Note: Descriptions are shown in the official language in which they were submitted.
CA 02289147 1999-11-22
APPARATUS FOR SEPARATING COMPONENTS IN WELL FLUIDS
Field of the Invention
This invention relates to an apparatus for separating components of well
effluent, and more particularly, t;o a system for use in processing drilling
fluids utilized
in the under-balanced drilling technique of production zones.
This is a division of co-pending Canadian Patent Application Serial No.
2,184,511, filed on August 28, 1996.
Description of the Prior Air
The use of under-balanced drilling, while presently a more expensive operation
to perform than conventional methods, is gaining acceptance in view of
enhanced rate
of recovery and total well production which is achieved by this method. The
better
production characteristics obtained result from the lack of damage caused to
the
surrounding formation of the borehole experienced in known methods utilizing
drilling
mud which presents a borehole pressure greater than that present in the
formation.
In the closed separating systems developed for under-balanced systems to date,
a number of the operating characteristics have presented major problems,
including
those relating to safety, erosion of parts of the system, incomplete
separation and
potential disruptions or failures due to the presence of hydrates. The
principle of under-
CA 02289147 1999-11-22
balanced drilling involves pumping fluids into the drilling
area of the bore:hole at a pressure which is below the
pressures in the formation surrounding the borehole, as
opposed to that of providing a higher drilling fluid pressure
by the~use of dnillinc~ mud. When areas of high pressures are
encountered in the formation, during under-balanced drilling,
the sudden expul,sion.of higher pressure fluids into the
closed system may cause serious problems. This condition
presents problems in i:he quality of separation and with
regard to safety. In addition to not having facilities to
deal with such abnormal conditions which develope, known
facilities of tree typE:, which include separating chambers in
a single stage Horizontal or vertical .vessel, do not
accomplish suffi.cient:ly complete separation, particularly of
the gas from thE: liquid under the varying conditions
experienced.
A corrunon practice in known systems is to provide a main
choke valve in i:he pipe returning the fluids from the well
head to the clo:~ed separator vessel so as to effectively
determine the arnount of fluid reaching the vessel. These
r:luids contain, of course, the drill cuttings, and these,
together with a significant amount of pressure drop across
the choke valve, result in serious erosion problems. The
continued damage: to the valve is a safety concern and
significantly adds to the expense of operating the. system,
not only due to the high cost of such valves, but because of
2
CA 02289147 1999-11-22
downtime and maintenance costs.
Also, the expansion of the fluids caused by the choking
action of the valve in the control _of the~amount of fluids
entering the system may also cause the formation of hydrates
in the~fluid to the extent there is a loss of control of the
flow of the drilling fluids into the system or even a
complete blockage of the inlet. Moreover serious damage can
be caused within the system if parts of the frozen material
break away and are forced rapidly downstream by the back-up
of pressure behind the blockage. The presence of hydrates
are also known to cause problems in other parts of the system
such as a freeze up in the gas line running from the
separator vessel to th,e flare stack.
In order to deal with such problems caused by the
hydrates and also to achieve better separation
characteristics in known systems, heating units are used. For
example, heating devices have been adopted to apply heat to
the incoming fluid in the line both before and after the
choke valve which precedes the inlet to the separator vessel.
This is done by passing the incoming fluid through coils
which are externally exposed to heat such as a heated medium
in a chamber. The well fluid being carried in the coils
contains the drill cuttings, and therefore, the heating unit
is also exposed internally to a higher rate of erosion due to
the abrasive effect of the drill cuttings.
3
CA 02289147 1999-12-20
Summarar of the Invention
It is an object o~f the present invention to provide a separating system,
which when used in association with an under-balanced drilling procedure, will
cope with significant varying fluid pressures of the drill fluid received from
the
borehole without necE~ssitatirng an interruption of the drilling procedure.
It is also an object of the present invention to accomplish satisfactory
separation of the gases and liquids in the drilling fluid in spite of
fluctuations in
the incoming drill fluids, and to achieve effective separation of the drill
cuttings
in a manner to reduce erosion due to the presence of the drill cuttings.
According to the present invention there is provided a separating
apparatus for use in separating components contained in a return fluid from a
borehole being formed by a downhole drill penetrating subsurface formations
during a drilling operation of the type in which a selected drill fluid is re-
circulated from the separating apparatus to the downhole drill to provide a
pressure at the downhole drill generally below existing pressures encountered
in the formations. The' separating apparatus includes at feast first and
second
separating stages. Tree first separating stage includes a closed first vessel
having an inlet for receiving tree return fluid under pressure from the
borehole,
a first vessel liquid outlet means for maintaining liquids separated from the
return fluid entering the first vessel at a level to provide thereabove a
space in
the first vessel for containing ;~ volume of gas separated from the return
fluid, a
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CA 02289147 2000-02-11
First gas outlet means in communication with the volume of gas above the level
of
the liquid in the first vessel, valve means in gas outlet means for varying
the
quantity of outflow of gas from the volume of gas in the first vessel, and
pressure
sensor means responsive to pressures in the first stage affected by the
pressure of
the return fluid and controlling the valve means for varying the outflow of
gases to
thereby maintain a pressure in the first vessel within a preselected range.
The
second separating stage includes a horizontal second vessel of greater volume
than
the first vessel, an inlet means in the second vessel for receiving liquids
transferred
from the liquid outlet means of the first vessel, the second vessel containing
separating means providing a first collecting chamber for accumulating a first
liquid in the first chamber and a second chamber for collection of a second
liquid
of a density heavier than the first liquid in the first chamber, a first
separated liquid
outlet means for removing the first liquid from the first chamber of the
second
vessel, and a second separated liquid outlet means for removing the second
liquid
from the second chamber of the second vessel. The apparatus further includes
conduit means communicating with at least one of the first and second
separated
liquid outlet means for supplying drill fluid to the drilling operation.
In a specific embodiment of the invention the first stage includes a demister
providing communication between the volume of gas in the first vessel and the
gas
outlet means of the first vessel for removing liquid particles suspended in
the
volume of gas on leaving the space above the liquid level of the
S
CA 02289147 1999-12-20
first vessel.
Preferably the inlet of i:he first vessel includes an initial separator for
separating gas from liquids in the return fluid upon entry of the return fluid
into
the first vessel. The initial separator may include means for separating drill
cuttings from the return fluids upon entry of the return fluid into the first
vessel.
