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International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 07 Issue: 03 | Mar 2020 www.irjet.net p-ISSN: 2395-0072
© 2020, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 4899
Evaluation of Wheat Husk as Environment Friendly Fluid Loss Additive
as a Substitute of CMC(LVG) in Water based Drilling Fluid up to 100 oC.
Althamas Yaseer1.a, Mubarak Khan1.a, Shaik Abdul Mugni1.a,Malavika Reddy Kummetha1.a, Ved
Prakash1.b, Munmun Bhattacharya1.b
1.aDepartment of the Petroleum Engineering, Presidency University, Bangalore, India
1.bDepartment of the Drilling Fluid Engineering, Institute of Drilling Technology, ONGC, Dehradun,
Uttrakhand, India
----------------------------------------------------------------------***---------------------------------------------------------------------
Abstract - Filtration control is an important property of a
drilling fluid particularly while drilling through the
permeable formations. This property of a drilling mud is
obtained or enhanced using various additives. Currently
organic polymers are commonly used as additives to
control filtrate loss in water based drilling mud and exhibits
negative impacts on the environment when released, Hence
there is a tremendous need for new environmental friendly,
biodegradable additives which can help in controlling
filtration loss with least effect on environment and also on
worker's health. this study involves the introduction of
environmental friendly food waste product i.e. "wheat husk
powder" (WHP) as a filtration loss additive. The effects of
various concentration of WHP on physical and chemical
properties of a mud such as mud weight, pH, PV, AV, YP, gel
strength, filtration loss (API), BHR and AHR rheological
properties were evaluated and all the results were
compared with the properties of the reference mud
prepared with the conventionally used filtration loss
additive CMC(LVG) in order to asses and validate the
effectiveness of WHP in optimizing the performance of
drilling mud. The results obtained showed that WHP was
behaving as a filtration loss reducer and the drilling mud
prepared with WHP was thermally stable at up to 100 0C.
Hence WHP is successful replacement of CMC(LVG) in aspect
of cost effectiveness, filtration loss reduction, environmental
friendly and thermal stability.
Key Words: WHP - wheat husk powder ,Filtration loss,
Mud cake, CMC(LVG) - carboxy methyl cellulose (Low
Viscous Grade), Water based mud, Natural additive.
1. INTRODUCTION
Drilling fluids are the most important parameter in the
drilling operations[1].The main function of the drilling
fluid is to provide sufficient density to counter balance the
formation pressure and seal the permeable formation by
forming a filter cake[2-3]. Among the various functions of
the drilling mud the most desired application is the
minimum fluid loss volume by forming a low-permeable
mud cake across the wall of the borehole [4]. Drilling fluid
with excessive filtration loss may influence the property of
the well such as wellbore stability, differential sticking,
core recovery process, loss in mud volume and formation
damage [5]. Hence an efficient drilling fluid is one which
minimizes the filtrate loss in the formation by forming a
thin filter cake with low permeability [6]. In the
formulation of conventional water based mud additives
such as carboxy methyl cellulose, starch, poly anionic
cellulose, acryl amide polymers are widely used as
filtration control agents [7]. carboxy methyl cellulose is
probably the most common and is used routinely both to
control fluid loss and to increase the viscosity of the
drilling fluid[8]. Various chemicals that are used in
formulation of drilling fluid to enhance its properties have
an adverse effect on the environment. These concerns
have made the oil industry to shift towards the use of safer
and eco-friendly additives in drilling mud [9].
In recent years various studies have been performed to
develop an eco-friendly additive for drilling mud. Natural
products such as rice husk was used to control fluid
loss[10], iheagwara 2005, Adebowale and raji 2015 used
banana peels as replacement to NaoH to control pH of the
mud[11]. In order To enhance the rheology and the
filtration loss property of drilling mud cellulose from
corncob[nmeghu 2014],waste grass[al hameedi 2019],
cashew and mango leaves extract[omotioma], potato peel
powder [al hameedi] were used.
In this study we have implemented the use of waste food
product i.e. wheat husk powder to enhance the filtration
loss property of the drilling fluid. Wheat husk is a by-
product of milling and is used in the preparation of some
food products [15]. Recent studies have shown that India
alone generates 21million tones of wheat waste ever
year.[16].
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 07 Issue: 03 | Mar 2020 www.irjet.net p-ISSN: 2395-0072
© 2020, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 4900
1.1 Properties of wheat husk:
Table 1: Physical and Chemical properties of WHP
Color Light brown
Odor Odorless
Physical state Amorphous
Moisture Content 4.6
Organic % 87%
2. Materials and Methods:
2.1. Sample preparation:
wheat husk hot air oven grinding sieveing
Figure 1: Flowchart representing sample preparation
The WHP sample was a collected and processed product
from wheat fields; the sample was then kept in a hot
vacuum oven at 100oC to remove all the moisture content
present. Later it was crushed down into fine particles with
a grinding machine for duration of 20minutes. The
crushed sample was then sieved to 125 microns to obtain
fine particles of that size (As it completely gets dispersed
with the additives added) . The complete procedure is
illustrated in the form of a flow chart as shown in Fig 1.
