Dowell
Well Conditions
PROBLEM Well control
over pressure and weak formations Temperature Permeable formations Mud removal Friction pressure Mixability/Pumpability Lost circulation Density Thickening time Fluid Stability Fluid loss control
Plugging/Bridging properties Density SLURRY PARAMETER Rheology Extenders Weighting agents Accelerators Retarders FLAC Dispersants Gelling Agents LCM Extenders ADDITIVE CATEGORY SOLUTIONS
Cement Additives
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Accelerators and Retarders
n Change thickening time
n Alter rate of compressive strength development
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Extenders
n Reduce slurry density
n Increase slurry yield
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Weighting Agents
n Increase density
Cement Additives
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Fluid Loss Control
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Lost Circulation Material
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Specialty:
n Antifoam/defoamer additives
n Bonding agents
n Expansive additives
n Gas migration control additives
n Gelling and suspending additives
Conductors
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Prevents washing out under
rig
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Short rig downtime
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Quick setting cement - rapid
development of compressive
strength
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Accelerated slurries, e.g..:
n Neat cement + NaCl (D44) 3-5%
Surface Casings
l Unconsolidated zonesl BOP support
l Protect surface waters
l Prevent fluid flow
l Very large volumes of slurry
l Light weight slurries
l Strong slurry at shoe (accelerated)
l Extended lead with neat tail, e.g..:
Thickening & Setting Time
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Control to
n Reduce WOC (reduce rig-time)
n Reduce chance for fluid/gas flow
n Allow time to complete job
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Affected by
n Temperature
n Pressure
n Cement type (class and grind)
Accelerators
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Applications
n Shallow casings (conductor, surface)
n Low temperature conditions
n Offset retarding effects of other additives
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Additives
n Calcium Chloride (CaCl2) - 1-4%
n Sodium Chloride (NaCl) - <15%
n Other salts (carbonates, silicates, nitrates, etc..)
Calcium Chloride
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S1, S2, D77
n Most active accelerator
n Range 1-4%
n Effect on Thickening Time
Thickening Time (h:mn)
CaCl
2(%BWOC)
91
oF
103
oF
113
oF
0
4:00
3:30
2:32
2
1:17
1:11
1:10
Compressive Strength
Compressive Strength at Temperature (psi) 60oF 80oF 100oF CaCl2 (%) 6 hr 12 hr 24 hr 6 hr 12 hr 24 hr 6 hr 12 hr 24 hr 0 NS 60 415 45 370 1260 370 840 1780 2 125 480 1510 410 1020 2510 1110 2370 3950 4 125 650 1570 545 1245 2890 1320 2560 4450
Secondary Effects of CaCl
2
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Increased temperature
n Heat of solution of CaCl2
n Additional accelerating effect (on surface?)
n Casing expansion
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Increased rheology (gelation)
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Possible permeability increase
Sodium Chloride
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Sodium Chloride (D44) as an accelerator
nNot very efficientnActs as an accelerator < 15% BWOW nPreferred range is 3 - 5 % BWOW
136°F (58°C) 154°F(68°C) 179°F (81°C) 8 6 4
Retardation of Cement Systems
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Applications
n Intermediate and production strings
n Surface and conductor casings (long pumping times)
n Squeeze and cement plugs
n High temperature and depth
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Chemical Classes of Retarders
n Lignosulphonates (D13, D81, D800, D801)
n Hydroxycarboxylic acids (D109, D110, D45)
n Inorganic compounds (D93, D74)
Mechanisms of Retardation
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Factors affecting mechanism of action
n Chemical nature of retarder
n Chemical composition of cement
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Theories of mechanism of action
n Adsorption theory
n Precipitation theory
n Nucleation theory
n Complexation theory
Cement Retarders
D13/D81 D13/D81 with Dispersant D800/D801 D800/D801 with D93/L10 D110 D110 with D93/L10 D28/D150 D28/D150 with D121 D28/D150 with D93 BHCT BHCT ooFF Retarder 100 200 300 400 140 100 185 125 250 250 310 300 175 300 375 220 300 350 300 400 300 100 Fresh Sea 37% NaCl X X X X X X X X X X X X X X X X X X X X X X XLignosulfonates