The first vessel preferably has drill cuttings outlet means in a lower part of
the
first vessel for withdrawing accumulated drill cuttings from below the initial
separator, and there rnay be provided sparging nozzles in the first vessel for
directing pressurized liquid towards the drill cutting outlet means to assist
in
removal of the drill cuttings from the first vessel.
In a specific embodiment of the invention, the liquid outlet means of the
first vessel may have flow control means actuated by level sensors within the
first vessel.
According to one aspect of the invention, the first vessel may be provided
with weir means defining chambers for separately accumulating in the first
vessel liquids of at least two different densities, and wherein the liquid
outlet
means may have at least two separate liquid outlets for separately withdrawing
liquid from each chamber. In such an embodiment, separate metering means
can be provided for determining the quantity of flow from each chamber of the
first vessel prior to directing flow of the liquids to the second separating
stage.
In a preferred e~mbodirr~ent of the invention the second stage has a
second gas outlet means for removing residual gas separated from the liquids
6
CA 02289147 1999-12-20
transferred from the liquid outlet means of the first vessel. There may be
further
provided a separator for receiving the liquids transferred from the first
vessel
and centrifugally separating residual gases from the transferred liquids prior
to
discharging the liquids into the second vessel for further separation of the
liquids in the second vessel by different densities and removal through the
first
and second separated liquid outlet means of the second vessel. Such
separator preferably includes means for also separating drill cuttings from
the
liquids transferred from the first vessel.
Another aspecl: of the present invention may reside in the first and
second outlet means of the second vessel including level control means for
maintaining an upper level to provide thereabove a volume for collecting gas
above the liquids from residual gases escaping from such liquids, and in such
a
structure a second gas outlet means is provided in the second vessel for
removal of gases accumulated above the liquids therein. The second gas outlet
means may have a flaw control means for establishing an operating pressure
range of the volume gas in the second vessel.
In yet another specific .aspect of the present invention, the first vessel is
a
horizontal high pressure vessel, and an initial separator is located at one
end of the
horizontal pressure vessel. The first vessel liquid outlet means may be spaced
away from the one end towards an opposite end of the horizontal pressure
vessel,
and the drill cutting outlet means is located below the initial separator.
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CA 02289147 1999-12-20
In yet another norm of the present invention, the inlet means of the
second vessel is located adjacent one end of the vessel, and this vessel has a
transverse weir spaced means at a distance from the one end and defining
therewith an inlet chamber for initially receiving the liquids from the first
stage,
the weir means defining an upper edge over which the liquids flow towards the
first and second chamber in the second vessel. The second vessel may also
have a solids outlet means for removing particles deposited in the inlet
chamber of the second vessel'.
Brief Description of the Drawings
In the accompanying drawings which show various features of the
present invention, by way of examples,
Figure 1 is an e~levational view illustrating a system according to this
invention as set up for operation adjacent a borehole, much of the pipe work
necessary for conducting the fluids and liquids being processed by the system
being removed for simplicity;
Figure 2 is a plan view of the high and low pressure vessels included in
the present invention with porlrions of the vessels cut away to show the
interiors
thereof and also showing in a somewhat schematic manner certain conduits
used in the transfer of the liquids in the system;
Figure 3 is an enlarged cross sectional view of a separator
means in the form of a vortex separator as seen
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CA 02289147 1999-11-22
from line 3--3 of Figure 2 and illustrating the main
separator means according to the present invention;
Figure 4 is across sectional view through the main
separator means as viewed from line 4--4 of Figure 3;
Figure 5 is a view from the right hand end of the low
pressure vessel as seen in Figure 2, and with the heating
device in place;
Figure 6 is a cross section view through the low
pressure vessel and the heating device as seen from the line
6--6 of Figure 2;
Figure 7 is a longitudinal cross sectional view through
the high pressure vessel as seen from line 7--7 of Figure 2,
again with certain ports removed for the sake of clarity;
Figure 8 is a side view of the high pressure vessel
which has been t~roken away to show interior components;
Figure 9 is. a cross sectional view through the high
pressure vessel as seen from line 9--9 of Figure 2.
Figure 10 is a cross sectional view through a part of a
gas outlet mean~~ used in both the high and low pressure
vessels as seen from line 10--10 in Figure 8 and showing a
de-misting device for removing liquid particles from the gas
leaving the ves:>els;
Figure 11 i.s a cross sectional view of the de-misting
device as seen from line 11--11 of Figure 10;
Figure 12 is a longitudinal cross sectional view through
the low pressurE: vessel as seen from the line 12--12 of
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CA 02289147 1999-11-22
Figure 2, with certain parts removed for the sake of clarity;
Figure 13 is a partial sectional view.taken through the
end of the high pressure vessel~at-the end containing the
separator means and showing a device for withdrawing drill
S cutting samples from within the vessel;
Figure 14 is a cross sectional view of the sample taking
device as seen from the line 14--14 of Figure 15;
Figure 15 is a partial sectional view taken through the
end of the high pressure vessel, and showing a solids level
lU indicator; and
Figure 16 is a view of the solids level indicator as
viewed in the direction of the arrow A in Figure 15.
Description of a, Preferred Embodiment
Referring t.o Figure 1, there is illustrated generally at
15 3U a separation apparatus or system according to the present
invention and wherein the system is set-up on site adjacent a
borehole 31 of a well 32 being drilled. The system is shown
as being built i.n a mobile form so that it can be moved from
site to site for- use particularly when under-balanced
20 drilling is being carried out. While the system 30 is shown
as being mounted on a wheeled flat bed trailer 37, it may
also be mounted on a skid arrangement if, for example, it
would appear that the system may not have to be frequently
moved significant~distances.
25 As earlier described, under-balanced drilling usually
results in a superior producing well. In utilizing an under-
lU
CA 02289147 1999-11-22
balanced system, it is a common practice to turn the downhole
drilling operation from the vertical borehole 31 shown in
Figure 1 and to continue drilling downhole substantially
horizontally into the underground reservoir zone (not shown)
to thereby maximize exposure of the drill hole to the
formation containing the hydrocarbons to be recovered. Once
the borehole is turned from the vertical, the driving of the
drill bit is usually accomplished by way of the drilling
fluid being forced down the drill tube, the flow of fluid
being depicted in Figure 1 by the arrow 34 through a drill
tube 33. The drill fluid, after providing the drive to the
cutter bit of the drill, (not shown), passes back up a well
casing 35 in the annular space between well casing 35 and the
drill tube 33, the drill cutting being carried in the drill
fluid, as indicated by arrow 36. The systern 30 of the
present invention is set up at a distance from a wellhead
area 42, which also includes the associated drilling rig
equipment which has not been included in Figure 1 for the
sake of clarity.
