| Literature DB >> 31890794 |
Abo Taleb T Al-Hameedi1, Husam H Alkinani1, Shari Dunn-Norman1, Mohammed M Alkhamis1, Justin D Feliz1.
Abstract
The oil and gas industry is moving towards more environmentally friendly practices. The environmental regulations regarding drilling waste management and disposal are motivating the industry to be more efficient with drilling operations. Environmentally friendly drilling fluid additives used in drilling operations reduces not only the negative implications on the environment but also reduces costs. This paper provides an experimental dataset of utilizing biodegradable waste materials as environmentally friendly drilling fluid additives. The data were collected through experimental evaluations of several waste materials including Potato Peels Powder (PPP), Mandarin Peels Powder (MPP), Fibrous Food Waste Material (FFWM), Palm Tree Leaves Powder (PTLP), Grass Powder (GP), and Green Olive Pits' Powder (GOPP). The data presented herein are the raw results of the experiments, which were conducted to examine the ability of the biodegradable waste materials to improve the water-based drilling fluids. The data include the effects of adding these waste materials on different drilling fluid properties such as mud weight, filtration, pH, and the rheology. The mud weight was measured using mud balance, the filtration data were collected using API filter press for both low/high pressure and temperature, the pH was measured using pH meter, and the rheology was characterized using viscometer. The dataset is potentially useful to assist researchers working on developing environmentally friendly drilling fluid additives.Entities:
Keywords: Biodegradable; Drilling fluid; Eco-friendly; Food waste
Year: 2019 PMID: 31890794 PMCID: PMC6926130 DOI: 10.1016/j.dib.2019.104945
Source DB: PubMed Journal: Data Brief ISSN: 2352-3409
Effect of variation in the concentration of the PPP on the properties of water-based mud.
| Property | RF | 1% PPP | 2% PPP | 3% PPP | 4% PPP |
|---|---|---|---|---|---|
| Mud Density, (ppg) | 8.6 | 8.6 | 8.62 | 8.64 | 8.65 |
| Plastic Viscosity (PV), (cp) | 7 | 7 | 8 | 9 | 10 |
| Yield Point (YP), (Ib/100ft2) | 11 | 7 | 6 | 6 | 6 |
| Initial Gel Strength, (Ib/100ft2) | 12 | 9 | 8 | 8 | 8 |
| Final Gel Strength, (Ib/100ft2) | 17 | 13 | 12 | 12 | 12 |
| pH | 10 | 8.4 | 8.2 | 8.1 | 7.9 |
| Mud Resistivity, (ohms-mt) | 7 | 5 | 4 | 3.75 | 3.4 |
| Mud Temperature, (°F) | 73 | 73 | 73 | 73 | 73 |
| Mud NaCl Concentration, (ppm) (nomograph) | 750 | 1100 | 1350 | 1500 | 1650 |
| 30 min Filtrate, (cc) | 12.5 | 11 | 10 | 9 | 8.75 |
| Filter Cake Thickness, (mm) | 3 | 1.7 | 1.75 | 1.8 | 1.8 |
| Filter Cake Thickness (mm) * (32/25.4), (1/32 inch) | 3.78 | 2.14 | 2.21 | 2.26 | 2.26 |
| Filter Cake Resistivity, (ohm-mt) | 2.1 | 1.6 | 1.5 | 1.3 | 1.1 |
| Filter Cake NaCl Concentration, (ppm) (nomograph) | 2700 | 3700 | 3900 | 4500 | 5200 |
| Pf, (cc) | 0.6 | 0.1 | 0.07 | 0.05 | 0.02 |
| Mf, (cc) | 1 | 0.3 | 0.35 | 0.4 | 0.5 |
| Pm, (cc) | 0.7 | 0.05 | 0.04 | 0.02 | 0.01 |
| Ca++, (mg/l) | 40 | 8 | 8 | 6 | 6 |
| NaCl, (mg/l) (ppm) | 182 | 324 | 578 | 625 | 775 |
| % by Vol. Solids (S.C) | 1 | 1 | 1 | 2 | 2 |
Effect of adding various concentration of MPP and PAC-LV on the properties of reference fluid.
