For Mate Manual A5 Crystallization Temperature
Transcript of For Mate Manual A5 Crystallization Temperature
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P A G E 1S E C T I O N A 5
Section A5
Crystallization Temperature
NOTICE AND DISCLAIMER. The data and conclusions contained herein are based on work believed to be reliable; however, CABOT cannotand does not guarantee that similar results and/or conclusions will be obtained by others. This inormation is provided as a convenience and orinormational purposes only. No guarantee or warranty as to this inormation, or any product to which it relates, is given or implied. CABOTDISCLAIMS ALL WARRANTIES EXPRESS OR IMPLIED, INCLUDING MERCHANTABILITY OR FITNESS FOR A PARTICULAR PURPOSE AS TO (i)SUCH INFORMATION, (ii) ANY PRODUCT OR (iii) INTELLECTUAL PROPERTY INFRINGEMENT. In no event is CABOT responsible or, and CABOTdoes not accept and hereby disclaims liability or, any damages whatsoever in connection with the use o or reliance on this inormation or anyproduct to which it relates.
2011 Cabot Corporation, M.A.-U.S.A. All rights reserved. CABOT is a registered trademark o Cabot Corporation.
A5.1 Introduction ........................................................................................... 2
A5.2 TCT in ormates what does it mean and why is it so hard to get right? 2A5.3 Crystallization mechanisms in ormate brines ..................................... 2
A5.4 Procedure or TCT determination in ormate brines .............................3
A5.4.1 Selecting and preparing seeding material ......................................... 4
A5.4.2 TCT determination method ............................................................... 4
A5.5 TCT data or ormate brines ................................................................. 5
A5.5.1 TCT in single-salt sodium ormate ..................................................... 6
A5.5.2 TCT in single-salt potassium ormate ............................................... 6
A5.5.3 TCT in single-salt cesium ormates .................................................. 6
A5.5.4 TCT in blended ormate brines ......................................................... 6
A5.6 Pressurized crystallization temperature PCT ...................................... 15
A5.6.1 Introduction ...................................................................................... 15
A5.6.2 Methods or determining PCT in ormate brines ............................. 15
A5.6.3 PCT data or ormate brines ............................................................ 15
A5.7 How to apply TCT / PCT data in the feld ............................................. 18
A5.8 How to lower crystallization temperature o ormate brines ............. 18
A5.8.1 Lowering TCT in single-salt ormate brines ...................................... 18
A5.8.2 Lowering TCT in ormate brines .................................................... 18
Reerences .................................................................................................. 18
The Formate Technical Manual is continually updated.
To check if a newer version of this section exists please visit www.formatebrines.com/manual
CHEMICAL AND PHYSICAL PROPERTIES
F O R M A T E T E C H N I C A L M A N U A LC A B O T S P E C I A L T Y F L U I D S
V E R S I O N 3 0 4 / 1 1 P A G E 1S E C T I O N A 5
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P A G E 2 V E R S I O N 3 0 4 / 1 1
F O R M A T E T E C H N I C A L M A N U A L
S E C T I O N A 5
A5.1 Introduction
Crystallization temperature is an important property
o well construction and intervention uids that are
used in cold weather conditions and / or under high
pressure. True crystallization temperature (TCT) has
historically been used to defne the perormance
ceiling o oilfeld brines and uids. In traditional
oilfeld brines and uids there is typically only a small
dierence (saety margin) between the TCT as
measured in the laboratory and the uids perormance
ceiling in the feld. Formate brines behave very
dierently. With a massive supercooling eect and
the ormation o metastable crystals, the dierence
between TCT as measured in the laboratory and the
perormance ceiling in the feld is enormous, and it is
questionable whether TCT is suitable or measuring
the perormance ceiling o the uid.
Not only is true crystallization temperature (TCT) a
questionable measure o the perormance ceiling oormate brines, but it is also extremely difcult to
measure correctly. Measurements o TCTs in
ormate uids have, over the past years, become a
true stumbling block or many test laboratories.
An assortment o conicting TCT curves and mixing
tables exist in the industry today. For a concentrated
potassium ormate brine, or example, TCT data can
be ound to vary rom -18 to +7C / -4 to +45F.
A5.2TCT in ormates whatdoes it mean and why is itso hard to get right?
The most commonly used procedure or measuring
TCT in oilfeld brines is the API 13J method [1].
In this procedure a brine sample is cooled at a set
rate, oten with a generic seed crystal o barium
sulate, until the onset o precipitation. Once
precipitation starts, a small rise in temperature is
usually seen due to the exothermic nature o the
event. Ater precipitation has been noted the
sample is heated until all crystals have redissolved.
The data recorded rom this procedure includes:
FirstCrystaltoAppear(FCTA):Thetemperature
at which precipitation frst occurs. TrueCrystallizationTemperature(TCT):The
temperature at which the sample spontaneously
rises ater precipitation onset. This point is only
valid i there is less than a 1.5C / 3F dierence
between FCTA and TCT.
LastCrystaltoDissolve(LCTD).Thetemperature
at which no more crystals are present when the
sample is heated.
From a thermodynamic point o view, FCTA, TCT,
and LCTD should be the same. In practice, kinetic
considerations imposed by the method cause
discrepancies.
The API procedure is designed to be reproducible
with minimal training and allows or a rapid sample
throughput or traditional oilfeld brines (halides).
Unortunately, ormate brines were not considered
when this method was developed. The API 13J
guidelines are thereore currently being rewritten
by an API workgroup.
Two problems discovered with the current API
method when applied to ormate brines are
supercooling and ormation o metastable phase
crystals. The enormous amount o supercooling that
takes place in ormate brines makes it impossible
or most laboratories to even reach the low
temperatures required to orm the frst crystals.
