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Chemically Modification of Lignin Biopolymer andChemically Modification of Lignin Biopolymer and
its Industrially Application as a Hydrocarbonits Industrially Application as a Hydrocarbon
Drilling Well AdditiveDrilling Well Additive
Mohamed-Rashid Ahmed Mohamed Haras
Associate Professor. Dr. Mohamad Nasir Mohamad Ibrahim
Associate Professor. Dr. Coswald Stephen Sipaut @ Mohd Nasri
 In the course of drilling an oil or gas
well by means of rotary drilling
tools, a so called ( Drilling mud ) is
circulated downwardly through the
hollow drill stem and bit to the
bottom of borehole and then
upwardly to the surface through the
annular space between the drill stem
and the interior of the borehole.
 The most common mud used in the
drilling process is Bentonite due to;
its mixed friendly with water and
allow mud additives to perform
efficiently. Beyond that, it is cheap.
During the drilling process, drilling
mud is applied to the borehole
through the drill pipe and back to the
surface in order to achieve specific
functional :
 Cool and lubricate the bit and drill
string.
 Clean the bottom of the hole
beneath the bit
 Transport cuttings to the surface.
 Suspend drill cuttings in the annulus
when circulation is stopped.
 Drop off the cuttings at the surface.
 Support the walls of the borehole.
 Control subsurface pressure.
 Stabilize the borehole.
The main chemical
functional groups in
Kraft lignin are the
hydroxyl, methoxyl,
carbonyl groups (El
Mansouri & Salvadó,
2007).
Such functional
groups could open
newer possibilities
to expand the
chemically
modification process
of lignin. This will
enhance its
applicability in many
industrial aspects.
Preparation of Lignin Graft
Copolymer
Preparation of Lignin Graft
Copolymer
The water-basedThe water-based
drilling muds withdrilling muds with
viscosity-buildingviscosity-building
and suspension-and suspension-
carrying abilitiescarrying abilities
for oilfieldfor oilfield
applications requireapplications require
thermally stablethermally stable
water-solublewater-soluble
polymers to controlpolymers to control
the rheologicalthe rheological
property of drillingproperty of drilling
mudsmuds
DSC thermogram for the Lignin
No melting
temperature Tm
or
crystallization
temperature Tc
has been
recorded
DSC thermogram for Lignin Graft Copolymer
High Tg vlue:
The bulkiness and the
reticulation of the phenolic
groups in the lignin
structure.
Low Tg value:
Hydrocarbon chain without bulky
groups that gives PAA molecules
enough space to move with more
flexibility.
KL has a rough
surface with
shapeless configure
and the granular
structure can be
observed (Bonini,
D'Auria, Ferri,
Pucciariello &
Sabia, 2003).
Continues
wavy
surface
Pores that
could
facilitate
the
penetration
and enhance
the
solubility
- Two values of temperatures were chosen in order
to confirm whether the performance of LGC is
consistent both at room and high temperature.
- The results obtained are used to highlights the
importance of using the correct dosage of
treatment for optimization performance of
gelling agent and viscosifier as well as to save
unnecessary cost.
- Table 1 shown the optimum dosage of LGC is
0.5 % which gave moderate viscosity, gel
strength and yield point as well as sufficient pH
value compared to others at both temperatures.
- In addition, the use of excessive or insufficient
dosage may also bring out negative impact to
the mud properties.
Types of Mud T AV PV YP GS pH
Brae-Based Mud 27 28 12 16.35 23 11.91
Base Mud + 0.3% LGC 27 32.50 11 21.97 75 10.49
Base Mud + 0.5% LGC 27 40.00 14 26.57 73 9.63
Base Mud + 0.7% LGC 27 45.00 15 30.66 67 7.45
Bare-Based Mud 90 30.50 15 15.84 31 11.82
Base Mud + 0.3% LGC 90 41.50 11 31.71 95 10.15
Base Mud + 0.5% LGC 90 40.50 11 30.14 76 9.20
Base Mud + 0.7% LGC 90 43.00 11 32.70 60 7.22
 As a drilling mud takes place downwardly
the drilling mud temperature tends to
increase rapidly due to friction and this
increase influences the mud rheological
properties negatively.
