8. Squeeze Cementing

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    Section 8

    Squeeze Cementing

    Table of Contents

    Introduction................................................................................................................................................8-3

    Topic Areas ............................................................................................................................................ 8-3

    Learning Objectives ...............................................................................................................................8-3

    Unit A: Squeeze Cementing Background ..................................................................................................8-3

    Purposes of Squeeze Cementing ............................................................................................................8-3Squeeze Cementing Terminology .......................................................................................................... 8-4

    Hesitation ...............................................................................................................................................8-5

    Planning Squeeze Cementing Jobs.........................................................................................................8-5

    Unit A Quiz ............................................................................................................................................ 8-6

    Unit B: Squeeze Cementing Calculations..................................................................................................8-7

    Squeeze Problem One ............................................................................................................................8-9

    Squeeze Problem Two..........................................................................................................................8-17

    Unit B Quiz .......................................................................................................................................... 8-22

    Answers to Unit Quizzes ......................................................................................................................... 8-23

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    Use for Section Notes

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    Introduction

    If all primary cementing jobs were completely

    successful, there would rarely be a need for

    squeeze cementing. However, if drilling mud

    has been bypassed (channeling) during the

    primary job, squeeze cementing may be required

    to correct or remediate the problem.

    Squeeze cementing is the process by which

    cement is forced into the casing-hole annulus.Fluid returns are not normally expected at the

    surface. Perforations in the pipe are often

    required to obtain a flow path to the annulus.

    The channel or area of poor bond, as well as the

    perforations, are filled with cement. Pumppressure is allowed to rise in order to "squeeze"

    cement slurry into the desired area. Thecement

    is allowed to harden into a plug which blocks

    fluid movement. Drill-out of set cement inside

    the casing is normally required.

    Existing production perforations may be

    abandoned by squeeze cementing. Also, casing

    leaks due to pipe corrosion may be sealed with

    this process. The bottom of casing strings (shoe)

    and liner tops may also require squeezing tocorrect problems. These types of jobs may not

    require perforating prior to squeezing.

    Topic Areas

    In this section, these units will be included:

    A. Squeeze Cementing Background

    B. Squeeze Cementing Calculations

    Learning Objectives

    Upon completion of this section, you should be

    familiar with:

    The purposes of squeeze cementing

    How to calculate a basic squeeze cementingjob

    Unit A: Squeeze Cementing Background

    To perform a successful squeeze job, it is first

    necessary to become familiar with

    the purposes of squeeze cementing

    terminology associated with squeezecementing

    planning considerations for squeeze jobs.

    Purposes of SqueezeCementing

    Some of the more common reasons for

    performing a squeeze job are

    to correct a defective primary cementing jobcaused by channeling or insufficient fill-up

    to provide a seal for places purposely notcemented during primary cementing for

    example, squeezing liner tops

    to reduce the gas/oil ratio by shutting offsome of the gas-producing perforation

    (isolating the gas and oil zones)

    to improve the oil/water ratio by shutting offsome of the water-producing formation

    (isolating the oil and water zones) to close-off an unproductive formation from

    the wellbore

    to prevent fluid migration

    to repair casing holes caused by corrosion,perforation, etc. (Fig. 8.1)

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    Figure 8.2 Whole cement slurry does notenter the formation

    In squeeze jobs, forcing the formation to fractureis not the objective. If the formation fractures, it

    will break down. Then whole cement slurry (not

    just the filtrate) will be displaced into the

    formation. Therefore, care must be taken so that

    the pump pressure and the pressure exerted by

    the weight of the fluid are not sufficient to force

    a fracture of the formation. The pressure

    required to force filtrate into the formation

    without fracturing it is called the pump-in

    pressure.

    Figure 8.1 Squeezing to repair casing.

    Squeeze CementingTerminology

    In order to understand the different methods

    used in squeeze cementing, it is necessary to

    first be familiar with the following terms:

    The volume per minute at which the fluid will be

    pumped during the squeeze job is called theinjection rate. Both the pressure and rate should

    be established by performing an injection test in

    which well fluid is pumped into the formation to

    determine at what rate and pressure the fluid will

    be absorbed into the formation.

    Cement dehydration

    Pump-in pressure and injection rate

    Low- and high-pressure squeeze

    Block squeezing

    Cement slurry is composed of cement, additives

    and water. When slurry reaches a permeableformation, only the water (filtrate) will pass into

    the cracks of the formation (Figure 8.2). Cement

    dehydration is the process by which the cement

    forms a cake and hardens on the face of the

    formation.

