Membrane Bio Reactor Varsseveld
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The new wastewater treatment plant in Varsseveld is the first full-scale
membrane bioreactor (MBR) for the treatment of domestic wastewater in the
Netherlands. The plant produces 755 cubic metres of clean water per hour
using membranes through which the wastewater is passed.
Dutch Crown Prince Willem-Alexander officially opened the Varsseveld WWTP
on 3 May 2005. See the press
release for
more information.
On 25 April 2005 an international MBR Symposium was held at the plant in Varsseveld.
Click here for more information, photos and to download all handouts.
April 2005 the third MBR Special of the Dutch H2O magazine was published.
Download it now here.
The membrane surface at the Varsseveld plant totals more than 20,000 square
metres (approximately the size of four football pitches). If you want to see
how a membrane tank is constructed, take a look at this video.
Background
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The Rhine and IJssel Water Board decided to modernize the Varsseveld wastewater
treatment plant in order to comply with the following requirements and preconditions:
- improvement of effluent quality due to stricter requirements;
- prevention of sludge leaching;
- expansion of biological capacity;
- limiting odour and noise emissions;
- general upgrading of the technical installations.
Improvement of the effluent quality is necessary because the effluent
of the treatment plant at Varsseveld is discharged into a small and
ecologically vulnerable
inland waterway called the Boven Slinge, which forms part of an ecological
corridor. The desired improvement of effluent quality could have been
achieved
using conventional technology in combination with effluent polishing
through sand filtration. In the past few years, however, an alternative
has been
developed in the form of MBR technology. In early 2000, this prompted
the Rhine and IJssel
Water Board to commission DHV Water NV to conduct a feasibility study
into the application of the MBR concept at the Varsseveld treatment
plant. The
results of this study were so interesting that it was decided to make
the plans more
specific.
The innovative character of MBR technology played an important role
in the decision-making process. This model installation showcasing
MBR technology
was constructed with support from all the Dutch water boards through
a fund
for technological innovation.
MBR technology
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Membrane bioreactor (MBR) technology is a hot item in the water treatment
industry. The combination of biological purification processes with membrane
filtration seems to have a promising future when it comes to purifying (waste)water.
Nevertheless, much is still unknown about MBR: How does it work? Where can
it be applied? What are the benefits and costs? What are the latest technological
innovations?
Together with the Foundation for Applied Water Research (STOWA), WaterForum
Online is closely following developments in this area and compiling news
items, background information, project details, products and links in the ‘Membrane
bioreactor file’ at www.waterforum.net.
Planning
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Construction work on the wastewater treatment plant in Varsseveld started
in the second half of 2003. Based on an extensive system selection study, the
decision to construct a membrane bioreactor (MBR) was already taken in 2001.
The treatment plant in Varsseveld is the first MBR installation for the treatment
of domestic wastewater in the Netherlands.
Construction work took place between the end of 2003 and the end of
2004. The various installations and the control software were tested
and completed in November 2004 and the membranes were placed in the installation
on 1 and 2 December. After the membranes had been tested, the MBR plant
was started up just before Christmas 2004, using sludge from the existing
wastewater treatment plant in Varsseveld. In February 2005, the biological
start-up process of the MBR plant was completed and the installation
was fully operational.
The official opening of the plant took take place on 3 May 2005.
Design
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Load
The load of the Varsseveld wastewater treatment plant will total 23,150 population
equivalents and 755 cubic metres per hour in 2015. The design is based
on stricter effluent requirements than stipulated by law, namely nitrogen < 5
mg Ntotal/l and phosphate < 0.15 mg Ptotal/l. Because weather conditions
in the Netherlands lead to a high level of rain drainage via the sewer
system, this aspect played an important part in the design. As a result,
the maximum hydraulic load of the MBR plant is almost three times the average
supply level. The treatment of wastewater from a nearby cheese factory
also played an important role in the design.
Pre-treatment
Because the membranes are vulnerable to contamination and damage, a great deal
of attention was paid in the design to the pre-treatment of raw wastewater.
Leaves, plastic, sand, grease, hairs and the like must all be removed from
the water supply. To achieve this, the wastewater is first led over a screen
with a rod distance of 6 mm. It then flows through an aerated sand and
grease trap and finally through microsieves with a perforation of 0.8 mm.
