Journal of Environmental Management xxx (xxxx) xxx–xxx
Contents lists available at ScienceDirect
Journal of Environmental Management
journal homepage: www.elsevier.com/locate/jenvman
Review article
Conversion of food and kitchen waste to value-added products
Raveendran Sindhua,∗, Edgard Gnansounoub, Sharrel Rebelloc, Parameswaran Binoda,
Sunita Varjanid, Indu Shekhar Thakure, Ramkumar B. Nairf, Ashok Pandeyg
a
Microbial Processes and Technology Division, CSIR-National Institute for Interdisciplinary Science and Technology (CSIR-NIIST), Trivandrum 695 019, India
Ecole Polytechnique Federale de Lausanne, ENAC GR-GN, GC A3, Station 18, CH, 1015, Lausanne, Switzerland
Communicable Disease Research Laboratory, St. Joseph's College, Irinjalakuda, India
d
Gujarat Pollution Control Board, Gandhinagar 382 010, India
e
School of Environmental Sciences, Jawaharlal Nehru University, New Delhi 110067, India
f
Mycorena AB, Stena Center 1A, 412 92 Gothenburg, Sweden
g
CSIR-Indian Institute of Toxicology Research (CSIR-IITR), 31 MG Marg, Lucknow 226 001, India
b
c
A R T I C LE I N FO
A B S T R A C T
Keywords:
Bioconversion
Value-added products
Biorefinery
Food waste
Utilisation
Food and kitchen waste - omnipresent in every corner of the world serve as an excellent source of value added
products owing to high organic content. Regardless of existence of various traditional methods of land filling or
biogas production used to harness food waste energy, effective conversion of food to valuable resources is often
challenged by its heterogenous nature and high moisture content. The current paper tries to lay down the
prospects and consequences associated with food waste management. The various social, economical and environmental concerns associated with food waste management especially in terms of green house gas emission
and extended rate of leachate generation also has been discussed. The difficulties in proper collection, storage
and bioconversion of food waste to valuable by-products are pointed as a big hurdle in proper waste management. Finally, the wide array of value added products developed from food waste after pretreatment are also
enlisted to emphasis the prospects of food waste management.
1. Introduction
Industrialization as well as improper waste management leads to
accumulation of large amount of kitchen and food waste. As per the
reports of FAO, a major portion of food produced, harvested and used is
lost as waste in almost all types of food as depicted in Fig. 1 (http://
www.fao.org/save-food/resources/keyfindings/en/). Improper waste
management leads to several health hazards as well as environmental
issues. Collection, storage as well as improper segregations are the
major concerns limiting proper waste conversion. Hence steps to be
adopted by Government by adopting strict rules as well as by introducing waste collection, sorting and storage centres to make it feasible to a certain extent.
Compared to the tonnes of waste generated, a proper waste management strategy is lacking in most of developing countries. Concepts of
waste to wealth strategy currently practiced in most industrialized
countries have solved this issue to a certain extent. Several countries
like USA, Japan, Singapore, Sweden, Canada as well as Germany have
operational waste to energy plants that proved the efficient conversion
of wastes to energy. This has dual benefits like waste management as
∗
well as contribution to energy security of the country. Most of the developing countries like India lack systems for proper waste management due to insufficient infrastructure, improper planning, policy framework and funds (Sharholy et al., 2008). Furthermore, the gap
between the policy and implementation is very large and is one of the
main barriers for efficient bioconversion.
Recent studies showed that though composting is an effective
method for bioconversion of waste, its main challenges are gaseous
emissions and impurities. Nitrous oxide and methane generated during
composting, contributes significantly to global warming. Their impact
is reported to be 310 and 20 times higher than carbon dioxide (Nasini
et al., 2016). In most countries, food wastes contribute almost half of
the total municipal wastes whereas; this percentage may be higher in
developing countries. Organic components of food wastes include
fruits, vegetables, cooked food wastes, meat etc. Food wastes are generated during production, handling, storage, processing and consumption (Gustavsson et al., 2011).
Esteban and Ladero (2018) reported an overview of food waste as a
source of value added chemicals and materials. This presents an overview of chemical, enzymatic and biotechnological processes for the
Corresponding author.
E-mail addresses: sindhurgcb@gmail.com, sindhufax@yahoo.co.in (R. Sindhu).
https://doi.org/10.1016/j.jenvman.2019.02.053
Received 31 August 2018; Received in revised form 7 February 2019; Accepted 8 February 2019
0301-4797/ © 2019 Elsevier Ltd. All rights reserved.
Please cite this article as: Raveendran Sindhu, et al., Journal of Environmental Management, https://doi.org/10.1016/j.jenvman.2019.02.053
Journal of Environmental Management xxx (xxxx) xxx–xxx
R. Sindhu, et al.
conventional energy. Food wastes are biodegradable and contain high
moisture hence suitable for the production of bioenergy by anaerobic
digestion. The major limitations in anaerobic digestion of food waste
are the lowering of pH during anaerobic digestion due to production of
volatile fatty acids. This will inhibit growth of methanogenic microbes.
Adopting integrated or alternative strategies can overcome this issue.
Previous studies revealed that focussing on the production of a single
product from food and kitchen waste is not economically viable. Several
research and developmental activities are going on throughout the
world for the conversion of heterogeneous food wastes to multiple
value added products, which will lead to the development a feasible
and economically viable strategy of bioconversion of food wastes
(Dahiya et al., 2018).
Fig. 1. Percentage of food lost in different food categories after production,
harvest and use as per reports of FAO.
3. Value added products from food and kitchen waste
production of chemicals and materials using food waste as raw material. Dahiya et al. (2018) reported a review on food waste biorefinery –
a sustainable strategy for circular bioeconomy. This review presents an
overview of various bioprocesses employed for the generation of energy
as well as various commodity chemicals.
Food and kitchen waste are mainly composed of organic fraction
that includes carbohydrates, proteins, fats, lipids as well as inorganic
components. The main challenge in conversion of food wastes is their
heterogeneous nature as well as high moisture content and low calorific
value. Composition of the food wastes varies depending upon the
source. Hence, a common strategy cannot be adopted for all food
wastes. Based on the source as well as composition, some kind of
treatment may be carried out to make it accessible for the growth of
microorganisms and to produce desired product of interest in an ecofriendly and economic way.
The present review gives an overview of different value added
products produced from food and kitchen wastes.
Different value added products can be produced from kitchen and
food wastes. This includes activated carbon adsorbent, antioxidants,
bioactives, bioethanol, biobutanol, biodiesel, biogas, bioelectricity,
biopolymer, bionanocomposite, chitosan, corrosion inhibitors, DHA,
industrial enzymes, films, high fructose syrup, levulinic acid, mushroom cultivation, nutraceuticals, organic acids, pigments, single cell
protein, sugars, vermicompost, wax esters and xanthan gum. Table 1
gives an overview of different value added products produced from
food and kitchen wastes.
3.1. Activated carbon adsorbent
Activated carbon adsorbent finds applications in various fields like
purification and separation in various industrial fields. Hence, its demand is increasing day by day. Saygili et al., (2015) reported conversion of grape industrial processing waste to activated carbon and its
application in the adsorption of cationic and anionic dyes.
The study revealed that grape industry processing waste as a low
cost and cleaner precursor for the production of low cost activated
carbon with activation with zinc chloride. It effectively removes cationic and anionic dyes from aqueous solution. The adsorption capacity
was found to be higher than commercially available as well as agrowaste based carbonaceous materials.