2.2. Experimental procedure:
The effect of WHP was studied by preparing 9 samples of
mud (each of 500 ml) categorized as set A, set B, set C. set
A is considered as reference mud with the composition
500ml of water, 0.3% XC-polymer and 0.1% soda ash. Set
B comprises of four muds with 1,2,3,4 percent of
CMC(LVG) along with 500ml of water(dispersion
medium), 0.3% XC-polymer (viscosifier) and 0.1% soda
ash(to reduce salt content in water) and in Set C 1,2,3,4
wt% of wheat husk powder was added by replacing
CMC(LVG) while maintaining the same aforementioned
composition. For the preparation of mud samples the
following equipments were used
 Electronic Precision balance to
measure the mass of different
chemicals for proper composition.
 1000ml measuring cylinder to
measure the volume of the water.
Hamilton Beach Mixer for proper stirring/mixing of water
and additives in order to generate desired homogeneous
mixture of drilling mud. The prepared mud sample was
evaluated for rheological parameters followed by filtration
loss and mud cake thickness measurements. The pH of the
sample was tested and the mud sample was kept in hot
roller oven for a period of 16 hours at 100oC to obtain
dynamic fluid properties. The drill mud's physical and
chemical parameters were observed before and after hot
roll condition.
2.3. Laboratory measurement procedure:
2.3.1Rheological Properties:
In the R&D perspective rotational viscometer provides
accurate results of the characteristics of a drilling mud
compared to marsh funnel. Hence a rotation viscometer
was used for measurements. Mud samples (Set A,B,C)
were poured into the viscometer cup up to the mark and
was placed on a stand and was lifted up, to immerse the
rotating sleeve of the viscometer. A steady dial reading
was noted at different RPM, (600, 300, 200, 100, 6, 3) to
determine plastic viscosity, apparent viscosity, yield point,
which are considered as fundamental rheological
properties. Gel strength determination is an extension of
mud rheological property (10), The gel strength at 10
second and 10 min was determined at 3 rpm. the obtained
results are represented in Table 2,3,4,5,6.
Formulae: to determine rheological properties
AV
PV
YP= PV
2.3.2 Filtration properties:
The API standard LP-LT test was carried out to determine filtration loss of the prepared sample at room temperature and
700 kPa (100 psi). Mud was contained in a cell fitted with a Whatman 50 filter paper with a diameter 90mm at bottom
along with a filter screen. After the necessary connections a 100 Psi pressure was exerted on drilling mud using Nitrogen
gas for a period of 30 min. filtrate was collected below using measuring cylinder and readings were noted along with the
mud cake thickness deposited on the bottom . The same procedure was repeated with different concentrations.
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 07 Issue: 03 | Mar 2020 www.irjet.net p-ISSN: 2395-0072
© 2020, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 4901
3. RESULTS AND DISCUSSIONS:
The following section includes all the comparisons made between the reference mud(Set A) and the 2 category of mud
samples composed of CMC(LVG) and WHP. The basis of comparison included the readings of PV,YP,YP, Gel strength and
filtration properties. Moreover filtration property comparison stands out to be the core of this paper as it is directly
related to mud cake thickness (MCT). The more thin and impermeable the mud cake is, the best drilling mud it tends out to
be. The study includes
Table 2: Rheological properties of reference mud
Parameters BHR AHR
AV 11 14
PV 5 7
YP 12 13
Gel0 7 10
Gel10 8 9
API 30 35
PH 10.4 10.3
Table 3: Rheological properties of CMC(LVG) mud (BHR)
Parameters Concentration
1% 2% 3% 4%
AV 17.5 29.5 55 62
PV 10 19 40 44
YP 15 21 30 36
Gel0 5 6 6 7
Gel10 7 6 7 8
API
Mud cake thickness(mm)
17
1.1
12
1.2
10
1.4
9
1.7
Table 4: Rheological properties of CMC(LVG) mud (AHR)
Parameters Concentration
1% 2% 3% 4%
AV 15 27.5 54 60
PV 9 20 39 45
YP 12 15 30 35
Gel0 4 7 8 9
Gel10 5 8 9 10
API 18.5 16 13 12.5
PH
Mud cake
thickness
(mm)
9.8
1.5
9.9
1.6
9.9
1.8
9.9
2.4
Table 5: Rheological properties of WHP mud (BHR)
Parameters Concentration
1% 2% 3% 4%
AV 12.5 21 27.5 32.5
PV 7 11 15 20
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 07 Issue: 03 | Mar 2020 www.irjet.net p-ISSN: 2395-0072
© 2020, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 4902
YP 11 20 25 30
Gel0 5 7 10 12
Gel10 6 9 11 13
API 16 8 7.4 6
PH 9.7 9.7 9.8 9.7
Mud cake
thickness
(mm)
1.8 2.0 2.1 2.5
Table 6: Rheological properties of WHP mud (AHR)
Parameters Concentration
1% 2% 3% 4%
AV 17 22.5 27.5 32.5
PV 11 14 18 19
YP 12 17 19 24
Gel0 6 8 12 14
Gel10 7 9 10 15
API 18 8.4 8 6.5
PH 9.7 9.7 9.8 9.7
Mud cake
thickness (mm)
1.6 1.7 1.9 2.6
3.1Effect on Filtration properties:
The comparison made is based on the concentration (1-
4% CMC(LVG) and WHP) in mud. From Table 3,4,5&6
and Fig 1, 2 it is clear that 3-4% of WHP works best as a
filtration loss agent as compared to 3-4% CMC(LVG). The
filter loss volume obtained from the reference mud was
35ml, this when compared with 1-4% CMC(LVG) AHR
filter loss volume the percentages obtained are 47.14%,
54.28%, 62.85% and 64.28% respectively. Whereas WHP
Filter loss volumes obtained with WHP samples were
better than that of CMC(LVG), as 1-4% of AHR WHP
showed 48.571%, 76%, 77.14% and 81.42% reduction in
filter loss. (Note: All were compared with respect to
reference mud)
Figure 2: Filtrate Volume of CMC(LVG) & WHP mud BHR
Figure 3:Filtrate Volume of CMC(LVG) & WHP mud AHR.
