa ATCC 10145
produce 11.7 g/L glycolipid biosurfactant by utilizing 120 g soy molasses as fermentation
substrate. Ramírez et al., (2015) reported that Bacillus subtilis and Pseudomonas aeruginosa
utilized olive oil mill waste (OW) to synthesize biosurfactant. These bacteria utilize remaining
oil in OW supplements as carbon source, whereas other waste components serve as nutrients.
3.2. Bio-plastics
Plastics are traditionally being synthesized from petrochemicals through irreversible processes
(Tsang et al., 2019). Petroleum derived polymers are difficult to degrade by microorganisms and
their high persistence poses serious environmental concerns thus an alternative to these synthetic
plastics, i.e., bioplastics comes into play. As microorganisms utilizing various waste products
can synthesize these bioplastics. These bioplastics are preferred over synthetic ones delineating
environmental burden while being ecofriendly. Substitution with bioplastics also offers a
reduction in global warming concern as the energy requirement for petroleum based synthetic
plastic production (77 MJ/kg) is more as compared to bioplastics (57 MJ/kg) (Gironi and
25
pretreatment to enhance biological and physico-chemical properties. The pretreatment strategies
include physical, chemical, biological and enzymatic hydrolysis. Physical treatment converts FW
into fermentable organic compounds employing thermal and mechanical processes, including
heating, milling, ultrasound, and microwaves (Tsang et al., 2019). Fermentable sugars are
formed using chemical treatment, which includes acid or alkali treatment. Biological treatment
hydroxybutyrate (PHB), polybutylene succinate (PBS), starch blends, polyvinyl alcohol (PVA)
and polylactic acid (PLA) are the major biodegradable polymers (Prabisha et al., 2015; Pandey
and Soccol, 1998; John et al., 2007; Ramachandran et al., 2007; Tripathi et al., 2019; Tsang et
al., 2019).
Alcaligenes sp. NCIM 5085 through an optimized fermentation process (7.5 L) utilized cane
molasses and yielded 70.89 % of high molecular weight PHB with 0.312 g/L/h productivity
(Tripathi et al., 2019). Another strain Halomonas campaniensis strain LS21 grew in cellulose,
starch, fatty acids, fats, and proteins rich FW and produced 70% PHB at 37 °C. Bacillus
megaterium SRKP-3 utilized dairy waste to produce PHB (Pandian et al., 2010, Tsang et al.,
2019). Felix et al., (2015) reported the production of bioplastics from freshwater red swamp
crayfish. As per the United States Department of Agriculture, 45 % of the Crayfish entering in
United States of America food market resulted in waste only. Guidelines by European Union
suggested the preferential use of FW as animal feed, but disease control concerns made it illegal.
Thus, valorizing FW by converting it to value-added products holds an ideal end use practice.
fertilizers are considered effective alternative improving yield of crops along with reduction in
26
methane emission. As per a market research, it has been estimated that emerging market of
organic fertilizer would touch a value of over $150-109 per annum by 2020. FW has been
vermicomposting (Du et al., 2018). Agriculture waste has been utilized for mushroom
cultivation as a substrate (Philippoussis et al., 2006). It reduces environmental burden and also at
the same time enhances crop productivity and changes soil bacterial community. Residue of
biogas production from FW can be used as organic fertilizers or soil conditioner due to
nutritional and carbon content along with macronutrients (N, K, P, Ca, Mg) and microelements
(Fe, Cu, Zn and Al) capable of improving and stimulating plant growth (Zhu et al., 2015).
anaerobic digestion, aerobic composting using microbes, chemical hydrolysis method (treating
FW via alkaline or acid hydrolysis at 600-1000 C), and in-situ degradation of natural organic
matter. It produces fertilizers in the form of digestate / soil conditioner, compost, soluble bio-
waste compost (SBC), degraded crop, minerals and as liquid organic fertilizers (Du et al., 2018).