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Low to mid temperature use
n D13 (D81) <185oF
n D800 (D801) 140o - 220oF
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Pulping by-product
n Variable performance
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Efficiency improved 150
o- 175
oF
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Tendency to gel at higher concentrations
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May require dispersion
Hydroxycarboxylic Acid
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Powerful retarders
n D110 (D109) - 175o - 325oF
n D45 (salt dispersant)
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Detrimental effect with lattices
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Some dispersion
Inorganic Retarders
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Retarder aid - D93
n Has no retarding capacity by itself
n Extends temperature range for other retarders
n Detrimental effect on fluid loss
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Sodium Chloride (D44)
n Retards at concentrations over 20%
n May over-retard at low temperatures
Cellulose
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CMHEC (D8) - Diacel LWL
n Sometimes used for retardation
n Viscosifying
n Effective to 250oF
n Some fluid loss control
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Other fluid loss additives
Blended Retarders
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Generally lignosulfonate with other material
n D28 (D150) - 220o - +300oF
n D121 - 250o - 350oF
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Dispersing action as well, especially at high
concentration
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D121 erratic below 300
oF
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D121 may overdisperse
D161
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High Temperature Retarder (>250
oF)
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Rapid Strength Development
n Lengthens Dormant Period; not Hydration Rate
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Reduced Sensitivity to
n Concentration Error
n Temperature Error
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Effective in Fresh Water, Seawater, and Salt Water
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Liquid
Applications
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Cementing Long Liners and Casing
n Single Stage vs. Two-Stage Jobs
n Single Slurry Replacing a Lead and Tail Slurry
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Squeeze Cementing
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Kick-off Plugs
D161 Setting Characteristics
psi @ 320 o F to TT @ 350 o F 0 1 2 3 4 5 6 7 8 Conventional D161 Ratio of TTR 50 psi @ 320 o F to TT @ 350 o FCS to TT Ratio
D161 D121/D28 D93/D110 D66 (%BWOC) D47 (gps) D158 (gps) Disp (% or gps) 35 0.05 0.5 0.06 35 0.05 0.5 1.00 35 0.05 0.5 1.00 35 0.05 0.5 0.06 35 0.05 0.5 0.06 Retarder (% or gps) D93 (%BWOC) 1.25 ---1.50 ---2.00 ---0.24 0.40 0.40 0.40Thickening Time (hr:min) at 350oF:
5:27 3:32 4:12 4:12 8:53
Compressive Strength (hr:min) at 320oF:
TTR 50 psi TTR 500 psi 8:18 10:10 19:03 21:48 25:46 28:59 35:52 38:45 30:13 33:27
Compressive Strength Development
2 4 6 8 10 12 14 16 18 20 22Time to reach compressive
strength at 320 ° F (hr) 3000 psi 500 psi 50 psi
Slurry Density
CHANGING OF SLURRY DENSITY
LIGHTER MORE WATER* ABSORBENT LIGHT MATERIAL LOWER DENSITY
Cement Extenders
Bentonite
LITEPOZ* 3 D35 LITEPOZ 7 D61
TXI Lightweight Cement Diacel D D56 Expanded Perlite D72 Gilsonite D24 KOLITE* D42 Sodium Metasilicate D79 Sodium Silicate D75
Slurry Density (lb/gal) Extender or Lightweight System 6 7 8 9 10 11 12 13 14 15 15 12 14.7 10.8 13.6 12 14.2 11 14.5 10.6 13.8 12 15 11 14.5 14.5 11.5 11.5 12 15
Classification of Extenders
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Water “absorbing” extenders
n Clays (Bentonite) - D20, D128
n Chemical extenders (Silicates) - D75, D79
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Low density solids
n Pozzolans (Fly ashes) - D35, D56, D61, D602
n KOLITE* and gilsonite - D42, D24
n Expanded perlite - D72
n Silica fume (Microsilica) - D154, D155
Bentonitic Extenders
• General properties:
•
BENTONITE CLAY
BENEFICIATED (PEPTIZED) NON - TREATED
MONTMORILLONITE - D20 (FRESH)
ATTAPULGITE - D128 (SEA)
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n Water based extender n
Bentonite (D20)
l Allow addition of extra water, yet control free water
n Optimum water content must be determined
n Starting point - 5.3% additional water per 1% bentonite
l Additional water means
n Reduced cost (increased yield)
n Reduced strength
n Increased permeability
