Radical energy, cost and water savings from recycling food waste
Submitting Institution
Loughborough UniversityUnit of Assessment
Civil and Construction EngineeringSummary Impact Type
TechnologicalResearch Subject Area(s)
Engineering: Chemical Engineering, Environmental Engineering
Summary of the impact
Research into a new waste treatment process model at Loughborough
University (1993 to date) has resulted in the following benefits for
Unilever:
- Savings of £2m for wastewater treatment over the last 4 years
- In 2012 additional savings of £0.2m from biogas and £0.1m in water
supply and landfill costs
- A reduction in carbon dioxide emissions of 10 million tonnes (2012)
from the substitution of fossil fuels
- Significant reductions in the risks of spills, sewer overloads and the
recycling of scarce resources, namely water and fertilizer
- Newly developed underpinning generic principles to be incorporated in
updated designs and guides for users (to be published by Foundation for
Water Research/ICE/CIWEM)
- Researchers (five) being employed as a direct result of the
specialised expertise gained and their ability to provide similar
benefits to other sectors of industry
Underpinning research
Research at Loughborough University (LU) from 1993 to date had
established that combining biogas recovery with waste treatment would
improve the viability of recycling food-processing wastes, if the
stability of the process could be improved [R1 for example].
Surveys of biogas production from the traditional areas of application of
anaerobic digestion, namely sewage and animal slurry treatment [R2],
suggested half these plants suffered from breakdowns due to unforeseen
shock loads.
This research carried out by Andrew Wheatley (LU, 1991 to date), Kenneth
Johnson (RA 1993-1995) and Christopher Fell (RA 1997-2000) devised a
highly effective way of characterising food-processing effluent [G1]
[R3] to predict the changes likely to cause excesses of metabolic
intermediates. These were the most commonly reported cause of the problems
with the traditional applications of anaerobic digestion to treat domestic
sewage and agricultural wastes. The result was a technique that was
mathematically simple and easy to validate without the need for exotic
equipment, but was responsive to the potentially sudden diurnal and
seasonal variations in waste characteristics. It overcomes the inability
of the previously used mechanistic models, founded on classical kinetic
equations, to adequately represent rapidly changing and complex organic
food wastes [R4].
The resulting model was based on dividing the load into three proportions
according to particle size analysis (filtration and settlement R1) as a
surrogate for the kinetic microbial growth rate constants [G2].
This basic model was then used to guide new research necessary to optimise
pre-treatments to reduce particle size in difficult waste streams such as
those containing large amounts of solids, for example intact yeast cell
walls (Shelton Smith PhD 2008).
Wheatley, with the financial support of Unilever [G3], led
research by John Shelton-Smith (2003-2008) and Helen Theaker (2008-2009)
to apply and improve the knowledge on the effectiveness of novel particle
disruption techniques (ultrasound, microwaves, pressure swing, cavitation
and electropulses) to wastes from brewing and yeast processing. The
researchers were able to use the phase-analysis method of characterising
waste from their earlier work to predict risk and yields of biogas from
the proposed anaerobic treatment. The research was used to model the most
efficient sequence for the treatment train — and which waste streams to
include — to achieve both the best stability and biogas yields.
Alternatives were compared firstly in laboratory tests and then the
preferred design validated with a 25m3 pilot plant built with
Unilever and contractors to provide real time scale up data on the
resilience to shocks [R5].
A virtual full scale design was also produced to calculate the capital
and running costs for the Marmite site using the data from the pilot trial
[R5].
References to the research
R1 Monroy, O., Johnson, K.A., Wheatley, A.D., Hawkes, F. and Caine, M.