TCTs o ormate brines are thereore requently
reported as too low to be measured. When a low
enough temperature is reached, measurements areoten complicated by the ormation o metastable
potassium ormate crystals. In order to produce
meaningul TCT values or ormate brines, it is
thereore crucial to thoroughly understand the
chemistry o these brines and their complex
crystallization behavior.
A5.3 Crystallization mechanismsin ormate brines
A typical TCT curve or a brine system is shown in
Figure 1. This is a phase diagram consisting o
three phase equilibrium lines, an eutectic point, and
a critical point. The phase equilibrium line to the let
represents the brines reezing point. At conditions
along this line, ice crystals are in equilibrium with
the brine. The eutectic point represents the brine
composition (concentration) that gives the lowest
possible TCT. The center equilibrium line represents
the concentration range o the brine where a
hydrated version o the salt crystallizes. Along this
equilibrium line the hydrated salt crystal exists in
equilibrium with the brine. The right equilibrium line
represents the concentration range where dry salt
crystals precipitate. Along this equilibrium line, dry
salt exists in equilibrium with the brine. It is difcultto measure TCT at or just around the eutectic or
critical points. Metastable crystals can orm along
the stippled lines (shown in Figure 1). However,
extrapolating the measured equilibrium lines, which
intersect at the eutectic and critical points, can
generate good TCT curves.
All three ormate brines exhibit very dierent TCT
behavior. Sodium ormate (shown in Figure 4)
behaves just like the salt in Figure 1. Its TCT curve has
one critical point, where hydrated and dry salt orm.
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C A B O T S P E C I A L T Y F L U I D S
V E R S I O N 3 0 4 / 1 1
S E C T I O N A : C H E M I C A L A N D P H Y S I C A L P R O P E R T I E S
P A G E 3S E C T I O N A 5
The TCT curve o cesium ormate (Figure 6) has
no critical point, which means that only one
salt structure orms. Since cesium ormate is
known to exist as a monohydrate at ambient
conditions, this is the phase equilibrium line or
cesium ormate monohydrate in equilibrium with
cesium ormate brine. The critical point or the
cesium ormate TCT phase diagram is at a
temperature so high that it is impractical to measure.
Potassium ormate (Figure 5) exhibits very unusual
behavior as it precipitates crystals o two dierent
hydrated phases, here reerred to as metastable
and stable phases:
ThemetastablephasegivesalowTCT(around
-10C / 12F) or a concentrated (1.57 g/cm3 /
13.1 lb/gal) brine. This crystal phase is normally
crystallized spontaneously when a certain
degree o supercooling is reached or by seedingwith metastable potassium ormate crystals.
Thethermodynamicallystablephasegivesa
rather high TCT (around 7C / 19F) or a concen-
trated (1.57 g/cm3 / 13.1 lb/gal) brine. These
crystals orm rom the metastable phase crystals
ater some time (hours) in equilibrium with
saturated brine, or by seeding with stable
potassium ormate crystals.
The higher TCT, i.e. the one rom the stable phase,
is thermodynamically correct, and defned as the
scientifcally correct TCT. The TCT o the metastable
phase, on the other hand, oten contains more
useul inormation or many applications.
A5.4 Procedure or TCTdetermination in ormatebrines
With the standard API measuring method [1], the
supercooling eect can be overcome by using very
low cooling rates and cycling the temperature
between TCT and LCTD several times. Using low
cooling rates is not easible, however, when
determining TCT o uids with metastable phases.
A kinetic conversion may take place at any time,
potentially causing the measured TCT to graduallydrit rom the metastable phase TCT to the stable
phase TCT. In many cases, there is no knowledge
about which phase has been measured.
Consequently, Cabot Specialty Fluids (CSF) has
carried out extensive work on crystallization
behavior o ormate brines and on optimizing the
measuring method [2], [3], [4]. From this work, it
has been concluded that it is extremely important to
select the correct type o seeding material, and i
the correct seeding material is selected, the actual
Metastable phase TCT
Eutectic point
Water
Critical point
Ice
Salt-H2O
Salt
Typical TCT curve
Temperature
Brine concentration
Figure 1Typical TCT curve (or phase diagram) o brine, consisting o three phase equilibrium lines, an eutectic point and a critical point.
The phase equilibrium lines represent conditions where three dierent solid crystals exist in equilibrium with the brine. The eutectic point
represents the brine composition (concentration) with the lowest TCT, and the critical point is the point where the phase equilibrium lines
o the two dierent salt structures join.
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F O R M A T E T E C H N I C A L M A N U A L
S E C T I O N A 5
TCT measurement becomes relatively simple, with
no need or very low cooling rates. By seeding with
crystals o the same kind that crystallize rom the
test brine, one can make consistent and good
measurements, which are not inuenced by
supercooling. For potassium ormate brines and
their blends with metastable phase TCT, the
collection and storage method or seeding crystals
determines which phase is measured.
A5.4.1 Selecting and preparing seeding
material
Selection o seeding material is critical or measuring
TCT in ormate brines. Both the problem o super-
cooling and those associated with metastable phases
orming in potassium ormate and potassium
ormate blends are overcome by selecting a
suitable seeding material.
The rule is simple: Use the same kind o seeding
crystals as those crystallizing rom the test brine.The crystals should be prepared by crystallization
(not drying) and kept in a reezer.
Seeding material should be selected according to
the ollowing guidelines:
Single-saltbrines: For any low-density brines
that precipitate to the let side o the eutectic
point (re. Figure 1), i.e. the part where water
reezes out, no special seeding material is
required. For higher density brines that precipitate
to the right o the eutectic point, where hydrated
or dry salts crystallize, seed with a stable crystal
o this salt (see Figure 3 to Figure 5). Use a
potassium ormate metastable crystal to measure
the metastable phase TCT o a potassium
ormate brine.