3.2 Effect on Rheological properties:
Reference mud had very less gel strength, PV, AV and YP.
Whereas drilling fluids with WHP had significant effect on
the rheological properties especially at 3% and 4% were
the corresponding Gel0 and Gel10 values were 10, 12 and
11, 13 respectively as shown in Table 5. Later the same
sample showed a slight increase in their gel0 and gel10
values that is 12,14 and 10,15 respectively after hot roll
conditions. In most of the drilling operations CMC(LVG) is
used as the viscosifier and loss reducing agent and from
the study the optimum concentration of CMC(LVG) ranges
from 3-4% with gel0, gel10 values of 6,7 and 7,8
respectively in BHR conditions and whereas in AHR it was
8,9 and 9,10 respectively as shown in Table 3,4. Though
gel strength is high for WHP, the filtration loss volume was
significantly less. PV, YP and AV showed a steep increase
17
12
10
9
16
8
7.4
6
1 2 3 4
0
2
4
6
8
10
12
14
16
18
Fluid-lossVolume(ml)
Additive Content (%)
CMC
WHP
18.5
16
13 12.5
18
8.4 8
6.5
1 2 3 4
0
2
4
6
8
10
12
14
16
18
20
Fluid-lossVolume(ml)
Additive Content (%)
CMC
WHP
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 07 Issue: 03 | Mar 2020 www.irjet.net p-ISSN: 2395-0072
© 2020, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 4903
in their values but most significant increase was found
after AHR as shown in figure 4.
Figure 4: Rheological parameters of CMC(LVG) mud AHR
Figure 5: Rheological parameters of WHP mud AHR
3.3 Effect on Mud cake thickness:
A desired mud cake is one which is thin and has low
permeability. A thick mud cake is also efficient sometimes
as it may restrict fluid penetration on other hand it may
cause other drilling problems such as stuck pipe and
excessive torque and drag ( Ottesen et al 1999). From the
results obtained we can observe that the mud cake
thickness of mud sample with WHP ranges between 1.6-
2.6 mm. while sample of CMC(LVG) showed thickness in
the range of 1.5-2.4 mm. The results can be seen from
figure 5.
Figure 6: Mud cake thickness (CMC(LVG) Vs WHP)
4. CONCLUSION:
Fluid loss control is the parameter of drill mud and is
dependent on type and quantity of the solids added and
also the temperature and pressure, thus the WHP can be
evaluated as a filter loss additive in water referenced
drilling fluid. The following observations are made from
obtained results
 The WHP mud show that there has been a
filtration loss reduction of about 48.571%, 76%,
77.14% and 81.42% with concentration of 1%,
2%, 3%,4% respectively, however the following
reduction in filtration loss of CMC(LVG) mud with
respect to reference mud was 47.14%, 54.28%,
62.85% and 64.28% with concentration 1%, 2%,
3%,4% respectively.
 Mud cake thickness of the CMC(LVG) and WHP
was nearly identical with negligible effect on mud
weight.
 The alkalinity of both the mud's had a change and
was decreasing with increase in concentrations.
 It was observed that WHP and CMC(LVG) have
similar temperature stability up to. 100oC.
Since the wheat husk powder is providing the similar
properties to that of CMC(LVG) in a cost effective manner.
Hence it can be concluded that 3-4% of WHP is a better
substitute of CMC(LVG).