Even when this pre-treatment procedure is followed, solid content (e.g. encrusted
sludge or falling leaves) may end up in the activated sludge installation and
impair the operation of the membranes or damage them. To keep the activated
sludge clean, it is therefore continually recirculated over the microsieves
from the activated sludge tank. When the membrane tank is emptied during a
purification cycle, the entire content of the tank is also circulated over
the microsieves.
Biological
purification
In principle, the biological processes taking place in an MBR plant do not
differ from those in a conventional activated sludge plant. Because a lower
dry matter content can be used and no final sedimentation tanks are needed,
an MBR plant can be constructed in a much more compact manner. The design of
the biological purification process and the control of the biological processes
require a different approach because of shorter accumulation times and a different
oxygen balance. A dynamic simulation model of the MBR plant was therefore developed
for design and process control purposes. The model was based in part on the
IAWQ-1 model in the SIMBA software application.
Membrane
filtration
Following a European tender procedure, the contract for membrane filtration
was awarded to the membrane supplier Zenon. Positive experiences were gained
with capillary membranes in a number of treatment plants, including one in
Beverwijk, a town in the west of the Netherlands. The key design parameters
for the membrane filtration process are listed below in Table 1.
table 1 – Design data for
the membrane installation
| Parameter |
Unit |
Value |
| Capacity |
RWA
Average |
m3/h
m3/d |
755
5.000 |
| Flux |
RWA |
l/(m2.h) |
37,5 |
Required membrane surface
Surface area per element
Number of elements per cassette
Surface area per cassette
Required number of cassettes
Number of compartments
Number of cassettes per compartment |
m2
m2
-
m2
-
-
- |
20.160
31,5
40
1.260
16
4
4 |
All the
required membranes will be installed in four separate compartments.
To ensure that the membranes function properly, the load must be
distributed as evenly (i.e. symmetrically) as possible. To this end,
special attention was paid to the design of the inflow and outflow
facilities of these tanks.
The undersides
of the membrane modules have been fitted with coarse bubble aeration.
The air bubbles cause turbulence, so that activated sludge particles
cannot attach themselves to the membrane surface. The inclusion of
a back-flush step in the process cycle prevents membrane pore blockage.
The division into compartments makes it possible to take membranes
out of service in case of low supply levels, when full capacity is
not needed. This option saves energy because the membranes do not
have to be continually aerated and are given sufficient time for
relaxation. Periodic chemical cleaning is also required, in addition
to the continuous cleaning of the membrane surface.
Financing
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The costs for the entire installation amounted to approximately EUR 10 million.
Because the investment and operating costs for a membrane bioreactor (MBR)
are higher than for a conventional wastewater treatment plant, the Rhine and
IJssel Water Board sought additional financing. Key support was provided by
the Foundation for Applied Water Research (STOWA). To cover the additional
costs and risks, STOWA created an Innovation Fund with support from all Dutch
water boards. The Fund was established to enable the entire Dutch water treatment
sector to provide incentives for innovative technological development, such
as the MBR plant in Varsseveld.
The broader importance of the MBR project was also recognized by the European
Union, the Ministry of Housing, Spatial Planning and the Environment, and
the Ministry of Economic Affairs. For instance, the European Union provided
a financial
contribution as part of LIFE, the EU’s financial instrument for the environment.
The Ministry of Housing, Spatial Planning and the Environment concluded that
the project serves the interests of environmental protection and issued a so-called ‘green
declaration’ for it (meaning that the MBR project qualifies for incentive
schemes for ‘green investment’). The Minister of Economic Affairs
allocated subsidies to the project as part of the subsidy scheme for energy
supplies in the non-profit and special sectors (EINP scheme).
Stowa Innovation Fund
Innovative technologies such as the membrane bioreactor (MBR) are generally
not yet competing with conventional technologies because they are still under
development and market forces are therefore not yet functioning. Additionally,
putting such technologies into practice is not entirely without risk. After
all, the infrastructure of the water boards must be used to do so.
To jointly bear the risk of damage and the additional costs, the Dutch water
boards decided in 2001 to set up a so-called Innovation Fund. The Fund operates
as follows: the costs of the plant to be designed are estimated and compared
to the costs of a similar (fictitious) conventional plant. After deducting
a substantial extra contribution from the water board that is to ‘host’ the
proposed plant, the difference is paid out of the Innovation Fund. Should the
project fail to succeed, the renovation costs will also be borne jointly and
paid from the Fund. The Fund is managed by the STOWA Foundation for Applied
Water Research and is financed on the basis of the number of pollution units
produced by the control areas of the various water boards.
