U.S. patent number 3,578,080 [Application Number 04/735,684] was granted by the patent office on 1971-05-11 for method of producing shale oil from an oil shale formation.
This patent grant is currently assigned to Shell Oil Company. Invention is credited to Philip J. Closmann.
United States Patent |
3,578,080 |
Closmann |
May 11, 1971 |
METHOD OF PRODUCING SHALE OIL FROM AN OIL SHALE FORMATION
Abstract
A method of producing shale oil from a subterranean oil shale
formation by exploding a relatively high energy explosive device
therein thereby forming a chimney of rubble within the formation
having fractures extending from the chimney into the formation. A
plurality of spaced wells are extended into the formation radially
outwardly from the chimney and adjacent to at least some of the
fractures. Fluid flow paths are formed from the wells through the
fractures into the chimney and fluid is circulated from the wells
through these fluid flow paths and into the chimney at rates
creating a pressure drop from the wells to the chimney. Oil
shale-reactive properties are imparted to the circulating fluid
whereby the fluid reacts with the oil shale thereby moving solid
components thereof into void spaces formed within the chimney
thereby increasing the permeability of the oil shale formation
relative to the permeability of the chimney in regions surrounding
the chimney.
Inventors: |
Closmann; Philip J. (Houston,
TX) |
Assignee: |
Shell Oil Company (New York,
NY)
|
Family
ID: |
24956774 |
Appl.
No.: |
04/735,684 |
Filed: |
June 10, 1968 |
Current U.S.
Class: |
166/248; 166/247;
166/259; 166/299 |
Current CPC
Class: |
E21B
43/2635 (20130101); E21B 43/2403 (20130101) |
Current International
Class: |
E21B
43/24 (20060101); E21B 43/263 (20060101); E21B
43/25 (20060101); E21B 43/16 (20060101); E21b
043/24 (); E21b 043/26 (); E21b 043/29 () |
Field of
Search: |
;166/247,248,256,259,263,270--272,299,303,305,307 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Novosad; Stephen J.
Claims
I claim:
1. A method of producing shale oil from a subterranean oil shale
formation comprising the steps of:
placing a relatively high energy explosive device within the
formation;
exploding the relatively high energy explosive device within the
oil shale formation thereby forming a cavity within the oil shale
formation having a roof beneath the overburden which subsequently
collapses to form a chimney of rubble within the oil shale
formation and extends fractures from the chimney through the oil
shale formation;
extending a plurality of spaced wells into said oil shale formation
at locations radially outwardly from said chimney and adjacent to
at least some of said fractures;
forming fluid flow paths from said wells through said
interconnecting fractures to said chimney;
circulating fluid into and them from said wells and through said
interconnecting fractures into said chimney and out of said chimney
at rates creating a pressure drop from the wells to said
chimney;
imparting oil shale-reactive properties to said circulating fluid
whereby said fluid reacts with said oil shale thereby moving solid
components thereof into void spaces formed within said chimney
thereby increasing the permeability of the oil shale formation
relative to the permeability of the chimney in regions surrounding
said chimney;
forming a plurality of fractured regions adjacent at least some of
said fractures from said chimney, said fractured regions being
located at substantially the same depth of said first mentioned
chimney;
subsequently extending fractures from said plurality of spaced
wells into communication with said fractures from said chimney;
said plurality of fractured regions being formed by placing a
plurality of devices of substantially lesser explosive energy than
said relatively high energy explosive device within the formation;
and
spacing the plurality of devices such a distance from the
relatively high energy device that the exploding of the plurality
of devices causes fractures from said spaced wells to extend into
communication with fractures formed by said high energy explosive
device.
2. A method of producing shale oil from a subterranean oil shale
formation comprising the steps of:
placing a relatively high energy explosive device within the
formation;
exploding the relatively high energy explosive device within the
oil shale formation thereby forming a cavity within the oil shale
formation having a roof beneath the overburden which subsequently
collapses to form a chimney of rubble within the oil shale
formation and extends fractures from the chimney through the oil
shale formation;
extending a plurality of spaced wells into said oil shale formation
at locations radially outwardly from said chimney and adjacent to
at least some of said fractures;
forming fluid flow paths from said wells through said
interconnecting fractures to said chimney;
circulating fluid into and then from said wells and through said
interconnecting fractures into said chimney and out of said chimney
at rates creating a pressure drop from the wells to said
chimney;
imparting oil shale-reactive properties to said circulating fluid
whereby said fluid reacts with said oil shale thereby moving solid
components thereof into void spaced formed within said chimney
thereby increasing the permeability of the oil shale formation
relative to the permeability of the chimney in regions surrounding
said chimney;
extending a well into said chimney adjacent substantially the lower
portion thereof;
circulating said fluid from said plurality of wells through said
fractures, into said chimney and out of said well; and
producing fluid from said well at progressively higher places
within said chimney.
