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HOPE MEYERS
Rock and Fluid Laboratory
Absolute and Effective Porosity
Sieve Analysis
Absolute Permeability
Gas Permeability and Klinkenberg Effect
Energy and Mineral Engineering Department
The Pennsylvania State University
March 4, 2011
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TABLE OF CONTENTS
Effective Summary…………………………………………………………2
Introduction………………………………………………………………4
Results and Discussion……………………………………………………6
Conclusion…………………………...…………………………………..17
Sample Calculations……………………………………………………..18
Nomenclature……………………………………………………………18
References……………………………………………………………….19
1
Executive Summary
In the Absolute and Effective Porosity lab the objective was to illustrate the
concept of porosity and to determine the absolute and effective porosity of porous media.
I also had to estimate error in the porosity calculations from the errors associated to each
parameter measured. There were three parts to this experiment. In part one: The Marble
Experiment, I had to fill a beaker with several marbles, and then fill the beaker to the top
with water in order to measure the porosity. With the measurements of the weight of the
marbles, the size of the marbles, and the volume of water used, the porosity could be
determined. In part two: The Helium Porosimeter, I obtained a core sample and
vacuumed all the air out of the sample, and filled the pore space with helium gas. Using
the measurements of the core sample, as well as initial and final pressures of the gas, I
could determine the porosity. In part three: The Barnes Method, a core sample was used
and all the air from it was removed. After the air was removed, water was introduced to
the sample and the water filled up all the empty pore space. Using the weights of the
unsaturated and saturated core, the weight of the fluid absorbed, and the volume of the
fluid absorbed, I could calculate the effective porosity. In the Sieve Analysis lab the
objective was to conduct a standard grain size analysis test and determine the relative
proportions of different grain sizes. A sieve set was used, and 250 grams of sand was
poured into the sieve. The sieve was then placed in the sieve shaker for 10 to 15 minutes.
Afterwards, the sand was separated and weighed. This process was repeated four times.
This lab helped in seeing different grain sizes, and how they are distributed in sand
samples. In the Absolute Permeability lab the objective was to determine absolute
permeability of an unconsolidated pack using fundamental laboratory equipment and
procedures, and to compare results for different grain size distributions and generalize the
effect of grain size distribution on porosity and permeability. I connected the sample to a
valve which was connected to a beaker of water. I opened the valve to saturate the sample
and then weighed the saturated core. Then I let the water run through the sample and out
the other side in order to measure the flow rate. Using core measurements, viscosity and
density of water, and the flow rate I could calculate the “false” pore volume, calculated
pore volume, calculated bulk volume, and porosity. In the Gas Permeability and
Klinkenberg Effect lab the objective was to determine the apparent permeability of a
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reservoir rock using a gas permeameter, demonstrate and measure the dependence of
permeability to gas at varying pressures, and then predict the “absolute” permeability to
liquid using Klinkenberg’s correction, and exercise the use of the radial form of Darcy’s
flow equation. I used a Ruska Permeameter in order to determine gas permeability of a
core sample. As opposed to the previous labs, gas was used as the measurement fluid in
this lab.
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Introduction
Porosity is the backbone of the first experiment, Absolute and Effective Porosity.
Porosity is defined as, “a measure of the storage capacity [in a rock] that is capable of
holding fluids” (Ahmed, 32). There are two different types of porosity because in rocks
fluids can be stored in two different types of areas. Some areas are interconnected to each
other, while other areas are completely isolated (Ahmed, 32). The absolute porosity is
“the ratio of the total pore space in the rock to that of the bulk volume” (Ahmed, 32).
This means that all of the pore space, interconnected and isolated, is included. Effective
porosity is “the percentage of interconnected pore space with respect to bulk volume”
(Ahmed, 33). Porosity is important because the spaces in the rocks where fluids can
reside are where petroleum engineers can find oil. The porosity of the rock can determine
how easy or how difficult is would be to extract the oil. “The effective porosity is the
value that is used in all reservoir engineering calculations because it represents all the
interconnected pore space that contains the recoverable hydrocarbon fluids” (Ahmed, 33).
