Pet 364 Lab Manual (2)
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University of Alberta *
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Course
364
Subject
English
Date
Dec 6, 2023
Type
Pages
52
Uploaded by runabout83
PETE
364
Drilling
Engineering
Laboratory
Manual
Course
Instructor:
Dr.
ERGUN
KURU
Lab
Instructors:
Dr.
Shanshan
Yao
Mr.
John
Czuroski
School
of
Mining
and
Petroleum
Engineering
Civil
and
Environmental
Engineering
Department
University
of
Alberta
FALL
2023
PETE
364
Drilling
Engineering
Safety
Manual
School
of
Mining
and
Petroleum
Engineering
Civil
and
Environmental
Engineering
Department
University
of
Alberta
FALL
2021
Sanctioned
by
Environmental
Health
and
Safety,
U
of
A
Table
of
Contents
1.
General
Laboratory
Safety
Rules
.............
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3
2.
Specific
Equipment
Safety
Information
...........
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Eye
Imjuries:
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5
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S
RIrst
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R
SRR
6
3.5
Campus
Emergency
Phone
Numbers
...............
c.ccooevveecninnne.
6
This
manual
is
intended
to
make
the
students
aware
of
safety
concerns
to
themselves
as
well
as
to
the
equipment.
Before
using
a
certain
apparatus
the
students
must
read
the
short
section
that
applies
to
that
apparatus.
As
well,
the
instructor
will,
where
possible,
demonstrate
the
equipment
and
mention
the
safety
precautions.
The
instructor
is
to
be
listened
to
at
all
times.
Do
not
undertake
something
unless
the
instructor
has
said
it
is
permitted.
Students
will
be
expected
to
watch
the
Pet.
E.
364
lab
safety
videos
BEFORE
attending
the
lab
session.
These
should
be
available
on
eClass.
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General
Laboratory
Safety
Rules
1.
Lab
coats
and
safety
glasses
must
be
worn
and
are
the
responsibility
of
the
student.
Hearing
protection,
gloves,
dust
masks,
etc.
(if
necessary)
will
be
provided.
For
hygiene
reasons,
the
instructor
will
not
hand
out
spare
lab
coats
or
safety
glasses.
No
lab
coat/safety
glasses
=
no
lab.
2.
Be
prepared.
Read
carefully
and
fully
comprehend
the
laboratory
manual
for
each
test
before
beginning
any
experiment.
If
you
do
not
understand
the
procedure,
ask
your
instructor
to
explain
it.
3.
Think
safety.
No
practical
jokes
or
fooling
around.
4.
No
food
or
beverages
in
the
laboratory.
5.
Keep
noise
to
a
minimum.
Be
considerate
of
the
others
working
in
your
area.
6.
Dress
appropriately
for
lab
work.
No
open-toed
shoes.
No
loose
fitting
clothing.
Shorts
may
not
be
worn
in
the
labs.
7.
Be
aware
of
dangling
jewelry
or
long
hair
that
might
get
caught
in
equipment.
Long
hair
should
be
tied
back
and
jewelry
removed.
8.
Do
not
approach
or
touch
any
machine
operator
from
behind
while
any
equipment
is
in
operation.
9.
Gas
cylinders
are not
to
be
operated
by
the
student.
10.
Materials
and
equipment
may
not
be
removed
from
the
laboratory
without
proper
authorization.
11.
If
you
detect
any
equipment
that
appears
to
not
function
properly,
DO
NOT
USE
IT.
Report
it
to
the
instructor.
12.
Only
authorized
and
trained
persons
are
to
use
the
laboratory
equipment.
13.
When
finished
working
in
the
lab
make
sure
that
the lab
equipment
is
returned
to
the
proper
place.
Students
must
clean
up
all
equipment
properly
before
leaving
or
risk
losing
marks.
14.
Report
all
accidents
and
injuries
to
the
lab
instructor,
no
matter
how
minor.
15.
If
you have
any
medical
problems
which
could
be
potentially
dangerous
to
yourself
and/or
others,
report
these
to
the
laboratory
instructor
at
the
start
of the
lab.
16.
Never
work
alone.
All
laboratory
students
must
be
supervised
by
the
instructor.
17.
Anyone
under
the
influence
of
alcohol
or
other
drugs
will
not
be
allowed
in
the
lab.
If
necessary,
this
will
be
enforced
with
a
call
to
Campus
Security.
3
18.
Any
messes,
wet
or
dry,
must
be
cleaned
up
immediately,
not
left
until
the
end
of
the
lab.
19.
Stay
in
the
assigned
work
area.
Do
not
wander
around
the
lab
“exploring”
to
see
what
is
in
other
areas.
20.
Mud/drilling
fluid
that
is
thicker
than
water
is
to
be
disposed
of
in
the
garbage
cans,
not the
sinks.
1.
Specific
Equipment
Safety
Information
Bentonite:
This
is
the
primary
material
used
in
making
drilling
fluid.
Due
to
its
powdery
nature,
students
handling
it
MUST
wear
a
dust
mask
(supplied
to
them)
to
avoid
inhaling
the
dust
that
will
diffuse
into
the
air.
When
weighing
the
bentonite,
be
as
close
to
the
balance
as
possible
and
if
any
is
spilled
it
must
be
cleaned
up
immediately.
Mud
Mixer:
Be
aware
the
mud
mixer
spins
at
very
high
RPMs.
As such
it
creates
a
bit
of
a
“wind”
When
adding
the
bentonite,
wear
the
provided
dust
mask
or
this
“wind”
will
send
the
powder
into
your
face/lungs.
When
mixing
the
mud,
add
a
bit
of
water,
then
a
bit
of
bentonite
and
continue
until
done.
Do
not
pour
all
the
water
and add
all
the
bentonite
at
once.
Do
not
go
beyond
medium
speed
or
the
mud
will
spill
out.
Fann
VG
Viscometer:
The
viscometer
can
operate
at
various
RPMs,
some
of
which
could
be
considered
quite
high.
Care
should
be
taken
in
setting
the
RPMs.
Filtration
Apparatus:
High
pressure
is
required
to
operate
this
apparatus.
The
mud
chamber
contains
a
screen,
filter
paper
and
an
O-ring
(which
must
be
put
in
a
certain
order)
for
proper
sealing
of
the
apparatus
with
the
lid,
which
is
connected
to
a
gas
cylinder.
The
chamber
will
be
readied
for
you
by
the
instructor,
do
not
“play”
with
this
and
switch
the
parts
around.
The
instructor
will
always
check
to
make
sure
the
chamber
is
OK
and
do
not
put
mud
into
the
chamber
until
the
instructor
has
verified
this.
Once
verification
is
complete,
the
instructor,
and
only
the
instructor,
will
attach
the
mud-
filled
chamber
to
the
rest
of
the
apparatus
and
tighten
the
top
lid.
Only
the
instructor
will
turn
on
the
gas
tank
to
activate
the
experiment.
When
the
experiment
is
completed,
notify
the
instructor
who
will
then
shut
off
the
gas
tank
and bleed
off
the
pressure
safely.
5.
Mud
Retort:
The
mud
retort
is
used
to
boil
the
mud
so
that
water
evaporates
and
later
condenses
into
a
small
cylinder.
Do
not
touch
the
retort
while
it
is
warming
up
or
in
operation.
There
is
an
extremely
high
risk
of
being
severely
burned.
Also,
take
care
in
handling
the
glass
cylinder,
in
case
it
breaks
and
causes
a
cut.
6.
Chemicals
and
Other
Substances:
The
following
will
be
used
in
the lab
at
some
point:
Bentonite,
Sepiolite,
Xanthan
gum,
NaCl,
Quik-Trol
(a
bio-polymer),
Barafos
(a
polyphosphate),
barite,
lignite,
Calcium
oxide,
caustic
soda,
phenolphthalein,
sulfuric
acid,
Bromo
Cresol
Green
Methyl
Red.
The
“potential”
harmful
effects
of
each
of
these
are
too
numerous
and
varied
to
mention
here.
If
handled
in
a
proper
manner,
safety
would
not
be
an
issue.
Any
student
wanting
to
know
of
the
“potential”
effects
of
these
substances
should
consult
the
in-lab
MSDS
manual,
available
by
asking
the
instructor.
MSDS
is
an
acronym
for
Material
Safety
Data
Sheet.
In
Case
of
Emergency
3.1
Fire
Any
fire,
no
matter
how
small,
can
be
potentially
lethal.
This
is
especially
true
in
a
laboratory
setting,
where
toxic
fumes
may
accompany
smoke.
In
the
event
of
fire:
1.
Do
not
attempt
to
put
out
the
fire.
2.
Activate
the
nearest
fire
alarm.
It
is
beside
the
double
door
entrance
to
2-052,
in
the
hallway.
3.
All
building
occupants
must
exit
the
building
when
the
fire
alarm
is
activated.
4.
Evacuate
the
building
by
the
nearest
and
safest
exit.
DO
NOT
USE
ELEVATORS.
5.
Close
doors
to
isolate
the
fire.
3.2
Eye
Injuries
Chemical
spills
or
burns
to
the
eyes
are
extremely
serious.
This
lab
has
two
eyewash
stations.
Their
location
will be
indicated
at
the
start
of
the
term.
An
individual
with
an
injury
to
the
eyes
may
require
assistance.
If
so,
guide
the
casualty
to
the
eyewash
station
and
hold
their
head
in
position
while
the
water
is
running.
It
may
be
necessary
to
pry
the
lids
open.
The
eyes
should
be
5
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flushed
thoroughly
for
several
minutes,
and
professional
medical
attention
should
be
provided
immediately
by
proceeding
to
Campus
Health
in
the
Student
Union
Building,
second
floor.
3.3
Emergency
Shower
The
lab
also
has
an
emergency
shower.
Its
location
will
be
indicated
at
the
start
of
the
term.
3.4
First
Aid
First
aid
kits
are
available
in
the
lab
should
anyone
have
need
of
one.
The
instructor
has
taken
first
aid
courses,
though
there
is
a
limit
to
what
he
is
capable
of
doing,
physically
and
legally.
If
you
require
first
aid,
notify
the
instructor
and
he
will
assist
to
the
best
of
his
ability.
3.5
Campus
Emergency
Phone
Numbers
There
is
a
phone
(492-9207)
in
the
lab,
located
on
a
desk
by
the
double
door
entrance.
EMERGENCY:
phone:
911
(24
hrs)
any
life
threatening
emergency
Campus
Security:
phone:
2-5050
(24
hrs)
non-emergency
situations
Facilities
Management:
phone:
2-4833
(24
hrs)
maintenance/building
issues
Civil
Main
Office:
7-207
ICE:
phone:
2-4235
(8:30-4:30)
general
inquiries
Environmental
Health
and
Safety:
phone:
2-4555
(8:00-5:00)
general
inquiries
Near
the
in-lab
phone
is
a
green
sheet
of
Emergency
Information
that
summarizes
much
of
the
above.
This
sheet
is
also
located
beside
the
single
door
at
the
opposite
end
of the
lab.
Guidelines
for
Petroleum
Engineering
Laboratory
Reports
{Revised
JULY
2022)
A
report,
especially
one
produced
for
a
university
course,
is
written
for
the
purpose
of
conveying
information.
The
information
to
be
presented
in
these
reports
is
intended
to
show:
*
An
understanding
of
the
underlying
principles
behind
the
experiment,
and
how
the
experiment
tests
them.
%
An
ability
to
present
this
information
in
a
manner
such
that
it
is
clearly
understood
by
the
reader.
As
such,
laboratory
reports
are
expected
to
be
written
in
a
professional
manner
as
befits
a
university
student:
(1)
Text
(and
equations)
must
be
typed,
be
in
the
past
tense
and
be
impersonal.
That
is,
no
“I’,
“we”,
“you”,
etc.
(2)
Graphs
must
be
done
with
software,
not
by
hand,
and
be
neat
and
large
enough
to
be
readable.
(3)All
information
needed
to
write
the
report
must
be
included
in
the
report
and
not
referred
to
as
an
outside
source.
Data
tables
from
the
lab
manual,
or
the
necessary
portions
of
them,
should
be
retyped,
not
photocopied,
but
must
be
included.
This
is
not
considered
plagiarism.
(4)
Schematics
(diagrams)
of
equipment
must
be
neatly
hand
drawn,
not
photocopied
from
the
lab
manual
or
downloaded
from
the
Internet.
(5)
Plagiarism,
should
it
occur
in
any
form
(Internet,
other
students),
will
be
dealt
with
according
to
its
degree
of
severity.
Report
writing
is
an
important
aspect
of
the
job
of
any
engineer
for
accurately
conveying
the
findings
of
a
study.
The
report
should
read
smoothly
and
in
the
past
tense,
as
if
it
was
prepared
for
a
client
or
boss
or
instructor.
Ensure
proper
spelling
and
grammar.
Pages
must
be
numbered.
Title
and
number
the
tables/figures/graphs
and
refer
to
them
in
the
text,
by
their
titte/number
and
page
number.
Students
are
recommended
to
use
the
following
section
headings,
the
value
of
each
section
is
indicated
in
parentheses.
Each
section
should
begin
on
a
separate
page.
1.
Title
Page
(5)
This
page
must
include
all
of
the
following:
course
name
and
course
number,
experiment
number
and
title
of
experiment,
name
of
student,
ID
of
student,
group
number
(if
there
is
one
assigned
by
the
instructor),date
of
experiment
and
date
of
submitted
report.
2,
Cover
Letter
(10)
This
is
an
executive
summary
(on
the
order
of
1
page)
and
as
such
should
summarize
the
entire
experiment.
It
should
be
addressed
properly
(to
the
Course
Instructor,
Lab
Instructor
or
Teaching
Assistant
by
name),
define
briefly
but
exactly
what
was
performed
(do
not
to
repeat
the
objective
of
section
3,
below)
and
what
was
learned
from
it,
include
the
sample
name
and
the final
(not
raw,
in-lab
_data)
numerical
results.
