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International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 07 Issue: 04 | Apr 2020 www.irjet.net p-ISSN: 2395-0072
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Use of Bamboo Leaf Ash as an Additive to Aqueous Drilling Fluid and
Study the Variation of Rheological and Filtration Loss PropertieS.
Gautham V Nairy1, Mohammed Farhan Jameel2, Mariam Susan Matthew3, Anushka U N4
Bhairab Jyoti Gogoi5
1Student & Dept. Petroleum Engineering, Presidency University, Bengaluru, India
2Student & Dept. Petroleum Engineering, Presidency University, Bengaluru, India
3Student & Dept. Petroleum Engineering, Presidency University, Bengaluru, India
4Student & Dept. Petroleum Engineering, Presidency University, Bengaluru, India
5Assistant Professor, Dept. Petroleum Engineering, Presidency University, Bengaluru, India
---------------------------------------------------------------------***---------------------------------------------------------------------
Abstract - Requisition of efficient use of imprudent by-products for the enhancement of drilling fluid is preferentially
beneficial for a hassle-free and relentless drilling process. Intricately designed drilling fluids have been used in the petroleum
industry having significant properties to meet many operational requirements. The conventional methods are proven to be
efficient in the current scenario, but they have limited capability and may not be suitable for future drilling operations due to
the increasing challenges in the petroleum industry. A need exists for a strong, stable and customizable fluid which can not
only satisfy the basic functions of a drilling mud, but also make productive use of waste products for its enhancement. This
paper deals with the possibility of using Bamboo Leaf Ash (BLA) as an additive in Water Based Drilling Fluid (WBDF). The
main components of BLA include silica (SiO2), aluminum (Al2O3) and iron oxide (Fe2O3). The yield percentage of silica from
bamboo leaf ash is 78%. In our study we have attempted to use BLA as an additive to WBDF comparative analysis of the
rheological properties of drilling fluids with different percentage of BLA has been studied. Based on the comparative study it is
observed that BLA can be used as an additive to WBDF.
Key Words: Drilling Fluid, Rheological Properties, Bamboo leaf ash …
1. INTRODUCTION
The exploration and exploitation of hydrocarbon on offshore and onshore environment suggest the use of
environmentally friendly drilling mud and its additives thereby preventing any harm to the aquatic bodies and the
terrestrial environment. Currently, various kinds of drilling fluid systems are used in the oil industry, among which the
significant ones include, Polymer based drilling fluid system, oil-based drilling fluid system, etc. Nevertheless, most of
them have some serious environmental concern, degradability issue and difficulty in the post-treatment, which bring the
contradiction between clean drilling and requirements of drilling operation. Environmental regulations uplift the use of
water-based drilling fluid and its application in areas where oil-based drilling fluids have previously been used due to their
challenges [1]. Most of the efficient drilling fluids have high toxicity and this toxicity is limiting the use of such drilling
fluids. In this scenario, the oil industry is in need of something known as eco-friendly drilling fluid, but to go with the idea
of preparing the same, two things are to be considered, i.e., the efficiency of the drilling fluid and, the cost of the drilling
fluid. In most of the cases we must compromise either one of these three: eco-friendly, economical, or efficiency, and in a
few cases, two of them [2]. The various properties of the drilling mud are rheological properties, filtration loss properties,
lubricating quality, pipe sticking tendency, thermal and bacterial inhibition, etc. Myriad additives are added for making the
drilling mud most suitable for the different conditions for viscosity, mud weight, prevent mud loss, have enough gel
strength and be reliable. A few additives such as calcium carbonate, starch and xanthan gum are common incorporated in
the formulation of a drilling mud [3]. Xanthan Gum also used as a viscosifier which controls the rheology. Starch is a fluid
loss control additive widely used in aqueous drilling fluids and has a thermal stability upto 250 °F [4]. Carboxymethyl
Cellulose (CMC) is another polymer which tends to increase shear stress as its concentration in the mud increases and the
fluid loss decreases. An optimum concentration is favorable in the drill mud [10]. The usage of Calcium Carbonate (CaCO3)
provides an ionic inhibition and hence serves as a bridging agent [5][6][7][8][9][10]. Caustic Soda, which is also known as
Sodium Hydroxide (NaOH), is used in water-based mud to have a check on the pH level and does affect the salinity of the
drilling mud [11]. To increase the density and for shale inhibition, Potassium Chloride (KCl) is used [12]. Mica is another
Loss Circulation material. Unlike cellopane material, Mica tends to avoid absorbing large amounts of free water or oil [12].
Lube oil used to have a check on the increased torque/drag, limited displacement, increased equipment stress [13]. To
provide weight to the drilling fluid, the usage of an inert, high density Barite is employed [14]. The main purpose of using
weighting materials is to increase its density and thereby ensuring the borehole stability [15]. It provides the required
hydrostatic pressure in the hole and has a check on the fluid loss by the formation of mud cake of the inner walls on the
well [16]. Bamboos belongs to the grass family Poaceae, a flowering plant in the subfamily Bambusoideae. Its growth rate
is 910 mm per day [17]. Bamboo forests covers around 12.8% of the total forest area and is found in most of the states of
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India. More than 50 per cent of the bamboo species appears in North East India i.e. Arunachal Pradesh, Assam, Manipur,
Meghalaya, Mizoram, Nagaland, Sikkim, and Tripura. Apart from these regions, there are significant traces of Bamboo leaf
in the Andamans, Bastar region of Madhya Pradesh and the Western Ghats. Bamboo leaf is an agro-waste product. A
typical composition of bamboo leaf ash is SiO2: 78%, Al2O3: 4.96% Fe2O3: 2.01% CaO: 4.43% MgO: 1.02% K2O: 3.09% P2O5:
0.72% TiO2: 0.36%, LOI: 1.58% [18]. Bamboo leaf ash has a lot of application in concrete industry. B Olutoge F.A. and
Oladunmoye O.M. used bamboo leaf as a supplementary cementing material. Ernesto Villar-Cociña concluded that BLA is
formed by amorphous silica. In this paper, we have come up with an idea in which our objectives are equally balanced.
