Sludge handling in Bottrop
Sludge handling in Bottrop
Sludge handling in Bottrop
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<strong>Sludge</strong> <strong>handl<strong>in</strong>g</strong> <strong>in</strong> <strong>Bottrop</strong><br />
Dr.-Ing. K.-Georg Schmelz<br />
Emschergenossenschaft / Lippeverband<br />
Essen, Germany
<strong>Sludge</strong> <strong>handl<strong>in</strong>g</strong> <strong>in</strong> <strong>Bottrop</strong><br />
Structure<br />
1 Introduction<br />
2 <strong>Sludge</strong> network system<br />
3 Production of fuels on a sewage sludge basis<br />
- coal-polymer condition<strong>in</strong>g<br />
- trials us<strong>in</strong>g different high calorific fractions<br />
- shredder fluff<strong>in</strong>g agglomerate-polymer condition<strong>in</strong>g<br />
4 <strong>Sludge</strong> <strong>in</strong>c<strong>in</strong>eration <strong>in</strong> fluidised bed furnances<br />
5 Summary and conclusions
Where we are work<strong>in</strong>g
Where to f<strong>in</strong>d our wastewater treatment plants
EMSCHERGENOSSENSCHAFT and LIPPEVERBAND<br />
two water associations with wide experience<br />
• The EMSCHER Association founded <strong>in</strong> 1899<br />
• The LIPPE Association founded <strong>in</strong> 1926<br />
• EG and LV are two of the largest water associations<br />
<strong>in</strong> Germany<br />
Total area:<br />
Wastewater:<br />
4 248 square kilometres<br />
approx. 6 million PE
<strong>Sludge</strong> pressure pipel<strong>in</strong>es<br />
8 km<br />
20 km<br />
Folie 6
2 <strong>Sludge</strong> network system<br />
• Three WWTPs are connected:<br />
- Alte Emscher Duisburg: 500,000 PE<br />
- Emscher Mouth TP: 2,400,000 PE<br />
- <strong>Bottrop</strong> WWTP: 1,340,000 PE<br />
• The sludge of the three WWTPs is treated at the<br />
Central <strong>Sludge</strong> Treatment Plant <strong>in</strong> <strong>Bottrop</strong><br />
• 60,000 tons dry matter per year<br />
• Condition<strong>in</strong>g, dewater<strong>in</strong>g, <strong>in</strong>c<strong>in</strong>eration
Digestion<br />
Inc<strong>in</strong>eration<br />
Waste Water<br />
Treatment<br />
River Emscher<br />
Condition<strong>in</strong>g 1<br />
add<strong>in</strong>g coal<br />
Condition<strong>in</strong>g 2<br />
add<strong>in</strong>g polymers<br />
+ Dewater<strong>in</strong>g
3 Production of fuels on a sewage sludge basis<br />
• The production of fuels from sewage sludge is caused<br />
by history<br />
• The wastewater <strong>in</strong> the Emscher area was characterised<br />
by coal load<strong>in</strong>gs from the m<strong>in</strong><strong>in</strong>g companies<br />
• So the sewage sludge had a high f<strong>in</strong>e coal portion<br />
(up to 30 % of the dry matter)<br />
• The dewaterability on filter presses was very good<br />
(up to 50 % dry solids <strong>in</strong> the filter cake)<br />
• The dewatered sludge could be used as a fuel <strong>in</strong><br />
a power station <strong>in</strong> the neighborhood
3 Production of fuels on a sewage sludge basis<br />
• S<strong>in</strong>ce the late seventies of the last century the coal<br />
m<strong>in</strong><strong>in</strong>g <strong>in</strong> the Emscher area decreased rapidly<br />
• The content of f<strong>in</strong>e coal <strong>in</strong> the wastewater also<br />
decreased<br />
• In the early eighties coal admixture facility<br />
• Cont<strong>in</strong>ue produc<strong>in</strong>g a fuel from sewage sludge<br />
• Inc<strong>in</strong>eration <strong>in</strong> 2 new fluised bed furnances
3 Production of fuels on a sewage sludge basis<br />
- previous system (coal-polymer condition<strong>in</strong>g)<br />
• For an autonomous <strong>in</strong>c<strong>in</strong>eration <strong>in</strong> the fluised<br />
bed <strong>in</strong>c<strong>in</strong>erators the dewatered sludge must have:<br />
- calorific value: 4,400 kJ/kg (wet material)<br />
- water content: 55 – 60 % by weight<br />
- Ashes content: 45 % by weight<br />
• So it was necessary to add 20 – 25 % f<strong>in</strong>e coal<br />
• mixture of hard coal and lignite<br />
• Particle size: 0 – 2 mm
3 Production of fuels on a sewage sludge basis<br />
- previous system (coal-polymer condition<strong>in</strong>g)<br />
Condition<strong>in</strong>g 1 Condition<strong>in</strong>g 2<br />
DS = 20 %
3 Production of fuels on a sewage sludge basis<br />
- trials with various high calorific value fractions<br />
• Aim: replace the primary energy carrier coal<br />
• trials us<strong>in</strong>g other high calorific value materials<br />
- recycl<strong>in</strong>g materials (e. g. plastics)<br />
- renewable raw material (e. g. sawmill waste)<br />
• a lot of materials were suitable for condition<strong>in</strong>g<br />
and dewater<strong>in</strong>g<br />
• best results we got with shredder fluff<strong>in</strong>g<br />
agglomerate (made from old cars)<br />
<br />
see the next slides
Recycl<strong>in</strong>g of old cars: the situation today<br />
Liquids out/<br />
Demontage<br />
Shredder<br />
Waste<br />
• Let out all liquids<br />
• Take away battery, tyres<br />
• Take out spare parts<br />
• Press<strong>in</strong>g the body<br />
Spare parts<br />
Recycl<strong>in</strong>g<br />
Scrap steel<br />
• ma<strong>in</strong> gr<strong>in</strong>d<strong>in</strong>g<br />
• iron separation<br />
• non-iron separation<br />
Iron scrap<br />
Non iron metals<br />
SHF<br />
(Shredderheavy<br />
fraktion)<br />
50% 50%<br />
50% 50%<br />
SLF<br />
(Shredderlight<br />
fraktion)<br />
About 20% of<br />
the weight of the car<br />
are go<strong>in</strong>g to landfill<br />
From 2015 <strong>in</strong> the EU only 5% are allowed to be discharged
The Volkswagen-SiCon-Process for Shredderfluff<strong>in</strong>g<br />
Treatment<br />
Shredder-Material<br />
Shredder-Material<br />
Ma<strong>in</strong> process of treatment<br />
Fe NE Raw granular Raw fluff<strong>in</strong>g Raw sand<br />
Special treatment for different costumers<br />
granular fluff<strong>in</strong>g sand rest<br />
disposal<br />
Recycl<strong>in</strong>g (e.g. PVC)<br />
NE-metal production, ...<br />
Sewage sludge dewater<strong>in</strong>g, ...<br />
Blast furnance, ...