The annual contribution by the water boards was based on the costs of the
Varsseveld project. The water boards made a four-year commitment, which
was initially
intended only for the application of MBR technology. The water boards agreed
to evaluate the operation of the Fund after four years and to decide on
the Fund’s future on the basis of that evaluation. The Ministry of Transport,
Public Works and Water Management made a one-off contribution of approximately
EUR 1.4 million when the Fund was established. In the period 2002-2005, the
water quality managers have managed to raise over EUR 4.4 million for the Fund.
Subsidies for the Varsseveld project were obtained as part of the LIFE regulation
(an EU subsidy scheme) and the EINP scheme (a subsidy scheme of the Ministry
of Economic Affairs providing energy investment incentives to non-profit
organizations). These subsidies were partly allocated to the budget of
the STOWA Innovation
Fund. After deduction of the contribution to the Varsseveld project, the
remaining amount was recently allocated to two hybrid MBR projects in Heenvliet
and Ootmarsum.
In April 2004, the operation of the Innovation Fund was evaluated at a STOWA
meeting attended by all the water boards. A proposal was put forward at this
meeting to continue the contributions to the Innovation Fund after 2005.
Proposals were also put forward to broaden the objectives of the Fund beyond
MBR applications
or projects related to wastewater treatment systems. All task areas of the
water boards (water chain, water systems, and flood prevention and maintenance
of water barriers) should qualify for funding, including projects of a non-technical
nature. In mid-2004, the board of directors of the STOWA Foundation decided
to accept this proposal. From 2005 onwards, the Innovation Fund will be integrated
with the STOWA research program so that a mature R&D policy can be developed
for the water boards. In the long-range planning process, innovation forms
a separate theme across all task areas.
General
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The membrane bioreactor (MBR) at the Varsseveld wastewater treatment plant
of the Rhine and IJssel Water Board serves as the demonstration installation
for this technology in the Netherlands. The most important purpose of this
installation is to scale up the MBR technology and demonstrate its operation
on a practical level. Further research and development is necessary to achieve
this. An extensive research programme will therefore be conducted from May
2004 to the end of 2005. The programme will deal with all aspects of MBR technology,
i.e. pre-treatment, biological purification and membrane filtration. The goal
of this research programme is to acquire more knowledge about MBR technology
and to optimize the design guidelines for MBR installations.
Objectives
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In consultation with the STOWA supervision committee for MBR projects, the Rhine
and IJssel Water Board and DHV drew up a research programme containing the following
objectives:
- demonstrating the technical feasibility of scaling up the MBR technology;
- demonstrating the stability of the operational management;
- determining the technical results, subdivided into pre-treatment, biological
operation and membranes;
- investigating the need for redundancy;
- optimising process management;
- evaluating the design (based on items 1 to 5 inclusive);
- comparing the costs of the MBR plant with the costs of a conventional
plant.
Site studies
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Seven site studies have been defined based on the overall objectives. These studies
and the parties involved in them are listed in the table below:
| Site studies |
WRIJ |
Stowa |
DHV |
TNO |
Wetsus |
TU Delft |
BRCC |
| I |
Pre-treatment |
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| II |
Operational management |
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| III |
Effluent quality |
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| IV |
OC & Hydraulics |
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| V |
Sludge quality |
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| VI |
Process control technology |
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| VII |
Membranes |
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Pilot installation
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The use of a pilot installation is an important part of the research being
conducted at the Varsseveld MBR plant. Experiences gained worldwide with MBR
technology have shown that the use of a simulation unit can simplify and accelerate
the start-up and operational management of an MBR installation. In addition,
the simulation unit, which contains wastewater from the town of Varsseveld,
provides important support for practical research. Using the simulation unit,
changes to the process management of the installation can now be tested before
they are put into practice. This approach not only yields cost savings, but
also reduces the risks involved in the operational management of the actual
installation. The simulation unit also makes it possible to train the operators
and other employees of the Rhine and IJssel Water Board involved.
In the pilot research, much attention has been paid to energy reduction by
technical improvements. This part of the pilot research has been subsidised
by the SenterNovem programme on "Energy reduction by innovation".
The Rhine and IJssel Water Board commissioned Zenon Environmental, Inc. to
construct a simulation unit that was put into operation in May 2004. The
simulation unit is a mirror image of the full-scale installation.