(1994) "The Anaerobic Filtration of Dairy Waste: Results of a Pilot
Trial", Bioresource Technology, 50 (3), 243-251, ISBN 0950 9623,
doi: 10.1016/0960-8524(94)90097-3
R2 Johnson, KA, Wheatley, AD, Monroy, O (1994) "Mixing and Solids
Accumulation in Anaerobic Filters. Two Case Studies", Environmental
Technology, 15, 263-270, ISSN: 0959-3330, doi:
10.1080/09593339409385427
R3 Johnson, K.A., Wheatley, A.D. and Fell, C.F. (1995) "An Application
of an Adaptive Control Algorithm for the Anaerobic Treatment of
Industrial Effluent", Transactions of Inst. Chem Engineers,
73, 203-211, ISSN: 0957-5820
R4 Wheatley, A.D., Fisher, M.B. and Grobicki, A.M.W. (1997)
"Applications of Anaerobic Digestion for the treatment of Industrial
Wastewaters in Europe", Water and Environment Journal,
11, 1, 39-46, doi: 10.1111/j.1747-6593.1997.tb00086.x
R5 Shelton-Smith, J. and Wheatley, A.D. (2006) "Opportunities for
Centralised Anaerobic Digestion Facilities to meet the Food Waste
Regulations — A Business Plan", 11th European
Biosolids and Organic Resources Conference, Wakefield AquaEnviro,
ISBN-13: 978-1903958209
R6 Bryns, G., Smedley, V. and Wheatley, A.D. (2012) "Carbon dioxide
releases from wastewater treatment", Engineering sustainability — The
Proceedings of the Institution of Civil Engineers, 166, 111-121,
DOI: 10.1680/ensu.11.00037
Grants awarded:
G1 Wheatley et al., The anaerobic Digestion of industrial
Effluent, EPSRC GR/H/18494, 1992-1995, £300k
G2 Wheatley et al., Non-invasive wastewater analysis,
EPSRC GR/G/18858, 1991-1994, £150k
G3 Wheatley, Codigestion of domestic and industrial waste materials,
Muntons, Severn Trent and Biffa, 1995-2008, £100K
G4 Wheatley, Application of anaerobic digestion to a case study food
processing effluent, Unilever, 2000-2003, £150k
Details of the impact
Food waste is a highly publicised priority problem since land and water
used in its production are the largest demands on global resources.
According to the DECC/DEFRA Anaerobic Digestion Strategy and Action Plan (http://bit.ly/1995KKQ) 16 million
tonnes (dry weight) of food and drink waste is generated annually in the
UK, furthermore producing at least 10 times this in wastewater. It was
calculated [R6] that treating effluent using conventional
wastewater treatment requires about 800 KWh per wet tonne, up from 500KWh
in 2005.
The immediate impact from this research has been to demonstrate new
technology that provides renewable energy whilst reducing wastewater and
greenhouse-gas emissions. Dissemination throughout the food and processing
industry will have significant economic and sustainability benefits. Our
partners, Unilever, have pioneered this application (R1) led by its
commitment to innovation and sustainability. Reducing waste at food
processing sites is a priority during any major investment or
refurbishment. The Marmite plant generates 15 tonnes of high-strength
food-processing effluent an hour round the clock and if the company were
to discharge this into the sewer it would cost more than £0.5m per annum.
This was one of the alternatives, which were either to discharge to the
Utility for treatment, to build a conventional tried and tested but carbon
intensive plant, or to use the risky, anaerobic digestion technology.
Other questions that arose were whether all or only part of their
wastewater should be treated and if they should outsource operation of a
waste treatment plant.
Analysis of these alternatives started in 2005 against the backdrop of
the renewable-energy incentives offered by the UKs commitment to reducing
carbon emissions and the enhancement of support for recycling. Unilever
enlisted Wheatley's help in their decision-making based on his previous
contributions to solving waste problems at this and other sites.
Loughborough's work was fundamental to the feasibility and
decision-making meetings at Unilever (2005), at which the main
effluent-management options were compared and enumerated. A major
contribution was quantifying and reducing the risk from using innovative
technology for energy and water recovery. The uncertainty arose because
anaerobic reactors had rarely been used for treating industrial wastewater
in the UK and where they had, problems were reported. The incentives
however suggested site specific work and Unilever fully funded
Shelton-Smith at Loughborough [G4] to work out what would be
required to successfully adapt anaerobic digestion to the Marmite site.