With this approach, we use a natural organic material with bentonite and prepare a new drilling fluid which is less toxic,
economical, and environment friendly. We obtain it by processing the bamboo leaf in steps including drying, grinding,
heating it in a muffle furnace, removing the impurities to obtain an end product which consists of mainly silica. Bamboo
leaf ash has about 75.90% of SiO2 (Silicon Dioxide). The presence of silica provides high resistance to water penetration,
thermal and fungal decomposition [19]. This property can hence help in its usage to prevent fluid loss of the drilling fluid.
A comparative study between these additives is done to check for the rheological properties, filtration properties,
lubricating quality, stuck pipe efficiency, thermal and bacterial inhibition, and the various rheological properties.
2. MATERIAL AND METHODOLOGY
2.1 Material used
For the experiment we have used API Grade Bentonite, industry grade Barite (SG 4.2), Carboxy Methyl Cellulose (CMC,
Sigma Aldrich), Xanthan Gum (XC, Sigma Aldrich), Calcium Carbonate-Fine (CaCO3, Karnataka Fine Chem.), Sodium
Hydroxide (NaOH, Karnataka Fine Chem.), Potassium Chloride (KCl, Karnataka Fine Chem.), Lube Oil and Mica
2.2 Equipment used
API LPLT filter press (Fann Instrument Company): It is the most effective means of determining the filtration properties
of drilling muds and cement slurries.
Lubricity tester (Fann Instrument Company): The Lubricity tester is a high-quality instrument used to measure the
lubricating quality of drilling fluids.
Differential sticking tester (Model 21150 Fann Instrument Company, Houston, Texas): The Differential Sticking Tester
measures the “Stuck Pipe Tendency Coefficient” of drilling fluids, and determines how effective lubricants or treatments
might be with any given drilling fluid.
Fann VG meter (Fann Instrument Company): It is also known as direct-indicating viscometer or V-G meter, an
instrument used to measure viscosity and gel strength of drilling mud.
Muffle Furnace: Use for combustion of raw dry bamboo leaf
2.3. Methodology
2.3.1 Preparation of BLA
Bamboo leaf was sun dried in open atmosphere for 2 to 3 days then the dry leaves were grinded and converted to
powder. This powder is placed in a muffle furnace at 800°C for two hours to obtain BLA. After that the ash is passed through
a sieve with mesh size 120 micron. Larger particles which were left out on the top were removed and the remaining was
collected from the bottom.
2.3.2 Procedure to remove BLA impurities.
The sample which is heated in the furnace at a temperature of 800°C, is later subjected to acid washing. We use 100ml of
dilute Hydrochloric Acid (HCL) for this purpose. This mixture is heated at 70°C in hot air oven and left to open air for 30
minutes. The residue obtained is treated with an alkali to neutralize the acidic contaminants for which we use 100ml of
sodium hydroxide (NaOH) after which it is heated to 70°C and left to open air. The product obtained by the chemical
reaction is Na2SiO3, which is then washed with distilled water for about 4-5 times. To collect the filtrate, HCL is added drop
wise till a precipitate is formed. This precipitate can be collected and heated to 90-100°C for 4 hours. The precipitate
obtained after 4 hours is free from all kinds of impurities.
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2.3.3 Preparation of samples
For this experiment we prepare twelve samples using Hamilton Brach mixer following the American Petroleum Institute
(API) standards to investigate the properties of the fluids. The composition of each sample has been mentioned in Table 1.
2.3.4 Rheological test
Fann VG meter was used to determine Apparent viscosity (AV), Plastic Viscosity (PV), Yield Point (YP) and Gel strength
of the all samples. All dial readings were taken at 300 and 600 rpm. Similarly, to determine filtration loss and filter-cake
thickness, API LPLT filter press was used. To determine Lubricity coefficient and Differential sticking coefficient we used EP
Lubricity coefficient tester and Differential Sticking Tester.
Table 1 Composition of different samples
Bentonite g/L 30 30 30 30 30 30 30 30 30 30 30 30
Water mL 1000 1000 1000 1000 1000 1000 1000 1000 1000 1000 1000 1000
Barite g/L 10 10 10 10 10 10 10 10 10 10 10 10
CMC g/L -- 8 -- -- -- 8 -- -- -- 8 -- --
Xanthan
gum
g/L -- -- 8 -- -- -- 8 -- -- -- 8 --
Bamboo
leaf Ash
g/L -- -- -- 8 -- -- -- 8 -- -- -- 8
KCl g/L 5 5 5 5 5 5 5 5 5 5 5 5
NaOH g/L 7 7 7 7 7 7 7 7 7 7 7 7
CaCO3 g/L 8 8 8 8 8 8 8 8 8 8 8 8
Mica g/L -- -- -- -- 5 5 5 5 5 5 5 5
Lube oil mL -- -- -- -- -- -- -- -- 8 8 8 8
Figure 1 : Muffle Furnace Figure 2 : BLA
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3. RESULTS AND DISCUSSION
3.1 Fann VG meter results
The rheological test was performed using FANN VG meter on sample 1, 2, 3 & 4. Dial reading for each sample at 600
and 300 RPM were taken and using equation (A), (B) and (C) PV, YP and AV were determined.
