use of anaerobic digestion for food waste treatment … fs29 – use of anaerobic digestion for food...
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Research & Development
Factsheet 29
May 2009
Use of anaerobic digestion
for food waste treatment
in Orkney
Summary
Shellfish waste is a major financial and operational burden to the seafood processing industry. Current estimates show that around 63,000 tonnes of shellfish waste is sent for disposal each year at a cost of almost £3,000,000. In theory there are many uses for shell, but to date there is no one solution to treating and subsequently using these materials as by-products. Most processors rely on disposal outlets costing up to £150 per tonne of waste. Shellfish processors want simple, local, cost-effective solutions for managing shellfish waste. Anaerobic digestion (AD) has been identified as a potential solution. The process produces methane which can be used to generate electricity, and create digestate (fertiliser) which has applications in agriculture and horticulture.
What is anaerobic digestion?
AD is a natural biological process in which
biodegradable waste is broken down by bacteria,
in the absence of oxygen. The process uses a
gastight reactor vessel (the digester). Waste
materials (feedstock) are fed in daily and biogas
and fertiliser taken out.
The project team pictured in front of a digester
AD is very flexible in that it can use a wide range
of organic feedstocks from agricultural waste
through to food processing wastes. Biogas is
made up of methane (about 55-70%), carbon
dioxide (about 30-45%) and traces of hydrogen
sulphide and water vapour.
During digestion, the feedstock material goes
through a number of different biochemical
processes. The amount of biogas produced varies
with the amount and type of material fed into the
vessel, as does the rate of decomposition. The
rate of decomposition can depend on various
conditions, such as the temperature inside the
vessel. It is important that conditions inside the
vessel are properly balanced to enable the
different types of bacteria to work effectively. The
most important parameters are temperature (the
AD vessel is generally kept between 35 to 55oC
using recycled heat from utilising biogas) and pH.
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The four key biological and chemical stages of AD
Stage Activity
1. Hydrolysis A chemical reaction in which large
complex organic polymers
(cellulose, carbohydrates and
proteins) in the feedstock are
broken into smaller parts through
reaction with water. The smaller
molecules are simple sugars,
amino acids and fatty acids.
2. Acidogenesis Further simple molecules are
created ready for the third stage.
3. Acetogenesis Results in the production of acetic
acid, as well as carbon dioxide and
hydrogen.
4. Methanogenesis Bacteria convert the acids into
methane, carbon dioxide and
water. It is the methane and
carbon dioxide which form the
main components of biogas, which
can be extracted from the AD
vessel.
It is the feedstock that remains in the vessel which
the bacteria cannot feed upon, along with the
dead bacterial remains, which makes up the
digestate biofertiliser (this occurs after one to six
weeks depending on the feedstock).
One of the benefits of AD is the reduction in both
mass and volume of the input waste, thus
reducing storage requirements. Between 40-60%
of the organic matter in the AD process is
converted to biogas, the rest is left as odour-free
digestate. When a batch AD process has
completed, the vessel is emptied leaving about
10-15% behind which acts as a seed culture for
the next batch. The biogas is used as a biofuel to
generate electricity.
The AD process has been applied to many
agricultural and processing wastes, as well as
being an important element in sewerage treatment
plants. The nutrient-rich digestate can have a
variety of uses, such as spreading on land for
agricultural purposes and horticultural uses, as
well as soil cover for landfill sites.
The project
Heat and Power Ltd. were part funded by Seafish
to evaluate the potential of AD as a solution to the
shellfish waste disposal problem for Orkney based
shellfish and food processors. The main aims of
the project were to consider whether AD could
reduce commercial waste disposal costs, and if it
could be a sustainable waste management
solution for the island. It included a small-scale
batch digester trial on crab shells.
Food waste in Orkney
Food wastes from eleven sources were assessed
during the project, which included; meat, dairy,
salmon and crab processors. The quantities of
solid and liquid (effluent) waste were estimated for
each. In total, approximately 52,170 tonnes of
solid and liquid wastes are produced each year,
costing approximately £1,931,000 in disposal
costs. Only one company makes a profit from their
waste. Currently much of the food waste from
Orkney is sent to mainland Scotland.
The types of food wastes available are all
considered suitable for AD but they would have to
be mixed to achieve the correct carbon to nitrogen
ratio, lipid and dry matter content and to maximise
methane production.
