Zuivering. Gertjan Medema Cursus drinkwatermicrobiologie 2012
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1 Zuivering Gertjan Medema Cursus drinkwatermicrobiologie 2012
2 Elimination in water treatment Two principal processes: Inactivation - Natural (biological) - Forced: disinfection (chemical, physical) Removal - Sieving (ultra/nanofilters) - Attachment (sand filters, soil, ceramic filters) - Flocculation + floc removal 2
3 Virus structure Virus genome (RNA, ss/ds DNA) Capsid protein Spike 3
4 Inactivation 4
5 Virus inactivation in the environment Physical Heat or thermal effects Desiccation or drying Aggregation Adsorption to particles or surfaces Encapsulation or embedding Increasing inactivation at higher temperature; pasteurize Increased inactivation at lower moisture content or relative humidity; effects of RH differ between enveloped and non-enveloped viruses Clumping protects viruses from inactivating agents Adsorption protect viruses from inactivating agents; some specific chemical surfaces (heavy metals) are virucidal Viruses within membranes or larger particles are protected from inactivation Chemical Hydrogen ions; ph Viruses survive best near neutral ph and worst at ph extremes Organic matter Many viruses are stabilized and protected by dissolved, colloidal and solid organic matter, including fecal organics and natural organic matter (humic materials) Ammonia NH 3 has virucidal activity; manifest at higher ph (>ph 8) Salts and Ionic Strength Increased concentrations of salts are antiviral; some viruses are destabilized and inactivated by water lacking stabilizing salts (such as NaCl) ions such as Mg++ Enzymes Proteases and nucleases contribute to virus inactivation Biological Microbial activity Proteolytic activity Microbial predation Biofilms Biological treatment and microbial activity/metabolism in soils, sediments, water; several contributing mechanisms Proteolytic enzymes inactivate/denature virion proteins Engulfment, ingestion, etc. by protozoa, helminths, etc. Virus adsorption to biofilms can be protective or microbial activity in biofilms can cause virus inactivation and degradation 5
6 Principles of ozone process Ozone = strong oxidator Disruption of cell wall and reaction with nucleotides/enzymes: no reproduction At room temperature: ozone in gas Dosage of gas bubbles with diffusor Disinfection: contact time T of micro-organisms with ozone concentration C CT is design parameter (mg*l -1 min -1 ) 6
7 Ozone process in practice In Concrete construction C out Contact time T Ozone gas C in Inactivation versus CT 7
8 Inactivation kinetics: quantifying Decimal Elimination Capacity Inactivation (log) Chick-Watson: N T k* C * T N e 10 log( N T n ) k * C T N * CT mg*l -1 *min -1 8
9 Inactivation kinetics: variability Inactivation (log) Shoulder model: delayed inactivation Non-linear model: influence of conditions (microbial and technological aspects) CT mg*l -1 *min -1 9
10 Inactivation of viruses, bacteria, bacterial spores and protozoan oocysts Inactivation (log) Oocysts of Cryptosporidium parvum Spores of Clostridium perfingens Viruses, Bacteria Environmental spores surrogate full-scale performance? CT ((mg ozone /l)*min) 10
11 k-value of some micro-organisms k-value (log10 inactivation rate constant) E.coli Viruses USEPA 1991 Giardia USEPA 1991 Spores of Clostridium perfringens Oocysts of Cryptosporidium Temperature 11
12 E. coli concentration (CFP/l) Lab is not practice: ozone example Ozonation CT 2 mg.min/l Expected E. coli inactivation: >>5 logs Full scale E. coli data: 1000 E. coli present in 4% of samples after ozone Removal 2.7 log Ozone in Ozone out 0.01 Dec-02 Mar-03 Jun-03 Oct-03 Jan-04 Apr-04 Aug-04 Nov-04 12
13 Oxidation HOCl, O 3, OH et al Inactivation Concentration Time Temperature ph Organic compounds Inorganic compounds Virus type Virus protection 13
14 UV UV UV intensity Time Reactor Lamp type UV absorption Virus type Virus protection 14
15 Principles UV disinfection 15
16 UV sensitivity organisms: determined under well-defined batch conditions Collimated beam apparatus Inactivation Inactivation kinetics First order process inactivation rate constant k Tailing Shoulder UV-dose (mj/cm 2 ) 10 log( N t ) k * N Fluence 16
17 Inactivation (log) UV sensitivity of viruses: examples 8 7 Poliovirus 7 studies 8 7 Adenovirus 5 studies, type 2,15,40, UV-fluence (mj/cm 2 ) 2 UV-fluence (mj/cm) 17
18 Log inactivation UV sensitivity of viruses (in collimated beam experiments) UV dose (mj/cm2) Poliovirus 1 (ssrna) Rotavirus SA11 (ssdna) Hepatitis A (ssrna) Coxsackie B5 (ssrna) Calicivirus bovine (ssrna) Adenovirus 40 (dsdna) 18
19 K-values of pathogenic micro-organisms Campylobacter jejuni Vibrio cholerae Shigella dysenteriae Yersinia enterolitica Campylobacter jejuni E. coli O157 Salmonella typhi Legionella pneumophila Giardia muris Cryptosporidium parvum Hepatitis A Calicivirus Poliovirus Coxsackie virus Rotavirus Adenovirus k-value (cm 2 /mj) Bacteria Susceptible Protozoa, viruses Less susceptible
