U.S. patent application number 11/305609 was filed with the patent office on 2006-05-25 for aqueous storable cement spacer system.
This patent application is currently assigned to BJ SERVICES COMPANY. Invention is credited to Charles Joseph JR. Fanguy, Timothy Ivan Mitchell, Jerry Patrick Sanchez.
Application Number | 20060111246 11/305609 |
Document ID | / |
Family ID | 32682488 |
Filed Date | 2006-05-25 |
United States Patent
Application |
20060111246 |
Kind Code |
A1 |
Fanguy; Charles Joseph JR. ;
et al. |
May 25, 2006 |
Aqueous storable cement spacer system
Abstract
A storable cement system comprises a suspending agent, a cement
spacer and water. The composition may further optional contain a
surfactant and/or an organic solvent and/or a weighting material.
The suspending agent is preferably a carrageenan or scleroglucan.
The cement system may be stored for an extended period of time
prior to being interposed between a cement slurry and a drilling
fluid. As such, the aqueous cement system may be made off-site and
used when desired for preventing contact between non-compatible
hydrocarbonaceous and aqueous fluids.
Inventors: |
Fanguy; Charles Joseph JR.;
(Houma, LA) ; Sanchez; Jerry Patrick; (Lafayette,
LA) ; Mitchell; Timothy Ivan; (New Orleans,
LA) |
Correspondence
Address: |
JONES & SMITH, LLP
THE RIVIANA BUILDING
2777 ALLEN PARKWAY, SUITE 800
HOUSTON
TX
77019-2141
US
|
Assignee: |
BJ SERVICES COMPANY
|
Family ID: |
32682488 |
Appl. No.: |
11/305609 |
Filed: |
December 16, 2005 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
|
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10448576 |
May 30, 2003 |
7007754 |
|
|
11305609 |
Dec 16, 2005 |
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Current U.S.
Class: |
507/110 |
Current CPC
Class: |
C04B 28/02 20130101;
C04B 28/02 20130101; C09K 8/424 20130101; C04B 14/06 20130101; C04B
14/308 20130101; C04B 24/38 20130101; C04B 14/28 20130101; C04B
2103/408 20130101; C04B 2103/0082 20130101; C04B 24/2652 20130101;
C04B 24/02 20130101; C04B 22/16 20130101; C04B 14/10 20130101; C04B
24/383 20130101; C04B 28/02 20130101 |
Class at
Publication: |
507/110 |
International
Class: |
C09K 8/00 20060101
C09K008/00 |
Claims
1. An aqueous storable cement spacer system comprising: a cement
spacer; a suspending agent selected from a carrageenan or
scleroglucan; and an aqueous fluid.
2. The aqueous storable cement spacer system of claim 1, wherein
the suspending agent is iota carrageenan.
3. The aqueous storable cement spacer system of claim 2, wherein
the iota carrageenan has a molecular weight of between about
150,000 and about 250,000.
4. The aqueous storable cement spacer system of claim 1, wherein
the cement spacer comprises at least one member selected from the
group consisting of, xanthan gum, attapulgite, bentonite, sodium
montmorillionite, hydroxyethyl cellulose, guar gum and derivatives
thereof.
5. The aqueous storable cement spacer system of claim 1, wherein
the cement spacer comprises a polysaccharide.
6. The aqueous storable cement spacer system of claim 1, wherein
the cement spacer comprises welan gum.
7. The aqueous storable cement spacer system of claim 10, wherein
the surfactant comprises an ethoxylated alcohol.
8. The aqueous storable cement spacer system of claim 1, further
comprising a weighting agent.
9. The aqueous storable cement spacer system of claim 8, wherein
the weighting agent is selected from the group consisting of
barite, calcium carbonate, hematite, sand, illmanite, trimanganese
tetraoxide, iron oxide, and fly ash.
10. The aqueous storable cement spacer system of claim 1, further
comprising a dispersant or surfactant.