Blendedbrines(e.g. a cesium / potassium
ormate blend, Figure 6): For brines to the let o
the eutectic point, where potassium ormate
crystals precipitate frst, seed with a stable
potassium ormate crystal. Alternatively, use a
metastable potassium ormate crystal to measure
the blends metastable TCT. For higher density
brines to the right o the eutectic point, use a
cesium ormate seeding crystal.
Seeding crystals are easiest prepared in the reezer(set at -45C / -49F or lower) according to the
ollowing method:
Placeasampleofbrineinacleanplasticsample
bottle in the reezer.
Addseedingcrystalstothebrineatanytemperature
lower than 10C / 50F below its expected TCT.
For potassium ormate brines, be aware that
seeding with stable phase crystals gives stable
phase crystals and seeding with metastable
crystals gives metastable crystals. The seeding
crystal needs to be o the same type as those
required. Crystallization time varies rom a ew
seconds to a ew hours ater seeding depending
on the samples TCT.
Ifseedingcrystalsarepreparedforthersttime,
i.e. no seeding crystals are available or seeding;
they need to orm rom a brine that crystallizes
along the same phase equilibrium line (re. Figure 1),
but that has a high enough TCT to overcome
supercooling at reezer temperature. For potassium
ormate, whenever crystals are ormed rom such
a spontaneous crystallization process, these
crystals are always metastable. They can then be
converted to stable crystals by leaving them or
some time at higher temperature. This is tricky,
so always keep a sample in the reezer once
success is frst achieved.
Stablephasecrystalsremainstableforever.
Metastable (potassium ormate) crystals should
remain metastable as long as they are kept at low
enough temperature. However, always be
prepared or a situation where these can transormto stable phase crystals.
A5.4.2TCT determination method
The method used by CSF or determining TCT is
based on the API recommended method [1].
Beore TCT measurement can start, determine an
approximate TCT or the sample. This is easiest
completed using the inormation already available in
Figures 4 to 6. By knowing brine type and density,
TCT can be predicted with airly high accuracy.
CSF uses a Grant GR-150 cooling bath controlled by
LabwiseTM sotware. Attached to the bath is a
liquid-cooled sample cup with a stirrer. The test
brine is added directly to this cup. The ollowing
procedure should be ollowed to measure stable
phase TCT:
ProgramtheLabwiseTM temperature controller to
set the frst target temperature at approximately
8C / 14F below approximate TCT.
Whensampletemperatureisaround1C/2F
below its approximate TCT add a seeding crystal.
As soon as the frst crystals appear, note the
temperature (FCTA = First Crystal To Appear). At
this point, the stirring rate should be reduced and
temperature should increase by 1 3C / 2 4Fbeore alling again. The maximum temperature
obtained at this stage is the frst estimation o TCT.
Oncetemperaturestartstodecrease,adjustthe
cooling bath to 2C / 4F above the frst TCT
estimation and switch the cooling system o.
Observe the sample or the Last Crystal To
Dissolve (LCTD) and note temperature. I the
sample has become completely solid, temperature
should rise slowly in small increments until the
sample is completely crystal-ree.
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P A G E 5S E C T I O N A 5
Oncethesampleiscompletelycrystalfree,repeat
this cooling / heating cycle two to three times.
Duringthemeasuringprocess,stirringspeed
should be kept high, but lowered to watch or
signs o FCTA and LCTD.
TCTcanbecalculatedasanaverageofthe
repeat measurements detailed above. Discrepancies
o around 1C / 2F between the results are
normal. However, i one result is signifcantly
lower, this should be rejected.
To measure metastable phase TCT in a potassium
ormate brine or a potassium ormate blend the
same method should be used, with the ollowing
exceptions:
Ametastablecrystalofthebrineitselfshouldbe
used or seeding.
Duringthetemperaturecyclingsteps,crystalscan
start converting to stable phase crystals at any
time. This is represented by a sudden increase in
TCT rom one cycle to another. TCT eventuallystabilizes again at the stable phase TCT. The
correct metastable phase TCT is calculated as an
average o TCTs measured beore this sudden
increase. How likely the brine is to convert to
stable phase during the temperature cycling
depends on the amount o heating applied in
each temperature cycle and brine type or
concentration. The activation energy required to
transorm crystals to the stable phase depends
on brine concentration (or single salt brines) and
brine composition (or blended salts). A typical
temperature plot showing a transition rom
metastable to stable phase potassium ormate
crystals is shown in Figure 2.
A5.5TCT data or ormatebrines
The TCT data presented in this section are a
combination o TCT data measured by CSF and
TCT data taken rom various other sources. All
curves have been verifed with CSFs recommended
test method. As CSFs method involves seeding
with crystals o the ormate brine itsel, these
curves are likely to be rather conservative (read
higher values) than what one could expect rom
other methods.
TCT or single-salt brines are shown in Figure 3 to
Figure 6 and Table 1 to Table 3. Figures 4, 5, and 6
also show some measured points representingsupercooling. This is the temperature where the
brine has successully been held or at least two
weeks in the presence o traditional seeding
material and other particles (barite, bentonite, rust,
dust, etc.) without crystallizing. With the use o less
sophisticated measuring techniques that do not use
crystals o the brine itsel or seeding, measured
TCT values can typically be ound anywhere in the
range between the supercooling points and the
TCT curve.
Crystallized potassium formate transferring from metastable to stable phase
Temperature
Time
Stable TCT
Metastable TCT
Figure 2Temperature as a unction o time during a TCT measuring test where the crystallized potassium ormate transers rom a
metastable phase crystal to a stable phase crystal.
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F O R M A T E T E C H N I C A L M A N U A L
S E C T I O N A 5
A5.5.1 TCT in single-salt sodium ormate
TCT as a unction o uid density or a pure sodium
ormate single-salt brine is presented in Figure 4
and Table 1. The data represent a mixture o
measurements completed by Shell [5] and newer
measurements by Cabot Specialty Fluids and Baroid.