Liquid organic fertilizers (LOF) are directly delivered at root zone of individual plant in
irrigation system and are therefore, advantageous in plant growth than other fertilizers. They are
readily available for absorption by plant and the quantity required per field is also less, as well as
the degradation process of LOF is quite easier (More et al., 2017). The efficacy of organic
methanotrophs (Singh and Strong 2016). Organic fertilizers can support the growth of
microalgae also. It can be used as an alternative nutrient medium to cultivate Chlorella vulgaris
4. Conclusion
27
Food is an indispensable commodity contributing to major section of organic waste generated
components viz. greenhouse gases, nitrates, ammonia etc.. Presently, microbial processing of
FW offers environmental protection and a sustainable way for the genesis of billion dollar
revenue. It can be concluded from this review that microorganisms can be efficiently employed
Acknowledgment
The authors do not received any financial support for publication of this article.
28
References
1. Adhikari, B., Chae, M., Bressler, D., 2018. Utilization of Slaughterhouse Waste in Value-
2. Anal, A.K., 2017. Food Processing By‐ Products and their Utilization: Introduction.
3. Ashayerizadeh, O., Dastar, B., Samadi, F., Khomeiri, M., Yamchi, A., Zerehdaran, S.,
2017. Study on the chemical and microbial composition and probiotic characteristics of
4. Benjamin, S. and Pandey, A., 1997. Coconut cake–a potent substrate for the production
pp.241-251.
5. Bogar, B., Szakacs, G., Linden, J.C., Pandey, A. and Tengerdy, R.P., 2003. Optimization
6. Bogar, B., Szakacs, G., Pandey, A., Abdulhameed, S., Linden, J.C. and Tengerdy, R.P.,
7. Bolivar-Telleria, M., Turbay, C., Favarato, L., Carneiro, T., de Biasi, R.S., Fernandes,
A.A.R., Santos, A. and Fernandes, P., 2018. Second-generation bioethanol from coconut
29
8. Cercado-Quezada, B., Delia, M.L., Bergel, A., 2010. Testing various food-industry
wastes for electricity production in microbial fuel cell. Bioresource Technology, 101(8),
pp.2748-2754.
9. Chang, F.C., Tsai, M.J., Ko, C.H., 2018. Agricultural waste derived fuel from oil meal
and waste cooking oil. Environmental Science and Pollution Research, 25(6), pp.5223-
5230.
10. Chen, C., Sun, N., Li, D., Long, S., Tang, X., Xiao, G., Wang, L., 2018. Optimization and
11. Chen, H., Shen, H., Su, H., Chen, H., Tan, F., Lin, J., 2017. High-efficiency
12. Chen, J., Ma, X., Yu, Z., Deng, T., Chen, X., Chen, L., Dai, M., 2019. A study on
catalytic co-pyrolysis of kitchen waste with tire waste over ZSM-5 using TG-FTIR and
13. Chen, Y., Cheng, J.J., Creamer, K.S., 2008. Inhibition of anaerobic digestion process: a
14. Cheng, H., Hu, Y., 2010. Municipal solid waste (MSW) as a renewable source of energy:
15. Cubas, A.L.V., Machado, M.M., Pinto, C.R.S.C., Moecke, E.H.S., Dutra, A.R.A., 2016.
Biodiesel production using fatty acids from food industry waste using corona discharge
30
16. Dai, Y., Sun, Q., Wang, W., Lu, L., Liu, M., Li, J., Yang, S., Sun, Y., Zhang, K., Xu, J.,
Zheng, W., 2018. Utilizations of agricultural waste as adsorbent for the removal of
17. Dede, O.H. and Ozdemir, S., 2018. Development of nutrient-rich growing media with
hazelnut husk and municipal sewage sludge. Environmental technology, 39(17), pp.2223-
2230.
18. Dessie, W., Zhang, W., Xin, F., Dong, W., Zhang, M., Ma, J., Jiang, M., 2018. Succinic
acid production from fruit and vegetable wastes hydrolyzed by on-site enzyme mixtures
19. Dias, T., Fragoso, R., Duarte, E., 2014. Anaerobic co-digestion of dairy cattle manure and
20. Díaz, A.I., Laca, A., Laca, A. and Díaz, M., 2017. Treatment of supermarket vegetable
66.