11.-29. (canceled)
30. The aqueous storable cement spacer system of claim 10, wherein
the surfactant is anionic or non-ionic.
31. The aqueous storable cement spacer system of claim 1, wherein
the amount of suspending agent in the cement spacer system is
between from about 0.05 to about 1 weight percent of the fluid base
of the cement spacer system.
32. The aqueous storable cement spacer system of claim 31, wherein
the amount of suspending agent in the cement spacer system is
between from about 0.05 to about 0.5 weight percent of the fluid
base of the cement spacer system.
33. The aqueous storable cement spacer system of claim 32, wherein
the amount of suspending agent in the cement spacer system is
between from about 0.05 to about 1 weight percent of the fluid base
of the cement spacer system.
34. The aqueous storable cement spacer system of claim 33, wherein
the amount of suspending agent in the cement spacer system is about
0.3 weight percent of the fluid base of the cement spacer
system.
35. The aqueous storable cement spacer system of claim 1, wherein
the cement system is prepared by (i.) mixing the fresh water and
suspending agent for a time sufficient to hydrate the suspending
agent; (ii.) introducing the cement spacer to the mixture
containing the hydrated suspending agent; and (iii.) stirring for a
time sufficient to render a homogeneous cement system.
36. The aqueous storable cement spacer system of claim 1 which has
a viscosity of 20-200 cps at 25.degree. C.
37. The aqueous storable cement spacer system of claim 1, wherein
the iota carrageenan has a molecular weight of between about
150,000 and about 250,000.
38. An aqueous storable cement spacer system comprising: a cement
spacer; a hydrated suspending agent selected from a carrageenan or
scleroglucan; and an aqueous fluid base or mix water.
39. The aqueous storable cement spacer system of claim 1, wherein
the cement spacer is selected from the group consisting of
polybasic inorganic phosphate salts, mixed metal hydroxides, clays,
polyanionic cellulose derivatives, carboxyalkylcellulose
derivatives, nonylphenol ethoxylated with ethylene oxide,
polyacrylamide and derivatives thereof.
Description
FIELD OF THE INVENTION
[0001] The present invention relates to an aqueous cement spacer
system for use in the cementing of an area of a borehole
penetrating a subterranean formation and a method of making the
aqueous cement spacer system; the aqueous cement spacer system
capable of being stored for an extended period of time.
BACKGROUND OF THE INVENTION
[0002] The prior art is replete with many disclosures of cementing
in wells penetrating subterranean formations. In such operations,
drilling fluids (often referred to as "muds") are normally present
in oil and other similar wells at the time of cementing a casing
into a borehole with an aqueous cement slurry. Since the mud and
cement are not always compatible with each other, it is often
desirable to separate or prevent contact between them by use of a
cement spacer system. Without the use of such spacer systems, the
incompatibility of the aqueous cement slurry with the oil based mud
is often of such severity that a mixture of the two forms an
unpumpable mass. Such unpumpable masses may prevent displacement of
at least a portion of the drilling fluid with a cement spacer
system. Spacer systems also serve to water-wet the wellbore
surfaces to promote bonding of the cement sheath to the wellbore
and casing. Such cement spacer systems are often thought of as
flushing agents.
[0003] In a typical operation, the cement spacer system is prepared
at the site of entry into the well bore such that the density of
the system matches or exceeds the densities of the fluids to be
removed from the well and the like. Conventional mixing equipment
for such applications usually takes the form of a 50 to 100 barrel
"batch mixer". A typical batch mixer is a hydraulically powered,
self-contained unit which mixes the cement spacer formulation
immediately prior to the cementing operation. Such units are
equipped with large paddles to facilitate the mixing of the cement
spacer, centrifugal pumps for circulation of the spacer within the
batch mixer and pressurized bulk storage tanks for the transport of
the weighting agent for the cement spacer. Batch mixers may be
truck-mounted or skid mounted depending on wellsite location
requirements.
