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ISSN : 2248-9622, Vol. 5, Issue 1( Part 2), January 2015, pp.11-19
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Treatment of Sugarcane Industry Effluents: Science &
Technology issues
M. Rais1*
, A. Sheoran2
1
CSIR-National Institute of Science, Technology & Development Studies, Pusa Gate, K.S. Krishnan Marg, New
Delhi 110 012, India
2
Department of Civil Engineering Birla Institute of Technology & Science, Pilani Pilani 333031 (Rajasthan)
India
Abstract
The consumption of large volumes of water and the generation of organic compounds as liquid effluents are
major environmental problems in sugarcane processing industry. The inadequate and indiscriminate disposal of
this effluent in soils and water bodies has received much attention since decades ago, due to environmental
problems associated to this practice. Because of the large quantities of effluent produced, alternative treatments
have been developed. The low pH, electric conductivity, and chemical elements present in sugarcane effluent
may cause changes in the chemical and physical–chemical properties of soils, rivers, and lakes with frequent
discharges over a long period of time, and also have adverse effects on agricultural soils and biota in general.
The sugar cane industry is among those industries with the largest water demands and, in addition, is an
important source of non-toxic organic pollution combined with the fact that India it is second largest producer
and largest consumer makes it all the more important. This paper examines the present status of sugarcane
effluent, its characteristics and chemical composition. Keeping in view the relevant policy scenario in India,
various available treatment technologies are discussed.
Key words- Sugarcane industry, effluent management, treatment
I. Introduction
Increased demand for food and the need to
sustain the ever increasing world population have led
to massive increase in both agricultural and industrial
activities. Agriculture is one of the most significant
sectors of the Indian Economy. Agriculture is the
only means of living for almost two thirds of the
workers in India. The agriculture sector of India has
occupied 43% of India’s geographical area, and is
contributing 16.1% of India’s GDP. Agriculture still
contributes significantly to India’s GDP despite
decline of its share in India’s GDP. There are number
of crops grown by farmers. These include different
food crops, commercial crops, oil seeds etc.,
sugarcane is one of the important commercial crops
grown in India. There are around 45 millions of sugar
cane growers in India and a larger portion of rural
laborers in the country largely rely upon this industry.
Sugar Industry is one of the agricultural based
industries. Today, India is one of the first ten
industrialized countries of the world. India, like any
other developing countries, is faced with problems
arising from the negative impact of economic
development due to water or industrial pollution.
Rapid progress made in industrialization without
adequate environmental safety measures lead to
pollution of water, which in turn, results in lack of
good quality water both for irrigation and drinking
purposes. Every human society, whether urban,
industrial and most technologically advanced,
disposes of certain kinds of by-products and waste
products into the biosphere in large quantities,
ultimately affecting the normal functioning of the
ecosystem and have adverse effect on plants, animals
and human. Awareness of environmental problems
and the potential hazards caused by industrial
wastewater has promoted many countries to limit the
discharge of polluting effluents1
.
In many developing countries, especially in Asia
and South America, sugar cane industry is one of the
most important agricultural industries. As a
consequence, sugar cane industry has significant
wastewater production. Unfortunately, due to the lack
of know-how and financial support, most of sugar
cane industries in developing countries discharge
their wastewater without adequate treatment. Similar
with other wastewater generated by food processing
plants, wastewater from sugar cane industry generally
contains organic materials such as carbohydrates and
proteins2
. Generally effluent generated from
sugarcane industry is disposed off on land. While
moving on land, part of pollutants in the effluent may
be migrated and deposited between the gaps of soil
stratum and adsorbed on the soil particles surface,
resulting in pollution of soil. Furthermore, the
migrated effluent flows through the gaps in the soil
RESEARCH ARTICLE OPEN ACCESS
M. Rais Int. Journal of Engineering Research and Applications www.ijera.com
ISSN : 2248-9622, Vol. 5, Issue 1( Part 2), January 2015, pp.11-19
www.ijera.com 12 | P a g e
stratum and reaches the groundwater table, which
may cause impact to the aquifer and thereby pose a
potential risk to human health as well as the
surrounding environment3
.
36%
24%
11% 11%
5% 4% 3% 2% 2% 2%
0%
5%
10%
15%
20%
25%
30%
35%
40%
Major Producing States in India
Figure 1: Total % share of the sugarcane production by major sugarcane producing states in India in 2012-
201323
Figure 2: Production of sugarcane in India in last 10 years23
II. Sugar cane industry
In many developing countries, especially in Asia
and South America, sugar cane industry is one of the
most important agricultural industries. Sugar cane
mill industry is one of the oldest industries in India,
as in other parts of the world. In India, sugarcane
industry is highly responsible for creating significant
impact on rural economy after textiles3
. India is
the world’s second largest sugarcane producer, with
nearly 5 million hectares of cultivated area and
provides direct employment to more than 3.6 lakes
person Table 1.
The main final products of sugar cane industry
are crystalline sugar and bio-ethanol. The latter is
obtained from the fermentation and distillation of
sugar cane juice and molasses. Quantitatively, the
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ISSN : 2248-9622, Vol. 5, Issue 1( Part 2), January 2015, pp.11-19
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most significant by-product is bagasse, the solid
residue from sugar cane after juice extraction and
stillage (also called vinnasse or dunder), the liquid
waste effluent after the distillation process of sugar
cane juice. Sugar mill with annexed alcohol
distilleries generally release an average of 155 L of
stillage and 250 Kg bagasse per 1,000 Kg of sugar
cane to obtain 12 L of alcohol and 95 Kg of sugar 5
.