2. Current conversion strategies
Different types of waste conversion strategies are available which
can be adopted based on the properties of the waste (Fig. 2). Commonly
adopted conversion strategies include thermal, chemical or biochemical
conversions. Thermal conversions include gasification, pyrolysis and
incineration. Biochemical conversions include composting and anaerobic digestion. Recently several fermentation as well as combined
processes is available for the production of various industrially important products. Since food waste is a heterogeneous mixture, many
microbes cannot utilise this as such. Hence some kinds of physical or
chemical or combined pretreatment to be carried out to make it accessible for further enzymatic saccharification for the production of
value added products.
Most of the food wastes are used for land filling or for generation of
3.2. Antioxidants
Antioxidants are compounds that prevent oxidation of molecules to
form free radicals. Hence, these compounds play an important role as
preservatives in foods and cosmetics as well as function as oxidation
inhibitors in fuels. Antioxidants also reduce risk of certain human diseases. Synthetic antioxidants have potential health hazards. These lead
to increased consumption of natural antioxidants that have more health
benefits. Several food industry wastes like peels, seeds etc. serve as a
source for the production of antioxidants.
Amado et al., (2014) reported antioxidant extraction from potato
peel waste. The conditions for extraction were optimised by adopting a
response surface strategy optimising various process parameters like
temperature, solvent concentration and extraction time. The optimum
conditions of extraction were 34 min of extraction time, temperature of
89.9 °C and ethanol concentration of 71.2% and 38.6% for extraction of
phenolics and flavonoids respectively. The study revealed potato peel as
a good source for antioxidants that can effectively limit oxidation of
oils.
Barba et al., (2016) reported several green strategies for extraction
of antioxidant bioactive compounds from winery wastes and by-products like grapes stalk, grapes marc, grapes seeds etc. Grape seeds serve
as a rich source of antioxidant – vitamin E. These novel green strategies
seem to be superior when compared to conventional strategies in terms
of energy consumption and processing time as well as the use of
harmful and expensive solvents.
Fig. 2. An overview of food waste management.
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Table 1
Profile of value-added products from kitchen and food waste.
Section
Number
Product
Source
Microorganism
Reference
3.1.
3.2.
Activated carbon adsorbent
Antioxidant
3.3.
Bioactives
Grape industrial processing waste
Potato peel waste
Winery waste/by-products
Olive fruit/by-products
Marine processing waste/fish
–
–
–
–
–
3.4.1.
Bioethanol
Pineapple leaves
Potato peel/mash waste
Yeast
Aspergillus niger Saccharomyces
cerevisiae
Thermophilic anaerobe
–
Clostridium beijerinckii NCIMB 8052
Clostridium acetobutylicum ATCC 824
–
Saygili et al. (2015)
Amado et al. (2014)
Barba et al. (2016)
Wang et al. (2017)
Harnedy and FitzGerald
(2012)
Chintagunta et al., 2017
Chintagunta et al. (2016)
3.4.2.
Biobutanol
3.4.3.
Biodiesel
3.4.4.
Biogas
3.4.5.
Bioelectricity
3.5.1.
Biopolymer (Plastic films)
3.5.2.
Biopolymer (Medium chain length
polyhydroxyalkaonates)
Biopolymer (Polyhydroxybutyrate)
Bio-nanocomposite
3.5.3.
3.6.
3.7.
3.8.1.
Chitosan
Corrosion inhibitors
Docosahexanoic acid (DHA)
Amylase
3.8.2.
Cellulase
3.8.3.
3.8.4.
Protease
Pectinase
3.8.5.
3.9.
3.10.
3.11.
3.12.
Xylanase
pH indicator films
High fructose syrup
Levulinic acid
Mushroom cultivation
3.13.
Nutraceuticals
3.14.1.
3.14.2.
3.14.3.
Acetic acid
Fumaric acid
Citric acid
3.14.4.
Succinic acid
3.14.5.
Lactic acid
3.14.6.
3.14.7.
Propionic acid
Gluconic acid
Unprocessed food waste
Kitchen waste
Starchy food waste
Amorphophallus konjac waste
Mixed non-edible oils/castor seed
oil/waste fish oil
Waste pepper seeds
Waste palm oil
Waste oils with high acidic value
Food waste
Food waste
Orange peel biomass
Dhiman et al. (2017)
Nishimura et al. (2017)
Ujor et al. (2014)
Shao and Chen (2015)
Fadhil et al. (2017)
Lee et al. (2017)
Thushari and Babel (2018)
Hu et al. (2017)
Deepanraj et al. (2017)
Wu et al. (2016)
Miran et al. (2016)
–
–
–
–
–
Enterococcus Paludibacter
Pseudomonas
Geobacter Bacteroides
–
–
–
Jia et al. (2013)
Rikame et al. (2012)
Goud et al. (2011)
Nistico et al. (2017)
Pseudomonas resinovorans
Follonier et al. (2014)
Molasses spent waste
Waste vegetable oil
Jack fruit peel derived pectin
Shrimp shell waste
Tomato peel
Mash from potato chips industry
Kitchen waste
Banana peel
Soy bean hulls
Alkali pretreated kitchen waste
residue
Waste bread pieces
Hazelnut shell
–
–
–
–
–
Thraustochytriidae sp. AS4-A1
Chryseobacterium Bacillus sp.
Aspergillus niger NCIM 616
Aspergillus niger NRRL3
Aspergillus niger NS-2
Khardenavis et al., 2009
Fernandes et al. (2017)
Govindaraj et al. (2017)
Gomez-Rios et al. (2017)
Grassino et al. (2016)
Quilodran et al. (2010)
Hasan et al. (2017)
Krishna et al. (2012)
Julia et al. (2016)
Bansal et al. (2012)
Aspergillus awamori
Bacillus subtilis
Citrus waste peel
Grape pomace
Blueberry agro-waste
Beverage waste
Cellulosic food waste
Olive mill waste
Onion juice waste
Shrimp waste
Tomato processing waste
Aspergillus niger
Aspergillus awamori
–
–
–
Oyster mushroom
Pleurotus sajor-caju
–
–
Waste cheese whey
Apple industry waste biomass
Apple pomace ultrafiltration sludge
Banana peel
–
Rhizopus oryzae
Aspergillus niger NRRL 567
Aspergillus niger
Fruit wastes
Citrus peel waste
Oil palm empty fruit bunch
Aspergillus niger DS1
Actinobacillus succinogenes
Actinobacillus succinogenes ATCC
55618
Actinobacillus succinogenes
–
Aspergillus awamori Aspergillus oryzae
Melikoglu et al. (2015)
Uzuner and Cekmecelioglu
(2015)
Ahmed et al. (2016)
Botella et al. (2007)
Luchese et al. (2017)
Haque et al. (2017)
Chen et al. (2017)
Ruiz-Rodriguez et al. (2010)
Pereira et al. (2017)
Prameela et al. (2017)
Poojary and Passamonti
(2015)
Pal and Nayak (2016)
Das et al. (2015)
Dhillon et al. (2011)
Karthikeyan and Sivakumar
(2010)
Kumar et al. (2003)
Patsalou et al. (2017)
Akthar and Idris (2017)
Food waste
Acidogenic food waste leachate
Canteen based composite waste
Post-harvest tomato plants and
urban food waste
Fruit pomace/waste frying oil
Fruit and vegetable waste
Food waste/waste activated sludge
Mixed restaurant food waste and
bakery waste
Waste Curcuma longa biomass
Kitchen refuse
Apple pomace
Sugarcane molasses
Lactobacillus coryneformis
Lactobacillus paracasei
Bacillus coagulans
Propionibacterium freudenreichii T82
Aspergillus niger ARNU-4
Dessie et al. (2018)
Zhang et al. (2017)
Pleissner et al. (2015)
Nguyen et al., 2013
Tashiro et al. (2013)
Piwowarek et al. (2016)
Sharma et al. (2008)
(continued on next page)
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Table 1 (continued)
Section
Number
Product
Source
Microorganism
Reference
3.15.