[0004] Once at the drilling site, the spacer system must be
prepared from its constituent materials (typically water, gelling
agent and weighting agent) and combined with any additional
materials (such as surfactants or mutual solvents). The cement
spacer system must then be tested for the appropriate density, with
the density adjusted to fall within the appropriate range for the
particular well bore. Independent of the particular chemistry of
the cement spacer system, the storage time of the finished spacer
prior to pumping into the wellbore is generally limited to no more
than 12 hours due to gravitational settling of the weighting
agent.
[0005] It would be desirable to develop a cement spacer system that
was storable and which remained as a pumpable fluid over extended
periods of time. Such storable compositions would offer several
advantages over the conventional systems of the prior art. Most
notably, they could be made in advance and stored until needed. In
addition, the storable compositions may be made at a different
location from the job site. Such storable compositions may then be
transported to the job site before the introduction of the
cementitious slurry into the well bore. Further, the composition
may be stored in inexpensive nonpressurized tanks and easily
transferred. Still further, the mixing equipment used on the job
site would only be required to homogenize the composition as
required en route to the downhole pumps. Such storable compositions
may further undergo quality control prior to introduction into the
well bore.
SUMMARY OF THE INVENTION
[0006] The aqueous cement spacer system of the invention may be
storable for extended periods off-site and is highly desirable for
preventing contact between non-compatible fluids contained in a
conduit, well bore or other container. The storable cement spacer
system comprises a cement spacer and a suspending agent, preferably
a carrageenan or a scleroglucan. The preferred carrageenan is an
iota carrageenan, such as those having a molecular weight of
between about 150,000 and about 250,000. The storable cement spacer
system of the invention does not require a set retarder. Preferred
as the cement spacer are those containing polysaccharides, such as
welan gum, xanthan gum, carboxyalkylcellulose derivatives or
polyanionic celluloses.
[0007] The storable cement spacer system of the invention is
preferably formulated at one location and, when desired to be used,
is transferred to a second location where it is used. The mixture
is then pumped into the borehole.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0008] The storable cement spacer spacer systems of the invention
contain a fluid base or mix water, a suspending agent and a cement
spacer. The fluid base is typically water (fresh water or salt
water), natural or artificial brines and the like. In a preferred
embodiment, the aqueous fluid base is fresh water though salt water
may further be employed.
[0009] The storable cement spacer systems of the invention can be
made in advance, off-site from the well bore then transported to
the wellsite and stored for an indefinite period. The targeted
density of the storable cement spacer system is dependent upon well
conditions, most specifically, the density of the mud in the
wellbore at the time of cementation. Preferably, the density of the
cement spacer system matches or exceeds the density of the fluid to
be removed from the well. Storable cement spacers may also be
transported at higher than required densities for the sake of
saving space, then diluted to a lower density prior to pumping into
the wellbore. Preferably, the storable system exhibits a density
ranging from about 10 to about 20 lb/gal, more preferably in the
range of about 14 to about 20 lb/gal and most preferably about 16
to 20 lb/gal.
[0010] The storable cement spacer system of the invention is
prepared in a number of steps. Typically, the storable cement
spacer system is manufactured with the requisite materials taking
into account the specifications of the wellbore to which the system
is to be placed.
[0011] In a first step, the desired amount of fresh water,
depending on the desired density of the storable cement spacer
system, is measured. A suspension agent is then introduced to the
measured water. A principal objective of the suspending agent is to
maintain the composition with minimal separation over time and to
impart the requisite viscosity to the system to allow the weighting
particles to remain suspended over a period of time. As such, the
suspension agent is selected based upon desired surface storage
capabilities. The suspension agent is hydrated in water for a time
sufficient to obtain the desired viscosity of the solution.
Typically, the mixture containing the hydrated suspension agent
exhibits a target viscosity in the range of from about 10 to about
20 cps at 25 C. or ambient temperature, as measured with a Fann 35
rheometer.