5. ACKNOWLEDGEMENT:
Authors wishes to acknowledge IDT ONGC Dehradun for
giving us the opportunity to utilize their laboratories for
carrying out the experiments, We would also like to
express our sincere gratitude to Dr. Suman Paul Head of
the Department, Petroleum Engineering, (Presidency
1.0 1.5 2.0 2.5 3.0 3.5 4.0
0
10
20
30
40
50
60
RheologicalParameters(%)
Concenteration
AV
PV
PV
Gel0
Gel10
1.0 1.5 2.0 2.5 3.0 3.5 4.0
5
10
15
20
25
30
35
RheologicalParameters(%)
Concenteration
AV
PV
YP
Gel0
Gel10
1.1
1.2
1.4
1.7
1.8
2
2.1
2.5
1.5
1.6
1.8
2.4
1.6
1.7
1.9
2.6
1% 2% 3% 4% -- 1% 2% 3% 4%
0.0
0.5
1.0
1.5
2.0
2.5
3.0
MCT(mm)
Additive Content (%)
MCT BHR
MCT AHR
CMC WHP
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 07 Issue: 03 | Mar 2020 www.irjet.net p-ISSN: 2395-0072
© 2020, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 4904
University, Bangalore) for his constant guidance and
support throughout our work. At the end we thank
Presidency University for providing us the opportunity to
carry out our project in ONGC IDT Dehradun.
6. ABBREVITATIONS:
AV Apparent viscosity
PV Plastic viscosity
YP
GEL0
GEL10
Yield point
Gel strength at 10
sec
Gel strength at 10
sec
WHP Wheat husk powder
CMC(LVG) Carboxy methyl
cellulose (Low
Viscous Grade)
MCT Mud cake thickness
AHR After hot roll
BHR Before hot roll
Ml Mille Liter
Mm Mille meter
AV Apparent viscosity
PV Plastic viscosity
7. REFERENCES:
1: Coussat P, Bertrand F, Herzhaft B(2004) Rheological
Behavour of drilling fluids characterization using MRI
visualization par IRM du comportement. Oil Gas Sci
technoi 59:23-29.
2. Luo, z; pei, j; Wang L; Yu,P; Influence of an ionic liquid
on rheological and filteration properties of water
referenced drilling fluid at high temperatures. Appl. Clay
Sci.136,96-102(2017).
3. Zhang, L.-M.; Tan,Y.-B.; Li,Z.-M.: Application of new
family of amphoteric cellulose-referenced graft
copolymers as drilling mud additives. Colloid Polym. Sci.
277,1001-1004(1999).
4. Curti, E., Carini, E., Bonacini, G., Tribuzio, G. & Vittadini,
E. (2013). Effect of the addition of bran fractions on bread
properties. Journal of Cereal Science, 57, 325– 332.
5. Aston, M., Mihalik, P., Tunbridge, J. and Clarke, S. (2002).
Towards zero Fluid loss oil Referenced Mud. Society of
Petroleum Engineers. SPE Paper 77446.
6. Onyla, E. C. 1994. An analysis of experimental data on
lost circulation problems while drilling with oil-referenced
muds. SPEDrilling and Completion, March, pp.25–31
7. Coates JA, Farrar JM, Graham MH. Fluid loss-reducing
additives for oil-referenced well working fluids. US patent
4 941 983; 1990. URL:
http://www.freepatentsonline.com/ 4941983.html.
8. T. T.L. Hughes, T.G. and O.H/ Houwen, Chemical
Characterization Of CMC(LVG) and its Relationship to
Drilling Mud Rheology and Fluid Loss, Schlumberger
Cambridge Research.
9. Abo Taleb T. Al-Hameedi, Husam H. Alkinani, Shari
Dunn-Norman, Environmental Friendly Drilling Fluid
Additives: Can Food Waste Products be Used as Thinners
and Fluid Loss Control Agents for Drilling Fluid? SPE
Sympossium, Malaysia April 2019
10. Anietie N. Okon, Feancis D. Udoh, and Perpetua G.
Bassey, Evaluation of Rice Husk as fluod loss additive in
Water Referenced Drilling Fluid, Society of Petroleum
Engineeers Paper-172379-MS
11. Iheagwara, O. "Comparative Analysis of the Use of
Banana Peels and NaOH in Ph Control in Nigerian Clays"
Journal of the Nigerian Association of Mathematical
Physics, 2015. Vol 30.
12. Adebowale, A., and Raji, J. "Local Content Supplements
as an Alternative to Imported Corrosion Control Additives
for Drilling Mud Treatment (A Case Study of the Use of
Burnt Plantain and Banana Peels". Proceedings of the
International Academic Conference for Sub-Sahara African
Transformation and Development 2015. Vol. 3.
13. Nmegbu, J., and Bekee, B. A. "Evaluation of Corn Cob
Cellulose and its Suitability for Drilling mud Formulation".
Journal of Engineering Research and Applications 2014.
Vol. 4, pp.112–117.
14. Abo Taleb T. Al-Hameedi, Husam H. Alkinani, Shari
Dunn-Norman, Insights into the application of new eco-
friendly drilling fluid additive to improve the fluid
properties in water referenced drilling fluid system,
Journal of Petroleum Science and Engineering 183 (2019)
106424
15. Curti, E., Carini, E., Bonacini, G., Tribuzio, G (2013).
Effect of the Addition of bran Fractions on Bread
properties. Journal of Cereal Science, 57, 325-332
16. Report by Institute of Mechanical Engineers (IME) on
Global Food Wastage 2013.