Pigments
–
Panesar et al., 2015
Pigments (Carotenoids)
Pigments (Carotenoids)
Pigments (Yellowish-orange )
Molasses/Corn steep liquor/bran/
whey
Waste cooking oil
Food waste
Pineapple waste
Nanou and Roukas (2016)
Cheng and Yang (2016)
Aruldass et al. (2016)
3.16.
3.17.
Pigments
Quercetin
Single cell protein
Grape waste
Onion skin waste
Mixed food waste
Blakeslea trispora
Rhodotorula mucilaginosa
Chryseobacterium artocarpi CECT
8497
Monascus purpureus
3.18.1.
3.18.2.
3.18.3.
3.19.
3.20.
Glucose
D- Tagatose
D- Mannose
Vermicompost
Vinegar
3.21.
Wax esters
Potato peel waste
Onion waste
Coffee waste residue
Kitchen waste
Pineapple waste
Olive oil press mill waste
Food industry waste
3.22.
Xanthan gum
Kitchen waste
Saccharomyces cerevisiae
Kluyveromyces marxianus
–
–
–
–
Acetobacter aceti
–
Cryptococcus curvatus
Rhodosporidum toruloides
Lipomyces starkeyi
Xanthomonas campestris LRELP-1
Silveira et al. (2008)
Choi et al. (2015)
Aggelopoulos et al. (2014)
Kumar et al. (2016)
Kim et al. (2017)
Nguyen et al., 2017
Adi and Noor (2009)
Roda et al. (2017)
Leonardis et al. (2018)
Papadaki et al. (2017)
Li et al. (2017)
processing plants. Utilisation of this waste for bioethanol production is
a promising approach. Ethanol production was evaluated using potato
peel and mash wastes using a co-culture of Aspergillus niger and Saccharomyces cerevisiae. Under optimised conditions potato peels and
mash wastes produced respectively 6.18% v/v and 9.3% v/v of bioethanol. The study showed that wastes generated from potato processing
plants as an attractive raw material for bioethanol production.
Simultaneous hydrolysis and fermentation of unprocessed food
waste into ethanol using thermophilic anaerobic bacteria was reported
by Dhiman et al., (2017). Conversion of Raw and Untreated Disposal
into Ethanol (CRUDE) was carried out. This is the first report where
ethanol is produced in single reactor using a thermophilic anaerobe.
This is a clean and green process eliminating hazardous chemicals as
well as harsh conditions making it a green process.
Production of ethanol from a mixture of waste paper and kitchen
waste was carried out by Nishimura et al., (2017). To develop a cost
effective ethanol production strategy from waste paper, addition of
food waste proved to be successful. Liquefaction of kitchen waste was
carried out followed by simultaneous saccharification and fermentation, which is essential for effective fermentation. Ethanol concentration of 46.6 g/L and 45.5 g/L was observed after 96 h of fermentation in
lab scale and pilot scale respectively. The kitchen waste acts as carbon
source, nutrient source as well as acidity regulator.
Olive fruits and by-products serve as a good source for antioxidants.
Production of antioxidant phenolic compounds from olive pomace has
many ecological and environmental benefits. Wang et al., (2017) developed an eco-friendly strategy like ultrasound assisted-enzymatic
hydrolysis of olive waste for the extraction of antioxidant phenolic
compounds. The optimised conditions of extraction are treatment time
for 40 min, temperature of 55 °C and pH of 5.75. The study revealed
that the phenolic extract can be used as a food additive enhancing
antioxidant properties in fatty food with better economic benefits than
synthetic additives.
3.3. Bioactives
Bioactives are compounds that show an effect on living organisms.
These compounds show potential health benefits functioning as antimicrobial, antidiabetic, antihypertensive, anticoagulant, anticancer or
hypo-cholesteraemic agents. Fish and shell fish processing wastes serve
as an efficient source of bioactives. Harnedy and FitzGerald (2012)
reported several bioactive peptides, proteins and amino acids from
marine processing waste and fish. The marine processing wastes contain significant amount of diverse proteins that can act as a source for
the production of diverse class of bioactives. Marine derived peptides
function as promising nutraceuticals. Utilisation of the waste streams
for the production makes it economically viable.
3.4.2. Biobutanol
Biobutanol serves as a fuel for internal combustion engine. It is nonpolar and studies revealed that it can work in gasoline compatible engines without any further modifications. Substrate cost is one of the
major factors limiting butanol production. Ujor et al., (2014) first reported the feasibility of butanol production using industrial starchy
food wastes. The study revealed that starchy food wastes serves as a
viable source for the production of butanol. Batch fermentation carried
out with Clostridium beijerinckii NCIMB 8052 using starch industry food
wastes like inedible dough, breading's and batter liquids as substrate
produced 14.4, 14.8 and 15.1 g/L of ABE (acetone-butanol-ethanol)
concentration. The results demonstrate the potential of starchy food
waste as an economically feasible substrate for butanol production.
Shao and Chen (2015) evaluated the potential of Amorphophallus
konjac waste as a feasible substrate for ABE fermentation by Clostridium
acetobutylicum ATCC 824. Utilisation of konjac waste enhances the
feasibility of waste treatment and reduces environmental pollution. The
strain utilises konjac waste as a feasible substrate for ABE fermentation.
The results indicate that ABE concentration was more for separate
3.4. Fuels
3.4.1. Bioethanol
Increase in fossil fuel consumption as well as depletion of fossil fuels
leads to energy crisis. This leads to search for alternative strategies of
energy. Use of agro-residues or food waste serves as an ideal source for
bioethanol production. Chintagunta et al. (2017) reported bioethanol
production from pineapple leaf waste. Pineapple leaves are left out in
the field after pineapple harvesting. The leaves contain 60–80% of
holocellulose making them as an ideal feedstock for bioethanol production. Bioethanol production was carried out by simultaneous saccharification and fermentation using cellulase cocktail and yeast. Under
optimised conditions 7.12% v/v of bioethanol was produced. Utilisation of pineapple leaf waste addresses the problems of fossil resources
depletion and environmental pollution.
Bioethanol production from potato waste was evaluated by
Chintagunta et al. (2016). Disposal of potato peeling waste is major
ecological and environmental concerns associated with potato
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R. Sindhu, et al.
volatile solids.
hydrolysis and fermented (SHF) samples than simultaneous saccharified
and fermented (SSF) samples. Under SHF 7.1 g/L of butanol was produced by Clostridium acetobutylicum ATCC 824.
3.4.5. Bioelectricity
Food waste is a highly valuable, biodegradable and nutritious organic source that is available in excess amount rendering it difficult to
manage. Hence, utilisation for other novel applications is a viable alternative way for value addition. Microbial fuel cells (MFC) are a promising efficient electrochemical technology to treat wastewater by
providing clean energy. Bioconversion of organic components present
in wastewater to electricity can be carried out by microorganisms. The
main advantages of MFC for wastewater treatment include safe, clean,
efficient as well as direct electricity production along with removal of
organic components present in the wastewater. MFC are composed of a
cathode and anode chamber separated by a proton exchange membrane. The organic components present in the wastewater are oxidised
by bacteria and produce protons and electrons. Protons transferred
through proton exchange membrane while the electrons are transferred
through external circuit.