[0012] While conventional suspending agents, such as starch,
succinoglycan, polyethylene oxide, oil in water emulsions created
with paraffin oil and stabilized with ethoxylated surfactants, etc.
may be employed as the suspending agent, the preferred suspending
agent is either carrageenan or scleroglucan. Carrageenan, a high
molecular weight polysaccharide derived from seaweed, and
scleroglucan, a water soluble natural polymer produced by
fermentation of the filamentous fungi Sclerotium rofsii, provide
better stability and minimize the risk of settling of the cement
spacer system.
[0013] Although any carrageenan suitable for forming gels and/or
otherwise acting as a suspension agent may be employed (including
those carrageenans having a molecular weight greater than about
500,000 and less than about 75,000), typically a carrageenan has a
molecular weight of between about 75,000 and about 500,000. (Unless
otherwise noted, all molecular weights expressed herein refer to
weight average molecular weight.) More typically in the practice of
the disclosed method, a carrageenan has a molecular weight of
between about 150,000 and about 250,000, and even more typically a
carrageenan has a molecular weight of about 200,000. Specific
carrageenan types include kappa, iota and lambda carrageenans.
Typically, iota carrageenan is employed. Mixtures of carrageenan
types are also possible. A specific example of a suitable iota
carrageenan for use in the disclosed method is "LSS-1" from BJ
Services Company. Other suitable carrageenans include carrageenan
gums and are disclosed in U.S. Pat. No. 6,173,778, herein
incorporated by reference.
[0014] Some iota carrageenan materials may require heating to above
the solubility temperature to achieve hydration, for example to
about 80.degree. C. In other cases, an iota carrageenan material
may be hydrated without prior heating especially in the presence of
sodium ions. Examples of such iota carrageenan materials include
"cold water soluble" iota carrageenans, which are soluble at
temperatures of about 20.degree. C. without prior heating as long
as sodium is present, such as in the form of sodium hydroxide or
sodium carbonate.
[0015] Further preferred as the suspending agent for use in the
invention are scleroglucans including scleroglucan gums. Like
carrogeenans, scleroglucans are capable of imparting to the
composition a level of viscosity, which allows the cement spacer to
be suspended. Suitable scleroglucan gums include those commercially
available as Biovis, a product of SKW.
[0016] Typically, the amount of suspending agent in the cement
spacer system of the invention is between from about 0.05% to about
1% weight percent of the fluid base comprising the cement spacer
system, more typically between about 0.2 and about 0.5%, and most
typically about 0.3% by weight of the fluid base.
[0017] The cement spacer is introduced to the aqueous mixture
containing the suspension agent. The cement spacer may be any
conventional cement spacer known in the art. It is generally
aqueous-based. Suitable cement spacers are those based on
polybasic, inorganic phosphate salts, as disclosed in U.S. Pat. No.
4,548,270, herein incorporated by reference; polysaccharides, such
as welan gum and xanthan gum, as disclosed in U.S. Pat. No.
4,717,488, herein incorporated by reference, a polyanionic
cellulose and carboxyalkylcellulose derivatives such as
hydroxyethyl cellulose; as well as admixtures of nonylphenols
ethoxylated with ethylene oxide, as disclosed in U.S. Pat. No.
4,588,032, herein incorporated by reference, polyacrylamide or a
guar gum, mixed metal hydroxides, clays like attapulgite and
bentonite or sodium montmorillionite and derivatives thereof.
[0018] Once the suspending agent has been added to the base fluid
base, the preparation of the cement spacer system proceeds in
accordance with the defined instructions for that particular spacer
system. The respective components which may be in dry, water-based
liquid, non-aqueous liquid suspension or paste form, are then added
to the base fluid base containing the suspending agent.