Alcohol distilleries are a major agro-based industry in
India with around 300 units located mainly in rural,
sugarcane growing regions. The total installed
capacity is 3250 million L alcohol per annum with an
estimated production of 2300.4 million L in 2006–
2007. Most of the distilleries co-exist with sugar
mills and utilize the molasses from cane sugar
manufacture as the starting material for alcohol
production. As per the Ministry of Environment &
Forests (MoEF), Government of India, alcohol
distilleries are listed at the top of ―Red Category‖
industries having a high polluting potential. The
industry generates large volumes (8–15 kL/kL
alcohol) of dark brown colored wastewater
(―spentwash‖) with high biochemical oxygen demand
(BOD) and Chemical oxygen demand (COD).This
poses a serious pollution threat; thus it is mandatory
for distilleries to take appropriate measures to comply
with the discharge standards set by the Central
Pollution Control Board (CPCB), which is the
national agency responsible for environmental
compliance6,7
.
Table 1- Sugarcane production in major countries4
Harvest area
(million ha)
Annual production
(million t)
Average income
(t/ha)
Brazil 8.14 648 79.7
India 5.06 348 68.9
China 1.71 124 73.1
Pakistan 1.24 64 51.5
Thailand 1.05 73 69.7
Mexico 0.67 51 76.4
Colombia 0.38 39 100.4
Australia 0.39 34 87.1
South Africa 0.43 21 48.2
Cuba 0.38 16 41.3
M. Rais Int. Journal of Engineering Research and Applications www.ijera.com
ISSN : 2248-9622, Vol. 5, Issue 1( Part 2), January 2015, pp.11-19
www.ijera.com 14 | P a g e
Brazil
30%
India
21%Thailand
8%
Pakistan
4%
United States
6%
Mexico
4%
China
9%
Europian Union
13%
Columbia
2%
Australia
3%
Fig. 3- Sugarcane worldwide distribution24
III. Sugarcane Processing
The main final products of sugar cane industry
are crystalline sugar and bio-ethanol. The latter is
obtained from the fermentation and distillation of
sugar cane juice and molasses. Quantitatively, the
most significant by-product is bagasse, the solid
residue from sugar cane after juice extraction and
stillage (also called vinnasse or dunder), the liquid
waste effluent after the distillation process of sugar
cane juice. Bagasse can be used in boilers during
combustion, while stillage is mainly disposed to field
crops, incorporating a risk for aquatic pollution.
Surface water pollution potential is mainly due to the
high contents of organic matters in stillage. Organic
matters cause oxygen depletion by heterotrophic bio-
degradation when enter in surface water. Stillage also
contains high concentration of potassium which can
accumulate at toxic levels in the soil5
.
M. Rais Int. Journal of Engineering Research and Applications www.ijera.com
ISSN : 2248-9622, Vol. 5, Issue 1( Part 2), January 2015, pp.11-19
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Fig. 4- Flowchart of ethanol production process and underproduction of sugar cane vinasse
IV. Characteristics of sugar cane industry
wastewater
The wastewater or spillage products from such
distilleries contain huge quantity of dissolved organic
matter, heavy metals, dyes etc., along with other
pollutants. These discharge into water bodies, somber
the aquatic life in consonance with decrease in the
quality of water and irrigation land. Table 2 shows
the analyzed composition of molasses stillage coming
from the bottom of the stripper column of the ethanol
production plant.
Table 2- Characteristics of sugar cane vinnasse /Molasses stillage8
Sr. No. Parameter Range
1 pH 3.8-4.4
2 Total solids 60,000-90,000
3 Total suspended solids 2,000-14,000
4 Total dissolved solids 6,70,000- 73,000
5 Total volatile solids 45,000-65,000
6 Chemical oxygen demand 70,00,000- 98,000
7 Biochemical oxygen demand 45,000-60,000
8 Total nitrogen as N 1000-1,200
9 Potash as K 2,05,000-12,000
10 Phosphate as PO4 5,000-1,500
11 Sodium as Na 150--200
12 Chlorides as CI 5,000-8,000
13 Sulphates as SO4 2,000-5,000
14 Acidity as CaCO3 8,000—16,000
15 Temperature (after heat exchanger) 70-80o
C
Samuel and Muthukkaruppan (2011) conducted
experiment on the effluent and contaminated soil
from a sugar mill located at Cuddalore district, India
and reported that there was a gradual decrease in
the percentage seed germination and germination
value with sugar industry effluent concentration. The
untreated sugar industry effluent could possibly lead
to soil deterioration and low productivity. Terrestrial
and aquatic environmental pollution could be averted
by proper treatment of the effluents using suitable
conventional methods. In conclusion, sugar industry
effluent concentration governs seed germination. The
effects vary from crop to crop because each plant
species has its own tolerance of the different effluent
concentrations.
M. Rais Int. Journal of Engineering Research and Applications www.ijera.com
ISSN : 2248-9622, Vol. 5, Issue 1( Part 2), January 2015, pp.11-19
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V. Treatment of Effluents from Sugar
Cane Industry
Effective handling and disposal of the generated
effluent is a major concern in all Indian distilleries
since the units are required to meet the discharge
standards (Table 3) laid down by CPCB. To comply
with the disposal norms, it is recommended one or a
combination of the following schemes to treat the
generated wastewater.
Table 3- Distillery effluent composition limits ISI Standards (IS: 506-1980)
Characteristics For discharge into water
Course
For discharge into
public sewers
For discharge
on land
pH 5.5–9.0 5.5–9.0 5.5–9.0
BOD (mg/L) 100 500 500
Total suspended solids (mg/L) 100 600 –
Oil and grease (mg/L) 10 100 6–10
Temperature (◦
C) outlet Shall not exceed 40 ◦C in any
section of the stream within
15m from effluent
The various methods of treatment are as follows
VI. Biological Treatment
Anaerobic Process
The high organic content of wastewater from
sugar cane industry makes anaerobic treatment
attractive in comparison to direct aerobic treatment.
Therefore, biomethanation is the primary treatment
step and is often followed by two-stage aerobic
treatment before discharge into a water body or on
land for irrigation. Aerobic treatment alone is not
feasible due to the high energy consumption for
aeration, cooling, etc. Anaerobic treatment converts
over half of the effluent COD into biogas. Anaerobic
treatment can be successfully operated at high
organic loading rates; also, the biogas thus generated
can be utilized for steam generation in the boilers
thereby meeting the energy demands of the unit.