    During a low-pressure squeezejob, enough

    pressure is applied to form a filter cake of

    dehydrated cement on the formation. In other

    words, the pump-in pressure or the pressure

    necessary to place cement against the formation

    will not cause the formation to fracture.

    However, if the formation will not absorb filtrate

    at the pump-in pressure, (because of blocked

    perforations or low formation permeability),

    more pressure may be applied. This will result in

    a fractured formation - whole slurry will fill the

    fractures. This is considered a high-pressure

    squeezejob.

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    Block squeezingrequires that perforations be

    made at the interval to be squeezed. Then,

    cement is forced into this interval (Figure 8.3).

    Block squeezing is generally used to isolate the

    producing zone before completing a well.

    Figure 8.3 Block Squeeze

    Hesitation Squeeze

    At some point during a squeeze job, you will

    have attained the pressure planned for the job.

    That pressure is then held. If it drops off (that is,

    bleed off is occurring), you know that your

    cement is continuing to dehydrate.

    In this case, a hesitation squeeze may be

    conducted. Time is allowed for the cement to

    begin to set. The pressure is applied again. If

    bleed off continues, more time is allowed. This

    is repeated as many times as is necessary; the

    only limitation is the thickening time of the

    cement. If too long a period is allowed, the

    workstring may be cemented up.

    Planning Squeeze Cementing

    Jobs

    Before any type of squeeze job is undertaken,

    information must be obtained and choices must

    be made, including

    the types of well fluids to be used, whichwill affect the pressure to reverse out, and

    the necessity of using a spacer (in case of

    fluid incompatibility)

    the bottomhole static temperature, whichaffects the setting time of the cement

    the difference between the depths of the

    perforations and the packer (if used), whichshould from 100 to 150 ft to allow enough

    volume to continue the squeeze after the

    cement has cleared the workstring

    the maximum pressure to be used, whichcannot exceed the pressure limitations of the

    workstring, casing, BOPs, and other

    equipment to be used

    the type of cement to be used, in that fluid-loss additives are used to ensure that a small

    amount of cement filter cake will form

    against the formation, while the slurry in thecasing remains fluid enough to reverse out

    the amount of cement to be used, whichdepends on the volume of the workstring

    (volume of cement should not exceed the

    capacity of the tubular goods) and the length

    of the interval to be squeezed (a rule of

    thumb is to use 2 sk/ft).

    testing all wellhead equipment and annulusto the pressure required to reverse out the

    maximum height of cementing the

    workstring.

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    Unit A Quiz

    Fill in the blanks with one or more words to check your progress in Unit A.

    1. Common reasons for performing a squeeze job are to ___________ a defective primary cementingjob or to __________ holes in casing caused by corrosion. In addition, the ______________ ratio is

    improved.

    2. When the filtrate enters the formation, cement ____________ to form a cake on the formation.

    3. The pressure required to force filtrate into the formation without ___________ it is called the___________ pressure. This pressure is established by pumping _________________ into the

    formation to be squeezed.

    4. If the formation fractures during a squeeze job, then a _________ pressure squeeze job is beingperformed.

    5. If the pressure drops off during a squeeze job, this is called ______________. To correct thiscondition, a _______________ squeeze may be performed.

    6. The ____________ pressure to be used during a squeeze job cannot exceed the limitations of theequipment being used.

    7. Cement used for squeeze job usually contains ______________ additives.

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    Unit B: Squeeze Cementing Calculations

    Before beginning a squeeze cementing job,

    several calculations must be performed. The

    types of calculations to make depend on the

    nature of the job. Following are the basic

    squeeze problem calculations (Fig. 8.3,4):

    1 Volume of cement (bbl).

    2 Pressure to reverse one barrel of slurry from

    workstring.

    3 Minimum water requirements.

    4 Displacement volume to spot cement one

    barrel above packer.5 Pressure to reverse cement when spotted.

    6 Pressure to reverse cement from workstring

    when cement reaches top perforation.

    7 Pressure to reverse cement from workstring

    when cement reaches bottom perforation.

    8 Pressure to reverse out at the completion of

    the job.

    9 Amount of cement pumped though the

    perforations.

