CHAPTER ONE
INTRODUCTION
1.1 BACKGROUND OF STUDY
The average person excretes 72.5 kg of waste and urinates 500 gallons per year. With a world population of over seven billion people, we're talking about 507.5 billion kg of feces and 3,500 billion liters of urine per year. The single flush of a toilet may easily dispose of many people's wastes. However, the World Health Organization believes that a billion individuals are affected. People who do not have access to sanitation infrastructure defecate in pits and drains all over the world. Human excrement and urine now have immediate access to aquifers, contaminating drinking wells on a regular basis. Sanitation systems that are designed to recover resources in a safe and effective manner can aid in overall resource management in a community. On a scale ranging from a single rural household to a city, a variety of technologies and approaches can be used to acquire hugely beneficial resources and make them usable for safe, beneficial applications that support human well enough and overall sustainable development. But what if organic waste could be kept out of the water and used to generate electricity for farming? Excreta are most commonly used as a manure and soil enhancer in agriculture. This is also known as a "closing the loop" strategy for cleanliness in agriculture. It's an important part of the ecological sanitation strategy. Human feces include a variety of resources, including plant nutrients, organic materials, and energy. This study discusses the modeling of the variable parameters in developing safe fertilizer from human excreta to fertilize farms and gardens, which is especially important in areas without alternative sewage infrastructure.
1.2 PROBLEM STATEMENT
The indiscriminate disposal of human waste is mostly due to the fact that around one billion people around the world lack access to sanitary amenities rather they defecate in sewers and pits. Human excrement and urine now have immediate access to aquifers, contaminating water wells on a regular basis. If this is not addressed, the rate/level of pollution in the environment will rise to the point where it is unhealthy for everyone. As a result, it is critical that these wastes be processed and repurposed for environmental reasons.
1.3 OBJECTIVE OF STUDY
Biosolids (organic
fertilizer) are an environmentally beneficial and highly easy-to-handle
commodity that may be used to harness organic wastes for use as fertilizer in
farming. Biosolids are solid, semi-solid, or watery products of sewage
treatment that have been properly processed to allow safe land application as
an alternative to landfilling or cremation. This
research aims to find the optimum biosolids
properties by modeling the variable parameters in the production of
fertilizer (biosolids) from human excreta to improve biosolids handling
features and land economic feasibility, as well as reduce the risk to human
health, the environment, and unpleasantness issues that come with them.
1.4 SIGNIFICANCE OF STUDY
Biosolids
are often burnt, landfilled, or applied to the ground. General standards,
numerical restrictions on pollutant and pathogen amounts, managerial
approaches, and technical requirements are all part of each disposal technique.
Biosolids are now thought of to be valuable. This research sheds more light on
the effects of biosolid properties that can be modified to achieve better grade
biosolids, higher nutrient recovery, and the achieved properties can help
effect a better public perceptive and approval in order promote the use of
bisolids in agriculture.
1.5 SCOPE OF STUDY
The
following topics are the subject of this research:
a) A process for producing fertilizer (biosolids) from human
excrement for use as soil conditioners.
b) The advantages of reusing human feces.
c) The advantages of using biosolids over chemical fertilizers.
d) Development of models to show the effects of various variable
parameters on organic fertilizer (biosolids) produced from human excreta.
The land application processes of biosolids, the regulations governing biosolids application, and the biosolids utilization rate in Nigeria are not included in this study.
CHAPTER
TWO
2.0 LITERATURE REVIEW
2.1 FERTILIZER
To
maintain sufficient food production, it is critical to ensure that plants
receive the proper nutrients. Any natural or manmade substance
(excluding liming materials) that is added to soil or plant tissues to give one
or more plant nutrients required for plant growth is referred to as a
fertilizer. Fertilizer comes in a range of natural and synthetic forms. Commercial
fertilizer consumption has continuously expanded over the previous 50 years,
nearly doubling to a present pace of 100 million tonnes of nitrogen per year. One-third
of today's food could not be cultivated without industrial fertilizers,
according to estimates.
2.1.1 Mechanism
Fertilizers speed up the growth of plants. There are two ways to
accomplish this goal. The first method is to employ nutrient-dense additions.
The second method by which some fertilizers act is by modifying water retention
and oxygenation in the soil. Fertilizers usually contain the following
ingredients in varied proportions:
2.1.1.1 Three main macronutrients:
Nitrogen (N): contributes to leaves growth Phosphorus (P): Root,
flower, seed, and fruit growth. Potassium (K): Promotes
flowering and fruiting by promoting stem growth and water transport in plants
2.1.1.2 Three secondary macronutrients
Sulfur
(S), Magnesium (Mg), and Calcium (Ca).
2.1.1.3 Micronutrients
Zinc
(Zn), Boron (B), Manganese (Mn), Molybdenum (Mo), Copper (Cu), Iron (Fe) and
Silicon (Si), Cobalt (Co), vanadium (V).
The elements are used to define the nutrients
that plants require, but they are not employed as fertilizers. Fertilizers, on
the other hand, are made up of compounds that include these components. The
essential nutrients are consumed in increasing quantities and are present in
plant tissue in concentrations ranging from 0.15 % to 6.0 % dry matter
(0% moisture). The four fundamental elements found in plants are hydrogen,
oxygen, carbon, and nitrogen. Carbon, hydrogen, and oxygen are common in water
and carbon dioxide. Regardless of the fact that nitrogen constitutes up the
bulk of the atmosphere, plants are unable to use it. Nitrogen is an essential
fertilizer since it is present in proteins, DNA, and other constituents. To be
a nutrient for plants, nitrogen must be made available in a "fixed"
form. Only a few bacteria and their host plants (most notably legumes) are
capable of converting nitrogen (N2) in the atmosphere to ammonia.
Phosphate is required for the synthesis of DNA, ATP (the cell's primary energy
carrier), and some lipids.
Micronutrients are absorbed in smaller amounts and are detected in plant tissue at concentrations ranging from 0.15 to 400 parts per million (ppm) (less than 0.04% dry matter). These elements are typically found around the active sites of plant metabolic enzymes. Water-soluble salts are used to provide these nutrients. Iron converts into insoluble (bio-unavailable) molecules at moderate soil pH and phosphate concentrations, providing unique problems. As a result, iron is frequently given as a chelate complex, such as the EDTA derivative. Micronutrient requirements are determined by the plant and its surroundings. Sugar beets, for example, tend to require boron, while legumes require cobalt, and climatic factors such as heat or dryness reduce boron availability for plants. These elements have a significantly greater impact than their weight % because they enable catalysts (enzymes).
2.1.2 Classification
Fertilizers are classified in several ways. Straight fertilizers
are classified as single-nutrient fertilizers since they only provide one
nutrient (e.g., K, P, or N). Multinutrient fertilizers (also known as
"complex fertilizers") are fertilizers that contain two or more nutrients,
such as nitrogen and phosphorus. Fertilizers are also classed as inorganic or
organic (which is the subject of this article). Except for ureas, inorganic
fertilizers do not contain carbon-containing compounds. Organic fertilizers are
often made up of (recycled) plant or animal debris. Because of the multiple
chemical processes necessary for their synthesis, inorganic fertilizers are
sometimes referred to as synthetic fertilizers.
2.1.2.1 Single nutrient ("straight") fertilizers
The most often used nitrogen-based direct fertilizers are ammonia
or its solutions. Ammonium nitrate (NH4NO3) is also
extensively used. Urea, like ammonia and ammonium nitrate, is a basic nitrogen
source having the benefit of being solid and non-explosive. Calcium ammonium
nitrate (Ca(NO3)2 • NH4 • 10H2O)
has just a little share of the nitrogen fertilizer market (4 percent in 2007). Superphosphates
are the most common straight phosphate fertilizers. SSP is made up of 14–18
percent P2O5, this time in the form of Ca(H2PO4)2,
as well as phosphogypsum (CaSO4 • 2H2O). TSP is normally
made up of 44-48 percent P2O5 and no gypsum. Double superphosphate
is a compound composed of single and triple superphosphate. A typical
superphosphate fertilizer is water soluble to the tune of 90%. Muriate
of Potash is the most common potassium-based straight fertilizer (MOP). Muriate
of Potash is commonly offered as a 0-0-60 or 0-0-62 fertilizer and contains
95-99 percent KCl.
2.1.2.2 Multinutrient fertilizers
Fertilizers like this are routinely utilized.
They're made up of at least two nutrients.
♦Binary fertilizers (NP, NK, PK): Major two-component fertilizers provide both nitrogen and phosphorus to
plants. They're referred to as NP fertilizers. The two most commonly utilized
NP fertilizers are monoammonium phosphate (MAP) and diammonium phosphate (DAP)
(DAP). The water solubility of MAP and DAP fertilizers is around 85%.
♦NPK fertilizers:
The
three components of NPK fertilizers are nitrogen, phosphorus, and potassium.
The NPK rating system is a method of characterizing the amount of nitrogen,
phosphorus, and potassium in a fertilizer. NPK ratings (e.g., 10-10-10 or
16-4-8) are three digits spaced by dashes that characterize the chemical
composition of fertilizers. The first figure indicates the product's nitrogen
content; the second, P2O5; and the third, K2O.
Although fertilizers do not include P2O5 or K2O,
the system is a common abbreviation for the quantity of phosphate (P) or
potassium (K) in a fertilizer. A 50-pound (23 kg) bag of fertilizer branded 16-4-8
includes 8 pound (3.6 kg) of nitrogen (16 percent of the 50 pounds), 2 pounds
of phosphorus (4 percent of the 50 pounds), and 4 pounds of potassium (K2O)
(8 percent of 50 pounds). The N-P-K method is used by the majority of
fertilizers, however the Australian system, which employs an N-P-K-S system,
adds a fourth number for sulfur and uses elemental values for all components,
including P and K.
2.1.2.3 Organic fertilizers
The term
"organic fertilizers" relates to fertilizers of an organic biologic
origin, that is, fertilizers derived from live or previously living materials.
Organic fertilizers can also refer to commercially produced and regularly
packaged products that aim to satisfy the demands and restrictions set forth by
"organic agriculture" and "environmentally friendly"
gardening related food and plant production systems that use synthetic
fertilizers and pesticides to a considerable extent or avoid them entirely. Certain
organic materials, as well as appropriate additives such as nutritious rock
powders, ground sea shells (crab, oyster, etc. ), other prepared products such
as seed meal or kelp, and cultivated microorganisms and derivatives, are
generally included in organic fertilizer products.
Organic fertilizers include animal wastes,
agricultural plant wastes, compost, and treated sewage sludge (biosolids).
Aside from manures, animal supplies can include bloodmeal, bone meal, feather
meal, hides, hoofs, and horns from animal slaughter. Organically produced items
available to industry, such as sewage sludge, may not be ideal components of
organic farming and gardening due to difficulties ranging from residual toxins
to public perception. Processed organics, on the other hand, may be
incorporated in and promoted by commercially available "organic
fertilizers" due to their consumer appeal. The majority of these items,
regardless of definition or composition, have less concentrated nutrients that
are more difficult to assess. They may have soil-building properties and appeal
to those who want to farm or garden in a more “natural” way.
