Activated sludge systems [1] Constructed Soil Filter Advanced
Oxidation Process Aerated lagoon Aerobic granular reactor Aerobic
treatment system Anaerobic clarigester Anaerobic digestion API
oil-water separator Anaerobic lagoon ATP test Bead Filter Belt
press Bioconversion of biomass to mixed alcohol fuels Bioreactor
Bioretention Biorotor Bioroll [2] Biolytix Carbon filtering Cesspit
Chlorine disinfection Combined sewer Composting toilet Constructed
wetland Dark fermentation Dissolved air flotation Distillation
Desalination EcocyclET systems Electrocoagulation
Electrodeionization Electrolysis Electro-Fenton process [3]
Expanded granular sludge bed digestion Facultative lagoon Fenton's
reagent Flocculation & sedimentation Fluidized Bed Biofilter
Flotation process Froth flotation Fuzzy Filter Humanure
(composting) Imhoff tank Iodine Ion exchange Life Saver bottle
Living machines Maceration (sewage) Membrane bioreactor
Nanotechnology NERV (Natural Endogenous Respiration Vessel) N-Viro
Parallel plate oil-water separator Recirculating Sand Filter Reed
bed Retention basin Reverse osmosis Rotating biological contactor
Sand filter Septic tank Sequencing batch reactor Sewage treatment
Stabilization pond Submerged aerated filter [4][5] Treatment pond
Trickling filter Ultrafiltration (industrial) Ultraviolet
disinfection Upflow anaerobic sludge blanket digestion Upflow
Sludge Blanket Filtration (USBF) Wet oxidation
API oil-water separatorAn API oil-water separator is a device
designed to separate gross amounts of oil and suspended solids from
the wastewater effluents of oil refineries, petrochemical plants,
chemical plants, natural gas processing plants and other industrial
sources. The name is derived from the fact that such separators are
designed according to standards published by the American Petroleum
Institute (API). [1][2]Description of the design and operationThe
API separator is a gravity separation device designed by using
Stokes Law to define the rise velocity of oil droplets based on
their density and size. The design of the separator is based on the
specific gravity difference between the oil and the wastewater
because that difference is much smaller than the specific gravity
difference between the suspended solids and water. Based on that
design criterion, most of the suspended solids will settle to the
bottom of the separator as a sediment layer, the oil will rise to
top of the separator, and the wastewater will be the middle layer
between the oil on top and the solids on the bottom.[2]Typically,
the oil layer is skimmed off and subsequently re-processed or
disposed of, and the bottom sediment layer is removed by a chain
and flight scraper (or similar device) and a sludge pump. The water
layer is sent to further treatment consisting usually of a
dissolved air flotation (DAF) unit for further removal of any
residual oil and then to some type of biological treatment unit for
removal of undesirable dissolved chemical compounds.Parallel plate
separators are similar to API separators but they include tilted
parallel plate assemblies (also known as parallel packs).[2] The
underside of each parallel plate provides more surface for
suspended oil droplets to coalesce into larger globules. Any
sediment slides down the topside of each parallel plate. Such
separators still depend upon the specific gravity between the
suspended oil and the water. However, the parallel plates enhance
the degree of oil-water separation. The result is that a parallel
plate separator requires significantly less space than a
conventional API separator to achieve the same degree of
separation.
Other oil-water separation applicationsThere are other
applications requiring oil-water separation. For example: Oily
water separators (OWS) for separating oil from the bilge water
accumulated in ships as required by the international MARPOL
Convention.[3][4] Oil and water separators are commonly used in
electrical substations. The transformers found in substations use a
large amount of oil for cooling purposes. Moats are constructed
surrounding unenclosed substations to catch any leaked oil, but
these will also catch rainwater. Oil and water separators therefore
provide a quicker and easier cleanup of an oil leak.[5]
Bioconversion of biomass to mixed alcohol fuelsThe bioconversion
of biomass to mixed alcohol fuels can be accomplished using the
MixAlco process. Through bioconversion of biomass to a mixed
alcohol fuel, more energy from the biomass will end up as liquid
fuels than in converting biomass to ethanol by yeast
fermentation.The process involves a biological/chemical method for
converting any biodegradable material (e.g., urban wastes, such as
municipal solid waste, biodegradable waste, and sewage sludge,
agricultural residues such as corn stover, sugarcane bagasse,
cotton gin trash, manure) into useful chemicals, such as carboxylic
acids (e.g., acetic, propionic, butyric acid), ketones (e.g.,
acetone, methyl ethyl ketone, diethyl ketone) and biofuels, such as
a mixture of primary alcohols (e.g., ethanol, propanol, butanol)
and/or a mixture of secondary alcohols (e.g., isopropanol,
2-butanol, 3-pentanol). Because of the many products that can be
economically produced, this process is a true biorefinery[1]
[2][3].The process uses a mixed culture of naturally occurring
microorganisms found in natural habitats such as the rumen of
cattle, termite guts, and marine and terrestrial swamps to
anaerobically digest biomass into a mixture of carboxylic acids
produced during the acidogenic and acetogenic stages of anaerobic
digestion, however with the inhibition of the methanogenic final
stage. The more popular methods for production of ethanol and
cellulosic ethanol use enzymes that must be isolated first to be
added to the biomass and thus convert the starch or cellulose into
simple sugars, followed then by yeast fermentation into ethanol.