    Following are the well parameters needed for the

    calculations (Fig. 8.3):

    ADrillpipe/tubing size

    BPacker depth

    CTop of perforations

    DBottom of perforations

    ECasing size

    A

    B

    C

    D

    E

    2

    4

    5

    WellFluid

    WellFluid

    Cement

    Figure 8.3 Well schematic showing squeeze calculations and parameters.

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    WellFluid

    WellFluid

    6

    WellFluid

    7 8

    9Cement

    Figure 8.4 - Well schematic showing squeeze calculations and parameters.

    The remainder of this section presents two

    sample squeeze problems and shows, step by

    step, how to calculate all the needed data. Youwill need a copy of theHalliburton Cementing

    Tables (theRed Book) to use during the

    samples.

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    Squeeze Problem One

    Well Parameters

    Drillpipe/tubing size 2 7/8 in., 6.5 lb/ftEUE

    Packer Depth 5000 ft

    Top of perforations 5094 ft

    Bottom of perforations 5136 ft

    Casing size 7 in., 20 lb/ft

    Cement type Class G

    Cement volume 75 sk

    Displacement/well fluid Fresh water (8.33

    lb/gal)

    A

    B

    C

    D

    E

    2 7/8 in., 6.5 lb/ft

    EUE Tubing

    Packer at 5000 ft

    Perf top at 5094 ft

    Perf bottom at

    5094 ft

    7 in., 20 lb/ftCasing

    1 Volume of Cement (bbl)

    To convert the given volume of cement from

    sacks to barrels, you must determine the yield of

    the slurry.

    1. Using the Technical Data section of theRed Book, determine the yield of a neat

    Class G slurry, given its weight of 15.8

    lb/gal. The table shown in Fig. 8.6 (extractedfrom the Class G section of theRed Book)

    shows this to be 1.15 cu.ft/sk.Figure 8.5 Parameters for SampleProblem A. 2. Multiply the volume of cement in sacks by

    the slurry yield to determine the volume in

    cubic feet.

    75 sk 1.15 cu.ft/sk = 86.25 cu.ft

    Now, convert cubic feet to barrels using the

    conversion constant found in the Technical

    Data section of theRed Book:

    86.25 cu.ft 0.1781 bbl/cu.ft = 15.36 bbl

    Figure 8.6 Class G data from Red Book.

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    2 Pressure to Reverse One Barrel of

    Slurry from Workstring

    2

    WellFluid

    Figure 8.7 Determining pressure to

    reverse on barrel of slurry from drillpipe.

    The following is a quick way to calculate the

    pressure required to reverse out the slurry from

    the workstring. These calculations will be based

    on a column equal in height to one barrel of

    fluid in the workstring. (Your answer will be in

    psi/bbl.)

    1. Referring to the Calculations andFormulae section of theRed Book(shown

    in Fig. 8.8), look up the psi/ft (hydrostatic

    pressure gradient) of the 15.8 lb/gal cementand the 8.33 lb/gal water. Then find thedifference between these two values: 0.8208

    psi/ft and 0.4330 psi/ft:

    0.8208 psi/ft 0.4330 psi/ft = 0.3878 psi/ft

    2. Then, using the Capacity section (Table211) for 2 7/8 in., 6.5 lb/ft EUE tubing, find

    the number of feet that one barrel will fill

    inside the tubing, which is 172.76 ft/bbl.

    3. Multiply the differential pressure found inStep 1 by the value found in Step 2 to obtain

    the pressure required to reverse out one

    barrel of slurry from the workstring:0.3878 psi/ft 172.76 ft/bbl = 67.00 psi/bbl

    Later on, you will be calculating different values

    of cement left in the tubing, according to where

    you are in your job. You will then use the value

    determined in the step above to calculate the

    total pressure required to reverse out the cement.

    Figure 8.8 Hydrostatic pressure data fromRed Book.

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    First, determine the capacity of the tubing. It

    extends from the surface to the packer, a

    total of 5000 ft. Look up the capacity factor

    for the 2 7/8 in., 6.5 lb/ft EUE tubing in the

    Capacity section (Fig 8.9). This factor is

    0.00579 bbl/ft. Multiply the length of the

    tubing by its capacity factor to obtain thecapacity of the tubing:

    3 Minimum Water Requirements

    The minimum fluid (water) requirements for a

    squeeze job include the volumes needed for the

    following:

    Cement mixing water (always fresh waterunless the slurry is otherwise designed)

    Displacement fluid (the capacities of thetubing and the casing)

    5000 ft 0.00579 bbl/ft = 28.95 bbl

    3. Then figure the capacity of the 7 in., 20 lb/ftcasing (Table 214) from the packer to the

    lowest perforation (5136 ft 5000 ft = 136

    ft).