As previously described, in under-balanced drilling, the
fluid 34 being pumped into the drilling location of the
borehole, and in the case of horizontal drilling, also
utilized to drive the drill bit, is maintained at a downhole
pressure of a lesser,value than that existing in the
formation surrounding the borehole at the drilling location.
Having established the pressure in the formation, the
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CA 02289147 1999-11-22
selection of the fluid to be pumped into the well is
determined by ca:Lculating the pressure which will be provided
in the drilling ;area for the particular depth of well
involved. For example, for a S,OOU foot depth borehole,
based on the densities of water or an oil, such as diesel
oil, water would provide a downhole pressure of 2165 p.s.i.g,
while diesel oil provides a downhole pressure of 1750
p.s.i.g. Thus, if the pressure in the surrounding formation
of the drilling .area is determined as being 2,000 p.s.i.g.,
it can be seen that diesel oil would be utilized rather than
water, to provide an under-balanced condition. In the event,
the formation pressure is considerably less than the example
above or if due to a greater depth of the borehole, the
column of fluid is heavier, so that the column of diesel oil
is not significantly less than the formation pressure, it is
a known practice to insert gas, such as nitrogen into the
diesel oil to reduce its density. Thus, the column of fluid
in the well could be established to provide a pressure of the
drilling location of a lesser value of that in the formation.
In the event the fluid being pumped into the drill tube
33 is diesel oil, the fluid will pick up, of course, the
drill cuttings so that the returning fluid, as shown at 36,
will include such solid particles. In some instances, a gel
compound is added to the fluid entering the drill tube to
establish a different characteristic for the fluid, such as a
better capability of carrying the drill cuttings back up to
12
CA 02289147 1999-11-22
the surface in the drill fluid 36. Moreover, it is also
common for water from the surrounding formations to join the
drilling fluids, and the under-balanced condition also
encourages gas~as and oil to exit the formation and form part
of the drill fluids 36 returning to the separation system 30
of the present invention. As the system 30 is closed and
thereby prevents the escape of the gases in the fluid from
escaping to the atmosphere, the system 30 must be capable of
coping with significant fluctuations in the pressure of the
returning fluid 36 as well as providing the separation of the
gases and drill cuttings from the liquids and further
separating the liquids so that a separated oil is available
for returning to the drill tube.
In the system 30', the returning fluids 36 flow from
their annular passage in the borehole out through a delivery
pipe 38 to a high pressure vessel 40 which forms a first
stage 47 of the separating system. The delivery pipe 38
includes a choke valve means 41, which under certain
conditions, may be closed or partially closed to completely
shut off or to affect the flow from the borehole 31 to the
separating system 3U.
As will f~e described in more detail below, the high
pressure vessel 40, which is in the form of a closed
horizontal cylindrical tank, contains a separator means 43,
(Figure 2), ir.~ a first chamber 70 thereof which separates
from the incoming drill fluid 36 a major portion of the drill
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CA 02289147 1999-11-22
cuttings and gases. The separation of the liquids is further
achieved in following second and third chambers 91 and 94, in
the high pressure vessel 4U, before-the liquids separately
exit the high pressure vessel 40. The separate liquids are
S then metered by meters 104 and 105, recombined, heated by a
heating device 48 and conducted to a second stage 49 provided
by a low pressure vessel 44 which is a horizontal tank in the
form of an elongated cylindrical outer wall or shell 53. A
final separation of the liquids occurs in a second stage 49,
and further separations of gases and solid materials are also
carried out here. In the example of the drilling conditions
described above, the oi.l separated at the second stage 4y is
delivered from an outlE:t means 55 to a flow control means 52
located at the rig site via pipe 51 and this oil is returned
l~ to the interior of the drill tube 33 via a pipe 54.
The separated gases exit from the two vessels 40 and 44
and may be conducted to a flare stack 64. The gas exits the
high pressure vessel 40 via a pipe 56 through an outlet means
57 and includes a. flow control means 60 for permitting a
setting of the o~~erating pressure within the high pressure
vessel 4U. The gas exiting via pipe 56 is passed through the
heating device 48 before leaving the system 30. While the
flow control means 60 is preferable in the form of an
adjustable back F>ressure valve, the flow control may actually
be performed by the gas entering a gas gathering system or by
the back pressure of a gas compressor functioning as a
14
CA 02289147 1999-11-22
pressure booster. The gas exiting from the low pressure
vessel 44, by way of pipe 61 from a gas outlet means 62, is
preferably also heated by way of pipe 61 passing through the
heater device 48, and the magnitude of the flow is controlled
by a separate flow control means 63 which may be of the same
nature as that described in relation to flow control means
60.
As indicated abave, the pressure within high pressure
vessel 40 is determined by the setting of the flow control
1J means 60 in gas outlet pipe 56, which in turn governs the
flow of fluid 36 thraugh the delivery pipe 38 into the high
pressure vessel 40. Thus, during normal operating
conditions, the choke valve means 41 may be maintained in its
fully open condition. This avoids, therefore, a high rate of
1S erosion as normally occurs due to the presence of the Grill
cuttings in the fluid 36 and the large pressure drop due to~
the choking action of the valve as it would norrnally be used
to determine th,e rate of flow from the well. Also the
previously described problems due to the formation of
2U hydrates during such choking of the flow are also avoided.
Taking into account that common well head flowing
pressures are in the order of 50-500 p.s.i.g., the high
pressure vessel. 40 is designed for operating pressures of 50-
200 p.s.i.g. with a maximum operating pressure preset at 500
2S p.s.i.g., but higher maximum operating pressures may be
increased, for example, to 1,500 p.s.i.g. As shown both the
CA 02289147 1999-11-22
high pressure vessel 40 and the low pressure vessel 44 are
elongated horizontal cylindrical vessels with outwardly
curved ends, and preferably the low pressure vessel 44 is
considerably longer than the high pressure vessel 40.
A weir 66 extends transversely across the high pressure
vessel 40 a distance inward from a first end 67 of the high
pressure vessel 40 so as to define adjacent that end of the
vessel the first separating chamber 70 which receives
delivery of the well fluid 36 from pipe 38 to inlet means 71.
