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Publication numberUS3664440 A
Publication typeGrant
Publication dateMay 23, 1972
Filing dateJan 21, 1970
Priority dateJan 21, 1970
Also published asCA948620A1
Publication numberUS 3664440 A, US 3664440A, US-A-3664440, US3664440 A, US3664440A
InventorsElenburg Wayland D
Original AssigneeElenburg Wayland D
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Formation chip sampling apparatus
US 3664440 A
Abstract
Formation chip sampling method and apparatus for separating solids from the liquid contained in drilling mud which has been obtained from an earth boring operation. The returned drilling mud is flow connected in series relationship to a gas separator, a splitter which reduces the amount of sample to be treated, and to a reservoir. A pump flow connects the reservoir to a cyclone type separator which removes the solids from the sample. The reservoir further includes a level controller which provides make-up liquid so as to provide the pump with optimum suction conditions.
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Description  (OCR text may contain errors)

United States Patent 51 May 23, 1972 Elenburg [54] FORMATION CHIP SAMPLING APPARATUS [72] Inventor: Wayland D. Elenburg, Box 1588,

Monahans, Tex. 79656 [22] Filed: Jan. 21, 1970 [21] Appl. No.: 4,546

[52] US. Cl ..175/206, 175/66, 175/217 [51] Int. Cl ..E2lb 21/00 [58] Field of Search 175/66, 69, 205-207, 175/209, 217

[56] References Cited UNITED STATES PATENTS 2,786,652 3/1957 Wells ..175/206 X 2,852,091 9/1958 Boudreaux et al... ....175/206 X 2,870,990 1/1959 Bergey ..175/217 X 2,886,287 5/1959 Croley ..175/206 2,919,898 1/1960 Marwil et al.. ..175/66 2,923,151 2/1960 Engle et a1. 175/206 X 2,941,783 6/1960 Stinson ..175/206 Primary Examiner-David H. Brown Attomey-Marcus L. Bates ABSIRACT llClahm,8D|-awingligures PATENTEB MAY 2 3 1972 sum 1 or 3 FIG. I

INVBNTOR WAYLAND D. ELENBURG MARCUS L. BATES PATENTEDMY 2 3 m2 F'LF'EEI 2 OF 3 FIG. 3

FIG. 4

FIG. 5

INVENTOR WAYLAND D. ELENBURG MARCUS L. BATES PATENTEDMAY 23 I972 TAMI 3 BF 3 BOREHOLE FIG. 8

[NV/5N )R, WAYLAND 0. ELENBU BY MARCUS L. BATES FORMATION CHIP SAMPLING APPARATUS BACKGROUND OF THE INVENTION In the chip drilling process, dual concentrically arranged drill pipe are connected between a drill bit and a swivel with drilling fluid flowing to and from the bit in counter-current relationship in order to cool and lubricate the drill pipe and bit, and to remove chips and other cuttings from the bottom of the borehole by circulating the cuttings to the surface of the ground where the cuttings may be subsequently studied by geologists in order to determine the physical and chemical properties of the strata of the earth through which the borehole has been formed. At the bottom of the borehole the drilling fluid picks up or entrains the chips and cuttings and transports them upwardly within the central pipe, or altematively, within the annulus formed by the drill pipe, where the cuttings flow to the surface of the earth, all of which is known to those skilled in the art; as evidenced by Elenburg, US. Pat. No. 3,439,757; to which reference is made for further background of the invention.

Retrieving representative core samples, reducing the core samples to a convenient size which is conductive to study thereof, and relating the samples to the specific depth of the borehole from which they originated is extremely important in order for the geologist to carry out proper analysis of the various strata encountered.

Heretofore it has been customary for others to flow connect the entire drilling mud flow stream from the borehole to a flow divider apparatus which separates the major flow stream into several flow paths so as to greatly reduce the volumeof the drilling mud or chip bearing flow stream which is to be treated for subsequent analysis. Often the flow is improperly divided due to the physical characteristics of the solids and the mechanics of the flow divider, all of which results in inaccurate analysis of the borehole for the reason that one divided flow stream differs in composition or mixture from another divided flow stream. After the mud sample has been reduced in volume by selecting one of the flow streams for analysis, it is necessary to permit the solids to settle by gravity, after which the clarified water is siphoned off or decanted, and the remaining saturated solids or residue heated to evaporate the liquid therefrom.