The pilot research is financially supported by SenterNovem.
Results: Pilot installation
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Membrane filtration
The most important results for the membranes of the pilot
installation are as follows:
- The so-called Clean Water Permeability (CWP), which is indicative of
the quality of the membranes, is characteristic for high-end Zenon ZW500d
membranes. The
membranes were approved on the basis of these measurements.
- Although the tests were performed at relatively high process temperatures,
the membrane results were good. Most tests will be performed again
in the winter in order to evaluate the functioning of the membranes at lower
temperatures.
- The chemical purification of the membranes was optimised in the simulation
unit. The use of hydrogen peroxide proved to be ineffective due to
the relatively high grease content of the local wastewater. Good results
were obtained
using
a combination of sodium hydroxide and warm water.
- A significant reduction of the energy consumption of the membrane installation
seems possible on the basis of energy optimisation testing. Further
research at lower temperatures and during longer testing periods should provide
more
insight.
Biological process
The first biological start-up procedure of the simulation unit was cut short
due to software problems. As a result, the simulation unit did not receive
sufficient wastewater during the start-up procedure, leading to poor sludge
quality and excessive foaming. After the software had been repaired, the
biological process was restarted on 7 June 2004.
Although the initial research objectives of the simulation unit did not include
demonstrating the effectiveness of the biological processes, the results
are promising. The effluent requirement for the Varsseveld MBR plant
is 5.0 mg
Ntotal/l. The nitrogen content of the effluent stayed below this level
during the entire study period, with the exception of a few minor exceedances.
During
a period of a few weeks, we even managed to achieve the MTR standard
value of 2.2 mg Ntotal/l. This makes the simulation unit at Varsseveld
the first
installation in the Netherlands to meet the MTR standard for nitrogen
removal without dosage from a carbon source. These positive results can
largely be
explained by the favourable composition of the influent, the advantageous
process conditions and the optimal process design.
The phosphate content of the effluent is largely dependent on the values
set for iron dosage. Since the beginning of September 2004, we have managed
to
achieve a phosphate content of approximately 0.1 to 0.3 mg Ptotal/l at
an iron dosage level of approximately 0.8 mol Fe/mol P. Iron dosage was
discontinued
at the beginning of November 2004. The effects of relocating the dosage
point will be examined during a later stage of the study.
The pilot installation was dismantled on Thursday 20 January 2005. The
biological media were removed and the filtration unit was relocated
and directly connected
to the full-scale MBR plant. The key research objective for the filtration
unit is the continuing investigation of energy savings in process
mode (permeate extraction) and in stand-by mode (no permeate extraction).
Results: Full scale installation
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The MBR plant at Varsseveld has been in operation since the end of December
2004. The installation was inoculated using activated sludge from the existing
Varsseveld wastewater treatment plant, which continued to operate during the
start-up process of the new plant. The sludge content after inoculation amounted
to approximately 2.5 g DS/l. In a period of about seven weeks, the sludge content
increased to the desired level of 10 g DS/l.
The biological results are promising. Five weeks after start-up, the total
nitrogen content in the effluent dropped below the required maximum level
of 5 mg/l. Since then, the effluent content has varied between 2 and 4
mg Ntotal/l
at a process temperature of around 12ºC. The phosphate content ranges
between 2 and 5 mg Ptotal/l. The iron-salt dosage system will soon be put into
operation in order to further decrease the effluent content to the desired
level of 0.15 mg Ptotal/l.
The four membrane channels have been in operation since the beginning of
2005 and are functioning according to expectations. In the coming weeks,
the membranes
will undergo further capacity testing.
Photos
© DHV
photos opening: © Harry Brouwer
/ TNO
Film material
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Structure of a membrane tank
At the MBR plant in Varsseveld,
we use so-called ZeeWeed® membranes manufactured
by Zenon Environmental, Inc. Thousands of these spaghetti-shaped membranes,
each over 2 metres in length, have been packed into one membrane module. At
Varsseveld, 40 of these modules have been placed into one membrane cassette.
Each of the four membrane tanks at the Varsseveld plant contains four of these
cassettes.
The membrane surface at the Varsseveld plant totals over 20,000 square metres
(equivalent to the surface area of four football pitches).
Start video (AVI,
7,5 MB)
Demonstration of filtration, back-flush and aeration process
Each membrane tank has a central pipeline through which the extracted
water (known as the permeate) is discharged. The permeate is also ‘flushed
back’ through this pipeline. This back-flush process removes the contamination
present on the membrane, as demonstrated in the video below. Note the activated
sludge particles and the aeration bubbles.