In the experiment titled Sieve Analysis, grain size was the main component. A
sieve is defined as “a utensil consisting of a circular frame with a finely meshed or
perforated bottom used to separate the coarser from the finer particles of any loose
material” (OED Online). The sieve was used to separate various grains of a sand sample.
Sieve analysis is important because grain size determines the porosity and permeability of
a rock sample. Permeability is “the degree to which a solid allows the passage through it
of liquid or gas” (OED Online). A larger grain size will have a higher permeability while
a smaller grain size will have a lower permeability.
In the Absolute Permeability lab the permeability of various grain sizes were
tested using water. As stated before in the Sieve Analysis lab, the permeability of a
sample is how well a liquid flows through it. Permeability is important because it
determines how easily a liquid or gas will flow through a rock sample, which is how
petroleum engineers know how easy or hard it will be do extract oil from rock. Rocks
that have larger grain sizes have greater permeability because they have more pore space
between the grains. Rocks that have smaller grain sizes have less permeability because
they have smaller pore spaces between the grains.
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In the Gas Permeability and Klinkenberg Effect lab, the permeability of a core
sample was tested by using gas. Since gas is a compressible substance its volume and
flow rate vary with the pressure that it is measured at. Liquids are not compressible, so
they can be measured more easily as they were in the previous experiment. The
Klinkenberg Effect is the dependence of the permeability of the reservoir rock to gas on
the mean pressure. When a gas behaves more like a liquid, it has permeability close to
that of a liquid but when a gas behaves more like a gas, it can give false readings of
permeability. This is what we call the Klinkenberg Effect.
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Results and Discussion
There were a total of four labs conducted over the course of a four week period,
and each lab built upon the ideas and concepts of the ones before. Overall, the labs
coincided with one another in the realm of porosity and permeability of gases and liquids.
Porosity was found to have an effect on permeability, because the higher the porosity a
substance, the greater the permeability. This is because if there is more pore space in a
material, a liquid or gas can flow through larger pore spaces more easily. Also, when gas
was used to determine permeability, the Klinkenberg Effect was evident as shown by lab
findings.
Absolute and Effective Porosity Lab
In the Absolute and Effective Porosity lab the results were very clear. The first
part was an activity where the porosity was measured by using marbles and water. By
finding the weight of all the marbles, the beaker, and the water, the bulk volume and the
pore volume could be calculated. The following table shows the values calculated for the
weights and volumes needed to determine pore volume by volume and by weight.
Average marble volume 1.73 cc
Weight of empty beaker (W1) 107.3 g
Weight of all marbles and beaker (W2) 373.13 g
Bulk Volume (V1) 489.06 cc
Pore Volume (V2) 116 mL
Number of marbles (Nm) 51
Grain Volume (V3) 88.23 cc
Bulk Volume 204.23
The pore volume was then determined in two different ways in order to calculate the
porosity. In the first way, it was determined volumetrically where the porosity was
calculated by dividing the pore volume by the bulk volume. The second way the pore
volume was determined was by the water’s weight. The following table shows the data
from the experiment used to calculate the different porosities.
Porosity (volume determined 0.57
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volumetrically)
Final weight of water in beaker (W4) 115.93 g
Volume of water in pore space (V4) 115.93 cc
Porosity (volume determined by weight) 0.515
By using different methods to find the pore volume, the porosity changed.
Although both porosities were relatively close in value, if the pore volume is determined
by volume or by weight, the results will differ. These values show that there is high
porosity in a group of marbles. Just by looking at the marbles in the beaker, it was clear
that there was a lot of pore space in between them. Also, only absolute porosity was
measured in this experiment. This part of the experiment was important in order to instill
a basic idea of the topic of porosity. There were multiple errors that may have occurred in
this experiment. Measuring the diameter of the marbles may have been skewed, because
they were very small. With their size, the measurements may have been slightly off. If the
diameter of the marbles was not accurate, then the volume of the marbles may have been
slightly inaccurate as well, which in turn would have affected the grain volume, and the
bulk volume.
In the second part of the Absolute and Effective Porosity lab, a core sample was
used and the air was evacuated from the core, and the pore spaces were then filled with
helium gas in order to determine the porosity. The following table lists the values
calculated from the experiment in order to determine porosity.
