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END-O-SLUDG an innovative holistic system approach to sludge management Author: Dr. Son Le, MBE (presenting author Herman Sioen, WATERLEAU) Meeting: “La gestion innovante des boues d’épuration à l’échelle européenne” (CEME Charleroi, 22 October 2013)
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END-O-SLUDG an innovative holistic system approach to sludge management

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END-O-SLUDG an innovative holistic system approach to sludge management. Author: Dr. Son Le, MBE (presenting author Herman Sioen, WATERLEAU) Meeting: “ La gestion innovante des boues d’épuration à l’échelle européenne ” (CEME Charleroi, 22 October 2013) . AIM & OBJECTIVE. - PowerPoint PPT Presentation
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Page 1: END-O-SLUDG an innovative holistic system approach to sludge management

END-O-SLUDGan innovative holistic system approach to sludge

management

Author: Dr. Son Le, MBE (presenting author Herman Sioen, WATERLEAU)Meeting: “La gestion innovante des boues d’épuration à l’échelle européenne” (CEME Charleroi, 22 October 2013)

Page 2: END-O-SLUDG an innovative holistic system approach to sludge management

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• Aim: to have marketable sludge derivatives from sustainable processing of wastewater in a highly integrated treatment plant.

• Objective: To research, develop and demonstrate a toolkit of novel processes together with development the market and integration methodologies that can be applied for sustainable sludge management.

AIM & OBJECTIVE

Page 3: END-O-SLUDG an innovative holistic system approach to sludge management
Page 4: END-O-SLUDG an innovative holistic system approach to sludge management

EU FP7 END-O-SLUDG Project, Author: 4

5. Management and sustainability• Pathogen risk assessment • Long-term soil impact assessment • Technology assessment including LCA, EIA, SEA, Social Political and Legal • Integration methodologies and implementation strategy

2. Sludge treatment• Pre-treatments• Inverted phase fermentation• Digestion intensification• Competitive exclusion

1. Sludge reduction• Enhanced solid removal• COD removal• P removal

Sludge derivatives Struvite Ammonium phosphate Ammonium bicarbonate Neighbourly cake Bio-granule Organo mineral fertiliser

4. Market development• End-o-Waste• Product trials• Nutrient management • Economic assessment

3. Downstream processing• N & P recovery• Dewatering• Granulation• Dehydration• Nutrient formulation

5. Management and sustainability• Pathogen risk assessment • Long-term soil impact assessment • Technology assessment including LCA, EIA, SEA, Social Political and Legal • Integration methodologies and implementation strategy

2. Sludge treatment• Pre-treatments• Inverted phase fermentation• Digestion intensification• Competitive exclusion

1. Sludge reduction• Enhanced solid removal• COD removal• P removal

Sludge derivatives Struvite Ammonium phosphate Ammonium bicarbonate Neighbourly cake Bio-granule Organo mineral fertiliser

4. Market development• End-o-Waste• Product trials• Nutrient management • Economic assessment

3. Downstream processing• N & P recovery• Dewatering• Granulation• Dehydration• Nutrient formulation

Scopeof

Project

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1.1 Sludge arising from conventional works

1° sediment Tertiary treatment

Treated effluent

Sludge Sludge Sludge

Advanced treatment

Biosolids

Biogas Anaerobic digester

2° sediment

Sludge

Activated sludgeor trickling filter

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1.1 Concept of Sludge Reduction

1° sediment Tertiary treatment

Treated effluent

Sludge Sludge Sludge

Advanced treatment

Biosolids

Biogas Anaerobic digester

DAF

P sludge

BIOSORBENT

VFA

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1.3 DAF performance

Trials in The Netherlands

TSS removal from >99% COD removal from up to 80%ASP load reduction 59%

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1.4 Sorbent performance

0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1

0 20 40 60 80 100 120

Volume of Sample (ml)

Frac

tion

of C

OD

(mg/

L)

PicaBiol

NORIT 1240W

Aquasorb 200

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• Pre-treatments• Inverted phase fermentation• Digestion intensification• Competitive exclusion

2. Sludge Treatment

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2.1 Ultrasonic sonication

Initial Ultrasound Fermentation0

5000

10000

15000

20000

25000

Untreated 3579 7157 10736 13917 21074

CODs

(mg/

L)

Ultrasound pre-treatment of secondary sludge from Baíña WTP(numbers = specific energy applied, kJ/kgTS)

Ultrasonic has most pronounced effect on SAS compared to other sludge types

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2.2 Inverted Phase Fermentation

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2.3 Digestion intensification

0 10 20 30 40 50 60 70 80 90 1000

5

10

15

20

25

30

0

5

10

15

20

25

30R1 BIOGAS R1 CH4

Days

Biog

as (L

)

CH4

(L)

HRT 3d HRT 2d HRT 1.5d HRT 1d HRT 0.83d

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2.4 Competitive exclusion

1.0E+00

1.0E+01

1.0E+02

1.0E+03

1.0E+04

1.0E+05

1.0E+06

1.0E+07

1.0E+08

1.0E+09

1.0E+10

1.0E+11

0 h 48 h

Time (h)