    Reversing fluid

    Therefore, each of these volumes needs to be

    calculated and then added together.136 ft 0.0404 bbl/ft = 5.49 bbl

    Note: This volume does not include both prime-

    up and wash-up volumes, which would also

    need to be accounted for.

    4. You may have to reverse out the excesscement remaining in the tubing (after

    unsetting the packer). This reversecirculation occurs around the setting depth

    of the packer (5000 ft). So the volume in the

    tubing to reverse out is the same as the

    displacement volume you have already

    calculated for the tubing (Step 2), which is

    28.95 bbl.

    1. With the help of the Technical Datasection of theRed Book, you can calculate

    how much mixing water you will need (see

    Fig. 8.6). Because you are using Class G

    cement with a weight of 15.8 lb/gal, the

    water requirement is 5.0 gal/sk. Multiplying

    the amount of cement needed, in sacks, by

    the water requirement gives you your total

    mixing water:

    Keep in mind that you should use the type

    and weight of fluid in the annulus for

    reversing fluid.5.0 gal/sk 75 sk = 375 gal

    5. Now, the minimum amount of fluid required

    for this job can be calculated by adding thecement mixing water (Step 1), the two

    displacement fluid volumes (tubing and

    casing- Steps 2 and 3), and the reversing

    volume (Step 4):

    To convert to barrels:

    375 gal 42 gal/bbl = 8.93 bbl

    2. As for the fluid needed for displacement,you will need to calculate the capacities of

    the appropriate parts of both the tubing and

    casing. Since there is no way of knowing

    when a well will squeeze (pressure will not

    bleed off), you must have enough fluid to

    displace all of the slurry to the lowest

    perforation.

    8.93 bbl + 28.95 bbl + 5.49 bbl + 28.95 bbl

    = 72.32 bbl

    NOTE: As a good practice, we recommend that

    you have double the volumes needed to reverse.

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    Figure 8.9 Tubing capacity data from Red Book.

    Figure 8.10 Casing capacity data from Red Book.

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    5 Pressure to Reverse when Cement

    Spotted

    4 Displacement Volume to Spot

    Cement One Barrel Above Packer

    After the cement is spotted one barrel above the

    packer, the packer will be set to avoid

    circulating any cement behind the packer. Whenthe packer is set and you attempt to begin

    pumping fluid into the perforations, you may

    experience problems establishing an injection

    rate, in which case you would unset the packer

    and reverse all the cement out of the tubing.

    Therefore, you need to calculate how much

    pressure is required to do this.

    4

    5

    WellFluid

    Cement

    The pressure needed to reverse out this cement

    in the tubing can be calculated by multiplyingthe barrels of cement in the tubing, which in this

    case is the total cement volume, by the

    differential pressure per barrel of fluid (ascalculated in Calculation 2 , 67.00 psi/bbl):

    15.36 bbl 67.00 psi/bbl = 1029 psi

    Figure 8.10 Displacement Volume.

    To avoid damaging the formation that can be

    caused by pumping all the well fluid ahead of

    the cement into the perforations, the packer is

    left unset while the cement is spotted one barrel

    above it. This allows well fluid to circulate out

    of the well.

    To determine the volume of displacement topump behind the slurry to spot it one barrel from

    the packer, you subtract the total cement volume

    plus one barrel from the tubing capacity

    (determined during Calculation 3 ):

    Tubing Capacity 28.95 bbl

    Cement Volume - 15.36 bbl

    Volume Above Packer - 1.00 bbl

    Displacement Volume 12.59 bbl

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    Use yourRed Bookto find the capacity

    factor (bbl/ft) of the 7 in., 20 lb/ft casing,

    then multiply this value by the length of

    casing between the packer and the top

    perforation (5094 ft 5000 ft = 94 ft).

    6 Pressure to Reverse Cement from

    Workstring when Cement Reachesthe Top Perforation

    6

    WellFluid

    Cement

    94 ft 0.0404 bbl/ft = 3.80 bbl2. Now, subtract this volume from the total

    volume of cement to determine how much

    slurry remains in the tubing:

    15.36 bbl 3.80 bbl = 11.56 bbl

    3. The final step in this calculation is tomultiply the volume of cement remaining in

    the tubing by the differential pressure per

    barrel of fluid (as calculated in Calculation

    2 , 67.00 psi/bbl):

    11.56 bbl 67.00 psi/bbl = 775 psi

    Figure 8.11 Pressure to reverse whencement reaches the top perforation.

