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Wastewater Reclamation & Reuse PlantsWastewater Reclamation & Reuse Plants
ROReclamationReuse
MFWastewater Disinfections
Reuse
Country Location Capacity Operation Plant Membrane (m3/d) Year Supplier Supplier
i l ibi1 Kuwait Sulaibiya 300,000 2003 IONICS Toray2 USA CA Fountain Val 264,950 2004 PROJECT 3 Singapore Ulu Pandan 140,000 20044 India Chennai 135 000 1999 CAMP DRESSER4 India Chennai 135,000 1999 CAMP DRESSER 5 USA CA San Diego 75,0006 Spain Almeria 42,000 2001 PRIDESA/INIMA PERMETEC ES7 Singapore Kranji 40,000 2003 HydranauticsVEOLIA 8 Singapore Bedok 32,000 2003 Hydranautics9 Saudi Arabia Jeddah 30,000 1990 BIWATER GB DuPont 10 Korea 26,182 1996 IONICS US Dow/Filmtec 11 Singapore Seletar 24 000 2003 Tora
HYFLUX
HYFLUX
(Nov 2003 :Based on IDA Inventory Report 2002)
11 Singapore Seletar 24,000 2003 Toray12 Japan 22,984 1983 KURITA JP Toray13 USA AZ Scottsdale 22,710 1998 ADVANCED ES USA Koch
HYFLUX
Toray less-fouling RO was selected at the world’s largest RO plantToray less-fouling RO was selected at the world’s largest RO plant
(Nov. 2003 :Based on IDA Inventory Report 2002)
공학한림원 선정 미래유망 기술 25선정근거 : 산업의 규모 전략적 측면 사회적 영향
구 분 내 용 구 분 내 용∙ 지능형 텔레매틱스 ∙ 환경기계기술
선정근거 : 산업의 규모, 전략적 측면, 사회적 영향
전기전자정보공학 기계공학
∙ 지능형로봇 ∙ 초미세 부품 장비∙ 차세대 반도체 ∙ 신․재생에너지 (풍력발전, 연료전지)∙ IPTV ∙ 로봇기술∙ 광대역 유․무선 통합 통신망 기술 ∙ 하이브리드 자동차▶ 분리막 생물반응조 공정
(MBR : Membrane ∙ 차세대 디스플레이용 (고분자)소재
건 설환경공
학
(M R MembraneBioreactor)
화 학생명공학
∙ 신에너지(석탄액화․가스화, 연료전지, 수소에너지)∙ 고성능콘크리트
∙ U-건설현장 관리 제어 시스템 ∙ 소재혁명, 나노 기술학 U 건설현장 관리 제어 시스템 소재혁명, 나노 기술∙ 실시간 버스통행거리 및 환승횟수 판단 기술 ∙ 차세대 전지용(고분자)소개
∙ 지속가능 건축시스템 기술 ∙ 재생에너지
재 료
∙ 고질소 오스테나이트계 스테인리스강∙ 염료 감응형 유기 태양전지∙ 초내식성 지르코늄핵연료 피복관 개발
출처 한국공학한림원, “미래기술전략 보고서”, 2006
자원공학 ∙ 화염분무열분해법(FSP)을 이용한나노분말 제조기술
∙ 반도체 조명 기술
2006.12
Membrane Market for Water Treatment
Water treatment Wastewater treatment
160 M$ → 330 M$(2010) (2016)
460 M$ → 900 M$(2010) (2016)
분리막Membrane
Seawater Desalination Water Reuse450 M$ → 800 M$ 120 M$ → 390 M$
(2010) (2016) 120 M$ 390 M$(2010) (2016)
시장규모: 100 200 % 증가시장규모: 100~200 % 증가(2010~2016)
Global European MBR market
65 new refs/year
Total Municipal in EuropeAbout 2 millions e.p (0.5% population)
45 new refs/year
30 new refs/year
European New-Comers ?
