awri water in oil sands research · relave stability of metalloporphyrins class

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1 AWRI Water in Oil Sands Research Alexander J.B. Zehnder, AWRI Scien6fic Director

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AWRI Water in Oil Sands Research Alexander J.B. Zehnder, AWRI Scien6fic Director 

AspartofAlbertaInnovates‐‐EnergyandEnvironmentSolu:ons,theAWRIfundsandleadsscienceandresearchtohelpfulfillthegoalsofWaterforLife:• Safe,securedrinkingwatersupply,• Healthyaqua:cecosystems,and• Reliable,qualitywatersuppliesforasustainableeconomy.

ThegoalsforAWRIare:• toservesasaknowledgebroker• toprovideanalysisandcontexttowaterresearch

 fordecision‐makers, policy‐makers, watermanagementprac::oners,

• toensuringunderstandable,relevantandaccessibleinforma:on

DILUENT

DEOILING

WATERRECYCLE

STEAMGENERATION

OIL/WATERSEPARATION

Atomic/molecular level 

Engineered processes Process 

understanding 

4

• MoleculardynamicsofAsphalteneaggrega:on• Interac:onbetweenbitumen,organic,andclaysurfaces

• Deposi:onofcolloids(fouling).• Membranefouling• De‐emulsifica:on

Uniformchannelsofapproximately3Åarepresent

ZeoliteMembrane

H2O

Hydrocarbons Salts (Ca++, Mg++ etc.)  H2O 

Hydrocarbons Salts 

Molecular sieving of water 

5

Highpressureandhightemperaturecross‐flowmembraneprocessforSAGDwaterTreatment

6

0.4 

0.8 

1.2 

1.6 

95 

96 

97 

98 

99 

100 

25  50  75 Water flux (k

g/m2.h) 

Toluen

e removal (%

Temperature (oC) Toluene removal 

Water flux 

0.1 

0.2 

0.3 

0.4 

0.5 

0.6 

0.7 

98 

98.4 

98.8 

99.2 

99.6 

100 

0  40  80  150 

Water flux (k

g/m2.h) 

Toluen

e removal (%

Feed side pressure (Psig) Toluene removal 

Water flux 

25oC 

FromStevenKuznicki

SyncrudeTailingsPond,FutureSiteofBase‐MineLake(2012)

Dr. J MarYn Project Lead Jon.mar:[email protected] 

Dr. M Belosevic  Dr. M Gamal El‐Din  Dr. J Giesy  Dr. T Gan  Dr. XC Le Team Lead [email protected]

Environmental Chemistry 

Mammalian Toxicology 

Advanced Oxida:on 

Aqua:c Toxicology 

Environmental Modeling 

Environmental Chemistry 

MulYdisciplinary Team of Experts 

OSPW Ozona:on and Analysis 

hcp://www.usask.ca/water/majorprojects.php

• NAsefficientlyremoved • MajorbyproductsarealreadypresentnaturallyinOSPW• MostpersistentNAspreferen:allyremoved

• Toxicitytomicroorganismsdecreases • Toxicitytoinvertebratesdecreases • Theendocrine disrupYng acYvity ofOSPWdecreases • Natural biodegradaYon and bioremediaYon increase aferozona:on• Newanaly:calmethodsprovidefingerprin:ngtoolformonitoringtheAthabasca

From:J.Mar:n,M.Belosevic,M.GamalEl‐Din,J.Giesy,T.Gan&XCLe

– VanadiumcontentinAthabascaOilSandsis~600μg/g(ppm)– VanadiumleachesfromcokeasbothV(V)andV(IV)– V(V)ispredominantspeciesinOSPW– Toxicityofvanadiumspecies:V(V)>V(IV)>V(III)

From:J.Mar:n,M.Belosevic,M.GamalEl‐Din,J.Giesy,T.Gan&XCLe

2500

2000

1500

1000

500

SignalIntensity

(cps)

6543210

Reten:on:me(min)

V(III) V(IV) 

V(V) ‐

EDTAcomplexesofV(III)and(IV)areseparatedfromV(V)species.

From:J.Mar:n,M.Belosevic,M.GamalEl‐Din,J.Giesy,T.Gan&XCLe

rela:vestabilityofmetalloporphyrins

Class I Al, Pd, V 

Class IV  Mg, Mn, Pb 

Class III Fe, In, Zn 

Class II Co, Cu, Ni 

Class V Ca, Sr, Ba 

FromManouchehrAminiet al. 2007

As OH OH

OH O

As OH OH

OH As OH OH

O CH 3

As OH OH

CH 3 As OH O

CH 3 CH 3

As OH CH 3 CH 3

As O

CH 3 CH 3

CH 3 As CH 3 CH 3

CH 3

2 e - CH 3 +

2 e - 2 e - CH 3 +

CH 3 +

2 e -

As V As III MMAV

D MA V MMAIII D MA III

TM AO V T MA III

Adaptedfrom:J.Mar:n,M.Belosevic,M.GamalEl‐Din,J.Giesy,T.Gan&XCLe

forming mobile As 

volaYlizaYon & detoxificaYon 

Fe3+H2As5+O4

Fe3+H2As3+O3

Fe2+  +H2As3+O3‐

2e‐

1e‐

fromorganicmacer

fromorganicmacer

15

Seclingofsolids Recoveryofporewater

16

Conven:onalDe‐oiling

ThermalWaterRecycle

O/WSepara:on

SteamGenera:on

FWKOProduc:onfrom

wellpads80:20water/oil

emulsion

Treater

DilbitSales$/Bbl

Sludgetodisposal

SkimTank

SlopOilTank

IGFWSF

Sofened,brackishmake‐upwater

BFWTank

OTSG

99%steam

qualitytowellpads

DiluentTank

Evaporator

Crystalizer

RO

SuccessFactors:

Robust&reliable

Minimizedown:me

Stabilityat85‐90°C

UFde‐oilingflux

BFWsilicareduc:on

Impact(30,000bopd):

40%Evapenergy↓($1.8MM/yr.)

20%Capex↓($6MM)

40%↓CO2(68,000t/yr)

Reducedrisk‐mul:barriertooil

Improvedprocessreliability

DesiredOutcomes(GreenFieldExample)

1.DeoilingFieldPilot

2.ReverseOsmosisMembranePilot

3.CombinedDemonstra:onPlant

From100‐1000ppmoilcontent@850C

To<1ppmoilcontent

2009 2010 2011 2012

TechSelec:on

RecruitIndustryPartner

FEED DD

Build

Operate

On‐goingResearch

Build

DD

Operate

DD

Build

Operate

AWRIAgreement

PartnerAgreement

Deoiling Pilot 

PreconcentraYon Pilot 

DemonstraYon Plant 

What about the groundwater? 

1.  SADG my mobilize arsenic through abioYc reducYon.  

3.  Vanadium porphyrinate complexes may be mobilized by  the reducYon of viscosity. Lifle is known about their  toxicity, since most studies where based on uptake  of dust through the lung. 

3.  AcidificaYon through CSS may decrease the binding  between iron oxides and arsenate but will also decrease   the reacYvity of iron as redox mediator. 

Conclusion: Close monitoring of the SAGD and CSS sites will  reduce the risks and will allow to implement remedial measures if needed. 

Thankyouverymuchforyouracen:on!