Abstract
The focus of this research was to present a data article for analyzing the cost of displacing a drilling fluid during the drilling operation. The cost of conventional Spud, KCl and Pseudo Oil base (POBM) muds used in drilling oil and gas wells are compared with that of a Reversible Invert Emulsion Mud. The cost analysis is limited to three sections for optimum and effective Comparison. To optimize drilling operations, it is important that we specify the yardstick by which drilling performance is measured. The most relevant yardstick is the cost per foot drilled. The data have shown that the prices for drilling mud systems are a function of the mud system formulation cost for that particular mud weight and maintenance per day. These costs for different mud systems and depend on the base fluid. The Reversible invert emulsion drilling fluid, eliminates the cost acquired in displacing Pseudo Oil Based mud (POBM) from the well, possible formation damage (permeability impairment) resulting from the use of viscous pill in displacing the POBM from the wellbore, and also eliminates the risk of taking a kick during mud change-over. With this reversible mud system, the costs of special fluids that are rarely applied for the well-completion purpose (cleaning of thick mud filter cake) may be reduced to the barest minimum.
Specifications Table
Subject area | Petroleum Engineering |
More specific subject area | Drilling Engineering |
Type of data | Table, figure |
How data was acquired | An oil well in Niger-Delta region, it was planned to be drilled as an Appraisal and Development oil well to a depth of 9513 ft in four hole sections. These are the 20” (stove pipe), 16”, 12 ¼” and 8 ½” hole sections. The cost of additives and chemicals used were received on March, 2018 from Best Land and Sea (BLS) Service. |
Data format | Raw, Analyzed |
Experimental factors | The prices are based on build cost for a certain mud weight and daily maintenance expense. |
Experimental features | To optimize drilling operations, it is important to specify the yardstick by which drilling performance is measured. For the data set, the most relevant yardstick is the cost per foot drilled; which can be used in drilling contracts. |
Data source location | Rivers State, Nigeria. |
Data accessibility | Data are available within this article. |
Related research article | None. |
Value of the data
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These data describe the volume and material estimate needed for each hole section and the type of mud necessary to achieve smooth drilling operation in each hole section.
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The data showed the cost, the quantity of materials and sequence at which these materials are applied to achieve optimum displacement.
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These data can be used to study the economic analysis of new mud systems proposed by researchers and also help to compare if these mud systems are economically viable.
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These data can also be used to analyze and predict prices and/or build cost for drilling mud systems for a certain mud weight and daily maintenance expense.
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The data reveals that cost varies according to the different mud types and are dependent on the base fluid phase.
1. Data
The type of drilling fluid systems and the volume of drilling fluid needed for each hole section is summarized in Table 1. The well was spudded with Bentonite/Polymer mud system. The mud was then converted to KCl/Polymer mud system by the addition of Pre-hydrated KCl into the system. The 12 ¼” hole section was drilled with Pseudo Oil Based Mud (POBM) system. The 8 ½” development hole section was drilled with Non-Aqueous Fluid system (NAF).
Table 1.
Summary of mud types used during the drilling operation.
Components | Well sections | |||
---|---|---|---|---|
Open hole diameter | 24 ˝ | 16 ˝ | 13 5/8 ˝ | 12 1/4 ˝ |
Casing/ liner diameter | 16 ˝ | 13 5/8 ˝ | 12 1/4 ˝ | 8 1/2 ˝ |
Description | Surface/conductor | Top hole | Intermediate | Reservoir section |
Conventional mud type | SPUD | KCL | POBM | NAF |
The volume of drilling fluids needed for three sections was estimated and presented in Table 2, Table 3, Table 4. The cost and how successful an oil or gas well will be completed depends to a substantial extent, on the properties and characteristics of the drilling fluid (Amorin et al. [1]). A considerable number of drilling fluid formulations have been developed by researchers and the selection of the best fluid to meet the formation to be drilled conditions will minimize well costs.
Table 2.
Volume estimate for the bentonite/ polymer mud system (SPUD mud).
S/N | Section | Internal diameter, ID | ID square | Depth (ft) | Conversion factor | Volume of mud |
---|---|---|---|---|---|---|
1 | Surface volume | 600 | ||||
2 | 24" Casing to 400 ft | 24 | 576 | 400 | 1029 | 223.9067055 |
3 | 16" Open hole to 2000ft | 16 | 256 | 1600 | 1029 | 398.0563654 |
4 | Wash out 20% | 244.3926142 | ||||
5 | Losses behind casing 20% | 0 | ||||
6 | PIT/transit losses 5% | 61.09815355 | ||||
7 | Hole enlargement | 39.80563654 | ||||
8 | Total volume (bbl) | 1567.259475 |
Table 3.
Volume estimate for KCl/ polymer mud.