The weir 66 has a horizontal upper edge 72 over which the
liquid must flow from the first chamber 70 to the second
separating chamber 91. Connected to the inlet means 71 is
the separator means 43 which is located in the first chamber
70. The separator means 43 is provided to separate a major
portion of the solids, which are, in the main, the drill
cuttings, and also to separate a significant amount of the
gaseous components from the liquids which may include water,
oil and other liquid petroleum products.
Referring to Figures 3 and 4, the separator means 43
includes a main m.anifol.d portion 73 which is in the form of a
horizontal, elongated tubular member 74 having its interior
in communication at an inner end with the inlet means 71 so
as to receive fluid 36 directly~from delivery pipe 38. The
outer end 75 of the tubular member 74 is closed so as to form
an interior manifold chamber 76. Disposed beside the
manifold portion 73 are a plurality of separate housing means
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CA 02289147 1999-11-22
77 which may be of identical form. As best seen in Figure 2
the individual housing means 77 are arranged along one side
of the manifold portion 73 and in .two rows in which the
housing means 77 are staggered so as to be able to
accommodate six housing means. Depending on the space
available and the relative size of the housing means 77, any
number of such housing means 77 may be provided, and
alternatively two sets of housing means, one set on each side
of the manifold portion 73, could be utilized. Each housing
means 77 has an inner cylindrical wall 80 defining a swirl
chamber 81, the central axis 79 of the cylindrical wall 80
being disposed vertically. Each housing means 77 is affixed
to the tubular member 74 forming the manifold portion 73 by
way of a tubular connector member 82. The tubular member 82
is in communication at one end with the manifold chamber 76
at an inner end and with an upper portion of the swirl
chamber 81 at an outer end, thus providing a fluid passage 83
from the manifold portion 73 to the upper end of the swirl
chamber 81.
A lower end 78 of the swirl chamber 81 is open, and
during operation, the lower end 84 of the housing means 77 is
disposed below a liquid level 68 of the first separating
chamber 70. A vertical tubular portion 84 of the housing
means 77, which is open at opposite ends, extends through the
otherwise closed upper end of the housing means 77 and
terminates in an upper open gas outlet end 85 above the
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CA 02289147 1999-11-22
separator means 43. The tubular portion 84 has a lower gas
inlet end 86 below the upper end of the swirl chamber 81.
Thus, as the fluid 36, which is at a pressure in the manifold
chamber 76 higher than the internal pressure within the high
pressure vessel 40, i.s expelled through the fluid passage 83
and into the swirl chamber 81, the rotating motion of the
heavier solids 88 and liquids carries these components
through the open lower end of the housing means 77 into the
portion of the first separating chamber 70 below the
separator means. 43. To ensure an effective swirl is imparted
to fluid entering the upper part of the chamber which, in
cross section i.s in the form of an annulus surrounding
tubular portion 84, the fluid passage 83 joins the annulus in
a longitudinal direction as best seen in Figure 4. The
lighter gas denoted by the arrows 89 escapes from the
swirl of liquid and solid particles 88 and is forced to the
central portion of the swirl chamber where it is able to
escape upwardl~~ through the tubular portion 84 as indicated
by arrow 89a to join the volume of gas 87 separated from the
2U fluid and located above the liquid level 68 in the high
pressure vessel. 40. The swirl mixture of drill cuttings or
particles 88 and liquids being.expelled out the lower of the
housing means 77 enters the liquid surrounding the lower end
of the housing means, and a majority of the heavier drill
cuttings, and particularly the coarser particles, continue
towards the bot:tom~of the first separating chamber 70 and
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CA 02289147 1999-11-22
accumulate there, as indicated at 9U. The liquids as
indicated by arr~~ws 107, on the other hand, reverse direction
outside of the h~~using means 77 and flow towards the upper
level of the liquid in the first separator chamber and
overflow the upper edge 72 of weir 66 to enter the second
separating chamber 91.
The second separating chamber 91 in the high pressure
vessel 90 is defined between the weir 66 and a second weir 92
which is spaced inward from a second end 93 of the high
pressure vessel 40, the upper liquid level in this chamber
being substantially the same as that in the first separating
chamber 70. A third separating chamber 94 is defined between
the weir 92 and the second end 93 of the high pressure vessel
40. As the liquids from the first chamber 70 pass over the
weir 66, the liquids become less turbulent, and as a result
some of the finer solid particles still remaining in
suspension settle to the bottom. The, height of the second
weir 92 assists in retaining the solid particles in the
second separating chamber 91. In the second chamber 91 there
is also substani~ial separation between the different liquids.
Thus, in the ex~~mple suggested above, the water 109 content
settles out bel~~w the lighter oil 101 and is retained in the
second chamber 91. To assist in the separation in the second
chamber 91, there is provided internally of the high
pressure vessel 40, a heating means 95 which will be
described in further detail below. Located within separation
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CA 02289147 1999-11-22
chamber 91 is a water level sensing means 98 which is
utilized to control water outlet means 96 in a water outlet
pipe 97 of the high pressure vessel. The sensing means 98
which is preferably of the float type is disposed and
calibrated for maintaining the level 99 of the water in the
second separating chamber 91 below an upper edge 111 of the
second weir 92 so that the oil which collects above the
heavier water flows over the weir 92 and collects in the
third separating chamber 94. The level 110 of the oil
collected in the third chamber 94 is sensed by a level sensor
100, (Fig. 7) and the level thus sensed is used in oil outlet
means 102 (Fig. 8) which regulates the flow of the oil 101
from third chamber 94 though an oil outlet pipe 103 (Fig. 2>.
Again in the third chamber 94 of the high pressure vessel 40,
because of the lack of turbulence, additional fine cuttings
may settle to the bottom of the chamber.
Located in the water outlet pipe 97 and the oil outlet
pipe 103 there are provided water meter 104 and oil meter
105, respectively. The readings from the meters 104 and 105
provide important information regarding the proportions of
water and oil in the drilling fluid returning from the well
which is used in the drilling operation. Subsequent to being
metered, the liquids passing through pipes 97 and 103 are
recombined in pipe 106 which passes through heating device 48
before entering the second stage of separation in low
pressure vessel 44.