Further, low nutrient requirements and stabilized
sludge production are other associated benefits.
Anaerobic lagoons are the simplest option
for the anaerobic treatment of distillery spentwash9
. it
was reported that employing two anaerobic lagoons
in series resulted in final BOD levels up to 600 mg/l.
However, large area requirement, odor problem and
chances of ground water pollution restrict its usage.
These reactors offer the advantage of separating the
hydraulic retention time (HRT) from solids retention
time (SRT) so that slow growing anaerobic
microorganisms can remain in the reactor
independent of wastewater flow10
.
Aerobic treatment
The post-anaerobic treatment stage effluent still
has high organic loading and is dark brown in color,
hence it is generally followed by a secondary, aerobic
treatment. Solar drying of biomethanated spentwash
is one option but the large land area requirement
limits this practice. Further, in India, solar drying
beds become non-functional during the rainy season
(Nandy et al., 2002). The other treatment options that
have been demonstrated for biomethanated distillery
effluent are Aquaculture, Constructed wetlands
(CWs), Biocomposting, Fungal Treatment, Bacterial
treatment, and Algal treatment.
Physico-chemical treatment
Sugarcane molasses spentwash after biological
treatment by both anaerobic and aerobic method can
still have a BOD of 250–500 mg/l .Also, even though
biological treatment results in significant COD
removal, the effluent still retains the dark color .In
this context, various physico-chemical treatment
options have been explored10
.
Adsorption: Activated carbon is a widely used
adsorbent for the removal of organic pollutants from
wastewater but the relatively high cost restricts its
usage. Decolorization of synthetic melanoidin using
commercially available activated carbon as well as
activated carbon produced from sugarcane bagasse
was investigated11
.
Coagulation and flocculation: Coagulation studies
on spentwash after anaerobic–aerobic treatment have
also been conducted using bleaching powder
followed by aluminum sulfate. The optimum dosage
was 5 g/l bleaching powder followed by 3 g/l of
aluminum sulfate that resulted in 96% removal in
color, accompanied by up to 97% reduction in BOD
and COD12
.
Oxidation process: Oxidation by ozone could
achieve 80% decolorization for biologically treated
spent wash with simultaneous 15–25% COD
reduction. It also resulted in improved
biodegradability of the effluent. However, ozone only
M. Rais Int. Journal of Engineering Research and Applications www.ijera.com
ISSN : 2248-9622, Vol. 5, Issue 1( Part 2), January 2015, pp.11-19
www.ijera.com 17 | P a g e
transforms the chromophore groups but does not
degrade the dark colored polymeric compounds in the
effluent13
.
Membrane treatment: Pre-treatment of spentwash
with ceramic membranes prior to anaerobic digestion
is reported to halve the COD from 36,000 to 18,000
mg/l (Chang et al., 1994). The total membrane area
was 0.2m2
and the system was operated at a fluid
velocity of 6.08 m/s and 0.5 bar transmembrane
pressure. In addition to COD reduction, the pre-
treatment also improved the efficiency of the
anaerobic process possibly due to the removal of
inhibiting substances14
. In addition, reverse osmosis
(RO) has also been employed for distillery
wastewater treatment.
Electrodialysis: Electrodialysis has been explored
for desalting spentwash using cation and anion
exchange membranes resulting in 50–60% reduction
in potassium content (de Wilde, 1987). In another
study, Vlyssides et al. (1997) reported the treatment
of vinasse from beet molasses by electrodialysis
using a stainless steel cathode, titanium alloy anode
and 4% w/v NaCl as electrolytic agent. Up to 88%
COD reduction at pH 9.5 was obtained; however, the
COD removal percentage decreased at higher
wastewater feeding rates15,16
.
Evaporation/combustion: Molasses spentwash
containing 4% solids can be concentrated to a
maximum of 40% solids in a quintuple- effect
evaporation system with thermal vapor
recompression17
. The condensate with a COD of 280
mg/l can be used in fermenters. Combustion is also
an effective method of on-site vinasse disposal as it is
accompanied byproduction of potassium-rich ash that
can be used for land application18
.
Discussion: A range of biological and physico-
chemical methods have been investigated for the
treatment of wastewater from sugar cane industry
wastewater. Because of the very high COD,
anaerobic treatment with biogas recovery is
employed extensively as the first treatment step. this
treatment method reduces the organic pollution load
and brings down BOD to 80–95% of the original
value; however, the biodigested effluent still contains
BOD in the range of 5000–10,000 mg/l. further the
problem of color associated with this effluent not
only remains unsolved but actually gets aggravated
since the color causing melanoidin pigment
intensifies under anaerobic conditions19
. Therefore
anaerobically treated effluent is darker in color
compared to untreated spentwash and needs several-
fold dilution by fresh water prior to discharge.
Biological treatment using aerobic processes like
activated sludge, biocomposting etc. is presently
practiced by various molasses-based distilleries. Due
to the large volumes generated, only a part of the
total spentwash gets consumed in biocomposting.
Biocomposting utilizes sugarcane pressmud as the
filler material; thus it is typically employed by
distilleries attached to sugar mills. Since sugar
manufacturing is a seasonal operation, pressmud
availability is often a constraint. Further,
biocomposting requires large amount of land; also, it
cannot be carried out during the rainy season.
Though aerobic treatment like the conventional
activated sludge process leads to significant reduction
in COD, the process is energy intensive and the color
removal is still inadequate. Thus several pure cultures
of fungi, bacteria and algae have been investigated
specifically for their ability to decolorize the effluent
as discussed earlier. In all instances, supplementation
with either nitrogen or carbon source is almost
always necessary because the microbial species are
not able to utilize the spentwash as the sole carbon
source. Further, high dilution (typically up to 1:10
fold for untreated spentwash and 1:16–1:2 fold for
biomethanated spentwash) is required for optimal
microbial activity. In addition, these studies are
mostly limited to laboratory scale investigations and
no pilot/commercial scale operations are reported as
yet.