In terms of volume, peat is the most widely
utilized commercially available organic soil supplement. It's an immature form
of coal that improves soil aeration and water absorption while giving plants no
nutritional value. As a result, it is classified as an amendment rather than a
fertilizer, as stated at the beginning of the article. Coir (made from coconut
husks), bark, and sawdust all behave similarly (though not identically) to peat
when applied to soil because of their restricted nutrient inputs. Organic soil
additions and texturizers are other names for them. Some organic texturizers
(as well as compost and other materials) can have a negative impact on
nutrition. Fresh sawdust can deplete soil nutrients, lowering pH, but organic
texturizers (as well as compost, etc.) can improve nutrient availability by
boosting cation exchange or promoting the proliferation of microbes, which in
turn raises the availability of certain plant nutrients. Organic fertilizers
such as composts and manures can be distributed locally without going through
the production process, making accurate tracking of actual consumption more
challenging.
2.2 HUMAN EXCRETA
According to
research, (Niwagaba C.B., 2009) on (Treatment Technologies for Human Feces and
Urine): Feces and urine, which make up human
excreta, are waste products of biological metabolism. The aesthetic, physical,
and chemical characteristics of urine and feces vary depending on the health of
the person excreting the waste, as well as the amount and type of food and
fluids eaten (Lentner et al., 1981; Feachem et al., 1983). Material that passes
through the intestines undigested is combined with material absorbed from the
bloodstream or shed from glands and the intestines (Guyton, 1992), mucus, and
bile, giving feces their unique brown hue (Featherstone, 1999). Feces include large
amounts of dangerous viruses, bacteria, protozoa cysts, and helminth eggs
(Faechem et al., 1983; WHO, 2006). Urine is the blood's excreta portion, which
is filtered by the kidneys (Guyton, 1992). Because the body uses urine to
balance liquids and salts, the amount of urine excreted by an individual varies
(Jönsson et al., 2004). Water makes up 93-96 percent of urine (Vinners et al.,
2006), with high amounts of water-soluble plant nutrients (Jönsson et al.,
2004).
2.2.1 Generation rate
The volume of feces produced by an individual is determined by the type of food ingested. Foods that are low in fiber, such as meat, produce less feces (both in terms of mass and volume) (Guyton,1992). Feces output in affluent countries ranges from 80 to 140 g/p,d (wet weight), equivalent to 25 to 40 g/p,d dry matter (Lentner et al., 1981; Feachem et al., 1983; Jönsson et al., 2005; Vinners et al., 2006). The average fecal excretion rate in developing countries is 350 g/pd in rural areas and 250 g/pd in urban areas (Feachem et al., 1983). In China, Gao et al. (2002) reported 315 g/p,d, while Pieper (1987) found 520 g/p,d. Schouw et al. (2002) determined that the wet feces generation rates of 15 people in three different areas of Southern Thailand ranged from 120 to 400 g/p,d. One stool per person per day is the normal rate of feces excretion, but it can range from one stool per week to five stools per day (Lentner et al., 1981; Feachem et al., 1983).
The
amount of urine excreted is determined by how well a person drinks and sweats,
as well as other factors like nutrition, physical action, and weather (Lentner
et al., 1981; Feachem et al., 1983). Excessive sweating produces concentrated
urine, whereas excessive liquid ingestion dilutes the pee. The average adult's
urine production rate is between 1000 and 1300 g/p,d (Feachem et al., 1983).
Based on observations in Sweden, Vinners et al. (2006) proposed a design value
for pee generation of 1500 g/p,d, while Schouw et al. (2002) discovered that
600-1200 g/p,d of urine was excreted in Southern Thailand. Rossi et al. (2009)
reported a urine generation rate of 637 g/p,d on working days and 922 g/p,d on
weekends based on measurements in Switzerland, which is consistent with Jönsson
et al. (1999) who reported 610-1090 g/p,d based on measurements in Sweden.
2.2.2 Nutrients in excreta
The nutrients in feces
are derived from the food that has been consumed. (Berger, 1960; Lentner et
al., 1981; Guyton, 1992; Vinners et al., 2006) estimate that 10-20% nitrogen
(N), 20-50% phosphorus (P), and 10-20% potassium (K) are transferred to the
fecal fraction in proportions of 10-20% N, 20-50% P, and 10-20% K. (K).
Ammonia, which is biochemically degraded from proteins, peptides, and amino
acids, accounts for 20% of fecal nitrogen, while live bacteria account for 17%,
and the rest is organic nitrogen mixed in with substances like uric acid and
enzymes (Lentner et al., 1981). (Jönsson et al., 2005; Vinners et al., 2006)
found that feces in Sweden contain an average of 550 grams of nitrogen, 183
grams of potassium, and 365 grams of potassium per person and year. Among the
waste and wastewater portions, urine contains the largest concentration of
plant nutrients (Figure 4). Plant nutrients evacuated by urine have been
measured at 2.5-4.3 kilogram N, 0.4-1.0 kg P, and 0.9-1.0 kg K per person and
year (Lentner et al., 1981; Vinners et al., 2006).
Figure 2.1: Proportions of nutrients found in household wastewater fractions and biowaste in Sweden. Source: Jönsson et al., 2005.
Jönsson et al. (2005)
and Vinners et al. (2006) looked at previous urine nutritional content studies
and found that the annual excretion rate per person in Sweden is roughly 4000g
N, 330-365 g P, and 1000 g K. In Sweden, 4500-4600 g N, 500-550 g P, and 1400 g
K are discovered in urine and feces per year (Jönsson et al., 2005; Vinners et
al., 2006). Based on FAO food supply figures, Jönsson and Vinners (2004)
calculated the amount of nutrients in Ugandan excreta to be 2500 g N and 400 g
per person per year.
2.2.3 Pathogens in excreta
A healthy person's
feces include a significant number of bacteria from a variety of non-pathogenic
species, referred to as normal intestinal microbiota. Pathogenic bacteria in
the gastrointestinal tract are not found in the normal microbiota of the
intestine (Feachem et al., 1983). Their presence in feces indicates infection
in the population that contributed to the analyzed feces. However, some
commensal bacteria, also known as normal gut microbiota, might cause disease on
rare occasions. This scenario is more likely to occur when a person's immune
system has been impaired, such as during illness or old age, allowing
opportunistic infections to flourish (Madigan and Martinko, 2006).
Many other intestinal
pathogenic or potentially pathogenic microorganisms enter a new host through
ingestion (dirt, water, food on fingers and lips, aerosols captured in the nose
and swallowed), inhalation (after inhalation of aerosol particles), or eye
(when eyes are rubbed with contaminated fingers) (Feachem et al., 1983). After
infecting the host, a large number of germs may be discharged. Depending on the
population's health, harmful bacteria, viruses, parasite protozoa, and
helminths may be detected in the feces of the population, and hence in the
mixed wastewater. In terms of hygiene, any contact with fresh/untreated
excrement offers a risk (Feachem et al., 1983; Schönning and Stenström, 2004;
WHO, 2006). Esrey et al. (1998) developed a disease transmission channel chart
that began with the letter F and ended with the letter F. As a result, it's
known as the F-diagram (Figure 2.2).
Figure 2.2: The F-diagram,
showing the faecal disease transmission routes to a new host and the possible sanitation barriers.
Adapted from Esrey et al.,
1998.
Bacteria of various
species are among the pathogens that can be found in feces (e.g. Aeromonas
spp., Campylobacter jejuni/coli, Shigella spp., pathogenic E.
coli, Pleisiomonas shigelloides, Vibrio cholerae and Yersinia spp.), Salmonella
typhi/paratyphi, Salmonella spp., viruses (e.g. Enteric
adenovirus 40 and 41, Hepatitis A virus, Hepatitis E virus, poliovirus and
rotavirus), parasitic protozoa (e.g. Entamoeba histolytica, Cryptosporidium
parvum, Giardia intestinalis) and helminths (e.g. Trichuris
trichiura (whipworm), Ancylostoma duodenale/Necator americanus
(hookworm), Schistosoma spp.
(blood flukes), Taenia
solium/saginata (tapeworm), and Ascaris lumbricoides (roundworm))
(Schönning and Stenström, 2004; WHO, 2006). Most fecal pathogens induce gastrointestinal
symptoms such diarrhoea, vomiting, and stomach cramps, but some can also cause
symptoms in other organs (Schöning and Stenström, 2004; WHO, 2006).
Few pathogens, such as Salmonella typhi, Schistosoma
haematobium, Leptospira interrogans, and Salmonella paratyphi, are found in
urine during infection (Feachem et al., 1983; WHO, 2006), while others, such as
Mycobacterium tuberculosis, are in urine during renal tuberculosis infection
(Feachem et al., 1983; WHO (Daher et al., 2007). Viruses including BK virus and
Simian virus 40 have also been found in the urine of children (Vanchiere et
al., 2005). Leptospira interogans is conveyed via diseased animals' urine, and
human urine transmission is uncommon (Feachem et al., 1983). Despite the fact
that Salmonella typhi and Salmonella paratyphi can be discharged in urine from
typhoid and paratyphoid patients after the bacteria have been disseminated by
blood, environmental transmission via urine is limited due to Salmonella
sppshortshort .'s survival time in urine (only a few hours) (WHO, 2006).
Feces were discovered
in 22% of the source-diverted urine samples tested in a Swedish examination.
Höglund et al. (2002) found an average of 9 mg of feces per litre of pee in the
contaminated samples. The urine must first be cleansed before it can be used as
a fertilizer.
2.3 TREATMENT OF URINE
2.3.1 Urine Storage and Treatment These studies investigated how dilution (and
hence ammonia content) and temperature affect organism inactivation, as well as
how solar exposure affects the rate of inactivation and the time required to
sanitize urine. Three urine dilutions and four storage temperatures were
studied in triplicate for seven months in the laboratory. The dilutions
(urine:water) ranged from undiluted urine (6.0 g NNH3/NH4 L-1)
to 1:1 to 1:3 (1.5 g NNH3/NH4 L-1) to represent urine
dilutions found in practice in sanitation systems, and the was carried out at 4, 14, 24, or 34 °C to
account ambient storage temperatures found around the world. At the above
dilutions and temperatures, the die-off of S. Typhimurium phage 28B, coliphage ɸx 174, Enterobacteriophage
MS2, Enterococcus faecalis (E. faecalis) and Salmonella Typhimurium (S. Typhimurium)
was investigated.
