Desalination, 31(1979)289+?98 O~~ScientifiicPublishingCompany,Amstadam-_PrintedinTheNeth~ds
CBEMISTRY SEAWATER
OF ALEALINE
DESALINATION
S. W. Walinsky Pfizer
Central
SCALE
INBIBITION
BY FLOCON
and
Research,
IN
ANIISCALANT
247
B. J. Morton
Groton,
CT,
USA
06340
SUNNARY
Alkaline chemical
scaling
changes
which
FLOCON Antiscalant and
magnesium
and mineral
are
247,
hydroxide
show
that
foulings
247
reducing
seawater's
antiscalant
complexes
disrupts
bicarbonate FLOCON
its
High
clearly
sealant scales
threshold
decomposition
inhibitor, at both
seavater
scale and
of pbysico-
of bicarbonate
suppresses
calcium
the bicarbonate
vbich
bicarbonate/carbouate
alkaline
by a series
ions.
carbonate
decomposition
sequence.
synthetic
interactions
FLOCON
that
the
antiscalant
scale
impedes
provides
alkaline
scaling
calcium
scale
contained
magnesium
14C-sodium
decomposition The
potential.
catalyzed
bicar-
rates,
thereby
formation
of Ca+2/Mg+2-
mechanisms
for accel-
the
scales
14
247
chemical
under
high
calcium carbonate and . experiments using Atlantic
significantly
into
further
the
reduced
incipient
and
of sparingly force
temperature
the
Ocean
the
alkaline
by
in-
of anti-
precipitated earth-autiscalant
incorporation
desalination
hydroxide
seavater
fouling
Codeposition
disperses
soluble, for
magnesium
alkaline
scales.
precipitation
driving
C-radiolabelled maleic anhydride
vith
control
Formation
in the bloudown.
complexes into
of
with
thermal
scale
247 vas synthesized vith
temperature
demonstrate
corporation
the
occurs
decomposition.
Antiscalant
to determine scales.
plants
intervention
the
retards
effectively
erated
by
of
in refluxing
FLOWN
by
threshold
stages
studies
distillation
initiated
a new
deposition
Kinetic bonate
in seavater
of antiscalants
conditions.
INTRODUCTION In support plants, hold
the
scale
mechanistic FLOCON
of research
chemistry inhibition studies,
on new
the
have and
been
247
- a new, seavater
carbonate)
and/or
scaling
reexamined.
describes
the
maleic
brucite
for
threshold‘antiscalantsl
alkaline
operated
Autiscalant Carefully
(calcium
of
process This
chemistry
and
paper
(magnesium
289
are
reports
of alkaline
acid-containing,
evaporators
affected
hydroxide)
seawater
the mechanisms tbe
scale
polymeric primarily scaling.
distillation of
results inhibition
scale by
thresof
these by
inhibitor. aragonite
Recently.
these
wALINSKYANDMOKr~
290
scales have
mineral lant.Such acid
treatments
controlled
eliminate
carbonate 26 reactions-
chemical
+2
by
desalination
4
20B
anhydride
thereby
+ Hz0
co2
4
sodium FLOCON
hazards
E3
+ H*O
frequency
bicarbonate
enabling
scaling
sulfuric
by
the
fol-
(1) (2)
+ + 2ou-
(3)
(brucite)
rates
was
(4)
of reactions
to synthetic 247
with
occurs
antisca-
(aragonite)
relative
Antiscalant
polymeric
co;
*
Mg
the
by
associated
hydroxide
+
+
investigated
conditions.
1,4-14C-maleic
and
co2
+COIj
wg+2+ present study has 14 C-radiolabelled adding
corrosion
B
co;
The
increasing
and magnesium
2Iico; Ca
with
the
Calcium
dosing.
loving
been
brines
synthesized
its mechanisms
(1 and
under from
of action
3)
varied
radiolabelled
to be
determined.
EXPERIWENTAL Synthetic from
reagent
lnmol), and to give
Nuclear) The
sodium
of was
rate
added,
of carbon
in Oxifluor-CO2
was
standard
(1.23
used
NaOH
ing
(1.03
mmol),
for
the
solution
was
sodium the brine
the
samples
FLOCON
conditions
J,4-14C-maleic
anhydride
chemical
and
247, (1.0
properties
the
radioactivity
(10
repeated
a proprietary
brine Mark
for FLOCON Titrator
product,
Amershsm)
into
as desalination
prepared (1.01 water one
England (102 was
was
+
l°C)-
continually
dioxide
was
trapped
radioassayed
I Liquid
in
Scintillation 14 C-internal A
samples.
efficiencies-
in the
mmol! , and
active
Automatic
as well
filtered
(1.39
curves
ntci;
Carbon
of aliquot
ppm
New
to reflux
scintillation
were
sulfate
lo Millipore),
decomposition
Chicago
were
chloride
in distilled
(0.45
assays.