If
necessary,
these
data
can
be
tabuiated.
A
graph
is
only
a
pictorial
representation
of
numerical
data
and,
as
such,
should
not
be
included
in
the
cover
letter.
If
it
is
necessary
to
include
a
graph
for
visual
emphasis,
present
the
numerical
results
with
it.
Be
brief
but
specific,
and
include
numbers
where
possible.
For
instance,
do
not
say
“high
efficiencies
were
obtained”
but
“the
measured
efficiency
was
72%”".
There
is
no
need
for
any
amount
of
procedure,
theory,
etc.
here,
only
to
have
that
repeated
later
in
those
sections.
That
is,
don’t
write
the
entire
report
in
the
cover
letter;
avoid
repetition.
There
must
be
a
printed
name
and
signature.
This
is
the
most
important
section.
It
conditions
the
attitude
of
the
reader.
When
you
are
working
for
a
living
this
might
be
the
only
part
of
the
report
which
will
be
read
by
the
people
who
matter.
They
do
not
want
to
search
the
entire
report
for
key
information,
such
as
final
results
or
the
name
of
the
sample.
If
they
are
curious and
have
the
time
or
desire,
then they
might
read
further
to
see
how
the
experiment
was
done
(Procedure),
what
could
have
caused
problems
with
the
results
(Analysis
and
Discussion),
etc.
3.
Objectives,
Concepts
and
Theory
(10)
The
Objectives
are
the
intended
outcomes
of
the
experiment:
what
were
expected
to
be
achieved
or
learned
and
what
was
required
to
achieve
that
outcome.
Concepts
would
include
terms,
definitions
and
some
general
background
information
necessary
for
the
reader
to
understand
the
experiment.
Theory
describes
the
underlying
science/engineering
of
the
experiment.
Equations
used
in
the
Results
and
Calculation
section
must
be
introduced
and
explained
here.
Define
all
symbols
used
and
number
the
equations.
The
theory
of
how
the
equipment
works
(not
how
to
use
the
equipment,
as_in
the
Experimental
Procedure)
must
be
explained
here.
2
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4.
Experimental
Procedure
(10)
Explain
the
experimental
procedure
to
someone
who
was
not
in
the
lab
in
relatively
simple
words
—
do
not
just
repeat
the
steps
indicated
in
the
lab
manual.
The
procedure
should
indicate
to
the
reader
the
understanding
of
not
only
what
was
done
but
how
and
why
it
was
done.
Use
simple
hand
drawn
schematic
diagrams,
large
enough
to
be
readable
and
properly
labeled,
of
the
experimental
apparatus
used
in
the
experiment.
Do
not
photocopy
the
diagrams
from
the
lab
manual.
A
photograph
of
the
equipment
is
not
acceptable
by
itself
but
may
be
used
if
it
complements
the
hand
drawn
sketch
and
must
be
the
same
as
the
apparatus
used
in
the
lab.
Give such
sketches
as
are
necessary
to
define
the
experiment
or
to
describe
essential
features
of
the
apparatus.
Do
not
waste
time
on
artistic
flourishes
but
produce
sketches
which
befit
an
engineer.
If
necessary
or
possible,
include
significant
dimensions,
and
identify/label
the
most
important
items
of
equipment.
Describe
the
experimental
procedure
giving
due
prominence
to
those
aspects
which
are
crucial
and
omitting
reference
to
those
which
could
be
regarded
as
self-evident
to
the
reader
(but
do
not
assume
him/her
to
be
a
petroleum
engineer
who
has
seen
the
particular
equipment
being
used).
5.
Results
and
Calculations
(25)
Results
refer
to
the
raw
data
that
was
acquired
in
the
lab,
and
Calculations
refer
to
the
mathematical
processing
of
these
results
and
the
final
outcome.
In
general,
it
is
best
to
present
the
results/calculations
in
tabulated
form.
As
far
as
possible,
present
the
raw
data
in
addition
to
derived
results;
in
this
way
conversion
errors
will
not
completely
invalidate
the
report.
Experimental
accuracy
and
possible
numerical
errors
should
be
stated,
though
not
necessarily
in
a
rigorous,
mathematical
nature.
It
is
not
necessary
to
be
concerned
with
significant
figures.
Indicate
all
experimental
conditions,
tabulate
the
measured
data,
perform
sample
calculations,
and
plot
graphs
(if
necessary)
showing
the
calculated
or
interpreted
results.
Words
must
be
used
to
explain
the
calculations
so
that
they
are
more
clearly
understood.
The
reader
should
be
able
to
“read”
the
calculations
as
easily
as
reading
text
and
should
not
have
to
use
a
calculator
to
understand
them.
Ensure
that
the
scale
of
any
graph
is
such
that
the
data
of
interest
take
up
the
major
portion
of
the
graph
and
that
the
graph
is
large
enough
to
properly
convey
the
information.
Label
each
curve
or
axis
on
the
graphs
and
include
a
legend.
6.
Analysis
and
Discussion
(25)
The
title
means
what
it
says,
that
is,
Analyze
and
Discuss.
Do
not
just
repeat
the
numerical
results,
but
they
can
be
casually
referred
to.
Indicate
the
assumptions
made
for
interpreting
the
results,
explain
and
justify
differences
between
experimental
and
simulated
results,
if
any,
indicate
and
explain
any
data
behavior
that
is
expected
or
not
expected,
explain
errors,
limitations
of
the
equipment,
and
provide
advantages/disadvantages
of
experimental
procedures
used.
Why/why
not
do
the
data
look
the
way
they
do?
First,
note
any
interesting
observations
in
the
raw
results
—
trends,
scatter,
anomalies,
etc.
Then
analyze
the
results
in
terms
of
the
theory
previously
presented
and
discuss
the
outcome.
Do
not
waste
many
words
stating
the
obvious,
but
try
to
account
for
significant
discrepancies.
Try
to
do
this
specifically,
if
possible
using
numbers,
and
not by
fuzzy
arguments.
Justify
the
analysis,
that
is,
why was
it
done
and
what
did
it
accomplish.
7.
Conclusions
and
Improvements
(10)
This
section
should
not
be
a
repetition
of
the
cover
letter
or
of
the
Analysis
and
Discussion
sections,
but
rather
a
summary
of
what
was
accomplished/learned
from
the
lab
(do
not
give
numerical
results)
—
text
only,
no
numbers
or
figures.
It
should
partly
be
a
refiection
of
the
Objectives
from
part
3
above,
that
is,
were
the
statements
mentioned
in
the
Objectives
achieved?
Indicate
suggestions
for
improvements.
Why
are
the
improvements
needed
and
how
would
their
implementation
affect
the
data
taken
in
the
lab
or
the
outcome
of
the
experiment?
The
conclusions
should
be
numbered
and
be
brief.
In
general,
do
not
introduce
new
material
in
this
section,
that
is,
repetition
of
previous
statements
is
encouraged.
8.
References
(5)
Author’'s
name,
Title
of
Publication,
Journal
Year,
Volume,
and
Page,
as
applicable.
The
link
to
the
website
if
such
a
reference
is
used.
Any
other
materials
used,
such
as
videos
or
conversations
with
other
parties.
Two
final
comments.
(1)
Though
he
may
at
times
assist
in
the
lab,
the
instructor
is
not
to
be
mentioned
in
the
report.
Also,
no
other
student
in
the
group
should
be
referred
to.
In
other
words,
the
work
and
the
report
was
done
by
only
one
person.
(2)
Above
all,
READ
and
UNDERSTAND
THOROUGHLY
all
of
the
information
given
to
you
(the
Guidelines,
lab
manual,
etc,
If
there
are
any
questions,
or
for
clarifications,
the
student
should
contact
the
lab
instructor.
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Addendum
to
the
Guidelines
for
Petroleum Engineering
Reports
Preface
This
document
supplements
the
Guidelines
for
Petroleum Engineering
Reports
by
making
clearer
what
is
required
in
each
section.
The
Guidelines
must
still
be
followed.
Note
the
following:
1.
All
of
the
report,
including
equations
and
calculations,
must
be
typed.
2.
All
graphs
must
be
done
with
EXCEL
or
some
other
graphing
software,
but
not
by
hand.
3.
The
graphs
and
labels
must
be
large
enough
for
the
reader
to
see
the
information
conveyed
clearly.
A
1.0
mark
will be
deducted
for
each
graph
not
deemed
large
enough.
4.
All
figures
or
diagrams
of
the
equipment
must
be
hand
drawn,
neat,
and
large
enough
to
be
readable.
Any
figure
or
diagram
copied
from
the
lab
manual,
or
another
source
will
have
a
1.0
mark
deducted
for
each
infraction.
If
not
neat
enough,
0.5
will
be
deducted
each
time.
5.
Each
figure,
diagram,
table
or
graph
must
be
labelled
with
a
proper
title
and
number.
For
example,
Figure
1:
The
Idiosyncratic
Discombobulator.
Not
labelling
a
figure,
diagram,
table,
or
graph
will
result
in
a
loss of
1.0
mark
each
time.
The
label
(title)
can
be
either
at
the
top
or
bottom.
6.
These
figures,
diagrams
or
graphs
must
be
referred
to
in
the
text,
or
0.5
will
be
deducted
each
time.
This
is
best
done
before
the
reader’s
attention
is
drawn
to
them.
The
writer
should
say
something
like:
“Refer
to
Figure
1
for
a
depiction
of
the
Idiosyncratic
Discombobulator.”
Then
start
talking
about
the
Idiosyncratic
Discombobulator.
It
makes
little
sense
to
talk
about
an
apparatus
when
the
reader
can’t
see
a
depiction
of
it.
7.
Spelling
will
be
deducted
0.5
marks
for
each
incorrect
spelling
(the
same
word
misspelled
several
times,
in
the
same
way,
is
counted
only
once),
up
to
a
total
of
5
marks
maximum
(10
misspellings).
The
marker
will
list
these
on
the
Title
Page
with
the
correct
spelling,
and
this
misspelling
mark
will
be
deducted
from
the
total
mark,
not
from
each
section.
8.
Itis
permissible
(and
it
will
be
necessary)
to
take
data
from
tables
in
the
lab
manual,
but
instead
of
‘copying’
the
entire
table,
just
make
a
new
table
in
the
report
with
the
needed
data.
9.
The
section
headings
must
be
as
indicated
in
the
Guidelines,
or
0.5
marks
will
be
deducted
each
time.
For
example,
the
section
is
called
Analysis
and
Discussion.
There
is
not
a
section
called
Discussion,
nor
is
there
a
section
called
Calculations
and
Analysis.
Do
not
consider
the
lab
report
as
just
an
“exercise”
to
be
done
as
part
of
a
course
requirement.
The
lab
report
could
also
be
considered
as
such:
-
Areport
to
your
boss
for
a
project
he
has
asked
you
to
do.
-
Areport
to
someone
for
whom
you
are
doing
a
test
and
from
whom
you
expect
payment.
In
either
case,
the
reader
wants
to
find
the
proper
information
in
the
correct
sections.
He/she
is
a
busy
person
who
does
not
have
the
time
to
waste
searching
a
multi-page
report
looking
for
the
results
he/she
paid
good
money
for
you
to
supply.
Neither
does
he/she
want
to
pull
out
a
calculator
and
go
through
the
calculations
to
find
the
result
when
it
was
your
job
to
supply
that
result.
In
either
case,
you
would
probably
find
yourself
out
of
a
job.
It
is
best
to
learn
and
refine
the
techniques
of
report
writing
here.
One
final
note:
Students
have
been
told,
or
should
know,
that
they
can
always
come
to
the
lab
instructor
for
help.
Title
Page
(5
marks):
In
the
title
page,
put
those items
as
mentioned
in
the
Guidelines
or
fose
0.5
for
each.
For
example,
if
you
were
taking
Basket
Weaving
101:
Introduction
to
Making
Baskets,
Basket
Weaving
101
is
the
course
number,
and
Introduction
to
Making
Baskets
is
the
course
name.
The
group
number
is
that
assigned
to
you
(see
the
lab
schedule)
when
you
are
in
the
lab
and
working
with
others
and
not
that
designated
by
Bear
Tracks.
The
experiment's
name
is
as
in
the
lab
manual,
and
any
variation
will
have
0.5
marks
deducted.
Cover
Letter
(10
marks):
If
there
is
no
address,
1.0
mark
will
be
deducted.
If
the
salutation
or
honorific
is
improper,
0.5
will
be
deducted.
Either
“Dear”
or
“To”
is
acceptable.
Mr.
(professor’s
name)
is
not.
DO
NOT
put
the
objectives
(or
a
version
of
them)
here,
only
to
repeat
them
in
the
next
section.
Just
state
what
was
done/accomplished.
For
example:
“In
this
experiment,
three
different
types
of
baskets
were
made,
using
different
materials
such
as
straw,
wire
and
plastic.
The
wire
basket
was
determined
to
hold
more
weight
before
breaking
than
the
other
two
types,
60
pounds
versus
40
pounds
for
straw
and
48.5
pounds
for
plastic.”
In
this
case,
straw,
wire
and
plastic
would
be
the
names
of
the
samples.
No
sample
designation
is
deducted
1.0
marks.
The
weights
they
hold
would
be
the
numerical
results.
All
of
the
final
numerical
results
(as
calculated
in
the
Results
and
Calculations)
section
must
be
here.
Up
to
5.0
marks
are
given
for
these,
and
partial
marks
are
given
depending
on
how many
of
these
results
are
missing,
or
if
units
are
missing
or
wrong,
etc.
No
marks
will
be
deducted
for
calculation
errors;
that
will
be
done
in
the
Results
and
Calculations
section.