A5.5.2TCT in single-salt potassium
ormate
TCT as a unction o uid density or a pure
potassium ormate single-salt brine is presented in
Figure 5 and Table 2. Freezing point data (the
phase equilibrium line to the let o the eutectic
point) has been taken rom OSCA [6]. Stable and
metastable crystallization temperatures (the phase
equilibrium lines to the right o the eutectic point)
are all measured by CSF [3] according to the
method described above.
A5.5.3TCT in single-salt cesium ormate
TCT as a unction o uid density or a pure cesiumormate single-salt brine is presented in Figure 6
and Table 3. Freezing-point data (the phase
equilibrium line to the let o the eutectic point) has
been taken rom Shell [5]. Crystallization tempera-
tures (the phase equilibrium line to the right o the
eutectic point) are all measured by CSF [2][3]
according to the method described above.
A5.5.4TCT in blended ormate brines
When concentrated cesium ormate and concen-
trated potassium ormate are blended, the blends
TCT depends on the blend ratio. An eutectic point
(minimum TCT) is achieved at around 50 / 50 blend
ratio or, more exactly, at a density o 1.91 g/cm3 /
15.9 lb/gal (see Figure 7 or a blend o 1.57 g/cm3 /
13.1 lb/gal potassium ormate brine and 2.20 g/cm3 /
12.9 lb/gal cesium ormate brine). In winter, blends
are oten made rom more diluted potassium ormate
brine (1.54 g/cm3 / 12.9 lb/gal), which lowers TCT.
Some blends also retain a sae TCT even i water is
removed. The TCT curve in Figure 7 should
thereore not be used as a defnitive guide to TCTs
in blended cesium and potassium ormate blends
supplied by CSF.
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S E C T I O N A : C H E M I C A L A N D P H Y S I C A L P R O P E R T I E S
P A G E 7S E C T I O N A 5
Figure 3 True Crystallization Temperature (TCT) or sodium, potassium, and cesium ormate brines.
-80
-60
-40
-20
0
20
40
60
80
100
8 9 10 11 12 13 14 15 16 17 18 19 20
NaFoKFo stable phaseKFo metastable phase
CsFo
-70
-60
-50
-40
-30
-20
-10
0
10
20
30
1.0 1.1 1.2 1.3 1.4 1.5 1.6 1.7 1.8 1.9 2.0 2.1 2.2 2.3
NaFo
KFo stable phaseKFo metastable phaseCsFo
TCT of formate brines
TCT of formate brines
Density [lb/gal]
Temperature[C]
Temperature[F]
METRIC
FIELD
Density (g/cm3)
METRIC
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P A G E 8 V E R S I O N 3 0 4 / 1 1
F O R M A T E T E C H N I C A L M A N U A L
S E C T I O N A 5
Figure 4 True Crystallization Temperature (TCT) or sodium ormate (single salt). The supercooling points represent the temperature
where the uid has been successully kept or at least two weeks in the presence o standard seeding material.
-20
-10
0
10
20
30
40
50
60
8.2 8.4 8.6 8.8 9.0 9.2 9.4 9.6 9.8 10.0 10.2 10.4 10.6 10.8 11.0 11.2
NaFo
NaFo supercooling
-25
-20
-15
-10
-5
0
5
10
15
20
1.00 1.05 1.10 1.15 1.20 1.25 1.30 1.35
NaFo
NaFo supercooling
Density [lb/gal]
Density (g/cm3)
Temperature[C]
Temperature[F]
METRIC
FIELD
TCT sodium formate single salt
TCT sodium formate single salt
FIELD
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S E C T I O N A : C H E M I C A L A N D P H Y S I C A L P R O P E R T I E S
P A G E 9S E C T I O N A 5
Table 1True Crystallization Temperature (TCT) or sodium ormate single salt.
METRIC FIELD
Density TCT Density TCT
[g/cm3] [C] [lb/gal] [F]
1.00 0.0 8.34 32.0
1.01 -0.7 8.40 31.21.02 -1.6 8.50 29.4
1.03 -2.5 8.60 27.5
1.04 -3.4 8.70 25.5
1.05 -4.4 8.80 23.3
1.06 -5.4 8.90 21.0
1.07 -6.5 9.00 18.4
1.08 -7.8 9.10 15.5
1.09 -9.1 9.20 12.3
1.10 -10.6 9.30 8.8
1.11 -12.1 9.40 4.9
1.12 -13.9 9.50 0.6
1.13 -15.7 9.60 -4.2
1.14 -17.8 9.70 -5.9
1.15 -20.0 9.80 3.8
1.16 -22.5 9.90 12.5
1.17 -18.2 10.00 20.2
1.18 -13.9 10.10 26.9
1.19 -10.0 10.20 32.7
1.20 -6.4 10.30 37.4
1.21 -3.3 10.40 41.2
1.22 -0.5 10.50 44.0
1.23 1.9 10.60 45.7
1.24 3.9 10.70 47.6
1.25 5.5 10.80 54.2
1.26 6.7 10.90 60.0
1.27 7.6 11.00 65.2
1.28 8.0 11.10 69.8
1.29 10.7
1.30 13.6
1.31 16.2
1.32 18.61.33 20.7
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P A G E 1 0 V E R S I O N 3 0 4 / 1 1
F O R M A T E T E C H N I C A L M A N U A L
S E C T I O N A 5
Figure 5 True Crystallization Temperature (TCT) or potassium ormate (single salt). The stable phase TCT is measured by seeding with
stable phase potassium ormate crystals. The metastable phase TCT is measured by seeding with metastable phase potassium ormate
crystals. The supercooling points indicate the temperature where the uid has been successully kept or at least two weeks in the
presence o standard seeding material.