It is therefore desirable to be able to split a stream of drilling mud containing samples from the chip drilling process into any desired fraction of the main flow stream wherein the smaller fraction of the main flow is identical in composition or mixture to the remainder of the flow. It is also desirable to be.

able to treat this fraction of flow in an improved manner which removes the solids therefrom, and to be able to relate the retrieved solid samples to the particular depth of the borehole from which the sample originated.

SUMMARY OF THE INVENTION This invention relates to formation chip sampling apparatus and method for separating solids from drilling mud which may be obtained from an earth boring operation so as to enable subsequent analysis thereof. As the drilling mud flows from the borehole, it exits at the swivel and flows to a separator where the air is removed therefrom. From the separator the flow continues to a splitter where a fraction of the flow is separated from the main flow. The fractional flow continues to a reservoir with the reservoir having fluid level control means associated therewith for supplying makeup water thereto in order to always maintain a fluid level therein. The contents of the reservoir is pumped under a positive pressure to a cyclone separator. The pump flow and the physical dimensions of the cyclone separator are sized with respect to one another so as to provide an optimum separation of solids from the liquid at the cyclone separator. Where deemed desirable, and especially when utilizing the chip drilling process, a screen may be interposed between the splitter means and the reservoir so as to reduce the load on the pump while at the same time maintaining large chips in an undamaged condition which will enhance the subsequent analysis thereof. The screened solids are combined with the solids removed from the cyclone separator and placed in a suitable container for storage or shipment.

It is therefore a primary object of this invention to provide a method of obtaining formation chip samples by separating solids from drilling mud.

Another object of the present invention is the provision of a method of obtaining a fraction of the flow obtained from a borehole forming operation which is representative of the main flow; and of separating the solids from the liquid contained in the fractional flow.

A still further object of the present invention is the provision of apparatus which obtains formation chip samples from a chip drilling operation by separating solids from the drilling mud.

A still further object of the present invention is the provision of formation chip sampling apparatus which removes air from drilling mud, separates the drilling mud flow stream into a fractional part wherein the fractional part contains solids which are representative of the solids contained within the main flow stream, and which separates the solids from the liquid of the fractional component of the main stream.

Still another object of the present invention is a method of removing solids from drilling mud so as to provide a formation chip sample which can be related to the particular depth of borehole from which the sample originated.

The above objects are attained in accordance with the present invention by the provision of method and apparatus for obtaining formation chip samples as set forth in the above abstract and summary.

Various other objects and advantages of this invention will become readily apparent to those skilled in the art upon reading the following detailed description and by referring to the accompanying drawings.

BRIEF DESCRIPTION OF THE DRAVVINGS FIG. 1 is a part diagrammatical, part schematical representation in the form of a flow sheet which describes the essence of the method of the present invention;

FIG. 2 is a side elevational view of apparatus previously seen in FIG. 1;

FIG. 3 is a top plan view of the apparatus disclosed in FIG. 2;

FIG. 4 is a top plan view of part of the apparatus seen in FIG. 1, with some parts thereof being diagrammatically illustrated by dot-clash lines; and

FIG. 5 is a cross-sectional view taken along line 5-5 of FIG. 4, with some parts thereof being unsectioned for clarity;

FIG. 6 is a part diagrammaticahpart schematical representation in the form of a flow sheet which describes another embodiment of the present invention;

FIG. 7 is an enlarged, part cross-sectional view, taken along line 7-7 of'FIG. 6; and

FIG. 8 is a reduced top plan view of a part of the apparatus disclosed in FIG. 6, with some parts thereof being broken away therefrom in order to better disclose the invention.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT As seen in the diagrammatical representation of FIG. I, the present invention is used in conjunction with a borehole forming operation, broadly indicated by the arrow at numeral 10, wherein there is seen concentrically arranged drill pipe extending into the ground with the upper terminal end thereof being connected to a swivel 12. Drilling fluid, or drilling mud, is pumped to the swivel in the usual manner while drilling fluid containing chips and particles of the formation being penetrated are retrieved at gooseneck 16. The gooseneck is flow connected to tangential inlet 17 of air separator means I 18. The air separator has an upwardly depending-centrally located conduit 19 from which air escapes. Theair-free liquid flows through bottom outlet and is directed into a splitter means 21.