A Nuclear
247
on a Netrohm
Antiscalant
rapidly
bicarbonate
experiments
titrationfcomplexation
filtered
heated
and
magnesium
dissolved
was
to determine
Antiscalant
were
potassium
(10 ng/uCi;
Nuclear),
determining
experiments
mmol),
bicarbonate
scintillation
Nuclear).
decomposition
and
ambient
and
which
(N-E.
and/or
(47.2
mmol),
evolution
(N.E.
decomposition
chloride
(0.31
liquid
to the
mnol)
titrant. 14 C-FLOCON
Physical
dioxide
added
Reported under
then
cocktail
Bicarbonate chloride
and
solution
was
for bicarbonate sodium
bicarbonate
by radiochemical
an Aquafluor System
brines
chemicals,
After solution. 14 C-radiolabelled
50 ml
microcurie
measured
seawater grade
presence magnesium
of calcium chloride
dosage). Antiscalant - Hodel
was
247 were E436
using
synthesized
the polymerization scale
control
by
determined 0.45E
incorporatreaction.
performance
W&INSKp of
AND EfoBTON
14 C-FLCCON
247
Radiochemical minute
per
groups
which
the
stage
flash
standard
Scales
were
analyzed
247
was
was
determined
determined
for by
by
liquid
scanning
(2.44
(503.64
of brine.
Total
dissolved
(2.44
uenol),
sulfate
(28.21
of synthetic
Bicarbonate
10.5
magnesium
mmolar
bicarbonate alkaline plants
represents
by
of
that
catalysis
for
fouling
X-ray
prepared
from
was
and
chloride
(9.92
solids
- 35.10
from
mmol)
presence
measured.
Carrutbers. and
sodium
morphology
mmol),
one
sodium
kilogram
bicarbonate
(555.35
to afford
analyses.
bicarbonate
(25.24
sodium
17
FLCCON
Scale
to make
chloride
the
diffraction
chloride mm011
prepared
sodium
in
absorption,
and
(9.92
was
hr
Ocean conditions.
in a laboratory
(Oxifluor-C02).
magnesium
g/kg.
Atlantic
11.5
by Auerbach
(SDI)
seawater
and
ion
ussol), one
sodium
kilogram
g/kg.
The pR
increases
seawater
vas
flash
magnesium
decomposition
by magnesium
and
ions. which
contained carbon
recycle
rates Calcium
plants,
to assess are
is consistent
the
added
vith
onset
of
14C-sodium
assays.
The
concentration and, their
is markedly previous
in rate-
investigated
factor
seawater
of 2.0, the
Figure in
more
The
.
continually
synthetic
influence. faster
desalination
bicarbonate
in addition,
mmolar,
the maximum
scaling
was
55.4
2.50
in
1) was
evolution
significantly
acceleration
determines
(equation
are
is only
of bicarbonate
dioxide
scintillation
varied
which
controls
preconcentrated,
(HSF)
were
species decomposition
and
seawater
concentration
decomposition
which
liquid
in typical
bicarbonate
thermal
Bicarbonate
experiments
or magnesium
concentrations
whereas
disappearance
multi-stage
bicarbonate
calcium
acid
pressure
conducted
atomic
vas
chemical-limiting
radiochemical
in these
calcium
calcium
the
synthetic
of bicarbonate
simulate
by
- 35.26
dissolved
potential.
decomposition.
in refluxing
used
exchanger
assays
mmol),
for
heat
metals
mnol),
(10.21
refluxed were
chloride
potassium
and
is responsible
monitored
(28.22
respectively,
scaling
limiting
rate
and Total
per
carboxylic
Decomnosition
Since and
anaol),
product.
disintegration
with
or elevated
described
seawater
solids
x 10'
conducted
runs
microscopy
potassium
chloride
brine.
was
been
earth
Synthetic
calcium
were
atmospheric
scintillation
and
Calcium-containing
antiscalant's
in which
has
electron
sulfate
mmol),
the
of
pressure
synthetic
ussol), magnesium
fraction
seavater
(SSFE) SSRE
alkaline
Ragnesi-containing
chloride
the
of the
9.63
under
Elevated
evaporator
operation
commercial
was
experiments
to reflux
ppm).