TCT potassium formate single salt
TCT stable phase
TCT stable phase extrapolated
TCT metastable phase
TCT metastable phase extrapolated
KFo supercooling
-80
-70
-50
-60
-40
-30
-20
-10
0
10
20
30
40
50
60
70
80
90
8.0 8.5 9.0 9.5 10.0 10.5 11.0 11.5 12.0 12.5 13.0 13.5 14.0
-60
-50
-40
-30
-20
-10
0
10
20
30
1.00 1.05 1.10 1.15 1.20 1.25 1.30 1.35 1.40 1.45 1.50 1.55 1.60 1.65
TCT stable phase
TCT stable phase extrapolated
TCT metastable phase
TCT metastable phase extrapolated
KFo supercooling
Density [lb/gal]
Density [g/cm3]
Temperature[C]
Temperature[F]
METRIC
FIELD
TCT potassium formate single salt
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P A G E 1 1S E C T I O N A 5
Table 2True Crystallization Temperature (TCT) or potassium ormate single salt.
METRIC FIELD
DensityTCT
(stable)TCT (metastable) Density
TCT(stable)
TCT (metastable)
[g/cm3] [C] [C] [lb/gal] [F] [F]
1.00 0.0 8.34 30.8
1.01 -1.2 8.40 30.1
1.02 -1.7 8.50 28.9
1.03 -2.4 8.60 27.5
1.04 -3.1 8.70 25.9
1.05 -3.9 8.80 24.1
1.06 -4.8 8.90 22.1
1.07 -5.8 9.00 20.0
1.08 -6.8 9.10 17.7
1.09 -7.9 9.20 15.2
1.10 -9.1 9.30 12.5
1.11 -10.4 9.40 9.7
1.12 -11.7 9.50 6.7
1.13 -13.1 9.60 3.5
1.14 -14.6 9.70 0.2
1.15 -16.1 9.80 -3.3
1.16 -17.7 9.90 -6.9
1.17 -19.3 10.00 -10.7
1.18 -21.0 10.10 -14.71.19 -22.7 10.20 -18.8
1.20 -24.6 10.30 -23.0
1.21 -26.4 10.40 -27.4
1.22 -28.3 10.50 -31.9
1.23 -30.3 10.60 -36.6
1.24 -32.3 10.70 -41.3
1.25 -34.4 10.80 -46.3
1.26 -36.5 10.90 -51.3
1.27 -38.6 11.00 -56.5
1.28 -40.8 11.10 -61.8
1.29 -43.0 11.20 -67.2
1.30 -45.3 11.30 -58.6
1.31 -47.5 11.40 -49.4
1.32 -49.9 11.50 -40.7
1.33 -52.2 11.60 -32.31.34 -54.6 11.70 -24.3 -71.9
1.35 -52.1 11.80 -16.8 -63.0
1.36 -47.8 11.90 -9.6 -54.5
1.37 -43.6 12.00 -2.9 -46.4
1.38 -39.6 12.10 3.4 -38.8
1.39 -35.7 12.20 9.3 -31.6
1.40 -32.0 -58.6 12.30 14.8 -24.9
1.41 -28.5 -54.4 12.40 19.9 -18.6
1.42 -25.1 -50.3 12.50 24.6 -12.7
1.43 -21.8 -46.5 12.60 28.9 -7.3
1.44 -18.8 -42.8 12.70 32.8 -2.4
1.45 -15.9 -39.3 12.80 36.2 2.2
1.46 -13.1 -36.0 12.90 39.3 6.3
1.47 -10.5 -32.8 13.00 42.0 9.9
1.48 -8.1 -29.8 13.10 44.2 13.1
1.49 -5.8 -27.0 13.20 46.0 15.91.50 -3.7 -24.3 13.30 47.4 22.8
1.51 -1.7 -21.8 13.40 65.6 41.2
1.52 0.1 -19.5 13.50 89.3 59.7
1.53 1.8 -17.3
1.54 3.3 -15.4
1.55 4.6 -13.5
1.56 5.8 -11.9
1.57 6.8 -10.4
1.58 7.7 -9.1
1.59 8.4 -8.0
1.60 12.4 0.4
1.61 23.4 14.2
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C A B O T S P E C I A L T Y F L U I D S
P A G E 1 2 V E R S I O N 3 0 4 / 1 1
F O R M A T E T E C H N I C A L M A N U A L
S E C T I O N A 5
Figure 6True Crystallization Temperature (TCT) or cesium ormate (single salt). The supercooling points indicate the temperature where
the uid has been successully kept or at least two weeks in the presence o standard seeding material.
TCT cesium formate single salt
-80
-70
-60
-50
-40
-30
-20
-10
0
10
20
30
40
50
60
70
80
90
8 9 10 11 12 13 14 15 16 17 18 19 20 21
TCT CsFo
TCT CsFo extrapolated
CsFo supercooling
-70
-60
-50
-40
-30
-20
-10
0
10
20
30
1.0 1.1 1.2 1.3 1.4 1.5 1.6 1.7 1.8 1.9 2.0 2.1 2.2 2.3 2.4 2.5
TCT CsFo
TCT CsFo extrapolated
CsFo supercooling
Density [lb/gal]
Density [g/cm3]
Temperature[C]
Temperature[F]
METRIC
FIELD
TCT cesium formate single salt
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C A B O T S P E C I A L T Y F L U I D S
V E R S I O N 3 0 4 / 1 1
S E C T I O N A : C H E M I C A L A N D P H Y S I C A L P R O P E R T I E S
P A G E 1 3S E C T I O N A 5
Table 3 True Crystallization Temperature (TCT) or cesium ormate single salt.