3. A method of producing shale oil from a subterranean oil shale
formation comprising the steps of:
placing a relatively high energy explosive device within the
formation;
exploding the relatively high energy explosive device within the
oil shale formation thereby forming a cavity within the oil shale
formation having a roof beneath the overburden which subsequently
collapses to form a chimney of rubble within the oil shale
formation and and extends fractures from the chimney through the
oil shale formation.
extending a plurality of spaced wells into said oil shale formation
at locations radially outwardly from said chimney and adjacent to
at least some of said fractures;
forming fluid flow paths from said wells through said
interconnecting fractures to said chimney by electrically
fracturing the portion of the oil shale formation between the
chimney and said plurality of spaced wells;
circulating fluid into and then from said wells and through said
interconnecting fractures into said chimney and out of said chimney
at rates creating a pressure drop from the wells to said chimney;
and
imparting oil shale-reactive properties to said circulating fluid
whereby said fluid reacts with said oil shale thereby moving solid
components thereof into void spaces formed within said chimney
thereby increasing the permeability of the oil shale formation
relative to the permeability of the chimney in regions surrounding
said chimney.
4. A method of producing shale oil from a subterranean oil shale
formation comprising the steps of:
placing a relatively high energy explosive device within the
formation;
exploding the relatively high energy explosive device within the
oil shale formation thereby forming a cavity within the oil shale
formation having a roof beneath the overburden which subsequently
collapses to form a chimney of rubble within the oil shale
formation and extends fractures from the chimney through the oil
shale formation;
extending a plurality of spaced wells into said oil shale formation
at locations radially outwardly from said chimney and adjacent to
at least some of said fractures;
forming fluid flow paths from said wells through said
interconnecting fractures to said chimney;
circulating fluid into and then from said wells and through said
interconnecting fractures into said chimney and out of said chimney
at rates creating a pressure drop from the wells to said
chimney;
imparting oil shale-reactive properties to said circulating fluid
whereby said fluid reacts with said oil shale thereby moving solid
components thereof into void spaces formed within said chimney
thereby increasing the permeability of the oil shale formation
relative to the permeability of the chimney in regions surrounding
said chimney;
stopping the circulating of fluid from said wells through said
fractures and out of said chimney; and
circulating fluid from said chimney through said fractures and out
of said wells while imparting oil shale-reactive properties to said
fluid circulating from said chimney and out of said wells.
Description
BACKGROUND OF THE INVENTION
1. Field of the Invention
The present invention relates to a method of producing shale oil
from a subterranean oil shale formation more 20 particularly, it
relates to a method for creating a zone of relatively high
permeability within an oil shale formation.
2. Description of the Prior Art
The use of contained nuclear explosions has been proposed in
subterranean oil shale formations in an attempt to break up the oil
shale formation so that shale oil can be recovered from the rubbled
zone by known techniques such as in situ retorting.
Experience has shown that when a relatively high energy device,
such as a nuclear bomb, is exploded within a subterranean earth
formation, an almost spherical cavity filled with hot gases is
formed. This cavity expands until the pressure within the cavity
equals that of the overburden. On cooling, the roof of the cavity
collapses since, generally, it cannot support itself, and a
so-called "chimney" develops. Chimney growth ceases when the rock
pile substantially fills the cavity, or a stable arch develops. In
both cases, a substantially void space is formed below the
overburden and above the rubble contained within the chimney.
Surrounding the chimney is a fractured zone which results from the
shock of the nuclear explosion.
One of the chief uncertainties with regard to the effects of
nuclear explosions within a subterranean oil shale formation is the
permeability distribution surrounding the cavity and subsequent
chimney produced by a detonation. Evidence from prior explosions
suggests that permeability of the fragmented zone may drop very
rapidly with distance radially out from the primary rubble zone. A
high and uniform permeability is important in order to provide
maximum sweep efficiency in any underground hydrocarbon recovery
process.