PV= θ600 -θ300……………………………………………………………….…(A)
YP= θ300 –PV …………………………………………………………………(B)
AV= θ600/2 ..………………………………………………………………….(C)
Comparison of the values are shown in the Fig 3, 4 and 5. Being a mud thickener, XG and CMC both show enhanced PV
and AV value, but when we added BLA it was found that the obtained PV and AV values are in the mid-range of the values
we get from both XG and CMC. It means that BLA can be used as a mud thickener because these results are comparable to
XG and CMC added aqueous drilling mud (i.e., For PV 8-15 cP & for AV 25-37.5 cP). It was observed that YP values of the
drilling fluid was increasing when we added XG and CMC. The YP values of BLA added drilling fluid were also obtained. It
is seen that YP value of BLA added drilling fluid is comparable with the samples with XG and CMC. We know that YP is very
important to lift the drill cuttings back to the surface. Hence from our study it is evident that cutting carrying capacity is
increasing with the addition of BLA (Fig.5). This also reduces the annular frictional pressure drop. The YP obtained for the
sample with BLA is 27 lb./100 sq.ft. In their work Bourgoyne et al., 1991, recommended that sample with YP value range
3–30 lb/100 ft2 is most suitable for carry cuttings to the surface. In such cases frictional pressure drops in the annulus is
also less. Therefore, YP values of the BLA added drilling fluid has the ability to lift the cuttings. According to Chilingarian et
al., 1986, YP/PV ratio is the major factor to check whether the mud is stable or not. If the YP/AV ratio is less than the mud,
it is considered to be stabilized. Whereas if the ratio is more than the mud, it is considered to be flocculated. Among all
four samples (1, 2, 3 & 4), the YP/PV ratio is the least for the sample 4, i.e. the drilling mud with BLA as an additive. This
indicates that the mud is stable. It has been observed from the Fig. 4 that the gel strength of the mud samples increased as
we are increasing the amount of XG and CMC in it. This suggests that the mud is getting thicker. The 10 sec strength of the
polymer added mud was found to be in the range of 22 to 38 lb./100 ft2 (Table 2), and 10-min gel strength ranged from 24
to 20 lb./100 ft2 (Table 2). It was also observed that the mud with BLA also has a significant initial and final gel strength.
This gel strength value is almost comparable with the gel strength values of XG and CMC. Increasing trend in final gel
strength is also observed in this case.
3.2 API Filter Press results
API filtration loss test was performed to measure the filtration loss and the mud cake thickness of the drilling fluid. The
results obtained are shown in the Table 3. From the Fig. 6 and Fig. 7 and from the results it is distinct that fluid loss
decreased with the addition of polymers such as XG and CMC. The filtrate loss obtained after addition of XG and CMC were
24 & 27 mL respectively. Whereas after addition of BLA the obtained filtrate loss is 24 mL. Similarly, the mud cake
thickness of mud with BLA is also comparable with the mud cake obtained from XG and CMC added drilling fluid (Table 3).
Based on the filtration loss and cake thickness results, it was observed that BLA can be added in the drilling fluid system
and its filtration loss behavior is almost identical with XG and CMC.
3.3 EP Lubricity Tester results
Lubricity is one of the major properties of an aqueous drilling fluid. Lubricating property of drilling fluid reduce the
friction in the downhole equipment and, the wear and tear of drill string. In Lubricity coefficient test, 150 in-pounds of
force is applied between two hardened steel surfaces, a block, and a ring rotating at 60 RPM. Lubricity coefficient for
different samples (Sample 9, 10, 11 & 12) are shown in Table 4. It is observed that sample with BLS shows a comparable
result with mud with XG and CMC (Fig 8). In fact, compared to other samples we have better lubricating property of mud
when we add BLA in the drilling system. With this, it can be concluded that lubricating property of drilling fluid can be
enhanced by adding BLA.
3.4 Differential Sticking Tester
Differential sticking typically occurs in the downhole where there is higher pressure differential between wellbore and
the formation. In such cases drill string assembly gets stuck in the mud cake. The sticking force is a product of the Pressure
differential and the contact area. Table 5 shows the differential sticking coefficient of different samples. It is also observed
that among all four samples (Sample 9, 10, 11 & 12) mud sample with BLA has the least tendency to stick (Fig. 9). Hence, it
can be concluded that BLA can be solution for possible differential sticking problem in the downhole condition.
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4. CONCLUSION
From the study we can conclude that bamboo leaf ash has a significant effect on the properties of the drilling mud. The
following is the conclusion of our study:
a) Based on the study it can be concluded that addition of BLA in drilling fluid has a significant effect in the PV and
AV.
b) The cutting transport properties of the drilling fluid also enhances upon addition of BLA in the drilling fluid
c) Gel strength property is enhanced, especially as there is improvement in the final gel strength over initial gel
strength, which is an indication of mud stabilization.
d) There is a significant reduction in the filtration loss for the mud having BLA as an additive. The results are almost
comparable with XG and CMC.
e) Lubricating property of the drilling fluid is enhanced with the addition of BLA in the drilling fluid system.
f) Sticking tendency is also reduced for the drilling fluid with BLA as an additive
g) After careful observation of all the properties it can be concluded that BLA can be used in Drilling fluid as a mud
thickener to improve rheological and filtration loss properties of drilling fluid.
5. AUTHOR AFFILIATION
With the help of this paper we are trying to find a solution for one of the biggest problems faced in the oil industry, i.e. the
lack of an eco-friendly water-based drilling fluid. In this paper we have introduced a new water-based drilling fluid with
the help of a natural additive in form of bamboo leaf ash with which we have also solved the economic part of drilling fluid
additive. We think this water-based drilling mud can be very widely used in the drilling process because of its economical,
efficiency and eco-friendly advantage over other drilling fluids which are currently used.
6. ACKNOWLEDGEMENT
We would like to thank Mr. Bhairab Jyoti Gogoi, Assistant Professor, Department of Petroleum Engineering, Presidency
University, Bangalore, for his constant guidance and motivation, we also thank him for providing tremendous resource
and references about the current Scenario in oil and gas field.
We are also grateful to all the faculty and staff of Petroleum Engineering Department for their valuable insights.
NOMENCLATURE:
AV: Apparent viscosity (cP)
PV: Plastic viscosity (cP)
YP: Yield point (lb./100ft2)
θ: Bob dial reading
XG: Xanthan Gum
CMC: Carboxy Methyl Cellulose, cP: centipoise
Table 2. Values obtained from Fann VG meter
SAMPLE PV (cP)
YP (lb./100
sq. ft.)
AV
(cP)
Initial Gel
Strength
(lb./100
sq.
ft.)
Final
Gel
Strength
(lb./100
sq. ft.)