Volume of reference chamber 33.17 cc
Volume of sample chamber 141.57 cc
Core length 3.1 cm
Core diameter 2.4 cm
Bulk volume (Vbulk) 14.02 cc
Solid sleeve volume (VSolid Sleeve) 3.2 cc
Reference chamber pressure, after
stabilization (pi1)
56.11 psia
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Vacuumed sample chamber initial pressure
(pi2)
0 psia
Final pressure (pf) 11.66 psia
Rock volume (Vrock) 11.92 cc
Porosity 0.1498
In this case, the porosity was very small compared to the porosity of the marbles
in the beaker. This is because the grain size of the core was much smaller than the
marbles, which means there was much less pore space between the grains in the core
sample. Also, because helium was used to determine the porosity, this calculation was
more accurate than the marble experiment because gas has smaller molecules than liquid,
which means the molecules can fit into more pore spaces than liquid could. The
porosimeter gave us information to calculate absolute porosity, not effective porosity.
One source of error that may have occurred was the measurements of the core. If the
measurements were not accurate, then the bulk volume would have been inaccurate. The
initial pressure in the vacuumed sample chamber of the porosimeter was taken to be zero
psia. Considering this porosimeter was very old and took multiple days to start up, the
vacuum may not work as efficiently as it used to. If the initial pressure of the vacuumed
sample chamber was more than one, this would have affected the results of the rock
volume. The valves on the porosimeter needed to be opened and closed often in this
experiment, so if the valves were not completely closed when needed, this could have
affected the pressure values. Because the porosimeter used in the experiment was very
old and outdated, I think a more recent version of a porosimeter could have been useful in
data gathering.
In the third part of the experiment, the Barnes Method was used to find the
effective porosity of the core sample. All of the air from the sample was evacuated, and
then the sample was introduced to water which filled all the pore spaces in the core.
Because water was used as the fluid, this made it easier to calculate the effective porosity
because the density of water is 1 g/cc. The following table contains the values calculated
in order to determine the effective porosity.
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Fluid density 1.00 g/cc
Weight of unsaturated core 33.29 g
Weight of saturated core 36.69 g
Weight of fluid absorbed 3.4 g
Volume of fluid absorbed 3.4 cc
Effective porosity 0.243
The absolute porosity was not found during this part of the experiment. One
source of error could have been when the saturated core was weighed. The excess water
on the core sample was removed as much as possible, but there may still have been some
excess water which would have made a difference in the weight of the saturated core, and
the weight of the fluid absorbed. Also, while letting the water into the vacuumed
chamber, it was very important to let the water in through the stop cock extremely
slowly. While this was done as efficiently as possible, some air could have gone into the
vacuumed chamber which would have caused a difference in the amount of water that
entered the core sample.
Sieve Analysis Lab
In the Sieve Analysis experiment samples of sand was sorted into different
variables of fineness using a sieve. The sand was very fine and was sorted into five
different grain sizes. The sieving process was conducted four times in order to sieve a
total amount of 1000 g of sand. The following table shows how the sand was sorted in
each trial.
Sieve # Sieve
size (in)
1st Trial 2nd Trial 3rd Trial 4th Trial Total
weight
50 0.0117 100 g 87 g 79 g 82 g 348 g
70 0.0083 3 g 1 g 3 g 2 g 9 g
100 0.0059 81 g 82 g 84 g 81 g 328 g
120 0.0049 33 g 51 g 48 g 55 g 187 g
140 0.0041 30 g 23 g 35 g 25 g 113 g
Bottom 3 g 4 g 4 g 4 g 15 g
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Total
Sand
250 g 248 g 253 g 249 g
This particular sample of sand is important to sieve because the grain distribution
can determine the porosity and permeability of a sedimentary rock made by this type of
sand. Although sieving the sand took a lot of time, the way it was completed with a sieve
shaker was the most effective way to properly sort the sand particles. One source of error
in this experiment was that most of the sieves had left over sand particles stuck in the
holes that could not be brushed out. This could have added some weight to the final
numbers if the sand fell out into the samples. Also, when weighing the sand some of the
sand particles did not come out of the holes of the sieve by brushing them, and some of
the sand did not fall exactly on the paper towel used to weigh the sand, which means
small portions of sand may not have been measured.