There
must
be
a
printed
name
and
signature,
or
1.0
mark
will be
deducted.
If
one
of
these
is
missing,
0.5
will
be
deducted.
Objectives,
Concepts,
and
Theory
(10
marks):
The
objectives,
worth
2.0
marks,
must
be
at
the
start
of
this
section,
not
elsewhere
or
lose
0.5
marks.
They
should
be
reflected
in
the
Conclusions
and
Improvements
section
as
having
been
achieved.
Partial
marks
are
awarded
depending
upon
the
strength
of
the
objectives.
In
the
basket
weaving
example,
the
objectives
might
be
similar
to
this:
“The
objectives
of
this
experiment
were
to
learn
the
art/science
of
basket
weaving
and
to
make
baskets
out
of
different
materials.
Further,
students
will
learn
the
use
of
different
techniques
or
equipment
to
make
these
baskets
and
realize
that
these
can
make
a
difference
in
how
the
basket
can
be
used
and
how
much
they
can
hold
before
breaking.”
Concepts
are
worth
up
to
2.0
marks
and
are
explained
in
the
Guidelines.
For
the
basket
weaving
example,
a
definition
of
what
a
basket
is,
what
it
is
used
for,
and
why
it
is
necessary
to
use
different
materials
would
be
a
good
beginning.
More
could
be
said,
though.
Theory
is
worth
up
to
6.0
marks
and
is
explained
in
the
Guidelines.
Equations
must
be
numbered
or
fose
1.0
mark
total
and
thoroughly
explained
here
before
being
used
in
the
Results
and
Calculations
section.
Simply
listing
the
equations
without
explaining
what
the
symbols
or
equations
mean
is
improper.
One
aspect
of
the
theory
might
be
that
baskets
are
weaved
because
doing
so
makes
the
basket
stronger,
and
different
materials
can
affect
this
strength.
Theoretical
graphs
or
outcomes
should
be
presented.
Also
includes
the
fundamental
theory
of
the
equipment.
ii
Experimental
Procedure
(10
marks):
A
“procedure”
that
simply
lists
the
steps
performed
in
the
lab
is
not
correct
and
will
result
in
no
marks.
Explain
to
the
reader
the
how
and
why
of
each
step
to
understand
what
was
done.
It
will
be
necessary
to
use
diagrams
or
figures
of
the
equipment
(refer
to
items
3
through
6
in
the
Preface
section
above)
as
a
visual
explanation.
These diagrams/figures
can
appear
either
in
the
Theory
section
or
the
Procedure
section
since
they
will
probably
need
to
be
discussed
in
both
sections.
For
example,
don’t
say:
“Valve
one
was
opened,
then
valve
3
was opened.”,
but
“Valve
one
was
opened
so
that
the
flow
of
gas
could
enter
the
Idiosyncratic
Discombobulator
from
the
main
gas
tank,
and
valve
3
was
opened
so
that
the
gas
could
then
enter
the
main
chamber
of
the
Discombobulator.
Figure
1
shows
the
location
of
these
valves.”
The
procedure
is
worth
a
maximum
of
10
marks,
and
deductions
are
based
on
how
complete
this
procedure
is
with
regard
to
text
and
figures.
If
there
are
no
figures
or
diagrams
of
the
equipment,
then
2.0
marks
are
deducted.
Results
and
Calculations
(25
marks):
Present
all
of
the
in-lab
results
first
before
any
calculations
are
done.
These
data
must
be
organized
in
an
ordered
manner
(a
table,
where
convenient)
and
their
meaning
clearly
explained.
The
reader
must
be
able
to
understand
what
these data
show,
not
have
to
guess.
Up
to
5.0
marks
are
given
for
this,
less
if
some
data
are
missing
or
units
are
not
mentioned,
etc.
Calculations
are
to
be
in
a
logical
order.
Calculate
a
value
first
before
using
it
in
another
equation.
The
calculations
should
be
as
readable
as
text,
so
use
words
to
explain
thoroughly
what
is
being
done.
The
reader/marker
should
not
have
to
do
the
math
to
determine
what
is
being
calculated.
Depending
on
this
“readability,”
up
to
2.0
marks
could
be
deducted.
For
example,
don’t
say:
“xy/5x
=
2.0”
but
say:
“Since
x
=5
and
y
=
10,
then
from
equation
(6),
xy/5x
=
(5x10)/(5x5)
=
2.0.”
A
sample
calculation
must
be
shown
for
every
unique
calculation,
or
a
deduction
of
1.0
mark
will
occur
each
time.
When
all
calculations
are
completed,
a
table
should
be
made
to
show
all
the
final
calculations
in
one
place.
In
most
cases,
graphs
will
be
needed
to
display
the
calculated
data.
Failure
to
include
a
graph
will
lead
to
a
deduction
of
2.0
marks
each
time.
Refer
to
steps
3
to
6
in
the
Preface
section
as
well.
Missing
calculations
will
be
deducted
1.0
mark
each
time.
Wrong
calculations
will
be
deducted
up
to
2.0
marks
each
time,
depending
on
their
importance
or
severity,
that
is,
how
they
impact
the
other
calculations.
Analysis
and
Discussion
(25
marks):
As
it
says
in
the
Guidelines:
“Analyze
and
Discuss”.
Don’t
state
the
obvious,
be
meaningful.
For
an
example
analysis,
do
not say:
“The
graph
(see
Figurel)
of
tachyon
density
is
linear
with
respect
to
time.”
That
is
obvious
from
anyone
looking
at
the
graph.
What
must
be
addressed
is,
why
is
it
linear? A
better
analysis
is
to
say:
“The
graph
(see
Figure
1)
of
tachyon
density
is
linear
(with
negative
slope)
with
time
because
as
time
increases,
the
number
of
tachyon
particles
spread
further
and
further
apart
into
larger
and
larger
volumes;
hence
there
are
fewer
tachyon
particles
per
unit
volume,
which
is
the
definition
of
density.”
11
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The
discussion
could
be
like:
“One
reason
that
the
tachyon
density
is
not
as
high
as
expected
could
be
that
the
vacuum
in
the
Idiosyncratic
Discombobulator
(1.D.)
was
not
as
high
as
it
should
have
been.
This
may
have been
caused
by
a
vacuum
pump
that
was
not
working
efficiently
since
it
was
noticed
that
the
vacuum
reading
was
only
22.5
inches
of
mercury
and
not
closer
to
29
inches
that
it
should
be
if
working
properly.
Tachyons
need
a
strong
vacuum
if
they
are
to
form
properly.
There
may
have
been
a
loose
connection
from
the
pump
to
the
1.D.,
thus
preventing
the
vacuum
pump
from
removing
all
the
air,
or
which
caused
some
of
the
room
air
to
leak
into
the
[.D..”
Since
there
are
essentially
two
sub-sections
here,
up
to
12.5
marks
will
be
given
for
the
“analysis™
(technical/scientific/engineering
explanation
of
the
final
results)
and
up
to
12.5
marks
will
be
given
for
the
“discussion”(limitations
of
the
equipment/method,
advantages/disadvantages
of
the
equipment/method,
sources
of
potential
error,
etc.).
Conclusions
and
Improvements
(10
marks):
Up
to
7.0
marks
will
be
given
for
the
conclusions
part,
and
up
to
3.0
marks
will
be
given
for
the
improvements
part.
Referring
to
the
basket
weaving
experiment,
one
conclusion
might
be
that
several
different
types
of
baskets
were
successfully
made.
Another
could
be
that
students
learned
how
to
use
the
equipment
to
make
these
baskets,
whereas,
before
the
lab,
they
had
no
understanding
of
this
equipment.
An
improvement
could
be
that
different
types
of
straw
should
have been
used,
instead
of
only
one
kind,
to
see
if
different
types
would
hold
more
weight.
Regardless,
the
improvement
must
be
justified;
that
is,
do
not
just
say:
“Different
types
of
straw
should
have
been
used.”
State
why.
References
(5
marks):
When
referencing
the
lab
manual.
0.5
marks
will
be
deducted
for
each
bit
of
missing
information.
For
other
references
that
should
be
there
but
are
missing,
1.0
mark
will
be
deducted.
iv
Reference
Material
The
lab
manual
should
be
read
before
the
relevant
experiments.
Suggested
textbook
material
includes:
A-
Mitchell,
R.F.,
Miska,
S.
“Fundamentals
of
Drilling
Engineering”,
SPE
Textbook
Series,Vol
12.,
2011
Chapter
3,
pp.
87-138.
B-
American
Petroleum
Institute
(API),
“Recommended
Practice
for
Field
Testing
Water-based
Drilling
Fluids,”
ANSI/API
13B-1,
4™
Ed.,
March
2009.
C-
American
Petroleum
Institute
(API),
“Recommended
Practice
for
Field
Testing
Qil-based
Drilling
Fluids,”
ANSI/API
13B-2,
4"
Ed.,
2005.
D-
Darley
H.C.H,
and
Gray
G.R,
“Composition
and
Properties
of
Drilling
and
Completion
Fluids,”
Gulf
Professional
Publishing,
5th
Edition,
1988.
Concept
of
This
Laboratory
Course
All
experiments
will
be
tied
together
through
the
use
of
a
single
well.
Through
the
use
of
offset
data
and
knowledge
gained
in
the
lab,
the
students
will
be
able
to
make
recommendations
on
the
mud
program
as
the
drilling
progresses.
These
recommendations
should
include:
the
mud
weight
required,
drilling
precautions,
and
cost
analysis
of
drilling
mud.
The
well
will
be
divided
into
three
sections:
surface,
intermediate,
and
production.
The
surface
section
of
the
hole
will
deal
with
mud
problems
associated
with
unweighted
mud.
The
determination
of
rheological
properties
and
treatment
of
solids
in
an
unweighted
system
will
be
addressed.
The
intermediate
section
of
the
hole
will
deal
with
problems
associated
with
contaminates
and
weighted
muds.
The
intrusion
of
salt
and
lost
circulation
will
be
addressed.
The
production
section
of
the
hole
will
deal
with
problems
associated
with
inhibitive
muds.
Surface
Hole
In
this
section
of
the
hole,
the
most
common
problems
encountered
are
related
to:
1)
Highly
unconsolidated
formations
2)
Poor
circulation
velocity
3)
Weak
formations
4)
Shallow
gas
5)
Freshwater
sands
6)
High
volume
cuttings
generation
With
the
exception
of
the
freshwater
sands,
all
of
the
areas
of
concern
listed
above
relate
to
efficient
hole
cleaning
and
a
soiids
free
system.
Because
of
the
large
size
holes,
and
the
restrictive
pump
capacity,
hole
cleaning
by
normal
circulation
in
insufficient.
This,
together
with
the
limited
capacity
of
the
surface
solids
control
system,
results
in
a
continuous
degeneration
of
the
mud
due
to
solids
buildup.
Poor
hole
cleaning
usually
results
in
balled
bit
and
assembly
and
thick,
solids
filled,
wall
cake.
Both
of
these
problems
together
cause
tight
hole,
high
swab
and
surge
pressure,
loss
circulation,
well
kicks
and
stuck
pipe.
Stuck
pipe
is
directly
related
to
pressure
differential,
wall
cake
thickness
and
permeability
and
formation
permeability.
Because
of
this
and
the
fact
that
fresh
water
sands
are
usually
shallow
makes
the
surface
hole
more
prone
to
stuck
pipe,
even
with
unweighted
muds.
Water
sands
are
more
permeable
to
water
and
as
such
water
base
drilling
fluids
with
poor
filtrate
control
increase
the
susceptibility
to
stuck
pipe.
This
increased
permeability
also
increases
the
chances
of
loss
circulation
and
damage
to
the
fresh
water
sands.
In
the
design
of
a
mud
system
therefore
emphasis
must
be
placed
on
hole
cleaning,
solids
control,
mud
weight
and
filtrate
control.
Mud
System
Design
Hole
Cleaning
One
of
the
important
functions
of
the
drilling
fluid
is
to
lift
cuttings
from
the
borehole.
Failure
to
do
this
usually
results
in
solids
buildup,
balling,
reduced
penetration,
high
torque
and
drag,
stuck
pipe,
loss
circulation,
and
fill
on
bottom.
In
order
to
effectively
clean
the
hole
the
relative
movement
of
the
cuttings
in
the
annulus
must
be
in
the
upward
direction.
Because
of
the
large
size
holes
and
limited
pump
capacity
however,
annular
velocities
are
very
low.
In
order
to
achieve
a
net
upward
movement,
therefore,
the
slip
velocity
must
be
small.
y
_[33:5x(w,-w)xD*x¥
]
o
[665xYPx(D,~D,)+PVxV
|
V.:
Slip
velocity,
fi/sec
W,
.
Density
of
cuttings,
ppg
W
.
Density
of
mud,
ppg
V.
Average
annular
fluid
velocity,
ft/sec
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D:
Average
diameter
of
cuttings,
inches
YP:
Yield
point,
Ib/100sq.ft
PV
:
Plastic
viscosity,
cP
D,
:
Bit
size,
inches
D,
:
Outside
diamete,
inches
From
the
above
equation,
slip
velocity
can
be
reduced
by
increasing
the
yield
point
or
plastic
viscosity
in
a
fixed
hole
configuration
where
annular
velocity,
mud
weight,
cuttings
size
and density
are
constant.
Increasing
the
annular
velocity
will
increase
the
slip
velocity
because
of
the
change
in
flow
profile
from
plug
to
laminar.
Figure
1:
Effect
of
plastic
viscosity
(PV)
to
yield
point
(YP)
ratio
changes
in
flow
profile.
As
shown
in
above
figure,
plug flow
is
best
for
cuttings
removal.
To
achieve
this
however,
the
yield
point
must
be
raised
to
give
a
decreased
value
of
PV/YP.