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Small-scale batch digester trial on crab
shell
Part of the project included a trial with batch
anaerobic digestion using crab shell. Common
problems with digesting wastes such as crab
shells is the potential for silting conventional
designs of anaerobic digester. The solids
remaining after digestion often settle out rather
than remaining in suspension in the digestate. A
new form of digester was designed and trialled as
part of the project. The first stage was to build a
scale model of the proposed digester to ascertain
to what degree the shells would digest. A small 25
litre digester was constructed and the digested
shells were sent for laboratory analysis. The
positive results from this experiment led to the
construction of a larger two cubic metre batch
digester.
Mobile batch digester arrives and is unloaded at Westray Processors to collect crab shells.
The shell was crushed and heated at the shellfish
processors. The pasteurised shells were kept at
over 90oC for an hour, before emptying into a two
cubic metre tank, where they were kept above
70oC for a further hour. The tank was fitted with a
12mm screen and digestate from a cattle slurry
digester was added to provide the bacteria
required to initiate digestion. Approximately four
times the volume of digestate was added to the
pasteurised shells. A chopper pump suction pipe
was connected to the bottom of the tank and
processed the material, delivering back via the lid
section over a mesh section.
The shell material after a first pass via the crusher and loaded into the digester.
The material was held in anaerobic conditions for
a period of three weeks and produced some
limited amounts of biogas in the gas holder.
The digester was mixed daily via a power take-off driven chopper pump and connected to a small gas holder.
Costs
After analysis of all the different feedstocks it was
estimated that from the 52,170 tonnes of solid and
liquid wastes produced in Orkney, the total value
of electricity that could be generated from the
biogas is £263,410. Additional revenue would be
realised if the digestate could be sold for use in
agriculture, however there is currently no market
for this material.
One of the envisaged outcomes of the project is to
develop a commercial scale, mobile facility which
would travel to the different sites around the
island. A mobile AD plant would be used, enabling
the waste to be treated during transport. The gate
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Origin Way, Europarc, Grimsby, DN37 9TZ
t: 01472 252300 e: [email protected] w: www.seafish.org SIN: http://sin.seafish.org
supporting the seafood industry for a sustainable, profitable future
fees for a proposed commercial scale facility would
be kept as low as possible. This will be achieved by
following a not-for-profit social enterprise model
that will provide savings for the food processing
companies compared to current disposal costs.
However it is impossible to provide estimates of the
potential costs or savings.
Potential set-up costs for a commercial scale unit
are in the region of £1500 per cubic metre of
capacity. The running costs would be covered by
the gate fees and sales of electricity. Again it has
not been possible to provide estimates of the
running costs. Heat and Power estimate that
transporting material from Orkney mainland to
Westray where it is planned to site the main
digester, would cost in the region of £15 per tonne
of m3.
Conclusions & recommendations
AD treatment of shellfish and other food
processing wastes in Orkney is principally
feasible. Financial profits may be created and
environmental benefits achieved through more
efficient resource utilisation, reduced pollution
and reduced waste transport compared with the
current situation. There may also be additional
brand value for food processors. Using a not-for-
profit social enterprise model will provide further
savings for the food processing companies.
Batch anaerobic digestion is suggested as a
solution for crab shells. There are certain
challenges for the AD process operation but the
batch plant design appears to have solved some
of the major operational restrictions.
A full investor-ready study for digestion capacity
to provide for the industry in the Islands is
recommended.
Further research and trials into the use of
digested crab shell for metal biosorbents is
required.
It is recommended that cleaning equipment for
those shells (crab) not currently cleaned to ‘free
of flesh’ standards is developed.
Follow-on work
As a result of this study, Heat and Power have
applied for a licence for the AD treatment of animal
by-products. Heat and Power is also going to
construct a larger ten cubic metre mobile digester
which is suited to the transport and treatment of
food processing wastes from the Orkney mainland.
Contacts & further information
Michaela Archer – Seafish –
Heat and Power Ltd. – www.heatandpower.ltd.uk
Full details of the project are available in the
Seafish Report – SR609 Use of waste as a
biofuel and fertiliser in Orkney, Heat and Power
Ltd, April 2009. To download a copy of this
report go to the Seafish website -
http://www.seafish.org/resources/publications.asp and
search for ‘Orkney’ on the publications page