n Reduced resistance to chemical attack by brines
l Viscosifies slurries (requires dispersant >6% D20)
l Slurry stabilizer (free water and sedimentation)
Chemical Extenders
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Silicates
n React with cations in cement system (Ca2+, Mg2+)
n Form viscous, gelatinous silicate gel - Capable of binding extra water
- Low free water separation
n Low rheologies for turbulent flow
n Better properties and mixing than bentonite slurries
n No inherent fluid-loss control
n Relatively low concentrations required
Point of Departure
20 68 100 0 20 40 60 80 100 0 20 40 60 80 100 120 140 160 180 200 Time (min) Consistency (Bc) 470* 468* 245* 170** 24 hr compressive strength (psi) of slurry removed and cured at 170oF Class G + 2% D79 (12.5 ppg)
D75 Slurries
Shear 24 hr Compressive Strength
(min) (psi)
20 650
90 640
140 470
260 200
POD is 90 minutes - plateau of 40 Bc at 150 minutes
Class G + 0.28 gps D75 @ 12.5 ppg D109 POD Time to 70 Bc (gps) (hr:mn) (hr:min) 0 1:50 +4:00 0.04 2:00 3:15 0.07 4:10 5:35 Class G + 0.24 gps D75 @ 13.0 ppg Tests at 118oF
Silicate Slurry Design
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Point of departure is the thickening time
n Optimize D75/D110
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Use D110 (D109) as retarder (erratic behavior with
lignosulfonates)
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Calcium chloride has little effect on compressive
strength
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Mixing
Lightweight Aggregates
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POZZOLANS: Fly Ash( D35), Volcanic Ash and
Diatomaceous Earth (D61, D602)
n React with calcium hydroxide in cement
n Corrosion brine resistance
n Low permeability
n Thermal resistance
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EXPANDED PERLITE (D72)
n Inert material and does not affect thickening times
n Normally add 2 - 6% BWOC bentonite to prevent floatation
n Gives reduced cement permeability
Pozzolans
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Naturally occurring
n Volcanic ashes n Diatomaceous earth (D61)l
Artificial
n Fly ashu Type F (D35, D48) - most common
u Type C (D132) - more reactive (cementitious)
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Key Properties
Microsilica (silica fume)
l Amorphous sub-micron spheresl Pozzolanic properties (reactive)
l Low bulk density (<15 lb/ft3)
l Provides some slurry stability
l Frequently blended with other lightweight additives (HiLITE -blend with D124)
l Bulk blending is difficult with dry material
l Liquid can be stored with minimal agitation
l Concentration up to 20%
l Dispersant is required to effectively disperse in water and prevent gelation
Ultra-Lightweight Extenders
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Ceramic microspheres, LITEFIL* D124
n Ceramic or glass microspheres
n Inert
n Specific gravity 0.7 - 0.8
n Fragile - pressure limitation of 5,000 psi
n Density range: 8.5 lb/gal to 14.5 lb/gal
n Enhanced strength and permeability
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Foamed cement systems
Lost Circulation Control
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Reduce density
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Reduce friction pressure
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Add LCM
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Granular
Granular Lost Circulation Materials
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D42 - KOLITE* additive
n Ground coal
n SG - 1.3
n Concentration - 5 - 25 lb/sk
n Slurry stability is key
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D24 - Gilsonite
n Ground asphaltinic material
n SG - 1.07
n Similar to D42
Flake Lost Circulation Materials
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D29 (Cellophane flake)
n Concentration - 1/8 to 1/2 lb/skl
D130 (Polyester flakes)
n Concentration - 1/8 to 1/2 lb/skl
Mechanisms
n Form “mat” on fractures, vugs, etc..
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Handling
Intermediate Casings
l Protect weak or sensitiveformations (production)
l May be 2 stage
l Low cost
l Extended lead and neat tail
l Most slurries are retarded
l May require fluid loss control
l May require special properties (e.g.. gas migration control)
Production Casings
l Isolate production zonesl Smaller diameter casings
l Cost less important
l Good bonding
l Fluid loss control is usually required
l Low friction pressures
l Mud removal is important
l 15.8 ppg or more slurries
Dispersants
l Cement slurry rheology
n Volume of particles / total volume
n Particle interactions
n Aqueous phase rheology
Change with dispersants
l Why dispersants ?