21. Diwan, B., Parkhey, P., Gupta, P., 2018. From agro-industrial wastes to single cell oils: a
22. Du, C., Abdullah, J.J., Greetham, D., Fu, D., Yu, M., Ren, L., Li, S., Lu, D., 2018.
Valorization of food waste into biofertiliser and its field application. Journal of Cleaner
23. Felix, M., Romero, A., Cordobes, F., Guerrero, A., 2015. Development of crayfish
bio‐ based plastic materials processed by small‐ scale injection moulding. Journal of the
31
24. Fewtrell, L., 2004. Drinking-water nitrate, methemoglobinemia, and global burden of
25. Galanakis, C.M. ed., 2017. Handbook of Grape Processing by-Products: Sustainable
26. Gaur, V.K., Bajaj, A., Regar, R.K., Kamthan, M., Jha, R.R., Srivastava, J.K. and
Manickam, N., 2019a. Rhamnolipid from a Lysinibacillus sphaericus strain IITR51 and
27. Gaur, V.K., Regar, R.K., Dhiman, N., Gautam, K., Srivastava, J.K., Patnaik, S.,
28. Gironi, F., Piemonte, V., 2011. Bioplastics and petroleum-based plastics: strengths and
29. Girotto, F., Alibardi, L., Cossu, R., 2015. Food waste generation and industrial uses: a
30. Goud, R.K., Babu, P.S., Mohan, S.V., 2011. Canteen based composite food waste as
potential anodic fuel for bioelectricity generation in single chambered microbial fuel cell
32
31. Heater, B.S., Chan, W.S., Lee, M.M. and Chan, M.K., 2019. Directed evolution of a
genetically encoded immobilized lipase for the efficient production of biodiesel from
32. Henkel, M., Müller, M.M., Kügler, J.H., Lovaglio, R.B., Contiero, J., Syldatk, C.,
33. Heredia-Guerrero, J.A., Heredia, A., Domínguez, E., Cingolani, R., Bayer, I.S.,
Athanassiou, A., Benítez, J.J., 2017. Cutin from agro-waste as a raw material for the
34. Hong, Y.S., Yoon, H.H., 2011. Ethanol production from food residues. Biomass and
35. Huang, H., Singh, V., Qureshi, N., 2015. Butanol production from food waste: a novel
36. Hussein, M.H., El-Hady, M.F., Shehata, H.A., Hegazy, M.A., Hefni, H.H., 2013.
37. Jarunglumlert, T., Prommuak, C., Putmai, N., Pavasant, P., 2018. Scaling-up bio-
hydrogen production from food waste: Feasibilities and challenges. International Journal
38. Jesse, T.W., Ezeji, T.C., Qureshi, N., Blaschek, H.P., 2002. Production of butanol from
33
39. Ji, C., Kong, C.X., Mei, Z.L., Li, J., 2017. A review of the anaerobic digestion of fruit
40. Jia, J., Tang, Y., Liu, B., Wu, D., Ren, N., Xing, D., 2013. Electricity generation from
food wastes and microbial community structure in microbial fuel cells. Bioresource
41. John, R.P., Nampoothiri, K.M. and Pandey, A., 2007. Fermentative production of lactic
42. Karmee, S.K., 2016. Liquid biofuels from food waste: current trends, prospect and
43. Karmee, S.K., Linardi, D., Lee, J., Lin, C.S.K., 2015. Conversion of lipid from food
44. Karthikeyan, O.P., Trably, E., Mehariya, S., Bernet, N., Wong, J.W., Carrere, H., 2018.
Pretreatment of food waste for methane and hydrogen recovery: a review. Bioresource
45. Kiran, E.U., Trzcinski, A.P., Ng, W.J., Liu, Y., 2014. Bioconversion of food waste to
46. Kondamudi, N., Mohapatra, S.K. and Misra, M., 2008. Spent coffee grounds as a
versatile source of green energy. Journal of agricultural and food chemistry, 56(24),
pp.11757-11760.
47. Kumar, A., Kumar, D., George, N., Sharma, P., Gupta, N., 2018. A process for complete
34
simultaneous production of chitinase and chitin oligosaccharides. International journal of
48. Kumar, S., Sangwan, P., Dhankhar, R.M.V. and Bidra, S., 2013. Utilization of rice husk
and their ash: A review. Res. J. Chem. Env. Sci, 1(5), pp.126-129.