CA 02289147 1999-11-22
Referring to Figures 5 and 6, details of the heater
device 48 are ~~hown. The heater includes a sheet steel outer
jacket 112' having an outer vertical side plate 113, and a
shorter inner vertical side plate 114, a horizontal top plate
115 and a horizontal bottom plate 116. The inner edge of the
plate 115 and t:he top edge of side plate 114 are affixed to
the outer surface of the outer cylindrical shell 53 of the
low pressure vE:ssel 44 so that the arcuate section 117 of the
shell 53 together with side platels, and the top and bottom
plates, as well. as opposite end plates 119 define a closed
heater chamber 120 which contains a heating medium 121, such
as water. The arcuate section 117 of the shell 53 thus forms
a wall portion of the vessel 44 through which the heat of the
medium 121 in i:he chamber 120 can be transferred directly
into the fluids within the low pressure vessel 44. As may be
observed from l,igures 1 and 2, the jacket 112 of the heater
device 48 exteilds~for a substantial length of the low
pressure vessel 44 so that it has the ability to transfer a
significant amount of heat directly into the vessel 44. At
one end of the jacket 112 there is located a burner unit 122
(Fig. 5), whi~~h, for example, burns propane so as to produce
hot combustion gases which are conducted via a tube 123 (Fig.
6) through the length of the jacket. The tube 123 reverses
at the opposite end and communicates with a tube 124 which
conducts the c~~mbustion gases back to the first end where
they escape to atmosphere through an exhaust stack 125. The
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CA 02289147 1999-11-22
heat from the combustion gases is thus transferred to the
heating medium 121 within the jacket, and as explained a
portion of this heat is transferred directly to the fluids
within the low pressure vessel 44. Also, as explained above,
the pipes 56 ar.,d 61 carrying the gases collected above the
liquid levels in the high pressure vessel 40 and the low
pressure vessel. 44, respectively, also pass through the
length of the jacket 112 within the heated medium whereby the
gases therein a.re heated on the way to the flare stack 64 or
alternative sy~~tems. Thus, problems which might otherwise be
caused by the formation of hydrates in the delivered gases
are reduced. Moreover, as previously indicated the pipe 106
transferring the recombined liquids collected from the high
pressure vessel. 40 to the low pressure vessel 44 is also
further heated even before entering the low pressure vessel
44. This aids in the subsequent separation of the varying
fluid densitie:~.
The outer jacket. 112 of the heating device 48 is
provided with an outlet (not shown) with which a pipe 126
(Fig. 2) is in communication and feeds heated medium to a
circulatory system for heating the well fluids entering high
pressure vessel. 40. The pipe 126 is provided with a pump 127
(Fig. 2) for forcing the circulation in the system. In
addition to providing the heated medium to the internal
heating means ~~5 within the high pressure vessel 40, the pipe
126 may provide: heated water pumped by the pump 127 for
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CA 02289147 1999-11-22
external use such as washing down the equipment and for
providing sparging nozzles within the vessels 4U and 44 with
pressurized heai:ed water. It is necessary, of course, to
provide an inle~~ means (not shown) for adding top-up water to
the jacket 112 when water is used as the heating medium and
heated water is used for other purposes.
The high pressure vessel 40 is also formed from an
elongated outer cylindrical shell or wall 131, (Fig. 7> which
normally would :not have the same length as the outer shell 53
of the low pressure vessel 44, and the opposite ends of the
cylindrical shell are closed with outwardly curved ends 67
and 93. In the end 93, the high pressure vessel 40 is
provided with a manway 132, which, when open, allows access
to the interior of the vessel for maintenance purposes. In
addition to the gas outlet means 57 in the top of the high
pressure vessel 40, the high pressure vessel 40 is provided
with an outlet means 130 which is provided with a pressure
relief valve (not shown).
As previously described, a major portion of the drill
cuttings or solid particles 90 collect beneath the main
separator means 43 at the bottom of the first separating
chamber 70 (Fig. 3). There is provided at the very bottom of
chamber 70 belew separator means 43, an outlet means 13,3,
which is in communication with a pipe 134. A control valve,
135 is provided. in pipe 134 which is connected at this lower
end to a solids. discharge pipe 138. Therefore, as valve 135
23
CA 02289147 1999-11-22
is opened when the pile 90 of particles reaches a
predetermined maximum, the particles can be removed through
the pipe 138.as indicated by the arrow 136 (Fig. 8). The
particles and liquids mixed therein may be drawn off with a
pump 137, such as a progressive cavity pump, the inlet of
which is connected to pipe 135. The outlet of the pump may
be connected to a conduit which directs the particles to a
disposal area. There are located in the walls of the high
pressure vessel 40 adjacent to the chamber 70 sparging
nozzlesø 140, as indicated in Figure 8, these nozzles being
directed so as to provide a scrubbing action at the bottom of
the chamber 70 for assisting in the removal of the particles
in chamber 70 and directing the particles towards the outlet
means 133. The sparging nozzles 14U may be provided with
pressurized heated water from heating device 48, for example
by pipes (not shown) from the output of pump 127, or
alternatively from a water outlet 199 of the second state 49.
As previously described, finer particles also settle in
the less turbulent liquids in chambers 91 and 94 of the high
pressure vessel 40, and these particles and other sludge
which collect at the bottoms of chambers 91 and 94 can be
separately removed through outlet means 141 and 142,
respectively. Outlet means 141 and 142 are also connected to
particle discharge pipe 138 via pipes 143 and 144, which also
include control valves 145 and 146 (Fig. 8), respectively.
Again in the area of the lower part of each of chambers 91
24
CA 02289147 1999-11-22
and 94, there are provided in the outer cylindrical shell 131
of high pressure vessel 40 sparging nozzles 147 and 150 (Fig.
8> for use in flushing the sediment in chambers 91 and 94
down the outlet means 141 and 142, these sparging nozzles
also being supplied with pressurized water by lines (not
shown) from pum~~ 127.