The permeability in the region immediately surrounding the primary
rubble zone of an oil shale formation may be increased by
surrounding a primary high energy explosive device with a plurality
of radially-placed devices of explosive energy, nuclear or
nonnuclear. As disclosed in a copending application to Closmann et
al. Ser. No. 653,139, filed July 13, 1967, now U.S. Pat. No.
3,448,801, the radially-placed devices are programmed to be
detonated by either the main shock wave from the primary device or
exploded by other means after the main shock wave has passed. The
explosive energy devices are preferably detonated between the time
the spherical cavity caused by the explosion of the primary device
begins to expand radially outwardly and the time at which a chimney
is formed by the collapse of the cavity roof. Heated fluids may
then be circulated through the chimney and surrounding rubbled
areas by known means so as to increase the volume of the permeable
zone swept by the circulating fluid.
While a mass of oil shale is being pyrolyzed by the heated fluids,
fluid products are removed from surface portions of the kerogen
comprising the oil shale as rapidly as they are formed. But, since
the mass of oil shale is impermeable, the fluid which is formed
within the mass remains in place until its pressure becomes
sufficient to fracture and displace the solid components that block
its flow. In the oil shale around a nuclear-detonation chimney, the
least resistant direction in which solid components may be moved
tends to be toward the chimney where solid materials can be
squeezed together or pushed towards a void space formed at the top
of the chimney.
SUMMARY OF THE INVENTION
It is an object of this invention to improve the distribution of
the permeability in and around a chimney formed within an oil shale
formation while shale oil is being produced.
It is a further object of this invention to increase the rate at
which the permeability in the outlying areas from a chimney formed
within an oil shale formation is increased relative to that within
the chimney.
These objects are accomplished by exploding a relatively high
energy explosive device within an oil shale formation thereby
forming a chimney of rubble within the formation having fractures
extending from the chimney through the formation. A plurality of
spaced wells are extended into the formation radially outwardly
from the chimney and adjacent to at least some of the fractures.
Fluid flow paths are formed from the wells through the fractures
into the chimney and fluid is circulated through these fluid flow
paths and into the chimney at rates creating a pressure drop from
the wells to the chimney. Oil shale-reactive properties are
imparted to the circulating fluid whereby the fluid reacts with the
oil shale thereby moving solid components thereof into void spaces
formed within the chimney increasing the permeability of the oil
shale formation relative to the permeability of the chimney in
regions surrounding the chimney.
BRIEF DESCRIPTION OF THE DRAWING
FIG. 1 is a vertical cross-sectional view of an oil shale formation
prior to detonating a plurality of explosive devices within the
formation;
FIG. 2 is a diagrammatic plan view of the cavities formed by
detonating the explosive devices within the oil shale formation of
FIG. 1; and
FIGS. 3 thorough 5 are vertical cross-sectional views of the
teachings of this invention as applied to the final rubble zones
created by detonating all of the explosive devices of FIG. 1.
DESCRIPTION OF THE PREFERRED EMBODIMENT
FIG. 1 shows subterranean oil shale formation 11 having a primary
explosive device 12 located within the formation 11. Primary
explosive device 12 is preferably surrounded by a plurality of
explosive devices 13. Devices 13 may be of lesser energy than
device 12, if desired. However, optimum results may be obtained by
the formation of substantially equal-size chimneys as will be
discussed further hereinbelow. The device 12 can be either nuclear
or nonnuclear; if a nuclear device is detonated in the subterranean
oil shale formation 11, a strong shock wave from the nuclear device
begins to move radially outwardly, vaporizing, melting, crushing,
cracking and displacing the oil shale formation 11. After the shock
wave has passed, the high-pressure vaporized material expands, and
a generally spherical cavity (i.e., the central cavity 14 in FIG.
2) is formed which continues to grow until the internal pressure is
balanced by the lithostatic pressure. The cavity 14 persists for a
variable time depending on the composition of the oil shale
formation 11 and then collapses to form a chimney 15 (FIG. 3).
Collapse progresses upwardly until the volume initially in the
cavity is distributed between the fragments of the oil shale
formation 11. The size of the cylindrical rubble zone (i.e., the
"chimney" 15) formed by the collapse of the cavity 14 can be
estimated from the depth and explosive yield of the nuclear device
and properties of the earth formations.