Start
video (AVI,
11 MB)
A video player, such as the Windows Media Player, is required to watch this
video.
© Zenon
Opening of membrane bioreactor in Varsseveld
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The opening program started on Wednesday 20 April 2005 and concluded with
the official opening by Dutch Crown Prince Willem-Alexander on Tuesday 3 May.
Click here for
the photos.
The international MBR symposium ‘Varsseveld in international perspective’ was
held on Monday 25 April. More information can be found here.
The plant was open to the public on Saturday 30 April and Sunday 1 May
from 10.00 am to 16.00 pm. About 1,100 people visited the plant.
Tuesday 3 May the official opening took place by Prince Willem-Alexander.
More information can be found here.
Eerste full-scale zuivering met membraanbioreactor vrijwel gereed
De nieuwe rioolwaterzuiveringsinstallatie Varsseveld is bijna gereed.
Deze eerste full-scale zuivering met een membraanbioreactor wordt momenteel
getest.
Op 3 mei 2005 vindt de officiële opening plaats. De nieuwe zuivering zorgt
ervoor dat meer fosfaat en stikstof uit het afvalwater gehaald wordt en dat
schoner water geloosd kan worden op de Boven Slinge, een beek die is aangemerkt
als ecologische verbindingszone.
De rwzi van Waterschap Rijn en IJssel gaat uiteindelijk 755 kubieke meter
schoon water per uur leveren. Naast de nu in aanbouw zijnde MBR-installatie
is al enige tijd een ‘klein broertje’ in bedrijf om ervaring op
te doen met het opstarten en de elektronica voor de ‘grote’ installatie.
Ook is met deze unit onderzocht welke chemicaliën het best bij de reiniging
kunnen worden gebruikt.
Sinds begin november worden de diverse installaties en software van de grote
zuivering getest. De membranen zijn begin deze maand geplaatst (zie foto) en
worden nu getest. Het waterschap en de andere betrokken partijen bij de bouw
van de installatie (STOWA, DHV en Zenon) verwachten dat het opstarten van de
membraanbioreactor over enkele weken hierdoor zonder problemen zal verlopen.
© H2O
Filters vormen hart in zuivering Varsseveld
De nieuwe hightech rioolwaterzuivering in Varsseveld heeft een hart gekregen.
Gisteren en vandaag zijn de zestien grote filters geplaatst die het slib
in de laatste fase van de zuivering van het rioolwater van vrijwel alle verontreinigingen
zullen ontdoen.
In de nieuwe rioolwaterzuivering (een investering van 10 miljoen euro) arriveert,
net als in de verouderde installatie uit 1972, het vloeibare afval van ruim
twintigduizend inwoners en een aantal bedrijven uit Mariënvelde, Heelweg,
Halle en Westendorp.
Alleen schoon water en pesticiden kunnen de filters passeren. Zelfs de uiterst
kleine virussen en bacteriën die met traditionele technieken amper zijn
tegen te houden, worden zo uit het oppervlaktewater gehouden.
En dat is belangrijk, want het Varsseveldse rioolwater komt na de zuivering
terecht in de Boven Slinge. Die maakt daar deel uit van een ecologische verbindingszone.
Het water moet daar van de hoogst haalbare kwaliteit zijn.
Het is voor het eerst dat de filters, honderdduizenden membranen in een pakket
van 2 bij 2,5 meter, in Nederland op deze schaal wordt toegepast. Als het
komende anderhalf jaar blijkt dat deze zuiveringstechniek in typisch Nederlandse
omstandigheden werkt en ook nog financieel haalbaar is, zal ze naar verwachting
door tal van waterschappen in het hele land worden toegepast.
Na kleinere testopstellingen is Beverwijk en Varsseveld, is projectleider
Philip Schyns van het Waterschap Rijn en IJsel er van overtuigd dat het gezuiverde
water voor de Boven Slinge aan de wettelijke eisen zal voldoen. Maar het
hoge en dus dure energieverbruik is mogelijk een hobbel voor een verdere
invoering van het systeem.
Om te voorkomen dat er verstopping ontstat in de uiterst fijne gaatjes in
de membranen, moet het rioolslib met enorme bellenblazers voortdurend in
beweging worden gehouden. Voorlopig zullen de apparaten een kwart van de
tijd blazen, de helft minder dan de fabrikant van de membranen heeft voorgeschreven.