This process does not need the addition of such enzymes as these
microorganisms make their own [4].As the microoganisms
anaerobically digest the biomass and convert it into a mixture of
carboxylic acids, the pH must be controlled. This is done by the
addition of a buffering agent (e.g., ammonium bicarbonate, calcium
carbonate), thus yielding a mixture of carboxylate salts.
Methanogenesis, which, as mentioned, is the natural final stage of
anaerobic digestion, is inhibited by the presence of the ammonium
ions or by the addition of an inhibitor (e.g., iodoform). The
resulting fermentation broth contains the produced carboxylate
salts that must be dewatered. This is achieved efficiently by
vapor-compression evaporation. Further chemical refining of the
dewatered fermentation broth may then take place depending on the
final chemical or biofuel product desired.The condensed distilled
water from the vapor-compression evaporation system is recycled
back to the fermentation. On the other hand, if raw sewage or other
waste water with high BOD in need of treatment is used as the water
for the fermentation, the condensed distilled water from the
evaporation can be recycled back to the city or to the original
source of the high-BOD waste water. Thus, this process can also
serve as a water treatment facility, while producing valuable
chemicals or biofuels.Because the system uses a mixed culture of
microorganisms, besides not needing any enzyme addition, the
fermentation requires no sterility or aseptic conditions, making
this front step in the process more economical than in more popular
methods for the production of cellulosic ethanol. These savings in
the front end of the process, where volumes are large, allows
flexibility for further chemical transformations after dewatering,
where volumes are small.
Carboxylic acidsFor more details on this topic, see Carboxylic
acid.Carboxylic acids can be regenerated from the carboxylate salts
using a process known as "acid springing". This process makes use
of a high-molecular-weight tertiary amine (e.g., trioctylamine),
which is switched with the cation (e.g., ammonium or calcium). The
resulting amine carboxylate can then be thermally decomposed into
the amine itself, which is recycled, and the corresponding
carboxylic acid. In this way, theoretically, no chemicals are
consumed or wastes produced during this step. [5][edit] KetonesFor
more details on this topic, see Ketone.There are two methods for
making ketones. The first one consists on thermally converting
calcium carboxylate salts into the corresponding ketones. This was
a common method for making acetone from calcium acetate during
World War I[6]. The other method for making ketones consists on
converting the vaporized carboxylic acids on a catalytic bed of
zirconium oxide [7].[edit] AlcoholsFor more details on this topic,
see Alcohol.[edit] Primary alcoholsThe undigested residue from the
fermentation may be used in gasification to make hydrogen (H2).