| Property | RF | 1% MPP | 1% PAC-LV | 2% MPP | 2% PAC-LV | 3% MPP | 3% PAC-LV | 4% MPP | 4% PAC-LV |
|---|---|---|---|---|---|---|---|---|---|
| Mud Density, (ppg) | 8.6 | 8.4 | 8.6 | 8.2 | 8.4 | 8 | 8.35 | 8 | 8.35 |
| PV, (cp) | 7 | 14 | 25 | 24 | 52 | 38 | 69 | 63 | None |
| YP, (Ib/100ft2) | 11 | 14 | 26 | 17 | 68 | 33 | 109 | 57 | None |
| Initial Gel Strength, (Ib/100ft2) | 12 | 10 | 15 | 10 | 37 | 12 | 55 | 24 | 110 |
| Final Gel Strength, (Ib/100ft2) | 17 | 14 | 36 | 14 | 68 | 17 | 99 | 28 | 185 |
| pH | 10 | 8 | 9.7 | 7.7 | 9.3 | 7 | 9.3 | 6.8 | 9.2 |
| Mud Resistivity, (ohms-mt) | 7 | 5.8 | 5.5 | 5.2 | 4 | 5 | 3 | 4.8 | 2.2 |
| Mud Temperature, (°F) | 73 | 76 | 74 | 76 | 76 | 76 | 82 | 74 | 84 |
| Mud NaCl, (ppm) | 750 | 900 | 950 | 1000 | 1300 | 1050 | 1600 | 1100 | 2200 |
| 7.5 min Filtrate, (cc) | 6 | 3.5 | 3 | 2.75 | 2.5 | 2 | 2 | 1.75 | 1.75 |
| 30 min Filtrate, (cc) | 12.5 | 7 | 6 | 6 | 5 | 4.5 | 4.5 | 4 | 3.75 |
| Filter Cake Thickness, (mm) | 3 | 1.6 | 1.9 | 1.4 | 2.2 | 1.35 | 2.3 | 1.35 | 2.5 |
| Filter Cake Resistivity, (ohm-mt) | 2.1 | 1.3 | 0.85 | 0.85 | 0.71 | 0.77 | 0.4 | 0.77 | 0.32 |
| Filter Cake Temperature, (°F) | 73 | 72 | 74 | 74 | 76 | 74 | 84 | 74 | 78 |
| Filter Cake NaCl, (ppm) | 2700 | 4500 | 6600 | 7000 | 8000 | 7500 | 13000 | 7500 | 18500 |
| Ca++, (mg/l) | 40 | 4 | 8 | 4 | 12 | 4 | 12 | 4 | 12 |
| NaCl, (mg/l) (ppm) | 182 | 247.5 | 330 | 330 | 450 | 330 | 495 | 330 | 660 |
Effect of variation in the concentration of the FFWM on the properties of water-based mud (pH = 9.3).
| Property | RF | 1% FFWM | 2% FFWM |
|---|---|---|---|
| Mud Density, (ppg) | 8.6 | 8.6 | 8.6 |
| PV, (cp) | 6 | 8 | 8 |
| YP, (Ib/100ft2) | 9 | 11 | 13 |
| Initial Gel Strength, (Ib/100ft2) | 8 | 11 | 13 |
| Final Gel Strength, (Ib/100ft2) | 14 | 15 | 16 |
| 30 min Filtrate, (cc) | 12.5 | 10.25 | 8.75 |
| Filter Cake Thickness, (mm) | 3 | 2.4 | 1.9 |
| Filter Cake Thickness (mm) * (32/25.4), (1/32 inch) | 3.8 | 3 | 2.4 |
Effect of variation in the concentration of the FFWM on the properties of water-based mud (pH = 11.5).