Physico-chemical treatment, viz. adsorption,
coagulation/ flocculation, oxidation processes,
membrane treatment have been examined with
particular emphasis on effluent decolorization.
Though these techniques are effective for both color
removal as well as reduction in organic loading,
sludge generation and disposal is a constraint in
coagulation/flocculation and adsorption.
Also, the cost of chemicals, adsorbents and
membranes is a deterrent to the adoption of these
methods. Membrane operations like microfiltration/
ultra filtration for spent wash treatment are
characterized by significant membrane fouling that
limits its applicability. Decolorization through
chemical treatment with ozone and chlorine leads to
temporary color reduction because of transformation
of the chromophore groups so these are not preferred
solutions20
.
Table 4-Status of Effluent Treatment of Sugarcane Industry7
,21,22
Status of Effluent
Treatment(Internationally)
Status of Effluent
Treatment(India)
Anaerobic digestion being used being used
Aerobic treatment being used being used
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ISSN : 2248-9622, Vol. 5, Issue 1( Part 2), January 2015, pp.11-19
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Adsorption, being used being used
Coagulation/ flocculation, being used being used
Oxidation processes, being used being used
Membrane treatment(RO) being used being used
VII. Possibilities of Use of Byproducts of
Sugarcane
The various possible uses of sugar can by
products are given in table 5- and use of vinasse for
various alternatives range from low capital cost
options to high capital cost technologies are as
follows:
 The simplest approach is the use of stillage as
fertilizer which returns most of the minerals back
into the soil for the next crop. Producing a feed
from stillage, one requires less capital
investment, since it consists of drying the
outcoming effluent before direct use as a
supplement. However, the main disadvantage of
this approach is the high mineral content in the
stillage, especially potassium, limiting the
maximum percentage which can be added to a
balanced feed.
 The recycling of stillage as substrate for the
cultivation of Candida yeast as a high protein
supplement
 Recycling of stillage as a source of energy by
evaporating the residual stream to a solids
content ranging from 50 to 60% prior to being
injected into the stillage fired boiler.
Methane generation through anaerobic digestion
has become one of the more convenient options, and
many research groups have reported about its benefits
Table 5-Possibilities of Use of Byproducts of Sugarcane (Internationally and India)7
,21
Product Internationally India
Bagasse Fuel, Paper and pulp industries Fuel
Molasses Ethanol ,dry yeast, Amino acids, and feed
supplement
Ethanol
Stillage, also known as
mosto, vinasse or rum
slops
Fertilizer, Animal feed, Stillage fired boiler,
Methane generation through anaerobic
digestion
Methane generation
through anaerobic
digestion
VIII. Conclusions
The main conclusions which could be drawn
from the above review are as follows:
The sugar cane industry employs various
treatment sequences to save water and to meet
regulatory norms. The combination of
biomethanation and biocomposting is a popular
choice for wastewater treatment and disposal.
Reverse osmosis and drying of biomethanated
effluent are emerging technologies for efficiently
managing this effluent. Considerable water saving
can be achieved by better house keeping, segregating,
recycling and reusing of non-process wastewater.
There are several initiatives being followed by Indian
distilleries to minimize their water consumption and
recycle the treated wastewater. However, in addition
to this, research to address existing gaps is also
necessary to provide a comprehensive and cost
effective solution to enable the industries to become
low water consuming and zero discharge units.
Reference
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Treatment of Sugarcane Industry Effluents: Science & Technology issues

  • 1. M. Rais Int. Journal of Engineering Research and Applications www.ijera.com ISSN : 2248-9622, Vol. 5, Issue 1( Part 2), January 2015, pp.11-19 www.ijera.com 11 | P a g e Treatment of Sugarcane Industry Effluents: Science & Technology issues M. Rais1* , A. Sheoran2 1 CSIR-National Institute of Science, Technology & Development Studies, Pusa Gate, K.S. Krishnan Marg, New Delhi 110 012, India 2 Department of Civil Engineering Birla Institute of Technology & Science, Pilani Pilani 333031 (Rajasthan) India Abstract The consumption of large volumes of water and the generation of organic compounds as liquid effluents are major environmental problems in sugarcane processing industry. The inadequate and indiscriminate disposal of this effluent in soils and water bodies has received much attention since decades ago, due to environmental problems associated to this practice. Because of the large quantities of effluent produced, alternative treatments have been developed. The low pH, electric conductivity, and chemical elements present in sugarcane effluent may cause changes in the chemical and physical–chemical properties of soils, rivers, and lakes with frequent discharges over a long period of time, and also have adverse effects on agricultural soils and biota in general. The sugar cane industry is among those industries with the largest water demands and, in addition, is an important source of non-toxic organic pollution combined with the fact that India it is second largest producer and largest consumer makes it all the more important. This paper examines the present status of sugarcane effluent, its characteristics and chemical composition. Keeping in view the relevant policy scenario in India, various available treatment technologies are discussed. Key words- Sugarcane industry, effluent management, treatment I. Introduction Increased demand for food and the need to sustain the ever increasing world population have led to massive increase in both agricultural and industrial activities. Agriculture is one of the most significant sectors of the Indian Economy. Agriculture is the only means of living for almost two thirds of the workers in India. The agriculture sector of India has occupied 43% of India’s geographical area, and is contributing 16.1% of India’s GDP. Agriculture still contributes significantly to India’s GDP despite decline of its share in India’s GDP. There are number of crops grown by farmers. These include different food crops, commercial crops, oil seeds etc., sugarcane is one of the important commercial crops grown in India. There are around 