A zone of permeability 17 within the fragmented oil shale formation
is formed surrounding the "chimney" 15 as can be seen in FIG. 3.
The permeability of this zone 17 may be preferably increased by
surrounding the primary explosive device which formed the central
cavity with a plurality of devices 13. For example, in FIG. 1, a
primary nuclear explosive device 12 is surrounded by explosive
devices 13, equally spaced from each other and radially spaced from
the primary explosive device 12. These devices 13 are preferably on
substantially the same horizontal plane as the primary nuclear
device (see FIG. 1) and 500 to 1,000 feet from the nearest part of
the outer wall of the central cavity 14 produced by the explosion
of the high energy nuclear device 12. As discussed above, the
devices 13 preferably have an energy yield substantially equal to
that of the primary high energy nuclear device 12 and can be either
nuclear or nonnuclear.
The explosive devices 13 form cavities 18 (FIG. 2) when detonated,
surrounded by fractured zones 19 as can be seen in FIG. 2. The
devices 13 may be preset with detonating means adjusted to explode
upon arrival of the main shock wave from the explosion of the
primary explosive device 12. Alternatively, the devices 13 may be
suitably delayed to explode after passage of the main shock wave.
Of course, another characteristic of the explosion of the primary
explosive device 12 can be utilized to detonate the devices 13, as,
for example, changes in temperature or pressure as a result of the
explosion of the primary explosive device.
Because of this time delay, either detonating the devices 13 upon
arrival of the main shock wave or after the main shock wave has
passed but before the central cavity 14 becomes filled with rubble
due to the chimney collapse from above, the shock waves from the
secondary explosions (that is, the explosions of the devices 13)
will cause spalling into the central cavity. The movement of rock
towards the central cavity 14 due to the satellite explosions will
enhance the permeability in the regions between these explosions
and the central cavity 14, by allowing development of a greater
void space in this region. This void space, indicated as a zone of
increased permeability 17 in the drawings, has a high and uniform
permeability in the fragmented oil shale formation 11.
Thus, chimney 15 includes a lower rubble zone 21 and an upper void
space 22. Similar "chimneys" formed by the detonation of the
devices 13 also include lower rubble zones and upper void spaces.
For example, as illustrated in FIG. 3, two such chimneys 23, and
24, formed, for example by devices such as explosive devices 13,
form lower rubble zones 25 and 26 and upper void spaces 27 and 28,
respectively. A plurality of fractures 29 are formed between the
satellite "chimneys" and the central chimney 15 as illustrated in
FIG. 3. Fractures 29 are generally substantially horizontally
extensive through formation 11; however fractures 9 may also be
substantially vertically extensive. A more detailed discussion of
the formation of chimneys 15, 23 and 24 appears in the
aforementioned copending application to Closmann et al., Ser. No.
653,139, filed July 13, 1967, now U.S. Pat. No. 3,448,801.
Alternatively to forming chimneys 25 and 26 as indicated
hereinabove, after chimney 15 is formed, fluid flow paths through
fractures 29 may be formed by hydraulically or explosively
fracturing wells 32 and 33 by fracturing procedures such as those
known in the art, so that the latter fractures communicate with
fractures 29.
Referring to FIG. 3, in accordance with the teachings of this
invention, a producing well borehole 30 is extended from the earth
surface 31 into communication with the lower portion of chimney 15.
A plurality of outlying injecting well boreholes, such as well
boreholes 32 and 33, shown in FIG. 2, are extended from earth
surface 31 into communication with the upper portion of chimneys 25
and 26, respectively. Well boreholes 30, 32, and 33 are preferably
cased as is well known in the art. The vertical intervals, that is,
the "chimneys" or rubbled or fractured regions into which the
outlying wells are opened are preferably located at substantially
the same depth as the chimney 15.
Fluid flow paths are then formed from the outlying well boreholes
32 and 33 to chimney 30 through the fractures extending out from
chimneys 25 and 26 into communication with interconnecting
fractures 29. These flow paths are preferably enlarged by
circulating acidizing fluids from well boreholes 32 and 33 through
fractures 29 and into chimney 30. Another method of forming or
enlarging such fluid flow paths from the outlying wells to the
central chimney 15 is to fracture the oil shale formation by
flowing an electrical current between electrodes that contact the
oil shale. A more detailed description of this process for
fracturing an oil shale is given in an article by Melton and Cross,
Journal of Petroleum Technology, Jan., 1968, pp. 37--41, which is
incorporated herein by reference. The electrical energy may be
applied prior to or during the initial circulation of fluid from
the outlying wells to central chimney 15 as will be explained
further hereinbelow.