E. c

oli

conc

entra

tion

(cfu

/g D

S)2 day control

2 day experiment

4 day control

4 day experiment

E. coli culture

Competition culture:BROM1 and E. coli

Probiotic culture

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3. Downstream Processing

Liquor treatment

High quality product for end-o-waste (OMF Manufacture)

Resource recovery (N & P)

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Product requirement:Granular, free flowing, dust free3-5mm size, >1.3 g/ccGuaranteed nutrient content

Issues:• Energy intensive process• High wearing / high maintenance• Explosion risk

3. 1 The OMF challenge

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3. 2 Two-stage OMF manufacturing process

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3. 3 First stage – Waterleau PUTTART® technology

coated pellets

incondensables

boiler

oil pump

air, fuel

cooling water

condenser

condensate to

treatment

Dry granules (>90%DS) to storage

Green granules (<65%DS)

to dehydration unit

sieve

granule recirculation

coater

LilliPutt ® pilot

granulator

granulesve

rtica

l tra

nspo

rt

sludge pump

Digested sludge cake

vapours

warm water

Nutrients(urea/TSP)

Nutrient dosing

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3. 4 second stage – Valsave THERMALOOP™ technologyTHERMALOOP™ Innovative solution for biogranule manufacture

1

5

610

1. Dehydration chamber2. Air circulator3. Air scrubber4. Water circulator5. Heat recovery unit

6. Compressor7. Air heater8. Green granules9. Biogranules10. Wastewater

2

4

7

55°C 62°C

42°C

36°C

42°C

31°C 72°C

41°C

8 9

3

THERMALOOP™ Innovative solution for biogranule manufacture

1

5

610

1. Dehydration chamber2. Air circulator3. Air scrubber4. Water circulator5. Heat recovery unit

6. Compressor7. Air heater8. Green granules9. Biogranules10. Wastewater

2

4

7

55°C 62°C

42°C

36°C

42°C

31°C 72°C

41°C

8 9

3

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3.5 OMF Pilot plant (Ellesmere Port)

Dehydration unit(artist impression)

Granulator unit

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PUTTART® VERTICAL DISC DRYER-GRANULATOR

Cold structure

Shell (insulated)

Trays

Raking arms with ploughs

Central rotating shaft

Drive

Reference plant: Poznan, Poland3 lines of each 3.1 TPH H2O evap.

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MOUNTING ON SITE

LILLIPUTT®

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IN OPERATION

LILLIPUTT®

First granules

LilliPutt® Test plant in operation

Page 23: END-O-SLUDG an innovative holistic system approach to sludge management

KEY DATA Technology: LilliPutt® Plant Capacity

Dry solids 2.4 TPD Wet Cake 12 TPD Evaporation 10 TPD N° of lines 1

Wet Sludge Data Digested secondary municipal sludge 21% dry solids

Dry Sludge Data >90% dry solids

Start of operation: November 2012 Current status: test completed, plant will be decommissioned this month Site location: Ellesmere Port, (Manchester), UK

LILLIPUTT®

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Aim: To develop a distinct knowledge base by which farmers and agriculturalists integrate OMF-based products.

Two products to be developed:Grassland application (NPK: 10-4-0)Arable crop application (NPK: 3-8-0)Note : Digested sludge = NPK 4-5-0

Market demand key factor in gaining End of Waste status

4. Market Development

Page 25: END-O-SLUDG an innovative holistic system approach to sludge management

4.1 Plot trials at Broxton (Cheshire)

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4.2 Plot trials at Broxton (Cheshire)

Deeks LK, Chaney K, Murray C, Sakrabani R, Gedara S, Le MS, Tyrrel S, Pawlett M, Read R, Smith GH (2013). Field evaluation of a sewage sludge derived novel organo-mineral fertilizer on combinable crops. Agronomy for Sustainable DevelopmentDOI 10.1007/s13593-013-0135-z

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• Product status is key aim of the OMF development• Legal status is complex• Demonstrate equivalence with existing fertilisers• Development of specifications for OMF• Continuing plot/field trials• Development of grower protocols• Engage with Regulators

4.3 End of Waste: Practical Steps

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• Sustainable, renewable sources of phosphate are required.

• OMF has the potential to fulfil market requirements• Unlike UK the application of biosolids to land is not

universally accepted by all stakeholders. E.g. Netherlands recycling is prohibited.

• END-O-SLUDG working to address these issues

4.4 End of Waste: Market Development

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CONCLUSION END-O-SLUDG aims to create a portfolio of useful new products

from sludge that meet End of Waste as part of a new concept for sewage sludge management in Europe.

This involves development of new technologies for:• Sludge volume reduction• More efficient sludge treatment• Economical downstream processing• Renewable source of P that could sustainably support crop

production

Results so far have been very promising

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Acknowledgement: The research leading to these results has received funding from the European Union Seventh Framework Programme (FP7-ENV.2010.3.1.1-2 ENV) under grant agreement N° 265269.

www.end-o-sludg.eu

Dr. Son Le, [email protected]

Herman [email protected]