The heating' means 95 which is in effect a heat transfer
means shown in Figures 2, 8 and 9 is formed of a large coiled
tubular member 1.51 of cylindrical form having an outer
diameter slightly smaller than that of the interior of the
outer cylindrical shell or wall 131 forming high pressure
vessel 40. Accordingly, more than one half of the exterior
of the coiled tubular member is exposed to the liquid in the
second chamber ~~1 of the high pressure vessel 40, while a
significant portion of the coiled tubular member is also
exteriorly exposed to the volume of gas 87 above the level of
the liquids. Thus, not only is heat transferred to the
liquids, but thE: gas is at least initially heated before
passing out through the gas outlet means 57. Thus, the
medium in the j<~cket 112 which is continuously heated is
continuously circulated via pump 127 through the coiled
tubular member :L28 to heat the fluids in the high pressure
vessel 40. The heated medium from the heating device 48 is
pumped to the c~~iled tubular member 151 via pipe 126 which is
attached to a first end 152 of the coiled tubular member by
way of a feed pipe 153 which passes through the bottom of the
CA 02289147 1999-11-22
- high pressure vessel 40. A second end 154 of the coiled
tubular member 151 is attached via an outlet pipe 155 which
exits through the top of the high pressure vessel 40 to a
return pipe 156 which returns to the jacket 112 of the
heating device 48.
Better separation of the liquids from each other and the
gas from the liquid occurs as the liquids are heated as a
result of the heating means 95 in the high pressure vessel
40. Thus, gases. separation not only occurs because of the
operation of the. main separator means 43, but they continue
to escape from the surface of the liquids along the complete
length of the high pressure vessel 40. In the event gel is
added to the fluid being pumped into the well for the purpose
of giving the fluid more ability to carry the drill cuttings
back to the separating system, the heating of the liquids
facilitates the release of the drill cuttings from the gel in
both the high and low pressure vessels.
As comparec! to known heating arrangements used in
separating systE:ms, wherein the incoming drill fluids are
heated immediatE:ly prior to and after the fluid passes
through the cho~;e valve of the pipe corresponding to the
delivery pipe 38 of the present invention, the heating system
of the present :Lnvention does not involve the passing of the
abrasive incoming drill fluids through a heat transfer
device. In the present invention the choke valve means 41 is
normally maintained in a fully open position and the drill
26
CA 02289147 1999-11-22
fluids containing the drill cuttings pass directly to the
main separator m~sans 43 where a substantial proportion of the
drill cuttings a:re removed. The fluids are then subsequently
heated by means which permits effective transfer of heat to
the fluids at different locations so as to achieve more
effective separation in both the high pressure vessel 40 and
the low pressure vessel 44. Also the form of the heating
system in the present invention provides for a convenient
method of heating the separated gases to avoid the formation
of hydrates in the gas leaving the separation system.
In Figures 10 and 11 there is shown a de-misting device
157 which forms part of the gas outlet means 57 of the high
pressure vessel 40. The de-misting device 157 also forms
part of the gas outlet means 62 of the low pressure vessel 44
as is shown in Fig. 12. The separating process within both
vessels results in a considerable amount of mist, i.e., tiny
particles of liquid, being carried by the escaping gases into
the volume of gas above the level of the liquid, such as the
volume of gas 87 in the high pressure vessel 40. It is
2U desirable, of course, that the.mist not be carried into
either of the pipes 56 or 61 and the de-mister provides an
effective way of separating the liquid from the escaping
gases and returning it to the liquid in the lower part of the
vessels. The de:-misting device 157, as used in gas outlet
means 57, for eX:ample, provides communication between the
volume of gas 8T and the pipe 56 and is disposed above the
27
CA 02289147 1999-11-22
level of the l:Lquids in the high pressure vessel 40. The de-
misting device 157 includes a housing means 159 in the form
of a bowl-shapE:d housing portion 160 with a closed flat top
161. The housing portion 160 forms an inner wall 162
providing an upper substantial cylindrical chamber 164 about
a vertical axis 163 of the device. The lower part of the
housing portion 160 provides a lower part 165 of the chamber
164. The chamber is substantially closed except for a small
moisture outlei~ 166.
A tubular portion 170 of the de-misting device has an
open lower end 158 well below the top of the housing, and the
tubular portion extends upwardly through the otherwise closed
top 161 of the chamber 164. Above the device, the tubular
portion communicates with the pipe 56. As shown the.de-
misting device is provided with a pair of like gas inlet
means having of?en.outer ends 167, and passages 168 extending
from the open outer ends 167 through to inlet openings 171 at
the top of the chamber 164, the passages approaching the
upper portion of the chamber 164 in a substantially
tangential manner.
As the ga;~ flows into the upper part of the chamber 164
about the tubu:Lar portion 17U as indicated by arrows 173
(Figure 11>, it swirls in the annular space between the
tubular portio~a 170 and the inner wall 162 so that the
heavier liquid particles are thrown outwardly by centrifugal
force to the w,~ll 162, and due to gravity run down the wall
28
CA 02289147 1999-11-22
as indicated at :L74 (Figure 10), and flow out through the
opening 166. ThES gas turns sharply at the bottom of the
vortex formed by the swirling gas and exits into the pipe 56
as indicated by arrows 175. The sharp turning.of the gas
throws most of the residual moisture particles to the bottom
of the housing portion 160.
While both 'the high pressure vessel 40 and the lower
pressure vessel ~44 are both of the horizontal type, the
liquid capacity ~~f the lower pressure vessel 44 is of
considerably greater maximum capacity than the high pressure
vessel 40. As an example, the high pressure vessel 40 may
have a maximum capacity of 50 barrels, while the low pressure
vessel 44 may have a maximum capacity to be more in the order
190 barrels. An important feature of one aspect of the
invention is to provide a system which is capable of removing
a major portion of the drill cuttings at an early stage of
the separation of the constituents of the well fluid returned
from the borehole and yet be also capable of disposing of
large volumes of gases which may be rapidly released within
the borehole during the drilling procedure using a under-
balanced drilling method. In the system of the present
invention, when high flow rates are encountered, particularly
due to an increased gas production in the well, there is no
disrupting of the process, such as that caused by utilizing
the choke valve means 41 to decrease or even block off the
return of the fluid from the well. As previously indicated,
29
CA 02289147 1999-11-22
the high pressurE: drop across the choke valve during such
choking is highl~~ detrimental. In the present system, the
pressure within t:he high pressure vessel 40 can be maintained
within the permitted maximum under most conditions
encountered in under-balanced drilling by way of the flow
control means 60 in pipe 56 which conducts the separated
gases exiting from the high pressure vessel 40 through gas
outlet means 57. The valve in the flow control means is
opened further to permit the additional gases to flow
otherwise unobstructed to the flare stack 64 or other system
collecting the g<is output of the vessels 40 and 46. As the
higher quantity of gas is free to flow through the high
pressure vessel X10, the liquids and drill cuttings continue
to separate in the usual manner without interruption due to
the excess of gas flow. The liquids and any residual solids
exiting from the high pressure vessel 40 then continue on in
the usual manner to the lower pressure vessel 44 for further
and more completE~ separation.
