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Petroleum Recovery Research Center, A Division of the New Mexico Institute of Mining and
TechnologyPRRC
Desalination
Using Zeolite Membranes
Robert L. LeePetroleum Recovery Research Center (PRRC)
New Mexico Tech, Socorro
Petroleum Recovery Research Center, A Division of the New Mexico Institute of Mining and
TechnologyPRRC
PRRC/NM Tech:• A research arm of New Mexico oil and gas industry, only for oil
and gas industry, dedicated to industry’s interests alone.
• PRRC/NM Tech research directions are governed by its advisory board members including:(1) New Mexico Oil & Gas Association (NMOGA)(2) Independent Producers Association (IPANM) (3) New Mexico Oil Conservation Division (NMOCD)(4) New Mexico State Land Office (NMSLO)
• NMOGA, IPANM, NMOCD, and SLO are policy-making organizations but PRRC/NM Tech is for research only.
Petroleum Recovery Research Center, A Division of the New Mexico Institute of Mining and
TechnologyPRRC
PRRC Produced Water Research • Water Shutoff and Conformance Improvement
(Seright, PRRC/NM Tech)• Optimal Process Identification
(Hightower, Sattler, Sandia)• Produced Water Quality Data/Mapping
(Cather, PRRC/NM Tech)• Brine Treatment Innovations, WaterDog
(Dong, PRRC/NM Tech)
Petroleum Recovery Research Center, A Division of the New Mexico Institute of Mining and
TechnologyPRRC
Funding & Acknowledgements• Funding:
– 1/3 of PRRC/NM Tech’s resources are devoted to produced water projects.
– Current contracted budget: ~ $3.6M
• Acknowledgements:
– NPTO/NETL/DOE ~ $2.0M
– State of New Mexico ~ $1.4M
– NM Tech President Office ~ $0.2M
– Endorsements from NMOGA, IPANM, NMOCD, and SLO
Petroleum Recovery Research Center, A Division of the New Mexico Institute of Mining and
TechnologyPRRC
1) In 1998, PRRC/NM Tech started its desalination research effort.
2) Research focused on high-salinity produced water:- >> 50,000 ppm in San Juan basin- >> 100,000 ppm in Permian basin
3) 1999-2002 (Whitworth), studied compacted bentonite clay membranes. Unfortunately, the charged layers are destroyed in highly concentrated brines.
WaterDog Phase I, 1998-2002
Petroleum Recovery Research Center, A Division of the New Mexico Institute of Mining and
TechnologyPRRC
WaterDog Phase II, 2003 --
• The new synthetic Zeolite membrane was successfully tested by Dr. Dong’s group at PRRC/NM Tech.
• The Zeolite membrane has ~ 90% salt rejection rate of an 80,000 ppm produced water.
• It is an inorganic membrane.
• It should be easy to manufacture, is promising to be commercialized…………………..
• The patent application was filed in May 2003.
Liangxiong, Li a,b; Junhang, Dong a; Robert L. Lee b
a Department of Petroleum & Chemical Engineering b Petroleum Recovery Research Center (PRRC)
New Mexico Tech, Socorro
Polycrystalline Zeolite Membranes for produced water treatment
Introduction
• Produced water treatment
– High salt concentration (as high as 20 wt%, 200,000 ppm)
– Dissolvable hydrocarbon
– High cost of treatment ($1.7/barrel)
• Polymeric membrane
– Serious hydrolysis at produced water condition
– Sensitive to pH changes
• Inorganic membrane– High flux ($$)
– High thermal and chemical stability ($$)
– Regeneration capability ($$)
– Perhaps, low pretreatment cost ($$$$$$)
Zeolite Membrane Synthesis
Film formation
Nucleation Crystal growth
Synthesis methods used:
• In-situ crystallization• Second growth• Vapor phase conversion
Continuous zeolite layer
Porous -alumina support
Water bottle to prevent sample evaporation
Sample collector
Feed outlet
Feed tank
Sample analysis
Membrane cell
Feed pressure control and pressure gaugeHigh pressure N2
from cylinder
Flow control valve
Feed solution
Salt Removal Experiment
Mechanisms of Ion Removal by Zeolite Membrane
Mechanism A Size exclusion
Pore size5.6Å
(0.56 nano)
Ion Hydrated Diameter (Angstroms)
H2O 5.6
Li+ 7.6
Na+ 7.2
K+ 6.6
Mg++ 8.6
Ca++ 8.2
OH- 6.0
Cl- 6.6
NO3- 6.8
Mechanism B Double layerOverlapping
(inter crystals)
Zeolite Membrane--Image of Surface
• In situ crystallization
Zeolite Membrane--Image of Cross-Section
Zeolite
Alumina Support
XRD Pattern of Zeolite Layer
2
0 10 20 30 40 50
Rel
ativ
e In
ten
sity
alumina substrate
Zeolite Membrane
MFI type zeolite
Ion Removal Testing of Brine
Number Ions in feed solution
TDS
(104mg/l)
Pressure
(MPa)
Ion Rejection
(R, %)
Flux
(kg/m2.h)
AZA01 K+,Na+,Ca2+,Mg2+
, NH4+, and Cl-
3.92
(39K ppm)
2.41
(350 psi)
74.5% 0.112
AZS04 Na+, and Cl- 0.55 2.07 89.2% 0.135
BZA04 Mg2+, and Cl- 0.94 2.07 68.6% 0.081
BZA05 Ca2+, and Cl- 1.10 2.07 57.6% 0.096
BZA06 Na+, and SO42- 1.42 2.07 57.4% 0.097
EZA01 Na+, and Cl- 0.50 2.07 76.8% 0.240
tA
QF
m
w
%100
)(
)()(
feeds
permsfeeds
C
CCR
Ion Removal Testing of Brine
0 20 40 60 80 100Time, h
0.15
0.25
0.35
0.10
0.20
0.30
0.40
Flu
x, k
g m
h
-10
10
20
30
50
60
70
0
40
80
Rej
ection (R
), %
-2
-1
Flux
Rejection
0.00
0.20
0.40
0.60
0.80
1.00
1.20
0 20 40 60 80 100 120 140 160 180 200
Time (hours)
Flux
(kg/
(m2.
h))
0%
10%
20%
30%
40%
50%
60%
70%
80%
90%
100%
Ion
reje
ctio
n (%
)
Flux
Rejection
Membrane-AZA01 Membrane-AZS04
TDS, 3.92104 mg/l
Ion rejection, 74.5%
Flux, 0.112 (kg/m2.h)
TDS (0.55104mg/l)
Ion rejection, 89.2%
Flux, 0.135 (kg/m2.h)
Temperature (oC)
0 20 40 60 80 100
Flu
x (K
g/(
m2 .
h))
Per
mea
nce
(K
g/(
Mp
a.m
2 .h
))
0.0
0.5
1.0
1.5
2.0
2.5
3.0
3.5
Flux Permeance
Separation and Flux at Different Temperature
Temperature (C)
0 20 40 60 80 100
Sep
arat
ion
eff
icie
ncy
(%
)0
10
20
30
40
50
60
70
80
Na+
K+
Ca2+
NH4+
Mg2+
a. Flux vs. temperature b. Separation vs. temperature
Separation for Various Ions (Membrane BZA)
Ion
Sal
t re
ject
ion
(%
)
0
20
40
60
80
Na+ K+ Ca2+ Mg2+ SO42- Br- Cl-
• Zeolite membranes show promising properties for ion removal in
produced water.
• The preliminary ion removal cross-flow experiment revealed that:
- MFI Zeolite membrane shows salt rejection of 75% in 4104 mg/l brine
and 90% for 5500mg/l sodium chloride solution.
- Thin and defect-free Zeolite membranes may show high ion rejection
and high flux for application in produced water treatment.
Summary
• Future work:
- Optimize Zeolite synthesis to minimize the cost of membrane
preparation;
- Synthesize and test the desalination of A-type and Y-type
Zeolite membranes;
- Study the mechanism of ion rejection by various types of
Zeolite membrane.
Summary
Acknowledgement
NPTO/NETL/DOE (Dr. Lawson, John Ford)State of New Mexico (Governor, Senators, Representatives)NM Tech President Office (Dr. Lopez)NMOGA, IPANM, NMOCD, and SLO(Bob Gallagher, Deborah Seligman, Jeff Harvard,
Tucker Bayless, Lori Wrotenbery, and Jami Baily)
PRRC Separation group members:Dr. Junhang Dong (group leader)Ashlee RyanXuehong GuAditi MajumdarKatsuya SugimotoAmber WoodyattLiangxiong Li