the unlabelled
atoms.
control
experiments,
to
antiscalant
a small
carbon
scale
(lo-13
identical
isolated
Only
heated
atmospheric
single The
was
247
the
radioactive
temperature
of PMCON
essentially of
(dpm/g).
contained
seawater In
were
activity gram
High
291
the
to
concentrations 1 shows
presence
pronounced 7,g publications.
of than
WALINSKP
292
AND !KnlToN
13 HCOs- (6.15 mmolar) with no polyvalent metal ions 0 HC03‘ (6.15 mm&r) a
0
and Mg+2 (52.5 mmolar)
HCOJ- (6.15 mmolar) and Ca+2 (20.6 mmolar)
10
20
40
30
-< 50
60
Time (min) Figure 1. RATE OF THERMAL
BICARBONATE
DECOMPOSITION
(102OC)
Synthetic Seawater (Concentration Factor = 2.0)
Bicarbonate
decomposition
is reported'
-d(HCO;) -= dt
Direct to
involve
with
interaction a relatively
a double
negative
of
energy
a second
order
reaction.
(5)
k(HCO;)2
two negatively
high
to be
charged
transition
bicarbonate
state,
ions
hypothetical
would
appear
structure
co;
Calcium
and magnesium
Figure
1, reduces
ration
via
In similar and
the
complex
magnesium
catalyzed
overall
formation.
experiments levels,
1 J
charge.
FLOCON
decomposition
activation
energy
as shown
of bicarbonate, for
reaction
(6) by
charge
(6)
in stabili-
2 with 247
synthetic
sezvater
was
to decrease
shown
which the
contained rate
typical
calcium
of bicarbonate/car-
W.AJJNSKf
bonate
AND MORTON
293
decomposition,
duction
in the
Figure
fouling
2.
4.0z 2 ; sz z g
A consequence
of
such
retardation
would
be
a re-
rate.
&
FLOCON 247 (10 $5 m Active) in Synthetic Seawater with HCOi (52.5 mmolar) and Ca+* (20.6 mmolar) (6.15 mm&r). Mg
0
Control reaction without Antiscalant
3_0-
2.0-
x d 1.o-
Time (min) Figure 2. RATE OF CARBONATE DECOMPOSITION OF FLOCON ANTISCALANT 247
(102OC) IN THE PRESENCE
Synthetic Seawater (Concentration Factor = 2.0)
The
importance
desalting high
operations.
temperature
calcium
in solution use
at
with
threshold 2 cannot
A likely complex
which
bonate
calcium
and magnesium
ions
dosages,
disrupts
the
retardation by
is the the
on precipitated
formed.
shown
be explained
mechanism
scale
be
simple
the calcium
recycle
is more
later,
carbonate
may
decomposition
catalyzed
, thereby
by
of FLOCON's observed
in
cations. earth-bicarbonate
decomposition forming
preventing
in mag-
associates
In view
of divalent
function
temperature
resulting
of an antiscalant-alkaline
and magnesium
once-through
rapidly
complexes.
in field
is incomplete,
in high
247
of bicarbonate
antiscalant
and
extensive
FLOCON
to form
displayed
decomposition
Whereas,
sequestration
formation
calcium
is clearly
temperature
bicarbonate
decomposition
As will
rates
where
predominant
scaling.
Alternatively,
carbonate. loidsl'
is the
in low
plants
bicarbonate/carbonate
hydroxide
Figure
decomposition
Qualitatively,
desalination
carbonate
MSF plants, nesium
of bicarbonate
of the bi-
protective
heterogeneous
colbicar-
decomposition.
FLOCON 247
-
Chemical
Ca+2/b++2
Ccqmlexes
interactions
of FLOCON
Antiscalant
247 with
seavater's
major
scale
294
WALINSKY
AND
HORTON
forming cations were investigated. The titration curve in Figure 3 shovs that FLOCON 247 as a carboxylic acid polymer is largely neutralized under the alkaline operating conditions of HSF desalination plants.
When the titration curves were
repeated in the presence of calcium or magnesium ions, the acidity of the polymer was increased.
The titration curve shifts indicate that FLOCON 247 rapidly forms
alkaline earth complexes.
Little difference was noted iu the selectivity of calcium
or magnesium binding.