Mediator-less MFC were evaluated for conversion of orange peel
biomass to bioelectricity by Miran et al., (2016). Under optimised
conditions 0.59 V was generated from orange peel waste. The maximum
power density and current density obtained were 358.8 mW/m2 and
847 mA/m2 respectively. Dominant microbial flora in the anode film
was Enterococcus, Paludibacter and Pseudomonas. Jia et al., (2013) reported bioelectricity generation from food waste using MFC. The study
revealed that organic loading rate of food waste has a significant effect
on power output of MFC. Microbial community analysis revealed that
exoelectrogenic Geobacter and fermentative Bacteroides are the dominant species that help in organic food waste conversion to bioelectricity. Rikame et al., (2012) generated electricity from acidogenic food
waste leachate using dual chamber mediator less microbial fuel cell. In
this study acidogenic fermentation and electrochemical performance
were evaluated. Under optimised conditions maximum power density
of 15.14 W/m3, open circuit voltage of 1.12 V and 90% of COD removal
were observed. The study revealed the possibilities of bioelectricity
production from food waste leachate. Canteen based composite waste is
a rich source of organic constituents. Goud et al., (2011) exploited
canteen based composite waste as a suitable substrate for the production of bioelectricity using MFC. Maximum power output (295 mV,
390 mA/m2) was observed with organic loading rates of 1.74 kg COD/
m3-day. Energy conversion efficiency was increased with intermittent
loading rate due to effective utilisation of substrate.
3.4.3. Biodiesel
Biodiesel is composed of mono-alkyl-esters of long chain fatty acids.
It has low volatility and high viscosity this may lead to gelling issues at
low temperatures, which in turn leads to clogging of pumps. Blending
can improve the fuel properties and common blend is B20. One of the
main limitations in biodiesel production is the high cost associated with
the production. This can be overcome by using non-edible oils as a
source for biodiesel production. Mixed non-edible oils, castor seed oil
(CSO) and waste fish oil (WFO) were evaluated for cost-effective biodiesel production by Fadhil et al., (2017). Different blends were tried
and highest production was observed with equivalent blend (50: 50%
WFO: CSO w/w). Under optimised conditions 95.2% w/w of biodiesel
was obtained. The fuel properties were also in the acceptable range.
Using mixed oil reduced the optimum temperature required for biodiesel production there by reducing the energy input, which in turn
reduces the overall process economics.
Rapid biodiesel synthesis from waste pepper seeds (WPS) without
lipid isolation step was developed by Lee et al., (2017). The study revealed that WPS contains 26.9 %w of lipid and 94.1 %w of the lipids
can be converted into biodiesel. The optimum transmethylation temperature was observed as 390 °C. The process was carried out in presence of silica and proved to be effective in biodiesel production from
waste pepper without lipid extraction.
Thushari and Babel (2018) reported utilisation of waste palm oil
and sulfonated carbon acid catalyst derived from coconut meal residue
for biodiesel production. Inexpensive catalyst was used for biodiesel
production. The highest biodiesel yield from waste palm oil residue is
92.7% in an open reflux system using the catalyst. Fuel properties also
were found to be compatible. Catalyst was found to be highly stable and
reusable for four cycles without losing its activity.
Novel efficient procedure for biodiesel synthesis from waste oils
with high acid value using 1-sulfobutyl- 3-methylimidazolium hydrosulphate ionic liquid as catalyst was developed by Hu et al. (2017).
Various process parameters affecting biodiesel production were optimised like molar ratio of methanol to waste oils, catalyst concentration,
reaction temperature and reaction time. Under optimised conditions
biodiesel yield was 94.9%. Catalyst retained 97% activity after 5 cycles.
The study proves an efficient and eco-friendly catalyst for the production of biodiesel from waste oils with high acid value.
3.5. Biomaterials
3.4.4. Biogas
Biogas is a renewable gas that is a mixture of methane, carbon dioxide, hydrogen sulphide, moisture and siloxanes. It is produced by the
anaerobic digestion of different wastes. Food waste is an important
issue and its anaerobic conversion to biogas is promising. Several research and developmental activities are going throughout the world to
address this issue. Deepanraj et al. (2017) observed that substrate
pretreatment have significant effects on biogas production from food
wastes. Different pretreatments like autoclave, microwave and ultrasonication of food waste were carried out and anaerobic digestion was
carried out with poultry manure. Maximum biogas production
(10.12%) and yield (9926 mL) was observed with ultrasonication pretreated samples. 41.96–46.52 g/L of volatile solids were also removed
during the process.
Wu et al., (2016) developed an improved biogas production from
food waste by co-digestion with de-oiled grease trap waste. The study
was carried out in different digesters like mesophilic digester (MD),
temperature-phased anaerobic digester (TPAD) and temperaturephased anaerobic digester with recycling (TPAD-R). Mono-digestion of
food waste as well as co-digestion with de-oiled grease trap waste was
carried out. The results indicate that co-digestion increased the biogas
yield by 19% in MD and TPAD-R with a biogas yield of 0.60 L/g of
3.5.1. Biopolymer
Nistico et al., (2017) reported manufacture of plastic films from
post-harvest tomato plants and urban food wastes. Composite films
were prepared by compounding poly (vinyl alcohol-co-ethylene) with
2–10% post-harvest tomato plant powder. The study revealed that postharvest tomato plant powder can be blended to make composite films in
a cost competitive way. Follonier et al., (2014) evaluated the potential
of fruit pomace and waste frying oil as a resources for the bio-production of medium chain length polyhydroxyalkanoates. One of the
main limiting factors for the production of biopolymer when compared
with petroleum based polymers is the high production cost and the
main part is contributed by the carbon source. Hence, utilisation of
cheap and waste by-product stream as a source of carbon like sugars
and fatty acids seems a promising strategy. In this study, sugars and
fatty acids derived from nine different fruit wastes were evaluated for
medium chain length polyhydroxyalkanoates (mcl-PHA) by Pseudomonas resinovorans. Highest sugars were observed with Solaris grapes
while apricot pomace contains the lowest level of inhibitors. Maximum
mcl-PHA production of 21.3 g/L was observed with Solaris grapes. This
study indicates a low cost strategy for the production of mcl-PHA by
Pseudomonas resinovorans.
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myocardial infarction and cancer. Quilodran et al., (2010) evaluated
the potential of residual mash from brewery by-product and liquid residues from potato chip processing factory as nutrient source for the
production of DHA by Thraustochytriidae sp. AS4-A1. The percentage of
DHA varies depending upon the composition of growth media. With
residual mash from brewery by-product the strain produced 576 mg/L
and supplementation of yeast extract, B-complex vitamins and monosodium glutamate significantly increased the productivity to 540 mg/L/
day. The DHA production was observed during the growth period. The
results indicate that brewery by-product serves as a cost-effective excellent nutrient source for the production of DHA by Thraustochytriidae
sp. AS4-A1.
Utilisation of molasses spent waste for the production of bioplastic,
polyhydroxybutyrate from activated sludge was reported by
Khardenavis et al., (2009). Molasses spent wash were processed to
obtain different ratios of carbon and nitrogen. The study revealed that
there was 52% removal of chemical oxidation demand with a polyhydroxybutyrate accumulation of 28%. The study revealed the benefits
of an un-utilizable and toxic molasses spent wash for the production of
a value added product polyhydroxybutyrate.
3.5.2. Bio-nanocomposite
Waste vegetable oils (WVO) serve as an alternative source for the
production of epoxy resin blends and composites. It is a potential low
cost material and does not compete with food crops. Fernandes et al.,
(2017) reported production of epoxy resin blends and composites from
waste vegetable oil. Purification of the WVO was carried out for the
removal of by-products produced during frying and epoxidised for the
formation of oxirane rings that are essential to obtain materials with
good mechanical properties. Then milled recycled carbon fibres were
added to the blends for further improvement of mechanical properties
and reinforcement. The effect of epoxidised vegetable oils was compared with pure oil. The results demonstrate compatibility in tensile
properties. This indicates the potential of valorisation of WVO as an
alternative source for triglycerides and opens a novel application.