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IRJET - Evaluation of Wheat Husk as Environment Friendly Fluid Loss Additive as a Substitute of CMC(LVG) in Water based Drilling Fluid up to 100 Oc

  • 1. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 07 Issue: 03 | Mar 2020 www.irjet.net p-ISSN: 2395-0072 © 2020, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 4899 Evaluation of Wheat Husk as Environment Friendly Fluid Loss Additive as a Substitute of CMC(LVG) in Water based Drilling Fluid up to 100 oC. Althamas Yaseer1.a, Mubarak Khan1.a, Shaik Abdul Mugni1.a,Malavika Reddy Kummetha1.a, Ved Prakash1.b, Munmun Bhattacharya1.b 1.aDepartment of the Petroleum Engineering, Presidency University, Bangalore, India 1.bDepartment of the Drilling Fluid Engineering, Institute of Drilling Technology, ONGC, Dehradun, Uttrakhand, India ----------------------------------------------------------------------***--------------------------------------------------------------------- Abstract - Filtration control is an important property of a drilling fluid particularly while drilling through the permeable formations. This property of a drilling mud is obtained or enhanced using various additives. Currently organic polymers are commonly used as additives to control filtrate loss in water based drilling mud and exhibits negative impacts on the environment when released, Hence there is a tremendous need for new environmental friendly, biodegradable additives which can help in controlling filtration loss with least effect on environment and also on worker's health. this study involves the introduction of environmental friendly food waste product i.e. "wheat husk powder" (WHP) as a filtration loss additive. The effects of various concentration of WHP on physical and chemical properties of a mud such as mud weight, pH, PV, AV, YP, gel strength, filtration loss (API), BHR and AHR rheological properties were evaluated and all the results were compared with the properties of the reference mud prepared with the conventionally used filtration loss additive CMC(LVG) in order to asses and validate the effectiveness of WHP in optimizing the performance of drilling mud. The results obtained showed that WHP was behaving as a filtration loss reducer and the drilling mud prepared with WHP was thermally stable at up to 100 0C. Hence WHP is successful replacement of CMC(LVG) in aspect of cost effectiveness, filtration loss reduction, environmental friendly and thermal stability. Key Words: WHP - wheat husk powder ,Filtration loss, Mud cake, CMC(LVG) - carboxy methyl cellulose (Low Viscous Grade), Water based mud, Natural additive. 1. INTRODUCTION Drilling fluids are the most important parameter in the drilling operations[1].The main function of the drilling fluid is to provide sufficient density to counter balance the formation pressure and seal the permeable formation by forming a filter cake[2-3]. Among the various functions of the drilling mud the most desired application is the minimum fluid loss volume by forming a low-permeable mud cake across the wall of the borehole [4]. Drilling fluid with excessive filtration loss may influence the property of the well such as wellbore stability, differential sticking, core recovery process, loss in mud volume and formation damage [5]. Hence an efficient drilling fluid is one which minimizes the filtrate loss in the formation by forming a thin filter cake with low permeability [6]. In the formulation of conventional water based mud additives such as carboxy methyl cellulose, starch, poly anionic cellulose, acryl amide polymers are widely used as filtration control agents [7]. carboxy methyl cellulose is probably the most common and is used routinely both to control fluid loss and to increase the viscosity of the drilling fluid[8]. Various chemicals that are used in formulation of drilling fluid to enhance its properties have an adverse effect on the environment. These concerns have made the oil industry to shift towards the use of safer and eco-friendly additives in drilling mud [9]. In recent years various studies have been performed to develop an eco-friendly additive for drilling mud. Natural products such as rice husk was used to control fluid loss[10], iheagwara 2005, Adebowale and raji 2015 used banana peels as replacement to NaoH to control pH of the mud[11]. In order To enhance the rheology and the filtration loss property of drilling mud cellulose from corncob[nmeghu 2014],waste grass[al hameedi 2019], cashew and mango leaves extract[omotioma], potato peel powder [al hameedi] were used. In this study we have implemented the use of waste food product i.e. wheat husk powder to enhance the filtration loss property of the drilling fluid. Wheat husk is a by- product of milling and is used in the preparation of some food products [15]. Recent studies have shown that India alone generates 21million tones of wheat waste ever year.[16].
