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Chlorine Dioxide as a Successful Antifoulant Treatment in a Large ...

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CHLORINE DIOXIDE CHARACTERISTICSCHARACTERISTICSSUITABLE FOR:b io cid a l a ct iv ity %10090807060504030201 0045678p Hchlor<strong>in</strong>edioxide9chlor<strong>in</strong>e1011The biocidal activityis constant over thepH 6 - 9u sea water once-throughcool<strong>in</strong>g system (pH 8.5)u recirculat<strong>in</strong>g cool<strong>in</strong>gwater system (pH > 8)HHNHHONo reaction withammonia and ureau fertiliser & ammonia plantcool<strong>in</strong>g systemu w<strong>as</strong>te waterOClOrganicONo reaction withorganic matterand oilu ref<strong>in</strong>ery and petrochemicalcool<strong>in</strong>g systemu seawater desal<strong>in</strong>ation plantOCl


CHLORINE DIOXIDE CHARACTERISTICSCHARACTERISTICSSUITABLE FOR:OTTHMspecursorsClONo formation ofhalogenatedcompounds(TTHMs-dangerousfor human health)u potable waterworksu food and beverage <strong>in</strong>dustryu w<strong>as</strong>te water treat. plantssulfatereduc<strong>in</strong>gbacteriaOClOStrong biocidalactivity aga<strong>in</strong>stanaerobic bacteriau m<strong>in</strong>imize corrosionOClOFeSOxidation ofsulfide to sulfate(sulfide scavenger)u m<strong>in</strong>imize corrosionu m<strong>in</strong>imize bad smell


CHLORINE DIOXIDEClO 2+ e - ---> ClO 2-(E o= 0,95 V)ClO 2+ 4 H + + 5 e - ---> Cl - + 2 H 2O (E o= 1,51 V)<strong>Chlor<strong>in</strong>e</strong> <strong>Dioxide</strong> is very active aga<strong>in</strong>st:- bacteria- viruses- algae- fungi-macroorganism


CHLORINE SPECIES FORMATION IN WATERACCORDING TO pH10090chlor<strong>in</strong>e species <strong>in</strong> solution %80706050403020Cl2HOClOCl -1000 0,5 1 1,5 2 2,5 3 3,5 4 4,5 5 5,5 6 6,5 7 7,5 8 8,5 9 9,5 10pH


Bacteria wallBacteria colonyx- -- --Cl -STILL ALIVENEWGROWINGSTILL ALIVESTILL ALIVE-----ClO 2-ClO 2-ClO 2-NOgrow<strong>in</strong>g


CHEMICAL FEATURES OF CHLORINEDIOXIDE (ClO 2 )u it is a g<strong>as</strong> and must be generated on siteu it is soluble <strong>in</strong> wateru it does not undergo hydrolysis at pH ofcool<strong>in</strong>g wateru it is a strong oxidis<strong>in</strong>g agent


MICROFOULINGThe Biofoul<strong>in</strong>g problem• Bacteria, Algae, Fungi,• Microbial corrosion• Loss of the heat exchange (loss <strong>in</strong>the efficiency of the thermal cycle)MACROFOULING• Mussels, Barnacles, Serpulidworms, Hidroys• Encrust<strong>in</strong>g, loss of water flow, tubesplugg<strong>in</strong>g corrosion under deposit.


<strong>Chlor<strong>in</strong>e</strong> dioxide and chlor<strong>in</strong>e comparisonaga<strong>in</strong>st bacteria100ClO2 and Cl2 effectiveness <strong>in</strong> seawater at pH 8,2- Cl2 demand = 1,7 mg/l- ClO2 demand = 0,9 mg/l9080Cl2 1,0 mg/lOrganism survival %70605040Cl2 3,0 mg/l3020ClO2 0,3 mg/l100ClO2 1 mg/l0 30 60 90 120 150 180 210 240 270 300Contact time second