Absolute Permeability Lab
In the Absolute Permeability experiment the absolute permeability of three
different particle sizes was found using various laboratory equipments. For each grain
size, there was a core filled with that specific grain size that had been vacuumed in order
to evacuate all the air. Each core was measured in order to find the volume of the core.
The bulk volume was the volume of the core holder, which was the same value for all
groups because the core holders were all the same size. The following table shows the
values calculated for the core filled with fine grains.
Core diameter 2.9 cm
Core cross sectional area 6.61 cm2
Core length 64.14 cm
Unsaturated core and tubing weight 2022.1 g
Saturated core and tubing weight 2206.1 g
Viscosity of saturation fluid 1.0020 cp
Density of saturation fluid 1.00 g/cc
“False” pore volume 184 cc
Calculated pore volume 73.93 cc
Calculated bulk volume 423.7 cc
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Porosity 17.5 %
Sand volume 350 mL
Flow rate was also measured for each grain type, and the following chart shows the flow
rate data for the fine grain sample.
Trial Flow rate (mL/min) Height of beaker (in)
1 7.8 19.25
2 6.8 17.5
3 6.0 15.5
4 5.6 14.0
5 4.4 11.25
The following table shows the data found for the coarse grain sample.
Core diameter 2.9 cm
Core cross sectional area 6.61 cm2
Core length 64.14 cm
Unsaturated core and tubing weight 2035.2 g
Saturated core and tubing weight 2179.3 g
Viscosity of saturation fluid 1.0020 cp
Density of saturation fluid 1.00 g/cc
“False” pore volume 144.1 cc
Calculated pore volume 77.3 cc
Calculated bulk volume 423.7 cc
Porosity 18 %
Sand volume 350 mL
The following table shows the flow rates of the coarse grains.
Trial Flow rate (mL/min) Height (in)
1 12 19
2 11 17.9
3 9 15.6
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4 6.5 12.5
5 4.5 7.5
The following table shows the values measured and calculated for the mixed grains core
sample.
Core diameter 2.9 cm
Core cross sectional area 6.61 cm2
Core length 64.1 cm
Unsaturated core and tubing weight 2035.6 g
Saturated core and tubing weight 2175.5 g
Viscosity of saturation fluid 1.0020 cp
Density of saturation fluid 1.00 g/cc
“False” pore volume 139.9 cc
Calculated pore volume 96.7 cc
Calculated bulk volume 423.4 cc
Porosity 23 %
Sand Volume 326.7 mL
This table shows the flow rates calculated for mixed grains.
Trial Flow rate (mL/min) Height (in)
1 8.8 19.15
2 8.5 16.5
3 7.2 13.5
4 6.6 12
5 4.6 7.9
From this data, it is easy to see that the porosity of the samples increased as the
sample grain size increased. This means that the smaller the grain size, the less pore
space there is available for fluid to be contained, and the larger the grain size, the more
pore space there is. An interesting point to note in the data collection is that the flow rate
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of the fine grains was significantly slower than the flow rates of the coarse and mixed
grains. The flow rate was slower because the grains were smaller, which makes it harder
for water to flow through such small spaces. Since the flow rate was slow, this means that
the core sample was less permeable than the other samples. For the coarse grains, the
flow rate was much faster than the fine and mixed grains at the greater heights, but then
the flow rates became about the same as the mixed grains at the lesser heights. The coarse
grain sample had minimal flow rates at the greater heights, which is unusual considering
the porosity was so much greater than the coarse and fine grain samples. I have included
a graph for the flow rates for each of the grain sizes, in order to easily visualize the
concept.
4 4.5 5 5.5 6 6.5 7 7.5 80
102030
Height vs Flow Rate (Fine Grains)
Series2
Flow Rate (mL/min)
Hei
ght (
in)
4 5 6 7 8 9 10 11 12 1302468
101214161820
Height vs Flow Rate (Coarse Grains)
Series2
Flow Rate (mL/min)
Heig
ht (i
n)
4 5 6 7 8 9 1005
10152025
Height vs Flow Rate (Mixed Grains)
Series2
Flow Rate (mL/min)
Heig
ht (i
n)
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With the increase in height of the beaker to the core sample, there was greater
pressure, and when the height was closer to the core sample there was less pressure.