The splitter includes a large outlet 22 which is flow connected to mud pit 23 by any suitable means, and to which the major portion of the flow is conducted. Small outlet 24 receives the remaining fraction of the drilling mud which is originally returned from the borehole. The remaining portion or fraction of the mud flows through screen 25 in order to remove large particles or chips therefrom. The fraction of the drilling fluid which includes the smaller cuttings or particles which were not retained by the screen continues to flow on to the reservoir at 26. The upwardly opening reservoir has a sloped bottom to which a lower outlet is flow connected to pump means 27.

The pump can be actuated by any suitable means, as for example, a gasoline motor. The pump provides a high pressure flow to tangential inlet 28 of cyclone separator 29. As the drilling fluid flows through the cyclone separator, the liquid is separated from the remaining solids contained therein, with the liquid finally exiting at 30 where it can be flow connected to any suitable disposal means, as for example, the mud pit, while solids fall through lower outlet 31 where they are retrieved within any suitable receptacle 32. A source of makeup water (not shown) is connected to valve means 33 which in turn is controllably flow connected to a journaled float means 34 by the illustrated linkage. The float and valve assembly provides a level controller device for controlling the flow of makeup water into the reservoir so as to maintain a suction for the pump at all times.

FIGS. 2 and 3 show the details of the separator apparatus which includes a gear driven pump 27 having rubber impellers thereon and which is capable of producing a flow rate and pressure consistent with the design of cyclone separator 29 and to the mud flow rate into the reservoir.

The reservoir is provided with a means for maintaining a fluid level therein, preferably in the form of a styrofoam float 34 which has a support arm depending therefrom and journaled to any convenient structure, as for example a side wall of the reservoir. The arm is connected by linkage 33' to the valve means 33 so as to actuate the valve as the fluid level within the reservoir changes. The valve means has an inlet which is flow connected to any suitable source of makeup water and an outlet into the trough. The valve means can alternatively be connected to flow directly into the outlet of the reservoir if deemed desirable.

The pump is driven by an internal combustion gasoline motor of the following described type: Wisconsin Engine, 3 X 3% size. The pump is of the followingdescribed type: gear driven, rubber impellers, capable of 40 g.p.m. at 9-15 p.s.i.g., manufactured by Booie. The inlet of the cyclone separator is provided with 40 g.p.m., and is available from Kerbs Engineering, 1205 Crysler Drive, Menlo Park, California, Model D4B-l 2.

Looking now to the details of FIGS. 4 and 5, the before mentioned air separator 18 is seen to be in the form of a cylindrical tub having tangental inlet 17 connected to an upper extremity of the sidewall thereof, and with an upwardly depending reduced diameter air outlet 19 being provided at the upper end thereof. Outlet 20 is in the form of a downwardly and outwardly directed elbow which is arranged in overhanging rela tionship with respect to the splitter so as to cause the mud flowing therefrom to impinge against the rotating vanes of the splitter, as will be pointed out in greater detail later on.

The splitter has an upwardly opening interior as indicated by the arrow at numeral 35 which is formed by the stator or fixed tub portion 36. Within the stator there is rotatably disposed a rotor comprised of cylinder 37 having a multiplicity of radially disposed vanes 38 which rigidly connect the cylinder to a tubular element 39. The tubular element is rigidly affixed to a shaft 40 with the shaft having spaced apart bearings 41, 42, each of which are located at the upper and lower extremity of the shaft so as to rotatably support the shaft from the fixed members 43 and 44. Tubular member 39 is received within the upwardly opening complementary fixed tubular member 45. Inwardly sloped floor members 46, 48 are affixed between adjacent vanes and form spaced apart catch basins between some of the vanes, with the lower extremity of the basins being apertured as seen at 49 so as to communicate the interior of the complementary fixed tubular member therewith.