The
treatment of urine in 10 L plastic jerry cans was evaluated in the field for
three months in Kampala, Uganda, under three different ambient exposures:
totally in the sun (S), partly in the sun near a wall (W), and within a
ventilated room (R). Complementary research was conducted on urine in 50 mL
centrifuge tubes in a laboratory incubator adjusted to mimic a cyclic temperature
pattern comparable to that obtained from the field study's exposure to the sun.
The researches were motivated by the fact that the majority of the existing
literature focused on pathogen die-off in preserved urine at constant
temperature. However, in real-world modest treatment systems, such as jerry can
storage, the urine temperature varies during the day. The temperature of the
contents of exposed containers can be raised by direct sunshine. It's crucial
to know how many hours of direct sunshine are required to elevate the
temperature of urine in exposed containers. The monthly average daily relative
sunlight duration in Kampala is approximated to be between 0.31-0.62 hours,
equating to 3.7-7.4 hours (Mubiru and Banda, 2007; Mubiru et al., 2007), which is
consistent with the approximated 2-3 hours of bright sunlight per day during
the research (Mubiru and Banda, 2007; Mubiru et al., 2007). E. coli O157:H7,
Enterococcus spp., S. Typhimurium, and Ascaris suum eggs were researched in the
field. Instead of Enterococcus spp., E. faecalis was researched in the lab, and
the phages studied were included.
2.3.1.1 Dilution and temperature
The concentration of
ammonia in urine is affected by dilution. At 24 °C, the predicted
concentrations of uncharged ammonia (NH3) in 1:0, 1:1, and 1:3 urine:water
dilutions were 156 11, 60 4, and 24 6 mM, respectively (Paper IV). Organism
inactivation was slow and showed little dependence on ammonia concentration
below a concentration of approximately 40 mM of unionised ammonia (Figure 2.3).
Figure 2.3: Time (days) for one decimal reduction (t90)
plotted as a function of uncharged
ammonia for S. Typhimurium (●
), Enterococcus faecalis (○ ),
MS2 (■ ) and ɸ x 174 (□ ) and S. Typhimurium phage 28 B (× ) in
urine stored at temperatures a) 34, b) 24,
c) 14 and d) 4 °C. The correlation trend is indicated with thin lines for
the bacteria (Enterococcus faecalis broken line) and with bold lines for the
phages (ɸ x 174 broken).
pH was only marginally
influenced by the rate of dilution investigated, making single inactivation
effects owing to pH difficult to separate. The pH values match up favorably to
those obtained from Ugandan urine. After spiking with the organisms, the
average pH of the collected urine decreased slightly to 8.8. The lower the pH
changes between the temperatures, the less diluted the urine is. At 4 and 14
°C, the pH of concentrated urine (1:0) was 9.1; at 24 and 34 °C, it was 9.0. At
4 and 14 °C, the pH of diluted urine was 8.8, 8.7-8.8 at 24 °C, and 8.8 at 34
°C. At 4 °C, the pH of diluted urine was 9.1, 8.9 at 14 °C, and 8.7 at both 24
and 34 °C. Even when free ammonia was 50 mM, the reduction in E. faecalis and
phages (MS2, ɸx, and 28B) was slow at 4 and 14 °C, as seen by significant t90
values (Table 2.1), and the inactivation rate was less linked with free ammonia
concentration. To sanitize urine stored at 4-14 °C, lengthy retention times of
up to 6 months are required (Schönning and Stenström, 2004; WHO, 2006).
Table 2.1: Decimal reduction (t90) in days ±
S.D(%) for the bacteria S. Typhimurium, E. faecalis, MS2, ɸ x 174 and phage 28B
at different temperatures and urine concentrations.
NR = no reduction detected during 182 days, except for the temperature
control (0:1) which was studied during 40 days.
The death of S.
Typhimurium occurs at 24 °C. According to the t90 values in Table
2.1, its die off was rapid regardless of the dilution. E. faecalis t90
values rose dramatically (by around 20 times) from pure urine through 1:1 to 1:3
dilutions (Table 2.1). Only in unadulterated urine did the t90
values for MS2, ɸx, and 28B differ slightly, and they all climbed to t90
values around 5 to 6 times as long with 1:3 dilution (Table 2.1; Figure 2.3).
The reduction rates of
all species studied at 34 °C exhibited a linear relationship with NH3.
S. Typhimurium and E. faecalis were decreased to less discovery limits between
a day and three days, respectively, at this temperature, resulting in extremely
short t90 values (Table 2.1). This data, along with the decrease in
apparently stable phages with t90 of 2 days to 2 weeks (Table 2.1),
suggests that urine should not be stored at 34 °C for more than 2 months, even
if it is used to fertilize lettuce. At 34 °C and with urine diluted 1:0, 1:1,
and 1:3, no live Ascaris suum eggs were identified on days 7, 8, and 10, with
440 to 1,446 eggs seen on each day (Nordin et al., 2009a). Chandran et al.
(2009) recommended that undiluted urine held for roughly 1 week at 30 C should
be safe for use as a crop fertiliser based on E. coli, S. Typhimurium, and MS2
studies.
For every 10 degrees
Celsius increase in temperature, biological activity is projected to double
(Madigan and Martinko, 2006). The rate of ammonia permeability entering a cell
is affected by temperature, with low permeability at low temperatures (Jenkins
et al., 1998).
When the concentration
of free ammonia in urine is above 40 mM, e.g. 2.8 g NNH3/NH4 L-1
and pH 8.8, low or no numbers of organisms remain after just brief storage
times at 24oC, according to Figure 2.3 and the short t90
values (Table 2.1). A slightly lower ammonia concentration would result in the
same concentration of unionised ammonia at a higher pH or temperature (NH3).
At 34°C, all dilutions, as well as 1:0 and 1:1 at 24°C, exceeded the
sterilising concentration of approximately 40mM of free ammonia, below which
almost all organisms demonstrated a much longer life span according to t90
values (Figure 2.3), whereas only the undiluted urine (1:0) reached this
dilution at 4 and 14°C. As a result, urine is sanitized by a combination of
warmth and free ammonia.
2.3.1.2 Microbial Inactivation
When the urine was
diluted, the t90 values for E. faecalis were higher than those for
S. Typhimurium (Table 2.1). The reduction in S. Typhimurium was not highly
associated to the various urine dilutions examined, as t90 was
unaffected by the 1:1 and 1:3 dilutions and was only 6.5 days at most (Table
2.1). At 34 °C, regardless of urine content, E. faecalis was rapidly reduced,
however at lower temperatures, undiluted urine had a substantially shorter t90
than diluted urine (Table 2.1). At all temperatures, the t90 of undiluted urine
was less than 7 days, whereas the t90 of 1:3 dilution was 33 days at
4°C. During the 40 days of study, only a tiny decline was discovered in the
temperature controls at 34°C, and the reduction was slight at 24°C and below
(Table 2.1). E. coli O157:H7
was shown to be more susceptible to ammonia than S. Typhimurium when tested in
a 1:1 urine:water dilution at 4 and 34 °C. According to Mendez et al. (2004),
the outcome of ammonia treatment of S. Typhimurium and E. coli 0157:H7 are
consistent. The lowest NH3 concentration examined was 15 mM, which
corresponds with Park and Diez-Gonzalez (2003), who found that 5 mMNH3
was the lowest inhibitory concentration for S. E. coli and Typhimurium In a
broth solution, there are E. coli. As a result of this, E. S. coli and E. coli
Typhimurium appears to be particularly sensitive to uncharged ammonia, and will
always be killed off quickly, even at levels lower than those commonly
encountered in source separating sewage systems. E. S. coli and E. coli in
urine collected and retained from these systems for short periods of time (days
to weeks), especially at temperatures over 20°C, Typhimurium should not be a
concern.
Figure 2.4: Log concentration (pfu mL-1) of MS2, studied in triplicate, as a function of time (days) in urine diluted 1:1 at 34 °C.
MS2 and ɸx 174
reduction kinetics diverged from first order kinetics, with an initial fast
decrease followed by a breakpoint, followed by a slower decline. The reduction
in MS2 phage in urine diluted 1:1 and held at 34°C demonstrates this (Figure
2.4). The ostensibly initial quick reduction phase was left out of the fitting
since it would have exaggerated sanitation effectiveness and was explained by
artefacts like urine particle adhesion.
Chandran et al. (2009)
found a rapid drop of MS2 in urine held at 30°C and 15°C (within 1 week), which
differs significantly from the model depicted in Figure 2.4. Their urine was
not diluted and was maintained in locked containers for 6 months before to
their experiments, resulting in a high ammonia/ammonium content of 8.57 g L-1.
Chandran et al. (2009) found that the ammonium concentration in urine was
roughly twice that previously measured, and that storing it at 30°C resulted in
significant quantities of aqueous ammonia, which is the most likely reason for
the pee's quick cleanliness.
The t90 for
ɸx 174 and MS2 at 4°C and 14°C ranged from 28 to 240 days, with little link to
urine dilution and no difference in sensitivity between the two phages. At 4
and 14°C, S. Typhimurium phage 28B showed little or no decrease. Höglund et al.
(2002) found very little decline in S. Typhimurium phage 28B at 5°C after 200
days, which corresponds with our findings. Höglund et al. (2002) found that
rhesus rotavirus had a significantly shorter inactivation period (T90
= 35 days) than S. Typhimurium phage (T90 = 71 days). Studies of the
ammonia sensitivity of coated viruses, such as Avian influenza, show that
coated viruses reduce ammonia levels significantly faster than phages
previously used (Emmoth et al., 2007). As a result, pathogenic viruses appear
to be more susceptible to ammonia treatments than the phages investigated,
providing a buffer when urine is treated.
2.3.2 Urine storage at varying temperatures
2.3.2.1 Organism Inactivation
In a field research in
Uganda, neither Salmonella spp. nor E. coli were discovered in large amounts in
fresh urine, although Enterococcus spp. were (106 cfu mL-1 urine).
The starting concentration of all organisms tested was 105-108 cfu mL-1
urine after spiking. After 24 hours of urine exposure at any of the three
exposure locations, S. Typhimurium and E. coli were inactivated and
undetectable (sun, wall and room). E. coli and S. Typhimurium were decreased
from 6log10 to non detectable amounts (10 cfu mL-1 urine) in just 11
and 14 hours, respectively, in a separate laboratory research.
Enterococcus spp. were far more resistant than the other bacteria
studied, and they were discovered in the field research until day 37, but at
concentrations close to the discovery limit (10 cfu mL-1), with
nearly identical t90 values for all locations (S, W and R; Table
2.2). In a separate experiment, Enterococcus spp. reached non-detectable levels
on day 6 (t90 = 1.8 days). In the complementing investigations, the
inactivation rate for Enterococcus spp. was more than four times higher than in
the field study (Table 2.2). MS2 was the most sensitive of the three phages
investigated, and on day 22, it was close to the discovery limit (1 cfu mL-1
urine). With t90 values of 37 and 55 days, respectively, the ɸX and
S. Typhimurium phage 28B, which were sampled for 42 and 48 days, respectively,
expressed slower inactivation (Table 2.2).