49. Kushwaha, J.P., Srivastava, V.C. Mall, I.D., 2011. An overview of various technologies
for the treatment of dairy wastewaters. Critical reviews in food science and
50. Lam, M.K., Lee, K.T., 2012. Potential of using organic fertilizer to cultivate Chlorella
51. Lappa, I.K., Papadaki, A., Kachrimanidou, V., Terpou, A., Koulougliotis, D., Eriotou, E.,
Kopsahelis, N., 2019. Cheese Whey Processing: Integrated Biorefinery Concepts and
52. Li, C., Fang, H.H., 2007. Fermentative hydrogen production from wastewater and solid
53. Li, H., Tian, Y., Zuo, W., Zhang, J., Pan, X., Li, L., Su, X., 2016. Electricity generation
54. Li, P., Zeng, Y., Xie, Y., Li, X., Kang, Y., Wang, Y., Xie, T., Zhang, Y., 2017. Effect of
35
55. Liu, W., Dong, Z., Sun, D., Chen, Y., Wang, S., Zhu, J., Liu, C., 2019. Bioconversion of
kitchen wastes into bioflocculant and its pilot-scale application in treating iron mineral
56. Ma, H., Wang, Q., Qian, D., Gong, L., Zhang, W., 2009. The utilization of acid-tolerant
bacteria on ethanol production from kitchen garbage. Renewable Energy, 34(6), pp.1466-
1470.
57. Madurwar, M.V., Ralegaonkar, R.V., Mandavgane, S.A., 2013. Application of agro-
58. Mahboubi, A., Ferreira, J.A., Taherzadeh, M.J. and Lennartsson, P.R., 2017. Value-added
products from dairy waste using edible fungi. Waste management (New York, NY), 59,
p.518.
59. Marques, R.V., Paz, M.F.D., Duval, E.H., Corrêa, L.B., Corrêa, É.K., 2016.
Staphylococcus xylosus fermentation of pork fatty waste: raw material for biodiesel
60. Matharu, A.S., de Melo, E.M., Houghton, J.A., 2016. Opportunity for high value-added
chemicals from food supply chain wastes. Bioresource technology, 215, pp.123-130.
61. More, A., Srinivasan, A., Liao, P.H., Lo, K.V., 2017. Microwave enhanced oxidation
treatment of organic fertilizers. Journal of the science of food and agriculture, 97(10),
pp.3233-3239.
62. Murthy, P.S., Naidu, M.M., 2012. Sustainable management of coffee industry by-
products and value addition—A review. Resources, Conservation and recycling, 66,
pp.45-58
36
63. Naran, E., Toor, U.A., Kim, D.J., 2016. Effect of pretreatment and anaerobic co-digestion
64. Nikolaidis, P., Poullikkas, A., 2017. A comparative overview of hydrogen production
65. Ning, Z., Zhang, H., Li, W., Zhang, R., Liu, G., Chen, C., 2018. Anaerobic digestion of
66. Nishimura, H., Tan, L., Kira, N., Tomiyama, S., Yamada, K., Sun, Z.Y., Tang, Y.Q.,
Morimura, S., Kida, K., 2017. Production of ethanol from a mixture of waste paper and
67. Okino-Delgado, C.H., Do Prado, D.Z., Facanali, R., Marques, M.M.O., Nascimento,
A.S., da Costa Fernandes, C.J., Zambuzzi, W.F., Fleuri, L.F., 2017. Bioremediation of
cooking oil waste using lipases from wastes. PloS one, 12(10), p.e0186246.
68. Panda, S.K., Mishra, S.S., Kayitesi, E., Ray, R.C., 2016. Microbial-processing of fruit
and vegetable wastes for production of vital enzymes and organic acids: Biotechnology
69. Pandey, A. and Soccol, C.R., 1998. Bioconversion of biomass: a case study of ligno-
70. Pandey, A. and Soccol, C.R., 2000. Economic utilization of crop residues for value
addition: A futuristic approach, Journal of Scientific and Industrial Research, 59, 12-22.