Although pressure measurements were not taken during this experiment, it is evident that
with an increase in pressure, there is an increase in flow rate. Ultimately, a sample with
larger grains would have higher porosity and greater permeability because of the more
spaces in between the grains that allows fluids to flow more easily.
Because of the difference in flow rate, there may have been some errors in the
experiment. When measuring the flow rate, the volume of the water in the beaker needed
to remain fairly constant in order to be accurate. If the volume was not constant and was
not being filled as the water was running through the sample, this may have cause
discrepancies in the flow rate. The height from the water level to the core sample during
the flow rate estimation was difficult to measure accurately because the apparatus used
was abstract and hard to measure with the measuring tape. The measurements for this
were eyeballed. Also human error caused the “false” and calculated pore volume to have
discrepancies. The “false” pore volumes should have been less than the calculated pore
volume because the “false” pore volume is the weight of the water added to the core, and
the calculated pore volume is the calculated volume of the tube and the volume of the
sand that was added to fill the core tube. Although, the sand that was added to the core
tube was not densely packed, which could also be why the “false” pore volume was more
than calculated pore volume. One way to improve the data was to make the saturation of
the core sample more effective. When the water was connected to the core sample with a
long tube, there were often large bubbles that got in the way of the water flowing into the
vacuumed core. It took a long time for the water to go through the sample and at a point
the water completely stopped flowing and a vacuum had to be used to suck the water
through the rest of the sample in order to saturate it.
Gas Permeability and Klinkenberg Effect Lab
In the Gas Permeability and Klinkenberg Effect lab the apparent permeability and
“absolute” permeability of a sample was found using gas. Using the Ruska Permeameter
and a core sample the permeability of the sample could be found. Measuring all of the
core sample’s measurements, and watching the dials on the Ruska Permeameter, the
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permeability could be found. The following data table shows the measurements used to
obtain the permeability of the core.
Trial Tube Size Tube height (cm) Pressure (atm)
1 Large 2.3 1.39
2 Medium 8.6 1.33
3 Small 3.8 1.29
Core diameter 3.4 cm
Core length 3.2 cm
Barometric pressure 1.00 atm
Temperature 23 degrees C
Average (Large) tube height 2.3 cm
qdown at average tube height 9.75 cc/sec
μair at 23 degrees C 0.0176 cp
Core area 9.08 cm2
Permeability of core A 0.157 mD
The gas that was used in the Ruska Permeameter to determine the permeability of
the core was nitrogen. Using formulas that were provided, the permeability was found.
Because gas was used in this experiment to determine permeability, the
Klinkenberg Effect needed to be tested in order to see how it affects the outcome of
permeability. The radial flow experiment showed the Klinkenberg Effect. The following
data sheet includes all of the data found when using the Radial Permeameter.
Inside core diameter 3.015 cm
Outside core diameter 6.025 cm
Core height 5.012 cm
Barometric pressure 0.95 atm
Temperature 28 degrees C
Ln(rout/rin) 0.692
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Pressure Upstream Pressure differential
Trial Vg (ft3,
L)
t(sec) qdown
(cc/sec)
mV psi mV psi
1 3 5 600 1.7 6.613 0.6 1.608
2 3 6 500 2.7 10.503 0.6 1.608
3 3 7 428.57 3.7 14.393 0.6 1.608
4 3 8 375 4.7 18.283 0.6 1.608
When the data above is calculated into permeability, the Klinkenberg Effect is evident
when graphed in relation to the inverse of the mean pressure of the system.
1.4 1.5 1.6 1.7 1.8 1.9 2 2.1 2.2 2.3 2.40
0.10.20.30.40.50.60.70.8
Klinkenberg Effect
Series2Linear (Series2)
1/pmean (atm-1)
kg(D
arcy
)
This graph on the Klinkenberg Effect shows that as a gas behaves more like a liquid, it
tends to have a permeability of liquid quality. So, if the gas is at high pressure, the
permeability is more accurate. If the gas is at low pressure and behaves more like a gas, it
can skew the values when measuring permeability.