Zo kan alvast op de energierekening worden bespaard, verwacht Schyns.
© de Gelderlander
Compacte rioolwaterzuivering Varsseveld
Door Paul Versluis
Varsseveld – Eind volgend jaar beschikt Varsseveld over de meest geavanceerde
compacte grote zuivering voor huishoudelijk afvalwater in Nederland.
Het water dat hier vandaan op de Boven-Slinge wordt geloosd is schoner dan
voorheen: geen enkele vaste stof zal de nieuwe ‘membraan-reactor’ kunnen
passeren. Ook nitraten en fosfaten zullen vaker dan ooit achterblijven. “Het
gezuiverde water komt er bijna als drinkwater uit”, voorspellen de
betrokkenen.
Klik hier (PDF,
553 kB) voor het volledige artikel.
© de Gelderlander
Rioolwater zuiveren met een MBR-installatie
TNO coördineert het onderzoek rond de opstart van de eerste full-scale
MBR-waterzuiveringsinstallatie.
(…) TNO is, door middel van een uitgebreid onderzoeksprogramma, betrokken
bij de voorbereidingen en de opstart van de MBR-installatie. Het onderzoek – in
nauwe samenwerking met de hoofdaannemer en ontwerper, ingenieursbureau DHV – moet
de risico’s minimaliseren die de opstart van een dergelijke innovatieve
installatie met zich meebrengt, en daarnaast kennis opleveren voor het ontwerpen
van andere, nog grotere installaties.
Ook de TU Delft en universitair onderzoekscentrum WETSUS zijn betrokken bij
het onderzoek.
Klik hier (PDF, 44 kB) voor het volledige artikel.
© TNO magazine
Articles
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H2O MBR Special III, April 2005:
Download the special (PDF, 4,6
MB)
H2O MBR Special II, April 2003:
MBR Varsseveld, a demonstration of progression
Authors: ir. P.F.T. Schyns, ir. C. Petri, ir. A.G.N. van Bentem,
ing. L.S.D.M. Kox M.Sc
H2O MBR Special II, April 2003:
MBR-technology, the Dutch contribution to the worldwide hype
Authors: ir. J. Leenen, ir. H.F. van der Roest
H2O MBR Special I, October 2001:
First Dutch full scale MBR application on WWTP Varsseveld
Authors: ir. J. Leunk, drs. C. Roos, ir. P.F.T. Schyns
Persbericht 1 december 2004, Waterschap Rijn en IJssel
Rioolwaterzuiveringsinstallatie Varsseveld bijna gereed
De nieuwe rioolwaterzuiveringsinstallatie Varsseveld van Waterschap
Rijn en IJssel nadert zijn voltooiing. Het is Nederlands eerste full-scale
membraan-bioreactor, dus innovatief van opzet. De installatie gaat met
behulp van membranen, waar het afvalwater doorheen wordt gezogen, per
uur 755 m3 schoon water afleveren. Belangrijkste doelstellingen voor
de nieuwbouw waren: stiller produceren, meer fosfaat en stikstof uit
het afvalwater halen en helder en schoner water lozen op de Boven Slinge,
een beek die is aangemerkt als ecologische verbindingszone.
Simulatie-unit
Al een tijdje is naast de in aanbouw zijnde membraanbioreactor (MBR)
een klein broertje in bedrijf. Het is een simulatie-unit, waarmee de
juiste opstartmethode voor de echte MBR is bepaald. Ook is met deze
unit besturingselektronica getest en is onderzocht welke reinigingschemicaliën
het beste kunnen worden toegepast. Het waterschap en zijn partners
bij de bouw van de installatie, de Stichting Toegepast Waterbeheer
(Stowa), ingenieursbureau DHV en Zenon, verwachten dat daardoor het
opstarten van de MBR over een paar weken, zonder problemen verloopt.
De simulatie-opzet is ook gebruikt voor het verder opleiden van het
waterschapspersoneel. De zuiveringsresultaten van de unit zijn uitstekend.
Testen en opstart
Sinds begin november worden de diverse installaties en software getest
en worden onderdelen in gebruik genomen. Ook is gestart met het testen
van de membraaninstallatie, zonder de aanwezigheid van de membranen
zelf. Deze zijn/worden woensdag 1 en donderdag 2 december in de installatie
gehesen. Daarna wordt opnieuw getest en begin volgend jaar is de biologische
opstart van de MBR.
