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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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    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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    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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    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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    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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    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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    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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    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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    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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    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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    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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    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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    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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    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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    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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    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]