One possible source of error for this experiment could be the efficiency of the
Ruska Permeameter. The one that my group used had a pressure gauge that was off, so
we had to compensate our values for the incorrect readings that it would give us. Also,
our lab group did not have a chance to conduct the Radial Permeameter portion of the
experiment, and only the values from another experiment were available. I think being
able to conduct the entire lab would have made the experience worthwhile. Not being
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able to visualize what happened during the experiment made it difficult to interpret what
was really going on.
Conclusion
All of these experiments were conducted in order to give a greater understanding
of porosity, permeability, and how the two can be tested and relate to one another. The
experiments progressed in an effective manner, starting very simply with the subject of
porosity. Porosity, as shown by the first lab, increases with the size of the grains because
there are more spaces in between the grains for water or gas to flow. The second lab also
dealt with porosity, because the larger grains that were sieved would have had a greater
porosity than the smallest grains that were sieved. Also, the sand that we sieved in that
experiment was used to create the core samples for the third experiment. In the third
experiment, permeability and porosity came together to show that the greater the
porosity, the greater the permeability. The fine grains had slower flow rates, which mean
the permeability was less than the permeability of the coarse and mixed grains. Finally,
the permeability was tested using gas. Because gas is highly compressible, it sometimes
gives false readings of permeability, which we tested for using the Radial Permeameter.
The Klinkenberg Effect was proven correct, and by using the Ruska Permeameter the
permeability of a core sample using Nitrogen gas was found.
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Sample Calculations
1. Φ = V2/V1 = 116 mL/204.23 mL = 0.57
2. Vrock = Vreference chamber (p1i-pf) / (p2
i-pf) + Vsample chamber – Vsolid sleeve
Vrock = 33.17cc (56.11psia – 11.66psia) / (0psia – 11.66psia) + 141.57cc –
3.2cc
Vrock = 11.92 cc
3. Φ = 1 – Vrock / Vbulk = 1 – 11.92cc / 14.02cc = 0.1498
4. Φeffective = Vi / Vbulk = 3.4cc / 14.02cc = 0.243
5. pdownqdown = pupqup 1.14atm(qdown) = 1.39atm(8cc/s) qdown=9.75cc/sec
6. kg = [2μLqdownpdown] / [A(pup2 – pdown
2)] = [2(0.0176cp)(2.3cm)(9.75cc/sec)
(1.14atm)] / [9.08cm2(1.392 – 1.142)]
kg = 0.157mD
7. qmean = [qdownpdown] / pmean = [600cc/sec(1.302atm)] / 1.351atm = 578 cc/sec
8. kg = [qdownpdownμln(ro / ri)] / [πh(pup2 – pdown
2)]
= [600cc/sec(1.302atm)(0.0176cp)ln(6.025cm/3.015cm)] / [π(5.012cm)(1.42 –
1.3022)] kg = 2.28 Darcies
Nomenclature
1. Φ—Absolute porosity V2—Pore volume (mL) V1—Bulk volume (mL)
2. Vrock—Rock volume (cc) Vreference chamber—Reference chamber volume (cc)
p1i –Pressure in reference chamber after stabilization (psia)
p2i –Initial pressure in vacuumed sample chamber (psia)
Vsample chamber –Volume of sample chamber (cc)
Vsolid sleeve –Volume of solid sleeve (cc)
3. Vbulk = Bulk Volume (cc)
4. Φeffective = Effective porosity Vi—Interconnected pore volume
5. pdown—downstream pressure (atm) pup—upstream pressure (atm)
qdown—downstream flow rate qup—upstream flow rate
6. kg –apparent permeability (Darcy) μ—viscosity (cp)
L—tube height (cm) A –core area (cm2)
7. qmean—mean flow rate (cc/sec) pmean—mean pressure (atm)
8. ro—outside core diameter (cm) ri—inside core diameter (cm) h—core height(cm)
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9. References
Ahmed, Tarek. Working Guide to Reservoir Rock Properties and Fluid Flow. Burlington:
Elsevier Science & Technology, 2009. Print.
OED Online. November 2010. Oxford University Press. 28 February 2011
<http://www.oed.com/view/Entry/179420?rskey=u1NU7h&result=1&isAdvanced
=false>.
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