Table 2.2: Reduction coefficients with standard error,
k±SE (log10 cfu/pfu d-1) for the linear regression of exponential
inactivation of the organisms studied. Time for 1log10 reduction (t90)
is given as mean/upper 95% confidence interval in days.
At day 42 of the field
investigation, the viability of the Ascaris suum eggs in the sun site was 1%,
whereas the viability in the wall and room locations was 4±1% and 40±5%,
respectively (Figure 2.5) When compared to the initial viability, the NaCl
end-controls from days 40 to 42 exhibited no significant loss.
A lag phase with no
inactivation or even higher viability than the initial was reported in the
supplementary study until day 15. A lower inactivation rate was found starting
on day 24, when the viability had dropped to 12%, (Figure 2.5). There were no
viable eggs on day 40, (Figure 2.5). The best fit for the sun location for an
equation giving the die-off for a lag duration of 18.5 days and a T90
of 27.6 days was used to fit lag phase models for shouldered survival curves of
Ascaris suum (Table 2.2).
Figure 2.5: Viability of Ascaris suum eggs (% of initial viability) incubated in urine in 10 L jerry cans exposed to sun (●), wall (×) and room (□ ) location
The lag phase was less
pronounced at the wall and room locations, therefore a simple exponential
inactivation equation was adopted (Table 8), albeit linear regressions fit
almost equally well due to the few data points and large variation between
repetitions.
2.4 TREATMENT OF FAECES
Fresh feces should always be treated
with caution due to the possibility of high pathogen concentrations (Feachem et
al., 1983; WHO, 2006). As a result, feces should be sanitized at all times.
Storage, composting, burning, and chemical treatment are examples of treatment
and sanitation methods.
2.4.1 Storage
The number of
microorganisms (including pathogens) in feces should decrease after removal due
to natural die-off. This is especially true because enteric bacteria and
pathogens (as well as faecal markers) are accustomed to body temperature and a
little above, and thus are thought to grow best at 37 to 44 ℃. Certain bacteria, such as Salmonella, and some indicator
organisms, such as E. coli, will grow in their storage medium/environment if
conditions suitable to their growth are kept. The number of E. coli and
Enterococcus spp. may increase (Schönning and Stenström, 2004; WHO, 2006). Pathogen
counts are affected by pH, moisture, temperature, nutrition, oxygen, ammonia
content, and UV exposure during storage (Peasey 2000; Schönning and Stenström,
2004; WHO, 2006; Wichuk and McCartney, 2007; Austin and Cloete, 2008; Winker et
al., 2009).
In areas where the
ambient temperature reaches 20 degrees Celsius, a total storage time of 1.5 to
2 years (including time spent storing during primary treatment, i.e. under the
toilet vault) will remove most bacterial pathogens and greatly reduce viruses,
protozoa, and parasites (Schönning and Stenström, 2004; WHO, 2006),because
pathogens die quicker at higher temperatures (up to 35 °C), a one-year total
storage duration will achieve the same result in regions with higher ambient
temperatures (Schönning and Stenström, 2004; WHO, 2006). This is consistent
with Strauss and Blumenthal (1990), who claimed that under tropical
circumstances (28-30 °C), one year was adequate for inactivation of diverse
types of faecal pathogens, whereas at lower temperatures (17-20 °C), 18 months
would be required. At 22-37 °C, however, Ascaris has been found to have a
prolonged survival period of 2-3 years (Moe and Izurieta, 2004). Enterococcus
spp. were not reduced after 50 days of storage at 20 °C, while Salmonella spp.
were not reduced at 4 °C, according to Vinners et al. (2007). As a result, at
low temperatures, extensive storage times are required to provide adequate
faecal sanitation.
2.4.2 Composting
Composting is the
microbial biological decomposition of organic waste into a humus-like stable
product in an aerobic, moist, and self-heating environment. Composting is often
used to recycle potentially biodegradable trash, sterilize potentially
pathogen-contaminated materials, and bioremediate toxic waste (Haug, 1993). A
well-run and managed thermophilic compost process generates a product free of
pathogens and plant seeds that may be applied to land to give nutrients, humus,
and organic matter for soil improvement (Epstein, 1997; Arvanitoyannis et al.,
2006; Arvanitoyannis and Kassaveti, 2007).
When a
well-conditioned substrate (enough energy, nutrients, moisture, structure,
etc.) is composted, aerobic breakdown of organics occurs. Exothermic denotes
that the process generates heat and raises the temperature. The heat generated
either remains in the compost mass, exits by conduction, convection, and
radiation, or is lost as a byproduct of the exiting gas. Enough heat should be
retained in the compost matrix to keep the material in the composting process
hot enough for sanitation. This demands a well insulated compost, at least on a
small and medium scale. The outer sections of large compost piles act as
insulators for the inside parts of the pile, resulting in a temperature
gradient within the pile, with the highest temperature in the interior (Finger
et al., 1976).
Microorganisms perform
organic degradation, which is a biological process. Elements that affect
microbial development have an impact on the composting process. Moisture,
oxygen, pH, temperature, and the C/N ratio are all factors affecting substrate
composition (Miller, 1993; Haug, 1993).
Moisture: Moisture in the compost substrate provides a pathway for dissolved
nutrients to be transported to microorganisms for metabolic and physiological
processes (McCartney and Tingley, 1998). In a liquid environment with 100 percent MC
(Finger et al., 1976), the highest rate of transfer of nutrients and waste
products occurs, but controlling aerobic composting systems in these conditions
becomes problematic. The ideal moisture for efficient composting of various
forms of garbage was 25-80 percent (Ahn et al., 2008) and 50-60 percent (Tiquia
et al., 1998), according to Suler and Finstein (1977); Bishop and Godfrey
(1983); McKinley and Vestal (1984); Tiquia et al., 1998). (Suler and Finstein,
1977; Bishop and Godfrey, 1983; McKinley and Vestal, 1984; Tiquia et al.,
1998). The wide range of
ideal moisture content observed reflects the differing structural properties of
the various substrates undergoing composting. Wood chips, for example, can
compost at high moisture levels, whereas poorly structured substrates, such as
food waste, require lower moisture levels. At low beginning moisture (e.g.,
25%), early drying of the compost material happens readily, halting the
biological process and resulting in physically stable but biologically unstable
composts (Liang et al., 2003). (de Bertoldi and colleagues, 1983). Waterlogging can induce anaerobic conditions
in most substrates, preventing aerobic compost breakdown and creating acid
production and odor concerns (Schulze, 1962; Tiquia et al., 1996). (Schulze,
1962; Tiquia et al., 1996).
Oxygen: To function properly,
microorganisms engaged in aerobic composting of substrate organic matter
require oxygen. Composts can be oxygenated through mechanical aeration,
convective air flow (passive aeration), diffusion, and manual stirring
(Epstein, 1997). Regardless of the method used for oxygen supply, oxygen
diffusion in the aqueous layer around the substrates and into the pores of the
substrate is crucial during composting. The barrier to oxygen diffusion in the
compost matrix causes an oxygen gradient throughout the pile, with the lowest
oxygen concentrations in the interior (Finger, 1976).
pH: The early phases of the composting process cause pH to drop due to the
formation of organic acids, which are created by the fermentation of easily
degradable organic matter (Beck-Friis et al., 2003). Organic acids interfere
with microbial life processes when they are in their undissociated condition,
that is, when the pH is low (Sundberg, 2005). During the initial phase of
composting, organic acids tend to lower pH, but the carbonic and ammonia
systems, depending on the substrate, balance the pH drop to varying degrees of
efficacy (Sundberg, 2003). As the acids are used and ammonium is produced later in the
process, the pH rises to roughly 7.5-8.5 (Beck-Friis et al., 2003). (Beck-Friis
et al., 2003; Jeris and Regan, 1973). Most bacteria are unable to survive at pH
3 or lower, and they begin to die at pH 10.5 and above, with substantial
mortality occurring at pH 11.5, (Haug, 1993).
Temperature: Due to microbial metabolism, the temperature rises as the composting
process advances. The temperature increase inside composting materials is
influenced by the initial temperature, biological heat evolution, and heat
conservation (Miller, 1993). Based on temperature development, the composting
process can be divided into three basic phases: mesophilic, thermophilic, and
curing. During the mesophilic phase, temperatures reach roughly 40 degrees
Celsius. The transition from mesophilic to thermophilic happens about 40-45 °C.
The thermophilic phase is defined by temperatures ranging from 45 °C to 70 °C,
and sometimes even higher (Miller, 1996), while the curing phase is defined by
temperatures below 40-45 °C (Chiumenti et al., 2005). Thermal sanitation occurs
during the thermophilic phase.
Temperature affects
the rate of decomposition, which can be described as the rate of carbon dioxide
evolution. Temperatures below 20 degrees Celsius have been demonstrated to
hinder or impede composting (Mosher and Anderson, 1977). Depending on the type
of substrate composted, the temperature at which maximal decomposition occurs
is predicted to be between 50 and 67 degrees Celsius (Suler and Finstein, 1977;
Haug, 1993; Miller, 1993; Richard and Walker, 1999; Eklind et al., 2007). Pathogen
inactivation is achieved, according to Schönning and Stenström (2004) and WHO,
when temperatures above 50 °C are maintained for at least one week (2006). The
larger the temperature margin above 50 °C and the longer this temperature is
maintained, the stronger the sanitation impact. High temperatures cause protein
denaturation, which leads to cell death (Madigan and Martinko, 2006).
The temperature in the
center of a composting heap is usually higher than at the edges (Haug, 1993).
Insulation should be employed to prevent heat loss in order to attain and
maintain high temperatures throughout the pile (Karlsson and Larsson, 2000;
Björklund, 2002; Vinners et al., 2003a). Insulation is also necessary while
composting in tiny heaps in tropical climes (Karlsson and Larsson, 2000). Even
with insulation, low temperatures will exist in some locations of the compost,
such as at the air inlet. To subject the material to high temperatures in such
cold climates, the compost must be well mixed on a regular basis (Epstein,
1997; Vinners et al., 2003a).
C:N ratio: One of the criteria
that impacts the composting process and quality is the C:N ratio (de Bertoldi
et al., 1983; Michel et al., 1996). When microorganisms are growing, they
require digestible carbon for energy and nitrogen for cell formation (Epstein,
1997). During aerobic metabolism, microbes need around 15 to 30 parts C for
every part N. (Haug, 1993). At C/N ratios of 15 to 30, nitrogen is present in
sufficient proportions for cell synthesis, therefore no rate limit should be
implemented (Haug, 1993). If the C/N ratio is more than 35 in the start, the
bacteria will have to go through numerous lifecycles to oxidize the excess
carbon until they reach the C/N ratio that is best for their metabolism (de
Bertoldi et al., 1983). When composting substrates with low C/N ratios, excess
nitrogen is lost by ammonia volatilisation, which is exacerbated at high pH and
temperature (de Bertoldi et al., 1983; Eklind et al., 2007). When nitrogen is
released as ammonia or nitrous oxide, it diminishes the usefulness of compost
as a fertilizer and pollutes the air.