In operation, fluid is injected into the satellite chimneys 25 and
26 through well boreholes 32 and 33, through fractures 29 and into
the rubble zone 21 of chimney 15 as indicated by the arrows in FIG.
3. Fluids are then produced from central chimney 15 through
producing well borehole 30.
A preferred method for producing shale oil from the oil shale
formation 11 of FIG. 3 is to inject a combustion-supporting gas,
such as air or oxygen, into the satellite well boreholes after the
hydrocarbons in the formation have been raised to ignition
temperature. This may be accomplished by various means well known
in the art, such as by lowering suitable heaters down well
boreholes 32 and 33. A combustion zone is thus formed which
gradually moves through the intervening rock between chimneys 25,
26, and 15 by means of fractures 29 into central chimney 15. As
this rock is heated, it expands, releasing gas and other products
and effectively provides additional flow paths for the injected
fluid. At the same time, as the rock nearest the satellite chimneys
expands, it expands or moves towards the central rubble chimney 15
thus tending to relieve some of the thermal stress generated by the
hot fluids. This method makes the porosity distribution of oil
shale formation 11 more uniform by developing some porosity
adjacent the outside of chimneys 25 and 26 where the rock is first
heated and by exerting pressure due to thermal expansion on the
central rubble zone (i.e., chimney 15) thus tending to reduce the
porosity of central chimney 15.
As an alternative to air or oxygen, the injected fluid may be a
heated gas, liquid, or steam. If steam is used, thermal expansion
of the rock takes place. After the rock is heated, combustion may
again be carried out. The displaced fluids are produced from the
bottom of the central chimney 15 to which they drain and out of
production well borehole 30. As it becomes desirable to treat more
of the upper regions of the rock, the production well borehole 30
may be shut off at the bottom and perforated at progressively
higher places within the central chimney. This is illustrated in
FIG. 4 where the lower end of the well borehole 30 is packed off,
such as by a wireline-set or a tubing-set packer 34, and a
perforating device 35 is lowered into well borehole 30 by means of
cable 36. The casing of well borehole 30 is then perforated by
device 35 as is well known in the art thus forming a plurality of
perforations 37 which may be progressively moved up well borehole
30 as the central chimney 15 is produced.
Alternatively to injecting a fluid such as disclosed hereinabove,
acid may be injected from the outlying chimneys through fractures
29 and into central chimney 15. The acid flows through fractures
29, leaching out part of the rock and developing some heating. This
acid is produced from the central chimney 15. In some cases, fine
suspended material (e.g., produced by decomposition of the oil
shale during combustion or acidizing) may be carried from the
inlets of this flow system (e.g., chimneys 25 and 26 and/or
fractures communicating with wells 32 and 33) and deposited near
the central chimney 15. This action makes the overall flow path
more uniform. This step may be then followed by hot fluid injection
or a combustion process such as previously discussed
hereinabove.
In both cases, that is, the circulation of a fluid such as a gas or
an acid, when the oil shale-reactive properties of a fluid comprise
or include a temperature sufficient to pyrolyze kerogen in the oil
shale and the fluid is flowing through interconnected fractures
between chimneys at a rate providing a pressure gradient along the
flow path, pyrolysis-induced fracturing tends to enhance the
movement of solids and fluids in the direction of the lowest
pressure. Within a nuclear detonation chimney, such as, for
example, chimney 15, the permeability increases with increases in
height and becomes substantially infinite in the void at the top.
Since the fractures that are formed by a nuclear detonation are
initiated by a radially expanded bubble centered in the lower
portion of the region that becomes a chimney, the density of
radially extending fractures is less at depths near the top of the
chimney. Conventional equipment and techniques, such as heaters,
pumps, a separator and a heat exchanger, may be used for
pressurizing, heating, injecting, producing, and separating
components of the fluid circulated through the oil shale formation
11. The production of the fluid may be aided by downhole pumping
means, not shown, or restricted to the extent necessary to maintain
the selected pressure within the oil shale formation 11.