    As with the previous question, problems with

    injection rates may occur when cement reaches

    the top perforation. In this case, we can only

    reverse out the cement that is left inside the

    tubing, and not the cement that has exited below

    the packer and is now inside the casing.

    The first calculation we need to make, therefore,

    is the volume of cement remaining in the tubing.

    1. To do this, you calculate the volume ofcement in the casing and subtract that

    volume from the total volume of cement.

    Determining the volume of cement in the

    casing requires you to calculate the capacity

    of the casing from the packer depth (5000 ft)

    to the depth of the top perforation (5049 ft).

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    7 Pressure to Reverse Cement from

    Workstring when Cement ReachesBottom Perforation

    WellFluid

    7

    Figure 8.12 Pressure to reverse whencement reaches bottom perforation.

    Related to the calculation just completed, this

    calculation will be based on the fact that cement

    has made it to the bottom perforation, but no

    cement has entered the perforations. Therefore,

    we need to once again calculate the volume of

    cement that remains in the tubing.

    1. First, find the volume of cement that is inthe casing. This calculation has already been

    performed in Calculation 3 (5.49 bbl).

    2. Now subtract this volume from the totalvolume of cement:

    15.36 bbl 5.49 bbl = 9.87 bbl

    3. The pressure needed to reverse out thiscement in the tubing can now be calculated

    by multiplying the barrels in the tubing

    (Step 2) by the differential pressure per

    barrel of fluid (as calculated previously in

    Step 3 of the calculation for pressure to

    reverse out one barrel, 67.00 psi/bbl):

    9.87 bbl 67.00 psi/bbl = 661 psi

    Note: The effects of friction have beendisregarded in all these calculations.

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    9 Amount of Cement Pumped

    Through the Perforations

    8 Pressure to Reverse Out at the

    Completion of the Job

    Using information obtained from previous

    calculations, you can calculate the amount of

    cement pumped through the perforation duringthis squeeze job.

    WellFluid

    8

    9

    1. The total volume of slurry (15.36 bbl) minusthe volume of slurry in the casing (5.49 bbl)

    minus the volume of slurry now in thetubing is the volume of cement in the

    formation:

    15.36 bbl 5.49 bbl 4.95 bbl = 4.92 bbl

    2. Divide this by the yield of the cement, 1.15cu.ft/sk, to obtain the amount of cement in

    the formation:

    27.62 ft3 1.15 ft3/sk = 24 sk

    Results of Calculations

    The following table presents the results of the

    nine calculations for Squeeze Problem One:

    Squeeze Cementing Calculation Results

    Description Result

    1 Volume of cement (bbl). 15.36 bbl

    2 Pressure to reverse one

    barrel of slurry from workstring.

    67.00 psi/bbl

    3 Minimum water

    requirements.

    72.32 bbl

    4 Displacement volume to

    spot cement one barrel abovepacker.

    12.59 bbl

    5 Pressure to reverse cement

    when spotted.

    1029 psi

    6 Pressure to reverse cement

    from workstring when cementreaches top perforation.

    775 psi

    7 Pressure to reverse cementfrom workstring when cementreaches bottom perforation.

    661 psi

    8 Pressure to reverse out at

    the completion of the job.

    332 psi

    9 Amount of cement pumped

    though the perforations.24 sk

    Figure 8.13 Pressure to reverse out at the

    completion of the job.

    For the following calculations, you have to

    assume that some arbitrary volume of

    displacement fluid was pumped behind the

    cement at the time squeeze pressure is reached.

    The volume chosen here is 24 bbl.