Op 3 mei 2005 vindt de officiële opening plaats.
Persbericht 20 oktober 2003, Waterschap Rijn en IJssel
Start bouw high tech zuiveringsinstallatie Varsseveld
Vrijdag j.l. is officieel de bouw gestart van Nederlands eerste membraanbioreactor
op de rioolwaterzuiveringsinstallatie Varsseveld. Met de nieuwbouw is
een bedrag gemoeid van twaalf miljoen euro. Eind 2004 wordt de membraanbioreactor
in bedrijf genomen. Alle waterschappen in Nederland en ook de Europese
Gemeenschap ondersteunen het innovatieproject en kijken uit naar de resultaten
van deze primeur.
Membraantechnologie
De rioolwaterzuiveringsinstallatie Varsseveld, die afvalwater van huizen
en bedrijven binnenkrijgt uit Varsseveld, Mariënvelde, Heelweg,
Halle en Westendorp, is één van de kleinere zuiveringsinstallaties
van de 14 die in het beheersgebied van Waterschap Rijn en IJssel werkzaam
zijn.
Deze rwzi wordt de eerste in Nederland die huishoudelijk afvalwater met
membranen zuivert. De membraan technologie is een nieuwe ontwikkeling
in de afvalwaterwereld, die zowel betere resultaten levert als minder
ruimte nodig heeft dan de huidige zuiveringsinstallaties. In een membraanbioreactor
wordt het vuil in het afvalwater, net als in het ‘normale’ zuiveringsproces,
ook afgebroken door bacteriën. Deze zuiverende bacteriën blijven
in de zuiveringsinstallatie aanwezig. Normaliter worden ze in grote bezinktanks
van het gezuiverde water gescheiden. In Varsseveld zal deze scheiding
via membranen plaatsvinden. De membranen zijn een soort kunststof rietjes
met minuscuul kleine gaatjes. Het gezuiverde water wordt door deze gaatjes
gezogen, maar deze gaatjes zijn zo klein dat de bacteriën er niet
doorheen kunnen. Zij blijven dus achter in de zuivering en gaan door
met hun zuiverende werk.
Het water wordt op deze manier heel schoon, bevat geen enkel vast deeltje
meer en erg weinig fosfaat en stikstof.
Vervolg
De waterkwaliteit van de Boven Slinge, die als ecologische verbindingszone
fungeert, vaart er wel bij. Daarin komt namelijk het effluent (=gezuiverde
water) terecht. Voor Nederland, waar ruimte schaars is en de oppervlaktewaterkwaliteit
nog beter moet, is dit een prima oplossing.
Op basis van de resultaten met de rwzi Varsseveld zullen naar verwachting
ook grotere zuiveringsinstallaties in Nederland worden uitgerust met
membranen.
De realisatie van het project wordt mede mogelijk gemaakt met financiële
steun van de STOWA (innovatiefonds van alle Nederlandse waterschappen)
en subsidie van de Europese Gemeenschap via LIFE.
Planning
Eind 2004 is de nieuwbouw gereed. Gedurende de bouw zal het zuiveringsproces
in de huidige zuiveringsonderdelen vrijwel ongehinderd doorgaan. De
bestaande onderdelen zullen pas worden gesloopt nadat de nieuwe zuivering
bewezen heeft betrouwbaar te functioneren.
Press release 1 April 2005, Waterboard Rhine and IJssel
Crown Prince Willem-Alexander to open Varsseveld wastewater treatment plant
On Tuesday 3 May 2005 at 10.00 am, His Royal Highness the Prince of
Orange will perform the official opening of the wastewater treatment
plant in Varsseveld. This plant is the first in the Netherlands to purify
domestic wastewater using membranes. Thanks to the membrane bioreactor,
the wastewater will be considerably cleaner. Based on the results of
the Varsseveld plant, larger treatment plants in the Netherlands are
expected to be fitted with membranes as well. All Dutch Water Boards,
the STOWA Foundation for Applied Water Research and the European Community
are supporting the project and are eagerly awaiting the results.
Press release 8 april 2005, Waterboard Rhine and IJssel
Welcome to WWTP Varsseveld
Press release 3 May 2005, Waterboard Rhine and IJssel
Crown Prince Willem-Alexander has opened Varsseveld WWTP
On Tuesday 3 May 2005, His Royal Highness the Prince of Orange has
performed the official opening of the wastewater treatment plant in Varsseveld.