[0019] In a preferred embodiment, the cement spacer contains welan
gum, which may be applied as a dry powder or in the form of a
non-aqueous suspension having a high solids content non-aqueous
suspension (paste). Preferably, the cement spacer is a cement
spacer known in the art, such as UltraFlush 2.TM., a product of BJ
Services Company. UlraFlush 2.TM. is formulated by adding a
concentrate containing a biopolymer and a powdered surfactant to
the base fluid bases and allowing the concentrate to disperse into
the aqueous phase. Barite is then added as weighing agent, to
adjust the density according to the requirements of the well. Such
cement spacer concentrates may contain a dispersant, such as
lignosulfonate, or a surfactant, typically a non-ionic or anionic
surfactant. Suitable non-ionic or anionic surfactants include those
discussed in the paragraphs below. Examples of a dry surfactant,
such as an ethoxylated alcohol, may be added to the cement spacer
concentrate.
[0020] Generally, the cement spacer is stirred with the mixture
containing the suspension agent for a period of time in order to
obtain the desired viscosity. Generally, the desired viscosity of
the product, after introduction of the cement spacer to the
mixture, is from about 20 to about 200 cps at 25.degree. C.
[0021] It is preferable, but not essential, that the cement spacer
system of the invention introduced into the well bore have a
density at least equal to or greater than the density of the
drilling mud and less than or equal to the density of the
cementitious slurry to be introduced into the well bore. Increase
in densities can be attained by the addition of one or more
weighting agents. The weighting agent may be part of the cement
spacer introduced to the aqueous mixture containing the suspension
agent or may be applied subsequent to the introduction of the
cement spacer.
[0022] Weighting agents that can be utilized are preferably
insoluble in water and liquid hydrocarbons and include sand,
barite, hematite, fly ash, calcium carbonate, silica sand,
illmanite, manganese oxide, trimanganese tetraoxide, iron oxide,
and fly ash and the like. Barite is especially preferred. The
weighting agent is employed in an amount sufficient to provide the
desired density of the storable cement spacer system. Typically,
the amount of weighting agent in a spacer cement system is from
about 90 to about 650 lbm per barrel of finished cement spacer
system.
[0023] It may further be desired to add a surfactant and/or solvent
to the resulting mixture, subsequent to the addition of the spacer
cement. The amount of surfactant or solvent used in the cement
spacer system is generally dependent upon the desired compatibility
of the desired system, as defined by API RP-10B or ISO 10426-2.
Typically therefore, the rheological properties of the system are
first determined. The amount of surfactants, if any, would then be
determined to ensure the requisite compatibility. Generally, the
concentration of surfactant and/or solvent in the cement spacer
system of the invention will generally be from about 0.1 to about
5.0% by weight, and more preferably from about 0.2 to about 3.0% by
weight, of the storable cement spacer system. The surfactant may be
part of the cement spacer initially added to the mixture containing
hydrated suspension agent.
[0024] The surfactant is preferably either anionic or non-ionic and
is chosen based on the carrier of the cement spacer as well as the
wellbore fluid. Other surfactants may be chosen in order to make
the cement spacer system more compatible with the wellbore fluids.
Typically, the surfactants used in this step of the process are
water compatible surfactants and are often used to control the
fluidity of the cement spacer system. Further, the surfactants or
mixtures of surfactants should be soluble in the cement spacer
system and not precipitate or otherwise degrade under normal
storage conditions.
[0025] Inclusive of preferred surfactants are alkanol amides,
ethoxylated alkylarylsulfonates, amine oxides, ethoxylated amines,
ethoxylated amides, sulfates and sulfonates of ethoxylated
alcohols, ethoxylated alkyl phenols, sulfates or sulfonates of
ethoxylated alkyl phenols (and their salts), ethoxylated quaternary
ammonium chlorides, fluorocarbon-based surfactants, sulfates or
sulfonates of alkanols, coco fatty betaines, condensation products
of ethylene oxide and glycols, such as propylene glycol, sulfonated
alkyl aldehyde condensates, such as sulfonated naphthalene
formaldehyde condensates, sulfonated ketone/acetone formaldehyde
condensates, melamine formaldehyde derivatives such as melamine
formaldehyde-sodium bisulfite, sulfonated styrene maleic anhydride
copolymers, polyacrylamides, such as polyacrylamide
dimethylaminoethyl methacrylate copolymer, sulfonated ketone.