YP/PV
ration
pH
Sample 1 6.00 3.00 7.50 3.00 1.00 0.50 7.40
Sample 2 8.00 34.00 25.00 22.00 24.00 4.25 8.65
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Sample 3 15.00 45.00 37.50 38.00 40.00 4.25 8.44
Sample 4 13.00 27.00 26.50 33.00 35.00 3.89 8.00
Table 3. Values obtained from API Filter Press
API Filter Press
SAMPLE Mud Filtrate (mL) Mud Cake thickness (1/32")
Sample 5 50 2
Sample 6 27 4
Sample 7 24 5
Sample 8 24 4
Table 4. Values obtained from EP Lubricity Tester
EP Lubricity tester
SAMPLE
Average
Reading
Correction
factor
Meter
Reading
Lubricity
Coefficient
Sample 9 22 1.55 21 0.32
Sample 10 24 1.42 28 0.40
Sample 11 27 1.26 33 0.42
Sample 12 29 1.17 37 0.43
Table 5. Values obtained from Differential Sticking Test apparatus
Differential Sticking Tester
SAMPLE
Torque
reading
Sticking
Coefficient
Sample 9 150 0.1500
Sample 10 141 0.1410
Sample 11 137 0.1370
Sample 12 126 0.1260
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GRAPHS:
Chart 1: Comparison of PV and AV
Chart 2: Comparison of YP
6.00
8.00
15.00
13.00
7.50
25.00
37.50
26.50
0.00
5.00
10.00
15.00
20.00
25.00
30.00
35.00
40.00
SAMPLE 1 SAMPLE 2 SAMPLE 3 SAMPLE 4
SAMPLES
COMPARISON OF PV AND AV
PV (cP) AV (cP)
3.00
34.00
45.00
27.00
0.00
10.00
20.00
30.00
40.00
50.00
0 0.5 1 1.5 2 2.5 3 3.5 4 4.5
Samples
COMPERISON OF YP
YP (lb/100 sq ft)
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Chart 3: Comparison of Gel Strength
Chart 4: Comparison of Mud Filtrate loss
Initial Gel Strength (lb/100 sq ft.)
Final Gel Strength (lb/100 sq ft.)
0.00
10.00
20.00
30.00
40.00
Sample
1
Sample
2
Sample
3
Sample
4
3.00
22.00
38.00
33.00
1.00
24.00
40.00
35.00
Samples
COMPARISON OF GEL STRENGTH
Initial Gel Strength (lb/100 sq ft.) Final Gel Strength (lb/100 sq ft.)
0 10 20 30 40 50
Mud Filtrate (mL)
50
27
24
24
Mud Filtrate Loss (mL)
COMPARISON OF MUD FILTRATE
LOSS
Sample 8
Sample 7
Sample 6
Sample 5
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Chart 5: Comparison of Mud cake thickness
Chart 6: Comparison of Lubricity coefficient
0 1 2 3 4 5
2
4
5
4
Mud cake thickness (1/32")
COMPARISON OF MUD CAKE
THICKNESS
Sample 8
Sample 7
Sample 6
Sample 5
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Chart 7: Comparison of Sticking coefficient
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0.15
0.141
0.137
0.126
0.11
0.115
0.12
0.125
0.13
0.135
0.14
0.145
0.15
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COMPARISON OF STICKING
COEFFICIENT
Sticking Coefficient
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[23] Dick, M. A., Heinz, T. J., Svoboda, C. F., and Aston, M. (2000). Optimizing the selection of bridging particles for
reservoir drilling fluids, SPE-58793, SPE International Symposium on Formation Damage Control, Lafayette,
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[24] Fastest growing plant, Guinness World Records. Archived from the original on 3 September 2014. Retrieved
22 August 2014.
[25] G. Iscan & M. V. Kok (2007) Effects of Polymers and CMC Concentration on Rheological and Fluid Loss
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[26] Gerogiorgis, D.I., Reilly, S., Vryzas, Z., Kelessidis, V.C., 2017. Experimentally validated firstprinciples
multivariate modelling for rheological study and design of complex drilling nanofluid systems. In: SPE/IADC
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[27] Oliveira, M. O., Neto, J. M., Inocencio, M. C., Ando Junior, O. H., Bretas, A. S. and Perrone, O. E. (2012). Viability
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[28] OlutogeF.A., Oladunmoye O.M., 2017, Bamboo Leaf Ash as Supplementary Cementitious Material, American
Journal of Engineering Research (AJER) e-ISSN: 2320-0847 p-ISSN : 2320-0936 Volume-6, Issue-6, pp-01-08
[29] Richard O. Afolabi⁎, Oyinkepreye D. Orodu, Ifeanyi Seteyeobot - Predictive modelling of the impact of silica
nanoparticles on fluid loss of water based drilling mud. Department of Petroleum Engineering, Covenant
University, P.M.B 1023, Ota, Ogun State, Nigeria.
[30] Salih, A.H., Elshehabi, T.A., Bilgesu, H.I., 2016. Impact of nanomaterials on the rheological and filtration
properties of water based drilling fluids. In: SPE Eastern Regional Meeting. Society of Petroleum Engineers,
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[31] Villar-Cociña, E., Morales, E. V., Santos, S. F., Savastano, H., & Frías, M. (2011). Pozzolanic behavior of bamboo
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33(1), 68–73. doi:10.1016/j.cemconcomp.2010.09.003
[32] Yili Kang a, Jiping She a, *, Hao Zhang b, Lijun You a, Minggu Song a - Strengthening shale wellbore with silica
nanoparticles drilling fluid.