This H2 can then be used to hydrogenolyze the esters over a
catalyst (e.g., copper chromite)[8], which are produced by
esterifying either the ammonium carboxylate salts (e.g., ammonium
acetate, propionate, butyrate) or the carboxylic acids (e.g.,
acetic, propionic, butyric acid) with a high-molecular-weight
alcohol (e.g., hexanol, heptanol)[9]. From the hydrogenolysis, the
final products are the high-molecular-weight alcohol, which is
recycled back to the esterification, and the corresponding primary
alcohols (e.g., ethanol, propanol, butanol).[edit] Secondary
alcoholsThe secondary alcohols (e.g., isopropanol, 2-butanol,
3-pentanol) are obtained by hydrogenating over a catalyst (e.g.,
Raney nickel) the corresponding ketones (e.g., acetone, methyl
ethyl ketone, diethyl ketone)[10].[edit] Acetic acid versus
EthanolCellulosic-ethanol -manufacturing plants are bound to be net
exporters of electricity because a large portion of the
lignocellulosic biomass, namely lignin, remains undigested and it
must be burned, thus producing electricity for the plant and excess
electricity for the grid. As the market grows and this technology
becomes more widespread, coupling the liquid fuel and the
electricity markets will become more and more difficult.Acetic
acid, unlike ethanol, is biologically produced from simple sugars
without the production of carbon dioxide:C6H12O6 2 CH3CH2OH + 2 CO2
(Biological production of ethanol)C6H12O6 3 CH3COOH (Biological
production of acetic acid)Because of this, on a mass basis, the
yields will be higher than in ethanol fermentation. If then, the
undigested residue (mostly lignin) is used to produce hydrogen by
gasification, it is ensured that more energy from the biomass will
end up as liquid fuels rather than excess heat/electricity [11].3
CH3COOH + 6 H2 3 CH3CH2OH + 3 H2O (Hydrogenation of acetic
acid)C6H12O6 (from cellulose) + 6 H2 (from lignin) 3 CH3CH2OH + 3
H2O (Overall reaction)A more comprehensive description of the
economics of each of the fuels is given on the pages alcohol fuel
and ethanol fuel, more information about the economics of various
systems can be found on the central page biofuel.[edit] Stage of
developmentThe system has been in development since 1991, moving
from the laboratory scale (10 g/day) to the pilot scale (200
lb/day) in 2001. A small demonstration-scale plant (5 ton/day) is
under construction as is expected to be operational mid 2008 and a
100 ton/day demonstration plant is expected in 2009.[edit] See
also
BioreactorA bioreactor may refer to any device or system that
supports a biologically active environment.[1] In one case, a
bioreactor is a vessel in which is carried out a chemical process
which involves organisms or biochemically active substances derived
from such organisms. This process can either be aerobic or
anaerobic. These bioreactors are commonly cylindrical, ranging in
size from liters to cubic meters, and are often made of stainless
steel.A bioreactor may also refer to a device or system meant to
grow cells or tissues in the context of cell culture. These devices
are being developed for use in tissue engineering.On the basis of
mode of operation, a bioreactor may be classified as batch, fed
batch or continuous (e.g. Continuous stirred-tank reactor model).
An example of a continuous bioreactor is the chemostat.Organisms
growing in bioreactors may be suspended or immobilized. The
simplest, where cells are immobilized, is a Petri dish with agar
gel. Large scale immobilized cell bioreactors are: moving media
packed bed fibrous bed membrane Batch type bioreactor n General
structure of bach type bioreactor
Bioreactors are also designed to treat sewage and wastewater. In
the most efficient of these systems there is a supply of
free-flowing, chemically inert media that acts as a receptacle for
the bacteria that breaks down the raw sewage. Examples of these
bioreactors often have separate, sequential tanks and a mechanical
separator or cyclone to speed the division of water and biosolids.
Aerators supply oxygen to the sewage and media further accelerating
breakdown. In the process, the liquids Biochemical Oxygen Demand
BOD is reduced sufficiently to render the contaminated water fit
for reuse. The biosolids can be collected for further processing or
dried and used as fertilizer. An extremely simple version of a
sewage bioreactor is a septic tank whereby the sewage is left in
situ, with or without additional media to house bacteria. In this
instance, the biosludge itself is the primary host (activated
sludge) for the bacteria. Septic systems are best suited where
there is sufficient landmass and the system is not subject to
flooding or overly saturated ground and where time and efficiency
is not of an essence.In bioreactors where the goal is to grow cells
or tissues for experimental or therapeutic purposes, the design is
significantly different from industrial bioreactors. Many cells and
tissues, especially mammalian ones, must have a surface or other
structural support in order to grow, and agitated environments are
often destructive to these cell types and tissues. Higher organisms
also need more complex growth medium.Composting toiletA composting
toilet is an aerobic processing system that treats excreta,
typically with no water or small volumes of flush water, via
composting or managed aerobic decomposition[1]. This is usually a
faster process than the anaerobic decomposition at work in most
wastewater systems, such as septic systems.Composting toilets are
often used as an alternative to central wastewater treatment plants
(sewers) or septic systems. Typically they are chosen (1) to
alleviate the need for water to flush toilets, (2) to avoid
discharging nutrients and/or potential pathogens into
environmentally sensitive areas, or (3) to capture nutrients in
human excreta. Several manufactured composting toilet models are on
the market, and construct-it-yourself systems are also
popular.[2]These should not be confused with pit latrines (see
latrine, pit latrine, and arborloo or tree bog), all of which are
forms of less controlled decomposition, and may not protect ground
water from nutrient or pathogen contamination or provide optimal
nutrient recycling.