| Property | 1% FFWM | 2% FFWM |
|---|---|---|
| Mud Density, (ppg) | 8.6 | 8.6 |
| PV, (cp) | 8 | 9 |
| YP, (Ib/100ft2) | 15 | 17 |
| Initial Gel Strength, (Ib/100ft2) | 17 | 18 |
| Final Gel Strength, (Ib/100ft2) | 25 | 27 |
| 30 min Filtrate, (cc) | 8.5 | 7 |
| Filter Cake Thickness, (mm) | 1.8 | 1.8 |
| Filter Cake Thickness (mm) * (32/25.4), (1/32 inch) | 2.26 | 2.26 |
Effects of adding various concentrations of PTLP to the reference fluid (fresh conditions).
| Property | RF | 1.5% PTLP | 3% PTLP |
|---|---|---|---|
| Plastic Viscosity (PV), (cp) | 8 | 9 | 12 |
| Yield Point (YP), (Ib/100ft2) | 12 | 5 | 5 |
| Initial Gel Strength, (Ib/100ft2) | 15 | 6 | 7 |
| Final Gel Strength, (Ib/100ft2) | 20 | 11 | 12 |
| pH | 11 | 8.8 | 8 |
| 7.5 min Filtrate, (cc) | 6 | 4 | 3.25 |
| 30 min Filtrate, (cc) | 12.5 | 9.25 | 8.5 |
| Filter Cake Thickness, (mm) | 3 | 1.9 | 2 |
Effects of adding various concentrations of PTLP to the reference fluid (aged conditions).
| Property | 1.5% PTLP | 3% PTLP |
|---|---|---|
| Plastic Viscosity (PV), (cp) | 9 | 9 |
| Yield Point (YP), (Ib/100ft2) | 6 | 5 |
| Initial Gel Strength, (Ib/100ft2) | 6 | 6 |
| Final Gel Strength, (Ib/100ft2) | 12 | 11 |
| pH | 8.7 | 8.1 |
| 7.5 min Filtrate, (cc) | 4.25 | 4 |
| 30 min Filtrate, (cc) | 9.5 | 9 |
| Filter Cake Thickness, (mm) | 2 | 2 |
Effect of variation in the concentration of the GP and starch on the reference fluid properties of water-based mud.
| Property | RF | 0.5% GP | 0.5% Starch | 1% GP | 1% Starch | 1.5% GP | 1.5% Starch |
|---|---|---|---|---|---|---|---|
| Mud Density, (ppg) | 8.6 | 8.6 | 8.6 | 8.6 | 8.6 | 8.5 | 8.55 |
| Marsh Funnel Viscosity, (Sec.) | 33 | 41 | 46 | 44 | 56 | 49 | 67 |
| PV, (cp) | 8 | 9 | 10 | 9 | 12 | 13 | 17 |
| YP, (Ib/100ft2) | 17 | 19 | 22 | 20 | 27 | 25 | 36 |
| Initial Gel Strength, (Ib/100ft2) | 12 | 20 | 21 | 22 | 23 | 26 | 39 |
| Final Gel Strength, (Ib/100ft2) | 24 | 25 | 33 | 26 | 35 | 33 | 50 |
| pH | 11 | 9.4 | 10.4 | 9.2 | 10.3 | 8.7 | 9.9 |
| Mud Resistivity, (ohms-mt) | 7 | 4 | 5.5 | 3.5 | 4 | 3 | 3.2 |
| Mud Temperature, (°F) | 77 | 77 | 77 | 77 | 77 | 77 | 77 |
| Mud NaCl Concentration, (ppm) | 750 | 1300 | 900 | 1400 | 1150 | 1850 | 1550 |
| 7.5 min Filtrate, (cc) (LTLP) | 6 | 3.5 | 4 | 3.5 | 3.25 | 3 | 2.75 |
| 30 min Filtrate, (cc) (LTLP) | 12.5 | 7.25 | 9 | 7 | 7.5 | 6.25 | 6 |
| Filter Cake Thickness, (mm) (LTLP) | 3 | 2 | 2.6 | 2 | 2.4 | 2.5 | 2.8 |
| 7.5 min Filtrate, (cc) (HTHP) | 19 | 13 | 18 | 11.5 | 13 | 10.5 | 11 |
| 30 min Filtrate, (cc) (HTHP) | 35 | 26 | 34 | 23 | 27 | 20 | 23 |
| Filter Cake Thickness, (mm) (HTHP) | 4.9 | 3.4 | 5.4 | 3.5 | 5 | 4.7 | 6.5 |
| Filter Cake Resistivity, (ohm-mt) | 2.1 | 0.51 | 0.82 | 0.4 | 0.5 | 0.34 | 0.41 |
| Filter Cake Temperature, (°F) | 77 | 77 | 77 | 77 | 77 | 77 | 77 |
| Filter Cake NaCl Concentration, (ppm) | 2700 | 11000 | 6500 | 14000 | 12300 | 17000 | 14250 |