 The negative effect includes sever decrease
of drilling mud viscosity and yield point
and that makes most of drilling mud
additives not functional at high
temperature.
 In this regard, a polymeric drilling mud
additive with a higher yield point exhibits
higher gel strength, which imparts a
desirable structural property to the drilling
mud (Gray & Darley, 1980).
Types of mud
AV PV YP
Before After Before After Before After
Base mud + 0.5% LGC 38 58.5 13 37 25.55 21.97
Base mud + 0.5 % CMC 97.5 25 19 18 61.8 7.154
Base mud + 0.5 % Guar Gum 105 23.5 35 18 71.5 5.621
Base mud + 0.5 % Xanthane 82.5 21 64 16 28.10 5.11
 There are times when circulation has to
be stopped, the drilling mud must have
that gelling characteristics ( gel strength)
that will prevent drill cuttings from
settling down at the bit.
 With proper thermally stable gel strength
can help suspend cuttings in the hole and
allow them to settle out on the surface.
 A mud pH range between 9 and 10.5 is
almost always desired in drilling
operations. This range suppresses the
corrosion rate of drilling equipment
especially drill pipe and bit.
Types of mud
GS pH
Before After Before After
Base mud + 0.5% LGC 73 74 9.65 9.25
Base mud + 0.5 % CMC 96 14 11.62 9.30
Base mud + 0.5 % Guar Gum 79 7 11.53 8.73
Base mud + 0.5 % Xanthane 67 4 11.62 8.64
 LGC has been successfully synthesized by exploiting the
waste of palm oil industry in the polymeric field.
 From an experimental point of view, the use of 0.5 % LGC as
drilling mud additives is not required any additional additives
like thermal stabilizer (alkyl metal chromate and starch) or pH
controlling agent ( soda ash and acetic acid), thereby it may
reduced the cost of drilling operation and minimize the
environmental damage.
 LGC exhibited good compatibility with commercial drilling
mud additives in terms of ; viscosity building, gelling abilities,
pH controlling and thermal degradation resistance.
thank YOU
FOR YOUR
kInD
attentIOn

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Drilling fluid technology, Oil & Gas Industry

  • 1. Chemically Modification of Lignin Biopolymer andChemically Modification of Lignin Biopolymer and its Industrially Application as a Hydrocarbonits Industrially Application as a Hydrocarbon Drilling Well AdditiveDrilling Well Additive Mohamed-Rashid Ahmed Mohamed Haras Associate Professor. Dr. Mohamad Nasir Mohamad Ibrahim Associate Professor. Dr. Coswald Stephen Sipaut @ Mohd Nasri
  • 2.  In the course of drilling an oil or gas well by means of rotary drilling tools, a so called ( Drilling mud ) is circulated downwardly through the hollow drill stem and bit to the bottom of borehole and then upwardly to the surface through the annular space between the drill stem and the interior of the borehole.  The most common mud used in the drilling process is Bentonite due to; its mixed friendly with water and allow mud additives to perform efficiently. Beyond that, it is cheap.
  • 3. During the drilling process, drilling mud is applied to the borehole through the drill pipe and back to the surface in order to achieve specific functional :  Cool and lubricate the bit and drill string.  Clean the bottom of the hole beneath the bit  Transport cuttings to the surface.  Suspend drill cuttings in the annulus when circulation is stopped.  Drop off the cuttings at the surface.  Support the walls of the borehole.  Control subsurface pressure.  Stabilize the borehole.
  • 4.
  • 5. The main chemical functional groups in Kraft lignin are the hydroxyl, methoxyl, carbonyl groups (El Mansouri & Salvadó, 2007). Such functional groups could open newer possibilities to expand the chemically modification process of lignin. This will enhance its applicability in many industrial aspects.