    1. Find out how much cement is in the tubingnow, given that 24 bbl of displacement fluid

    were pumped behind it:

    28.95 bbl 24 bbl = 4.95 bbl2. Now multiply the amount of cement in the

    tubing by the pressure required to reverse

    one barrel out of the tubing (67.00 psi/bbl)

    4.95 bbl 67.00 psi/bbl = 332 psi

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    Squeeze Cementing

    2

    WellFluid

    1 Volume of Cement

    MaterialName

    Material(lb)

    Factor(gal/lb)

    AbsoluteVolume

    (gal)

    MixingWater

    Required(gal)

    Class HCement 94 0.0382 = 3.5908 4.3

    0.4% Halad-413

    0.376 0.0811 = 0.0305 0 +

    = +

    Water 35.819 = 8.33 4.3 gal +

    Totals 130.20 7.92 4.3 gal

    Total mixing water must be entered under absolute gallonsbefore totaling.Find the weight of the mixed cement by using this formula:Total Pounds/Total Absolute gallons = pounds/gallonsFind the cement yield in cubic feet per sack by using thisformula:Total Absolute gallons / 7.4805 gal/cu.ft. (constant) = cu.ft./ sackThe mixing water per sack is the sum of the gallons in the farright column

    Cement Density(lb/gal)

    130.20 / 7.92 = 16.4 lb/gal

    Cement Yield(ft

    3/sk)

    7.92 / 4.4805 = 1.06 ft3/sk

    Mixing Waterrequired

    4.3 Gal/sk

    Figure 8.15 Determining pressure toreverse one barrel of slurry from workstring.

    Based on the worksheet,

    150 sk 1.06 cu ft/sk = 159 cu ft

    159 cu. ft 0.1781 bbl/cu. ft = 28.32 bbl

    3 Minimum Water Requirements2 Pressure to Reverse One Barrel ofSlurry From Workstring

    1. Cement Mix Water:

    Hydrostatic pressure gradients (from

    Calculations and Formulae section ofRed

    Book)

    150 sk 4.3 gal/sk = 645 gal

    645 gal 42 gal/bbl = 15.36 bbl

    2. Displacement Fluid:16.4 lb/gal cement 0.8519 psi/ft

    8.33 lb/gal water 0.4330 psi/ftTubing: 6200 ft 0.00579 bbl/ft = 35.90 bbl

    Casing: 6250 ft 6200 ft = 50 ft

    50 ft 0.0404 bbl/ft = 2.20 bblDifferential Hydrostatic Pressure Gradient =

    3. Reversing Fluid: 35.90 bbl0.8519 psi/ft 0.4330 psi/ft = 0.4189 psi/ft

    Feet/Barrel Factor For Workstring = 172.76 lb/ft0.4189 psi/ft 172.76 ft/bbl = 72.37 psi/bbl Minimum water required:

    15.36 bbl + 35.90 bbl + 2.02 bbl + 35.90 bbl

    = 89.18 bbl

    NOTE: Always plan to reverse with 2 times the

    tubing capacity. Therefore in this problem plan

    for an additional 35.9 bbls.

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    4 Displacement Volume to Spot

    Cement One Barrel Above Packer

    6 Pressure to Reverse Cement from

    Workstring when Cement ReachesTop Perforation

    Tubing Capacity 35.90 bbl

    Cement Volume - 28.32 bbl

    Volume Above Packer - 1.00 bbl

    Displacement Volume 6.58 bbl

    Capacity of casing from packer (6200 ft) top

    perforation (6240 ft):6240 ft 6200 ft = 40 ft

    40 ft 0.0404 bbl/ft = 1.62 bbl5 Pressure to Reverse Cement

    When Spotted 28.32 bbl 1.62 bbl = 26.70 bbl remaining intubing

    26.70 bbl 72.37 psi/bbl = 1932 psi28.32 bbl 72.37 psi/bbl = 2050 psi

    4

    5

    WellFluid

    Cement

    6

    WellFluid

    Cement

    Figure 8.17 Pressure to reverse cement.Figure 8.16 Calculations 4 and 5.

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    7 Pressure to Reverse Cement from

    Workstring when Cement ReachesBottom Perforation

    Capacity of casing from packer to bottom

    perforation = 2.02 bbl (from Calculation 3 )28.32 bbl 2.02 bbl = 26.30 bbl

    26.30 bbl 72.32 psi/bbl = 1903 psi

    WellFluid

    7

    Figure 8.18 Pressure to reverse cement.

    8 Maximum Pump Pressure when

    Cement Slurry Has Reached theBottom Perforation

    It is necessary to determine the maximum

    pressure that can be applied at the surface for

    this squeeze job. The pressure applied at the

    surface may be transmitted through the channel

    to the outside of the casing above the packer. If

    the pressure applied is high enough, it may

    collapse the casing.

