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Publication numberUS3774702 A
Publication typeGrant
Publication dateNov 27, 1973
Filing dateMay 22, 1972
Priority dateJan 21, 1970
Publication numberUS 3774702 A, US 3774702A, US-A-3774702, US3774702 A, US3774702A
InventorsElenburg W
Original AssigneeElenburg W
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Formation chip sampling method
US 3774702 A
Abstract  available in
Previous page
Next page
Claims  available in
Description  (OCR text may contain errors)

' United States Patent ['1 Elenburg FORMATION CHIP SAMPLING METHOD [76] Inventor: Wayland D. Elenburg, Box 1588,

Monahans, Tex. 79756 [22] Filed: May 22, 1972 [21] Appl. No.1 255,727

Related US. Application Data [62] Division of Ser. No. 4,546, Jan. 21, 1970, Pat. No.

[52] US. Cl. 175/66, 175/206 [51] Int. Cl E2lb 21/00 [58] Field of Search 175/50, 60, 58, 59,

[56] References Cited UNITED STATES PATENTS 3,016,962 l/1962 Lummus et al. 175/66 3,494,188 2/1970 Boatman 175/50 X 2,225,973 12/1940 Brown et a1. 175/66 X 2,301,371 11/1942 Corwinn, 175/206X [451 Nov. 27, 1973 2,919,898 1/1960 Marwil et al 175/66 2,923,151 2/1960 Engle et al.... 175/206 X 2,941,783 6/1960 Stinson 175/206 3,039,545 6/1962 Rogers 175/66 2,167,393 7/1939 Muncy 175/60 Primary Examiner-David H. Brown Attorney-Marcus L. Bates [57 ABSTRACT Formation chip sampling method 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.

3 Claims, 8 Drawing Figures PATENTEUNUYZYIHH v 3 774 FIG. 3


I FORMATION CHIP SAMPLING METHOD application Ser. No. 004,546 filed Jan. 21, 1970, now

U.S. Pat. No. 3,664,440 issued May 23, 1972.

BACKGROUND OF THE INVENTION In thechip 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 subsequently may be 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 alternatively, transports them upwardly within the annulus formed by the drill pipe, where the cuttings ultimately flow to the surface of the earth, all of which is known to those skilled in the art; as evidenced by W.D. Elenburg, U.S. 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 studyv 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. V

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 volume of 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 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 a method by which formation chip samples are obtained from a chip drilling operation by improvements in separating solids from the drilling mud.

A still further object of the present invention is the provision of formation chip sampling methods 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 DRAWINGS FIG. I 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-dash lines; and

FIG. 5 is a cross-sectional view taken along line55 of FIG. 4, with some parts thereof being unsectioned for clarity;

FIG. 6 is a part diagrammatical, part 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. 1, 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 18. The air separator has an upwardly depending centrally located conduit 19 from which air escapes. The air-free liquid flows through bottom outlet 20 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 drill 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 make-up 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 make-up 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 following described type: gear driven, rubber impellers, capable of 40 g.p.m. at 9-l5 p.s.i.g., manufactured by Booie. The inlet of the cyclone separator is provided with 40 g.p.m. flow rate. The separator is available from Kerbs Engineering, 1205 CryslerDrive, 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 tangential 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 relationship 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 of 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, othe rsplits may be achieved by merely varying the number of floor members employed within the rotor.

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 160 is connected to a bypass T 161, with the T having the illustrated valve therein for flowing mud to the mud pit. Valve 162 connects the T to pump 127, which in turn is connected to inlet 128 of separator means 129.

The separator has a liquid outlet I30 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 tobe 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 418.

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 mud which flows into the catch basin, however, is trapped by the floor member and diverted through aperture d9, into the rotatable tubular member, and into fixed tubular member 455,

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 determines 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 25 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 the spaced apart support members 511 as generally indicated by the arrow at numeral 25'.

Since most chip drilling operations employ a fluid circulation rate of about gallons per minute when making a 4 /2 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 five 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 evaporation 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 five 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 125 and combined with th centrifuged solids obtained at 132. The use of a splitter downstream of air separator 118 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 tangential inlet 167 where the side walls of the reservoir are cleaned of cuttings. The float at 134 main tains a fluid level within the reservoir which enables the pump to provide the separator means with a constant flow so as to achieve optimum efiiciency 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 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 method 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 because they would float off 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 from the separator into the receptacle, and so long as carry-over of solids into the discharge is avoided.

I claim:

I. In a borehole forming operation wherein liquid is used to circulate formation chips formed by the drill bit from the bottom of the borehole to the surface of the earth during the drilling operation, the method of obtaining formation chip samples comprising the steps of:

dividing the liquid bearing the formation chips flowing from the borehole into a plurality of equal flow paths; flowing one of said plurality of flow paths into a reservoir, and continuously pumping the material contained in the reservoir into a cyclone type separator to separate the chip samples from the liquid;

maintaining said continuous flow rate to said separator by adding make-up liquid to the reservoir in an amount as needed to maintain a constant liquid level in the reservoir.

2. The method of cliam 1 wherein said one of the flow paths is flow conducted through a screen so as to remove part of the formation chip samples therefrom prior to the separation step of the cyclone separator.

3. The method of claim 1 wherein the spent liquid from the cyclone separator is recirculated to the reservoir to provide for the make-up liquid.

Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US4250974 *Sep 25, 1978Feb 17, 1981Exxon Production Research CompanyApparatus and method for detecting abnormal drilling conditions
US4599172 *Dec 24, 1984Jul 8, 1986Gardes Robert AFlow line filter apparatus
US4613347 *May 21, 1985Sep 23, 1986Compagnie Francaise Des PetrolesVertical colum, inert gas bubbles
US4666471 *Aug 2, 1985May 19, 1987Cates Thomas DMud degasser
US4982396 *Apr 8, 1988Jan 1, 1991Hitachi, Ltd.Information recording medium and apparatus using reversible phase change
US5109933 *Aug 17, 1990May 5, 1992Atlantic Richfield CompanyDrill cuttings disposal method and system
US5129469 *Dec 16, 1991Jul 14, 1992Atlantic Richfield CompanyDrill cuttings disposal method and system
US5339912 *Mar 26, 1993Aug 23, 1994Abb Vetco Gray Inc.Cuttings disposal system
US5344570 *Jan 14, 1993Sep 6, 1994James E. McLachlanEntrainment of solids, centrifuging, pumping and separation of solids
US5494584 *Jun 16, 1994Feb 27, 1996James E. McLachlanMethod and apparatus for controlling a pump upstream of a centrifuge
US5794722 *Aug 26, 1996Aug 18, 1998Sundowner Offshore Services, Inc.Gumbo removal
US5944195 *Jul 3, 1996Aug 31, 1999Exxon Production Research CompanyMethod for separation of solids from drilling fluids by magnetic separation and centrifugation
WO1992003633A1 *Jul 22, 1991Feb 18, 1992Atlantic Richfield CoDrill cuttings disposal method and system
U.S. Classification175/66, 175/206
International ClassificationE21B21/00, E21B21/06
Cooperative ClassificationE21B21/065
European ClassificationE21B21/06N2