Solids
Control
Solids
control
can
be
achieved
chemically
or
mechanically.
lonic inhibition,
encapsulation
inhibition,
oil
phase
inhibition
and
deflocculation
are
ail
chemical
methods
of
solids
control.
Chemical
control
focuses
prevention
of
cuttings
dispersion
but
its
physical
removal
is
usually
by
mechanical
means.
Mechanical
removal
of
cuttings
is
achieved
by
the
use
of
shale
shakers,
desanders,
desilters,
centrifuges,
settling
tanks
and
water
dilution.
The
efficiency
of
these
methods
of
control
reduces
with
increased
plastic
viscosity
and
gel
strength.
As
such therefore
it
is
advisable
to
also
control
both
of
these
rheological
properties.
Mud
Weight
and
Filtrate
Control
With
good
solids
control,
and
proper
maintenance
of
commercial
bentonite,
these
two
properties
can
be
effectively
controlled.
The
maintenance
of
a
proper
commercial
bentonite
concentration
can
be
achieved
by
performing
the
methylene
blue
test.
Usually
it
is
more
prudent
to
use
a
pump
and
dump
technique
in
the
unweighted
section
of
the
hole.
This
usually
results
in
cheaper
and
less
troublesome
control
of
drilled
solids
and rheological
properties.
To
effectively
train
and
familiarize
the
student
with
these
problems
and
the
design
consideration
needed
for
their
alleviation,
the
following
experiments
are
recommended.
EXPERIMENTS
No.
1
&
2
+
Yield
of
Bentonite
and
Sepiolite
Clays
/
Rheological
Characterization
of
Water-based
Drilling
Fluids
%
Filtration
Properties
of
Water-based
Drilling
Fluids
Purpose:
Experiment
No.
1
is
meant
to
familiarize
the
student
with
the
rheological
properties,
behavior
and
application
of
both
gels.
Experiment
No.
2
investigates
the
filtrate
control
properties
of
a
simple
gel
and
water
system.
Recommendation:
A.
Recommendation
of
type
of
clay
and
blend
to
be
used
for
surface
hole
drilling.
The
foliowing
points
should
be
noted:
l.
Bentonite
gives
better
filtrate
control
.
Bentonite
provide
superior
quality
.
Sepiolite
is
not
affected
by
increase
in
salinity
With
reference
to
the
study
well,
the
salt
formations
are
in
the
lower
section
of
the
well.
In
this
case,
therefore,
it
will
more
beneficial
to
drill
with
a
bentonite
system
and
achieve
better
filtrate
control
and
wall
cake
quality
across
the
shallower
and
lowered
pressured
formations.
B.
Addition
of
filtration
control
agent
increases
the
cost
but
greatly
reduces
the
cake
thickness
and
water
loss.
Low
values
of
water
loss
and
cake
thickness
usually
result
in
the
following.
I
Thin
cake,
of
1/32
and
less,
constantly
erodes
under
dynamic
drilling
conditions
Il
Low
water
loss
associated
with
polymers
results
in
higher
mud
viscosities.
On
completion
of
these
two
experiments
the
student
is
expected
to
acquire
better
understanding
of
drilling
fluid
rheology,
yield
point
and
fluid
loss.
EXPERIMENT
ONE
PART
1:YIELD
OF
BENTONITE
AND
SEPIOLITE
CLAYS
PART
2:
RHEOLOGICAL
CHARACTERIZATION
OF
WATER-BASED
DRILLING
FLUIDS
OBJECTIVES:
In
this
lab
session
two
different
groups
of
experiments
will
be
conducted
to
achieve
the
following
objectives:
1)
Determine
the
effect
of
clay
concentration
on
drilling
fluid
viscosity
for
the
two
most
common
commercially
available
clays,
bentonite
and
sepiolite.
2)
Select
the
best
model
describing
rheological
behavior
of
water-based
drilling
fluids.
Part
1
—
Yield
of
Bentonite
and
Sepiolite
Clays
Introduction
Clay
material
is
added
to
the
drilling
fluid
to
give
certain
characteristics
that
assist
the
mud
to
perform
the
functions
described
earlier.
Generally
two
types
of
clay
are
used,
montmorillonite
clay
used
in
fresh
water,
and
attapulgite
clay
used
in
salt
water.
Sodium
montmorilionite,
commonly
called
bentonite
or
gel,
is
capable
of
swelling
to
approximately
ten
times
its
original
volume
when
mixed
with
fresh
water.
Calcium
montmorillonite,
commonly
called
sub-bentonite
will
swell
only
2-4
times
its
original
volume
when
mixed
with
water.
Montmorillonite
clay
has
a
mica-type
crystal
structure
made
up
of
a
crystal
lattice
of
silica
and
alumina
as
shown
in
the
figure
1-a.
The
lattice
is
loosely
bound
with
a
cation
such
as
sodium
or
calcium
as
in
figure
1-b.
In
the
presence
of
water
the
crystal
lattice
absorbs
water
allowing
the
crystal
to
swell.
The
covalent
calcium
ion
holds
the
crystal
lattice
together
tighter
allowing
less
swelling.
In
this
experiment
bentonite
and
sepiolite
will
be
used
primarily
to
build
viscosity.
Figure
2
is
a
typical
clay
yield
curve.
The
yield
of
clay
in
fresh
water
is
defined
as
the
number
of
barrels
of
15
centipoise
(cP)
mud
obtained
from
one
ton
of
dry
clay.
The
15
cP
is
the
apparent
viscosity
measured
at
600 rpm
(i.e.
©g00/2)
using
rotational
viscometer.
Notice
that
above
15
cP
a
small
change
in
solids
results
in
a
significant
change
in
the
apparent
viscosity
of
the
mud.
10
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EXPERIMENTAL
PROCEDURE
1.
Calibrate
the
mud
balance
with
tap
water
at
room
temperature.
2.
Measure
the
viscosity
of
water
at
room
temperature
with
the
Marsh
Funnel.
Ideally,
the
Marsh
funnel
should
require
26
seconds
for
946
cc.
(1
quart)
of
water
to
flow
through
it.
3.
Mix
three
samples
of
mud
using
4%,
7%,
and
10%
bentonite
by
weight
in
fresh
water.
Add
the
bentonite
slowly,
a_bit
at
a
time,
and
definitely
not
all
at
once.
Stir
for
10
minutes
at
medium
speed.
If
the
speed
is
too high, the
mud may
spill
out
and
result
in
a
loss
of
sample.
NOTE:
All
mud
samples
made
are
based
on
350
cc.
of
water.
By
convention,
the
volume
of
water
is
to
be
measured
when
the
bottom
of
the
interface
lies
on
top
of
the
350
cc.
mark.
4.
Measure
the
apparent
viscosity
of
each
bentonite
sample
at
600
rpm.
5.
Measure
the
density
of
the
10%
bentonite
sample,
ppg
to
2
decimals,
using
the
mud
balance.
Discard
the
three
samples
in
the
garbage
cans,
not
the
sink.
6.
Mix
three
samples
of
drilling
fluid
using
4%,
7%, and
10%
sepiolite
by
weight
in
fresh
water.
Use
the
same
procedure
as
in
step
3
above.
7.
Measure
the
apparent
viscosity
of
each
sepiolite
sample
at
600
rpm.
8.
Measure
the
density
of
the
10%
sepiolite
sample
using
the
mud
balance,
ppg
to
2
decimals.
9.
Mix
15,000
mg/L
NaCl
solution
by
placing
15
grams
of
NaCl
in
a
1000
ml.
container
and
filling
with
water
to
the
1000
ml.
mark.
Stir
thoroughly.
10.Mix
samples
of
(a)
7%
bentonite
and
(b)
7%
sepiolite
(by
weight)
in
350
cc
of
the
salt
solution.
Mix
for
10
minutes
at
medium
speed.
11.Measure
the
apparent
viscosity
of
each
sample
in
step
10
at
600
rpm.
Lab
Report
and
Data
Reduction
1.
Water
properties
Water
Properties
Density,
ppg
Funnel
Viscosity,
sec/qt.
1"
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2.
Mud
viscosities
Apparent
Viscosity,
cP
Fresh
Water
15000
mg/L
Brine
CI‘?A,VV?IZ;‘Q"::
b
Bentonite
Sepiolite
Bentonite
Sepiolite
4
N/A
N/A
T
-
'
10
N/A
N/A
3.
Mud
densities
Mud
Density,
ppg
10
%
Bentonite
in
Fresh
water
10
%
Sepiolite
in
Fresh
Water
4.
Plot
apparent
viscosity
vs.
clay
content.
Discuss
swelling
properties
of
bentonite
and
sepiolite.
5.
Compare
your
results
to
Fig.
2.
What
is
sepiolite?
6.
Compute,
mathematically,
the
yield
of
bentonite
and
sepiolite
in
fresh
water
(bbl
/
ton).
7.
Graphically
illustrate
and
discuss
the
effect
of
water
salinity
on
viscosity
and
clay
yield.
AR,
P
v/
'
A5,
27
,///////////////
-4
wNA*
,//////////////
F1.1
)
Typical
Berfonkto
Pertite
P
/////////////
=
"
S
FIG.1
b)Na
montmorienite(efy
4
Camontmorerita(ight
4/////////////
“
,////////I///
Figure-1a,
tb:
Crystal
Structure
of
Clay
Minerals
12
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Weight
in
Pounds
per
Cubic
Foot
637
675
71.2
750
87
82.5
86.2
Weight
in
Pounds
per
Gallon
85
90
95
100
105
1.0
115
12.0
60
l
I
>
kS
<
£
T
el
i
i
z
3]
b
[¢]
50
o
2
¢
g
1HEE
]
s
w
=
=
kS
o
Q
3
=
3
t3
5]
4
3
2]
(D‘Tf
<)
'S
3
FH
s
B
Q
Q
40
b3
2
o
W
:
I
:
s/
[
2
a
3
-
.
l
s
/
9
€4
2
/
/
-
]
|
2
/
/
SRRy
/
/
(1
/
/A
/
10
/
/
v4
/’
4
/
L
o
5
10
5
20
25
30
35
a0
a5
50
Percent
Solids
by
Weight
SPECIFIC
GRAVITY
OF
SOLIOS
=
24
200
10075
50
40
0
25
20
18
16
14
12
10
8
Yield
(15
Centipoise
Mud)
in
Barrels
per
Ton
H
4
6
8
10
12
14
18
18
20
25
30
Percent
Solids
by
Volume
10
20
30
40
50
75
100
150
200
250
Pounds
Solids
per
Barrel
of
Mud
Figure-2:
Typical
Clay
Yield
Curves
(Gray
and
Darley,
1988)
13
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Part
2
—
Rheological
Characterization
of
Water-based
Drilling
Fluids
Introduction
At
a
given
temperature
and
pressure,
fluids
are
characterized
by:
A)
Their
behavior
under
transient
conditions,
as
manifested
by
their
response
time
to
changed
conditions
of
flow
B)
Their
behavior
in
laminar
flow,
characterized
by
their
experimental
flow
curve
or
rheogram.
The
constant
coefficients
of
the
equation
of
flow
represented
by
this
curve
are
rheological
parameters,
specific
to
a
particular
fluid.
C)
Their
behavior
at
rest,
as
manifested
by
gel
formation
after
a
certain
period
of
time
for
thixotropic
fluids.
A
fluid
is
thixotropic
if:
i-)
It
forms
a
gel
after
being
shaken
and
left
to
stand
ii-}
It
returns
to
its
original
condition
after
it
has
been
shaken
again.
If
the
flow
is
laminar,
the
equation
of
flow
relates
the
shear
stress.
t
with
the
shear
rate
,y.
In
laminar
flow
the
fluid
is
sheared
into
laminar
layers,
parallel
to
the
direction
of
flow,
each
layer
moving
at
its
specific
velocity.
A
shear
rate
is,
then,
defined
as:
_dv_
_Velocity
difference
between
two
adjacent
layers
dY
distance
between
the
two
layers
%)
The
dimensional
equation
of
y
is:
1
L
=T
@)
i.e.,
the
dimension
of
y
is
an
inverse
time
(
s1or
1/S)
The
shear
stress
is
defined
as
the
force
per
unit
area
of
the
laminar
layer
inducing
the
shear.
The
dimensional
equation
of
tis:
MLTZ
_
pp-1
72
L2
3
14
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The
shear
stress,
T,
has
the
dimension
of
pressure.
|t
is
often
expressed
in
Ibf/100
ft
2
orin
the
Sl
unit
system
in
pascal
(Pa).
For
a
given
shear
rate,
the
apparent
viscosity,
u
:
is
defined
as
follows:
Pa=%‘
@)
The
dimensional
description
of
pg
is:
MLIT2_
\p-1p-1
i
(5)
It
is
often
expressed
in
centipoise,
cP.
The
rheological
models
generally
used
by
drilling
engineers
to
approximate
fluid
behavior
are:
A.
The
Newtonian
Model
B.
Non-Newtonian
Fluids
.
The
Bingham
Plastic
Model
.
The
Power
Law Model
Rheological
Models
A.
Newtonian
Model:
The
shear
stress
of
Newtonian
fluids
is
directly
proportional
to
the
shear
rate;
if
one
variable
is
doubled,
the
other
one
is
doubled
also.
The
rheological
equation
is:
=py
(6)
Examples
of
such
fluids
are
water
and
gasoline.
15
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B.
Non-Newtonian
Fluids:
Most
drilling
fluids
are
too
complex
to
be
characterized
by
a
single
value
of
viscosity.
The
apparent
viscosity
depends
on
the
shear
rate
at
which
the
measurement
is
made
and
the
prior
shear
rate
history
of
the
fluid.
Three-types
of
non-Newtonian
fluids
are
most
often
encountered
in
drilling
fluids
and
cement
slurries:
I.
Bingham
fluids
.