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IRJET - Use of Bamboo Leaf Ash as an Additive to Aqueous Drilling Fluid and Study the Variation of Rheological and Filtration Loss Properties

  • 1. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 07 Issue: 04 | Apr 2020 www.irjet.net p-ISSN: 2395-0072 © 2020, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 2023 Use of Bamboo Leaf Ash as an Additive to Aqueous Drilling Fluid and Study the Variation of Rheological and Filtration Loss PropertieS. Gautham V Nairy1, Mohammed Farhan Jameel2, Mariam Susan Matthew3, Anushka U N4 Bhairab Jyoti Gogoi5 1Student & Dept. Petroleum Engineering, Presidency University, Bengaluru, India 2Student & Dept. Petroleum Engineering, Presidency University, Bengaluru, India 3Student & Dept. Petroleum Engineering, Presidency University, Bengaluru, India 4Student & Dept. Petroleum Engineering, Presidency University, Bengaluru, India 5Assistant Professor, Dept. Petroleum Engineering, Presidency University, Bengaluru, India ---------------------------------------------------------------------***--------------------------------------------------------------------- Abstract - Requisition of efficient use of imprudent by-products for the enhancement of drilling fluid is preferentially beneficial for a hassle-free and relentless drilling process. Intricately designed drilling fluids have been used in the petroleum industry having significant properties to meet many operational requirements. The conventional methods are proven to be efficient in the current scenario, but they have limited capability and may not be suitable for future drilling operations due to the increasing challenges in the petroleum industry. A need exists for a strong, stable and customizable fluid which can not only satisfy the basic functions of a drilling mud, but also make productive use of waste products for its enhancement. This paper deals with the possibility of using Bamboo Leaf Ash (BLA) as an additive in Water Based Drilling Fluid (WBDF). The main components of BLA include silica (SiO2), aluminum (Al2O3) and iron oxide (Fe2O3). The yield percentage of silica from bamboo leaf ash is 78%. In our study we have attempted to use BLA as an additive to WBDF comparative analysis of the rheological properties of drilling fluids with different percentage of BLA has been studied. Based on the comparative study it is observed that BLA can be used as an additive to WBDF. Key Words: Drilling Fluid, Rheological Properties, Bamboo leaf ash … 1. INTRODUCTION The exploration and exploitation of hydrocarbon on offshore and onshore environment suggest the use of environmentally friendly drilling mud and its additives thereby preventing any harm to the aquatic bodies and the terrestrial environment. Currently, various kinds of drilling fluid systems are used in the oil industry, among which the significant ones include, Polymer based drilling fluid system, oil-based drilling fluid system, etc. Nevertheless, most of them have some serious environmental concern, degradability issue and difficulty in the post-treatment, which bring the contradiction between clean drilling and requirements of drilling operation. Environmental regulations uplift the use of water-based drilling fluid and its application in areas where oil-based drilling fluids have previously been used due to their challenges [1]. Most of the efficient drilling fluids have high toxicity and this toxicity is limiting the use of such drilling fluids. In this scenario, the oil industry is in need of something known as eco-friendly drilling fluid, but to go with the idea of preparing the same, two things are to be considered, i.e., the efficiency of the drilling fluid and, the cost of the drilling fluid. In most of the cases we must compromise either one of these three: eco-friendly, economical, or efficiency, and in a few cases, two of them [2]. The various properties of the drilling mud are rheological properties, filtration loss properties, lubricating quality, pipe sticking tendency, thermal and bacterial inhibition, etc. Myriad additives are added for making the drilling mud most suitable for the different conditions for viscosity, mud weight, prevent mud loss, have enough gel strength and be reliable. A few additives such as calcium carbonate, starch and xanthan gum are common incorporated in the formulation of a drilling mud [3]. Xanthan Gum also used as a viscosifier which controls the rheology. Starch is a fluid loss control additive widely used in aqueous drilling fluids and has a thermal stability upto 250 °F [4]. Carboxymethyl Cellulose (CMC) is another polymer which tends to increase shear stress as its concentration in the mud increases and the fluid loss decreases. An optimum concentration is favorable in the drill mud [10]. The usage of Calcium Carbonate (CaCO3) provides an ionic inhibition and hence serves as a bridging agent [5][6][7][8][9][10]. Caustic Soda, which is also known as Sodium Hydroxide (NaOH), is used in water-based mud to have a check on the pH level and does affect the salinity of the drilling mud [11]. To increase the density and for shale inhibition, Potassium Chloride (KCl) is used [12]. Mica is another Loss Circulation material. Unlike cellopane material, Mica tends to avoid absorbing large amounts of free water or oil [12]. Lube oil used to have a check on the increased torque/drag, limited displacement, increased equipment stress [13]. To provide weight to the drilling fluid, the usage of an inert, high density Barite is employed [14]. The main purpose of using weighting materials is to increase its density and thereby ensuring the borehole stability [15]. It provides the required hydrostatic pressure in the hole and has a check on the fluid loss by the formation of mud cake of the inner walls on the well [16]. Bamboos belongs to the grass family Poaceae, a flowering plant in the subfamily Bambusoideae. Its growth rate is 910 mm per day [17]. Bamboo forests covers around 12.8% of the total forest area and is found in most of the states of