CHLORINE DIOXIDE AND CHLORINECOMPARISON ON MACROFOULING GROWTHKg/m2*y807060504030ClO2Cl2blank20Dosage mg/l100Summer- Cl2 2.0- ClO2 0.4apr-99 mag-99giu-99lug-99 ago-99set-99ott-99nov-99dic-99gen-00feb-00mar-00W<strong>in</strong>ter- Cl2 1.3- ClO2 0.2


CHLORINE DIOXIDE AND CHLORINE COMPARISONON THM FORMATION IN SEAWATER HAVINGA TOC OF 5 MG/L800total THM ppbCHLORINE35°C25°C15°CCHLORINEDIOXIDE35°C25°C15°C7006005004003002001000contact time 60 m<strong>in</strong>utecontact time 20 m<strong>in</strong>utedosage rate mg/l20 contact time 10 m<strong>in</strong>ute2 1 0,5From “ environmental impact of biocidal antifoul<strong>in</strong>g alternative treatments of seawater once through cool<strong>in</strong>g systems ”R. Ambrogi ENEL


CHLORINE DIOXIDE ADVANTAGESu very performant <strong>in</strong> short time contact systemu reduced corrosion (compared with chlor<strong>in</strong>e)u very performant at high pH (sea water, all organic andZn/phosphonate treat.)u very performant <strong>in</strong> ammonia contam<strong>in</strong>ated system(fertilizer and ammonia plant)u It can be applied by a simply chlor<strong>in</strong>e plant modification orpossibility no chlor<strong>in</strong>e treatmentu environment friendly dis<strong>in</strong>fection treatment


CHLORINE DIOXIDE GENERATIONClO 2 can be generated on site by us<strong>in</strong>g water solutions of:Sodium Chlorite,Hypochlorite and acidaccord<strong>in</strong>g to the follow<strong>in</strong>g reaction:Or by us<strong>in</strong>gSodium Chlorite and <strong>Chlor<strong>in</strong>e</strong>2NaClO2 + NaClO + 2HCl 2ClO2 + 3NaCl + H2Oaccord<strong>in</strong>g to the follow<strong>in</strong>g reaction:Or by us<strong>in</strong>gSodium Chlorite and Hydrochloric Acidaccord<strong>in</strong>g to the follow<strong>in</strong>g reaction:2 NaClO 2+ Cl 2--> 2 ClO 2+ 2 NaCl5 NaClO 2+ 4 HCl --> 4 ClO 2+ 5 NaCl + 2 H 2O


pH<strong>Chlor<strong>in</strong>e</strong> dioxideto dosage po<strong>in</strong>tpHNaClO fromelectrochlor<strong>in</strong>atorHCl 33%Sodium chlorite


<strong>Chlor<strong>in</strong>e</strong> dioxideto dosage po<strong>in</strong>tChlor<strong>in</strong>ated waterSodium chlorite


ClO2 “hypochlorite” generat<strong>in</strong>g systemConversion of hypochlorite from electrochlor<strong>in</strong>ator <strong>in</strong>to <strong>Chlor<strong>in</strong>e</strong> <strong>Dioxide</strong>


ClO2 “under water” generat<strong>in</strong>g systemReaction chamber located <strong>in</strong>to the dilution water l<strong>in</strong>eWater to bedis<strong>in</strong>fectedWater to bedis<strong>in</strong>fectedNaClO 2H 2OHClH 2OClO 2DilutionH 2OClO2Water solution


ClO 2ISIA SISTEMI


<strong>Chlor<strong>in</strong>e</strong> dioxide reagents storage tanks


<strong>Chlor<strong>in</strong>e</strong> dioxide reagents pump<strong>in</strong>gstation and control monitor<strong>in</strong>g system


<strong>Chlor<strong>in</strong>e</strong> dioxide “underwater reactionchambers”


water b<strong>as</strong><strong>in</strong> after 18 month operation.Reaction chamberslocated <strong>in</strong>side theracket pipe