  • 2. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 07 Issue: 03 | Mar 2020 www.irjet.net p-ISSN: 2395-0072 © 2020, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 4900 1.1 Properties of wheat husk: Table 1: Physical and Chemical properties of WHP Color Light brown Odor Odorless Physical state Amorphous Moisture Content 4.6 Organic % 87% 2. Materials and Methods: 2.1. Sample preparation: wheat husk hot air oven grinding sieveing Figure 1: Flowchart representing sample preparation The WHP sample was a collected and processed product from wheat fields; the sample was then kept in a hot vacuum oven at 100oC to remove all the moisture content present. Later it was crushed down into fine particles with a grinding machine for duration of 20minutes. The crushed sample was then sieved to 125 microns to obtain fine particles of that size (As it completely gets dispersed with the additives added) . The complete procedure is illustrated in the form of a flow chart as shown in Fig 1. 2.2. Experimental procedure: The effect of WHP was studied by preparing 9 samples of mud (each of 500 ml) categorized as set A, set B, set C. set A is considered as reference mud with the composition 500ml of water, 0.3% XC-polymer and 0.1% soda ash. Set B comprises of four muds with 1,2,3,4 percent of CMC(LVG) along with 500ml of water(dispersion medium), 0.3% XC-polymer (viscosifier) and 0.1% soda ash(to reduce salt content in water) and in Set C 1,2,3,4 wt% of wheat husk powder was added by replacing CMC(LVG) while maintaining the same aforementioned composition. For the preparation of mud samples the following equipments were used  Electronic Precision balance to measure the mass of different chemicals for proper composition.  1000ml measuring cylinder to measure the volume of the water. Hamilton Beach Mixer for proper stirring/mixing of water and additives in order to generate desired homogeneous mixture of drilling mud. The prepared mud sample was evaluated for rheological parameters followed by filtration loss and mud cake thickness measurements. The pH of the sample was tested and the mud sample was kept in hot roller oven for a period of 16 hours at 100oC to obtain dynamic fluid properties. The drill mud's physical and chemical parameters were observed before and after hot roll condition. 2.3. Laboratory measurement procedure: 2.3.1Rheological Properties: In the R&D perspective rotational viscometer provides accurate results of the characteristics of a drilling mud compared to marsh funnel. Hence a rotation viscometer was used for measurements. Mud samples (Set A,B,C) were poured into the viscometer cup up to the mark and was placed on a stand and was lifted up, to immerse the rotating sleeve of the viscometer. A steady dial reading was noted at different RPM, (600, 300, 200, 100, 6, 3) to determine plastic viscosity, apparent viscosity, yield point, which are considered as fundamental rheological properties. Gel strength determination is an extension of mud rheological property (10), The gel strength at 10 second and 10 min was determined at 3 rpm. the obtained results are represented in Table 2,3,4,5,6. Formulae: to determine rheological properties AV PV YP= PV 2.3.2 Filtration properties: The API standard LP-LT test was carried out to determine filtration loss of the prepared sample at room temperature and 700 kPa (100 psi). Mud was contained in a cell fitted with a Whatman 50 filter paper with a diameter 90mm at bottom along with a filter screen. After the necessary connections a 100 Psi pressure was exerted on drilling mud using Nitrogen gas for a period of 30 min. filtrate was collected below using measuring cylinder and readings were noted along with the mud cake thickness deposited on the bottom . The same procedure was repeated with different concentrations.
  • 3. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 07 Issue: 03 | Mar 2020 www.irjet.net p-ISSN: 2395-0072 © 2020, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 4901 3. RESULTS AND DISCUSSIONS: The following section includes all the comparisons made between the reference mud(Set A) and the 2 category of mud samples composed of CMC(LVG) and WHP. The basis of comparison included the readings of PV,YP,YP, Gel strength and filtration properties. Moreover filtration property comparison stands out to be the core of this paper as it is directly related to mud cake thickness (MCT). The more thin and impermeable the mud cake is, the best drilling mud it tends out to be. The study includes Table 2: Rheological properties of reference mud Parameters BHR AHR AV 11 14 PV 5 7 YP 12 13 Gel0 7 10 Gel10 8 9 API 30 35 PH 10.4 10.3 Table 3: Rheological properties of CMC(LVG) mud (BHR) Parameters Concentration 1% 2% 3% 4% AV 17.5 29.5 55 62 PV 10 19 40 44 YP 15 21 30 36 Gel0 5 6 6 7 Gel10 7 6 7 8 API Mud cake thickness(mm) 17 1.1 12 1.2 10 1.4 9 1.7 Table 4: Rheological properties of CMC(LVG) mud (AHR) Parameters Concentration 1% 2% 3% 4% AV 15 27.5 54 60 PV 9 20 39 45 YP 12 15 30 35 Gel0 4 7 8 9 Gel10 5 8 9 10 API 18.5 16 13 12.5 PH Mud cake thickness (mm) 9.8 1.5 9.9 1.6 9.9 1.8 9.9 2.4 Table 5: Rheological properties of WHP mud (BHR) Parameters Concentration 1% 2% 3% 4% AV 12.5 21 27.5 32.5 PV 7 11 15 20