Dispersants
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TIC* Additive
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Superplasticizers
n PNS - D65, D80, D604M, D604AM n PMS - D145l
Plasticizers
n Cement retarders (D13, D81, D800, D801) n Mud thinnersDispersant Action
CEMENT Dispersant Molecule SO3 SO3C
2SH
- -0
3S
+Ca
+ +Ca
+ -0
3S
C
2SH
-Use of TIC D80 in ETD
Yield Value ( /100ft 2 ) 20 15 10 5 5 10 15 20 30 5 10 15 20 30 25 25 Overdispersed Yield value Free water Viscosity Plastic Viscosity (Cp) Free Water (%) Underdispersed Acceptable RangeUse of TIC D604M in ETD
Yield Value ( lb /100ft 2 ) 20 15 10 5 5 10 15 20 30 5 10 15 20 30 25 25 Yield value Free water Viscosity Plastic Viscosity (Cp) Free Water (%) Underdispersed Acceptable RangeFluid Loss in Cement Slurries
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Definition:
n Filtrate lost to the formation
n Filter cake deposited at formation face
n Cement particles left in annulus
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Why cement loses water:
n Differential pressure
n Permeable medium (formation)
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Fluid loss stages:
Dynamic vs. Static Fluid Loss
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Dynamic
n Placement
n Loss is proportional to time
n Filter cake reaches pseudo-stable thickness
n Density increases
n Slurry properties change
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Static
n After placement
Effect of Fluid Loss
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Damage to some formations by filtrate
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Gas migration through thick filter cake and through
poor quality cement
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Other properties:
Slurry yield Free water Thickening time Settling Bulk Shrinkage REDUCED INCREASED n n Hydrostatic n n Slurry density n n Plastic viscosity n n Yield point n n Compressive strength n n n n n n n n n n n n n n n n n n n n n n n n n n n n n nThickening Time versus Density
THICKENING TIME THICKENING TIME
160
Thickening Time (min)
Mechanisms of Fluid Loss Control
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Reduce cement filter cake permeability
n Particulate materials to fill voids
n Polymer particles to plug pores
n Change cement particle distribution with dispersants
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Increase viscosity of aqueous phase
n Water soluble polymers
FLAC* Additives
l Particulate-n Gel - D20
n Latex - D600 (MT,M-HD,L) D134(HT,HD,L)
n Microgels - D300, D500(AD,LT,L)
l Water Soluble Polymers
n Cellulose Derivative uD60, D59(MT,ND,S) D112(MT,LD,S) n Non-Ionic Polymer uD127(LT,S) B30(LT,S) D159(L-MT,AD,L) D160(L-MT,AD,S) n Anionic Polymer uD603(MT,ND,L) D143, D158(M-HT,HD,L), D156(LT,AD,S)
Dispersant Effect on Fluid Loss
Mechanism of action
• Disperse cement grains and improve packing --> reduced permeability • Flocculate w/salt ---> plugging action
• •
FILTER CAKE
Acceptable Fluid Loss Limits
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Gas zones
30 - 50 mL/30 min
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Liner
< 50 mL/30 min
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Casing
200 - 300 mL/30 min
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Horizontal well
<50 mL/30 min
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High density slurries:
<50 mL/30 min
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Squeeze
:
n Formation with K < 1 md 200 mL/30 min
Slurry Density
Less Water Changing Slurry Density
Lighter Heavier
More
Water* WaterLess
Absorbent Light Material Heavy Material Dispersant Lower Density Higher Density
Weighting Agents
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Requirements
n High specific gravity
n Compatible particle size and distribution (settling)
n Low water adsorption (efficiency)
n Availability and acceptable cost
n Purity and consistency of product
n Inert
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Commonly used weighting agents
Code Agent SG Additional water
Strength Retrogression
Above 230oF cement undergoes:
n Reduction in strength
n Increase in permeability
l Due to crystalline changes in CSH gel
CSH gel ---> alpha dicalcium silicate
amorphous crystalline
strong, impermeable weak, permeable
C/S = 1.5 C/S = 2.0
l Prevented by addition of 30 - 40% BWOC silica (reduces C/S ratio of C-S-H gel)
D30 Silica Sand & D66 Silica Flour
Particle size US Mesh Additional Water Specific gravity Applications: High density Low density Settling Problems
NAME SILICA SANDD30 SILICA FLOURD66
70 - 200 ±10% 1.12 gal/sk 2.63 Preferred Alternative Alternative Preferred > 200 + 12% 1.34 gal/sk 2.63
Antisettling Agent D153
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Controls free water and/or sedimentation
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Compatible with all Dowell products and cements
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No significant effects on slurry properties, except
rheology
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Dry-blend or prehydrated (preferred), fresh or sea
water
Antifoam Agents
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Purpose
n Prevent slurry gelation
n Allow true slurry density to be mixed and pumped
n Prevent pump cavitation (due to aeration)
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Mechanism of action:
n Lower surface tension
n Reduces film and causes rupture
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Types of antifoam agents
n Polyglycol ethers