Drill Stem Testttt
Drill Stem Testttt
JUNE,1956
SPE 589-G 21
3. The Packer amount of hole to test; (3) packer a core hole, or hole of reduced diam-
o. To bridge the hole at Q point immediately above
(and also below on straddle tests) the zon,e to size or sizes; (4) location of packer eter, is drilled ahead for exploratory
be tested, thus permitting this zone to be relleve~ purposes. Successful use of conven-
of hydrostatic mud pressure when the tool IS
seat; (5) top and bottom choke
opened and isolating the zone from other forma- sizes; (6) probable length of flowing tional double-end wall packers re-
tions.
Important auxiliary components of and shut-in period and use of dual quires a very close fit to the hole
the drill-stem test tool are as follows: shut-in periods; (7) type of pressure size. Because· of this, a reduction in
the disk valve, the shut-in pressure gauges, manner of placement in the hole size or rathole for the last 300
valve or tool, the formation or bot- tool, and optimum pressure capacity to 500 ft of hole, including the test
tom choke, the anchor pipe, and the and clock speed; (8) use of, type, zone, permits greater packer clear-
pressure recorders. In addition to and location of circulating sub, safety ance while running in and out in
these, a circulating valve, a safety joint, and jar; (9) use of water cush- the full hole. Ratholing is largely
joint, and sometimes a set of jars ion and amount; (10) method of confined to soft formation areas.
may be included in the test tool or handling test production at the sur- It has been found that the ratio
in the drill pipe or tubing string. face; and (11) special packer ar- of hole size to packer size largely
rangements. governs the amount of packer com-
FUNCTIONS OF AUXILIARY COMPONENTS IN pression that will occur at pressure
TYPICAL TEST TOOL STRING
Amount of Hole to Test differentials up to 5,000 psi and that
1. The Disk Valve
o. To aid in preventing drilling mud from enter- In most instances, a more conclu- leakage or rupture of the rubber
ing the drill pipe while running in.
b. To permit the packer to be set firmly and tester sive test can be obtained by testing element will occur if the ratio of
valve opened before the tool is finally opened by
dropping a go-devil to rupture the disk valve (as
the shortest section practical. In thin hole size to packer size is such that
used with certain tool assemblies). sands, where it is desired to locate complete mandrel travel is attained.
2. The Shut-In Pressure Valve or Tool
is conditioned before the test. One cate that when testing sands of mod- Selection of Pressure Recorders
technique of testing under such con- erate to high permeability, the length No drill-stem test should be run
ditions, where a subsurface adjust- of the flow periods ordinarily used, without two subsurface pressure
JUNE, 1956 23
gauges; if possible, one gauge should mation and stick the anchor; (2) it pacKel carries the larger load. If the
measure the pressures upstream or may cause plugging of anchor per- lower packer fails, the upper packer
below the bottom choke inside the forations or the bottom choke, and assumes the load.
perforated anchor, and the other (3) it contributes to packer failures.
should be blanked-off so as to meas- Flui~ cushions or water blankets Straddle Packer Testing
ure pressures outside the perforated can be placed in the drill pipe above
anchor. Under this arrangement, the the test tool to reduce the pressure Open-hole straddle testing involves
two pressure records should agree differential that occurs across the testing a productive interval which
exactly unless the holes in the per- wall of the bore hole and packer as may be as much as several thousand
forated anchor become plugged, in the tool is opened; however, this feet from bottom. A wall packer is
which case the ~lanked-off gauge procedure may make test interpreta- set in a competent seat above and
will trend toward the formation shut- tion difficult, particularly when the below the interval to be tested so
in pressure while the inner gauge will recovery is small, because the forma- that a selected zone may be isolated
reflect the pressure inside the anchor, tion liquids may mix with the water for testing through means of a per-
either atmospheric pressure or that cushion. forated nipple which is placed be-
due to the head of fluid recovered tween the two packers; convention-
It is sometimes advisable to use
before the plugging occurred. If the ally, the blank anchor extends to
fluid cushions when testing high-
choke becomes plugged but the an- pressure gas sands for reasons of total depth. Use of a straddle packer
chor pipe does not plug, both gauges safety. The cushion will effect lower by-pass tool will permit mud pres-
should trend toward formation shut- surface pressures until it has been sure to be equalized above the top
in pressure. The backwashing that produced out of the pipe. Occasion- packer and below the bottom packer
JUNE, 195()
wall packer testing inside casing Salt Water Samples yields only formation water, the mud
since this type of test is usually con- Absence of oil or gas in a tested below the packer is displaced up-
ducted for a long enough period to formation cannot be considered ward into the drill pipe by water en-
permit the pipe to be entirely filled proved unless evidence is obtained tering the well bore. At first this
with formation liquids, and pump that representative formation water water is mud filtrate, followed in
pressure can be applied to the annu- is recovered. During the course of a turn by salt water. Fig. 2 illustrates
lus while the packer is set with min- study of subsurface waters in which the resultant variation of salinity
imum danger of breaking down the a large number of drill-stem tests with depth in the recovered water
formation. Reverse circulation in were made for the specific purpose column. The salinity increases rapid-
open hole is less attractive because of of obtaining representative water ly below the mud to a maximum
this danger, hazard of sticking the samples, a system of sampling was constant value. Any part of the water
pipe, and difficulty in accurate meas- column having this maximum con-
developed by M. S. Taggart, Jr., of
urement of small-volume recoveries. stant salinity is representative forma-
Production Research Division, Hum- tion water, or very nearly so.