Description of the Facility and Cool<strong>in</strong>g Water(PLANT 1)PLANT:FEEDING:SYSTEM:FLOWRATE:LARGE PETROCHEMICALSEAWATER FROM THE INTAKEBASIN, SCREEN FILTERS, PUMPING STATION BASINS,COOLING TOWERS BASIN,HEAT EXCHANGERS, RETURN TO THE TOWERS,BLOW DOWN TO THE SEA.RR. 175,000 m3/h (full capacity)CHLORINE DIOXIDE DOSAGE:from March to October 2 shot/day at 0.5 ppm <strong>as</strong> long <strong>as</strong> 1.5 hour eachshot (TOTAL 3 H/DAY).W<strong>in</strong>ter 2 shot/day at 0.5 ppm <strong>as</strong> long <strong>as</strong> 1 hour each shot(TOTAL 2 H/DAY).DOSAGE START UP: February 2009.


Description of the Facility and Cool<strong>in</strong>g Water(PLANT 2)PLANT:FEEDING:LARGE PETROCHEMICALSEAWATER FROM THE INTAKESYSTEM: SCREEN FILTERS, PUMPING STATION, PUMPING STATION,HEAT EXCHANGERS, RETURN TO THE TO THE SEA.FLOWRATE:32,000 m3/h (full capacity)CHLORINE DIOXIDE DOSAGE:2 shot/day at 0.3 ppm <strong>as</strong> long <strong>as</strong> 1 hour each shot (TOTAL 2 H/DAY).DOSAGE START UP: February 2009.


Why chlor<strong>in</strong>e dioxide?<strong>Chlor<strong>in</strong>e</strong> dioxide w<strong>as</strong> selected, to treat the 2 plants<strong>in</strong>stead of chlor<strong>in</strong>ation for safety, environmental andperformance re<strong>as</strong>ons.In fact, chlor<strong>in</strong>e and sodium hypochlorite areresponsible of bromate and bromoform formation <strong>in</strong>seawater which are considered very toxic for aquaticlife of the Arabian Gulf.<strong>Chlor<strong>in</strong>e</strong> dioxide demonstrated to be very efficient atvery low dosage rate, m<strong>in</strong>imiz<strong>in</strong>g its residual and theformation of brom<strong>in</strong>ated compounds at the dischargepo<strong>in</strong>t.


E<strong>as</strong>yaReadox SYSTEMelectrochemical biofilm sensor.


As chlor<strong>in</strong>e dioxide shots <strong>in</strong>cre<strong>as</strong>e, the b<strong>as</strong>el<strong>in</strong>e come backto its orig<strong>in</strong>al value show<strong>in</strong>g no biofilm activity


Constant b<strong>as</strong>el<strong>in</strong>e value <strong>in</strong>dicates that no biofilm activitytakes place and the whole system is clean.


ConclusionsWe underl<strong>in</strong>e the follow<strong>in</strong>g advantages:•<strong>Chlor<strong>in</strong>e</strong> dioxide h<strong>as</strong> allowed to m<strong>in</strong>imize the grow<strong>in</strong>g ofboth micro and macro-foul<strong>in</strong>g <strong>in</strong>side cool<strong>in</strong>g systems ofpetrochemical plants at very low dosage rate,•Monitor<strong>in</strong>g system h<strong>as</strong> demonstrated to be the “Bra<strong>in</strong>” ofthe treatment programme. It h<strong>as</strong> permitted to <strong>in</strong>jectchlor<strong>in</strong>e dioxide <strong>in</strong> a proper quantity and <strong>in</strong> the rightmoment, sav<strong>in</strong>g material and protect<strong>in</strong>g the environment.


أشكركم على حسن ضیافتكم واھتمامكمThank you very much for your hospitality and yourk<strong>in</strong>d attentionOOClFor further <strong>in</strong>formation:ISIA INTERNATIONAL FZCODubai Airport Free Zone AuthorityOffice 238- 6WBP.O.Box 293896-DUBAI-UAETel. +971.(0)47017959Fax. +971(0)47017962e.mail: gpetrucci@isia<strong>in</strong>ternational.com

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