A pair of spaced apart rails 51 underlie the trough 24 and provides a support means for the before mentioned screen so as to enable the screen to be conveniently interposed between small outlet 24 and the reservoir. While the particular embodiment disclosed herein illustrates each sixth area as being a basin, it is preferred that each fourth area between adjacent vanes be provided with a lower bulkhead or floor so as to provide the before mentioned split of 25 percent of the flow. Alternatively, other splits may be achieved by merely varying the number of floor members employed within the rotor.

In the embodiment set forth in FIGS. 6-8, the numerals used in conjunction therewith refer to similar numerals used in conjunction with FIGS. 1-5, wherever possible. As seen in FIGS. 6-8, mud from the drilling operation flows through air separator 118, which may be identical to the air separator of FIGS. l-5. A screen is interposed between the air separator liquid outlet 120 and the entrance of hopper or reservoir 126. The upper edge portion of the reservoir forms a support for the frame of the screen.

Valve 133 is actuated by float level device 134 in a manner similar to the arrangement of the level controller disclosed in FIGS. 1-5. Outlet is connected to a bypass Tee" 161, with the tee having the illustrated valve therein for flowing mud to the mud pit. Valve 162 connects the tee to pump 127, which in turn is connected to inlet 128 of separator means 129.

The separator has a liquid outlet 130 and a solids outlet 131. Receptacle 132 can be any suitable container for receiving core samples from the separator means.

The liquid outlet 130 is freely received within the inlet elbow 163 of storage tank 165 with the outer peripheral wall surface of the outlet being spaced apart from the inner peripheral wall surface of the elbow. Overflow 164 can be flow connected to the mud pit, and is located below the inlet of the elbow so as to maintain the liquid height within the tank at a level which always leaves room for liquid flow from the separator. Outlet 166 is flow connected to the valve 133 of the liquid level control means.

OPERATION In operation, drilling mud is circulated from a main mud pump (not shown), to the swivel where it is forced through the drill string annulus downhole to the drill bit, and back through the central passageway to the inlet 17 of the air separator. The formation samples cut by the action of the bit are in the form of chips and cuttings, and are transported by the drilling fluid into the air separator 18. The air separator can take on several different forms but preferably is similar to a centrifuge in that a vortex is established by the tangental inlet 17, thereby causing the drilling fluid to be separated from air contained therewithin. The air separator is especially useful where the chip drilling process is supplemented with air drilling, but is not considered indispensable to the process. As drilling mud exits from outlet 20, it impinges against the vertically disposed radiating vanes of the splitter, causing a rotational motion to be imparted into the rotor. Since the rotor is spaced apart from the wall of the stator and journaled at its upper and lower extremity, it will rotate at a r.p.m. or with a peripheral velocity which is dependent upon the flow rate of the drilling mud received therewithin. The major portion of the mud flow stream is free to flow through the spaced-apart vanes at 47 and to the outlet 22, while a smaller fraction thereof is intercepted by the catch basins formed by the floor members 48.

As the mud flows through the spaced apart vanes 38, that is, the adjacent vanes which have no floor therebetween, it continues on through the rotor and into the lower extremity of the tub or stator where it then flows through outlet 22 and is directed to the mud pit 23. The smaller fraction of the drilling fluid which flows into the catch basin, however, is trapped by the floor member and diverted through aperture 49, into the rotatable tubular member, and into fixed tubular member 45, where it then flows from lower chamber 50 and through outlet 24.

The number of catch basins 48 may be varied to provide any split desired, as for example, one sixty-fourth or one-half of the total returned mud flow may be deemed desirable as a feed rate into the reservoir 26. The number of catch basins determine the formation sample size as well as the load placed on the screen, reservoir, pump, and cyclone.