  • 2. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 07 Issue: 04 | Apr 2020 www.irjet.net p-ISSN: 2395-0072 © 2020, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 2024 India. More than 50 per cent of the bamboo species appears in North East India i.e. Arunachal Pradesh, Assam, Manipur, Meghalaya, Mizoram, Nagaland, Sikkim, and Tripura. Apart from these regions, there are significant traces of Bamboo leaf in the Andamans, Bastar region of Madhya Pradesh and the Western Ghats. Bamboo leaf is an agro-waste product. A typical composition of bamboo leaf ash is SiO2: 78%, Al2O3: 4.96% Fe2O3: 2.01% CaO: 4.43% MgO: 1.02% K2O: 3.09% P2O5: 0.72% TiO2: 0.36%, LOI: 1.58% [18]. Bamboo leaf ash has a lot of application in concrete industry. B Olutoge F.A. and Oladunmoye O.M. used bamboo leaf as a supplementary cementing material. Ernesto Villar-Cociña concluded that BLA is formed by amorphous silica. In this paper, we have come up with an idea in which our objectives are equally balanced. With this approach, we use a natural organic material with bentonite and prepare a new drilling fluid which is less toxic, economical, and environment friendly. We obtain it by processing the bamboo leaf in steps including drying, grinding, heating it in a muffle furnace, removing the impurities to obtain an end product which consists of mainly silica. Bamboo leaf ash has about 75.90% of SiO2 (Silicon Dioxide). The presence of silica provides high resistance to water penetration, thermal and fungal decomposition [19]. This property can hence help in its usage to prevent fluid loss of the drilling fluid. A comparative study between these additives is done to check for the rheological properties, filtration properties, lubricating quality, stuck pipe efficiency, thermal and bacterial inhibition, and the various rheological properties. 2. MATERIAL AND METHODOLOGY 2.1 Material used For the experiment we have used API Grade Bentonite, industry grade Barite (SG 4.2), Carboxy Methyl Cellulose (CMC, Sigma Aldrich), Xanthan Gum (XC, Sigma Aldrich), Calcium Carbonate-Fine (CaCO3, Karnataka Fine Chem.), Sodium Hydroxide (NaOH, Karnataka Fine Chem.), Potassium Chloride (KCl, Karnataka Fine Chem.), Lube Oil and Mica 2.2 Equipment used API LPLT filter press (Fann Instrument Company): It is the most effective means of determining the filtration properties of drilling muds and cement slurries. Lubricity tester (Fann Instrument Company): The Lubricity tester is a high-quality instrument used to measure the lubricating quality of drilling fluids. Differential sticking tester (Model 21150 Fann Instrument Company, Houston, Texas): The Differential Sticking Tester measures the “Stuck Pipe Tendency Coefficient” of drilling fluids, and determines how effective lubricants or treatments might be with any given drilling fluid. Fann VG meter (Fann Instrument Company): It is also known as direct-indicating viscometer or V-G meter, an instrument used to measure viscosity and gel strength of drilling mud. Muffle Furnace: Use for combustion of raw dry bamboo leaf 2.3. Methodology 2.3.1 Preparation of BLA Bamboo leaf was sun dried in open atmosphere for 2 to 3 days then the dry leaves were grinded and converted to powder. This powder is placed in a muffle furnace at 800°C for two hours to obtain BLA. After that the ash is passed through a sieve with mesh size 120 micron. Larger particles which were left out on the top were removed and the remaining was collected from the bottom. 2.3.2 Procedure to remove BLA impurities. The sample which is heated in the furnace at a temperature of 800°C, is later subjected to acid washing. We use 100ml of dilute Hydrochloric Acid (HCL) for this purpose. This mixture is heated at 70°C in hot air oven and left to open air for 30 minutes. The residue obtained is treated with an alkali to neutralize the acidic contaminants for which we use 100ml of sodium hydroxide (NaOH) after which it is heated to 70°C and left to open air. The product obtained by the chemical reaction is Na2SiO3, which is then washed with distilled water for about 4-5 times. To collect the filtrate, HCL is added drop wise till a precipitate is formed. This precipitate can be collected and heated to 90-100°C for 4 hours. The precipitate obtained after 4 hours is free from all kinds of impurities.
  • 3. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 07 Issue: 04 | Apr 2020 www.irjet.net p-ISSN: 2395-0072 © 2020, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 2025 2.3.3 Preparation of samples For this experiment we prepare twelve samples using Hamilton Brach mixer following the American Petroleum Institute (API) standards to investigate the properties of the fluids. The composition of each sample has been mentioned in Table 1. 2.3.4 Rheological test Fann VG meter was used to determine Apparent viscosity (AV), Plastic Viscosity (PV), Yield Point (YP) and Gel strength of the all samples. All dial readings were taken at 300 and 600 rpm. Similarly, to determine filtration loss and filter-cake thickness, API LPLT filter press was used. To determine Lubricity coefficient and Differential sticking coefficient we used EP Lubricity coefficient tester and Differential Sticking Tester. Table 1 Composition of different samples Bentonite g/L 30 30 30 30 30 30 30 30 30 30 30 30 Water mL 1000 1000 1000 1000 1000 1000 1000 1000 1000 1000 1000 1000 Barite g/L 10 10 10 10 10 10 10 10 10 10 10 10 CMC g/L -- 8 -- -- -- 8 -- -- -- 8 -- -- Xanthan gum g/L -- -- 8 -- -- -- 8 -- -- -- 8 -- Bamboo leaf Ash g/L -- -- -- 8 -- -- -- 8 -- -- -- 8 KCl g/L 5 5 5 5 5 5 5 5 5 5 5 5 NaOH g/L 7 7 7 7 7 7 7 7 7 7 7 7 CaCO3 g/L 8 8 8 8 8 8 8 8 8 8 8 8 Mica g/L -- -- -- -- 5 5 5 5 5 5 5 5 Lube oil mL -- -- -- -- -- -- -- -- 8 8 8 8 Figure 1 : Muffle Furnace Figure 2 : BLA