| Ca++, (mg/l) | 50 | 14 | 50 | 14 | 50 | 8 | 50 |
| Filtrate NaCl Concentration, (ppm) | 182 | 577 | 330 | 825 | 495 | 990 | 660 |
| % by Vol. Solids (S.C) | 1 | 1 | 1 | 1 | 1 | 1 |
Impact of variation in the concentration of green olive pits’ powder (GOPP) on the specifications of water-based mud.
| Property | RF | 0.75% GOPP | 1.5% GOPP |
|---|---|---|---|
| Mud Density, (ppg) | 8.6 | 8.6 | 8.5 |
| Plastic Viscosity (PV), (cp) | 5 | 6 | 7 |
| Yield Point (YP), (Ib/100ft2) | 11 | 30 | 26 |
| Initial Gel Strength, (Ib/100ft2) | 12 | 23 | 20 |
| Final Gel Strength, (Ib/100ft2) | 17 | 31 | 29 |
| pH | 9.7 | 8.5 | 8.1 |
| 7.5 min Filtrate, (cc) | 6 | 5 | 5.5 |
| 30 min Filtrate, (cc) | 12 | 10 | 11.5 |
| Filter Cake Thickness, (mm) | 2.6 | 2.4 | 3 |
Specifications Table
| Subject | Waste Management and Disposal |
| Specific subject area | Drilling fluid characteristics for water-based mud |
| Type of data | Table |
| How data were acquired | Experimental measurements using various equipment such as Electronic Analytical Balance, pH Meter, Mud Mixer, Mud Balance, LTLP Filter Press, HTHP Filter Press, Model 800 Viscometer, Marsh Funnel Viscometer, Digital and Manual Vernier Calipers, Resistivity Meter, Chemical Titration, Retort Kit, Aged Cell and Accessories, and Roller Oven and Accessories |
| Data format | Raw |
| Experimental factors | Various properties of water-based drilling mud samples at different temperatures and pressures have been studied |
| Experimental features | In summary, all the experimental studies indicated that biodegradable and environmentally friendly waste products can be exploited as an alternative or supportive additive to conventional drilling fluid chemicals |
| Data source location | Missouri University of Science and Technology |
| Data accessibility | With the article |
The focal point of this data is to recognize various eco-friendly waste materials and how they can be exploited in drilling operations, particularly in drilling fluids. The data are useful because using eco-friendly additives in drilling fluid is a limited topic in the literature and due to strict environmental regulations, oil companies are shifting to use more environmentally friendly additives to reduce the effect on the environment and cost. The data will benefit any interested researchers who want to further investigate the use of eco-friendly waste materials in the drilling operation or other oil and gas-related applications. The data in this article will serve as a base for future researchers on the subject of utilizing biodegradable wastes in the petroleum industry. The researchers will be able to test different waste materials under different temperatures and aging conditions. Finally, once these materials prove their potential under hostile environments, they can be tested and applied in the oilfield. |