Trough 24 preferably is arranged in overhanging relationship with respect to reservoir 26 so as to enable fluid therefrom to flow by gravity thereinto. Screen is preferably of 60 mesh size and is interposed between trough 24 and the reservoir by merely resting the edge portions of the screen on spaced apart support members 51 as generally indicated by the arrow at numeral 25 Since most chip drilling operations employ a fluid circulation rate of about 140 gallons per minute when making a 4% inch diameter hole, it is evident that the fraction of this amount which will be divided out by the splitter and received within the reservoir is dependent upon the ratio of catch basins to the open vanes. Since the pump 27 preferably receives exactly 40 gallons per minute, and assuming a 25 percent split, it is evident that the float 34 must open valve 33 a sufficient amount to supply 5 gallons of fresh make-up water per minute in order to maintain a fluid level within the reservoir.

Pump 27 delivers a constant flow of fluid to the cyclone separator, which can take on several different forms, and preferably is essentially a vertical cylinder with the usual inlet stream 28 being introduced tangentally near the top so as to give a spinning motion to the liquid traveling therethrough. The centrifugal force acting on the suspended solids tends to throw them radially to the side of the cyclone as the solids spiral downward to the conical bottom where they are removed at 31. The separated liquid is disposed of at the top, with the conduit 30 being a conventional outlet. With the cyclone separator operating within its most efficient range, essentially no liquid is lost through the solids outlet, and essentially saturated solids drop into the receptacle 32. it is for this reason that the pump 27 must always operate within its most efficient range, or otherwise the operation of the cyclone will not produce this desired effect.

The cyclone effectively removes all of the suspended solids. in one series of test carried out in accordance with the present method, one half gallon of 60 mesh sand was introduced into the reservoir, and separated by the cyclone with five passes through the separator portion of the equipment being made. The accumulated loss of sand during these five passes was negligible, being on the order of 1 percent loss.

The sample attained at 32 is related to the borehole depth by changing the screen 25 and receptacle 32 each 5 foot of hole, although other increments of penetration may be used where deemed desirable. Since the splitter divides out any desired portion of the returned mud, and since the divided portion of the flow stream is identical in composition to the remainder thereof, the present invention provides formation samples which are more representative of the strata being penetrated than has heretofore been possible to attain. All of the suspended solids passing the screen 25 are effectively separated from the liquid in a manner which obviates the necessity of decantation and evaporative treatment as has heretofore been necessary with prior art devices. By utilizing the present invention, each time the screen and receptacle is changed for the next 5 foot sample, it is now possible to immediately bag the obtained core sample and send it to the geologist. Accordingly, possible contamination of the sample is avoided since it is exposed a minimum length of time to the elements. This also avoids inadvertent interchange or mix-up of the samples.

This combination of equipment is rugged, inexpensive, and provides the unexpected advantage of enabling relatively liquid free samples to be obtained at outlet 31. The term liquid free formation sample" is intended to mean samples which are saturated in liquid but which requires substantially no decantation or evaporation in order to be sealed and transported to the geologist.

In carrying out the invention in accordance with the embodiment disclosed in FIGS. 6-7, the large cuttings are obtained on screen and combined with the centrifuged solids obtained at 132. The use of a splitter downstream of air separator l 18 is considered optional, depending upon the flow rates involved. While making hole through known strata, the valve at 161 can be opened, while valve 162 is closed, so as to flow all of the mud to the mud pit, thereby leaving the pump and centrifuge inactive until they are needed.

When a mineral bearing strata is encountered, the valve at 161 is closed, the valve at 162 opened, and circulation through pump 127 initiated. Mud now flows into the air separator, through the screen, and into the reservoir. Make-up water flows from 166, 133 and through tangental inlet 167 where the side walls of the reservoir are cleaned of cuttings. The float at 134 maintains a fluid level within the reservoir which enables the pump to provide the separator means with a constant flow so as to achieve optimum efficiency of separation.