Jack fruit peel derived pectin/apatite bio-nanocomposites for bone
healing applications was reported by Govindaraj et al., (2017). In this
study, pectin was isolated from jack fruit peel and was mixed with
apatite for the production of pectin/apatite bio-nanocomposite. Optimisation studies were carried out to get the bio-nanocomposite with
better properties. Fabricated bio-nanocomposite showed cyto-compatibility, anti-inflammatory as well as cell adhesion testing showed good
biocompatibility indicating its potential application as bone graft material. Physico-chemical and biological properties make them suitable
for orthodontic and orthopaedic tissue engineering.
3.8. Enzymes
3.8.1. Amylase
Amylases are enzymes which degrades starch to smaller carbohydrates units like glucose, maltose and maltotriose. It is one of the most
important industrial enzymes and finds applications in paper, textile,
food, detergent and for fuel ethanol production. Commercial carbon
and nitrogen source and commonly used for the production of amylases. Utilisation of agro-residues as well as food and kitchen waste
serves as an alternative source for cost-effective amylase production.
Hasan et al., (2017) observed amylase production by Chryseobacterium
and Bacillus species using kitchen waste. Various process parameters
affecting production were optimised and the study revealed that both
the strains could utilise starchy kitchen waste for amylase production.
Krishna et al., (2012) utilised banana peel for the production of
amylase by Aspergillus niger NCIM 616. The study revealed solid state
fermentation as a promising strategy when compared to submerged
fermentation. Supplementation of mineral salts to the medium improved amylase production by A. niger NCIM 616. Under optimised
conditions the strain produced 13,000 units/mg protein/g substrate of
amylase.
3.5.3. Chitosan
Chitosan is a polymer of N-acetylglucosamine units. Chemically it is
produced by the de-acetylation of chitin. Chitosan is nontoxic, biodegradable and biocompatible and finds applications in various industries
like food, agriculture and medicine. Chitin is found as a structural
compound in arthropods and fungi. Utilisation of shrimp shell waste for
the production of chitosan was reported by Gomez-Rios et al., 2017.
Techno-economic analysis was carried out using Aspen plus software
and it was found that the process is profitable as well as cost competitive. One of the major constrains in chitosan production is the material
cost and the quality of the final product. Utilisation of shrimp shell
waste serves as an economically viable alternative source for chitosan
production.
3.8.2. Cellulase
Cellulases are complex enzymes consisting of endocellulase, exocellulase and β-glucosidase. Complete hydrolysis of cellulose is brought
about by the sequential action of these enzymes. These enzymes play an
important role in biomass hydrolysis. Cellulase finds applications in
different industries like biofuel, paper and pulp, textile, detergent, food
and feed.
Julia et al., (2016) reported potential use of soy bean hulls and
waste paper as supports in solid state fermentation for cellulase production by Aspergillus niger NRRL3. The use of soybean hulls provided
high volumetric productivity at shorter times, this will have a positive
impact on overall process economics. Endoglucanase activity (5914.29
U/L) was found to be four times higher, the exoglucanase activities
(4551.19 U/L) were 9.5 times higher and β-glucosidase activities
(984.01 U/L) were 1.7 times higher than waste paper alone at the same
fermentation time. This process has economic benefits especially when
a cellulase complex is required.
Complete cellulase system by Aspergillus niger NS-2 in solid state
fermentation using agricultural and kitchen residues was reported by
Bansal et al., (2012). Alkali pretreated agricultural and kitchen waste
residues like corn cobs, carrot peelings, composites, wheat bran, wheat
straw, orange peelings, potato peelings, pineapple peelings saw dust,
rice husk moistened with water were found to be suitable for the production of cellulases without any additional nutritional sources. Maximum production was observed after 96 h of incubation. Wheat bran
showed highest production CMCase, FPase and β-glucosidase activities
of 310, 17 and 33 U/gds respectively.
3.6. Corrosion inhibitors
Grassino et al., (2016) evaluated the potential utilisation of tomato
peel from canning factory as a source of pectin production and its application as a tin corrosion inhibitor. This helps in the waste disposal
problem of canning factory waste to a value added product-waste to
wealth strategy. Only few reports were available on the application of
pectin extracted from fruit industrial waste as a corrosion inhibitor. The
study revealed that the pectin extracted from tomato peel serves as an
efficient corrosion inhibitor for tin, even at very low concentrations.
Maximum inhibition efficiency was reported as 71%.
3.7. Docosahexaenoic acid (DHA)
Docosahexaenoic acid (DHA) is a long chain omega-3-fatty acids
and is an essential polyunsaturated fatty acid. Deficiencies of DHA are
associated with several diseases. Currently the main source of DHA is
fish oil. Dietary DHA has positive impacts on hypertension, diabetics,
3.8.3. Protease
Protease are enzymes which catalyses the hydrolysis of proteins. It
finds applications in medicine, food and detergent industries. Waste
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indicator films. Blueberry powder which is a by-product of fruit processing industry rich in anthocyanins was added with films to evaluate
its role as an indicator because of the ability of anthocyanin to change
its colour in acidic or basic environment. The pH indicator films were
evaluated with buffers having different pH. The results indicate that
blueberry powder acts as a potential pH indicator for intelligent food
packing as well as for sensible food deterioration.
bread pieces as a source for protease production by Aspergillus awamori
in a packed –bed reactor were evaluated by Melikoglu et al., (2015).
Highest protease activity was 80.3 U/g bread when the air flow was
kept at 1.50 vvm. The study indicates the potential of waste bread as a
feasible raw material for protease production.
Bread serves as an ideal substrate for solid state fermentation. It
serves as a major food waste in many countries. Currently most of the
bread wastes are used for land filling and it leads to methane production by anaerobic digestion. Methane shows 21 times more global
warming potential when compared to carbon dioxide. Hence, utilisation of this waste for value addition seems promising in terms of economical as well as ecological benefits. Melikoglu et al., (2013) optimised various process parameters affecting protease production from
Aspergillus awamori by adopting a stepwise strategy. Protease activities
of 83.2 U/g of bread were recorded with particle size of 20 mm and
incubation time of 144 h.
3.10. High fructose syrup
High fructose syrup (HFS) is commonly produced by enzymatic
saccharification of starch to glucose followed by enzymatic isomerisation to fructose. Haque et al., (2017) made an effort to produce high
fructose syrup from beverage waste. This is the first report on the
conversion of beverage waste to HFS. The steps involved in the conversion of beverage waste to HFS include enzymatic hydrolysis, activated carbon treatment, ion exchange chromatography and ligand exchange chromatography. In this study, 47.5% of sugars were recovered
as HFS. This proves a green process for nutrient recovery in beverage
waste valorisation.
3.8.4. Pectinase
Pectinases are enzymes that hydrolyse pectins and find wide applications in food industries for clarification of fruit juice as well as tea
and coffee fermentation. Other applications include production of
pectic oligosaccharides, DNA extraction from plants and degumming of
fibres. To meet the increasing demands, it is essential to develop strategies for cost-effective production. Several agro-industrial residues as
well as fruits and vegetable wastes serve as an ideal substrate for pectinase production. Ahmed et al., (2016) evaluated the potential of citrus
waste peel as a source for pectinase production by Aspergillus niger.
Citrus waste contains high amount of soluble carbohydrates. Submerged fermentation was carried out in Czapecks - Dox medium supplemented with citrus peel waste that serves as sole carbon source.