Power-Law
fluids
For
Bingham
plastic
type
fluids,
the
shear
stress
also
varies
linearly
with
shear
rate
but,
unlike
Newtonian
fluids,
a
minimum
force
must
be
applied
to
impart
motion
to
them.
This
force
is
known
as
the
yield-point
or
yield
value.
The
theoretical
equation
of
flow
behavior
of
such
fluids
is:
T
TotHpY
)
1
o
=
Yield
point
as
yield
value,
1bf/100
ft
2
Kp=
Plastic
Viscosity
in
cp
Power
law
fluids,
like
Newtonian
fluids,
will
flow
under
any
applied
stress,
however
small.
But
as
distinct
from
Newtonian
fluids,
the
shear
stress
is
not
proportional
to
the
shear
rate,
but
to
its
nth
power.
Therefore,
these
type
of
fluids
are
called
as
power
law
fluids.
The
equation
of
flow
behavior
is:
Tt
=KyN
8)
where
K
=
Consistency
Index,
Ibf-s/100
ft2
n
=
Flow
behavior
index,
dimensionless
T
1
2
3
1.
Bingham
Plastic
Fluid
2.
Power
Law
Fluid
3.
Newtonian
Fluid
16
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Determination
of
Flow
Behavior
Model
Parameters
Using
a
Rotational
Viscometer:
Rotational
viscometers
are
used
in
the
standard
API
diagnostic
tests
to
determine
flow
behavior
model
parameters
of
drilling
fluids.
These
determinations
are
carried
out
in
a
6
Speed
Fann
Viscometer
according
to
APl
RP13B.
Fann
Viscometer
readings
can
be
correlated
to
the
shear
stress
and
shear
rate as
follows.
Shear
Stress:
t
=1.0676
9)
where
6
:
Dial
(viscometer)
reading
corresponding
to
the
applied
shear
rate
(i.e.
rotating
speed)
Shear
Rate:
y
=1.703
N
(10)
N
:
Viscometer
rotating
speed,
RPM
Flow
behavior
parameters
can
be
determined
by
using
Fann
Viscometer
readings
as
follows
;
Plastic
Viscosity
(PV):
L
p=9600-9300:
cP.
(11)
8
o0
=
Fann
Reading
at
600 rpm
8
300
=
Fann
Reading
at
300 rpm
Yield-point
(YP):
To=8a00
-
e,
Ibf/100
ft
2
(12)
[¢]
300
p
_
0
600
Flow
Behavior
Index
(n):
n=3.32log
—=
(13)
300
510
6
Consistency
Index
(K):
K
=
(51—1),,
,
equivalent
cP.
(14)
Apparent
Viscosity:
The
apparent
viscosity,
p
5,
of
drilling
fluids
and
cement
slurries
is
to
be
determined,
in
accordance
with
APl
standard.
If
u 4
is
expressed
in
centipoises:
(15)
HéOO
o
17
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Gel
Strength:
Thixotropy
(i.e.
change
in
rheological
behavior
as
a
function
of
time)
can
be
estimated
by
observing
the
changes
in
strength
taking
place
in
a
gel
as
function
of
time.
According
to
APl
RP
13
B,
two
values,
the
10
second
gel-strength
and
the
10
minute
gel-strength,
are
determined
in
6-speed
Fann
Viscometer.
The
rotor
is
run
at
600
rpm
for
30
sec.
then,
the
motor
is
stopped
for
10
sec.,
and
after
10
sec.
have
elapsed,
the
rotor
is
run
at
3
rpm
speed
and
the
corresponding
scale
deflection
is
noted
as
10
sec.
gel-strength,
in
Ibf/100
ft
2.
A
period
of
10
min.
is
allowed
to
elapse
without
disturbing
the
mud,
and
the
operation
is
repeated.
The
maximum
scale
deflection
is
equal
to
the
10
minute
gel-strength
in
Ibf/100
ft
2
Selection
of
Model
The
rheological
model
chosen
will
be
a)
Closest
to
the
Bingham
model,
or
b)
Closest
to
the
Power-Law
model
In
most
cases
it
is
impossible
to
make
this
choice
on
the
shape
of
the
curve
alone,
whether
plotted
in
Cartesian
or
in
Logarithmic
Coordinates.
A
6
speed
Fann
Viscometer
provides
only
4
experimental
points
because
the
readings
at
3
and
6
rpm
cannot
be
used
if
the
fluid
has
a
yield
point
(plug
flow)
or
if
it
is
thixotropic.
The
four
experimental
points
may
be
used
for
linear
regression,
in
Cartesian
and
in
logarithmic
coordinates
corresponding
to
Bingham
Plastic
model
and
Power
Law
model
respectively.
The
model
with
correlation
coefficient
closest
to
unity
will
be
chosen
for
subsequent
calculation.
This
correlation
coefficient
is
given
by
the
following
equation:
=
PZxy-Zx
Xy
Y[pzx2-(zx2][Pzy2-(2y?]
(16)
where
,
P
is
the
number
of
Fann
readings
made
x
is
the
shear
rate
or
its
logarithm
(
y
or
logy)
y
is
the
shear
stress
or
its
logarithm
(
z
or
log
)
18
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EXPERIMENTAL
PROCEDURE
1.
Calibrate
the
mud
balance
with
tap
water
at
room
temperature.
2.
Place
350
mi.
of
water
in
the
blender
can,
a
little
at
a
time
to
avoid
spillage
while
mixing.
NOTE:
All
mud
samples
made
are
based
on
350
cc.
of
water.
By
convention,
the
volume
of
water
is
to
be
measured
when
the
bottom
of
the
interface
lies
on
top
of
the
350
cc.
mark.
3.
Add
30
grams
of
bentonite
while
mixing.
Add
the
bentonite
slowly,
a
bit at
a
time,
and
definitely
not
all
at
once.
Stir
for
5
minutes
at
medium
speed.
If
the
speed
is
too
high,
the
mud
may
spill
out
and
result
in
a
loss
of
sample.
4.
Record
the
mud
temperature.
5.
Measure
the
mud
density
using
the
mud
balance,
ppg
to
2
decimals,
SG
{gm/cc)
to
3
decimals.
6.
Place
the
mud
in
a
Fann
Viscometer,
measure
and record
the
600,
300,
200,
100,
and
6
rpm
readings.
Note
that
at
6
rpm
the
reading
could
be
higher
than
it
should
be
because
of
the
effect
of
“gelling”,
whereby
the
rpm’s
aren't
powerful
enough
to
put
the
mud
into
a
liquid
state.
Discard
this
value
if
the
mud
appears
to
gel,
use
this
value
only
if
it
enhances
the
data.
7.
Determine
the
10
second
and
10
minute
gel
strengths.
Remember,
gel
strength
readings
are
taken
at
3
rpm’s.
Refer
to
top
of
page
18
for
information
on
how
to
perform
a
gel
strength.
8.
Repeat
steps
1
to
7
using
3
grams
of
Xanthan
Gum
instead
of
bentonite
as
a
viscosifier.
Lab
Report
and
Data
Reduction
1)
Plot
the
rheograms
of
Bentonite
and
Xanthan
Gum
solutions
(i.e.
shear
stress
vs.
shear
rate
diagrams)
2)
Select
the
model
which
fits
closest
to
the
rheological
behaviors
of
Bentonite
and
XG
solutions
3)
Determine
the
flow
behavior
parameters
of
the
models
selected
at
step
2.
19
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EXPERIMENT
TWO
FILTRATION
PROPERTIES
OF
WATER-BASED
DRILLING
FLUIDS
OBJECTIVES:
Determine
the
effect
of
clay
and
water
soluble
polymers
on
(API)
filtration
loss
characteristics
of
water-
based
drilling
fluids.
INTRODUCTION
One
of
the
most
important
functions
of
the
drilling
fluid
is
to
"control
filtrate
loss
into
the
formation".
This
is
important
for
several
reasons:
1.
The
Filtrate
lost
to
the
formation
must
be
made
up
at
the
surface
to
maintain
the
desired
mud
volume.
2.
The
filtrate
lost
to
the
formation
will
affect
the
logs
obtained
after
the
hole
is
drilled.
For
example,
the
filtrate
can
flush
hydrocarbons
from
the
rock
changing
the
in-situ
saturations
and
changing
the
resistivity
of
the
formation
water
near
the
well
bore.
3.
The
filtrate
lost
to
the
formation
can
react
with
clays
in
the
formation
rock
and
cause
irreversible
formation
damage
near
the
well
bore.
This
is
referred
to
as
"skin
effect”
when
the
permeability
next
to
the
well
bore
is
reduced
to
a
very
low
value
compared
to
the
rest
of
the
reservoir.
4.
The
filtrate
lost
to
the
formation
leaves
the
solid
portion
of
the
mud
behind,
deposited
on
the
wall
of
the
hole.
This
deposit
can
become
sufficiently
thick
to
stick
the
drill
string
or
casing.
When
the
mud
system
is
circulating
(dynamic
filtration)
the
mud
cake
tends
to
wash away
and
is
not
as
big
a
problem
as
when
circulation
is
stopped
(static
filtration).
In
this
experiment
you
will
investigate
static
filtration
using
a
standard
API
filter
press
with
a
filtrate
area
equal
to
45.8
cm”.
Specifically
you
will
investigate
the
effect
of
time
on
filtrate
loss
and
filter
cake
thickness.
You
will
also
observe
several
methods
used
in
the
field
to
control
filtrate
loss.
Consider
a
unit
volume
of
mud
that
contains
x
fraction
of
filtrate.
The
volume
of
non-filtrate
that
will
be
deposited
against
the
side
of
the
hole
is
then
equal
to
(1-x).
Therefore
if
V.
is
the
volume
of
filter
cake
and
Vi
is
the
volume
of
filtrate;
2.1)
=
e
20
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If
the
filter
cake
is
deposited
on
a
unit
area
then
the
thickness
of
the
cake
(h)
after
time
period
(t)
is
equal
to;
2.2)
h
=
-
Vi
where
V;
is
the
volume
of
filtrate
that
is
filtered
through
a
unit
area.
Darcy's
law
states
that;
dvi
kAP
(2.3)
e
dt
uh
where:
k
=
permeability
in
darcies
AP
=
differential
pressure
in
atm
n
=
viscosity
of
filtrate
in
cP
h
=
cake
thickness
in
mm
Substituting
Equation
(2.2)
into
Equation
(2.3),
separating
variables
and
performing
the
integration;
Vé
kAP
x
24)
=
e
()
t
2
po
1x
Solving
for
the
volume
of
filtrate
per
unit
area
as
a
function
of
time;
(2.5)
Vi
=B
(1)"?
2
kAPx
where
B=[-meomeeee
]1/2
r(1-x)
This
states
that
the
filtrate
that
flows
through
the
filter
cake
is
proportional
to
the
square
root
of
time.
You
should
notice
that
the
terms
in
(B)
are
not
time
dependent.
The
term
k
is
controlied
by
the
size
distribution
and
type
of
material
in
the
non
filtrate
portion
of
the
mud.
The
relationship
between
pressure
and
filtrate
volume
is
not as
easily
defined
as
the
relationship
between
filtrate
volume
and
time.
However
it
can
be
stated
that
the
filtrate
volume
is
proportional
to
the
pressure
raised
to
some
power,
i.e.,
21
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(2.6)
Vy
is
proportional
to
P¥
Notice
that
y
cannot
have
a
value
greater
than
0.5.
For
example,
if
the
filter
cake
is
non-compressible,
i.e.,
k
remains
constant
for
any
pressure,
then
y
is
equal
to
0.5
as
predicted
by
Equation
(3.5).
On
the
other
hand,
if
the
filter
cake
is
compressible,
which
is
usually
the
case,
then
k
will
decrease
with
an
increase
in
P
and
the
final
result
will
be
that
y
is
less
than
0.5.
In
a
severe
case
y
can
have
a
negative
value.
AP
Filtrate
Loss
is
defined
as
the
volume
of
filtrate
collected
in
30
minutes
from
a
standard
filter
press
when
a
pressure
of
one
hundred
psi
is
applied.
Spurt
Loss
is
the
amount
of
filtrate
volume
at
time
zero.
EXPERIMENTAL
PROCEDURE
1.
Mix
the
following
samples
using
tap
water
and
stir
for
10
minutes
at
medium
speed.
NOTE:
All
mud
samples
made
are
based
on
350
cc.
of
water.
By
convention,
the
volume
of
water
is_to
be
measured
when
the
bottom
of
the
interface
lies
on
top
of
the
350
cc.
mark.
Add
the
bentonite
slowly,
a
bit
at
a
time,
and
definitely
not
all
at
once.
6%
bentonite
by
weight
6%
sepiolite
by
weight
9%
bentonite
by
weight
9%
bentonite
by
weight
plus
1
Ibm/bbl
bio-polymer
(QUIK-TROL)
9%
bentonite
by
weight
plus
6
Ibm/bbl
polyphosphate
(BARAFOS)
See
step
3
below
~poooow
Note
that
when
making
350
cc.
of
mud,
1
Ibm/bbl
is
equal
to
1
gram.
2.
Measure
the
filtrate
volume
versus
time
at
100
psig
of
the
samples
(a)
to
(e)
above.
After
the
filtration
test,
which
lasts
for
30
minutes,
measure
the
mud
cake
thickness
of
these
5
samples.
The
thickness
must
be
reported
as
32nds
of
an
inch.
Take
more
than
one
reading
and
average
them.
3.
Make
another
sample
just
like
that
in
(1e)
above.
Measure
the
filtrate
volume
at
50
psig,
and
the
mud
cake
thickness.
22
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DATA
REDUCTION
AND
LAB
REPORT
1.
Plot
filtrate
volume
(measured
at
100
psi)
of
all
5
samples
on
the
same
graph
paper
versus
time
and
versus
square
root
of
time.