METRIC FIELD
Density TCT Density TCT
[g/cm3] [C] [lb/gal] [F]
1.00 0.0 8.34 32.0
1.05 -1.0 8.5 31.4
1.10 -2.3 9.0 29.01.15 -3.8 9.5 25.9
1.20 -5.5 10.0 22.2
1.25 -7.5 10.5 17.8
1.30 -9.8 11.0 12.8
1.35 -12.3 11.5 7.2
1.40 -15.0 12.0 1.0
1.45 -18.0 12.5 -5.9
1.50 -21.2 13.0 -13.4
1.55 -24.7 13.5 -21.6
1.60 -28.4 14.0 -30.4
1.65 -32.4 14.5 -39.8
1.70 -36.6 15.0 -49.8
1.75 -41.0 15.5 -60.5
1.80 -45.7 16.0 -71.8
1.85 -50.6 16.2 -70.41.90 -55.8 16.3 -61.9
1.92 -58.0 16.4 -53.9
1.94 -57.4 16.5 -46.2
1.96 -49.6 16.6 -38.9
1.98 -42.5 16.7 -32.0
2.00 -35.9 16.8 -25.5
2.02 -30.0 16.9 -19.3
2.04 -24.5 17.0 -13.5
2.06 -19.6 17.1 -8.0
2.08 -15.1 17.2 -2.8
2.10 -11.0 17.3 2.1
2.12 -7.2 17.4 6.8
2.14 -3.8 17.5 11.2
2.16 -0.7 17.6 15.3
2.18 2.2 17.7 19.3
2.20 4.9 17.8 23.02.22 7.4 17.9 26.5
2.24 9.9 18.0 29.9
2.26 12.2 18.1 33.1
2.28 14.5 18.2 36.2
2.30 16.9 18.3 39.1
2.32 19.2 18.4 41.9
2.34 21.7 18.5 44.7
2.36 24.3 18.6 47.3
2.38 27.1 18.7 49.9
2.40 30.1 18.8 52.4
18.9 55.0
19.0 57.5
19.1 60.0
19.2 62.5
19.3 65.019.4 67.6
19.5 70.3
19.6 73.1
19.7 75.9
19.8 78.9
19.9 82.0
20.0 85.2
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C A B O T S P E C I A L T Y F L U I D S
P A G E 1 4 V E R S I O N 3 0 4 / 1 1
F O R M A T E T E C H N I C A L M A N U A L
S E C T I O N A 5
Figure 7 True Crystallization Temperature (TCT) or a blend o 1.57 g/cm3 / 13.10 lb/gal potassium ormate and a 2.20 g/cm3 / 18.36 lb/gal
cesium ormate. The stable phase TCT is measured by seeding with stable phase potassium and cesium ormate crystals, whilst the
metastable phase TCT is measured by seeding with metastable potassium ormate crystals. Blends o potassium and cesium ormate
used in the feld can contain more or less water than this standard blend, so feld brine TCTs might be higher or lower than shown in
this plot.
12.0 12.5 13.0 13.5 14.0 14.5 15.0 15.5 16.0 17.0 17.5 18.0 18.5 19.016.5
-30
-20
-10
0
10
20
30
40
50
-45
-40
-35
-30
-25
-20
-15
-10
-5
0
5
10
15
1.45 1.50 1.55 1.60 1.65 1.70 1.75 1.80 1.85 1.90 1.95 2.00 2.05 2.10 2.15 2.20 2.25
Density [lb/gal]
Density [g/cm3]
Temperature[C]
Temperature[F]
METRIC
FIELD
TCT and supercooling data for blended Cs and K formate
TCT and supercooling data for blended Cs and K formate
CsKFo stable phaseCsKFo metastable phaseCsFo
KFo stable phaseKFo metastable phaseCsKFo supercooling
CsKFo stable phaseCsKFo metastable phaseCsFoKFo stable phaseKFo metastable phase
CsKFo supercooling
-40
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C A B O T S P E C I A L T Y F L U I D S
V E R S I O N 3 0 4 / 1 1
S E C T I O N A : C H E M I C A L A N D P H Y S I C A L P R O P E R T I E S
P A G E 1 5S E C T I O N A 5
A5.6 Pressurized crystallizationtemperature PCT
A5.6.1 Introduction
In deep-water environments, crystallization can
become a serious problem. High pressure and low
temperature can cause the salts in high-density brine
solutions to become more susceptible to crystallization.
Extremely high pressure and low temperatures are
normally encountered at the mud line and during
pressure testing o equipment. Pressure as high as
16,000 to 18,000 psi is not unusual. Thereore, it is o
great importance to know the crystallization
temperature or the uid at realistic pressure conditions.
There are two major problems associated with PCT
measurements in general. The frst problem is the lack
o a dependable standardized method. The second
problem is the poor availability o high-pressure
testing equipment to identiy the TCT under dynamic
conditions o pressure and temperature. For ormatebrines, with the additional difculties o extreme
supercooling and existence o metastable phases,
these measurements become extremely complicated.
A5.6.2 Methods or determining PCT in
ormate brines
PCT measurements o ormate brines have been
carried out at two test laboratories: Westport
Technology Center International and Baroid. The
test methods that have been used to determine
PCT in ormates are:
Westport Technology Center International:
acoustic method
Westport has chosen an acoustic method or
determination o PCT. This technique was chosen
due to serious limitations in standard determination
techniques, such as visual detection, temperature-
time-plot, and volume change. The equipment can
measure down to -30C / -22F. The pressure
range is rom 0.07 to 140 MPa / 10 to 20,000 psi,
and the sample volume is rom 5 to 350 mL. Both
the arrival time o the acoustic wave and attenuation
o the wave amplitude are unctions o the number
o solid particulate in the brine solution.
To ensure temperature and compositionhomogeneity, the cell is rocked back and orth,
which also helps reduce the supercooling eects.