Manufactured composting toilet systems"Self-contained"
composting toilets complete or begin the composting in a container
within the receiving fixture. "Remote," "central," or "underfloor"
units collect excreta via a toilet stool, either waterless or
micro-flush, from which it drains to a composter. "Vacuum-flush
systems" can flush horizontally or upward with a small amount of
water to the composter. "Micro-flush toilets" use a small amount of
water usually 1pint (.5liter) per use."Self-contained" composting
toilets are slightly larger than a flush toilet, but use roughly
the same floor space. Some units use fans for aeration, and
optionally, heating elements to maintain optimum temperatures to
hasten the composting process and to evaporate urine and other
moisture. Operators of composting toilets commonly add a small
amount of absorbent carbon material (such as untreated sawdust,
coconut coir, peat moss) after each use to create air pockets for
better aerobic processing, to absorb liquid, and to create an odor
barrier. This additive is sometimes referred to as "bulking agent."
Some owner-operators use microbial "starter" cultures to ensure
composting bacteria are in the process, although this is not
critical."Remote," "central," and "under-floor" models each feature
a chamber below the toilet stool (such as in a basement or outside)
where composting takes place. These are typically used for
high-volume and year-round applications as well as to serve
multiple toilet stools. Several systems are available as well as
many build-it-yourself options.In contrast, "desiccating toilets"
dry the excreta to destroy pathogens, though one study suggested
that drying can result in rehydration of pathogens when in contact
with moisture later.[3]The performance testing standard for
composting toilets in the United States is American National
Standard/NSF International Standard ANSI/NSF 41-1998: Non-Liquid
Saturated Treatment Systems.[4] Systems might also be listed with
CSA, cETL-US, and other standards Build-it-yourself, site-built,
and owner-built designSite-built indoor composting toilet designs
vary, ranging from rollaway containers fitted with aerators to
large concrete sloped-bottom tanks.These are not to be confused
with "direct outdoor composting," which typically uses a collector
bucket, where each deposit is covered with sawdust or other dry
organic material, with the collector periodically being hand
transported to an outdoor composting bin, where it may be added to
yard waste or other organic material being composted.Public
useIncreasingly, composting toilet systems are commonly used in
water closets in public facilities. One example is the three-storey
C.K. Choi Building at the University of British Columbia (Canada),
which features five composting toilet systems with 12 toilet stools
that serve 300 employees. They may also be found in various places
around Europe, like many of the roadside facilities in Sweden (see
image).Composting toilets greatly reduce the volume of excreta on
site through psychrophilic, thermophilic or mesophilic composting
and yield a soil amendment that can be used in horticultural or
agricultural applications as local regulations allow.Public
composting toilet facility on E6 highway in Sweden
Although there are many designs, the process factors at work are
the same. Rapid aerobic composting will be thermophilic
decomposition in which bacteria that thrive at high temperatures
(40-60C / 104-140F) oxidizes (breaks down) the waste into its
components, some of which are consumed in the process, reducing
volume, and eliminating potential pathogens.Drainage of excess
liquid or "leachate" via a separate drain at the bottom of the
composter is featured in some manufactured units, as the aerobic
composting process requires moisture levels to be controlled
(ideally 50% +/-10): too dry, and the mass decomposes slowly or not
at all; too wet and anaerobic organisms thrive, creating
undesirable odors (cf. Anaerobic digestion). This separated liquid
may be diverted to a graywater system or collected for other
uses.An approach that is becoming more common is the "dry" toilet,
or urine-separating (also: urine-diverting) toilet. Where solar
heat is used, this might be called a "solar" toilet.[5] These
systems depend on desiccation to achieve sanitation safety goals[6]
features systems that make use of the separated liquid fraction for
immediate area fertilization.Urine can contain up to 90 percent of
the N (nitrogen), up to 50 percent of the P (phosphorus) and up to
70 percent of the K (potassium)) present in human excreta.[7] In
healthy individuals it is usually pathogen free, although undiluted
it may contain levels of inorganic salts and organic compounds at
levels toxic to plants.[8]The other requirement critical for
microbial action (as well as drying) is oxygen. Commercial systems
provide methods of ventilation that move air from the room, through
the waste container, and out a vertical pipe, venting above the
enclosure roof. This air movement (via convection or fan forced)
will vent carbon dioxide and odors.Most units require manual
methods for periodic aeration of the solid mass such as rotating a
drum inside the unit or working an "aerator rake" through the mass.