40 40
Distribution of MBR plants per capacity (m3/d) and supplier – All applications
25
30
35
40KubotaGEOther (EU)Toray
52005
25
30
35
402008
Mitsubishi
10
15
20
10
15
20
0
5
[100-500[ [500-2 000[ [2 000-10 000[ [10 000-50 000[
0
5
[100-500[ [500-2 000[ [2 000-10 000[ [10 000-50 000[
• A3 Water Solutions• Berghof• Huber
•Microdyn Nadir• Norit – X-Flow• Novasep• Huber
• Koch-Puron• Martin Systems
• Novasep• SFCU• Weisse WSMartin Systems Weisse WS• Wehrle Umwelt
정수처리용정수처리용
분리막분리막
(중수도)
하폐수 유입 MBR 여과수여과수
(음용수)
분리막분리막
하폐수처리용하폐수처리용
분리막분리막
한강 원수
분리막분리막
미생물
분리막 생물반응조분리막 생물반응조(MBR, membrane bioreactor)
현재 MBR 시스템의 단점 및 핵심장애물 (생물막 형성)
(중수도)
하폐수 유입 MBR 여과수
RO 여과수
(음용수)
역삼투막(RO)
RO 공정정밀여과막(MF)
/ 한외여과막(UF)“생물막(Biofilm)”
RO 공정
MBRMBR 시스템의시스템의 핵심핵심 장애물장애물활성슬러지 반응조
MBR 분리막 표면투수도(Water flux) 감소
MBR MBR 시스템의시스템의 핵심핵심 장애물장애물
여과수 (Permeate)
낮은낮은 투수도투수도 : 10~20 L/m: 10~20 L/m22⋅⋅hh짧은짧은 막막 수명수명 : 3: 3 55 년년 높은 설치비 및짧은짧은 막막 수명수명 : 3: 3--5 5 년년높은높은 에너지에너지 소모소모 : 0.3~0.6 kWh/m: 0.3~0.6 kWh/m33
높은 설치비 및운전비
Scanning electron micrographs (SEMs) of individual cells and microcolonies growing on the permeate (product water) surfaces of polyester Texlon fibers of cellulose acetate (CA) reverse osmosis (RO) membranes. The membranes were fed with a pretreated municipal wastewater at Water Factory 21 in Orange County, California. Note the copius production of extracellular polymeric substances (EPS) by the attached bacteria,especially those cells associated with the larger microcolonies. Such EPS mediates early cell attachment and physically stabilizes and protects the biofilm.
Membrane Fouling & TMP Rise-up in submerged MBR
At constant flux (J) TMP
Chemical Recovery Cleaning60kPa
ChemicalC e caBackwashing
Physical Backwashing
30kPa
Step 1Step 1gradual increase in ΔP
Step 2Step 2rapid increase in ΔP
Operating time
Analysis of MBR Operating Cost
Membrane 15%
8%
Chemicals
Membranereplacement
15%
√√
Equipment
Energy40%√gy
37%√
√ ; Directly Related to Biofilm
Biofiouling Control methods over last 20 years
BiofoulingBiofoulingBiofoulingBiofouling
Engineering Material Chemical Biologicalg gapproaches
• Critical flux
approaches
• New material
approaches
• Chemical additives
approaches
• Analysis of biofilm• Module design
• Hydrodynamics• Membrane modification
Chemical additives
• Activated carbon
Analysis of biofilm
• SRT, DO
출처 Yun et.al. Wat. Res (2006)Biofouling in lab. Scale MBR
((높은높은 투수도투수도))((낮은낮은 투수도투수도))
MembraneMembrane
270270 μm
MembraneMembraneMembraneMembrane
270 270 μm
70 70 μm
CLSMCLSM ––CLSM CLSM Image AnalysisImage Analysis
Textural parameters Volumetric parameters
Porosity TexturalEntropy
Biovolume(×105μm3)
AXRL(μm)
AYRL(μm)
AZRL(μm)
High DO 0.78(±0.07)
7.24(±0.30)
3.3 (±0.9)
1.34(±0.30)
1.31(±0.30)
6.85(±2.67)
Low DO 0.63(±0.04)
8.08(±0.60)
2.1(±1.6)
1.52(±0.38)
1.49(±0.37)
3.33(±1.23)
Does microbial physiology affect membrane biofouling in MBR ?