2.4.2.1 Moisture and pH
Substrates with an initial
moisture content of 37-57 percent self-heated swiftly to sterilizing
temperatures, reaching >65 °C in just two days, but those with a moisture
level of more than 63 percent self-heated slowly or not at all. This shows that
starting the composting process somewhat drier and adding water as needed is
preferable to starting with a high moisture level that could hinder the
process. A moisture content of 40-60% is recommended for composting operations
(Golueke, 1977, cit. Epstein, 1997; Haug, 1993; Chiumenti et al., 2005). Composting
appears to be impeded beyond a moisture content breakpoint of 60-65 percent in
the faeces/ash and food waste substrate, restricting the temperature increase. When
substrates with an initial moisture content of >63 percent were composted,
the moisture content remained high, resulting in evident water-logging. In
fact, the mixtures dissolved into wet pastes. Spreading the combinations on a
polyethylene sheet and drying them in the open air to roughly 50-60% moisture
content did not cause them to heat up since they had lost their structure.
According to Golueke, moisture content greater than 60% in composts impacts
particle aggregation and air-filled porosity, which inhibits oxygen transfer
throughout the composting process (1977, cit. Epstein, 1997).
Moisture affects pH;
in one experiment, with a moisture content of 63 percent and a low pH,
self-heating took 37 days to achieve 65 degrees Celsius. As seen in Figure 2.6,
there appears to be a relationship between moisture and pH, with materials with
a high initial moisture content (>65%) exhibiting low pH after composting. This
is in line with other researchers' findings, and it's most likely the result of
organic acid generation and buildup in anaerobic conditions (Sundberg et al.,
2004; Nakasaki et al., 2009). Organic acids restrict microbial activity and
development at low pH. (Sundberg et al., 2004). In the high-moisture-content
experimental runs, this could have repressed microbial activity, preventing
temperature rise even after sun-drying. The production of the cakes, as well as
their lack of structure, may have hindered the composting process.
Figure 2.6: Minimum pH during
composting plotted against the initial moisture
content of the substrates.
The larger the amount
of faeces/ash mixture, the higher the initial pH of the substrates. Materials
with a pH of at least 6.9 (and up to 9.3) composted well, achieving
thermophilic and sanitizing temperatures from the beginning or later.
Thermophilic temperatures could not be reached by materials having a pH of less
than 6. There appears to be a pH breakpoint between 6 and 7 below which
thermophilic composting of substrates/materials is impeded, and above which the
composting process proceeds easily, with thermophilic and sanitizing
temperatures achieved. This is supported by Haug (1993), Epstein (1997), and
Sundberg (2001). (2005). The quick rise in temperature in substrates with pH as
high as 9.8 implies that the composting process can continue at this pH.
2.4.2.2 Substrate conditioning for moisture and energy
The ability of the
compost to reach sterilizing temperatures is determined by feed conditioning.
Co-composting with food waste or other organic waste may be necessary since a
feces/ash mixture may not contain enough organics to maintain sterilizing
temperatures (>50oC) for a long enough duration (at least one
week) to achieve sanitation. Haug (1993) developed a set of guidelines for
determining whether the energy content of a material is sufficient for thermal
composting. Because water evaporation consumes the most energy in composting,
the ratio of water to the mass of biological volatile matter (W) can be used to
determine whether enough energy is available to heat and evaporate the water.
The ratio W is calculated using Equation 1 according to Haug (1993).
W =
………………………………………………..Equation (1)
Where kS
denotes the percentage of the substrate volatile solids that can be composted;
Vs denotes the volatile solids content of the dry solids; Ss denotes the
fractional solids (dry matter) content of the substrates; and Xs denotes the
wet weight of the feed substrate.
To see if the compost
substrate has enough energy to raise the temperature and evaporate the water,
the computed W is compared to the recommended literature value of W8. When
W>10, there is usually insufficient energy to raise the temperature and evaporate
enough water. Equation 2 is also used to calculate another important statistic,
the energy ratio (E) (Haug, 1993).
E =
…………………………………………………….…..….Equation (2)
Hs denotes the amount
of heat released per gram of biodegraded volatile solids. Haug, (1993)
calculates Hs = 23.24 MJ g-1 deteriorated Vs (5550 cal g-1
degraded Vs). Composts with E>700, on the other hand, theoretically have
enough energy for composting and drying, whereas composts with E˂600 do not
(Haug, 1993).
Haug (1993) gives a
rule of thumb for how much water a compost can store while remaining thermophilic.
The thermodynamic conditions for temperature elevation and water evaporation
during thermophilic composting are not met if the energy ratio, E (Calculated
according to Eqn. 1), is less than 600 cal g-1 and the water ratio,
W (Calculated according to Eq. 2), is greater than 10. The calculated E and W
values for all of the composts are presented in Figure 2.7, demonstrating that
the E and W rule of thumb agrees well with the data. Except for one, all
well-functioning composts had E>600 cal g-1 and W˂10. The
exception is the W1:0 compost in Experiment 2, which had E=500 cal g-1,
close to 600 cal g-1, while its W was 11, i.e. just over 10
(Figure 2.7). This demonstrates the validity of the basic rule of thumb that E
and W are important indicators of compost performance.
Figure 2.7: Theoretical energy ratio, E (cal g-1)
versus water ratio, W. Dotted lines are limit
values for non-functional composts (Haug, 1993).
2.4.3 Incineration
Incineration of feces
is a treatment method that eliminates germs while also being a compact and
quick operation that allows for rapid inactivation. Furthermore, the amount of
material left diminishes until all that is left is ashes. There is little need
for extra disposal because the ashes can be reused as cover material during the
collecting process in UDD toilets. As a result, the issue of providing cover
material for the collecting phase, which is common, can be addressed.
The temperature is
raised to such a high level during incineration that any germs present should
be rendered inactive after only a few minutes of exposure. Low-cost small-scale
incinerators made of steel sheets have been promoted by international
organisations, mostly for the disposal of healthcare waste. In most of these
circumstances, incinerators are used to eliminate potential health risks
associated with sharps scavenging, as well as the risk of disease transmission
such as hepatitis and HIV/AIDS (WHO, 2004b).
Incinerating materials
that contain inorganic or organic chlorides yields more dioxins than
non-chloride materials (Shibamoto et al., 2007). Temperatures above 450 °C
result in the synthesis of dioxin, which is considerably reduced at
temperatures above 850 °C (Shibamoto et al., 2007). This is in accordance with
EU directives (89/429/EEC, discussed in Nasserzadeh et al. (1995)), which
stipulate that air pollution is reduced when the combustion chamber temperature
reaches at least 850 °C and the gases are exposed to this temperature for at
least two seconds in the presence of at least 6% oxygen.
90-100 percent losses
of N, S, and C (Partridge and Hodgkinson, 1977; Heard et al., 2000) and 24
percent losses of P, 35 percent losses of K, and 75 percent losses of S
(Partridge and Hodgkinson, 1977; Heard et al., 2000) have been reported, as
well as 24 percent losses of P, 35 percent losses of K, and 75 percent losses
of S (Partridge and Hodgkinson, 1977; He (Heard et al., 2000). According to
Jönsson et al. (2004), excrement incineration ash has high levels of P and K
and can be utilized to fertilize soil for agricultural purposes, just like
plant ash.
2.4.4 Chemical treatment
To treat feces for
pathogen reduction, acids (e.g. phosphoric acid), bases (e.g. ammonia and
lime), and oxidizing agents can all be utilized (e.g. chlorine). Agronomically
beneficial molecules can be found in disinfection chemicals such Ca(OH)2,
NH3, KOH, and PO43-. These disinfectants are
favored for substrates that will be recycled as fertilizers since the
disinfectant's nutritional content increases the product's fertiliser value
(Winker et al., 2009; Vinners et al., 2009).
For faecal matter
sanitation (Vinners et al., 2003b; Nordin et al., 2009a,b; Vinners et al.,
2009), as well as manure sanitation (Vinners et al., 2009), urea has been
examined (Vinners et al., 2009). (Ottoson and colleagues, 2008). Ammonia, which
is formed by enzymatic breakdown and results in uncharged ammonia, is used as a
disinfectant in urea treatment systems. The pH rises as urea degrades, and when
pH>9 is achieved, the majority of the ammonium/ammonia is uncharged ammonia,
leading in even more bacterial cell disinfection due to ammonia toxicity
(Warren, 1962; Pecson et al., 2007). Urea at a dose of 30 g ammonia nitrogen
per kilogram of feces (3 percent ammonia nitrogen) is sufficient to make the
material generally harmless after two months at 20 °C (Vinners et al., 2003b).
In the study by Vinners et al., adding urea to feces resulted in a pH rise of
roughly 9.3. (2003b). As a result, effective E. Escherichia coli (E. coli)
disinfection E. coli, Enterococcus spp. Salmonella spp. and other bacteria,
including E. coli. Within three weeks, there was a >6log10 drop in
chemical-resistant phage S, as well as a decrease in chemical-resistant phage
S. Typhimurium 28B, which translates to a 7.5-day decimal reduction or a 45-day
6log10 reduction.
At high pH, ammonia
inactivates bacteria (Warren, 1962; Nordin et al., 2009b), viruses (Cramer et
al., 1983; Pesaro et al., 1995; Nordin et al., 2009b), Cryptosporidium oocysts
(Jenkins et al., 1998), and Ascaris eggs (Ghiglietti et al., 1997; Pecson et al.,
2007; Nordin et al., 2009a). Nordin et al. (2009a) studied the inactivation of
Ascaris suum eggs in feces by ammonia at storage temperatures corresponding to
different ambient temperatures (4, 14, 24, and 24oC), and reported that
uncharged ammonia in concentrations of 60mM was effective in sanitizing feces. Ascaris
suum eggs were reduced by 6log10 after one month of storage at 34oC
and six months at 24oC. At 14oC or lower, inactivation of
Ascaris suum eggs was modest, with viable eggs after 6 months of storage at
60mM NH3. In 2 months at 14°C or 1 week at 24°C and 34°C,
respectively, treatment of feces from source-separating dry toilets with 1
percent urea achieves Salmonella reduction levels that meet the guidelines for
safe reuse of feces as fertilizer (i.e. 6log10 reduction) (Nordin et al.,
2009b). When 2 percent urea is added to S. Typhimurium phage 28B at 24 oC
and 34 oC, a safe fertiliser for unrestricted use is produced in 8
months and 1 month, respectively (Nordin et al., 2009b).