37
71. Pandian, S.R., Deepak, V., Kalishwaralal, K., Rameshkumar, N., Jeyaraj, M.,
Gurunathan, S., 2010. Optimization and fed-batch production of PHB utilizing dairy
waste and sea water as nutrient sources by Bacillus megaterium SRKP-3. Bioresource
72. Papageorgiou, M., Skendi, A., 2018. Introduction to cereal processing and by-products.
73. Papanikolaou, S., Dimou, A., Fakas, S., Diamantopoulou, P., Philippoussis, A.,
cooking olive oil into lipid‐ rich biomass using Aspergillus and Penicillium
74. Parashar, A., Jin, Y., Mason, B., Chae, M., Bressler, D.C., 2016. Incorporation of whey
permeate, a dairy effluent, in ethanol fermentation to provide a zero waste solution for the
75. Parate, V.R., Talib, M.I., 2015. Characterization of tur dal (Cajanuscajan) husk carbon
and its kinetics and isotherm study for removing Cu (II) ions. IOSR J. Environ. Sci.,
76. Paritosh, K., Kushwaha, S.K., Yadav, M., Pareek, N., Chawade, A., Vivekanand, V.,
2017. Food waste to energy: an overview of sustainable approaches for food waste
77. Park, J., Lee, B., Tian, D., Jun, H., 2018. Bioelectrochemical enhancement of methane
production from highly concentrated food waste in a combined anaerobic digester and
38
78. Patowary, R., Patowary, K., Kalita, M.C., Deka, S., 2016. Utilization of paneer whey
Springer, Dordrecht.
80. Pleissner, D., Lam, W.C., Sun, Z., Lin, C.S.K., 2013. Food waste as nutrient source in
81. Prabisha, T.P., Sindhu, R., Binod, P., Sankar, V., Raghu, K.G. and Pandey, A., 2015.
Production and characterization of PHB from a novel isolate Comamonas sp. from a
dairy effluent sample and its application in cell culture. Biochemical engineering journal,
101, pp.150-159.
82. Prameela, K., Venkatesh, K., Immandi, S.B., Kasturi, A.P.K., Krishna, C.R., Mohan,
C.M., 2017. Next generation nutraceutical from shrimp waste: The convergence of
83. Ramachandran, S., Singh, S.K., Larroche, C., Soccol, C.R. and Pandey, A., 2007. Oil
pp.2000-2009.
84. Ramírez, I.M., Tsaousi, K., Rudden, M., Marchant, R., Alameda, E.J., Román, M.G.,
Banat, I.M., 2015. Rhamnolipid and surfactin production from olive oil mill waste as sole
39
85. Rikame, S.S., Mungray, A.A., Mungray, A.K., 2012. Electricity generation from
acidogenic food waste leachate using dual chamber mediator less microbial fuel
86. Rodrigues, M.S., Moreira, F.S., Cardoso, V.L., de Resende, M.M., 2017. Soy molasses as
pp.18699-18709.
87. Rohm, H., Brennan, C., Turner, C., Günther, E., Campbell, G., Hernando, I., Struck, S.,
Kontogiorgos, V., 2015. Adding value to fruit processing waste: innovative ways to
incorporate fibers from berry pomace in baked and extruded cereal-based foods—a
88. Sabu, A., Sarita, S., Pandey, A., Bogar, B., Szakacs, G. and Soccol, C.R., 2002. Solid-
89. Sadh, P.K., Duhan, S., Duhan, J.S., 2018. Agro-industrial wastes and their utilization
using solid state fermentation: a review. Bioresources and Bioprocessing, 5(1), p.1.
90. Sajna, K.V., Sukumaran, R.K., Jayamurthy, H., Reddy, K.K., Kanjilal, S., Prasad, R.B.
and Pandey, A., 2013. Studies on biosurfactants from Pseudozyma sp. NII 08165 and
91. Sakai, K., Ezaki, Y., 2006. Open L-lactic acid fermentation of food refuse using
40
92. Schieber, A., 2017. Side streams of plant food processing as a source of valuable
compounds: Selected examples. Annual review of food science and technology, 8, pp.97-
112.