Does
the
theoretical
relationship
of
filtrate
volume
proportional
to
the
square
root
of
time
hold?
2.
Calculate
spurt
foss
using
7.5
min.
and
30
min.
data.
Determine
AP|
water
loss
and
mud
cake thickness
for
each
sample
and display
the
results
in
a
table.
3.
Discuss
the
effectiveness
of
bentonite,
sepiolite,
bio-polymer
and
polyphosphate
as
filtration
control
additives.
Also
discuss
the
type
of
mud
cake
observed
for
each
additive.
4.
What
value
of
"y"
(Equation
2.6)
did
you
obtain
for
your
polyphosphate
mud
system?
Explain
how
you
obtained
the
value
of
"y"
and
what
the
physical
significance
of
the
number
is.
Time
VTime
Filtrate
Volume,
m!
6%
6%
9%
9%
9%
9%
i
i
Bentonite
Sepiolite
Bentonite
|
Bentonite
+
|
Bentonite
+
|
Bentonite+
Quik-Trol
Barafos
Barafos
@
50
psi
0.25
1
2
3
4
5
6
7.5
10
20
30
23
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THE
INTERMEDIATE
HOLE
Experiments
3
and
4
pertain
to
the
drilling
fluid
design
for
intermediate
hole.
In
Experiment
3,
the
student
will
study
preparation
and
solids
analysis
of
weighted
mud
systems.
In
Experiment
4,
the
students
will
learn
about
identification
and
treatment
of
salt
contaminated
muds.
WEIGHTING
UP
MUD:
Solids
in
weighted
mud
systems
When
weighting
up
a
drilling
fluid
one
should
be
able
to
calculate
the
following:
a-)
The
volume
increase
due
to
barite
addition
without
water
addition.
b-)
The
weight
of
barite
necessary
for
a
particular
change
in
weight
without
water
addition.
¢-)
The
volume
to
be
discarded
due
to
volume
increase
when
adding
barite
with
water.
d-)
The
weight
of
barite
necessary
for
a
particular
change
in
weight
with
water
addition.
e-)
The
volume
of
water
to
be
added
with
the
barite
(0.01
gal/lbm).
The
equations
to
be
used
for
these
calculations
are
as
follows:
Volume
Increase
Due
To
Barite
Addition
Without
Water
Addition:
dV
=
Vi*
[
(35
-
Dom)
/
(35-
Dim)
-11
(1)
Weight
of
Barite
Required
For
Weighting
Up
Without
Water
Addition:
Mp=dV
*
1470
2
Volume
of
Mud
To Be
Discarded
Before
Weighting
Up
With
Water
Addition:
Discarded
volume
=
V4
=
V;
*
[1
-(28.0856
-Dpy)
/
(28.0856
-Dom)]
(3)
Weight
of
Barite
Required
For
Weighting
With
Water
Addition:
Mpw=
Vg
*
1088.89
4)
Volume
of
Water
to
Be
Added
With
Barite
Addition:
V=
Mp*
0.01
(5)
dV
=
Change
in
volume
due
to
dry
barite
addition
(bbls)
Vi
=
Initial
volume
(bbls)
Dom
=
Old
mud
weight
(ppg)
Dnm
=
New
mud
weight
(ppg)
Mp
=
Barite
required
without
water
Msw
=
Barite
required
with
water
addition
Vi
=
Volume
of
water
required,
gal.
24
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Table
1:
Barite
Required
to
Raise
Weight
of
100
Barrels
of
Mud
for
Different
Mud
Weights.
BARITE
REQUIRED
TO
RAISE
WEIGHT
OF
100
BARRELS
OF
MUD
(number
of
100
Ib
socks)
DESIRED
MUD
WEIGHT
(ppg)
8.0
8.5
|
9.0
9.5]10.0}10.5{11.0
|
11.5|
12,0]
12.5{
13.0]
13.5|
1n.0]
14.5]
15.0
}15.5
}16.0
|16.5
[17.0
7.5
|18.0
35
)
6u
9
|
125)
1090
1ot
231
]
271
313]
3577
4os|
wssi
509
s67
|
6304
(27
|
720
1
g9
|
93n
jozs
ii3p
Il
7.35
-
|28
57
871
120
154
190
|
228]
269]
312|
358|
407{
ue0|
S16|
5761
641
|
212
|
788
|
872
|
962
11052
8.0
g
28
S8
90f
123
1584
196]
235|
77|
322|
370
21|
76|
5351
509
|
667
[
7u2
|
823
|
912
|ioos
8.5
17
4r]
78|
111
w6
)
183|
222f
26u)
308y
355)
406|
w60
|
519
582
|
650
)
723
|
804
[891
|98
||
87
29)
60|
92|
127
{
163)
202
2u3]
286)
333
383
436
|
49u
|
5%
|
623
|
696
|
725
[
861
[
ase
||
9.0
30y
621
95|
130;
168;
208)
251|
2964
3u5|
397
|
453
|
513
|
578
|
649
|
226
|
810
|
903
i
9.5
31|
63
98|
34|
173
215}
259
306|
3571
412
[
420
[
S34
|
603
|
678
|
760
{
850
[10.0
32
65)
101]
139|
19|
222|
268|
317
370
|
u2s
|
wse
|
567
[
629
{708
[
796
{10.5
330
67
dou|
1u3)
15|
230)
28|
329
|
385
|
wes
|
s10
|
581
{ess
{73
[11.0
values
not
Listed
tn
the
table
con
be
30
69|
107(
148|
19)|
238
|
288
|
3u2
|
uoo
{
usu
|
533
|
608
|
690
|{11.
=
|2
comouted
using
the
followlng
equation:
.
¥
35
72|
111}
153}
198
|
247
299
|
356
|
417
|
wau_[
557
|
637
112.0
;g_g
A
=
1099
X
MUD
WT.
[NCREASE
se|
2l
11|
is9|
206§
257
|
su
{3
Juse
|sos
|
smw
f1os
|E
n
B
37
77|
118
165
|
2tu
[
267
|
325
|
387
[4s6
|
s31
[|13.0
Q
=
28.35
-
N
&
EW
MUD
4.
38
91
123
|
170
| 222
|
278
|
339
[u0S
|
478
|[13.S
’?‘0*5
=
AsB
uo
)
82
|
128
|
17
|
232
|
291
|
355
|
w5
|1w0
ul
86
|
133
|
186
|
242
{304
|
372
[14.5
The
above
equation
and
the
values
In
the
table
are
based
H
89
|
139
119
1255
|31
fi1b.0
on
the
ossumption
that
one
gatlon
of
woter
will
be
odued
4o
|
93
|
145
1203
|
265
11155
with
each
seck
(100
Ib)
of
borite
used
in
welghting
up.
a6
97
|15
|
212
[16.0
48
1101
|
199
i16.5
Total
Mud
Volume
Increase
bbl
S1
|
106
11170
(0.091
x
Total
Sacks
of
Barite
Required)
53
jj1.s
_J
A
common
problem
with
intermediate
weight
muds,
especially
in
the
12
to
13
ppg
range,
is
differential
sticking,
lost
returns,
and
high
treating
costs.
Most
often
these
problems
can
be
traced
back
to
excess
solids.
Solids
are
difficult
to
control
in
intermediate
weight
muds
because
of
a
lack
of
mechanical
equipment.
Desanders,
desilters
and
shale
shakers
are
used
to
remove
unwanted
drill
solids
from
low
weight
muds
(muds
that
contain
no
barite).
Solids
control
in
weighted
muds
is
achieved
by
the
use
of
centrifuges
and
fine
screen
shale
shakers.
There
is
no
mechanical
equipment
available
for
removing
solids
from
intermediate
muds
(10-13
ppg)
other
than
shale
shakers.
Consequently,
the
mud
used
to
drill
this
section
of
the
well
is
difficult
to
control
and
excessive
chemicals
and/or
dilution
will
be
used.
In
addition,
this
mud
is
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usually
used
as
a
base
for
higher
weight
muds
used
to
drill
the
remainder
of
the
well
after
protection
pipe
is
set.
Use
of
a
poor
base
mud
to
build
a
weighted
system
will
increase
treating
costs
and
may
contribute
to
other
problems
such
as
lost
returns,
stuck
pipe,
etc.
Sand
and
drill
solids
greatly
affect
the
lubricity
of
both
the
fluid
and
the
wall
cake.
This
in
turn
seriously
affects
the
torque
and
drag
of
the
pipe
in
the
hole.
The
type
of
solids
and
the
abrasiveness
of
the
solids
in
the
filter
cake
are
also
important
factors
here
since
the
coefficient
of
friction
of
the
filter
cake
severely
affects
the
force
required
to
move
the
pipe
on
its
surface.
The
overpull
required
to
move
the
pipe
can
be
calculated
with
the
following
equation:
Overpull
(Ibf)
=
Differential
Pressure
(psi)*
Area
(in2)*
Coefficient
of
Friction
6)
F"
R
R
e
)
d
Wellbore
Resenvolt
Pressure
Figure
1:
Differential
sticking
(Schlumberger
Oilfield
Glossary
Website
&
Scribd
Website)
For
a
fixed
differential
the
over
pull
required
to
move
the
pipe
is
directly
proportional
to
both
the
contact
area
and
the
coefficient
of
friction.
The
contact
area
increases
with
an
increase
in
filter
cake
thickness.
The
coefficient
of
friction
changes
with
the
lubricity
of
the
fluid
and
the
abrasiveness
of
the
solids
making
up
the
wall
cake.
For
example
assuming
a
400
psi
differential
pressure
across
a
10
ft.
permeable
section
in
a
9-7/8
inch
hole
with
7-1/4
inch
drill
collars
the
over
pull
required
for
different
wall
cake
thickness,
using
the
above
equation
are:
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For
a
cake thickness
of
2/32"
The
over
pull
at
.2
coefficient
of
friction
=
27,456
Lbs
The
over
pull
at
.4
coefficient
of
friction
=
54,912
Lbs
For
a
cake
thickness
of
1/8"
The
over
pull
at
.2
coefficient
of
friction
=
35,616
Lbs
The
over
pull
at
.4
coefficient
of
friction
=
71,232
Lbs
For
a
cake
thickness
of
1/4"
The
over
pull
at
.2
coefficient
of
friction
=
50,592
Lbs
The
over
pull
at
.4
coefficient
of
friction
=
101,184
Lbs
For
a
cake
thickness
of
1/2"
The
over
pull
at
.2
coefficient
of
friction
=
72,288
Lbs
The
over
pull
at
.4
coefficient
of
friction
=
144,576
Lbs
For
a
cake
thickness
of
1"
The
over
pull
at
.2
coefficient
of
friction
=
104,640
Lbs
The
over
pull
at
.4
coefficient
of
friction
=
209,280
.Lbs
SOLIDS
BUILDUP
EFFECTS
AND
ANALYSIS
In
a
mud
system
there
are
several
different
types
of
solids
present.
These
are
salts,
commercial
clays,
weighting
material
and
drill
solids.
When
active
clays
are
drilled
they
become
dispersed
in
the
mud
causing
an
increase
in
the solids,
plastic
viscosity,
yield
point,
gels
and
mud
weight.
Evaluation
of
the
percent
solids
in
the
system
can
be
achieved
by
performing
a
retort
analysis.
Evaluation
of
the
concentration
of
commercial
bentonite
can
be
achieved
by
performing
a
methylene
blue
test.
A
high
MBT
can
signify
a
high
concentration
of
active
clays.
It
also
can
still
be
associated
with
other
contaminants
such
as
brine,
cement
or
lime,
hydrogen
sulphide
and
carbon
dioxide.
The
key
however,
lies
in
the
fact
that
other
chemical
contaminations
will
not
increase
the
solids
content
and
plastic
viscosity.
The
MBT
test
is
used
to
confirm
that
the
increase
in
solids
is
due
to
active
clays.
Inert
drill
solids
cause
an
increase
in
plastic
viscosity,
water
loss,
total
solids
and
mud
weight.
An
increase
in
the
yield
point
is
associated
with
either
high
temperature
or
chemical
action.
Based
on
this
any
increase
in
plastic
viscosity,
mud
weight,
solids
and
fluid
loss
without
an
increase
in
yield
point
can
be
safely
attributed
to
a
buildup
of
inert
drill
solids.
An
accompanying
increase
in
yield
point
signifies
the
presence
of
a
chemical
or
temperature
problem.
Flow
line
temperatures
are
readily
available
and
can
be
checked
at
any
time.
Usually
drill
solids
will
cause
an
increase
in
the
plastic
viscosity
due
to
the
increased
number
of
free
particles.
This
increase
in
plastic
viscosity
'will
result
in
greater
annular
pressure
losses,
greater
equivalent
circulating
densities,
loss
circulation
and
decreased
drilling
rate.
For
most
bit
conditions,
when
all
other
parameters
are
held
constant,
the
penetration
rate
varies
to
the
0.45
power
of
the
Reynold's
Number.
This
can
be
stated
as
follows:
27
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New
drilling
rate
=
Old
drilling
rate
*
(New
Re/Old
Re)***
(7)
But
the
Reynold's
Number
is
indirectly
proportional
to
plastic
viscosity
(PV)
resulting
in
the
following:
New
drilling
rate
=
OId
drilling
rate
*
(Old
PV/New
PV)**°
(8)
The
following
graph
shows
the
effect
of
PV
(cp)
on
the
drilling
rate
(ft/hr).
Here
we
can
see
the
decrease
in
drilling
rate
with
the
increase
in
PV.
Drilling
rate
vs
Plastic
viscosity
120
115
110
1
-
-
-
E
L
.
=
105
1
te
in
Dril
w
(4]
20
25
30
35
40
Plastic
viscosity
Figure
2:
Drilling
rate
vs.
Plastic
Viscosity
A
buildup
of
solids
in
intermediate
weight
muds
is
almost
unavoidable
with
the
present
mechanical
equipment
and
some
dilution
is
necessary.