This plant is the first in the Netherlands to purify domestic wastewater
using membranes.
Children from the local towns of Varsseveld and Ulft and the Children’s
Choir of the city of Baarn, led by Majel Lustenhouwer joined in the opening.
Thanks to the membrane bioreactor, the wastewater will be considerably
cleaner. Based on the results of the Varsseveld plant, larger treatment
plants in the Netherlands are expected to be fitted with membranes as
well. All Dutch Water Boards, the STOWA Foundation for Applied Water
Research and the European Community are supporting the project and are
eagerly awaiting the results.
Guided Tour
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Guided tours are organized on demand every Tuesday and Thursday afternoon.
To apply, please fill out the
application form below and click 'Send’.
Colophon
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This website is an initiative of the project team MBR Varsseveld consisting
of the Rhine and IJssel waterboard, the Dutch Foundation for Applied Water
Research (STOWA) and engineering and consultancy group DHV.
The purpose of this website is to disclose all information on the Varsseveld
membrane bioreactor project: the realization of the MBR Varsseveld as
well as the accompanying research program.
The editorial board consists of:
ir. P.F.T. Schyns, Rhine and IJssel
waterboard
ir. C.A. Uijterlinde, Foundation
for Applied Water Research (STOWA)
ir. H.F. van der Roest,
Engineering and consultancy group DHV
Editing: Suzette
Schreuder, DHV, +31 33 4682026
Design: Claudia
Mulder, DHV.
itinerary
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BY CAR:
Arnhem:
•
From Arnhem via the A12 towards Zutphen, Oberhausen • After 18
km take the Doetinchem / Enschede junction: A18 • At the end of
the A18, turn right towards Enschede / Winterswijk • At the traffic
lights, turn left towards Zelhem • After 60 m turn right onto the
Vlakkeeweg.
You are now at WWTP Varsseveld. Follow the parking instructions.
Germany (Border crossing at Beek, Germany A3 / Holland A12):
•
A3 towards Arnhem (after border crossing: A12) • Direct after the
border, take the A18 towards Enschede / Doetinchem • At the end
of the A18 turn right towards Enschede / Winterswijk • At the traffic
lights, turn left towards Zelhem • After 60 m turn right onto the
Vlakkeeweg.
You are now at WWTP Varsseveld. Follow the parking instructions.
Groenlo:
Head for Doetinchem over the N18 (Twente route) • After approximately
16 km at the traffic lights, turn right towards Zelhem • After
60 m turn right onto the Vlakkeeweg.
You are now at WWTP Varsseveld. Follow the parking instructions.
Winterswijk:
N318 towards Aalten / Varsseveld • At the end of the N318 turn
left on the N18 (Twente route) towards Doetinchem • After nearly
800 m turn right towards Zelhem, N330 • After 60 m turn right onto
the Vlakkeeweg.
You are now at WWTP Varsseveld. Follow the parking instructions.
Zelhem:
Head for Varsseveld (through Halle) • After approx. 10 km (from
Zelhem) turn left, onto the Vlakkeeweg.
You are now at WWTP Varsseveld. Follow the parking instructions.
Varsseveld centre:
•
Follow the signs towards Doetinchem / Zelhem (Doetinchemseweg)
•
Turn right at the roundabout: Zelhemseweg • At the crossroads with
the N18 (Twente route) carry straight on towards Zelhem. • After
60 m turn right onto the Vlakkeeweg.
You are now at WWTP Varsseveld. Follow the parking instructions.
BY PUBLIC TRANSPORT:
Arnhem:
At Arnhem central station, take the train to Doetinchem / Winterswijk;
get out at Varsseveld station.
WWTP Varsseveld is approximately 4 km from the station.
Zutphen:
At Zutphen central station, take the train to Winterswijk; get out at
Lichtenvoorde / Groenlo (Lievelde) station.
WWTP Varsseveld is approximately 10 km from the station.
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The membrane bioreactor in Varsseveld is the first full-scale MBR installation
in the Netherlands en therefore a demonstration project.
The project comprises of the realization and research of the MBR and
is completed in close collaboration between:
- Rhine and IJssel Water Board;
- STOWA (Dutch acronym for the Foundation for Applied Water Research);
- DHV, Consultancy and Engineering.
The project has been made possible through a LIFE subsidy, the EU instrument
for the environment.
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