S/N | Section | Internal diameter, ID | ID square | Depth (ft) | Conversion factor | Volume of mud |
---|---|---|---|---|---|---|
1 | Surface volume | 600 | ||||
2 | 24" Casing to 400 ft | 24 | 576 | 400 | 1029 | 223.9067055 |
3 | 16" Open hole to 5010 ft | 16 | 256 | 4610 | 1029 | 1146.899903 |
4 | Wash out 20% | 394.1613217 | ||||
5 | Losses behind casing 20% | 394.1613217 | ||||
6 | PIT/transit losses 5% | 98.54033042 | ||||
7 | Hole enlargement | 114.6899903 | ||||
8 | Total volume (bbl) | 2972.359572 |
Table 4.
Volume estimate for POBM mud.
S/N | Section | Internal diameter, ID | ID square | Depth (ft) | Conversion factor | Volume of mud |
---|---|---|---|---|---|---|
1 | Surface volume | 600 | ||||
2 | 13 3/8" casing @ 5000 ft | 13.375 | 178.89063 | 5000 | 1029 | 869.2450194 |
3 | 12 1/4" open hole to 9386 ft | 12.25 | 150.0625 | 4386 | 1029 | 639.625 |
4 | Wash out 20% | 421.7740039 | ||||
5 | Losses behind casing 20% | 421.7740039 | ||||
6 | PIT/transit losses 5% | 105.443501 | ||||
7 | Hole enlargement | 63.9625 | ||||
8 | Total volume (bbl) | 3121.824028 |
The cost for drilling a typical well may be constant when drilled without any instability case. Instability during a drilling operation in wells can quickly escalate cost dramatically (Okoro et al. [2]). The materials and their cost for each drilling fluid systems are presented in Table 5, Table 6, Table 7.
Table 5.
Spud mud material estimate.
Products | Unit size (kg) | Cost/unit (USD) | Conc.: lbs/bbl | Units | Total cost (USD) |
---|---|---|---|---|---|
Bentonite (1mt) | 1000 | 605 | 25 | 18 | 10890.00 |
Caustic Soda | 25 | 75 | 0.25 | 8 | 600.00 |
Soda Ash | 25 | 32 | 0.25 | 8 | 256.00 |
CMC HV | 25 | 124 | 2 | 57 | 7068.00 |
CaCO3 fine | 50 | 21 | 10 | 143 | 3003.00 |
CMC LV | 25 | 124 | 2 | 57 | 7068.00 |
Drilling surfactant | 55 | 945 | 0.5 | 7 | 6615.00 |
Ultra seal | 25 | 100 | 2 | 57 | 5700.00 |
Mica | 25 | 36.3 | 2 | 57 | 2069.10 |
Total cost (USD) | 43269.10 | ||||
Total volume (bbl) | 1567.26 | ||||
MD (ft) | 2000.00 |
Table 6.
KCl/ polymer mud material estimates.
Products | Unit size (kg) | Cost/unit (USD) | Conc.: lbs/bbl | Units | Total cost (USD) |
---|---|---|---|---|---|
Bentonite (1mt) | 1000 | 605 | 18 | 25 | 15125.00 |
Caustic soda | 25 | 75 | 0.25 | 14 | 1050.00 |
Soda ash | 25 | 32 | 0.25 | 14 | 448.00 |
PAC-R | 25 | 150 | 2 | 108 | 16200.00 |
Borhamyl starch | 25 | 62.5 | 4 | 216 | 13500.00 |
PAC-L | 25 | 150 | 1 | 54 | 8100.00 |
XCD polymer | 25 | 312 | 1 | 54 | 16848.00 |
KCl (1mt) | 1000 | 1450 | 21 | 29 | 42050.00 |
CaCO3 F/M | 50 | 21 | 10 | 270 | 5670.00 |
Soltex | 25 | 108 | 4 | 216 | 23328.00 |
Surfactant (gal) | 1 | 945 | 1 | 8 | 7560.27 |
Mica fine | 25 | 36.3 | 2 | 108 | 3920.40 |
Ultra seal LCM | 25 | 100 | 2 | 108 | 10800.00 |
Barite (1mt) | 1000 | 400 | 50 | 68 | 27200.00 |
Paraffin (bbl) | 36 | 266.65 | 2 | 24 | 6399.60 |
Total cost (USD) | 183074.27 | ||||
Total volume (bbl) | 2972.36 | ||||
MD (ft) | 5010.00 |
Table 7.
POBM mud system material and cost estimate.