  • 6. Preparation of Lignin Graft Copolymer Preparation of Lignin Graft Copolymer
  • 7. The water-basedThe water-based drilling muds withdrilling muds with viscosity-buildingviscosity-building and suspension-and suspension- carrying abilitiescarrying abilities for oilfieldfor oilfield applications requireapplications require thermally stablethermally stable water-solublewater-soluble polymers to controlpolymers to control the rheologicalthe rheological property of drillingproperty of drilling mudsmuds
  • 8. DSC thermogram for the Lignin No melting temperature Tm or crystallization temperature Tc has been recorded
  • 9. DSC thermogram for Lignin Graft Copolymer High Tg vlue: The bulkiness and the reticulation of the phenolic groups in the lignin structure. Low Tg value: Hydrocarbon chain without bulky groups that gives PAA molecules enough space to move with more flexibility.
  • 10. KL has a rough surface with shapeless configure and the granular structure can be observed (Bonini, D'Auria, Ferri, Pucciariello & Sabia, 2003).
  • 12.
  • 13. - Two values of temperatures were chosen in order to confirm whether the performance of LGC is consistent both at room and high temperature. - The results obtained are used to highlights the importance of using the correct dosage of treatment for optimization performance of gelling agent and viscosifier as well as to save unnecessary cost. - Table 1 shown the optimum dosage of LGC is 0.5 % which gave moderate viscosity, gel strength and yield point as well as sufficient pH value compared to others at both temperatures. - In addition, the use of excessive or insufficient dosage may also bring out negative impact to the mud properties.
  • 14. Types of Mud T AV PV YP GS pH Brae-Based Mud 27 28 12 16.35 23 11.91 Base Mud + 0.3% LGC 27 32.50 11 21.97 75 10.49 Base Mud + 0.5% LGC 27 40.00 14 26.57 73 9.63 Base Mud + 0.7% LGC 27 45.00 15 30.66 67 7.45 Bare-Based Mud 90 30.50 15 15.84 31 11.82 Base Mud + 0.3% LGC 90 41.50 11 31.71 95 10.15 Base Mud + 0.5% LGC 90 40.50 11 30.14 76 9.20 Base Mud + 0.7% LGC 90 43.00 11 32.70 60 7.22
  • 15.  As a drilling mud takes place downwardly the drilling mud temperature tends to increase rapidly due to friction and this increase influences the mud rheological properties negatively.  The negative effect includes sever decrease of drilling mud viscosity and yield point and that makes most of drilling mud additives not functional at high temperature.  In this regard, a polymeric drilling mud additive with a higher yield point exhibits higher gel strength, which imparts a desirable structural property to the drilling mud (Gray & Darley, 1980).
  • 16. Types of mud AV PV YP Before After Before After Before After Base mud + 0.5% LGC 38 58.5 13 37 25.55 21.97 Base mud + 0.5 % CMC 97.5 25 19 18 61.8 7.154 Base mud + 0.5 % Guar Gum 105 23.5 35 18 71.5 5.621 Base mud + 0.5 % Xanthane 82.5 21 64 16 28.10 5.11
  • 17.  There are times when circulation has to be stopped, the drilling mud must have that gelling characteristics ( gel strength) that will prevent drill cuttings from settling down at the bit.  With proper thermally stable gel strength can help suspend cuttings in the hole and allow them to settle out on the surface.  A mud pH range between 9 and 10.5 is almost always desired in drilling operations. This range suppresses the corrosion rate of drilling equipment especially drill pipe and bit.
  • 18. Types of mud GS pH Before After Before After Base mud + 0.5% LGC 73 74 9.65 9.25 Base mud + 0.5 % CMC 96 14 11.62 9.30 Base mud + 0.5 % Guar Gum 79 7 11.53 8.73 Base mud + 0.5 % Xanthane 67 4 11.62 8.64
  • 19.  LGC has been successfully synthesized by exploiting the waste of palm oil industry in the polymeric field.  From an experimental point of view, the use of 0.5 % LGC as drilling mud additives is not required any additional additives like thermal stabilizer (alkyl metal chromate and starch) or pH controlling agent ( soda ash and acetic acid), thereby it may reduced the cost of drilling operation and minimize the environmental damage.  LGC exhibited good compatibility with commercial drilling mud additives in terms of ; viscosity building, gelling abilities, pH controlling and thermal degradation resistance.