Desanders
and
desilters
generally
cannot
be
used
because
of
the
loss
of
almost
all
barite.
Centrifuges
will
salvage
most
of
the
barite
but
they
have
limited
capacity
and
cannot
process
sufficient
volume
to
keep
up.
If
mud
is
to
be
used
as
a
base
for
building
higher
weight
muds,
then
reducing
drill
solids
is
a
must.
Do
not
attempt
to
treat
a
solids
problem
with
chemical.
Consider
the
use
of
two
centrifuges
if
a
significant
amount
of
hole
is
to
be
drilled
with
an
11
to
13
Ib/gal
mud.
Screen
all
of
the
returns
through
an
80
mesh
screen.
Install
two
shakers
if
one
will
not
handle
the
volume.
Use
dilution
if
necessary
to
keep
the
drill
solids
at
an
acceptable
level.
Do
not
build
a
weighted
system
on
a
poor
base.
28
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EXPERIMENT
THREE
MUD
WEIGHT
-
WEIGHT
CONTROL
-
SOLIDS
DETERMINATION
OBJECTIVES:
»
Introduce
the
concept
of
drilling
fluid
weight
control.
»
Determine
the
effect
of
barite
on
the
rheological
properties
of
water
base
drilling
fluids.
»
Determine
solid
content
of
the
drilling
fluid
using
API
retort
test.
INTRODUCTION
A
primary
function
of
the
drilling
fluid
is
to
control,
or
hold
back,
the
formation
pressure
while
you
are
drilling
the
wellbore.
This
is
accomplished
by
adjusting
the
specific
gravity
of
the
drilling
fluid
so
the
pressure
gradient
of
the
drilling
fluid
within
the
wellbore
exceeds
the
pressure
gradient
of
the
fluid
in
the
formation.
The
specific
gravity
of
the
drilling
fluid
is
increased
by
adding
solids
to
the
drilling
fluid.
The
rheology
of
drilling
fluid
must
be
such
that
the
solids
will
be
held
in
suspension.
Two
major
considerations
occur
as
the
specific
gravity
of
the
drilling
fluid
is
increased.
The
first
consideration
is
that
the
pressure
gradient
in
the
wellbore
not
exceeds
the
fracture
gradient
of
the
formation.
The
second
consideration
is
how
the
solids
added
to
the
drilling
fluid
effect
the
rheology
and
filtrate
properties
of
the
drilling
fluid.
The
surface
area
of
the
solids
in
the
drilling
fluid
has
a
major
effect
on
the
viscosity
of
the
drilling
fluid.
Consequently,
when
increasing
the
specific
gravity
of
the
drilling
fluid,
the
denser
the
solids
added,
the
smaller
the
rheology
change
observed.
For
this
reason,
barite
(sp.gr.
4.2)
is
preferred
to
increase
the
specific
gravity
of
drilling
fluid
instead
of
the
drill
cuttings
(sp.
gr.
2.65).
Mud
that
contains
barite
is
referred
to
as
weighted
mud
and
mud
that
does
not
contain
barite
is
referred
to
as
low
weight
mud.
The
solids
content
of
low
weight
mud
can
be
determined
directly
from
the
mud
weight
without
using
a
mud
retort
provided
there
is
no
oil
in
the
mud
system.
To
determine
the
solids
content
of
weighted
mud,
a
retort
analysis
is
always
required
unless
no
low
solids
are
present,
which
is
seldom
the
case.
In
figure
1,
you
will
find
a
nomograph
that
will
assist
you
in
determining
the
percentage
of
low
solids
and
the
percentage
of
high
solids
in
a
weighted
mud.
29
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EXPERIMENTAL
PROCEDURE
1.
Put
350
cc.
of
water
in
your
container,
a
bit
at
a
time.
2.
Add
bentonite
(a
bit
at
a
time)
to
the
water
according
to
the
values
in
Table
1,
page
33
(a
new
mud
each
time)
and
mix
for
7
minutes.
Record
the
600
RPM
and
the
300RPM
reading
until
apparent
viscosity
(Ja
which
is
Qgp0/2),
reaches
a
value
between
15
and
20.
3.
Only
measure
the
mud
weight
and
10
second
gel
strength
when
Ogg0/2
reaches
the
above
value.
4.
The
600
and
300
rpm
viscometer
readings
are
needed
to
calculate
PV
and
YP.
5.
Estimate
and
record
the
amount
of
barite
(in
grams)
that
should
be
added
to
your
mud
to
increase
the
density
to
9.5
ppg.
Use
the
table
named
“Barite
Required
to
Raise
Weight
of
100
Barrels
of
Mud”
(page25).
In
the
report,
calculate
the
exact
amount
from
first
principles.
6.
Add
the
estimated
barite
to
your
mud
(an
entirely
new
sample),
mix
for
10
minutes
and
measure
the
mud
weight.
The
mud
weight
should
be
very
close
to
9.5
ppg.
7.
Measure
the
10
second
gel
strength.
8.
Record
the
300
and
600
RPM
viscometer
readings
to
calculate
PV
and
YP.
9.
Use
the
mud
retort
to
determine
the
low
solids
and
high
solids
concentration.
Apply
the
following
procedure:
a)
Disassemble
retort
assembly
and
fill
sample
cup
almost
level
full
of
the
fluid
to
be
tested.
Put
sample
cup
cover
in
place
firmly,
squeezing
out
excess
fluid
to
obtain
the
exact
10
cc
volume
required.
Clean
spill
over
from
cover
and
threads.
(If
threads
are
coated
with
silicone
grease,
it
will
prevent
sticking.)
b)
Lift
cover
slightly
and
slide
off
so
that
fluid
adhering
to
bottom
surface
will
be
scraped
back
into
the
sample
cup.
c)
To
prevent
boil
over,
fill
the
expansion
chamber
with
“steel
wool".
d)
Select
correct
heater
assembly
for
the
available
voltage
and
screw
into
top
of
expansion
chamber.
Keep
assembly
upright
so
that
mud
does
not
slosh
into
the
drain tube.
e)
Insert
drain
tube
into
hole
at
the
end
of
condenser,
seating
firmly.
Percentage
graduated
cylinder
should
be
clipped
in
place
to
catch
condensate.
30
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9
h)
)
10.
Plug
in
the
correct
connector
cord
to
the
power
supply
and
keep
power
on
until
distillation
stops
which
should
occur
in
15
to
25
minutes
depending
on
the
characteristics
of
solids
content
and
the
atmosphere
around
the
unit.
Read
the
amount
of
water
directly
from
the
graduated
cylinder.
At
end
of
test,
grasp
rubber
covered
connector
just
above
heater
and
separate
retort
assembly
from
condenser.
Handling
the
hot
retort
by
means
of
the
connector
cord,
dip
in
water
to
cool.
(Piug
is
waterproof
and
may
be
immersed
completely.)
Most
of
the
solids
remaining
in
retort
will
adhere
to
the
heater
where
removal
is
easy.
Use
spatula
to
scrape
out
cup
and
expansion
chamber.
Run
short
length
of
pipe
cleaner
through
condenser
hole
and
retort
drain
tube
to
remove
oil
residue.
The
specific
gravity
of
mud
solids
can
be
obtained
by
the
following
formulas.
Sp.Gr.Solids
=
[
100*Sp.Gr.Mud
-
(vol%water)
]/
(vol%solids)
Sp.Gr.Mud
=
MW(ppg)/8.33
or
Sp.Gr.Mud
=
MW(Ibm
per
cuft)/62.4
All
percentages
are
volume
percentages.
Enter
Fig.1
(page
32)
from
y
axis
with
Sp.Gr.
of
Solids
and
read
the
weight
%
of
high
gravity
solids
and
calculate
weight
%
of
low
gravity
solids
(100
—
Weight
%
of
High
Gravity
Solids).
DATA
REDUCTION
AND
LAB
REPORT
1.
2.
Discuss
the
effect
of
adding
barite
on
drilling
fluid
properties
measured.
Discuss
your
results
from
retort
analysis
(i.e.),
compare
your
retort
analysis
results
and
recorded
barite
and
bentonite
amounts
obtained
during
the
preparation
of
9.5
ppg
mud.
Soive
the
following
field
problem:
Surface
casing
13
3/8",
72
Ib/ft
(ID:
12.347
in.),
set
at
3,000’
Open
hole
11"
at
a
measured
depth
8,000’
Three
mud
tanks
each
has
8'
depth
*
8'
width
*
10’
length
full
of
mud.
The
drill
string
at
total
depth)
DP
4
1/2",
20
Ib/ft,
(ID:
3.64”)
DC
7"
x
3.5",
98
Ib/ft,
500'
31
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Questions:
1.
Determine
the
total
volume
of
mud
in
the
system
(i.e.,
mud
in
tank
+
mud
in
well).
2.
How
many
bbls
of
fluid
must
enter
the
wellbore
from
the
formation
to
increase
the
level
of
fluid
in
mud
tanks
(pits)
by
2"?
3.
You
are the
engineer
in
charge
of
this
drilling
rig.
You
have
sent
the
mud
engineer
to
town
for
a
brown
pop.
He
wrecked
the
pickup
so
he
will
not
be
back
to
help you.
While
you
were
taking
your
afternoon
nap
the
mud
got
into
the
shape
found
in
step
2
above.
The
tool
pusher
has
just
awakened
you
and
informed
you
the
well
is
kicking
and
the
mud
weight
should
immediately
be
increased
to
10.5 ppg.
Calculate
the
number
of
sacks
of
(100
Ibm)
barite
required
to
change
the
mud
system.
43
37
v
35
3.3
Mud
Solids
Specific
Gravity
27
"
0
20
40
60
80
100
120
Weight
%
High
Gravity
Solids
Figure-1:
Relative
Amount
of
Barite
and
Lower
Specific
Gravity
Solids
in
the
Suspended
Solids
32
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TABLE-1
Viscometer
Reading
Clay,
grams
300
RPM
600
RPM
5
10
15
20
25
30
35
40
33
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EXPERIMENT
FOUR
IDENTIFICATION
AND
TREATMENT
OF
SALT
CONTAMINATED
DRILLING
FLUIDS
OBJECTIVES:
Identify
and
treat
salt
contaminated
drilling
fluids.
INTRODUCTION
This
experiment
is
designed
to
familiarize
the
student
with
the
problems
associated
with
different
salts
and
the
treatment
necessary
to
alleviate
same.
Recommendation:
The
system
should
be
pre-treated
with
thinner
(i.e.
lignite,
phosphate,
etc.)
for
inhibition
against
brine
intrusion
and
loss
of
circulation.
Following
this
pre-treatment,
monitor
the
system
for
increase
in
circulating
pressure,
yield
point,
funnel
viscosity,
water
loss,
chlorides,
decrease
in
pit
volume,
flow
rate,
pH,
Pm,
and
Pf.
Such
monitoring
will
insure
early
identification
and
readiness
to
combat
the
effects
of
mud
contamination.
A
change
in
any
of
these
parameters
must
be
followed
by
pilot
testing
and
additional
treatment
accordingly.
The
first
indication
will
be an
increase
in
circulating
pressure
while
drilling.
As such,
the
drilling
crews
should
be on
the
look-out
for
this
sign.
Brine
intrusion
will
greatly
increase
our
chances
of
lost
circulation
due
to
annular
flocculation.
This
will
cause
an
increase
in
water
loss,
yield
point,
and
gels,
but
a
decrease
in
plastic
viscosity.
Successful
drilling
at
this
point
will
depend
on
successful
maintenance
of
an
inhibited
mud
system.
Additional
guidelines
for
safe
drilling
are
as
follows:
1.
At
the
first
sight
of
pressure
increase,
pickup
30
feet
and
circulate
bottoms
up.
2.
Perform
a
chloride
test
at
bottoms
up,
and
before
drilling
ahead
treat
the
mud
with
a
thinner
as
dictated
by
your
pilot
test.
If
the
chloride
count
increases
too
high
for
economic
treatment,
dump
and
add
new
mud
such
that
the
total
chlorides
stay
in
line
with
that
required
for
an
economically
controllable
contaminated
fresh
water
system.
3.
Always
rotate
the
pipe
first
to
break
the
gels
before
putting
the
pump
on.
Calculate
the
surge
pressures,
based
on
the
actual
rheological
properties.
Use
these
calculated
results
to
determine
the
pipe
speed
necessary
to
avoid
breakdown
while
running
in
the
hole,
during
connections,
and
during
trips.
Dress
the
bit
with
larger
nozzles
to
reduce
the
surge
and
swab
pressures
and
also
to
facilitate
spotting
of
lost
circulation
material
if
necessary.
Two
jets
with
one
blank
will
satisfy
this
requirement
by
affording
better
cross
flow,
the
required
bit
hydraulic
horsepower,
and
larger
nozzle
sizes.
34
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4.
At
casing
point,
circulate
bottoms
up
and
perform
a
pilot
test
on
the
mud
for
treating
the
gels
prior
to
tripping.
5.
On
all
trips
in
the hole,
stop
and
break
circulation
at
the
casing
shoe
and
monitor
the
return
while
running
in.
After
leaving
the
shoe,
stop
and
break
circulation
whenever
necessary.
6.
In
case
of
lost
circulation
pull
to
the
shoe, condition
the
mud
and
run
back
in,
circulating
and
conditioning
as
many
stages
as
necessary.
7.
Condition
the
mud
thoroughly
before
running
casing
and
adopt
the
same
precautions
as
stated
for
tripping
into
the
hole.
EXPERIMENTAL
PROCEDURE
1.
Prepare
a
sample
of
base
mud
by
mixing
30
grams
of
bentonite
and
350
cc.
of
water.
Mix
for
5
minutes.