Maximum enzyme yield (117.1 μm/mL/min) was observed on the fifth
day of fermentation.
Uzuner and Cekmecelioglu (2015) demonstrated the potential of
hazelnut shell hydrolysate as a suitable low cost medium for the production of pectinase by Bacillus subtilis. Various process parameters
affecting submerged fermentation was optimised by adopting statistical
design experiments. Maximum polygalacturonase activity (5.6 U/mL)
was observed with an incubation time of 72 h, pH of 7.0, incubation
temperature of 30 °C, yeast extract concentration of 0.5% w/v and
0.02% w/v of KH2PO4.
3.11. Levulinic acid
Levulinic acid is an important platform chemical and is a keto acid.
It is produced by degradation of cellulose. Chen et al., (2017) developed
a strategy for the production of levulinic acid from cellulosic food waste
by catalyzation with Bronsted acids. Amberlyst 36 produced levulinic
acid efficiently from vegetable waste. The yield was same with DMSOwater.
3.12. Fungal cultivation
Olive mill waste was exploited for cultivation of oyster mushrooms
by Ruiz-Rodriguez et al., (2010). Different strains of oyster mushrooms
were cultivated in wheat straw supplemented with different concentrations of olive mill waste (0–90%). The studies showed that except
for colour of fruiting bodies there is no significant difference when
compared to control grown on wheat straw. Total phenolic content,
antioxidant activities were similar to that of control and no phenolic
compounds were detected on oyster mushrooms grown on olive mill
waste.
Pereira et al., (2017) utilised onion juice waste for the production of
Pleurotus sajor-caju. Solid state fermentation was carried out using
onion waste for the production of fruiting bodies of Pleurotus sajor-caju.
The yield was 45.73%. The study proved the feasibility of onion waste
as a substrate for the cultivation of Pleurotus sajor-caju.
In a recent study, Nair et al., 2017 has demonstrated the use of
waste bread for the cultivation of food-grade edible strains of filamentous fungi, such as Neurospora intermedia, Aspergillus oryzae, belonging to ascomycetes and Mucor indicus, Rhizopus oryzae, belonging to
zygomycetes group. The fungal biomasses that are high in protein are
further used as animal or fish feed component. The study also demonstrated the use of waste bread as ethanol substrates using the filamentous fungi.
3.8.5. Xylanase
Xylanases are enzymes which catalyse the hydrolysis of plant
polysaccharide xylan. It finds applications in food, feed, paper and pulp
industries. Grape pomace is the residue that is left out after juice extraction from grapes. It is not suitable as an animal food due to its low
nutritive value as well as due to the presence of high level of phenolic
compounds. The disposal of grape pomace leads to serious environmental hazards. Hence, utilisation of this for value addition seems
promising. Grape pomace is unsuitable for fertilizer applications since
the high phenol content may inhibit seed germination. Feasibility of
grape pomace for the production of xylanases by Aspergillus awamori
was evaluated by Botella et al., (2007). The study revealed that supplementation of additional carbon source as well as initial moisture
content of grape pomace plays a significant role in enzyme production.
3.13. Nutraceuticals
3.9. pH indicator films
Nutraceuticals are nutritive pharmaceuticals that provide health
benefits. Shrimp processing industries generate tonnes of shrimp wastes
annually. They serve as a cheap source for the production of nutraceutical astaxanthin. It is the main xanthophyll carotenoid in crustacean waste. Quality of the nutraceutical depends on the strategies
adopted for extraction, nutrient content as well as its efficacy as a
dietary supplement. Astaxanthin finds wide applications as antioxidant,
cardio-protective, anti-hypersensitive, anti-tumorigenic. It can be extracted by several chemical strategies as well as green techniques like
Intelligent packing is an emerging area of food technology for better
preservation. It involves some sensors that provide visual information
to the customers like appearance or disappearance of a colour. Several
research and development activities are going on in this direction and
one such material is pH indicator film that is non-toxic and produces
response to pH change. Luchese et al., (2017) developed a pH indicator
film by blueberry agro-waste addition to starch based films. Corn
starch, glycerol and blueberry powder were used to produce pH
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Utilisation of fruit processing wastes has dual benefit converting waste
to a value added product.
microbial fermentation or enzymatic extraction. Utilisation of shrimp
waste for astaxanthin production helps in better waste management
(Prameela et al., 2017).
Lycopene, a red pigment, is a potent antioxidant. Poojary and
Passamonti (2015) extracted lycopene from tomato processing waste
that is an abundantly available industry by-product. It was extracted
using acetone-hexane mixture. Lycopene yield of 3.47–4.03 mg/100 g
of processing waste was obtained with a recovery of 65.22–75.75%.
3.14.4. Succinic acid
Succinic acid is a dicarboxylic acid that finds applications as food
additives, dietary supplement as well as a precursor for polymers and
solvents. Food waste from commercial and industrial sectors increased
in the last few decades. Though several research and developmental
activities are going on for the disposal as well as decomposition of food
waste, it may not be a proper solution. Hence, conversion of these
wastes to value added product will lead to an environmental sustainable process. Patsalou et al., (2017) demonstrated the potential of valorisation of citrus peel waste to succinic acid. In this study, citrus peel
wastes were pretreated with dilute acid and enzymatically saccharified
for the production of sugars that were then fermented by Actinobacillus
succinogenes for the production of succinic acid. Under optimised conditions, 0.7 g/g of succinic acid was produced. This strategy is a viable
alternative to energy intensive chemical strategies of succinic acid
production.
Oil palm empty fruit bunch (EFB) is an abundant agricultural residue available in Malaysia. Utilisation of this waste to value added
chemicals is a promising strategy. Akthar and Idris (2017) developed a
simultaneous saccharification and fermentation strategy for the production of succinic acid from EFB using Actinobacillus succinogenes
ATCC 55618. Pretreated samples were enzymatically saccharified.
Under optimised conditions 33.4 g/L of succinic acid was produced.
EFB serves as an alternative, easily available and economically viable
substrate for succinic acid production.
A novel biorefinery concept of succinic acid production from fruit
and vegetable wastes (FVW) hydrolysis by crude enzyme preparations
from Aspergillus niger and Rhizopus oryzae was developed by Dessie et al.
(2018). The hydrolysate was then fermented by Actinobacillus succinogenes for the production of succinic acid. Under optimised conditions
27.03 g/L of succinic acid was produced. Lam et al., (2014) studied the
economic viability of succinic acid production from bakery waste. The
study revealed that fermentative succinic acid production from bakery
waste is economically viable.
3.14. Organic acids
3.14.1. Acetic acid
Acetic acid is a carboxylic acid widely produced by anaerobic fermentation of substrates by anaerobic bacteria. Development of an
economically - viable strategy for the production of acetic acid and
whey protein from waste cheese whey was reported by Pal and Nayak
(2016). They have developed a multistage membrane integrated hybrid
reactor system for the production of high purity acetic acid and whey
protein from waste cheese whey. The study revealed an eco-friendly
and cost effective process for the continuous production of 98% pure
acetic acid.
3.14.2. Fumaric acid
Fumaric acid finds applications in food, medicine as well as in the
preparation of resins and mordants. The demand is increasing each
year. Mostly the fumaric acid is produced by petro-chemical route.
Biological route of fumaric acid production will be economically viable
and eco-friendly. Different waste biomass can be used as a source for
fumaric acid production. Fumaric acid production using apple industry
waste biomass by Rhizopus oryzae 1526 was evaluated by Das et al.,
(2015). The study revealed that solid state fermentation yields (52 g/kg
wt. of substrate) more fumaric acid when compared to submerged
fermentation (25.2 g/L). Small size fungal pellets favoured more fumaric acid production than large sized fungal pellets.