Especially preferred are nonylphenol ethoxylates, cocoamido
betaine, blends of N-alkyl coco trimethyl ammonium chloride and
bis(2-hydroxyethyl)cocoamide oxide, blends of ethoxylated
trimethylnonanol and perfluoro quaternary ammonium oxide,
C.sub.12-C.sub.15 linear alcohol ethoxylated sulfate,
C.sub.9-C.sub.11 linear alcohol ethoxylated sulfates, sodium lauryl
sulfate and ethoxy alcohol sulfates. Preferred solvents include
limonene, pinene and carotene, ketones such as acetone and
ethylmethyl ketones and ethers such as ethylene glycol monobutyl
ether. Especially preferred as surfactants and solvents are SS-2
and US-2, both proprietary products of BJ Services Company.
[0026] It may further be desirable to add a clay stabilizer to the
storable cement spacer system. Suitable stabilizers include salts
such as KCl and NH.sub.4Cl, or modified salts such as those of
quaternary ammonium chloride. Especially preferred is CLAYTREAT
3C.TM., a product of BJ Services Company.
[0027] Under normal conditions, the storable cement spacer systems
of the invention have considerable longevity. Typically, they
remain stable as a liquid preferably for about 7 to about 25 days
and more preferably about two to three months without setting,
depending on the type of cement spacer and concentration of cement
spacer used. In some cases, storage times in excess of six months
will be achieved.
[0028] Typically, the cement spacer systems of the invention are
formulated at one location, such as on land, with the density of
the desired spacer system measured and adjusted if desired. Next,
the formulated cement spacer system is transferred to a second
location, such as an offshore rig. At the second location the
transferred system may be used immediately or stored until needed.
At the time of pumping into the wellbore, the density can be
adjusted to the desired density.
[0029] The ability to store the cement spacer system of the
invention eliminates onsite mixing problems such as mechanical or
hydraulic system failure of the "batch mixer", reduces the
necessity for expensive "bath mixing" equipment to be placed at the
wellsite, reduces the manpower requirements for the cementing
operation, lowers the environmental risk by minimizing the
quantities of bulk chemicals stored at the wellsite and lowers the
discharge of dust associated with bulk pneumatic transfer of
weighting agent.
[0030] Simpler equipment can be used with the storable cement
spacer systems of the invention. The systems can be kept in
nonpressurized tanks and loaded and unloaded with conventional
fluid pumps. When in actual use, the mixing unit need do no more
than homogenize the fluid streams of the system en route to the
downhole pumps.
[0031] The ability to prepare and control the quality of a storable
cement spacer system at the base is obviously advantageous. The
spacer system is mixed and its initial density measured and
adjusted at the base rather than at the wellsite. The system need
only be homogenized before being introduced into the wellbore. The
stability of the system and long-term fluidity allow the system to
be prepared, transferred and stored a considerable time before
needed for wellsite operations. Thus, the system may be prepared at
a central facility and stored in liquid form at the facility. From
there it is loaded aboard trucks or workboats and transferred to
the remote wellsite. At the wellsite, it may be offloaded and
stored or used immediately for cementing operations.
[0032] Once introduced into the well bore, the storable cement
spacer systems of the invention exhibit normal performance. The
resultant cement spacer system can be kept with occasional
agitation for periods of time exceeding twelve weeks under normal
storage conditions.
[0033] At the appropriate time within the well cementing operation,
the cement spacer system of the invention is pumped down the
borehole and up through the annulus between the casing and the
formation face to remove at least a portion of the drilling mud
therefrom. It is not necessary to use an activator. The cement
spacer system may be displaced down the casing and up through the
annulus by the use of another liquid, but preferably, it is
immediately followed by the aqueous cement slurry to be employed to
cement the casing. The cement slurry then may be followed by an
additional volume of the cement spacer system.