  • 4. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 07 Issue: 04 | Apr 2020 www.irjet.net p-ISSN: 2395-0072 © 2020, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 2026 3. RESULTS AND DISCUSSION 3.1 Fann VG meter results The rheological test was performed using FANN VG meter on sample 1, 2, 3 & 4. Dial reading for each sample at 600 and 300 RPM were taken and using equation (A), (B) and (C) PV, YP and AV were determined. PV= θ600 -θ300……………………………………………………………….…(A) YP= θ300 –PV …………………………………………………………………(B) AV= θ600/2 ..………………………………………………………………….(C) Comparison of the values are shown in the Fig 3, 4 and 5. Being a mud thickener, XG and CMC both show enhanced PV and AV value, but when we added BLA it was found that the obtained PV and AV values are in the mid-range of the values we get from both XG and CMC. It means that BLA can be used as a mud thickener because these results are comparable to XG and CMC added aqueous drilling mud (i.e., For PV 8-15 cP & for AV 25-37.5 cP). It was observed that YP values of the drilling fluid was increasing when we added XG and CMC. The YP values of BLA added drilling fluid were also obtained. It is seen that YP value of BLA added drilling fluid is comparable with the samples with XG and CMC. We know that YP is very important to lift the drill cuttings back to the surface. Hence from our study it is evident that cutting carrying capacity is increasing with the addition of BLA (Fig.5). This also reduces the annular frictional pressure drop. The YP obtained for the sample with BLA is 27 lb./100 sq.ft. In their work Bourgoyne et al., 1991, recommended that sample with YP value range 3–30 lb/100 ft2 is most suitable for carry cuttings to the surface. In such cases frictional pressure drops in the annulus is also less. Therefore, YP values of the BLA added drilling fluid has the ability to lift the cuttings. According to Chilingarian et al., 1986, YP/PV ratio is the major factor to check whether the mud is stable or not. If the YP/AV ratio is less than the mud, it is considered to be stabilized. Whereas if the ratio is more than the mud, it is considered to be flocculated. Among all four samples (1, 2, 3 & 4), the YP/PV ratio is the least for the sample 4, i.e. the drilling mud with BLA as an additive. This indicates that the mud is stable. It has been observed from the Fig. 4 that the gel strength of the mud samples increased as we are increasing the amount of XG and CMC in it. This suggests that the mud is getting thicker. The 10 sec strength of the polymer added mud was found to be in the range of 22 to 38 lb./100 ft2 (Table 2), and 10-min gel strength ranged from 24 to 20 lb./100 ft2 (Table 2). It was also observed that the mud with BLA also has a significant initial and final gel strength. This gel strength value is almost comparable with the gel strength values of XG and CMC. Increasing trend in final gel strength is also observed in this case. 3.2 API Filter Press results API filtration loss test was performed to measure the filtration loss and the mud cake thickness of the drilling fluid. The results obtained are shown in the Table 3. From the Fig. 6 and Fig. 7 and from the results it is distinct that fluid loss decreased with the addition of polymers such as XG and CMC. The filtrate loss obtained after addition of XG and CMC were 24 & 27 mL respectively. Whereas after addition of BLA the obtained filtrate loss is 24 mL. Similarly, the mud cake thickness of mud with BLA is also comparable with the mud cake obtained from XG and CMC added drilling fluid (Table 3). Based on the filtration loss and cake thickness results, it was observed that BLA can be added in the drilling fluid system and its filtration loss behavior is almost identical with XG and CMC. 3.3 EP Lubricity Tester results Lubricity is one of the major properties of an aqueous drilling fluid. Lubricating property of drilling fluid reduce the friction in the downhole equipment and, the wear and tear of drill string. In Lubricity coefficient test, 150 in-pounds of force is applied between two hardened steel surfaces, a block, and a ring rotating at 60 RPM. Lubricity coefficient for different samples (Sample 9, 10, 11 & 12) are shown in Table 4. It is observed that sample with BLS shows a comparable result with mud with XG and CMC (Fig 8). In fact, compared to other samples we have better lubricating property of mud when we add BLA in the drilling system. With this, it can be concluded that lubricating property of drilling fluid can be enhanced by adding BLA. 3.4 Differential Sticking Tester Differential sticking typically occurs in the downhole where there is higher pressure differential between wellbore and the formation. In such cases drill string assembly gets stuck in the mud cake. The sticking force is a product of the Pressure differential and the contact area. Table 5 shows the differential sticking coefficient of different samples. It is also observed that among all four samples (Sample 9, 10, 11 & 12) mud sample with BLA has the least tendency to stick (Fig. 9). Hence, it can be concluded that BLA can be solution for possible differential sticking problem in the downhole condition.
  • 5. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 07 Issue: 04 | Apr 2020 www.irjet.net p-ISSN: 2395-0072 © 2020, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 2027 4. CONCLUSION From the study we can conclude that bamboo leaf ash has a significant effect on the properties of the drilling mud. The following is the conclusion of our study: a) Based on the study it can be concluded that addition of BLA in drilling fluid has a significant effect in the PV and AV. b) The cutting transport properties of the drilling fluid also enhances upon addition of BLA in the drilling fluid c) Gel strength property is enhanced, especially as there is improvement in the final gel strength over initial gel strength, which is an indication of mud stabilization. d) There is a significant reduction in the filtration loss for the mud having BLA as an additive. The results are almost comparable with XG and CMC. e) Lubricating property of the drilling fluid is enhanced with the addition of BLA in the drilling fluid system. f) Sticking tendency is also reduced for the drilling fluid with BLA as an additive g) After careful observation of all the properties it can be concluded that BLA can be used in Drilling fluid as a mud thickener to improve rheological and filtration loss properties of drilling fluid. 5. AUTHOR AFFILIATION With the help of this paper we are trying to find a solution for one of the biggest problems faced in the oil industry, i.e. the lack of an eco-friendly water-based drilling fluid. In this paper we have introduced a new water-based drilling fluid with the help of a natural additive in form of bamboo leaf ash with which we have also solved the economic part of drilling fluid additive. We think this water-based drilling mud can be very widely used in the drilling process because of its economical, efficiency and eco-friendly advantage over other drilling fluids which are currently used. 6. ACKNOWLEDGEMENT We would like to thank Mr. Bhairab Jyoti Gogoi, Assistant Professor, Department of Petroleum Engineering, Presidency University, Bangalore, for his constant guidance and motivation, we also thank him for providing tremendous resource and references about the current Scenario in oil and gas field. We are also grateful to all the faculty and staff of Petroleum Engineering Department for their valuable insights. NOMENCLATURE: AV: Apparent viscosity (cP) PV: Plastic viscosity (cP) YP: Yield point (lb./100ft2) θ: Bob dial reading XG: Xanthan Gum CMC: Carboxy Methyl Cellulose, cP: centipoise Table 2. Values obtained from Fann VG meter SAMPLE PV (cP) YP (lb./100 sq. ft.) AV (cP) Initial Gel Strength (lb./100 sq. ft.) Final Gel Strength (lb./100 sq. ft.) YP/PV ration pH Sample 1 6.00 3.00 7.50 3.00 1.00 0.50 7.40 Sample 2 8.00 34.00 25.00 22.00 24.00 4.25 8.65