The acoustic cell sits in a controlled temperature
chamber with a circulation system that provides
uniorm temperature distribution and cooling rates.
Baroid: Fiber optics technique
Baroid uses the ollowing methods or determining
crystallization:
Visual(beroptics)
Volumechange
Temperatureinectionpoint
The cell volume is 70 mL. The cell is equipped with a
stir disk. Testing starts at 10,000 psi and decreases
to the base line o 100 psi in 2,500 psi increments.
The test includes our cycles at each pressure
stage to check or supercooling eects. Each test
takes 16 to 21 hours with 0.05g o 5 micron marble
used as seeding agent.
A5.6.3 PCT data or ormate brines
By using the two measurement methods described
above some limited PCT values have been determined.
PCT data or a 2.195 g/cm3 / 18.3 lb/gal
cesium ormate brine with and without
0.5% KCl
TCT was measured as a unction o pressure or a
2.195 g/cm3 / 18.3 lb/gal buered cesium ormate
brine with and without the addition o 5% KCl.
KClwas added to reduce TCT. The tests were
completed at Westport Technology Center according
to its acoustic technique described above. Theresults are listed in Table 4 and plotted in Figure 8.
PCT data or various ormate brines
and blends
Baroid has carried out a number o PCT tests on
ormate uids by using their fber optics detection
technique mentioned above.
TCT as a unction o pressure (up to 20,000 psi)
was measured on buered, saturated cesium
ormate brine (2.18 g/cm3 / 18.18 lb/gal). The test
results are shown in Table 5 and plotted in Figure 8.
Similar tests were carried out on several buered
ormate brines: 1.32 g/cm3 / 11.01 lb/gal sodium
ormate, 1.58 g/cm3 / 13.17 lb/gal potassium
ormate, 2.18 g/cm3 / 18.18 lb/gal cesium ormate,
2.2 g/cm3 / 18.34 lb/gal cesium ormate, and 1.52
g/cm3 / 12.67 lb/gal potassium / cesium ormate.
From Figure 8 it can be seen that there is very
good consistency between the two methods o
PCT measurements. Also, by comparing the TCTs
when no pressure is applied, it is ound that the
TCTs measured with these instruments are similar
to the ones measured in standard TCT tests.
For cesium ormate and cesium / potassium
ormate blends, the ollowing rule o thumb applies:
Cs&Cs/K formate:
Increase in TCT ~ 1F per 1,000 psi
pressure increase.
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C A B O T S P E C I A L T Y F L U I D S
P A G E 1 6 V E R S I O N 3 0 4 / 1 1
F O R M A T E T E C H N I C A L M A N U A L
S E C T I O N A 5
Pressure PCT 2.195 g/cm3 / 18.3 lb/gal CsFoPCT 2.195 g/cm3 / 18.3 lb/gal CsFo
+5%KCl
[MPa] [psi] [C] [F] [C] [F]
0.14 21 7.2 41.0 -4.7 23.6
20.7 3,000 -2.3 27.834.5 5,000 7.5 42.048.3 7,000 -1.9 28.668.9 10,000 10.2 50.4 -0.33 31.4
Table 4TCT as a unction o pressure or a buered 2.195 g/cm3 / 18.3 lb/gal cesium ormate brine with and without 5% KCl. Measured
at Westport Technology Center International.
Table 5TCT as a unction o pressure or a variety o ormate brines and blends. The measurements have been carried out by Baroid. The
1.52 g/cm3 / 12.7 lb/gal potassium / cesium ormate blend has been designed specifcally to lower TCT / PCT.
Pressure PCT
[MPa] [psi] [C] [F]
1.32 g/cm3 / 11.0 lb/gal
NaFo
0.69 100 10.39 61.217.24 2,500 12.78 62.334.47 5,000 12.33 63.051.71 7,500 16.28 63.5
68.95 10,000 17.06 65.5
1.58 g/cm3 / 13.2 lb/gal
KFo
0.69 100 -8.3 17.017.24 2,500 -4.3 24.234.47 5,000 -2.0 28.451.71 7,500 0.56 33.068.95 10,000 1.96 35.5
1.52 g/cm3 / 12.7 lb/gal
KCsFo
0.69 100 -6.03 21.217.24 2,500 -4.67 23.634.47 5,000 -3.42 25.951.71 7,500 -2.18 28.168.95 10,000 -2.40 27.7
2.20 g/cm3 / 18.3 lb/gal
CsFo buffered
0.69 100 5.3 41.517.24 2,500 6.7 44.034.47 5,000 8.2 46.751.71 7,500 9.6 49.368.95 10,000 11.2 52.2
2.18 g/cm3 / 18.2 lb/gal
CsFo
132.5 19,221 15.5 59.9117.8 17,086 13.9 57.1102.2 14,830 12.6 54.786.7 12,574 11.0 51.871.4 10,352 9.2 48.568.2 9,888 10.8 51.451.2 7,433 8.4 47.234.3 4,969 7.2 44.917.1 2,476 5.7 42.30.56 81 4.2 39.6
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C A B O T S P E C I A L T Y F L U I D S
V E R S I O N 3 0 4 / 1 1
S E C T I O N A : C H E M I C A L A N D P H Y S I C A L P R O P E R T I E S
P A G E 1 7S E C T I O N A 5
Figure 8TCT as a unction o pressure or a variety o ormate brines and blends.