  • 4. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 07 Issue: 03 | Mar 2020 www.irjet.net p-ISSN: 2395-0072 © 2020, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 4902 YP 11 20 25 30 Gel0 5 7 10 12 Gel10 6 9 11 13 API 16 8 7.4 6 PH 9.7 9.7 9.8 9.7 Mud cake thickness (mm) 1.8 2.0 2.1 2.5 Table 6: Rheological properties of WHP mud (AHR) Parameters Concentration 1% 2% 3% 4% AV 17 22.5 27.5 32.5 PV 11 14 18 19 YP 12 17 19 24 Gel0 6 8 12 14 Gel10 7 9 10 15 API 18 8.4 8 6.5 PH 9.7 9.7 9.8 9.7 Mud cake thickness (mm) 1.6 1.7 1.9 2.6 3.1Effect on Filtration properties: The comparison made is based on the concentration (1- 4% CMC(LVG) and WHP) in mud. From Table 3,4,5&6 and Fig 1, 2 it is clear that 3-4% of WHP works best as a filtration loss agent as compared to 3-4% CMC(LVG). The filter loss volume obtained from the reference mud was 35ml, this when compared with 1-4% CMC(LVG) AHR filter loss volume the percentages obtained are 47.14%, 54.28%, 62.85% and 64.28% respectively. Whereas WHP Filter loss volumes obtained with WHP samples were better than that of CMC(LVG), as 1-4% of AHR WHP showed 48.571%, 76%, 77.14% and 81.42% reduction in filter loss. (Note: All were compared with respect to reference mud) Figure 2: Filtrate Volume of CMC(LVG) & WHP mud BHR Figure 3:Filtrate Volume of CMC(LVG) & WHP mud AHR. 3.2 Effect on Rheological properties: Reference mud had very less gel strength, PV, AV and YP. Whereas drilling fluids with WHP had significant effect on the rheological properties especially at 3% and 4% were the corresponding Gel0 and Gel10 values were 10, 12 and 11, 13 respectively as shown in Table 5. Later the same sample showed a slight increase in their gel0 and gel10 values that is 12,14 and 10,15 respectively after hot roll conditions. In most of the drilling operations CMC(LVG) is used as the viscosifier and loss reducing agent and from the study the optimum concentration of CMC(LVG) ranges from 3-4% with gel0, gel10 values of 6,7 and 7,8 respectively in BHR conditions and whereas in AHR it was 8,9 and 9,10 respectively as shown in Table 3,4. Though gel strength is high for WHP, the filtration loss volume was significantly less. PV, YP and AV showed a steep increase 17 12 10 9 16 8 7.4 6 1 2 3 4 0 2 4 6 8 10 12 14 16 18 Fluid-lossVolume(ml) Additive Content (%) CMC WHP 18.5 16 13 12.5 18 8.4 8 6.5 1 2 3 4 0 2 4 6 8 10 12 14 16 18 20 Fluid-lossVolume(ml) Additive Content (%) CMC WHP
  • 5. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 07 Issue: 03 | Mar 2020 www.irjet.net p-ISSN: 2395-0072 © 2020, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 4903 in their values but most significant increase was found after AHR as shown in figure 4. Figure 4: Rheological parameters of CMC(LVG) mud AHR Figure 5: Rheological parameters of WHP mud AHR 3.3 Effect on Mud cake thickness: A desired mud cake is one which is thin and has low permeability. A thick mud cake is also efficient sometimes as it may restrict fluid penetration on other hand it may cause other drilling problems such as stuck pipe and excessive torque and drag ( Ottesen et al 1999). From the results obtained we can observe that the mud cake thickness of mud sample with WHP ranges between 1.6- 2.6 mm. while sample of CMC(LVG) showed thickness in the range of 1.5-2.4 mm. The results can be seen from figure 5. Figure 6: Mud cake thickness (CMC(LVG) Vs WHP) 4. CONCLUSION: Fluid loss control is the parameter of drill mud and is dependent on type and quantity of the solids added and also the temperature and pressure, thus the WHP can be evaluated as a filter loss additive in water referenced drilling fluid. The following observations are made from obtained results  The WHP mud show that there has been a filtration loss reduction of about 48.571%, 76%, 77.14% and 81.42% with concentration of 1%, 2%, 3%,4% respectively, however the following reduction in filtration loss of CMC(LVG) mud with respect to reference mud was 47.14%, 54.28%, 62.85% and 64.28% with concentration 1%, 2%, 3%,4% respectively.  Mud cake thickness of the CMC(LVG) and WHP was nearly identical with negligible effect on mud weight.  The alkalinity of both the mud's had a change and was decreasing with increase in concentrations.  