3.14.3. Citric acid
Citric acid is widely used in food, beverages as well as pharmaceutical industries. It is widely used as an acidifying as well as a flavour
enhancing agent. Increase in demand of citric acid leads to search for
alternative novel as well as economically viable substrates for the
production. Fruit wastes are normally used as animal feed or disposed
to soil. Since these wastes are rich in carbohydrates as well as other
nutrients, it can be used as a cost-effective substrate for citric acid
production. Utilisation of inexpensive substrates is essential for the
reduction of production cost of citric acid. Several research and developmental activities are going on in this direction.
Apple pomace ultrafiltration sludge was used as a novel substrate
for citric acid production by Aspergillus niger NRRL 567 (Dhillon et al.,
2011). Various process parameters affecting citric acid production was
optimised by response surface methodology. Maximum citric acid
production (44.9 g/100 g dry substrate) was observed with initial solid
contents of 25 g/L, methanol concentration of 3% (v/v), total solids –
25 g/L and ethanol concentration of 3% (v/v). Utilisation of apple pomace ultrafiltration sludge helped in sequestration of carbon which is
an important element of greenhouse gas emissions.
Karthikeyan and Sivakumar 2010 reported citric acid production by
Aspergillus niger using banana peel as a substrate. Different process
parameters affecting fermentation were optimised by adopting a one
parameter at a time approach. This is the first report on utilising banana
peel as a substrate for citric acid production. The study revealed the
potential of banana peel as a suitable substrate for citric acid production.
Utilisation of fruits wastes for the production of citric acid by solid
state fermentation using Aspergillus niger DS1 was evaluated by Kumar
et al., (2003). Maximum citric acid was produced when the moisture
content was maintained at 70% level in presence of 4% methanol.
3.14.5. Lactic acid
Lactic acid is an important organic acid that finds wide applications
in food, pharmaceutical and cosmetic industries. It is also used for the
production of biopolymer-polylactate (PLA). Decrease in petroleum
reserve as well as environmental concerns lead to its production by ecofriendly fermentative strategy. It is one of the most important building
blocks derived from sugars. Zhang et al., (2017) carried out high rate
lactic acid production from food waste and waste activated sludge by
interactive control of pH and incubation temperature. Optimisation was
carried out by statistical design experiments and found that interaction
effect of alkaline addition and temperature contributes significantly to
L-lactic acid production. Optimum pH for lactic acid production decreased with increase of temperature.
Pleissner et al., (2015) reported lactic acid production using mixed
restaurant food waste and bakery waste. Enzymatic hydrolysis of the
food and bakery wastes were carried out by Aspergillus awamori and
Aspergillus oryzae and the defatted solids were used for the production
of lactic acid by Bacillus coagulans. The result indicates a green process
for lactic acid production.
Nguyen et al., (2013) developed a fermentative strategy for the
production of D- and L-lactic acid from waste Curcuma longa biomass
using Lactobacillus coryneformis and Lactobacillus paracasei by simultaneous saccharification and co-fermentation. Under optimised conditions 97.13 g/L and 91.61 g/L of D- and L-lactic acid were produced.
Results indicate economic lactic acid production using renewable biomass. Kitchen refuse as an effective biomass for lactic acid production
was reported by Tashiro et al., (2013). During the process of marine
animal resource composting, the dominant bacteria present in it
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Rhodotorula mucilaginosa. Maximum carotenoid production of 2611 μg/
L was observed using molasses as the substrate.
Utilisation of agro-industrial waste for the production of yellowish –
orange pigment from Chryseobacterium artocarpi CECT 8497 was reported by Aruldass et al., (2016). Pineapple waste medium was used for
pigment production. Optimisation was carried out by adopting statistical design experiments. Maximum pigment production (152 mg/L)
was observed with liquid pineapple waste concentration of 20% v/v,
12.5 g/L of K2HPO4 and 125 g/L of l-tryptophan. The production was
three fold higher when compared to nutrient broth. This pigment finds
application as a colouring agent in soap manufacture.
Monascus purpureus are known to produce pigments that are a group
of fungal metabolites known as azaphilones. These compounds find
wide applications in food industry. Red pigment from Monascus species
are widely used as a food colorant. Several factors affect pigment production like carbon and nitrogen source, agitation, aeration etc. Silveira
et al., (2008) reported grape waste as a substrate for cost – effective
production of pigment by Monascus purpureus. Statistical design experiments were carried out for improved production. Maximum pigment production was reported with 20–22.5 g/L of peptone at any
concentration of grape waste. Utilisation of agro-residues serves as an
eco-friendly strategy of waste management.
diminishes rapidly and Bacillus coagulans become the main microbial
source for L-lactic acid production. The study revealed that bacterial
consortium from marine animal resource composts produced 34.5 g/L
of lactic acid from kitchen refuse with 100% optical purity. This is the
first report on achievement of 100% purity of L-lactic acid using microbial consortium.
3.14.6. Propionic acid
Propionic acid is widely used as a preservative and food additive.
Currently, most of the propionic acid production takes place through
expensive petro-chemical route. Hence, there is a need to develop costeffective strategies for the production of propionic acid. Several research and developmental activities are going on in this direction.
Production of this metabolite by microbial source using cheap as well as
easily available waste biomass will be a promising alternative.
Piwowarek et al., (2016) developed a strategy for the production of
propionic acid using apple pomace. Wild strain of Propionibacterium
freudenreichii T82 was able to utilise apple pomace as sole carbon source
and produced 1.711 g/L of propionic acid after 120 h of incubation.
Industrial by-products is a major challenge for manufacturing sites as
well as environment. Hence, utilisation of these by-products will be a
promising approach to solve these issues.
3.14.7. Gluconic acid
Gluconic acid finds application in different fields like food, pharmaceutical, textile and leather industries. It is an oxidative product of
glucose. One of the main limitations of gluconic acid is the production
cost. Sharma et al., (2008) developed a solid state fermentation strategy
for the production of gluconic acid from sugarcane molasses using Aspergillus niger ARNU-4 incorporating tea waste as a novel support.
Various process parameters affecting fermentation were optimised.
Maximum gluconic acid (76.3 g/L) was observed with 70% moisture
level, incubation temperature of 30 °C, inoculum size of 3% and aeration volume of 2.5 L/min. The effect of different inducers on gluconic
acid production revealed that addition of 0.5% of yeast extract increased production to 82.2 g/L. This is the first report on utilisation of
tea waste as a solid support for the production of gluconic acid utilising
waste sugarcane molasses as sole carbon source.
3.16. Quercetin
Quercetin is a flavonoid widely distributed in fruits and vegetables.
It is widely used as a supplement in foods and beverages. These compounds are widely used for the treatment of diseases like cancers affecting kidney, colon, breast etc. Onion processing waste is a major
waste produced from processed onions. Choi et al., (2015) developed a
strategy for the valorisation of onion skin waste to quercetin. The onion
skin waste was enzymatically saccharified with a cocktail of cellulase,
pectinase and xylanase. Enzymatic saccharification could increase
quercetin extraction 1.61 fold. A novel magnetic matrix was used for
the easy separation and purification of quercetin.
3.17. Single cell protein
Food waste mixtures serve as an efficient source for the production
of value added product-single cell protein (SCP). Aggelopoulos et al.,
(2014) carried out solid state fermentation of mixed food waste for the
production of SCP. Saccharomyces cerevisiae and Kluyveromyces marxianus were grown on food industry waste. Highest protein and fat were
observed with substrate fermented by Kluyveromyces marxianus and can
be used for livestock feed enrichment.