After the fluids exiting from high pressure vessel 40
are metered and :recombined in pipe 106, they pass through the
heater device 48, where additional heat is added thereto
before entering :Low pressure vessel 44, by way of a vortex
separating means 176. While the separating means 176 may
have a form simi:Lar to the separator means 43 used in the
high pressure veasel 40, it is possible to use commercially
available separators known as de-sanders or desilting
CA 02289147 1999-11-22
devices. In the separating means 176, further gas is
separated by way of centrifugal force caused by the swirl
imparted to the liquids entering from pipe 126, and the
separated gases escape through the top of the separating
S means as indicated by arrow 177 (Fig. 12>. Also residual
solid particles 180 are also separated by centrifugal force
and pass out through the bottom of the separating means 176
and continue toward the bottom of the low pressure vessel in
a first chamber 181 of the low pressure vessel 44. The
chamber 181 is provided by a weir 182 which extends
transversely across the low pressure vessel 44 at a distance
inward from a first end 183 thereof. The weir 182 has a
horizontal upper edge 184, and the liquids issuing from the
lower end of the separating means 176, which is below an
upper liquid level 185, turn back upwardly and flow over the
upper edge 184, as indicated by arrows 186. The solid
particles, on the other hand settle below the separating
means 185 in first chamber 181.
Adjacent a second end 187 of the horizontal low pressure
vessel 44 is a second weir means 190. As best seen in Figure
2, the weir means 190 includes a first weir section 191 which
extends practically acrass the low pressure vessel 44 and a
second weir section 192 which extends in the longitudinal
direction of the low pressure vessel and joins the front weir
section 191 at right angles. The weir means 190, which has
an upper edge 193, thus forms a box-like chamber 194
31
CA 02289147 1999-11-22
effectively in a corner of the low pressure vessels at the
end of the low pressure vessel 44 opposite to the end at
which the liquids are introduced via pipe 106.
Thus, there is pravided between weir 182 and the weir
means 190 a long settling and separating middle chamber 195.
This area of the low pressure vessel 44 is also that to which
heat is transferred through arcuate section 117 of the outer
shell 53 directly from the heated medium 121 in the heating
device 48. Accordingly, there is effective separation
between the water 196 and the oil 197 in the relatively calm
section of the liquid in chamber 195. Also much of the
remaining gases in the liquids escape to the volume of gas
198 above the liquid level 185, and most of the remaining
sediment settles to the bottom of middle chamber 195.
The normal operating pressure in the low pressure vessel
44 is considerably below that of the high pressure tank,
normally in the range of about 10 to 25 p.s.i.g., with
maximum operating pressure of about 50 p.s.i.g. The lower
operating pressure encaurages the escape of the residual
gases from the surface or level 185 of the liquids. The
magnitude of this pressure within the low pressure vessel 44
is normally maintained by the setting of the flow control
means 63 in the F~ipe 61. The pipe 61 receives the gas
outflow through gas outlet means 62 which includes another
de-misting device 157. The volume of gas 198 is also in
communication with an autlet means 200 which is provided with
32
CA 02289147 1999-11-22
a pressure release means (not shown).
The low pressure vessel 44 is provided with a number of
sight glasses through which the various levels, collection of
solids; etc. can be observed from the exterior of the vessel.
Additionally, as described in relation to the high pressure
vessel 40, level sensors may be provided to provide an
indication as to the relative level 2U1 of the water 196
settled to the bottom of the middle chamber 195. The level
2U1 of the water is maintained below the upper edge 193 of
the weir means 190, the edge 193 being lower than the upper
edge 184 of the. weir 182. The water is withdrawn through the
water outlet 199 which is in communication with a lower part
of middle chamfer 195, and the withdrawn water is piped to a
storage reservoir or is otherwise disposed of. There is
provided a maximum liquid level sensor 202 for detecting the
level 185. This level is in turn utilized in controlling the
outlet means 5~i through which the oil flows from the chamber
194 to pipe 51,. Excess oil production is discharged from oil
outlet means 206 to a production tank (not shown).
Referring back to the description of the calculations
made as to the selection of the liquid for providing the
proper under-balanced pressure down-hole in a particular
drilling condii~ion, if a greater pressure may be used so that
a decision is made not to pump oil down-hole, but use water
instead, then the above described operation conditions would,
of course, be 'varied. This involves controlling the volume
33
CA 02289147 1999-11-22
of water 196 and the volume of oil 197 so as to maintain the
level 201 of water above the upper edge 193 of the weir means
190 so that the water averflows the weir means and occupies
the chamber 194. The water normally withdrawn from the water
outlet 199 of the: low pressure vessel 44 may now be
discharged through outlet means 55 and be returned to flow
control means 52 for controlled introduction back through the
drill tube 33. Z'his ensures a clean drilling fluid is
returned down the: drill tube 33. Hydrocarbon liquid, i.e.
oil, returned from the well in the drill fluids is separated
in the low pressure vessel 44 and may be collected and
discharged through the outlet means 206 to a production tank
(not shown).
Located below the separating means 176 in the first
chamber 181 of tt~e low pressure vessel 44 is an outlet means
203 through which the collection of drill cuttings and other
solids may be removed by way of a system similar to that
described in relation to the high pressure vessel 40. A
sparging nozzle l.not shown) may be associated with the outlet
means 203 so as t:o fluidize the solid materials exiting via
the outlet means 203. At opposite ends of the middle chamber
there are provided outlet means 204 and 205 for removal of
sediment from th:Ls chamber, again, in a fashion similar to
that used in relation to the chambers of the high pressure
vessel 4U.