The liquid outlet from the separator is freely received within the elbow 163 of the make-up water storage tank so as to prevent back pressure on the separator which could adversely affect its operation.

Since the overflow pipe 164 is located below the inlet elbow, the storage tank will overflow to the mud pit without affecting the liquid flow from the separator. Outlet 166 provides a constant source of make-up water to valve 133. Since the solids have been removed from the drilling mud, the only contaminate which can be contained within the make-up liquid is dissolved minerals. The reuse of this liquid is preferred to using make-up water which can be obtained from the mud pit for the reason that insoluble minerals are not recirculated through the system. Moreover, soluble minerals will be solublized at a slower rate as the recirculated make-up water dissolves a particular soluble element.

Where deemed desirable, liquid from outlet 164 can be returned directly to the borehole so as to achieve a completely closed circulation flow system, except for the addition of any make-up water which may be required for maintaining a proper fluid level within the make-up tank. This modified flow system is especially useful where water is at a premium.

The present invention provides a means of obtaining formation chip samples which permits both a qualitative as well as a quantitative analysis to be achieved since the weight percent of any material obtained in a formation chip sample can be directly related to the total amount of material removed from the borehole. This aspect of the invention is particularly important relative to ores such as copper and molybdenum, for example, since the economical breaking point of molybdenum is at about 0.5 percent, and accordingly 0.1 percent accuracy is very important when making a chemical analysis of the formation chip sample in order to determine the economics of sinking a mine shaft.

The specific splitter means together with the cyclone separator used herein is indespensible for handling ores which tend to float due to their surface tension and particle size. Material of this nature would otherwise be lost to the mud pit in the absence of the present method.

While a particular pump and cyclone separator have been disclosed herein for purposes of illustration, it is pointed out that other pumps and other types of cyclone separators or centrifuge means may be used so long as the inlet pressure and flow rate to the cyclone separator is maintained within a range which prevents liquid from falling into the receptacle and prevents carry-over of solids into the discharge.

1 claim:

1. In combination with a borehole forming apparatus having drilling fluid flowing to a drill bit for circulating cuttings to the surface of the ground; a formation chip sampling apparatus having:

a reservoir; a pump having an inlet and an outlet; fluid level control means; a source of make-up water; a separator means having an inlet, a liquid outlet, and a formation chip sample outlet;

said pump having the inlet thereof flow connected to said reservoir and the outlet thereof flow connected to said inlet of said separator means;

said level control means being connected to said source of make-up water and to said reservoir for maintaining a supply of liquid within said reservoir;

and means for flow connecting said reservoir to the drilling fluid from the borehole bearing the cuttings, whereby:

the separator means removes the cuttings from the drilling fluid to provide the formation chip sample, while the fluid level controller enables the pump to provide the separator means with a constant source of liquid under pressure.

2. The improvement of claim 1 wherein said means connecting said reservoir to the drilling fluid includes an air separator and a splitter, said splitter having means for dividing the flow of drilling fluid into a first and second flow path, the first flow path being flow connected to a mud pit and the second flow path being connected to said reservoir, so as to reduce the quantity of material which flows to the separator means.

3. The combination set forth in claim 1, wherein: said means for connecting said reservoir to the drilling fluid includes a splitter; said splitter having means for dividing the flow of drilling fluid into a first and second flow path with said second flow path being connected to the reservoir so as to reduce the quantity of material which flows to the separator means.

4. The combination set forth in claim 3, and further including a screen means interposed between said splitter and said reservoir for removing a portion of the cuttings from said second flow path to thereby reduce the amount of solids which flow to the separator means.

5. The improvement of claim 1 wherein said means connecting said reservoir to the drilling fluid includes a splitter, said splitter including a stator and a rotor, said stator being in the form of an upwardly opening tub, said rotor having a cylinder spaced apart from and coextensive with said stator, a tubular support member journaled to said stator, vertically disposed vanes radiating from said tubular support member and connected to said cylinder;

a bottom wall interconnecting two adjacent vanes and forming an upwardly opening catch basin; means forming an aperture through said tubular member for connecting the catch basin to the interior ofthe tubular member;

a tubular skirt enclosing the lower extremity of said tubular member for flow conducting fluid caught therein to said reservoir;

and means forming an outlet in said stator for flowing fluid away from the stator.