45 millions of sugar cane growers in India and a larger portion of rural laborers in the country largely rely upon this industry. Sugar Industry is one of the agricultural based industries. Today, India is one of the first ten industrialized countries of the world. India, like any other developing countries, is faced with problems arising from the negative impact of economic development due to water or industrial pollution. Rapid progress made in industrialization without adequate environmental safety measures lead to pollution of water, which in turn, results in lack of good quality water both for irrigation and drinking purposes. Every human society, whether urban, industrial and most technologically advanced, disposes of certain kinds of by-products and waste products into the biosphere in large quantities, ultimately affecting the normal functioning of the ecosystem and have adverse effect on plants, animals and human. Awareness of environmental problems and the potential hazards caused by industrial wastewater has promoted many countries to limit the discharge of polluting effluents1 . In many developing countries, especially in Asia and South America, sugar cane industry is one of the most important agricultural industries. As a consequence, sugar cane industry has significant wastewater production. Unfortunately, due to the lack of know-how and financial support, most of sugar cane industries in developing countries discharge their wastewater without adequate treatment. Similar with other wastewater generated by food processing plants, wastewater from sugar cane industry generally contains organic materials such as carbohydrates and proteins2 . Generally effluent generated from sugarcane industry is disposed off on land. While moving on land, part of pollutants in the effluent may be migrated and deposited between the gaps of soil stratum and adsorbed on the soil particles surface, resulting in pollution of soil. Furthermore, the migrated effluent flows through the gaps in the soil RESEARCH ARTICLE OPEN ACCESS
  • 2. M. Rais Int. Journal of Engineering Research and Applications www.ijera.com ISSN : 2248-9622, Vol. 5, Issue 1( Part 2), January 2015, pp.11-19 www.ijera.com 12 | P a g e stratum and reaches the groundwater table, which may cause impact to the aquifer and thereby pose a potential risk to human health as well as the surrounding environment3 . 36% 24% 11% 11% 5% 4% 3% 2% 2% 2% 0% 5% 10% 15% 20% 25% 30% 35% 40% Major Producing States in India Figure 1: Total % share of the sugarcane production by major sugarcane producing states in India in 2012- 201323 Figure 2: Production of sugarcane in India in last 10 years23 II. Sugar cane industry In many developing countries, especially in Asia and South America, sugar cane industry is one of the most important agricultural industries. Sugar cane mill industry is one of the oldest industries in India, as in other parts of the world. In India, sugarcane industry is highly responsible for creating significant impact on rural economy after textiles3 . India is the world’s second largest sugarcane producer, with nearly 5 million hectares of cultivated area and provides direct employment to more than 3.6 lakes person Table 1. The main final products of sugar cane industry are crystalline sugar and bio-ethanol. The latter is obtained from the fermentation and distillation of sugar cane juice and molasses. Quantitatively, the
  • 3. M. Rais Int. Journal of Engineering Research and Applications www.ijera.com ISSN : 2248-9622, Vol. 5, Issue 1( Part 2), January 2015, pp.11-19 www.ijera.com 13 | P a g e most significant by-product is bagasse, the solid residue from sugar cane after juice extraction and stillage (also called vinnasse or dunder), the liquid waste effluent after the distillation process of sugar cane juice. Sugar mill with annexed alcohol distilleries generally release an average of 155 L of stillage and 250 Kg bagasse per 1,000 Kg of sugar cane to obtain 12 L of alcohol and 95 Kg of sugar 5 . Alcohol distilleries are a major agro-based industry in India with around 300 units located mainly in rural, sugarcane growing regions. The total installed capacity is 3250 million L alcohol per annum with an estimated production of 2300.4 million L in 2006– 2007. Most of the distilleries co-exist with sugar mills and utilize the molasses from cane sugar manufacture as the starting material for alcohol production. As per the Ministry of Environment & Forests (MoEF), Government of India, alcohol distilleries are listed at the top of ―Red Category‖ industries having a high polluting potential. The industry generates large volumes (8–15 kL/kL alcohol) of dark brown colored wastewater (―spentwash‖) with high biochemical oxygen demand (BOD) and Chemical oxygen demand (COD).This poses a serious pollution threat; thus it is mandatory for distilleries to take appropriate measures to comply with the discharge standards set by the Central Pollution Control Board (CPCB), which is the national agency responsible for environmental compliance6,7 . Table 1- Sugarcane production in major countries4 Harvest area (million ha) Annual production (million t) Average income (t/ha) Brazil 8.14 648 79.7 India 5.06 348 68.9 China 1.71 124 73.1 Pakistan 1.24 64 51.5 Thailand 1.05 73 69.7 Mexico 0.67 51 76.4 Colombia 0.38 39 100.4 Australia 0.39 34 87.1 South Africa 0.43 21 48.2 Cuba 0.38 16 41.3
  • 4. M. Rais Int. Journal of Engineering Research and Applications www.ijera.com ISSN : 2248-9622, Vol. 5, Issue 1( Part 2), January 2015, pp.11-19 www.ijera.com 14 | P a g e Brazil 30% India 21%Thailand 8% Pakistan 4% United States 6% Mexico 4% China 9% Europian Union 13% Columbia 2% Australia 3% Fig. 3- Sugarcane worldwide distribution24 III. Sugarcane Processing The main final products of sugar cane industry are crystalline sugar and bio-ethanol. The latter is obtained from the fermentation and distillation of sugar cane juice and molasses. Quantitatively, the most significant by-product is bagasse, the solid residue from sugar cane after juice extraction and stillage (also called vinnasse or dunder), the liquid waste effluent after the distillation process of sugar cane juice. Bagasse can be used in boilers during combustion, while stillage is mainly disposed to field crops, incorporating a risk for aquatic pollution. Surface water pollution potential is mainly due to the high contents of organic matters in stillage. Organic matters cause oxygen depletion by heterotrophic bio- degradation when enter in surface water. Stillage also contains high concentration of potassium which can accumulate at toxic levels in the soil5 .