3.15. Pigments
Current increase in interest of using colouring agents leads to increase in cancer rate. Here comes the importance of safe and natural
colouring agents and their demand increased during the last decades.
Hence, pigment production using microorganisms is a safe strategy but
most of the strategies currently available are not economically viable
due to high cost of substrates used for fermentation. Agro-industrial
residues serve as a low cost substrate for the production of pigments.
Panesar et al., (2015) reviewed a variety of agro-industrial residues like
molasses, corn steep liquor, bran, whey etc. as a potential carbon, nitrogen and mineral source for the production of pigments. Production
of pigments from agro-industrial residues serves as a sustainable and
cost effective strategy for pigment production.
Carotenes are unsaturated isoprene derivatives. They find wide
applications in feed, pharmaceutical and food industries. They play an
important role as cardio-protectant as well as cancer prevention.
Several reports are available for the production of carotenoids from
Blakeslea trispora using synthetic medium and all these strategies are
economically non-viable. Nanou and Roukas (2016) developed a submerged fermentation strategy for the production of carotenoids from
Blakeslea trispora using waste cooking oil. The highest concentration of
carotenoids (2021 mg/L) was observed when waste cooking oil was
supplemented with 80 g/L of corn steep liquor and 4.0 g/L of butylated
hydroxytoluene. Oxidative stress induced by hydroperoxides of waste
cooking oil increased the carotenoid production. Cheng and Yang
(2016) evaluated carotenoid production using food waste by
3.18. Sugars
3.18.1. Glucose
Glucose finds applications to several fine chemicals and fuels. It can
be used for the production of fuel in fuel cells, ethanol, levulinic acid as
well as hydroxymethyl furfural. Kumar et al., (2016) demonstrated the
potential application of a low value potato peel waste under microwave
irradiation for the production of glucose. Chemical hydrolysis of potato
peel starch was carried out using silicotungstic acid as catalyst under
short microwave irradiation. Adopting this strategy 59% of glucose
yield was obtained after short microwave irradiation for 15 min. The
use of microwave and solid acid catalyst make it a green process for
glucose production from potato peel waste.
3.18.2. D-tagatose
Tagatose is a naturally occurring monosaccharide. It is widely used
a sweetener. It is sweeter like sucrose but with 38% less calories. Low
quantities of tagatose are found in fruits and dairy products. Utilisation
of agro-residues for high value products is a promising strategy. Kim
et al., (2017) developed a strategy for D-tagatose production from
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onion waste. Onion juice residue (OJR) was used as source for the
production of D-tagatose. Purified L-arabinose isomerase from Paenibacillus polymyxa was used for the conversion of OJR to D-tagatose.
0.99 g of D-tagatose was produced from 10 g of OJR. The study revealed
the potential of a low value agro-residue, OJR to a high value rare sugar
D-tagatose.
like esters derived from palm oil and comparable to natural waxes. The
oils were produced by cultivating oleaginous yeast strains in fermentation media derived from confectionary waste streams, cheese whey
and wine lees.
3.18.3. D-mannose
D-mannose is a sugar monomer that is widely used as nutrient
supplement. Coffee is one of the most consumed beverages. Coffee
processing generates a large amount of coffee residue waste (CRW).
Disposal of CRW to the environment leads to several environmental
issues. CRW contains caffeine, polyphenols, tannins and organic material. Nguyen et al., (2017) developed an integrated process for the
production of D-mannose and bioethanol from CRW. The process involves five unit operations like pretreatment, enzymatic hydrolysis,
fermentation, decolourization and pervaporation. The CRW was pretreated with ethanol and enzymatically hydrolysed to produce sugars
that were then fermented by yeast. Manipulations of fermentation
conditions were done in such a way that the yeast would ferment all the
glucose and galactose to ethanol, retaining D-mannose in the fermented
broth. Under optimised conditions 15.7 g dry weight of D-mannose was
produced.
Xanthan gum is an important microbial exopolysaccharide that is
produced by several microorganisms using glucose or sucrose as sole
carbon source. It is first microbial biopolymer produced at an industrial
scale. It finds application in many industries including pharmaceutical,
food as well as oil industries. In food industries it is widely used as
thickener, stabiliser and thickening agent. The use of pure glucose or
sucrose as carbon source for the production of xanthan gum makes the
process economically non-viable contributing to high cost of xanthan
gum. Hence, utilisation of low cost substrate for the production seems
to reduce the cost for fermentation.
Li et al., (2016) used kitchen waste as a sole substrate using Xanthomonas campestris LRELP-1. The maximal production of xanthan gum
of 11.3 g/L was observed using kitchen waste hydrolysate. The study
revealed a low cost strategy for the production of xanthan gum as well
as an effective strategy of kitchen waste management. Li et al., (2017)
reported production of xanthan gum using kitchen waste. In this study
the kitchen waste was pretreated with different chemicals and enzymatically hydrolysed and the hydrolysate was used for the production of xanthan gum. A concentration of 4.09–6.46 g/L was observed
with kitchen waste hydrolysate.
3.22. Xanthan gum
3.19. Vermicompost
Vermicomposting is one of the efficient strategies for management
of kitchen waste. Earthworms will convert kitchen waste to high quality
compost. Adi and Noor (2009) reported production of vermicompost
from coffee grounds and kitchen waste using Lumbricus rubellus. Composting was carried out for 49 days after precomposting for three
weeks. Different combinational treatments were carried out and the
study revealed that treatment with coffee grounds showed higher percentage of nutrient elements. Coffee grounds stabilise kitchen waste
and produce high quality vermicompost.
4. Conclusion and future perspectives
The kitchen and food waste constitute a valuable source of organic
carbon which can be utilised for the production of several chemicals
and high value compounds. Though several advantages and limitations
are there for the conversion of food waste to value added products, still
there is a lack of proper technology for efficient conversion. This
technological hindrance is mainly due to the heterogeneous nature of
the waste. But there exist a huge opportunity for an eco-friendly green
process for the production of value-added products from food waste.
Fine-tuning of the available technologies and strategies must be done
for the proper management of food and kitchen waste. Hence, intense
research is to be carried out in this direction to make it economically
viable.
3.20. Vinegar
Vinegar is a mixture of acetic acid and water and is produced by
microbial fermentation. Though vinegar has different applications, it is
commonly used for food preservation. Roda et al., (2017) reported vinegar production from pineapple waste. Pineapple peels were treated
and enzymatically saccharified and fermented with Saccharomyces cerevisiae for 7–10 days under aerobic conditions at an incubation temperature of 25 °C. This alcohol medium was used as seed medium for
acetic acid fermentation by Acetobacter aceti for a period of 30 days at
32 °C to get a concentration of 5% acetic acid. This vinegar is clear and
without any post-filtration deposits. The results indicate the potential of
pineapple peels as an alternative sustainable feedstock for the production of vinegar.
Effective, eco-friendly and simple strategy for the production of
vinegar from olive oil press-mill wastewaters was demonstrated by
Leonardis et al., (2018). The study revealed that sugar addition as well
as inoculum of selected yeast strains is the crucial factors affecting required acidification. This vinegar shows high content of ash and total
phenols when compared to apple or wine vinegars. Olive vinegar shows
high percentage of antioxidants indicating its nutraceutical potential.
Acknowledgement
Raveendran Sindhu acknowledges DST for sanctioning a project
under DST-WOS-B scheme. Raveendran Sindhu, Parameswaran Binod,
Sunita Varjani and Indu Shekhar Thakur acknowledge EPFL, Lausanne
for visiting fellowship.
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