2.5
MULTIPLE BARRIER CONCEPTS FOR SAFE USE IN AGRICULTURE
Since
the 1990s, Sweden has been researching methods to make the safe reuse of pee
and feces in agriculture. In 2006, the World Health Organization (WHO) issued
guidelines on the safe reuse of wastewater, excreta, and greywater. The many
barriers to reuse notions have resulted in a comprehensive grasp of how excreta
can be reused properly. The notion is also utilized in food production and
water supply, and is commonly regarded as a set of treatment steps and other
safety precautions to avoid disease transmission. The amount
of treatment that excreta-based fertilizers need before they can be utilized
safely in agriculture is determined by a variety of factors. It all depends on
the additional obstacles that will be erected as part of the multiple barrier concepts.
Choosing the right crop, farming methods, fertilizer application methods,
education, and so on are examples of such barriers. In the case of
urine-diverting dry toilets (UDDTs), secondary treatment of dried feces can be
done at the community level rather than at the household level, and can include
thermophilic composting (where fecal material is composted at over 50 °C),
prolonged storage (1.5 to two years), chemical treatment with ammonia from
urine to inactivate pathogens, and solar sanitation.
2.6 COMPARISON TO OTHER FERTILIZERS
Excreta from humans has untapped fertilizing potential. The theoretical amounts of nutrients that can be extracted from human excreta in Africa, for example, are similar to all of the continent's current fertilizer consumption. As a result, reuse can assist enhance food output while also serving as a viable alternative to chemical fertilizers, which are often out of reach for small-scale farmers. Dietary consumption, on the other hand, has a significant impact on the nutritional value of human excreta.
Heavy metals can be found in mineral fertilizers, which are created from mining activities. Heavy metals such as cadmium and uranium are found in phosphate ores and can enter the food chain through mineral phosphate fertilizer. Excreta-based fertilizers are exempt from this, which is a benefit.
Animal manure is frequently not applied as precisely as mineral fertilizers in intensive agricultural land usage, resulting in low nitrogen consumption efficiency. Excessive usage of animal manure can be a concern in intensive agriculture areas with large numbers of livestock and little farmland.
Organic fertilizers'
fertilizing ingredients are typically bonded in carbonaceous reduced compounds.
The fertilizing minerals are adsorbed on the breakdown products (humic acids)
and other degradation products if they have previously been partially oxidized,
as in compost. As a result, they have a slower release and are usually less
quickly leached than mineral fertilizers.
2.7 BIOSOLIDS
According to studies by
(Gregory K. Evanylo, 2003) (Department of Crop and Soil Environmental Sciences,
Virginia Tech.):
2.7.1 History of Biosolids Biosolids are organic wastewater
solids that can be reused after sewage sludge treatment techniques such as
anaerobic digestion and composting have stabilized the sludge.
Alternatively, municipal rules may
define biosolids as wastewater solids that have completed a specific treatment
sequence and/or have pathogen and hazardous chemical concentrations that are
below prescribed levels. The Clean Water Act was revised as public concern
developed about the dumping of larger volumes of particles collected from
sewage during the sewage treatment prescribed by the Clean Water Act in the
United States. The Water Environment Federation (WEF) needed a new term to
distinguish the clean, agriculturally viable product produced by modern
wastewater treatment from earlier varieties of sewage sludge, which were
infamous for being unpleasant or toxic. Biosolids is credited to Dr. Bruce
Logan of the University of Arizona, who was awarded by the World Economic Forum
in 1991. The United States
Environmental Protection Agency (EPA) defines sewage sludge and biosolids as
follows in CFR Title 40, Part 503: Sewage sludge refers to solids separated
during the treatment of municipal wastewater (including domestic septage),
whereas biosolids refers to treated sewage sludge that meets EPA pollutant and
pathogen requirements. A similar name has been used in other countries, such as
Australia. It's possible that the term "biosolids" will be
regulated by the government. In informal usage, however, sewage or sewage
sludge refers to a wide spectrum of semi-solid organic substances. This could
include any solids, slime solids, or liquid slurry residue created during the
treatment of home sewage, as well as scum and particles eliminated during
primary, secondary, or advanced treatment operations. "Wastewater
solids" is another word for materials that do not match the regulation
definition of "biosolids."
2.7.2 Physiochemical Properties and Nutrient Level Of Biosolids
Biological,
chemical, and physical analyses can be used to establish a biosolid's
appropriateness for land application. The composition of biosolids is
determined by wastewater elements and treatment techniques. The qualities that
arise will influence the application technique and rate, as well as the level
of regulatory control that is required. Biosolids have a number of key
qualities, including:
• Total
solids: are made up of
suspended and dissolved solids and are usually stated as a percentage of total
solids in biosolids. Total solids concentration is determined by the kind of
wastewater treatment and biosolids treatment prior to land application. Liquid
(2-12 percent), dewatered (12-30 percent), and dry or composted solids are
typical solids compositions of various biosolids processes (50 percent).
• Volatile solids:
are usually represented as a percentage of total solids and offer an assessment
of the rapidly decomposable organic matter in biosolids. At land application
sites, volatile solids concentration is a key driver of potential odor issues.
To lower volatile solids concentration and hence the possibility for odor, a
variety of treatment procedures can be applied, including anaerobic digestion,
aerobic digestion, alkaline stabilization, and composting.
• Trace Elements: Biosolids include trace
elements in low amounts. Heavy metals are the trace elements that are of
particular importance in biosolids. Some of these trace elements (e.g., Cu, Mo,
and Zn) are nutrients required for plant growth at low quantities, but at large
concentrations, all of these elements can be hazardous to humans, animals, or
plants. The potential for phytotoxicity (i.e., plant harm) or a rise in the
concentration of potentially dangerous compounds in the food chain are two
potential risks linked with trace element accumulation in the soil. The
following nine trace elements have federal and state regulations: arsenic (As),
cadmium (Cd), copper (Cu), lead (Pb), mercury (Hg), molybdenum (Mo), nickel
(Ni), selenium (Se), and zinc (Zn) (Zn).
• pH and Calcium Carbonate
Equivalent (CCE): are both measures of a substance's acidity or alkalinity.
To lower pathogen concentration and attract disease-spreading organisms, the pH
of biosolids is frequently raised with alkaline materials (vectors). Most
infections are killed by high pH (higher than 11), and most metals' solubility,
biological availability, and mobility are reduced. Lime also causes the ammonia
(NH3) type of nitrogen to gasify (volatilize), lowering the
N-fertilizer value of biosolids. The relative liming effectiveness of biosolids
is represented as a percentage of the liming capability of calcium carbonate
(calcitic limestone).
Figure 2.8: A plot of pH against Time (weeks)
• Nutrients: These are the nutrients
necessary for plant growth that give biosolids their commercial significance.
N, P, K, calcium (Ca), magnesium (Mg), sodium (Na), S, B, Cu, Fe, Mn, Mo, and
Zn are among them. Biosolids concentrations vary widely, hence the actual material
being considered for land application should be examined.
• Organic chemicals: are complex
compounds that incorporate both natural and man-made substances. Industrial
waste, household items, and insecticides all include chemicals. Many of these
chemicals are hazardous or carcinogenic to organisms when exposed to critical
quantities for long periods of time, however the majority of them are found in
biosolids at such low levels that the U.S. They do not represent a major risk
to human health or the environment, according to the EPA. Despite the fact that
no organic contaminants are currently included in federal biosolids laws, the
National Research Council has advised that more research be done on a number of
specific organic substances (2002).
• Pathogens: microorganisms that cause
disease, such as bacteria, viruses, protozoa, and parasitic worms. If pathogens
are conveyed to food crops cultivated on land where biosolids are treated,
included in runoff to surface waters from land application locations, or
transported away from the site by vectors such as insects, rodents, and birds,
they can pose a public health risk. As a result, pathogen and vector attraction
reduction standards for biosolids applied to land are specified in federal and
state laws.
2.7.3 Nutrient levels in
Biosolids
Over the last 25 years, there have been very few comprehensive
surveys of nutrient levels in biosolids. (Stehouwer et al. 2000) conducted a
recent study that found that the macronutrient (N, P, and K) concentration of
biosolids has remained relatively constant from the late 1970s to the mid
1990s. Between 1993 and 1997, more than 240 samples were collected and examined
from 12 publicly owned treatment works (POTWs) in Pennsylvania, and the data in
Table 2.4 represents the means and variability of those samples. The POTWs each
produced a minimum of 20 analytical records between 1993 and 1997. The 12 POTWs
produced 110 to 60,500 tons of biosolids per year and processed them using
aerobic digestion (3 facilities), anaerobic digestion (4 facilities), or
alkaline addition (5 facilities).
Table 2.4: Means and variability of nutrient concentrationsa
in biosolids collected and analyzed in
Pennsylvania between 1993 and 1997 (Stehouwer et al., 2000).
|
Nutrient (%) |
Total N |
NH4-N |
Organic N |
Total P |
Total K |
|
Mean |
4.74 |
0.57 |
4.13 |
2.27 |
0.31 |
|
Variability |
1.08 |
0.30 |
1.03 |
0.89 |
0.27 |
Concentrations
are on a dried solids basis.
2.7.4 Benefits of Land Application of Biosolids
Biosolids
might be considered a waste or a beneficial soil enhancement. Rather than
landfilling or cremation, land application recycles soil-enhancing materials
such as plant fertilizers and organic debris. The delivery of nitrogen (N),
phosphorus (P), and lime (L) are the key advantages of fertilizers (where
lime-stabilized biosolids are applied). Sulfur (S), manganese (Mn), zinc (Zn),
copper (Cu), iron (Fe), molybdenum (Mo), and boron (B)] are vital plant
nutrients that are rarely acquired by farmers due to the unpredictability of
crop reactions to their application.
2.7.5 Production of Biosolids:
The
biological treatment of domestic wastewater is the primary source of biosolids
(Figure 2.9). Physical and chemical techniques are frequently used to improve
biosolids handling qualities, boost land application economic viability, and
lower the risk of public health, environmental, and nuisance issues connected
with land application practices. These techniques treat wastewater solids to
kill disease-causing organisms and minimize qualities that can attract rats,
flies, mosquitoes, or other disease-carrying species. The degree of pathogen
reduction achieved and the possibility for odor creation will be influenced by
the type and extent of wastewater treatment techniques used. Table 2.5
summarizes common treatment techniques and their implications on biosolids
characteristics and land application strategies.
Figure 2.9: Schematic diagram of wastewater treatment facility (G.K. Evanylo , 2003)
|
| |||||||||||||
Because biosolids application rates are modest, large land
expanses may be required for agricultural usage. Careful planning is required
for transportation and application timing that is compatible with agricultural
planting, harvesting, and possible bad weather conditions.