    1. This calculation is done by first subtractingthe pressure to reverse out cement to lowest

    perforation and no cement in the formation

    (1903 psi) from the collapse resistance of

    the casing being used. This value can be

    found in the Dimensions and Strengths

    section of theRed Book. Refer to the correct

    table for the 7 in, 20 lb/ft, J-55 casing being

    used (Fig 8.20). The collapse resistance is

    2270 psi.

    2270 psi 1903 psi = 367 psi

    2. Since there is a differential pressure fromthe packer to the perforation (no cement is in

    the channel), you must also subtract this. To

    calculate the differential, multiply the

    distance from the packer to the lowest

    perforation (6250 ft 6200 ft = 50 ft) by the

    difference in the psi/ft for the cement and

    well fluid (0.8519 psi/ft - 0.4330 psi/ft =

    0.4189 psi/ft):

    50 ft 0.4189 psi/ft = 21 psi

    3. Now, subtract the differential pressure fromStep 1 to obtain the maximum pump

    pressure:

    368 psi 21 psi = 347 psi

    Remember, this is the maximum pressure that

    can be applied at the surface if the cement has

    reached the perforations.

    WellFluid

    8

    Figure 8.19 Maximum pump pressure.

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    Figure 8.20 Casing data from Red Book.

    Subtract the pressure to reverse the remaining

    cement slurry from the tubing from the collapse

    resistance of the casing to find the maximum

    pump pressure at surface:

    9 Calculation of Pressure to

    Reverse Out at the Completion of theJob

    2270 psi 789 psi = 14812 psiFinal Displacement Volume = 25 bbl

    Cement Volume Remaining in Tubing:

    WellFluid

    9

    10

    11

    35.90 bbl 25 bbl = 10.9 bbl

    Reverse Pressure:

    10.9 bbl 72.37 psi/bbl = 789 psi

    10 Amount of Cement PumpedThrough the Perforations

    Volume of Cement in Perforations:

    28.32 bbl 10.9 bbl 2.02 bbl = 15.4 bbl

    15.4 bbl 5.6146 cu ft/bbl= 86.46 cu ft

    86.46 cu ft 1.06 cu ft/sk = 82 sk

    11 Maximum Pump Pressure if the

    Channel is Full of Cement

    Assuming that 25 bbl of displacement fluid have

    been pumped behind the volume of slurry, and

    that the channel is full of cement, you know

    there is no differential pressure from the packerto the perforations in this case. What is the

    maximum pump pressure before the casing

    collapses?

    Figure 8.21 Calculations for 9, 10, and 11.

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    Results of Calculations

    The following table presents the results of the

    nine calculations for Squeeze Problem Two:

    Squeeze Cementing Calculation Results

    Description Result

    1 Volume of cement (bbl). 28.32 bbl

    2 Pressure to reverse one

    barrel of slurry from workstring.72.37 psi/bbl

    3 Minimum water

    requirements.89.18 bbl

    4 Displacement volume to

    spot cement one barrel abovepacker.

    6.58 bbl

    5 Pressure to reverse cement

    when spotted.2050 psi

    6 Pressure to reverse cementfrom workstring when cementreaches top perforation.

    1932 psi

    7 Pressure to reverse cement

    from workstring when cementreaches bottom perforation.

    1903 psi

    8 Maximum pump pressure

    when cement slurry hasreached the bottom perforation

    347 psi

    9 Pressure to reverse out atthe completion of the job

    789 psi

    10 Amount of cement

    pumped through theperforations

    82 sk

    11 Maximum pump pressure

    if the channel is full of cement1481 psi

    Unit B Quiz

    Fill in the blanks with one or more words to check your progress in Unit B.

    1. The well parameters needed for squeeze calculations include:

    ____________________________________

    ____________________________________

    ____________________________________

    ____________________________________

    ____________________________________

    2. To convert a given volume of cement from sacks to barrels, you must determine the

    ____________________________________________.

    Now check your answers in the Answer Key at the back of this section.

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    Answers to Unit Quizzes

    Items from Unit A Quiz Refer toPage

    1. correct, fill, oil/water 8-3

    2. dehydrates 8-4

    3. fracturing, pump-in, fluid 8-4

    4. high 8-5

    5. bleed-off, hesitation 8-5

    6. maximum 8-5

    7. fluid-loss 8-5

    Items from Unit B Quiz Refer toPage

    1. Drillpipe size

    Packer depth

    Top of perforations

    Bottom of perforations

    Casing size

    8-7

    2. yield of the slurry 8-9