6. The improvement of claim 5 wherein said means connecting said reservoir to the drilling fluid further includes means forming an air separator for removing air from the drilling fluid prior to the drilling fluid flowing to the splitter.

7. The improvement of claim 5 and further including a screen means interposed between said splitter and said reservoir for removing a portion of the cuttings therefrom.

8. A formation chip sampling apparatus for use in separating formation samples from drilling fluid, said formation chip sampling apparatus comprising:

a reservoir having a fluid inlet and a fluid outlet; a cyclone separator means having an inlet, a fluid outlet, and a solids outlet; a pump means having an inlet and a discharge;

flow conduit means for flowing drilling fluid and cuttings from a borehole to the reservoir; I a storage tank having a source of make-up liquid therein,

flow conduit means flow connected from said source of make-up liquid to said reservoir; valve means for controlling the flow through the last said flow conduit means; liquid level sensing means for determining the liquid level in said reservoir, said sensing means being connected to actuate said valve means for maintaining a supply of liquid in said reservoir;

flow conduit means by which said pump is flow connected from said reservoir to said cyclone separator inlet;

flow conduit means by which said liquid outlet of said cyclone is flow connected to said source of make-up liquid; whereby:

drilling fluid and cuttings flow into said reservoir, to said pump, and to said cyclone separator; while cuttings flow from said solids outlet of said cyclone separator; and, liquid flows from the liquid outlet of said cyclone separator to said source of make-up liquid.

9. The formation chip sampling apparatus of claim 8, wherein said reservoir is a downwardly converging, upwardly opening enclosure means, and said fluid inlet of said reservoir is tangentially disposed with respect to the interior thereof, whereby the inside peripheral wall surface of said reservoir is washed by the make-up liquid to thereby prevent deposition of cuttings thereon.

10. The formation chip sampling apparatus of claim 8,

wherein said reservoir is an upwardly opening enclosure means, and further including a screen means interposed in the flow path of the first recited flow conduit means, to thereby enable a first separation of cuttings to be effected at the reservoir and a second separation to be effected at said cyclone separator.

11. The formation chip sampling apparatus of claim 8, and further including an air separator means interposed in the flow path of the first recited flow conduit means;

and a splitter means for diverting a fraction of the formation samples and drilling fluid from said reservoir, to thereby reduce the quantity of fluid flowing through the cyclone separator.

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US2786652 *Dec 20, 1954Mar 26, 1957Wells Norman CBottom hole pressure control in well drilling
US2852091 *Apr 3, 1957Sep 16, 1958Phillips Petroleum CoSeparating means for aerated mud drilling
US2870990 *Mar 2, 1955Jan 27, 1959Bergey Taylor GDrilling fluid method
US2886287 *Jul 15, 1957May 12, 1959Phillips Petroleum CoHydraulic cyclone separation system
US2919898 *Aug 16, 1957Jan 5, 1960Phillips Petroleum CoTreatment of well drilling mud
US2923151 *Dec 17, 1956Feb 2, 1960Phillips Petroleum CoExtracting and analyzing gas from well drilling mud
US2941783 *Jul 15, 1957Jun 21, 1960Phillips Petroleum CoHydraulic earth boring and cyclone separation system
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3766997 *Mar 2, 1973Oct 23, 1973Exxon Production Research CoMethod and apparatus for treating a drilling fluid
US4482459 *Apr 27, 1983Nov 13, 1984Newpark Waste Treatment Systems Inc.Continuous process for the reclamation of waste drilling fluids
US20110030822 *Aug 9, 2010Feb 10, 2011Bear Patrick ADry Run Porting System
Classifications
U.S. Classification175/206, 175/66, 175/217, 209/17, 209/3
International ClassificationE21B21/00, E21B21/06
Cooperative ClassificationE21B21/065
European ClassificationE21B21/06N2