3 Production of fuels on a sewage sludge basis<br />
We have the follow<strong>in</strong>g requirements to the material:<br />
• a good dewater<strong>in</strong>g result (>40 % DS)<br />
• a calorific value of more than 4,400 kJ/kg wet sludge<br />
• no additional load <strong>in</strong> the filtrate water<br />
• no additional emissions from the <strong>in</strong>c<strong>in</strong>eration<br />
• no worsen<strong>in</strong>g of the ashes<br />
• as possible no changes of the exist<strong>in</strong>g system<br />
• low costs<br />
• availability over a long period <strong>in</strong> future<br />
• the exist<strong>in</strong>g disposal ways must be possible
Delivery and mix<strong>in</strong>g of the condition<strong>in</strong>g products<br />
Mix<strong>in</strong>g bas<strong>in</strong> situated <strong>in</strong> by-pass<br />
Mix<strong>in</strong>g bas<strong>in</strong><br />
at time<br />
<strong>in</strong> future
3 Production of fuels on a sewage sludge basis<br />
- new system (SA-polymer condition<strong>in</strong>g)<br />
Shredder<br />
agglomerate<br />
X
Filter cake with Shredder Fibres
3 Production of fuels on a sewage sludge basis<br />
- new system: results from the large scale trial<br />
• Dewater<strong>in</strong>g result could be improved<br />
(+2 to +5 %-po<strong>in</strong>ts!)<br />
• The fluff<strong>in</strong>g material can be mixed <strong>in</strong>to the sludge<br />
nearly as easy as the coal (dust)<br />
• The stripp<strong>in</strong>g behaviour of the filter cake from<br />
the filter presses was very good<br />
• combustion performance: no changes, normal<br />
• filtrate water: no higher concentrations<br />
• flue gas: no <strong>in</strong>creased emissions
4 <strong>Sludge</strong> <strong>in</strong>c<strong>in</strong>eration<br />
fluidized-bed furnance<br />
steamer<br />
400°C, 40 bar<br />
2 x 7.0 t/h<br />
waste gas wash<strong>in</strong>g<br />
chimney<br />
sludge<br />
2 <strong>in</strong>c<strong>in</strong>erators<br />
each 7.0 t/h<br />
turb<strong>in</strong>e<br />
2.7 MW<br />
filter for<br />
ashes<br />
wash<strong>in</strong>g-zone for<br />
heavy metals
Schlammanfall
4 <strong>Sludge</strong> <strong>in</strong>c<strong>in</strong>eration and disposal of ashes<br />
• <strong>in</strong> the past: ashes are used to produce m<strong>in</strong><strong>in</strong>g mortar<br />
for fill<strong>in</strong>g underground hollow spaces from m<strong>in</strong><strong>in</strong>g<br />
• today: build<strong>in</strong>g material for road construction<br />
• <strong>in</strong> future: store the phospherous-rich ashes <strong>in</strong> monodump-sites<br />
to recover the phospherous later (when<br />
the recycl<strong>in</strong>g methods are further developed and<br />
economic)
5 Summary and conclusions<br />
• Emschergenossenschaft and Lippeverband are<br />
two of the largest water associations <strong>in</strong> Germany<br />
• the production of fuels from sewage sludge is<br />
caused by history (coal m<strong>in</strong><strong>in</strong>g)<br />
• the content of f<strong>in</strong>e coal <strong>in</strong> the wastewater (and the<br />
sludge) makes it possible to produce a fuel for<br />
power stations<br />
• coal m<strong>in</strong><strong>in</strong>g decreased rapidly s<strong>in</strong>ce the seventies<br />
• from the eighties f<strong>in</strong>e coal must be added to the<br />
sludge to go on <strong>in</strong> fuel production from sludge<br />
• the aim today is to replace the coal through<br />
recycl<strong>in</strong>g or renewable raw materials
5 Summary and conclusions<br />
• the use of shredder fluff<strong>in</strong>g agglomerate for<br />
condition<strong>in</strong>g seems to make it possible to replace<br />
the coal by a recycl<strong>in</strong>g product<br />
• Advantages for both sides:<br />
- the car-<strong>in</strong>dustry<br />
- Emschergenossenschaft
Thank you for your attention!