Composting toilet brands have different provisions for emptying the
"finished product," and supply a range of capacities based on
volume of use. Frequency of emptying will depend on the speed of
the decomposition process and capacity, from a few months (active
hot composting) to years (passive, cold composting). With a
properly sized and managed unit, a very small volume (about 10% of
inputs) of a humus-like material results, which can be suitable as
soil amendment for agriculture, depending on local public health
regulations.Constructed wetlandA constructed wetland or wetpark is
an artificial marsh or swamp, created for anthropogenic discharge
such as wastewater, stormwater runoff or sewage treatment, and as
habitat for wildlife, or for land reclamation after mining or other
disturbance. Natural wetlands act as biofilter, removing sediments
and pollutants such as heavy metals from the water, and constructed
wetlands can be designed to emulate these features.Vegetation in a
wetland provides a substrate (roots, stems, and leaves) upon which
microorganisms can grow as they break down organic materials. This
community of microorganisms is known as the periphyton. The
periphyton and natural chemical processes are responsible for
approximately 90 percent of pollutant removal and waste breakdown.
The plants remove about seven to ten percent of pollutants, and act
as a carbon source for the microbes when they decay. Different
species of aquatic plants have different rates of heavy metal
uptake, a consideration for plant selection in a constructed
wetland used for water treatment.Constructed wetlands are of two
basic types: subsurface-flow and surface-flow wetlands.
Subsurface-flow wetlands can be further classified as horizontal
flow and vertical flow constructed wetlands. Subsurface-flow
wetlands move effluent (agricultural or mining runoff, tannery or
meat processing wastes, wastewater from sewage or storm drains, or
other water to be cleansed) through a gravel lavastone or sand
medium on which plants are rooted; surface-flow wetlands move
effluent above the soil in a planted marsh or swamp, and thus can
be supported by a wider variety of soil types including bay mud and
other silty clays. In subsurface-flow systems, the effluent may
move either horizontally, parallel to the surface, or vertically,
from the planted layer down through the substrate and out.
Subsurface horizontal-flow wetlands are less hospitable to
mosquitoes, whose populations can be a problem in constructed
wetlands (carnivorous plants have been used to address this
problem). Subsurface-flow systems have the advantage of requiring
less land area for water treatment, but are not generally as
suitable for wildlife habitat as are surface-flow constructed
wetlands. Plantings of reedbeds are popular in European constructed
wetlands, and plants such as cattails (Typha spp.), sedges, Water
Hyacinth (Eichhornia crassipes) and Pontederia spp. are used
worldwide. Recent research in use of constructed wetlands for
subarctic regions has shown that buckbeans (Menyanthes trifoliata)
and pendant grass (Arctophila fulva) are also useful for metals
uptake.Newly Planted Constructed Wetland. The same constructed
wetland two years later.
General contaminant removalPhysical, chemical, and biological
processes combine in wetlands to remove contaminants from
wastewater. An understanding of these processes is fundamental not
only to designing wetland systems but to understanding the fate of
chemicals once they have entered the wetland. Theoretically,
treatment of wastewater within a constructed wetland occurs as it
passes through the wetland medium and the plant rhizosphere. A thin
aerobic film around each root hair is aerobic due to the leakage of
oxygen from the rhizomes, roots, and rootlets.[1] Decomposition of
organic matter is facilitated by aerobic and anaerobic
micro-organisms present. Microbial nitrification and subsequent
denitrification releases nitrogen as gas to the atmosphere.
Phosphorus is coprecipitated with iron, aluminium, and calcium
compounds located in the root-bed medium.[2][3] Suspended solids
are filtered out as they settle in the water column in surface flow
wetlands or are physically filtered out by the medium within
subsurface flow wetland cells. Harmful bacteria and viruses are
reduced by filtration and adsorption by biofilms on the rock media
in subsurface flow and vertical flow systems.
ATP testThe ATP test is a process of rapidly measuring actively
growing microorganisms through detection of adenosine triphosphate,
or ATP.ATP testing methodATP is a molecule found in and around
living cells, and as such it gives a direct measure of biological
concentration and health. ATP is quantified by measuring the light
produced through its reaction with the naturally-occurring firefly
enzyme luciferase using a luminometer. The amount of light produced
is directly proportional to the amount of living organisms present
in the sample. [1]ATP tests can be used to: Control biological
treatment reactors Guide biocide dosing programs Determine drinking
water cleanliness Manage fermentation processes Assess soil
activity Determine corrosion / deposit process type Measure
equipment or product sanitationWithin a water sample containing
microorganisms, there are two types of ATP: Intracellular ATP ATP
contained within living biological cells. Extracellular ATP ATP
located outside of biological cells that has been released from
dead or stressed organisms.Accurate measurement of these two types
of ATP is critical to utilizing ATP-based measurements. Being able
to accurately measure these different types of ATP offers the
ability to assess biological health and activity, and subsequently
control water and wastewater processes.