10
15
20
25
30
35
40
45
50
55
60
65
70
75
80
0 2 000 4 000 6 000 8 000 10 000 12 000 14 000 16 000 18 000 20 000
-10
-8
-6
-4
-2
0
2
4
6
8
10
12
1416
18
20
22
0 10 20 30 40 50 60 70 80 90 100 110 120 130 140
Pressure [psi]
Pressure [MPa]
TCT
[C]
TCT
[F]
METRIC
FIELD
PCT in various formate brines and blends
1.32 g/cm3 NaFo (Baroid)
2.20 g/cm3 CsFo-buffered (Baroid)
2.12 g/cm3 CsFo (Westport)
2.18 g/cm3 CsFo (Baroid)
2.20 g/cm3 CsFo + 5% KCl (Westport)
1.52 g/cm3 KCsFo (Baroid)
1.58 g/cm3 KFo (Baroid)
PCT in various formate brines and blends
11.0 lb/gal NaFo (Baroid)
18.3 lb/gal CsFo-buffered (Baroid)
18.3 lb/gal CsFo (Westport)
18.2 lb/gal CsFo (Baroid)
18.3 lb/gal CsFo + 5% KCl (Westport)
12.7 lb/gal KCsFo (Baroid)
13.2 lb/gal KFo (Baroid)
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C A B O T S P E C I A L T Y F L U I D S
P A G E 1 8 V E R S I O N 3 0 4 / 1 1
F O R M A T E T E C H N I C A L M A N U A L
S E C T I O N A 5
A5.7 How to apply TCT / PCTdata in the feld
Although the scientifcally correct uid TCT is the
thermodynamically stable one, i.e. the highest one
measured, this might not be the most suitable TCT
value to use when ormulating drilling and completion
uids. As ormates supercool more than other
brines, and potassium ormate brines and their
blends precipitate metastable phase crystals, it is
impossible to apply measured TCT data in the
same way as in other brines.
Storage o potassium ormate brine (and ormate
blends with a high potassium ormate content) in
tanks is a good example o this. In the absence o a
stable-phase potassium ormate seeding crystal, a
thermodynamically stable phase cannot be ormed
beore metastable crystals exist in the uid. Thereore,
this uid can be stored saely at temperatures
down to the TCT o the metastable phase, or evenlower due to supercooling. In periods when
temperatures outside the tank go beyond the TCT
o the metastable phase, metastable crystals may
orm locally at the sides o the tank, although the
bulk temperature in the uid inside the tank is
signifcantly above this temperature. The extent o
this crystallization is limited, but within a ew hours
the transormation to thermodynamically stable
crystals can occur. These stable phase crystals
serve as seeding crystals or thermodynamically
stable-phase crystals to orm in the whole storage
tank, assuming bulk temperature inside the tank is
below the TCT o the stable phase. Crystallization
will be substantial as the uid can be regarded as
heavily supersaturated with respect to this type o
crystallization. In order to dissolve these crystals
again, the temperature obviously needs to be
above the LCTD value o the stable phase, which is
signifcantly higher than the LCTD temperature o
the metastable phase.
Thereore, potassium ormates can saely be
stored down to the lower TCT o the metastable
phase, and even lower due to supercooling.
However, one should keep in mind that localized
cooling and crystallization at the wall o the
container can have drastic consequences or theextent o crystallization and the ability to dissolve
the crystals aterwards.
A5.8 How to lower crystallizationtemperature o ormatebrines
In some applications it might be desirable to lower
the crystallization temperature o ormate brines
and blends.
A5.8.1 Lowering TCT in single-salt
ormate brines
TCT can be lowered in single-salt ormate brines by
adding chloride ions. The lowering o TCT by adding
15% and 20% potassium chloride to a sodium
ormate brine has been demonstrated by Shell [5],
and is shown in Figure 9.
Care should be taken, however, when adding
chloride ions to a ormate brine. Chloride is known
to cause localized corrosion problems, and is hard
to remove.
A5.8.2 Lowering TCT in ormate blends
In certain deepwater applications there is need or
ormate brine with the typical density o single-salt
potassium ormate brine, but with lower TCT than
can be obtained by this single-salt brine alone. In
this case, a blended potassium / cesium ormate
brine can be ormulated with some additional water
added.
Reerences
[1] API RP 13J: Testing o Heavy Brines.
[2] Obi, A.S.: Measurements o True Crystallisation
Temperature in High Density Caesium Brines used
in Drilling Fluids, MSc Thesis, Robert Gordon
University, Aberdeen, September 2008.
[3] Chrenowski, M.: TCT Behaviour o Formate
Drilling and Completion Fluids, MSc Thesis, Robert
Gordon University, Aberdeen, September 2009.
[4] TCT Cesium Potassium Formate Blends, Lab
Report LR-406, Cabot Operations & Technical
Support Laboratory, Aberdeen, September 2010.
[5] Howard, S.K., Houben, R.J.H., Oort, E. van, and
Francis, P.A.: Formate drilling and completion uids
Technical Manual, Shell Report SIEP 96-5091, 1996.
[6] OSCA report: Crystallization Temperatures or
Potassium Formate Brines Formate Brine Project
Task #1, March 1995.
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C A B O T S P E C I A L T Y F L U I D S
V E R S I O N 3 0 4 / 1 1
S E C T I O N A : C H E M I C A L A N D P H Y S I C A L P R O P E R T I E S
P A G E 1 9S E C T I O N A 5
Figure 9TCT in single-salt sodium ormate brine. Eect o adding 15% and 20% KClto a sodium ormate brine [5].
TCT sodium formate single salt
-20
-10
0
10
20
30
40
50
60
8.2 8.4 8.6 8.8 9.0 9.2 9.4 9.6 9.8 10.0 10.2 10.4 10.6 10.8 11.0 11.2
NaFo
NaFo +15% KCl
NaFo +20% KCl
TCT sodium formate single salt
-30
-25
-20
-15
-10
-5
0
5
10
15
20
1.00 1.05 1.10 1.15 1.20 1.25 1.30 1.35
NaFo
NaFo +15% KCl
NaFo +20% KCl
Temperature[C]
Temperature[F]
METRIC
FIELD
Density [lb/gal]
Density [g/cm3]