Tractor trucks carrying roughly 20 tons of biosolids are commonly
used to transport biosolids to the application location. This equates to about
3-5 dry tons per trailer at a solids concentration of 15-25 percent, or about
the amount of biosolids distributed on one acre of land for crops like corn,
soybeans, or wheat. As a result, there will be a significant amount of truck
traffic for huge sites of several hundred acres over the course of several
weeks. Increased traffic on local roads, odors, and dust are all potential
community consequences that should be addressed through public informational
briefings or public hearings. Biosolids transportation difficulties can be
minimized by devising delivery schedules that are least likely to cause
disruption.
Even when properly treated, biosolids will emit odors. Even in
rural communities accustomed to the use of animal manure, the odors may be
objectionable in unfavorable weather conditions. The stabilization process,
application method, storage type, climatological circumstances, and site
selection, as mentioned below, can all help to eliminate odors.
• Biosolids are
stabilized to reduce biological activity and odor. The scents produced by
aerobic digestion, heat treatment, and composting are generally the least
offensive. If not done correctly, anaerobic digestion has the potential to
produce greater odor than other treatment procedures. Similarly, if not
adequately stabilized and maintained, lime-stabilized biosolids, the most often
used material in the state, can produce odors.
• The manner of application has an impact on the odor potential at
the location. Immediate soil incorporation or direct soil injection will help
to avoid odor issues.
• Biosolids might be
stored at the treatment plant, at the application site, or in a temporary
facility. The preferred technique is to store the waste at the treatment plant
(if it is isolated from the public). Off-site storage necessitates careful site
selection and management in order to avoid odor issues.
• When
biosolids are applied to the surface, weather factors (such as temperature,
relative humidity, and wind) have an impact on odor severity. Spreading early
in the morning, when the air is warm and rising, will help to diffuse the odor
in the immediate area.
• The location of
the application is critical to the operation's success. The site should ideally
be situated away from residential areas. Despite
sufficient stabilizing techniques and favorable weather circumstances,
objectionable scents will occasionally be present. If nearby property owners
are subjected to chronic scents, expect complaints. A well-managed system with
the right equipment and stabilized biosolids will greatly limit the risk of
odors that are objectionable.
CHAPTER THREE
3.0
METHODOLOGY
3.1
PRODUCTION OF FERTILIZER FROM HUMAN EXCRETA
Biosolids (organic fertilizer) are produced primarily through
biological treatment of domestic wastewater.
According to studies by (G.K. Evanylo, 2003) as shown in figure 2.9,
the Primary Sedimentation tanks
are used to settle sludge while grease and oils rise to the surface and are
skimmed off. The settled sludge at the bottom of the tank moves to the digester
where the sludge is biologically stabilized by converting organic matter to
carbon dioxide, water and methane. The effluent (containing sludge) from the
primary sedimentation tank moves to the Aeration Tank where the sludge is acted
on by denitrifying bacteria. The bacteria convert nitrates to nitrites and
consume biodegradable soluble organic contaminants; (this process eliminates the
sludge odor). After treatment, the effluent move to the secondary sedimentation
tank where the excess sludge is separated and moves to the thickening unit
while the settled sludge is recycled back to the aeration tank. In the
thickening unit, a coagulant (polymer) is used to thicken the sludge then moved
to the digester where it is further treated before being dewatered; (removal of
its moisture content). The dewatered sludge (organic fertilizer) is collected
and can be use for agricultural purposes.
3.2 THEORETICAL BACKGROUND (relationship between variable parametric conditions)
The amount to which pathogens are inactivated and the maturity of the compost or organic fertilizer are determined by the chemical and physical variable conditions in the synthesis of fertilizer from human excreta. The variables are as follows:
♦Temperature ♦Time
♦Ammonia concentration
♦pH
♦Moisture content (MC)
To create a correlation, we must first identify all
of the variables that may influence it. Information on existing relationships
was acknowledged as a reference in modeling fertilizer production empirically
in a study conducted by Niwagaba (2009). The relationship between the
abovementioned criteria has been discovered in order to assess the rate at
which infections are inactivated as well as the substrate condition. The amount
of moisture in the compost has an impact on aerobic compost deterioration as
well as the pH. Pathogens are easily inactivated at a higher temperature for a
shorter period of time or at a lower temperature for a longer period of time
(according to literature, the higher the temperature beyond 50-55oC
(for feces) and 20, 24 or 30-34oC (for urine), the shorter the time
of inactivation, and vice versa). The links between these factors in achieving
pathogen inactivation and compost maturity are explored and simulated in order
to successfully model the creation of human excreta. Experiments on the
generation of organic fertilizer from human excreta provided the data for the
construction of models. The link between the above factors is used to create
equations (they are variables in the equations).
3.3 DEVELOPMENT OF MODELS
In this section
(section 3.3), some of the models were developed (eqns 3.3 and 3.4) while
others (eqns 3.1, 3.2, 3.5) and (eqn 3.6) were obtained from Kamalu, (2010) and Adeyemo, (20..) respectively.
3.3.1
Relationship between Time (days) for decimal reduction and
uncharged ammonia in urine stored at temperatures: 34OC, 24 OC,
14 OC and 4 OC as shown in Figure 2.3:
…………………………….. (3.1)
Where: ![]()
3.3.2
Relationship between Log concentration of MS2 (pathogen) and time
(days) in urine diluted at 34 OC as shown in Figure 2.4:
The relationship between log concentration of MS2
and Time is a straight line graph i.e y = mx + k, where in this; ‘y’ is ‘In C’,
‘x’ is ‘t’ and ‘k’ is constant, so that:
……………………………………..… (3.2)
Where: ![]()
m = slope of the graph
3.3.3 Relationship
between Viability of Ascaris suum eggs incubated in
urine and time (days) as shown in Figure 2.5:
…………………………. (3.3)
where:
![]()
3.3.4 Relationship between Minimum
pH during composting and Initial Moisture Content of the substrate
as shown in Figure 2.6:
i) y = constant ;
y = a0
ii) y α x ; y = a1x
iii) y α x2 ; y = a2x2
iv) y α x3 ; y = a3x3
Hence:
y =
………………………………………… (3.4)
where: y = pHmin
x = initial MC
a0 = constants
3.3.5 Relationship
between Theoretical Energy ratio, E and Water ratio,
W as shown in Figure 2.7:
…………………………………………………………………... (3.5)
where:
![]()
3.3.6 Relationship between Time
(weeks) and pH from Figure 2.8:
+A+B……………………………... (3.6)
where: ![]()
![]()
3.4 DATA COLLECTION
The data presented below were
extracted from research works carried out by other international scholars in
the net.
Table
3.1: Relationship
between Time (days) for one decimal reduction and
uncharged ammonia in urine stored at temperatures: 34OC, 24 OC,
14 OC and 4 OC as shown in Figure 2.3, (Niwagaba, 2009).
|
Decimal Reduction Time (days) |
10 |
20 |
40 |
60 |
80 |
100 |
120 |
140 |
150 |
|
NH3 Concentration (mM) |
95 |
60 |
36 |
26 |
22 |
20 |
17 |
16 |
15 |
Table
3.2: Relationship
between Log concentration of MS2 (pathogen) and time
(days) in urine diluted at 34 OC as shown in Figure 2.4, (Niwagaba, 2009).
|
Time (days) |
2.5 |
5.0 |
7.5 |
10 |
15 |
20 |
22.5 |
25 |
|
In (Conc.) |
3.13 |
3.00 |
2.45 |
2.12 |
1.34 |
0.75 |
0.34 |
0 |
Table
3.3: Relationship
between Viability of Ascaris suum eggs incubated in
urine and time (days) as shown in Figure 2.5, (Niwagaba, 2009).
|
Time (days) |
0 |
5 |
10 |
15 |
20 |
25 |
30 |
35 |
40 |
|
Viability (%) |
100 |
117.5 |
118 |
103 |
66 |
27 |
7 |
2.5 |
0 |
Table 3.4: Relationship between Minimum
pH during composting and initial moisture content of the substrate
as shown in Figure 2.6, (Niwagaba,
2009).
|
pHmin |
8.4 |
9.26 |
9.24 |
8.40 |
7.15 |
6.00 |
5.15 |
4.86 |
|
Moisture
Content (%) |
40 |
45 |
50 |
55 |
60 |
65 |
70 |
75 |
Table 3.5: Relationship between Theoretical
Energy ratio, E and Water ratio, W as shown in Figure 2.7, (Niwagaba, 2009).
|
Energy
(cal/g) |
2100 |
1088 |
600 |
376 |
268 |
223 |
200 |
|
Water
Ratio (W) |
3.23 |
5 |
10 |
15 |
20 |
25 |
30 |
Table
3.6: Relationship
between Time (weeks) and pH from Figure 2.8, (Yadav
et al., 2010).
|
pH |
6.50 |
9.33 |
9.25 |
8.90 |
8.60 |
8.38 |
8.25 |
|
Time(weeks) |
0 |
1 |
2 |
3 |
4 |
5 |
6 |
3.5
CURVE FITTING
The numerical values in the
tables (experimental values from the works of scholars) were plotted using
MATLAB toolbox to obtain scatter diagrams. The models were superimposed on the
scatter diagrams. The toolbox was made to apply the models on the scatter diagrams.
Profiles will be plotted showing the models following the scatter diagrams and
simultaneously, the numerical values of the constants of the models will be
declared with 95% confidence bound as well as their statistical goodness of
fits.
3.5.1
Goodness of Fit Statistics The proposed models were
fitted into plots corresponding to the data gathered in Tables 3.1-3.6. Curve
Fitting Toolbox software was used to do this. The Curve Fitting ToolboxTM
software can also be used to assess the goodness-of-fit statistics for
parametric models like:
a) The
sum of squares due to error (SSE),
b) R-square,
c) Adjusted
R-square,
d) Root mean squared error (RMSE).
3.5.1.1
Sum of Squares Due to Error
The overall deviation of the response values from the
fit to the response values is measured by this statistic. It's also known as
the summed square of residuals, and it's abbreviated as SSE.
…………………………………………… Equation 3.7
A
number around 0 suggests that the model's random error component is smaller,
and therefore the fit will be more effective for prediction.
3.5.1.2
R-Square (R2)
This number indicates how well the fit explains the
variation in the data. R-square is the square of the correlation between the
response values and the projected response values, to put it another way. It's
also known as the multiple correlation coefficient squared or the multiple
determination coefficient. The R-square is the ratio of the regression sum of
squares (SSR) to the overall sum of squares (SST). SSR is defined as follows:
……………………………………………. Equation 3.8
SST
is also called the sum of squares about the mean, and is defined as
SST=![]()
Where
SST = SSR + SSE.
Given
these definitions, R-square is expressed as:
…………………………………………….…. Equation 3.10
R-squared
can have any value between 0 and 1, with a value closer to 1 suggesting that
the model accounts for a bigger fraction of the variation. An R-square score of
0.9234, for example, indicates that the fit accounts for 92.34 percent of the
total variation in the data concerning the average. Although the fit may not
improve in a practical sense, R-square will increase as the number of fitted
coefficients in your model grows. You should use the degrees of freedom
adjusted R-square statistic mentioned below to prevent this problem. It's important to note that equations
without a constant term can have a negative R-square. Because R-square is
defined as the proportion of variation explained by the fit, it is negative if
the fit is worse than fitting a horizontal line. R-square cannot be understood
as the square of a correlation in this circumstance. In these cases, a constant
term should be included in the model.