20 Validation No legal requirement for validation of UV (or other) treatment systems in municipal water supply Water utility determines need for and strictness of validation Review by Inspectorate 20
21 Example 1: UV/H 2 O 2 PWN UV/H 2 O 2 system for disinfection and oxidation of micropollutants / NOM Fluence for oxidation 560 mj/cm 2 Fluence required for disinfection 120 mj/cm 2 System design: even at extremely low UVT (80%, 1 cm) and maximum flow at end of lamp life (80%) >120 mj/cm 2 Photo: PWN 21
22 Example 1: UV/H 2 O 2 Validation of disinfection PWN Experiments to determine inactivation of: Cryptosporidium (CB and pilot scale, collaboration of PWN, University of Alberta): > 4.8 log inactivation at 120 mj/cm 2 Giardia (CB, collaboration of PWN, University of Alberta) > 3.4 log inactivation at 120 mj/cm 2 Campylobacter (CB, see previous): >> 7.6 log inactivation at 120 mj/cm 2 Photo: PWN MS2 (CB, pilot scale, PWN): 4.2 log at 120 mj/cm 2 22
23 REF (mj/cm 2 ) Example 1: UV/H 2 O 2 Validation of reactor and fluence PWN Biodosimetry data of 2 10L30 systems in series show very good results REF avg = * dosimeter dose L30 reactors in series are expected to give superior performance REF 95CL = 0.982* dosimeter dose Dosimeter fluence (mj/cm 2 ) Data: Evides, PWN, Trojan, KWR 23
24 Example 2: UV as primary disinfection New reactor system Required fluence: 70 mj/cm 2 Biodosimetry at full scale Test unit constructed at water utility Local test water (with/without UVT reducer) 24
25 Bioassay setup Challenge vessel By-pass pump Dosing pump microbes Dosing pump coffee By-pass of feed water Vd Veer, Evides 25
26 REF (mj/cm 2 ) REF (mj/cm 2 ) Example 2: UV as primary disinfection REF mean = * dosimeter REF 95%CL = * dosimeter UVT 88 UVT 82 UVT Ca lcula 30te d flue 40nce, sce 50 na rio 60 2 (mj/cm 70 2 ) Dosimeter fluence (mj/cm 2 ) Medema & Beerendonk, 2005, in collaboration with Kruithof, van der Veer, Martijn, Dekker, Nugteren, Lem, van Loon (Evides, PWN, Trojan, Aqualab) Small scatter, slope > 1 and intercept > 0; 95%CL = ideal line: safe dosing without overdosing 26
27 REF (mj/cm 2 ) On-line monitoring of UV system performance Components Trojan UVT monitor Picture: Trojan UV CFD based UV fluence model REFmean = * dosimeter Flow meter UV sensor 30 REF95%CL = * dosimeter Dosimeter fluence (mj/cm 2 ) Biodosimetry to calibrate UV fluence model 27
28 Use of biodosimetry in process control in practice: the heart of the Water Safety Plan Inputs from online readings: Flow UVT UV intensity Microprocessor / PLC Calculate Reduction Equivalent Fluence 35 msec PLC Control lamp power Photo: P. Oostdam, Evides 28
29 Ultra/nanofiltration Virus elimination Removal: sieving 27 nm 29
30 Virus elimination filters Removal: attachment Electrostatic interactions Hydrophobic interactions - Virus characteristics pi capsid composition capsid structure - Particle composition composition electric charge structure - Matrix composition organic matter bivalent cations conductivity 30
31 Virus elimination Removal: flocculation Ca Ca Electrostatic interactions Hydrophobic interactions - Virus characteristics pi capsid composition capsid structure - Particle composition composition electric charge structure - Matrix composition organic matter bivalent cations conductivity 31
32 Coagulatie + snelfiltratie 32
33 Proefopstelling AKF locatie Berenplaat water na coagulatie/dlf Kool: Chemviron F400 Geen spoeling Filtratiesnelheid: 5 m/uur Contacttijd: 12 minuten 33
34 Concentratie (PFU.l Verwijdering van MS2 bacteriofagen -1 ) Verse AK in Verse AK uit Beladen AK in Beladen AK uit Dosering , Tijd (uren) 34
35 Concentratie (CFU/l) Verwijdering van E. coli en Clostridium-sporen E. coli SSRC Verse AK in Verse AK uit Beladen AK in Beladen AK uit , , Tijd (uren) 35
36 Concentratie (CFU/l) Verwijdering van Giardia en Cryptosporidium Cryptosporidium Giardia ,1 0,1 0,01 0,01 0, , Tijd (uren) Verse AK in Verse AK uit Beladen AK in Beladen AK uit 36
37 Verwijdering van micro-organismen DEC of logverwijdering van: Verse kool Beladen kool kolom 1 kolom 2 kolom 1 kolom 2 MS2 0,0 0,0 0,0 0,0 E. coli 0,0 0,1 0,3 0,3 Clostridium 0,4 0,6 0,4 0,4 Cryptosporidium 2,7 2,7 1,3 1,1 Giardia 2,1 2,0 2,1 2,2 37
38 Verwijdering natuurlijke indicatorbacteriën - onderzoek met grote volumes Lage concentraties indicatorbateriën in influent en effluent van het koolfilter Onderzochte volumes: liter Concentraties bepalen met: - Hemoflow (cross flow ultrafiltratie) 38
39 Verwijdering gedoseerde vs. natuurlijke organismen DEC of logverwijdering van: Verse kool Beladen kool kolom 1 kolom 2 kolom 1 kolom 2 E. coli gedoseerd 0,0 0,1 0,3 0,3 E. coli natuurlijk 0,4 0,4 1,1 1,0 Sporen gedoseerd 0,4 0,6 0,4 0,4 Sporen natuurlijk 1,1 1,0 0,9 0,9 Hypothese: pre-coagulatie bevordert de verwijdering door betere hechting 39
40 Micro-organism elimination in water treatment NL Inactivation Ozone UV UV/peroxide Chlorine dioxide Chlorine (safety) Removal Soil passage Membrane filtration (UF/NF) Sand filtration Flocculation/floc removal/filtration Reservoirs 40
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