Membrane Unit
Activated SludgeReactor
Permeate(Effluent)Influent
Retentate
Microbial Physiology vs. MBR Performance
Morphology of microbial flocs in MBR
• Pin point floc (left)• Pin point floc (left)• Bulking sludge (right)• Normal activated sludge (center)• Normal activated sludge (center)
Effect of floc morphology on biofouling
100
Side stream MBR
80
90
100
Normal Sludge
Pi i Sl d
60
70
w(%
)
Pin point Sludge
Bulking Sludge
40
50
J/Ji
w
10
20
30
0
10
1 2 3 4 5Concentration Factor
Fig. 3b Flux declines according to floc structures during ultrafiltration of activated sludge with PM30 membrane
Effect of foaming activated sludge on biofouling
Side stream MBR
YM30 Membranes
Side stream MBR
8090
100
Non-FoamingFoaming1
506070
Foaming1Foaming2
20304050
01020
1 2 3 4 5
Concentration Factor
In-Soung Chang and Chung-Hak Lee“Effect of physiological states of activated sludge on membrane fouling”
Desalination, (1998) 120, 221-233
bers
4545Citation no. since 1998: 249
Num
b
30
35
40 35 34
29 30
ation
15
20
25
30
1721 20
Cit
0
5
10
15
1
63
8
0
Yamamoto K et al (1989) Water science and technology 21 43-54Yamamoto K, et al. (1989), Water science and technology, 21, 43 54Citation no. since 1989: 276
Analysis & Control of Biofouling in MBR
Microbiological Biofilm formation mechanism(Quorum sensing etc )
Analysis & Control of Biofouling in MBR
Approach (Quorum sensing, etc.)Cell physiology& morphologyMicroorganism population dynamics (FISH, etc.)
Membrane Fouling
dynamics (FISH, etc.)
Membrane Fouling
PhysicochemicalApproach
HydrodynamicApproach
Membrane materialsMembrane surface modificationHybrid system
Flow regime: (side stream vs. submerged )Module type:y y
Chemical additivesSurface chemistry
(tubular, plate,holow fiber)Critical flux
Control of biofoulingg
Options available for submerged systems:Options available for submerged systems:1) Reduce flux (J)2) Increase membrane aeration2) Increase membrane aeration3) Employ physical or chemical cleaning
backflushing (HF only)– backflushing (HF only)– relaxation (ceasing permeation whilst continuing aeration)– in situ clean (chemically enhanced backwash)– in-situ clean (chemically enhanced backwash)– ex-situ clean (soak)
4) Patterned membrane5) Qurorum Quenching5) Qurorum Quenching
Results of Membrane Results of Membrane BiofoulingBiofouling (MBP) Assay(MBP) Assay* Fouling : Deterioration of membrane performance caused by stains
Bad Surface(Orange County water district: Dr.Ridgway)
0.12
0.14
疎水性微生物( )
(High attachment) 600nm
ROra
tio)
Cross section
Mycobacteria(h d h bi ll f )
0.08
0.10
Ratio
(Mycobacteria)
親水性微生物(Flavobacteria)
men
t (B
/F r
Surface
(hydrophobic cell surface)Flavobacteria(hydrophilic cell surface)
0.04
0.06
B/F
600nm
L f li ROeria
l Atta
chm
Cross section
0.00
0.02Standard level(Cellulose Acetate Membrane)
Low-fouling RO
Good(Low attachment)
Bac
te
0.00RO Low-fouling RO
(Cellulose Acetate Membrane)(Low attachment)
Toray less-fouling RO membrane has extremely low bacteria attachment
Toray less-fouling RO membrane has extremely low bacteria attachment
Challenge to the current membrane technology
Desired Membrane Technology
1) Hi h fl1) High flux2) High selectivity3) Long life span4) Less fouling) g5) Low energy
Conventional thinking
Creative imaginationthinking imagination
1) FoulingCurrentmembrane Technology
1) Fouling2) High energy3) Tortuous pores4) Wide range of pore sizes
Possible mechanisms for the TMP rise
“Factors affecting the membrane performance in submerged membrane bioreactor”“Factors affecting the membrane performance in submerged membrane bioreactor”Factors affecting the membrane performance in submerged membrane bioreactorFactors affecting the membrane performance in submerged membrane bioreactorJournal of membrane science, Vol 284. 54-66
Zhang, Fane, et.al. (2006)
Quorum Sensing ?