So,0 ≤ R2 ≤ 1.
If
SSR = SST, then R2 = 0, and model is not useful. If SSR = 0, then R2 = 1, and model
fits all points perfectly.
Almost all models will be between these extremes.
3.5.1.3
Degrees of Freedom Adjusted R-Square
The R-square statistic is used in this statistic,
however it is adjusted based on the residual degrees of freedom. The number of
response values n minus the number of fitted coefficients m calculated from the
response values equals the residual degrees of freedom.
………………………………………………………
Equation 3.11
The amount of independent pieces of information
regarding the n data points necessary to calculate the sum of squares is
denoted by the letter V. It's worth noting that if parameters are
bounded and one or more estimates are at or near their bounds, the estimates
are considered fixed. The number of such parameters increases the degree of
freedom. When comparing two nested
models — that is, a series of models each adding extra coefficients to the
preceding model — the modified R-square statistic is often the best indicator
of fit quality.
1
- SSR(n−1) SST(v) …………………………………………...Equation 3.12
………………………..... Equation
3.13
Any
value less than or equal to 1 can be used for the modified R-square statistic,
with a value closer to 1 indicating a better match. When the model incorporates
terms that do not help forecast the response, negative values can arise.
3.5.1.4
Root Mean Squared Error The fit standard error
and the regression standard error are two terms for the same statistic. It is
defined as:
…………………………………………..
Equation 3.14
Where:
MSE is the mean square error or the residual mean square
……………………………………………………… Equation 3.15
Just as with SSE, an MSE value
closer to 0 indicates a fit that is more useful for prediction.
CHAPTER
FOUR
4.0 RESULTS AND
DISCUSSION
4.1 RESULT PRESENTATION
The plots and their tables as obtained from the
previous section (chapter 3) are as shown here below: figures 4.1-4.6, and
tables 4.1-4.6
FIGURES:
Figure 4.1: A plot of Decimal
Reduction Time versus Ammonia concentration
(Model:
,
R-square: 99.94%)
Figure 4.2: A plot of logarithm concentration of MS2
(pathogen)
versus Time
(Model:
,
R-square: 99.62%)
Figure 4.3: A plot of Viability of Ascaris
suum eggs versus Time
(Model:
,
R-square: 99.94%)
Figure 4.4:
A plot of Minimum pH versus Initial Moisture content of compost
(Model: F(x) = p1 ×
+ p2 ×
+ p3 × X + p4, R-square: 99.96%)
Figure
4.5: A plot of Theoretical Energy Ratio versus Water Ratio
(Model:
, R-square: 99.42%)
Figure 4.6: A plot of pH against Time (weeks)
(Model:
, R-square: 99.85%)
TABLES:
![]()
Table
4.1: table of coefficients and statistical goodness of fit (Decimal reduction
time versus Ammonia concentration)
|
Coefficient (with 95% confidence bounds) |
Goodness of fit |
|
|
Parameter |
Value |
|
|
a = 129 |
SSE |
3.422 |
|
b = -0.07471 |
R-square |
0.9994 |
|
c = 35.76 |
Adjusted R-square: |
0.9991 |
|
d = -0.005931 |
RMSE |
0.8273 |
![]()
Where: X = time in days
Table 4.2: table of coefficients and
statistical goodness of fit (Natural log Concentration of MS2 versus Time)
|
Coefficients
(with 95% confidence bounds): |
Goodness
of fit: |
|
|
Parameter |
Value |
|
|
p1 = -0.1428 |
SSE |
0.03906 |
|
p2 = 3.56 |
R-square |
0.9962 |
|
|
Adjusted R-square |
0.9955 |
|
|
RMSE |
0.08068 |
![]()
Table 4.3: table
of coefficients and statistical goodness of fit
(Viability of Ascaris suum eggs versus Time)
|
Coefficients
(with 95% confidence bounds) |
Goodness
of fit |
|
|
Parameter |
Value |
|
|
p1
= -4.741x10-7 |
SSE |
11.69 |
|
p2
= 2.991x10-5 |
R-square |
0.9994 |
|
p3
= 7.46x10-5 |
Adjusted
R-square |
0.9978 |
|
p4
= -0.0256 |
RMSE |
2.417 |
|
p5
= 0.04836 |
|
|
|
p6
= 3.706 |
|
|
|
p7
= 100.1 |
|
|
F(x) = p1 ×
+ p2 ×
+ p3 × X + p4
Table 4.4: table of coefficients and
statistical goodness of fit (Minimum pH versus Initial Moisture
Content of compost)
|
Coefficient
(with 95% confidence bounds) |
Goodness
of fit |
|
|
Parameter |
Value |
|
|
p1
= 0.0004485 |
SSE |
0.009463 |
|
p2
= -0.08123 |
R-square |
0.9996 |
|
p3
= 4.655 |
Adjusted
R-square |
0.9993 |
|
p4
= -76.56 |
RMSE |
0.04864 |
![]()
Table
4.5: table of coefficients and statistical
goodness of fit
(Theoretical Energy Ratio versus Water Ratio)
|
Coefficients
(with 95% confidence bounds): |
Goodness
of fit: |
|
|
Parameter |
Value |
|
|
a = 4857 |
SSE |
1.662x104 |
|
b = 0.8898 |
R-square |
0.9942 |
|
|
Adjusted R-square |
0.9931 |
|
|
RMSE |
57.65 |
![]()
Table 4.6: table of coefficients and statistical
goodness of fit (pH against Time (weeks))
|
Coefficient (with 95% confidence bounds) |
Goodness of fit |
|
|
Parameter |
Value |
|
|
A = 3.3 |
SSE |
0.008282 |
|
B = 3.202 |
R-square |
0.9985 |
|
K2 = 0.1189 |
Adjusted R-square: |
0.997 |
|
K1=2.701 |
RMSE |
0.05254 |
4.2 RESULTS DISCUSSION AND DEDUCTION
A plot of Decimal Reduction Time against Ammonia concentration in the
production of organic fertilizer from human excreta is shown in figure 4.1.
Note that Decimal Reduction Time is the measure of the die-off of bacteria in
stored urine at a particular temperature in relation to the dilution of the
urine. They model
simulate the production of organic fertilizer
from human excreta with 99.94% (almost excellent) accuracy, leaving an error of
0.06%. They coefficient of the model constant are: a = 129, b =
-0.07471, c = 35.76, and d = -0.005931. Observe that when
Decimal Reduction Time is reducing rapidly, Ammonia concentration is increasing
very slowly up to a point (18-35days Decimal Reduction and 60-100mM Ammonia
concentration) where the rate of change of Decimal Reduction with Ammonia
concentration ceases to be rapid before the variation change hand that is
(where the manure is formed); Decimal Reduction begins to decrease slowly while
Ammonia concentration begins to increase rapidly.
A plot of
Viability of Ascaris suum eggs against Time in days is shown in figure 4.2.
Viability measures how capable the Ascaris suum eggs are for normal growth and
development. The accuracy of the plot is 99.94% (almost excellent) only being
fault with 0.06%. In the change of Viability with Time, we observe that the
percentage Viability first increased from 100-118% in 8days and begins to
decrease thereafter until about 30days when the percentage Viability is almost
zero and then maintains a range of 0-8% between 30days and 40days.
A plot of Natural
Logarithmic concentration against Time is shown in figure 4.3. A percentage
accuracy of 99.62% (good) with a fault of 0.28% was obtained. The model is a
straight line profile. It shows the inverse proportion relationship between
Natural Logarithmic Concentration and Time (days) that is; as Natural
Logarithmic Concentration decreases, the time in days increases.
A plot of Minimum pH
against Initial Moisture Content is shown in figure 4.4. An accuracy of 99.96%
(almost excellent) with a fault of 0.04% was obtained. As shown in the figure,
the Minimum pH increases with time from 8.3 to 9.8 as a peak at about 48%
Initial Moisture Content. After this point, the Minimum pH begins to decrease
with increase in Initial Moisture Content until it comes to zero at about 74 –
75% Initial Moisture Content.
A plot of Energy against Water Ratio is shown in figure
4.5. The energy source of
the compost is the fraction of organics in the substrate and the
availability of this affects the heat production in the compost. The heat
production together with the loss regulates the temperature increase during
composting and this also affects the water evaporation during composting. The
variation in figure 4.3 is similar to that in figure 4.1 only that the decrease
in energy and the increase in water ratio happen slightly slowly. The formation
of the manure is observed to be between 400 – 600cal/g of energy and 7 – 10
water ratios. The percentage accuracy of the model is 99.42% (good) hence
having an error of 0.58%.
A plot of pH against
Time in weeks is shown in figure 4.6. Observe that pH increase rapidly with
slow increase in time until it attained a peak value of 9.45 after which it
decreases slowly staying between the ranges of 8 – 9.45. The accuracy of the
plot is 99.85% (very good) leaving an error of 0.15%.
From the data
presented above, we observe that the variable parameters in the production of
fertilizer from human excreta can be represented mathematically and modeled so
that the prediction of the variations of these parameters can be achieved
outside the laboratory. The prediction of the variance in these variable
parameters gives a clear insight on what the nature of the expected end product
(fertilizer) should be. Hence, a standard of the properties of organic
fertilizer produced from human excreta can be established.
CHAPTER FIVE
5.0 CONCLUSION AND RECOMMENDATION
5.1 CONCLUSION
In this research
work, practical work was not done rather data from works of international
scholars were studied and the variable parameters were modeled. The models gave
an accuracy of between 99.42% - 99.96% and error of 0.04% - 0.58% only, showing
that these variable parameters from the production of fertilizer from human
excreta can be modeled.
This
work can be very useful to fertilizer production companies and municipal waste
water treatment plants in the analysis of the quality of fertilizer they
produce from human excreta ensuring they
are eco friendly. It will as well help them not dwell entirely on laboratory
test to predict variable parameters changes hence saves them time and cost of
production.
5.2 RECOMMENDATIONS
Material
handling in and around compost and waste water treatment plants should be
investigated in order to develop good and practical handling instructions that
will help to reduce the danger of disease spread.
More research is
needed to develop effective ways to reduce odors and dangerous emissions from
waste water treatment plants.
There is a need to
look at low-cost, resource-efficient collection techniques, as well as
encourage private sector participation in these practices, such as treatment,
branding/certification, and the sale of treated excreta.
Finally, research is
needed to evaluate the social and cultural acceptability, as well as barriers
to the usage and adoption of various facial treatment approaches. Such research
is also needed to determine whether the final products, compost, ash, and
stored faces, can be used as fertilizer.
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