When oil shale pyrolyzing fluid is circulated along a path
extending through fractures, from the outlying wells to a nuclear
detonation chimney, in the initial stages and at depth near the top
of the central chimney, the permeability is the least, the pressure
gradient is the highest and the resistance to solid-material
displacement toward the central chimney is the least. As fractures
are formed by the pyrolysis of the oil shale, they tend to form
first in the regions which are contacted by the hottest portion of
the fluid, and these regions are located near the outlying wells.
The largest fractures tend to form at depths near the top of the
central chimney where the resistance to the movement of solid
material is the least. In addition, the relatively high
permeability within the central chimney tends to decrease as solids
move into the central chimney. This results in both the creation of
additional permeability in regions surrounding the central chimney
and an increase in the permeability in the surrounding regions
relative to that within the central chimney. The creation of
additional permeability in regions surrounding the central chimney
increases the amount of permeable oil shale material that is
available for depletion and the increase in permeability in the
surrounding regions increases the uniformity of the depletion.
The fluid being circulated through central chimney 15 is preferably
injected into all the satellite chimneys or intervals into which
outlying wells have been opened and, at least initially, produced
from near the bottom of central chimney 15. The fluid circulation
may advantageously be initiated by circulating air or relatively
cool liquid to sweep out any shale oil released by the nuclear
detonation. When oil shale-reactive properties imparted to the
circulating liquid comprise or include a temperature sufficient to
pyrolyze the oil shale, the method of this invention provides a
unique advantage over processes in which production wells are
extended through the chimney, or through the immediately adjacent
relatively highly fractured zone, to provide conduits arranged for
a downward advance of a combustion front. In the process, when the
advance of a heat front towards the production well borehole 30
subjects the borehole 30 to a high temperature, the production well
borehole conduit or conduits, i.e., the well casing or tubing
string, may be shortened to terminate in a relatively cool zone
near the top of central chimney 15. After an extended and
relatively uniform permeability distribution has been obtained by
circulating fluid from the outlying wells to central chimney 15,
the flow direction may be reversed, with central chimney 15 now
operating as a very large diameter central injection well as
illustrated in FIG. 5. Such a flow reversal allows the pyrolysis
products to be produced from the tops of the intervals (for
example, chimneys 23 and 24) into which the outlying wells are
opened. This capability of the present process to avoid heat damage
to the production well conduits provides material improvement in
the economy of the shale oil-production process.
As discussed hereinabove, the oil shale-reactive properties
imparted to the circulating fluid may advantageously comprise or
include acidizing properties in respect to mineral components, such
as the carbonates, in the oil shale. In addition to acids that are
commonly used in well acidization treatments, acids suitable for
use in the process of this invention comprise those derived from
sulfur, such as sulfuric acid; sulfurous acid, etc., and/or their
anhydrides, such as oleum, sulfur trioxide, sulfur dioxide and the
like, and nitric acid and acids derived from the oxides of nitrogen
and the like. The sulfur-derived acids are not generally used in
well acidization treatments because of the tendency of the
resultant aqueous solutions of such acids to precipitate polyvalent
metal sulfates, sulfites, etc. In the initial stages of the present
process, such precipitates tend to be deposited within the large
voids in the central chimney 15, where the flow rate drop relative
to those in the smaller void spaces in the fractures 29 leading
central chimney 15. Thus, in the process of this invention, such a
initial dissolving of solid materials and subsequent precipitation
of solid materials is advantageous since it increases the rate at
which the permeability in the outlying regions is increased
relative to that within the central chimney 15.
Thus, the specific arrangement of injection and production
locations and fluid pressure gradients, together with the
fracturing pattern of a nuclear detonation and the behavior of a
mass of oil shale undergoing pyrolysis, improves the distribution
of the permeability of the oil shale formation in and around a
nuclear detonation-created chimney while shale oil is being
produced.
The outlying chimneys may be formed either in the manner disclosed
hereinabove as disclosed in the aforementioned copending
application to Closmann et al. In either case, it is preferable
that the outlying chimneys be located at substantially the same
depth as the central chimney. Optimum results are obtained when the
outlying chimneys are substantially equal to the height of the
central chimney, such as when the outlying chimneys are formed by
the use of explosive devices of relatively similar explosive energy
as that used to form the central chimney.
* * * * *