~Y!ITitration Curve for FLOCON
247
13 Titration Curve for FLOCON 247 in the presenceof Ca** (0.3 mmolar) o
Titration Curve for FLOCON 247 in the presenceof Mg+* (0.3 mmolar)
T&rant fml of O&N Figure 3. TITRATIONCOMPLEXATION
CURVES
NaOH) FOR FLOCON ANTISCALANT 247
Sequestration of alkaline earth metals by carboxylic acid polymers known for some time.
The stoichiometric chelation of calcium
has
been
by
anionic polymers 11 However, the has led to proposals to use these materials as detergent builders. stoichiotuetric use of polymeric sequestrants in detergent formulations or in scale control applications is too expensive.
Threshold scale control treatments use only
very low dosages, parts per million, of sequestrants.
The effectiveness of thres-
hold autiscalants in preventing scale formation is attributed to reduction of the 12 rate of crystal grovth. Nancollas and coworkers have demonstrated that calcium 13 14 15 and calcium sulfate crystal growth can be iucarbonate, magnesium hydroxide, hibited by the adsorption of very small amounts of scale inhibitors on the crystal surfaces.
The question has remsiued as to why other good wuomezic
such as ethylenediaminetetraacetic inhibitors.
chelating agents
(EBTA) do not work effectively as threshold scale
In the present study, a survey of mnaneric
and polymeric chelants
WALINSKY
295
AND NOBTON
such as poly(meth)acrylates,
polyphosphonates,
citrates, sulfonates, aminocarbo-
xylates, and many others indicates that sparingly soluble, aatiscalant-polyvalent metal ion complexes are required for threshold scale inhibition. The limited solu16 bility of these complexes provides the chemical driving force for incorporation of the scale inhibitor into the crystal lattice of the scales.
FLCCON 247 - Alkaline Scale Interactions A series of experiments was conducted with 14C-radiolabelled FLOCON 247 to determine whether the antiscalant is indeed incorporated into the alkaline scales formed.
Table I reports high temperature scale control results from experiments
conducted with authentic Atlantic Ocean seawater which was heated to reflux under both atmospheric and elevated pressures. (SSFE)‘~
A
laboratory single stage flash evaporator
which was designed to simulate field operating conditions was used to eval-
uate heat exchanger fouling.
In all of these experiments the scales were isolated
and then analyzed for calcium, magnesium, and antiscalant content.
Table I FLOCON Anriwalanr 247 - Alkaline Scale lnfcracrions Desalination ScaleControl Experimenrs Using Atlantic Ocean Seawater
The scale control results from the refluxing seawater and
SSFE
experiments
are in very good agreement considering the dissimilar nature of the experiments. Both experiments clearly demonstrate that FLOCON 247 is incorporated into alkaline scales under high temperature, threshold desalting conditions.
FLOCCN 247 intercepts
nucleation or incipient crystal growth at a very early stage since antiscalant/scale
WAUXXYANDHOR!TON
296 ratios
are
blowdown as
fairly
scales
inhibits
high. also
them.
Incorporation
indicates
The
that
of FMCON FLOCON
mechanistic
247
247
into
flash
disperses
implications
of
chamber
alkaline
this
data
and
scales
will
be
brine
as well
discussed
shortly. The was
selectivity
determined
or magnesium marized
in
of FLOCON the
SSFE
alkaline
in Table
247's
using
interactions
synthetic
scale
potential.
Sclrcti~iry
of FLOCON
The
SSFt:
97%
synthetic
of
the
chemical with are
alkaline
but
seawater
in these
of mixed
Ca+2/Mg+2
trol.
The
mixed
the
are
SSFE
not
trials
-FLOCON
double-layer
erals
as dolmite.
a
of antiscalant
amount
was
The
polymer
with
these
scales
either
experiments
calcium
are
sum-
did
not
ions,
complex
FLOCON
Antiscalant
antiscalantfscale
with
magnesium
contain
may
carbonate
investigated
Seawater
high
appears
complexes
Scalelntcracrions
Using Synrhcric
carbonate reports 12,18
any magnesium to enhance
interact or help
SSFE
precipitated,
the
The
with
amount
first,
formation scale the
in the
seawater. of
scale
con-
charged
snore soluble
complexes
synthetic
strong
synthetic
carbonate
to stabilize
with
shows
at
the
ions.
inhibited
interactions
results,
strongly
of Ca +2/Mg+2 -FLOCON in the
The
since
calcium
mre
247 ratio
scales.