When fluid recovery is believed to
ble Oil & Refining Co., which per- From the point of view of sam-
be large, a suggested procedure for
open-hole reversing is indicated mits determining by examination of pling, it may be seen that a sample
below. the samples themselves whether rep- taken just below the mud would have
resentative water is produced. The had a chloride content of only
PROCEDURE FOR OPEN HOLE REVERSING
following examples have been se- 32,000 ppm, whereas the true chlor-
1. At conclusion of flowing period, place 500
to 1,000 ft of fresh water of known chloride in lected from the results of this study ide content of the formation water
the drill pipe. was about 66,000 ppm. Except in ex-
to illustrate the variations of salinity
....."'oo.=o~"~"" .. ~.'"
_ -_ _
-m~---:i!fjli!"~~{
INDEX
=
packer in the test zone. A larger vol-
ume of mud in the recovery may be
..... ~m
n.,-eIlONII ... VOII,~
indicative of a fractured or vugular ~.~"'''CO OH.~. I
IHftIl",OCO.V:
Mud Fdt''''e
taken as evidence of representative & Soh w"' ••
! ~
less than that of representative water ~ I ~
I
recovered from open hole in the No. ~
a:: 15
I 15 --
~
-
~---=-=-____::_l_:c_____,,_L_L--------'
during a drill-stem test is inadequate
for determining the properties of for- ",000
_ 17_ 0
0
mation waters. The single sample CHLORIDE CONTENT: PPM CHLORIDE CONTENT, PPM
may be representative, but this can- Fig. 2 -- Example of usual variation Fig. 3--Example of effect of leaking
of salinity with depth in recovered packer on variation of salinity with
not be determined. A suite of sam- water column. depth in recovered water column:.
JUNE, 1956
ter the test zone to cause a slow where little oil, condensate, or water value of Q, the gas production rate,
buildup of pressure. Such formations is produced can be estimated from in Mcf per day on the horizontal
should not be rejected too hastily in the charts. scale,
view of the potentialities of acid 4. Draw a line through this point
Ability of the Well to Produce
treatment or fo~ation fracturing up and to the right at a 45° angle to
processes. the vertical axis.
Open Flow Potential
Fig. 7 shows schematic examples 5. Draw a line parallel to the hori-
of the several conditions discussed Frequently it will be desirable to
estimate the open flow potential of a
zontal axis along the value of in Ps,"
above. thousands. At the intersection of this
gas sand interval from drill-stem test line with the 45° line, read the value
Gas-Oil Ratio data. A reasonable estimate of open
If little or no water is produced of Q, in Mcf per day, which is the
flow potential based on data for one
during the test, the gas-oil ratio may approximate open flow potential of
rate of flow can be obtained as fol-
be estimated by using the charts, lows: the tested interval.