G b h iMi bi l it
Symbiosis
Group behaviorsMicrobial community
Symbiosis
Virulence
C tCompetence
Conjugation
Antibiotic production
MotilityMotility
Sporulation
Biofilm formation
: Signal molecules (autoinducer)
: Bacteria
Creative discovery occurs at the intersection !
“ Mr. Suzuki, The theory of relativity occurred to me by intuition, and Mr. Suzuki, The theory of relativity occurred to me by intuition, and music is the driving force behind this intuition. My parents had me study the violoin from the time I was six. My new discovery is the result of musical perception ” – Albert Einstein-of musical perception. – Albert Einstein-
Ph i ArtPhysics Art (music )
Theory of Relativity
Shinichi Suzuki (1898-1998)Albert Einstein (1879-1955)Relativity
Dual Phases in TMP rise up in MBR: Slow and then Rapid rise up
TM
PTM
P
Step 1Step 1
gradual increase in ΔP--------------------TT
Step 2Step 2
TimeTime
Rapid increase in ΔP
Quorum Sensing
We can not avoid the 2We can not avoid the 2ndnd phase TMP risephase TMP rise--up even under the critical fluxup even under the critical flux
Quorum quenching based biofouling control in MBR
• Low flux• High energy• Short life-span
BiofilmMembrane
p
Membrane
XX • High flux• Low energy• Long life-spanLong life span
Molecular level(Destruction of autoinducer)
Micro-scale(membrane-biofilm)
Engineering system(Uproot of Biofouling)
K.M. Yeon, C.H.Lee et al., Environmental Science and Technology, 43 ,380-385, 2009
The Little David defeated the Giant Goliath !from the Old Testament- from the Old Testament -
• Low flux• High energy
BiofilmM b
High energy• Short life-span
Membrane
XX • High flux• Low energy• Long life-span
Nano size molecules 100.000 ton /day MBR PlantNano size molecules 100.000 ton /day MBR Plant
First Announcement and Call for PostersFinal MBR-Network Workshop
“Salient outcomes of the European R&D j t MBR t h l “
Organised By:
projects on MBR technology“
Sponsored By:
www.MBR-Network.eu
ed
nce
Berlin Germany31 March – 1 April 2009
Hosted By: Spe
cial
isC
onfe
ren
Berlin, Germany
Abstract submission: [email protected]: 30 September 2008
Hosted by Trade Fair « Wasser Berlin 2009 »Hosted By: S C
EU Projects for the next generation membrane technology(2005~ 2009)(2005 2009)
- Green Lead Markets in Asia as well as in Europe
i) MEDINA (Desalination, )
ii)ii) EUROMBRA EUROMBRA ((MBRMBR, 10 , 10 countries )countries )
iii)iii) AMEDEUS AMEDEUS ((MBRMBR, 6 , 6 countries )countries )
iv)iv) MBRMBR--TRAIN TRAIN ((MBRMBR, 7 , 7 countries )countries )
) PURATRET) PURATRET 1010v) PURATRET v) PURATRET ((MBRMBR, 10 , 10 countries )countries )
- Japan restarts MBR Project
Paper Publication
1) Environmental Science and Technology, Vol. 43 (No.2), 380–385, 2009.
2) E i t l S i d T h l V l 43(N 19) 7403 7409 20092) Environmental Science and Technology, Vol.43(No.19), 7403-7409, 2009
3) Environmental Science and Technology, Vol.45, 1601-1607, 2011.
4) Environmental Science and Technology, Vol. 46, 4877-4884, 2012.
5) J. of Membrane Science, Vol. 411-412, 130-136, 2012.
6) Applied Microbiology and Biotechnology in press, 2012.) pp gy gy p ,
Patent
1) Korean Patent: 10-0981519, (Sept. 3, 2010)) , ( p , )
2) US Patent: 07867392, 2011-1-11 )
3) PCT Application/KR2009/006608, (Nov. 11, 2009)
4) Korean Patent Application 10-2010-0101114 (Oct.15, 2010)
5) Korean Patent Application 10-2011-0053850 (Jun.3, 2010)