The
literature
Precipitation
ions
Alhrlinc
as pronounced.
of calcium
of bicarbonate small
of
and Mg(OW)2
contained
II
-
calcium
complexes
antiscalant
217
scale.
carboxyl
consistent
electrical such
results
Expertments
without
magnesium of
carbonate
unexpected,
Scrle Corrrn~l
seawater
affinity
calcium
CaC03
which
II. T;blr
In
with
seawater
min-
absence Although
inhibitor
WALINSKY AND MOEJ!ON
297
deposited was only two percent alkaline scaling conditions.
incorporation level routinely obtained under
of
Therefore, FIRCON 247 is compatible with seawater at
high temperatures, and its precipitation is regulated by the amount of scale formed. Deposition of PLGCGN 247 into alkaline scales certainly retards mineral crystal growth, but high antiscalant/scale
ratios are not completely consistent with adsor19,20 of scale control, Coprecipitation of
ption-crystal growth inhibition mechanisms
sparingly soluble antiscalant complexes with alkaline scales is mechanistically Antiscalant-scale
more consistent with the data.
codeposition impedes further scaling
and disperses the precipitated scale into a less adhering formIn conclusion, formation of alkaline scale in seawater distillation plants is a sequential chemical-physical of bicarbonate ions. sition
process which is initiated by the decomposition
PLOCON Antiscalant 247 disrupts both the bicarbonate decompo-
scale forming stages of this sequence to inhibit calcium carbonate and
and
magnesium hydroxide
scaling.
ACKNOWLEDGENENl!S Authors
and Bryce
1.
2.
i: 5. 6.
would
Tate
like
for his
to thank helpful
John
O'Neill
discussions
for
and
conducting
review
the
SSFE
experiraents
of the manuscript.
scale inbibitors are additives ubich suppress mineral scale formation at usage levels which are too small to sequester the scale. For initial disclosures see references: E- A. BRBERLEIN, British Patent 223 614, 1923 and A. KIRKALDY, U.S. Patent 1 SO6 306, 1924. W. STDMD ARD J. J. MORGAN, Aquatic Chemistry, John Wiley C Sons, Nev York, 1970; Chapters 2 and 4. H. RILLIER, Proc. Inst. Hech, Eng. (London), Lp, 295 (1952). Threshold
W. F. LANGELIER, D. Il. CALDWELL AND W. 126 (1950). R. DOOLEY AND J. GLATER, Desalinationll, D. A. SKOOG AND D. M. WEST, FL, and Winston, New York, 19633 Rinehart,
B. LAWRRNGE,
Ind.
Eng.
Cbem.,
3,
1 (1972). Bolt, pg.
351.
7.
R. STUMPER, 2. Anorg. Allgem. Chem., 202, 227 (1931). R. STUM?ER~ 2. Anorg. Allgem. Chem., 204, 365 (1932).
9.
B. K. SRDKLA AND D. S. DATAR, Indian J. Appl. Chem., 35, 30 (1972). R. STIJHPER, 2. Anorg. Allgem. Chem., 208, 46 (1932). J. F. SCEAFFER AND R. T. WOODFMMS, Iad. Eng. Chem. s, 3 (1977). J. C. COWAN AND D. 3. WEINTRITT, Water-Formed Scale Deoosits, Gulf Publishing co., Houston, 1976; Chapter 7. M. M. REDDY AND G. H. RARCOLLAS, Desalination, l2, 61 (1973).
a.
10. ::: 13. 14. 15.
16.
S. T. LUI ARD G. H. NANGOLLAS, Desalination, 12, 75 (1973). G. Ii. NANCOLLAS AND J. S. GILL, Proceedings of International Symposium on Society of Oilfield and Geothermal Chemistry, Houston, Texas, Jan., 1979. Petroleum Engineers, SPE 7861. K. FAJANS, Radio Elements and Isotopes. Chemical Forces and Optical Properties of Substances, McGraw-Hill, New York, 1931.
298
17.
18.
19. 20.
WALINSKY AND MORTON
l4.Ii.AUERBACEANDM. S. CARRUTEERS, "Laboratory Applications Testing of Desalination Antiscalants," presented at the International Congress of Desalination and Water Reuse, Nice, October, 1979. M. IL RRDDY AND G. EL NANCOLLAS, J. Crystal Growth 35, 33 (1976). C. H. NESTLER, J- Colloid Interface Sci-, 26, 10 (1968). J. E. CRAWFORD AND B. R. SMITH, J. Colloid Interface Sci., 2l, 623 (1966).