Figs. 8 and 8-A. The rate of gas 1. Estimate of Mcf per day gas
production during tests of gas zones Productivity Factors and Specific
production rate, Q, during the drill- Productivity Factors
stem test by the procedure described
12r----,-------r-------,-------, e...n,on in the preceding paragraph. An index of the ability of the
\
- - CRITICAL FLOW
- - - NON· CRITICAL FLOW
45
'"
I
I
j\
Well No. 1 ~
TIm.
I
JO
<5 (TOP GAGE NOT BLANKED OFF. BOTTOM GAGE BLANKED OFF)
g LEGEND: - - TOP CHART (OR 80TH CHARTS)
- - - BOTTOM CHART
~ I 0
g ! (CRITICAL FLOW)
'"~ 2S
\
~
a:
-'
-'
ii'
0
"-
20
0 I
Well No. B-1
l'i
z DST 513()'5154 ft. - .....
thrjugh perforct,oi'
~
15
.
!
I PACKER FAIL£D NO SHUT-IN PRESSURE
!, !
10
,/_TJI\
1rt
i I
" i'+-! \ ~ \
. , ,
i '
I I \
i i
. ' \
I A C \ 0 E
j I \
20,000 40,000 60,000 so,ooo
OILORIDE CONTENT: PPM CHOKE PLUGGING ANCHOR PLUGGED TOP CLOCK STOPPED I} STARTED
Fig. 5 - Example of failure to test Fig. 6 - Pressure chart interpretation: Typical charts from a satisfactory test
formation behind casing. and charts from common types of mis-run.
,,~
,=
..~
," ..
'O~ ....
.>
.. '
..
,~
"
I" "
Ift.o
"
Fig. 8 - Gas-oil ratio chart: ¥s- and *-in. chokes. Fig. 8A - Gas-oil ratio chart: 3/16- and 3/8·in. chokes.
Flow of fluid and gas through 1/8- and 3/16-in. by 6-in. chokes. Flow of fluid and gao through 1/8- and 1/4-in. by 6-in. chokes.
(Plotted from test data for downstream pressures less than 125 psi (Plotted from fest data for downstream pressures less than 125 psi
for values of /10 from 0.5 to 2.0 and API gravities from 32 to 42) for values of /Lo from 0.5 to 2.0 and API gravities from 32 to 42)
JUNE, 1956
water. If substantial production is which agrees closely with the bottom gauge read-
ing of 5,818 psi. The bottom gauge was then
indicated by this method, flowing assumed as reasonably accurate.
2. Check for complete pr~ssure buildup
production is probable since the ac- Since the bottom gauge pressure chart was nof
tual flowing gradient will be reduced available for examination and since the summary
did not indicate whether or not the shut-in pres-
by dissolved or free gas. sure buildup was complete, a check on the normal --- -+ -_.-
shut-in pressure for the depth was made by ex-
Use of Specific Productivity Factors amining initial reservoir pressures measured in
other producing reservoirs of comparable depth in
At times it may be of interest to the area. It was found that an initial shut-in gra-
dient of 0.465 psi/ft subsea was normal for the
make an estimate of the effective area. The elevation of the well in question was
permeability of the tested zone. This taken as 0 ft for convenience since it was known
that a borge rig was in use.
estimate may be made by utilizing Computed normal pressure was:
10,866 X 0.465 = 5,050 psi
the approximate relationship, given This was considered a reasonable check with the
by Eq. 6, between specific PF, the 5,025 psi recorded by the bottom gauge and the
formation pressure was assumed to be 5,050 psi
viscosity of saturated reservoir oil since buildup may not have been complete.
at reservoir temperature and pres- 3. Check for critical flow during test
In order to determine that the recovery entered
sure, and effective permeability. the pipe at a constant rate, the head on the bot-
tom choke due to the recovery was computed and
Subsurface sample analysis is re- found to be less than 50 per cent of the upstream
quired to determine the viscosity of recorded maximum flowing pressure of 4,380 psi.
Head due to 1,100 ft of oil and 180 psi surface VISCOSITY OF SATURATEO RESERVOIR OIL AT Po&. T,. CENTIPOISE
the reservoir oil; however, examina- pressure:
1,100 X 0.35 + 180 = 565 psi Fig. 9 - Correlations of API gravity
tion of a large number of analyses as compared with: 50 per cent of 4,380 = 2,190 with viscosity.
revealed that for reservoir tempera- psi.
tures between 140 and 240°F, the 4. Compute daily production rate during test