Wheatley and Shelton-Smith were able to use the previous research [R3]
on how to characterise the variable nature of food-production effluents to
optimise anaerobic digestion. Monitoring of the waste in this way was used
to suggest the best process-flow sheet to achieve reliability and
sustainability. Using these data and their experience with anaerobic
treatment of other wastes, the research team shortlisted the most
promising reactor designs and pre-treatment techniques.
In all, the researchers worked with, contractors and other technical
experts from the Unilever group from 2005-2009 to detail the design and
commissioning. Extensive testing was crucial to gaining the confidence of
Unilever senior management in this untried approach to effluent-treatment.
They financed the research and based on the results, investment was
approved and £4m spent in 2009 on construction of a plant for energy and
water recovery implementing the treatment process developed and
established at Loughborough [R4].
Wheatley and Shelton-Smith advised in the competitive procurement process
organised by Unilever to select the contractor and subcontractor.
Loughborough researcher Theaker was appointed by Unilever in 2008 to lead
the commissioning of the plant, which has been operating successfully to
date [C1, C2, C3].
The impact and reach of the research extends well beyond the Unilever
application. Our innovative procedures provide a practicable and
fundamentally different approach to the design of anaerobic wastewater
treatment plants. Our approach simplified the reaction rate model through
radical changes to waste characterisation and monitoring procedures;
(three instead of thirty parameters). The procedure is easy to use and is
to be incorporated as an update to the mechanistic International Water
Association model and described to the industry by the Foundation for
Water Research, the Chartered Institution of Water and Environmental
Management and Institution of Civil Engineers design guidelines to new
bioreactor designs. These are the standard guidelines for practitioners
working in the £500m food waste processing sector.
The research had significant economic impact realised through the new
wastewater-treatment plant's production of biogas and clean water.
Unilever uses the biogas to produce energy, which currently the company
uses directly on site. Unilever have made the business case for further
investment for gas storage with the prospect of feeding electricity from
the plant into the national distribution network. Water from the treatment
plant is pure enough to be recycled for multiple uses. Excluding running
costs, the plant saved £0.9m in 2012, a figure projected to increase year
on year, particularly with energy price rises.
The new Marmite wastewater-treatment plant also makes a substantial
contribution to sustainability including the replacement of fossil fuel
from power generation estimated to be more than 10 million tonnes of CO2
per year [C1]. The other environmental benefits are the reduction
in the volume and strength of effluent discharged to the sewer, which is
reducing the risk of odour, sewer overflows and overloads as climate
changes generates more intensive rainfall. Current research focusses on
recovery of other materials as well as water and gas, particularly
nitrogen and phosphorus from the solids residues.
Unilever are working to extend the approach that we have pioneered at
Marmite to other Unilever food-processing plants across Europe, making use
of the EU wide incentives for renewable energy. The new procedures adopted
at Marmite have delivered a 10% reduction in operating costs through the
generation of renewable energy (20% of site use) and lowered
effluent-treatment costs by 90% [C1].
Through their participation in the research (doctoral and post-doctoral),
five researchers have been able to disseminate these developments in the
engineering of anaerobic treatment and industrial effluent management.
Shelton-Smith and Theaker were employed by Unilever as a result of these
research outcomes and to apply the technology to other company's sites [C1].
Fell and two others work for other companies in the water industry.
Sources to corroborate the impact
The following sources of corroboration can be made available at request:
C1 Letter of corroboration from Project Leader, Unilever Marmite Foods,
Burton on Trent
C2 Letter of corroboration from Managing Director, Aquabio (subcontractor
mainly responsible for design and build of the wastewater treatment plant
at Unilever's Burton upon Trent site)
C3 Letter of corroboration from the Technical Manager, Unilever Marmite
Foods, Burton on Trent