[0034] Sufficient cement spacer system is employed to separate the
drilling mud from the cement slurry. As the cement spacer system is
circulated through the well bore, it will mix with oil-based mud.
Before the drilling mud is completely removed from the area to be
cemented, there may be mixing of the drilling mud, cement spacer
system and cement slurry. However, the composition of the present
invention will not harden, gelatinize or otherwise become immobile
because of a commingling of the three components.
[0035] The following examples will illustrate the practice of the
present invention in its preferred embodiments. Other embodiments
within the scope of the claims herein will be apparent to one
skilled in the art from consideration of the specification and
practice of the invention as disclosed herein. It is intended that
the specification, together with the example, be considered
exemplary only, with the scope and spirit of the invention being
indicated by the claims which follow.
EXAMPLES
Example 1
[0036] To about 375.14 grams of fresh water, was added 1.13 grams
of iota carrageenan. The mixture was mixed for 30 minutes until a
viscosity of 15 cps was reached, at 25.degree. C. To the resulting
mixture was added 2.29 grams of the cement spacer ULTRA FLUSH 2.TM.
concentrate, a proprietary product, containing welan gum, of BJ
Services Company. Mixing was continued until the concentrate was
dispersed into the aqueous phase. 629 grams of barite was then
added to the resulting mixture. Mixing was continued for 10
minutes. 42.84 mls of SS-2, an oxyalkylated alkyl ester surfactant,
a proprietary product of BJ Services Company, and 28.56 mls of
US-2, a proprietary product of BJ Services Company containing
d-limonene, were then added to the mixture. Mixing was continued
until homogeneity was obtained. Upon transportation to the drilling
site, the mixture is highly effective as an aqueous cement spacer
system.
Example 2
[0037] A cement spacer system was prepared by slowly adding, to
about 468 grams of fresh water, about 0.7 g of scleroglucan. The
mixture was stirred for about 30 minutes at room temperature. To
the resulting mixture was slowly added about 2.3 g of ULTRA FLUSH
2.TM. concentrate while stirring. The mixture was stirred for at
least 5 minutes to assure proper dispersion of the ULTRA FLUSH
2.TM. concentrate. About 535.5 g of barite was then slowly added to
the mixture. The resulting mixture was then stirred or about 5
minutes. It was not necessary to add either SS-2 or US-2.
Example 3
[0038] To about 217 g of fresh water was slowly added about 2.6 g
of iota-carrageenan. The mixture was hydrated by stirring for about
30 minutes. About 217 g additional fresh water was added to a
blender cup, along with about 3.6 ml of FP-6L, a proprietary
alcohol based defoaming agent of BJ Services Company. About 1.7 g
of NaOH was further added to the blender cup and the mixture was
mixed for about 2 minutes. About 12.9 g of bentonite was then added
to the blender cup and the mixture stirred at 4,000 rpm for about
10 minutes. The contents of the blender cup were then added to the
mixture of iota-carrageenan and fresh water. To the resulting
mixture was then added about 405 g of barite. About 28.5 ml
lignosulfonate retarder, commercially available from BJ Services
Company as R-21L, was then added to the mixture. Optionally, a
portion of the R-21L may be added with the barite in order to get
the barite into the mixture. About 28.5 ml of a naphthalene
sulfonate dispersant, commercially sold as CD-31L, and about 3.6 ml
of an oxyalkylated alkyl ester in heavy aromatic hydrocarbon,
commercially sold as MCS-A, both products of BJ Services Company,
were further stirred into the mixture for about 5 minutes. About 14
ml of SS-2 solvent was then added and the mixture was stirred for
about 5 minutes. Depending on capability testing, as defined in API
RB 10(b), it may be desirable to add US-2, contemporaneously with
the addition of SS-2.
[0039] From the foregoing, it will be observed that numerous
variations and modifications may be effected without departing from
the true spirit and scope of the novel concepts of the
invention.
* * * * *