  • 6. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 07 Issue: 04 | Apr 2020 www.irjet.net p-ISSN: 2395-0072 © 2020, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 2028 Sample 3 15.00 45.00 37.50 38.00 40.00 4.25 8.44 Sample 4 13.00 27.00 26.50 33.00 35.00 3.89 8.00 Table 3. Values obtained from API Filter Press API Filter Press SAMPLE Mud Filtrate (mL) Mud Cake thickness (1/32") Sample 5 50 2 Sample 6 27 4 Sample 7 24 5 Sample 8 24 4 Table 4. Values obtained from EP Lubricity Tester EP Lubricity tester SAMPLE Average Reading Correction factor Meter Reading Lubricity Coefficient Sample 9 22 1.55 21 0.32 Sample 10 24 1.42 28 0.40 Sample 11 27 1.26 33 0.42 Sample 12 29 1.17 37 0.43 Table 5. Values obtained from Differential Sticking Test apparatus Differential Sticking Tester SAMPLE Torque reading Sticking Coefficient Sample 9 150 0.1500 Sample 10 141 0.1410 Sample 11 137 0.1370 Sample 12 126 0.1260
  • 7. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 07 Issue: 04 | Apr 2020 www.irjet.net p-ISSN: 2395-0072 © 2020, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 2029 GRAPHS: Chart 1: Comparison of PV and AV Chart 2: Comparison of YP 6.00 8.00 15.00 13.00 7.50 25.00 37.50 26.50 0.00 5.00 10.00 15.00 20.00 25.00 30.00 35.00 40.00 SAMPLE 1 SAMPLE 2 SAMPLE 3 SAMPLE 4 SAMPLES COMPARISON OF PV AND AV PV (cP) AV (cP) 3.00 34.00 45.00 27.00 0.00 10.00 20.00 30.00 40.00 50.00 0 0.5 1 1.5 2 2.5 3 3.5 4 4.5 Samples COMPERISON OF YP YP (lb/100 sq ft)
  • 8. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 07 Issue: 04 | Apr 2020 www.irjet.net p-ISSN: 2395-0072 © 2020, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 2030 Chart 3: Comparison of Gel Strength Chart 4: Comparison of Mud Filtrate loss Initial Gel Strength (lb/100 sq ft.) Final Gel Strength (lb/100 sq ft.) 0.00 10.00 20.00 30.00 40.00 Sample 1 Sample 2 Sample 3 Sample 4 3.00 22.00 38.00 33.00 1.00 24.00 40.00 35.00 Samples COMPARISON OF GEL STRENGTH Initial Gel Strength (lb/100 sq ft.) Final Gel Strength (lb/100 sq ft.) 0 10 20 30 40 50 Mud Filtrate (mL) 50 27 24 24 Mud Filtrate Loss (mL) COMPARISON OF MUD FILTRATE LOSS Sample 8 Sample 7 Sample 6 Sample 5
  • 9. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 07 Issue: 04 | Apr 2020 www.irjet.net p-ISSN: 2395-0072 © 2020, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 2031 Chart 5: Comparison of Mud cake thickness Chart 6: Comparison of Lubricity coefficient 0 1 2 3 4 5 2 4 5 4 Mud cake thickness (1/32") COMPARISON OF MUD CAKE THICKNESS Sample 8 Sample 7 Sample 6 Sample 5
  • 10. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 07 Issue: 04 | Apr 2020 www.irjet.net p-ISSN: 2395-0072 © 2020, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 2032 Chart 7: Comparison of Sticking coefficient REFERENCE [1] Tehrani, A., Gerrard, D., Young, S., & Fernandez, J. (2009). Environmentally friendly water-based fluid for HPHT drilling. In SPE International Symposium on Oilfield Chemistry (pp. 1–8). Texas: Society of Petroleum Engineers. [2] H.C.H. Darley, W. F. Rogers, "Composition and Properties of Oil Well Drilling Fluids" 4th Edition,Gulf Publishing Co., Houston, Texas, U.S.A.,1980 [3] V. Mahto, P. Srikanth & B. Vamsi Krishna (2013) Development of Non-damaging and Inhibitive Water Based Oil Well Drilling Fluids, Petroleum Science and Technology, 31:7, 721-726 [4] Talukdar, Prasenjit & Kalita, Sudarshana & Pandey, Amarjit & Dutta, Upasana & Singh, Rituraj. (2018). Effectiveness of different Starches as Drilling Fluid Additives in Non Damaging Drilling Fluid. International Journal of Applied Engineering Research. 13. 12469-12474. [5] Zitha, P. L. J. (1997). Water control by bridging colloids. SPE 38198, European Formation Damage Conference, The Hague, the Netherlands. [6] Abdo, J., Danish-Haneef, M., 2012. Nano-enhanced drilling fluids: pioneering approach to overcome uncompromising drilling problems. J. Energy Resour. Technol. 134, 1–6. [7] Hanssen, J. E., and Jiang, P. (1999). Recent advances in evaluation of formation damage and its use in designing reservoir drilling fluids for maximizing well productivity. Paper 065/08, Offshore Mediterranean Conference, Ravenna, Italy, March 24–26 [8] Abdou, M. I., Al-Sabagh, A. M., Ahmed, H. E.-S., & Fadl, A. M. (2018). Impact of barite and ilmenite mixture on enhancing the drilling mud weight. Egyptian Journal of Petroleum. doi:10.1016/j.ejpe.2018.02.004 [9] Simonides, H., Schuringa, G., and Ghalambor, A. (2002). Role of starch in designing nondamaging completion and drilling fluids. SPE 73768, SPE International Symposium and Exhibition on Formation Damage Control, Lafayette, Lousiana, February 20–21. [10] Patel, A., Young, S., and Friedheim, J. (2007). Advances in inhibitive water based drilling fluids— Can they replace oil based muds? SPE 106476, SPE International Symposium on Oilfield Chemistry, Houston, Texas, February 28 to March 2. [11] Saleh, Kamal Mohammed and Ahmed Mahmoud. “The effect of using different weights of caustic sodaon the water-base mud drilling fluid.” (2013). [12] Werner, Benjamin & Lund, Bjørnar & Myrseth, Velaug & Saasen, Arild & Gyland, Knud. (2016). Comparison of Rheological Properties of Oil-Based and KCl Drilling Fluids. 10.2118/180063-MS. Baker Hughes Company. 1999. Prevention and Control of Lost Circulation Best Practices. [13] Growcock, Frederick & Frederick, T. & Reece, A. & Green, G. & Ruffin, M.. (1999). Novel Lubricants for Water- Based Drilling Fluids. 10.2118/50710-MS. 0.15 0.141 0.137 0.126 0.11 0.115 0.12 0.125 0.13 0.135 0.14 0.145 0.15 0.155 Sample 9 Sample 10 Sample 11 Sample 12 Samples COMPARISON OF STICKING COEFFICIENT Sticking Coefficient
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