As is apparf:nt in the separating apparatus of the type
34
CA 02289147 1999-11-22
of the present invention for use in under-balance drilling,
the vessels must remain hermetically sealed, and particularly
in the case of the high pressure vessel 40, the system must
be capable of retaining high internal pressures. It is
necessary, however, when drilling in the production zone to
continually analyze the drill cuttings. The cuttings are in
the main separated in the first separating chamber 70 of the
high pressure vessel, and it is advantageous to be able to
retrieve the drill cuttings on a routine basis as they are
flushed to the surface from the borehole. Accordingly, there
is provided in the vicinity of the first separating chamber
70, immediately t>elow the main separating means 43, a sample
taking device 21CI illustrated in Figures 13 and 14 of the
accompanying drawings. While the device 210 is shown as
being provided in end wall 67 of .the high pressure vessel 40,
it may be located in the outer cylindrical shell 131 so as to
be insertable immediately under the lower end of the housing
means 77 of the main separator means 43. The device 210
includes a hollow tubular projection 211 formed integrally
2U with the end wall~~ 67 and having an open inner end 212 in
communication with the interior of the vessel 40, and more
particularly, below the level 68 of the liquids in first
chamber 70. A cE:ntral longitudinal axis 213 of the tubular
projection 211 is substantially horizontal and passes through
the area located directly below the open lower outlet ends of
the housing mean:; 77 so as to be positioned in the path of
CA 02289147 1999-11-22
the drill cuttings falling to the bottom of the high pressure
vessel at this location. Outwardly of the open inner end 212
is a valve means 214, which is preferably a full open ball
valve. The valve means has a manually operable handle 215
which may be turned by a person taking a sample between a
fully closed position so as to seal against and passage of
fluid from the high pressure vessel 40 and a fully open
position in which it provides no obstructing in the tubular
projection 211. An outer open end of the tubular projection
211 is enlarged and pravided with an external thread 216.
Between the outer open end of the tubular projection 211 and
the valve means 214 is a bleed valve 217 which can be
manually opened from a closed position to an open position
permitting communication of the interior of the tubular
projection outward of the valve means 214 to atmosphere.
The sample taking device further includes a tubular
member 220 which is attachable in an end-to-end fashion with
the tubular projection 211. The tubular member 220 has an
enlarged, internally threaded end portion 221 which may be
screwed onto the external threads 216 of the tubular
projection 211. The external threaded 216 and the internally
threaded end portion 221 form an attachment 222 preferably in
the form of a hanuner union which allows ready attachment and
removal of the tubular member 220 from the tubular projection
211. Disposed within an interior chamber 218 of the tubular
member is a collection member 223 which is in the form of an
36
CA 02289147 1999-11-22
open trough of substantially semi-circular cross section as
can be seen in Figure 14. The collection member is
preferably formed of screen and its radius is less than that
of the interior ~~f tubular projection 211 and tubular member
220. Attached t« an outer end of the collection member 223.
is a straight rod member 224 which slidably projects through
a seal 225 in the form of a stuffing box positioned in the
outer end of the tubular member 220. The rod member 224 is
provided with a inandle 226 at its outer end and is of
sufficient length to allow the collection member 223 to be
moved to an inner collecting position below the outlet of the
separator means 43 from which the drill cuttings fall.
Accordingly, normally the valve means 214 is maintained
in a closed condition. Without disturbing the separating
operation of the system, a sample of the drill cuttings being
brought to the surface from the drilling operation can be
obtained. The collection member 223 in an empty condition is
drawn into the chamber 218 within the tubular member 220 by
pulling on the T-bar handle formed by handle 226 at the outer
2U end of the rod member 224. The tubular member 220 is the
connected to the outer end of the tubular projection 211 in
an end-to-end closed, axially aligned, condition. With bleed
valve 217 closed, the valve means 214 is fully opened so that
by pushing in on the rod member 224, the collection member
223 is positioned beneath the output of the separator means
43 directly in the path of the drill cuttings falling to the
37
CA 02289147 1999-11-22
bottom of the first chamber 70. As the liquids are flushed
through the screen forming the collection member 223, the
drill cuttings are maintained in the trough-shape collection
member 223. The~~e drill cuttings are those initially
entering the system with.the drill fluids coming directly
from the borehole. The drill cuttings are immediately
removed by withdrawing the rod member 224 so as to position
the collection member 223 with its fresh load of drill
cuttings within the internal chamber 218 of the tubular
member 220. The valve means 214 is then closed, the bleed
valve 217 is opened, and the attachment 222 is unthreaded.
The tubular member 220 containing the filled collection
member 223 can then be removed for dumping and testing.
It is also possible to provide a solids level indicator
device 230 (Figures 15 and 16) in the closed high pressure
vessel so that while the separation process is in~operation,
it is possible to determine when there is a sufficient
accumulation at 90 to warrant the starting of pump 137 for
removal of the drill cuttings from chamber 70 through outlet
133. The device 23U may be provided in association with end
wall 67 as shown in Figure 15 and 16 or with a side wall
formed by the outer cylindrical shell 131 of the high
pressure vessel 40. The device 230 has a rod member 231
which includes a straight horizontal portion 232 and a second
portion 233 which is rigidly affixed to the horizontal
portion 232. A hollow tubular member 234 is affixed to the
38
CA 02289147 1999-11-22
end wall 67 and has an inner end in communication with the
interior of the high pressure vessel 40. The outer end of
the portion 232 of the rod member 231 extends through a seal
235 in the outer end of the tubular member 234. The seal
235, which may t>e in the form of a stuffing box, supports the
rod members 231 for rotation therein about the longitudinal
axis of the horizontal portion 232, but the seal is capable
of preventing the escape of high pressure fluid from within
the vessel 40. The outer end of the rod member 231 extends
beyond the outer end of the tubular member 234 and terminates
in a handle portion 236 by which one may grasp the rod member
and rotate it. The second portion 233 of the rod member 231
projects at an angle, preferably about 90 degrees, relative
to the horizontal portion 232, so that as the rod member 231
is turned within the tubular member 234, the free end of the
second portion :?33, which has an enlarged member 237 attached
thereto, swings along an arc as denoted by the arrow 240 in
Figure 16. The member 237 is preferably spherical, i.e. a
ball and it is weighted. Thus as one turns the handle to
raise the member 237 and then allows the ball to sink in the
liquid above thE: accumulation 90 of drill cuttings, the
weighted ball w:Lll sink until it engages the top of the
accumulation 90 and then it stops. A scale (not shown) can
be provided in <~ssociation with the exterior part of the rod
member so that i:he location of the rod as it turns to a stop
provides an indication of the depth of the drill cuttings
39
CA 02289147 1999-11-22
below the ball.
While various features have been shown to illustrate the
present invention, alternatives will be apparent to those
skilled in the a,rt without departing from the spirit of the
invention as defined i.n the appending claims.
15
25