93. Selvakumar, P., Ashakumary, L. and Pandey, A., 1998. Biosynthesis of glucoamylase
from Aspergillus niger by solid-state fermentation using tea waste as the basis of a solid
94. Sherazi, S.T.H., Mahesar, S.A., 2016. Vegetable oil deodorizer distillate: a rich source of
95. Singh, J.S., Strong, P.J., 2016. Biologically derived fertilizer: a multifaceted bio-tool in
96. Singh, N. B., Singh, R., Imam, M. M. 2014. Waste water management in dairy industry:
97. Singh, P., Patil, Y., Rale, V., 2019. Biosurfactant production: emerging trends and
98. Singh, S.K., Ahmed, S.U. and Pandey, A., 2006. Metabolic engineering approaches for
99. Sui, W., Xiao, Y., Liu, R., Wu, T., Zhang, M., 2019. Steam explosion modification on tea
100. Tan, L., Sun, Z., Zhang, W., Tang, Y., Morimura, S., Kida, K., 2014. Production of bio-
fuel ethanol from distilled grain waste eluted from Chinese spirit making
41
101. Thomsen, A.B., Medina, C., Ahring, B.K., 2003. Biotechnology in ethanol production.
102. Tripathi, A.D., Raj Joshi, T., Kumar Srivastava, S., Darani, K.K., Khade, S., Srivastava,
103. Tsang, Y.F., Kumar, V., Samadar, P., Yang, Y., Lee, J., Ok, Y.S., Song, H., Kim, K.H.,
Kwon, E.E., Jeon, Y.J., 2019. Production of bioplastic through food waste
104. Ujor, V., Bharathidasan, A.K., Cornish, K., Ezeji, T.C., 2014. Feasibility of producing
butanol from industrial starchy food wastes. Applied energy, 136, pp.590-598.
105. Valcarcel, J., Novoa-Carballal, R., Perez-Martín, R.I., Reis, R.L., Vázquez, J.A., 2017.
106. Verni, M., Rizzello, C.G., Coda, R., 2019. Fermentation biotechnology applied to cereal
107. Wu, Y., Ma, H., Zheng, M., Wang, K., 2015. Lactic acid production from acidogenic
108. Yaakob, M.A., Mohamed, R.M.S.R., Al-Gheethi, A., Tiey, A., Kassim, A.H.M., 2019.
using response surface methodology and potential utilisation as fish feeds. Environmental
42
109. Yan, N., Chen, X., 2015. Sustainability: Don't waste seafood waste. Nature
110. Yang, X., Lee, S.J., Yoo, H.Y., Choi, H.S., Park, C. and Kim, S.W., 2014. Biorefinery of
111. Yusoff, M.Z.M., Hu, A., Feng, C., Maeda, T., Shirai, Y., Hassan, M.A., Yu, C.P., 2013.
Influence of pretreated activated sludge for electricity generation in microbial fuel cell
112. Zhao, J., Liu, Y., Wang, D., Chen, F., Li, X., Zeng, G., Yang, Q., 2017. Potential impact
113. Zhao, K., Xu, R., Zhang, Y., Tang, H., Zhou, C., Cao, A., Zhao, G., Guo, H., 2017.
114. Zhu, N.M., Luo, T., Guo, X.J., Zhang, H., Deng, Y., 2015. Nutrition potential of biogas
residues as organic fertilizer regarding the speciation and leachability of inorganic metal
43
Legends
Table. 1. Value added and bioactive compounds from different food processing industrial waste.