  • 5. M. Rais Int. Journal of Engineering Research and Applications www.ijera.com ISSN : 2248-9622, Vol. 5, Issue 1( Part 2), January 2015, pp.11-19 www.ijera.com 15 | P a g e Fig. 4- Flowchart of ethanol production process and underproduction of sugar cane vinasse IV. Characteristics of sugar cane industry wastewater The wastewater or spillage products from such distilleries contain huge quantity of dissolved organic matter, heavy metals, dyes etc., along with other pollutants. These discharge into water bodies, somber the aquatic life in consonance with decrease in the quality of water and irrigation land. Table 2 shows the analyzed composition of molasses stillage coming from the bottom of the stripper column of the ethanol production plant. Table 2- Characteristics of sugar cane vinnasse /Molasses stillage8 Sr. No. Parameter Range 1 pH 3.8-4.4 2 Total solids 60,000-90,000 3 Total suspended solids 2,000-14,000 4 Total dissolved solids 6,70,000- 73,000 5 Total volatile solids 45,000-65,000 6 Chemical oxygen demand 70,00,000- 98,000 7 Biochemical oxygen demand 45,000-60,000 8 Total nitrogen as N 1000-1,200 9 Potash as K 2,05,000-12,000 10 Phosphate as PO4 5,000-1,500 11 Sodium as Na 150--200 12 Chlorides as CI 5,000-8,000 13 Sulphates as SO4 2,000-5,000 14 Acidity as CaCO3 8,000—16,000 15 Temperature (after heat exchanger) 70-80o C Samuel and Muthukkaruppan (2011) conducted experiment on the effluent and contaminated soil from a sugar mill located at Cuddalore district, India and reported that there was a gradual decrease in the percentage seed germination and germination value with sugar industry effluent concentration. The untreated sugar industry effluent could possibly lead to soil deterioration and low productivity. Terrestrial and aquatic environmental pollution could be averted by proper treatment of the effluents using suitable conventional methods. In conclusion, sugar industry effluent concentration governs seed germination. The effects vary from crop to crop because each plant species has its own tolerance of the different effluent concentrations.
  • 6. M. Rais Int. Journal of Engineering Research and Applications www.ijera.com ISSN : 2248-9622, Vol. 5, Issue 1( Part 2), January 2015, pp.11-19 www.ijera.com 16 | P a g e V. Treatment of Effluents from Sugar Cane Industry Effective handling and disposal of the generated effluent is a major concern in all Indian distilleries since the units are required to meet the discharge standards (Table 3) laid down by CPCB. To comply with the disposal norms, it is recommended one or a combination of the following schemes to treat the generated wastewater. Table 3- Distillery effluent composition limits ISI Standards (IS: 506-1980) Characteristics For discharge into water Course For discharge into public sewers For discharge on land pH 5.5–9.0 5.5–9.0 5.5–9.0 BOD (mg/L) 100 500 500 Total suspended solids (mg/L) 100 600 – Oil and grease (mg/L) 10 100 6–10 Temperature (◦ C) outlet Shall not exceed 40 ◦C in any section of the stream within 15m from effluent The various methods of treatment are as follows VI. Biological Treatment Anaerobic Process The high organic content of wastewater from sugar cane industry makes anaerobic treatment attractive in comparison to direct aerobic treatment. Therefore, biomethanation is the primary treatment step and is often followed by two-stage aerobic treatment before discharge into a water body or on land for irrigation. Aerobic treatment alone is not feasible due to the high energy consumption for aeration, cooling, etc. Anaerobic treatment converts over half of the effluent COD into biogas. Anaerobic treatment can be successfully operated at high organic loading rates; also, the biogas thus generated can be utilized for steam generation in the boilers thereby meeting the energy demands of the unit. Further, low nutrient requirements and stabilized sludge production are other associated benefits. Anaerobic lagoons are the simplest option for the anaerobic treatment of distillery spentwash9 . it was reported that employing two anaerobic lagoons in series resulted in final BOD levels up to 600 mg/l. However, large area requirement, odor problem and chances of ground water pollution restrict its usage. These reactors offer the advantage of separating the hydraulic retention time (HRT) from solids retention time (SRT) so that slow growing anaerobic microorganisms can remain in the reactor independent of wastewater flow10 . Aerobic treatment The post-anaerobic treatment stage effluent still has high organic loading and is dark brown in color, hence it is generally followed by a secondary, aerobic treatment. Solar drying of biomethanated spentwash is one option but the large land area requirement limits this practice. Further, in India, solar drying beds become non-functional during the rainy season (Nandy et al., 2002). The other treatment options that have been demonstrated for biomethanated distillery effluent are Aquaculture, Constructed wetlands (CWs), Biocomposting, Fungal Treatment, Bacterial treatment, and Algal treatment. Physico-chemical treatment Sugarcane molasses spentwash after biological treatment by both anaerobic and aerobic method can still have a BOD of 250–500 mg/l .Also, even though biological treatment results in significant COD removal, the effluent still retains the dark color .In this context, various physico-chemical treatment options have been explored10 . Adsorption: Activated carbon is a widely used adsorbent for the removal of organic pollutants from wastewater but the relatively high cost restricts its usage. Decolorization of synthetic melanoidin using commercially available activated carbon as well as activated carbon produced from sugarcane bagasse was investigated11 . Coagulation and flocculation: Coagulation studies on spentwash after anaerobic–aerobic treatment have also been conducted using bleaching powder followed by aluminum sulfate. The optimum dosage was 5 g/l bleaching powder followed by 3 g/l of aluminum sulfate that resulted in 96% removal in color, accompanied by up to 97% reduction in BOD and COD12 . Oxidation process: Oxidation by ozone could achieve 80% decolorization for biologically treated spent wash with simultaneous 15–25% COD reduction. It also resulted in improved biodegradability of the effluent. However, ozone only