Perform
the
following
tests:
(a)
Measure
the
mud
weight,
10
second
gel,
and
the
pH
of
the
mud.
(b)
Record
the
300 and 600
RPM
viscometer
readings
to
calculate
PV
and
YP.
(c)
Measure
filtration
loss.
Since
neither
a
filter
cake
nor
spurt
loss
is
being
measured,
the
filtration
only
needs
to
be
done
for
20
minutes,
in_order
to
get
a
representative
and
comparative
value.
It
would
be
a
good
idea
to
take
readings
at
5,
7.5,
10,
and
15
minutes
as
well.
Therefore,
this
is
not
an
actual
API
filtration
loss.
Prepare
a
second
mud
by
mixing
30
grams
of
bentonite
for
5
minutes.
At
the
end
of
the
5
minutes,
add
10
ml.
of
a
150,000
mg/L
Sodium
Chloride
(NaCl)
solution.
Mix
for
3
minutes.
Perform
the
same
tests
as
in
step
2
above.
Prepare
a
third
mud
by
mixing
30
grams
of
bentonite
for
5
minutes,
and
then
adding
10
ml.
of
a
150,000
mg/L
NaCl
solution.
Mix
for
3
minutes.
Treat
the
salt
contaminated
mud
by
adding
1.0
gram
of
lignite
and
mix
for
5
minutes.
Perform
the
same
tests
as
in
step
2
above.
RESULTS:
1.
Discuss
the
effect
of
salt
contamination
on
various
mud
properties.
2.
Discuss
how
salt
contaminant
could
be
identified.
3.
Discuss
the
effectiveness
of
the
lignite
treatment
used.
35
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Base
Dirilling
Fluid
Salt
Contaminated
Drilling
Fluid
Treated
Drilling
Fluid
Plastic
Viscosity,
cp
Yield
Point,
1b/100
sq.ft
10
second
Gel
Strength
1b/100
sq.ft
Filtration
Loss
mi
pH
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EXPERIMENT
FIVE
LIME
TREATED
INHIBITIVE
DRILLING
FLUIDS
OBJECTIVES:
Study
the
preparation,
properties,
and
applications
of
inhibitive
drilling
fluids.
INTRODUCTION
Primary
consideration
for
drilling
production
holes
is
to
minimize
interaction
between
drilling
fluid
and
formation
rock.
This
is
usually
accomplished
with
the
use
of
inhibitive
water-based
drilling
fluid
systems
or
oil-based
drilling
fluids.
The
decision
which
mud
system
to
use
is
dependent
upon
sensitivity
of
drilled
rocks
to
water,
cost
of
mud,
and
disposal
cost
(toxicity).
Common
mud
contaminants
such
as
cement,
anhydrite,
or
salt
will
not
normally
affect
inhibited
fluids
as
dramatically
as
they
do
conventional
dispersed,
non-inhibited
fluids.
The
problems
caused
by
non-
pressured
heaving
shales
and
tight
hole
conditions
are
more
easily
handled.
In
general,
inhibited
systems
have
lower
viscosities
(except
in
the
high
density
ranges)
and
low
gel
strengths.
The
principal
areas
of
use
for
these
fluids
are the
drilling
of
shale
formations.
Formulation:
Water
(fresh
or
salty)
Sodium
bentonite
not
to
exceed
15
Ib/bbl
Caustic
soda
11.5-
12.0
pH
Lignite
2-
6
Ib/bbl
used
at
breakover
and
not
in
highly
weighted
systems
Lime
High
density
fluids
2-
3
I/bbl
excess
Low
density
fluids
6-
8
Ib/bbl
excess
Lignosulfonate
1-
10
Ib/bbl
Starch
or
Polymers
0.75-
3.0 Ib/bbl
Lime
muds
perform
well
up
to
350
°F,
at
which
time
the
fluid
loss
may
become
hard
to
control.
This
leads
to
dehydration
of
the
system
and
solidification
can
occur.
In
most
cases
the
calcium
inhibited
system
is
made
from
the
native
mud
used
to
drill
the
surface
hole.
Downhole
temperature
aids
in
converting
the
system
to
an
inhibited
(calcium
-bentonite)
system.
This
procedure
is
called
a
"breakover”.
Normally
there
is
a
short
period
of
time
during
the
"breakover"
where
the
viscosity
may
become
very
high.
This
is
the
"Hump",
which
is
caused
by
the
clay
flocculating
and
converting
to
calcium
clay.
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The
procedures
necessary
for
the
conversion
and
maintenance
of
a
lime
based
mud
are
as
follows.
A
mud
system
having
a
lime
concentration
that
is
numerically
equal
to
its
phenolphthalein
mud
filtrate
alkalinity
(Py)
is
the
main
objective
when
running
a
lime
based
mud.
By
doing
this,
the
chemical
analysis
of
the
methyl
orange
alkalinity
of
the
mud
filtrate,
M
and
Pf
can
be
used
to
directly
calculate
the
lime
concentration
and
the
required
treatment.
It
is
very
important
to
perform
the
conversion
in
one
circulation.
To
achieve
this,
the
surface
system
must
be
first
converted
fully
and
displaced
down
the
hole.
This
procedure
is
repeated
until
the
hole
is
completely
displaced.
It
is
advisable
to
commence
the
conversion
by
treating
the
surface
system
while
waiting
on
cement.
The
conversion
should
be
started
by
first
diluting
the
system
with
fresh
water.
Caustic
soda
is
then
slowly
added
followed
by
chrome
lignosulfonate.
The
mud
will
thicken,
after
adding
the
caustic
soda,
due
to
the
increase
in
pH,
but
the
chrome
lignosulfonate
will
subsequently
reverse
this
change.
Stop
all
additions
and
allow
the
system
to
properly
mix
for
a
while
(30
minutes).
This
mixing
will
insure
an
even
consistency
of
the
chemical
treatment
throughout
the
system.
Any
addition
of
lime
before
the
system
is
thoroughly
mixed
will
cause
thickening
and
difficulty
in
conversion.
Slowly
add
hydrated
lime
and
again
allow
the
system
to
mix
for
a
while
(30
minutes).
If
the
mud
maintains
an
increased
thickness,
further
addition
of
chrome
lignosulfonate
will
help.
After
properly
mixing
the
system,
add
CMC
and
again
allow
the
system
to
mix
for
a
while
(30
minutes).
The
treatment
of
the
surface
system
is
now
completed.
Pump-this
treated
volume
down
the
hole
and
continue
to
repeat
the
same
procedure,
treating
and
pumping
in
batches,
for
one
full
cycle.
Use
the
procedures
described
in
APl
Recommended
Practices
13B-1
(RP
13B-1)
Section
#8
to
monitor
the
lime
concentration
and
the
required
treatment.
It
is
very
important
to
maintain
the
required
treatment
during
circulation
since
the
reaction
of
the
lime
and
active
clays
take
place
down
the
hole.
Closely
monitor
and
maintain
the
pH
at
12.
Any
increase
in
pH
will
cause
and
increase
in
the
amount
of
lime
in
solution
and
will
further
cause
mud
thickening.
Precede
all
future
additions
of
lime
while
drilling
with
the
proportional
additions
of
chrome
lignosulfonate
and
thorough
mixing
of
the
system.
Always
wait
for
bottoms-up
time
before
adding
any
lime.
Doing
this
will
insure
that
the
lime
is
added
only
to
the
treated
mud
as
it
returns
to
surface.
It
is
for
this
purpose
that
a
free
lime
concentration
is
maintained.
As
the
lime
in
solution
expends
downhole,
the
free
lime
goes
into
solution
giving
time
for
replenishment
of
the
free
lime
while
drilling.
This
is
a
very
delicate
system
to
control
and
require
extreme
care.
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EXPERIMENTAL
PROCEDURE
1.
N
Prepare
a
sample
of
base
mud
by
mixing
25
grams
of
bentonite
with
350
cc.
of
water
for
7
minutes.
.
Perform
the
following
test
on
the
base
mud:
(a)
Measure
the
mud
weight,
10
second
gel,
and
the
pH.
(b)
Carry
out
the
alkalinity
tests
by
determining
Pn,
Ps
,and
M;
(see
below,
Alkalinity
Determinations)
(c)
Record
the
300
and
600
RPM
viscometer
readings
in
order
to
calculate
PV
and
YP.
(d)
Measure
the
filtration
loss.
Since
neither
a
filter
cake
nor
spurt
loss
is
being
measured,
the
filtration
only
needs
to
be
done
for
20
minutes,
in_order
to
get
a
representative
and
comparative
value.
It
would
be
a
good
idea
to
take
readings
at
5,
7.5,
10,
and
15
minutes
as
well.
Therefore,
this
is
not
an
actual
AP!
filtration
loss.
Prepare
a
second
mud
by
again
mixing
25
grams
of
bentonite
with
350
cc.
of
water.
Dilute
270
ml.
of
this
mud
with
80
ml.
of
water
and
convert
to
lime
mud
as
follows:
While
mixing
the
mud,
add
3
Ib/bbl,
i.e.
3
grams,
of
caustic
soda
dissolved
in
5§
ml.
of
water.
Observe
the
viscosity
change.
Add
3
Ib/bbl,
i.e.
3
grams,
of
deflocculant
(polyphosphate-Barafos).
Observe
the
viscosity
change.
Mix
for
5
minutes
at
low
speed.
Add
4
Ib/bbl,
i.e.
4
grams,
Calcium
oxide,
commonly
known
as
burnt
lime,
lime
or
quicklime
(CaO).
Mix
for
5
minutes
at
low
speed.
Add
0.5
gram
Ib/bbl,
i.e.,
0.5
grams,
of
Quik
Gel.
Mix
for
5
minutes
at
low
speed.
10.Measure
the
same
properties
as
were
measured
in
step
2
above.
Alkalinity
Determinations
Py,
Py,
and
M;:
1.
Mud
Alkalinity,
Py,
:
This
test
measures
the
alkalinity
of
the
whole
mud.
When
used
along
with
the
filtrate
alkalinity
determination,
the
amount
of
excess
lime
present
in
lime
muds
can
be
determined.
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PROCEDURE
Py:
1.
Using
a
syringe,
measure
1
ml.
of
a
freshly
stirred
sample
of
mud
into
a
titration
dish.
Make
sure
there
are
no
air
bubbles.
Dilute
the
mud
with
25-50
ml
distilled
water.
Add
no
more
than
4
or
5
drops
of
phenolphthalein.
If
the
sample
does
not
change
color,
report
Pm
as
0.
If
the
sample
turns
pink,
titrate
rapidly
with
N/50
sulfuric
acid
until
pink
color
disappears.
Use
the
1cc
pipette
for
the
base
mud
and
the
10
cc
pipette
for
the
lime
mud.
Report
the
phenolphthalein
alkalinity
of
the
mud,
Pm,
as
the
number
of
mis
of
N/50
sulfuric
acid
added
to
discharge
the
pink
color.
2.
FILTRATE
ALKALINITY
P;
.and
Mg
These
tests
measure
the
alkalinity
of
the
filtrate
or
water.
PROCEDURE
Py
1.
2.
3.
4.
Pipette
1
ml.
of
filtrate
into
a
clean
titration
dish.
Do
not
dilute
with
distilled
water.
Add
no
more
than
2
or
3
drops
of
phenolphthalein.
If
no
color
develops,
Py
is
0,
and
the
pH
is
less
than
8.3.
If
a
pink
color
develops,
add
N/50
sulfuric
acid
through
a
pipette
until
the
color
changes
back
to
that
of
the
original
sample.
Use
the
1
cc
pipette
for
the
base
mud
and
the
10 cc
pipette
for
the
lime
mud.
The
Py
is
the
amount
of
N/50
sulfuric
acid
required
to
discharge
the
pink
color.
Excess
lime
content,
Ib/bbl
=
(Pm
-
Pf)/4.
PROCEDURE
Mg
1.
2.
3.
To
the
same
sample
used
for
the
P;
determination,
add
2
to
3
drops
of
Bromcresol
Green
-
Methy!
Red
Indicator.
Again
add
N/50
sulfuric
acid
until
the
color
changes
from
a
blue-green
to
a
light
pink.
Use
the
1
cc
pipette
for
either
mud.
Report
the
M;
alkalinity
of
the
filtrate
as
the
total
volume
of
N/50
sulfuric
acid
required
to
reach
the
end
point,
including
the
volume
required
to
reach
the
Ps
end
point.
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Results:
1.
Discuss
applications
of
calcium
treated
muds.
2.
Discuss
advantages
and
limitations
of
calcium
treated
muds.
3.
Based
on
your
observation
of
viscosity
changes,
discuss
the
conversion
mechanism
of
lime
mud.
Include
the
effects
of
adding
each
component.
4.
Compute
the
amount
of
free
lime.
Discuss
what
it
tells
you.
5.
Based
on
the
results
of
your
lab
experiment,
write
a
step-by-step
procedure
for
the
derrick
hand
to
convert
to
lime
mud.
Include
the
barrels
of
water,
sacks
of
caustic
soda,
polyphosphate,
lime,
and
bio-
polymer
(Quik-Gel)
needed
for
the
conversion
of
1500
bbl
base
mud
in
tanks
and
in
the
hole.
Show
all
calculations.
(1
sack
=
50
Ibs).
Base
Drilling
Fluid
]
Lime
Treated
Drilling
Fluid
Plastic
Viscosity,
(cP)
Yield
Point,
(Ib/100
sq.ft.)
10
second
Gel
Strength
(Ib/100
sq.ft.)
Filtration
Loss
(mi)
pH
Ps
Pm
My
Please
see
sections
12,
Alkalinity
and
lime
content,
and
13,
Chloride
ion
content
of
the
“Recommended
Practice
for
Field
Testing
Water-based
Drilling
Fluids”
—
ANSI/API
RP
13B-1,
4"
Edition,
March
2009
-
for
further
information.
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