Product | Unit size | Unit price (USD) | Conc.: ppb/bbl | Sxs/drm/bbl | Total cost (USD) |
---|---|---|---|---|---|
EDC 99 DW (1 bbl) | 0.5 | 266.65 | 0.64 | 8 | 2133.20 |
Primary emulsifier (gal) | 4 | 535 | 6 | 49 | 26215.00 |
Secondary emulsifier (gal) | 4 | 715 | 3 | 24 | 17160.00 |
Organophilic clay (kg) | 25 | 88 | 8 | 454 | 39952.00 |
Lime (kg) | 25 | 13.5 | 4 | 227 | 3064.50 |
Soltex (kg) | 25 | 108 | 4 | 227 | 24516.00 |
CaCO3 F/M (kg) | 50 | 21 | 8 | 227 | 4767.00 |
Barite (mt) | 1000 | 400 | 219 | 311 | 124400.00 |
Calcium chloride (kg) | 25 | 24.35 | 30 | 1700 | 41395.00 |
Rheology modifier (gal) | 4 | 810 | 1 | 8 | 6480.00 |
Wetting agent (kg) | 55 | 590 | 0.85 | 22 | 12980.00 |
Fresh water (1 bbl) | 0.5 | 0 | 0.236 | 3 | 0.00 |
Total cost (USD) | 303062.70 | ||||
Total volume (bbl) | 3122.08 | ||||
MD (ft) | 9386.00 |
Fig. 1, Fig. 2 illustrates the cost per barrel and cost per feet drilled respectively for the mud systems used in the drilling operations.
Fig. 1.
Cost per barrel for each mud systems.
Fig. 2.
Cost per feet drilled for each mud systems.
The build cost for a drilling fluid system is the price for the individual components and mixing requirements. The total build cost includes purchasing the initial drilling systems materials and the expenses involved with conditioning the drilling mud system in the well as it is drilled.
2. Experimental design, materials, and methods
The water-based mud in the wellbore from the previous hole section is displaced and replaced with POBM drilling fluid. The first step is to lower the viscosity and gel strength of the water-based mud. The suggested method is to dilute the fluid with water to obtain a low rheology (Patel [3]). The optimal thinning of the water-based mud will dictate how easy the mud will be displaced out of the hole. The spacer is pumped first, followed by the POBM mud at maximum pump rate to get the mud in the annulus moving (Table 8).
Table 8.
500 bbls sweep and seal pill formulation.
Products | Unit size (kg) | Cost/ unit (USD) | Concentration (ppb) | Units | Total cost (USD) |
---|---|---|---|---|---|
CaCO3 fine | 50 | 21 | 20 | 109 | 2289.00 |
CaCO3 medium | 50 | 21 | 10 | 55 | 1155.00 |
Soltex | 25 | 108 | 4 | 44 | 4752.00 |
OBM LCM (lb) | 50 | 59 | 4 | 22 | 1298.00 |
Total cost | 9494.00 |
After drilling and prior to running completion hardware, the fluid in the borehole is often displaced to a water-based completion fluid, usually a solution of various salts. During this displacement, chemical washes and viscous spacers are placed in the solution to make surfaces water- wet, while helping to remove oil mud and residual oil-wet material from the borehole (Ali et al. [4]).
The viscosity and gel strengths of the POBM are low prior to displacement. The suggested method was to dilute the fluid with premix, base fluid or a thinner to obtain the low rheology if this is necessary. The optimal thinning of the POBM fluid will dictate how easy the mud will be displaced out of the hole.
The volume of drilling fluid needed for each section was obtained using the equation below:
(1) |
Where,
ID = Hole Internal Diameter, inch
D = Hole Depth, ft
Eqs. (2), (3) were used to estimate the product units needed in gallons and kilogram respectively;
(2) |
(3) |
Eq. (4) was used to convert the quantity of additives used from lb/bbl to sxs:
(4) |
Where,
sxs = Sacks
lb/bbl = Pound per barrel
bbl = Barrel
Acknowledgments
The authors would like to thank Covenant University Centre for Research Innovation and Discovery (CUCRID) Ota, Nigeria for its support in making the publication of this research possible.
Footnotes
Transparency data associated with this article can be found in the online version at 10.1016/j.dib.2018.05.075.
Supplementary data associated with this article can be found in the online version at 10.1016/j.dib.2018.05.075.
Transparency document. Supplementary material
Supplementary material
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Appendix A. Supplementary material
Supplementary material
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References
- 1.Amorin R., Dosunmu A., Amankwah R.K. Economic viability of the use of local pseudo-oils for drilling fluid formulation. Ghana Min. J. 2015;15(2):81–90. [Google Scholar]
- 2.E.E. Okoro, A. Dosunmu, S. Iyuke and B. Oriji, Impact of reversible invert emulsion drilling fluid rheology on production. SPE-178308MS, Paper Presented at the Nigeria Annual International Conference and Exhibition, August 4–6, 2015.
- 3.A.D. Patel, Reversible invert emulsion drilling fluids – a quantum leap in technology. SPE 47772 presented at the IADC/SPE Asia Pacific Drilling Technology Conference, Jakarta, Indonesia, September 7-9, 1999.
- 4.S. Ali, M. Bowman, M. Luyster, A. Patel, C. Svoboda, A. McCarty and B. Pearl, Reversible drilling-fluid emulsions for improved well performance. Oilfield Review, Autumn, 2004.
Associated Data
This section collects any data citations, data availability statements, or supplementary materials included in this article.
Supplementary Materials
Supplementary material
Supplementary material