  • 7. M. Rais Int. Journal of Engineering Research and Applications www.ijera.com ISSN : 2248-9622, Vol. 5, Issue 1( Part 2), January 2015, pp.11-19 www.ijera.com 17 | P a g e transforms the chromophore groups but does not degrade the dark colored polymeric compounds in the effluent13 . Membrane treatment: Pre-treatment of spentwash with ceramic membranes prior to anaerobic digestion is reported to halve the COD from 36,000 to 18,000 mg/l (Chang et al., 1994). The total membrane area was 0.2m2 and the system was operated at a fluid velocity of 6.08 m/s and 0.5 bar transmembrane pressure. In addition to COD reduction, the pre- treatment also improved the efficiency of the anaerobic process possibly due to the removal of inhibiting substances14 . In addition, reverse osmosis (RO) has also been employed for distillery wastewater treatment. Electrodialysis: Electrodialysis has been explored for desalting spentwash using cation and anion exchange membranes resulting in 50–60% reduction in potassium content (de Wilde, 1987). In another study, Vlyssides et al. (1997) reported the treatment of vinasse from beet molasses by electrodialysis using a stainless steel cathode, titanium alloy anode and 4% w/v NaCl as electrolytic agent. Up to 88% COD reduction at pH 9.5 was obtained; however, the COD removal percentage decreased at higher wastewater feeding rates15,16 . Evaporation/combustion: Molasses spentwash containing 4% solids can be concentrated to a maximum of 40% solids in a quintuple- effect evaporation system with thermal vapor recompression17 . The condensate with a COD of 280 mg/l can be used in fermenters. Combustion is also an effective method of on-site vinasse disposal as it is accompanied byproduction of potassium-rich ash that can be used for land application18 . Discussion: A range of biological and physico- chemical methods have been investigated for the treatment of wastewater from sugar cane industry wastewater. Because of the very high COD, anaerobic treatment with biogas recovery is employed extensively as the first treatment step. this treatment method reduces the organic pollution load and brings down BOD to 80–95% of the original value; however, the biodigested effluent still contains BOD in the range of 5000–10,000 mg/l. further the problem of color associated with this effluent not only remains unsolved but actually gets aggravated since the color causing melanoidin pigment intensifies under anaerobic conditions19 . Therefore anaerobically treated effluent is darker in color compared to untreated spentwash and needs several- fold dilution by fresh water prior to discharge. Biological treatment using aerobic processes like activated sludge, biocomposting etc. is presently practiced by various molasses-based distilleries. Due to the large volumes generated, only a part of the total spentwash gets consumed in biocomposting. Biocomposting utilizes sugarcane pressmud as the filler material; thus it is typically employed by distilleries attached to sugar mills. Since sugar manufacturing is a seasonal operation, pressmud availability is often a constraint. Further, biocomposting requires large amount of land; also, it cannot be carried out during the rainy season. Though aerobic treatment like the conventional activated sludge process leads to significant reduction in COD, the process is energy intensive and the color removal is still inadequate. Thus several pure cultures of fungi, bacteria and algae have been investigated specifically for their ability to decolorize the effluent as discussed earlier. In all instances, supplementation with either nitrogen or carbon source is almost always necessary because the microbial species are not able to utilize the spentwash as the sole carbon source. Further, high dilution (typically up to 1:10 fold for untreated spentwash and 1:16–1:2 fold for biomethanated spentwash) is required for optimal microbial activity. In addition, these studies are mostly limited to laboratory scale investigations and no pilot/commercial scale operations are reported as yet. Physico-chemical treatment, viz. adsorption, coagulation/ flocculation, oxidation processes, membrane treatment have been examined with particular emphasis on effluent decolorization. Though these techniques are effective for both color removal as well as reduction in organic loading, sludge generation and disposal is a constraint in coagulation/flocculation and adsorption. Also, the cost of chemicals, adsorbents and membranes is a deterrent to the adoption of these methods. Membrane operations like microfiltration/ ultra filtration for spent wash treatment are characterized by significant membrane fouling that limits its applicability. Decolorization through chemical treatment with ozone and chlorine leads to temporary color reduction because of transformation of the chromophore groups so these are not preferred solutions20 . Table 4-Status of Effluent Treatment of Sugarcane Industry7 ,21,22 Status of Effluent Treatment(Internationally) Status of Effluent Treatment(India) Anaerobic digestion being used being used Aerobic treatment being used being used
  • 8. M. Rais Int. Journal of Engineering Research and Applications www.ijera.com ISSN : 2248-9622, Vol. 5, Issue 1( Part 2), January 2015, pp.11-19 www.ijera.com 18 | P a g e Adsorption, being used being used Coagulation/ flocculation, being used being used Oxidation processes, being used being used Membrane treatment(RO) being used being used VII. Possibilities of Use of Byproducts of Sugarcane The various possible uses of sugar can by products are given in table 5- and use of vinasse for various alternatives range from low capital cost options to high capital cost technologies are as follows:  The simplest approach is the use of stillage as fertilizer which returns most of the minerals back into the soil for the next crop. Producing a feed from stillage, one requires less capital investment, since it consists of drying the outcoming effluent before direct use as a supplement. However, the main disadvantage of this approach is the high mineral content in the stillage, especially potassium, limiting the maximum percentage which can be added to a balanced feed.  