It was observed that WHP and CMC(LVG) have similar temperature stability up to. 100oC. Since the wheat husk powder is providing the similar properties to that of CMC(LVG) in a cost effective manner. Hence it can be concluded that 3-4% of WHP is a better substitute of CMC(LVG). 5. ACKNOWLEDGEMENT: Authors wishes to acknowledge IDT ONGC Dehradun for giving us the opportunity to utilize their laboratories for carrying out the experiments, We would also like to express our sincere gratitude to Dr. Suman Paul Head of the Department, Petroleum Engineering, (Presidency 1.0 1.5 2.0 2.5 3.0 3.5 4.0 0 10 20 30 40 50 60 RheologicalParameters(%) Concenteration AV PV PV Gel0 Gel10 1.0 1.5 2.0 2.5 3.0 3.5 4.0 5 10 15 20 25 30 35 RheologicalParameters(%) Concenteration AV PV YP Gel0 Gel10 1.1 1.2 1.4 1.7 1.8 2 2.1 2.5 1.5 1.6 1.8 2.4 1.6 1.7 1.9 2.6 1% 2% 3% 4% -- 1% 2% 3% 4% 0.0 0.5 1.0 1.5 2.0 2.5 3.0 MCT(mm) Additive Content (%) MCT BHR MCT AHR CMC WHP
  • 6. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 07 Issue: 03 | Mar 2020 www.irjet.net p-ISSN: 2395-0072 © 2020, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 4904 University, Bangalore) for his constant guidance and support throughout our work. At the end we thank Presidency University for providing us the opportunity to carry out our project in ONGC IDT Dehradun. 6. ABBREVITATIONS: AV Apparent viscosity PV Plastic viscosity YP GEL0 GEL10 Yield point Gel strength at 10 sec Gel strength at 10 sec WHP Wheat husk powder CMC(LVG) Carboxy methyl cellulose (Low Viscous Grade) MCT Mud cake thickness AHR After hot roll BHR Before hot roll Ml Mille Liter Mm Mille meter AV Apparent viscosity PV Plastic viscosity 7. REFERENCES: 1: Coussat P, Bertrand F, Herzhaft B(2004) Rheological Behavour of drilling fluids characterization using MRI visualization par IRM du comportement. Oil Gas Sci technoi 59:23-29. 2. Luo, z; pei, j; Wang L; Yu,P; Influence of an ionic liquid on rheological and filteration properties of water referenced drilling fluid at high temperatures. Appl. Clay Sci.136,96-102(2017). 3. Zhang, L.-M.; Tan,Y.-B.; Li,Z.-M.: Application of new family of amphoteric cellulose-referenced graft copolymers as drilling mud additives. Colloid Polym. Sci. 277,1001-1004(1999). 4. Curti, E., Carini, E., Bonacini, G., Tribuzio, G. & Vittadini, E. (2013). Effect of the addition of bran fractions on bread properties. Journal of Cereal Science, 57, 325– 332. 5. Aston, M., Mihalik, P., Tunbridge, J. and Clarke, S. (2002). Towards zero Fluid loss oil Referenced Mud. Society of Petroleum Engineers. SPE Paper 77446. 6. Onyla, E. C. 1994. An analysis of experimental data on lost circulation problems while drilling with oil-referenced muds. SPEDrilling and Completion, March, pp.25–31 7. Coates JA, Farrar JM, Graham MH. Fluid loss-reducing additives for oil-referenced well working fluids. US patent 4 941 983; 1990. URL: http://www.freepatentsonline.com/ 4941983.html. 8. T. T.L. Hughes, T.G. and O.H/ Houwen, Chemical Characterization Of CMC(LVG) and its Relationship to Drilling Mud Rheology and Fluid Loss, Schlumberger Cambridge Research. 9. Abo Taleb T. Al-Hameedi, Husam H. Alkinani, Shari Dunn-Norman, Environmental Friendly Drilling Fluid Additives: Can Food Waste Products be Used as Thinners and Fluid Loss Control Agents for Drilling Fluid? SPE Sympossium, Malaysia April 2019 10. Anietie N. Okon, Feancis D. Udoh, and Perpetua G. Bassey, Evaluation of Rice Husk as fluod loss additive in Water Referenced Drilling Fluid, Society of Petroleum Engineeers Paper-172379-MS 11. Iheagwara, O. "Comparative Analysis of the Use of Banana Peels and NaOH in Ph Control in Nigerian Clays" Journal of the Nigerian Association of Mathematical Physics, 2015. Vol 30. 12. Adebowale, A., and Raji, J. "Local Content Supplements as an Alternative to Imported Corrosion Control Additives for Drilling Mud Treatment (A Case Study of the Use of Burnt Plantain and Banana Peels". Proceedings of the International Academic Conference for Sub-Sahara African Transformation and Development 2015. Vol. 3. 13. Nmegbu, J., and Bekee, B. A. "Evaluation of Corn Cob Cellulose and its Suitability for Drilling mud Formulation". Journal of Engineering Research and Applications 2014. Vol. 4, pp.112–117. 14. Abo Taleb T. Al-Hameedi, Husam H. Alkinani, Shari Dunn-Norman, Insights into the application of new eco- friendly drilling fluid additive to improve the fluid properties in water referenced drilling fluid system, Journal of Petroleum Science and Engineering 183 (2019) 106424 15. Curti, E., Carini, E., Bonacini, G., Tribuzio, G (2013). Effect of the Addition of bran Fractions on Bread properties. Journal of Cereal Science, 57, 325-332 16. Report by Institute of Mechanical Engineers (IME) on Global Food Wastage 2013.