44
13532 Banana Lignin, pectin, cellulose, Schieber 2017;
hemicellulose, phenolic Kiran et al., 2014
compounds (prodelphinidins,
flavonol glycosides),
procyanidins, and flavanols
45
(cellulose, hemicelluloses,
lignin, pectin, gums)
NA Tea Caffeine, polyphenols, Sui et al., 2019
triacontanol, and saponins
Dairy 16560 Milk Biodiesel, ethanol, whey Kiran et al., 2014;
Industry protein, Lactose, baker’s yeast, Parashar et al., 2016;
and minerals Lapppa et al., 2019
Meat and 1344.5 Meat and Fertilizer, animal feed, blood Kiran et al., 2014;
Seafood poultry meal, meat and bone meal, Ning et al., 2018;
Processing feather meal, lactic acid, and Yaakob et al., 2019
Industry probiotics,
NA Fishes Chitosan, and Prameela et al., 2017
glycosaminoglycans,
6000 to Shrimps Nutraceuticals (Astaxanthin), Kiran et al., 2014,
8000 chitin and chitinase Yan and chen, 2015;
Prameela et al., 2017;
Kumar et al., 2018
Crabs Chitin, calcium carbonate and Yan and chen, 2015
protein
Lobster Chitin Yan and chen, 2015
Edible oil 21462 Oil Biosurfactants Henkel et al., 2012,
Industry like rhamnolipids and Kiran et al., 2014
glycolipids, biodiesel,
tocopherols, sterols, squalene,
and single cell protein
Olives Phenolic compounds, Kiran et al., 2014;
polyphenols, carotenoids, Schieber 2017
phytosterols, squalene, and
dietary fiber
46
S. No. Substrate Biological Process Microbes Product References
Associated Associated Obtained
1. Noodle Waste Saccharification Saccharomyces Bioethanol and Yang et al.,
and fermentation cerevisiae K35 Biodiesel 2014
2. Waste cooking Fermentation Penicillium Biodiesel Papanikolaou
olive oil expansum et al., 2011
3. Mixed Food Enzymatic A mixture of α- Bioethanol Karmee et
Waste (Potato Hydrolysis and amylase, al., 2016
peel waste, Fermentation βamylase, and
Banana Peel, glucoamylase;
Household Saccharomyces
waste) cerevisiae H058
4. Agricultural Enzymatic Carbohydrase, Hydrochars and Karmee et
residue waste hydrolysis and protease and bio-oil al., 2016
Flash Pyrolysis lipase
5. Cooking oil Enzyme Lipase Biodiesel Heater et al.,
waste immobilization 2019
6. Spent coffee Extraction and Catalyst (KOH) Biodiesel Kondamudi
grounds transesterification et al., 2008
7. Cane molasses Fermentation Clostridium Biobutanol Girotto et al.,
and starch rich acetobutylicum, 2015; Huang
food waste Clostridium et al., 2015;
beijerinckii Ujor et al.,
P260 2014
8. Mixed food Microbial Exoelectrogenic Methane Park et al.,
Waste electrolysis cell bacteria 2018
(MEC) and
Anaerobic
Digestion
10. Carbohydrate Fermentation, Up-flow Biohydrogen Kiran et al.,
rich food waste anaerobic sludge 2014,
blanket (UASB) Karthikeyan
and anaerobic et al., 2018
sequencing
batch (ASBR)
reactors
11. Industrial Microbial Fuel Cell Catalyst Electricity Li et al.,
wastewater (Microbial cells) 2016;
47
domestic Cercado-
wastewater Quezada et
and excess al., 2010
sludge
12. Kitchen waste Fermentation Pseudomonas Biosurfactant Chen et al.,
oil aeruginosa 2018
13. Soy molasses Fermentation Pseudomonas Glycolipid Rodrigues et
aeruginosa biosurfactant al., 2017
ATCC 10145
14. Dairy effluent Fermentation Pseudomonas Biosurfactant Patowary et
(cheese whey) aeruginosa al., 2016
SR17
15. olive oil mill Fermentation Bacillus subtilis Biosurfactant Ramírez et
waste and al., (2015
Pseudomonas
aeruginosa
16. Cane molasses Fermentation and Alcaligenes sp. Polyhydroxybutyr Tripathi et
biosynthesis NCIM 5085 ate (PHB) al., 2019
17. Nutrient-rich Hydrolysis, Halomonashydr Polyhydroxybutyr Tsang et al.,
food waste fermentation and othermalis, ate (PHB) 2019
Biosynthesis Halomonascamp
aniensis
18. Dairy waste Fermentation and Bacillus Polyhydroxybutyr Pandian et al.
biosynthesis megaterium ate (PHB) 2010, Tsang
SRKP-3 et al., 2019
19. Food waste Anaerobic Microbial cells Liquid organic Ma et al.,
digestion, aerobic fertilizer and solid 2019, More
composting fertilizers et al., 2017
48
49
Highlights
Biofuel and bio-electricity production using food waste reduces environmental burden.
50