The recycling of stillage as substrate for the cultivation of Candida yeast as a high protein supplement  Recycling of stillage as a source of energy by evaporating the residual stream to a solids content ranging from 50 to 60% prior to being injected into the stillage fired boiler. Methane generation through anaerobic digestion has become one of the more convenient options, and many research groups have reported about its benefits Table 5-Possibilities of Use of Byproducts of Sugarcane (Internationally and India)7 ,21 Product Internationally India Bagasse Fuel, Paper and pulp industries Fuel Molasses Ethanol ,dry yeast, Amino acids, and feed supplement Ethanol Stillage, also known as mosto, vinasse or rum slops Fertilizer, Animal feed, Stillage fired boiler, Methane generation through anaerobic digestion Methane generation through anaerobic digestion VIII. Conclusions The main conclusions which could be drawn from the above review are as follows: The sugar cane industry employs various treatment sequences to save water and to meet regulatory norms. The combination of biomethanation and biocomposting is a popular choice for wastewater treatment and disposal. Reverse osmosis and drying of biomethanated effluent are emerging technologies for efficiently managing this effluent. Considerable water saving can be achieved by better house keeping, segregating, recycling and reusing of non-process wastewater. There are several initiatives being followed by Indian distilleries to minimize their water consumption and recycle the treated wastewater. However, in addition to this, research to address existing gaps is also necessary to provide a comprehensive and cost effective solution to enable the industries to become low water consuming and zero discharge units. Reference [1] Sureshkumar K & Mariappan V, Evaluation of Sugarcane Mill Effluent and its Impact on the Growth ,Biochemical and DNA Profile of Chloroxylos Swietenia, DC, International Journal of Research in Environmental Science and Technology; 3(3) (2013), 92- 99. [2] Nayono S E, Anaerobic Treatment of Wastewater From Sugarcane Industry, ( 2005) http://101.203.168.85/sites/default/files/132 231624/Treatment%20of%20Sugar%20Can e%20Wastewater_0.pdf (accessed 25.08.2014). . [3] Sivakumar D, A study on contaminant migration of sugarcane effluent through porous soil medium. Int. J. Environ. Sci. Tech., 8 (3) (2011), 593-604. [4] FAO, Food and Agriculture Organization of United Nations (2013) http://www.fao.org/statistics/en/(accessed 1.09.2014). [5] Siddiqui W A & Waseem M, A Comparative Study of Sugar Mill Treated and Untreated Effluent- A Case Study, Orient. J. Chem., 28(4) (2012) , 1899-1904. [6] (CPCB, 2002) CPCB (Central Pollution Control Board). Annual report; 2002–2003. http://www.cpcb.nic.in/ar2003/ar2- 3ch10.htm. [7] Tewari, P.K. Batra, V.S. Balakrishnan M. ―Water management initiatives in sugarcane
  • 9. M. Rais Int. Journal of Engineering Research and Applications www.ijera.com ISSN : 2248-9622, Vol. 5, Issue 1( Part 2), January 2015, pp.11-19 www.ijera.com 19 | P a g e molasses based distilleries in India ―Resources, Conservation and Recycling 52(2007), 351–367. [8] Seth, R., Goyal, S.K., Handa, B.K., 1995. Fixed film biomethanation of distillery spentwash using low cost porous media. Resources, Conservation and Recycling 14 (2), 79–89. [9] Wilkie, A.C., Riedesel, K.J., Owens, J.M. Stillage characterization and anaerobic treatment of ethanol stillage from conventional and cellulosic feedstocks. Biomass and Bioenergy 19 (2(2000)), 63– 102. [10] Mall, I.D., Kumar, V. Removal of organic matter from distillery effluent using low cost adsorbent. Chemical EngineeringWorld XXXII (7) (1997). , 89–96. [11] Bernardo, E.C., Egashira, R., Kawasaki, J., Decolorization of molasses wastewater using activated carbon prepared from cane bagasse. Carbon 35 (9(1997). ), 1217–1221. [12] Chandra, R., Singh, H., Chemical decolorization of anaerobically treated distillery effluent. Indian Journal of Environmental Protection 19 (11) (1999), 833–837. [13] Pena, M., Coca, M., Gonzalez, R., Rioja, R., Garcı´a, M.T., Chemical oxidation of wastewater from molasses fermentation with ozone. Chemosphere 51 (9) (2003), 893– 900. [14] Chang, I.S., Choo, K.H., Lee, C.H., Pek, U.H., Koh, U.C., Kim, S.W., Koh, J.H., Application of ceramic membrane as a pre- treatment in anaerobic digestion of alcohol- distillery wastes. Journal of Membrane Science 90 (1–2) (1994) 131–139. [15] de Wilde, F.G.N., Demineralization of a molasses distillery wastewater. Desalination 67, (1987), 481–493. [16] Vlyssides, A.G., Israilides, C.J., Loizidou, M., Karvouni, G., Mourafeti, V., Electrochemical treatment of vinasse from beet molasses. Water Science and Technology 36 (2–3) (1997), 271–278. [17] Bhandari, H.C., Mitra, A.K., Kumar, S., Crest’s integrated system: reduction and recycling of effluents in distilleries. In: Tewari, P.K. (Ed.), Liquid Asset, Proceedings of Indo-EU Workshop on Promoting Efficient Water Use in Agro- based Industries. TERI Press, New Delhi, India, (2004) 167–169. [18] Cortez, L.A.B., Perez, L.E.B., Experiences on vinasse disposal: Part III: combustion of vinasse-#6 fuel oil emulsions. Braz. J. Chem. Eng. vol. 14 no. 1 São Paulo Mar. 1997, http://dx.doi.org/10.1590/S0104- 66321997000100002 (accessed 21.09.2014). [19] Patil, P.U., Kapadnis, B.P., Dhamankar, V.S., Decolorization of synthetic melanoidin and biogas effluent by immobilized fungal isolate of Aspergillus niger UM2, All India Distiller’s Association (AIDA) Newsletter (2003).53–56. [20] Jain, S., Balakrishnan, M., Membrane fouling and cleaning in ultrafiltration of anaerobically treated distillery effluent. In: Euromembrane 2004, Hamburg, Germany, 28 September–1 October 2004. [21] Olguin E J, Doelle H W, Mercado G, Resource recovery through recycling of sugar processing by-products and residuals. Resources, Conservation and Recycling, 15 (1995) ,85-94. [22] Nataraj, S.K., Hosamani, K.M., Aminabhavi, T.M., Distillery wastewater treatment by the membrane-based nanofiltration and reverse osmosis processes. Water Research, 40 (12)( 2006),2349–2356 [23] http://agricoop.nic.in/imagedefault/trade/Sug arNew29.pdf (accessed 21.09.2014) [24] http://www.sucden.com/statistics/1_world- sugar-production (accessed 21.09.2014)