Wear-resistant, polycrystalline diamond compacts (“PDCs”) are utilized in a variety of mechanical applications. For example, PDCs are used in drilling tools (e.g., cutting elements, gage trimmers, etc.), machining equipment, bearing apparatuses, wire-drawing machinery, and in other mechanical apparatuses.
PDCs have found particular utility as superabrasive cutting elements in rotary drill bits, such as roller-cone drill bits and fixed-cutter drill bits. A PDC cutting element typically includes a superabrasive diamond layer commonly known as a diamond table. The diamond table is formed and bonded to a substrate using a high-pressure/high-temperature (“HPHT”) process. The PDC cutting element may be brazed directly into a preformed pocket, socket, or other receptacle formed in a bit body. The substrate may often be brazed or otherwise joined to an attachment member, such as a cylindrical backing. A rotary drill bit typically includes a number of PDC cutting elements affixed to the bit body. It is also known that a stud carrying the PDC may be used as a PDC cutting element when mounted to a bit body of a rotary drill bit by press-fitting, brazing, or otherwise securing the stud into a receptacle formed in the bit body.
Conventional PDCs are normally fabricated by placing a cemented carbide substrate into a container or cartridge with a volume of diamond particles positioned on a surface of the cemented carbide substrate. A number of such cartridges may be loaded into an HPHT press. The substrate(s) and volume(s) of diamond particles are then processed under HPHT conditions in the presence of a catalyst material that causes the diamond particles to bond to one another to form a matrix of bonded diamond grains defining a polycrystalline diamond (“PCD”) table. The catalyst material is often a metal-solvent catalyst (e.g., cobalt, nickel, iron, or alloys thereof) that is used for promoting intergrowth of the diamond particles.
In one conventional approach, a constituent of the cemented carbide substrate, such as cobalt from a cobalt-cemented tungsten carbide substrate, liquefies and sweeps from a region adjacent to the volume of diamond particles into interstitial regions between the diamond particles during the HPHT process. The cobalt acts as a catalyst to promote intergrowth between the diamond particles, which results in formation of a matrix of bonded diamond grains having diamond-to-diamond bonding therebetween, with interstitial regions between the bonded diamond grains being occupied by the solvent catalyst.
The presence of the solvent catalyst in the PCD table is believed to reduce the thermal stability of the PCD table at elevated temperatures. For example, the difference in thermal expansion coefficient between the diamond grains and the solvent catalyst is believed to lead to chipping or cracking of the PCD table during drilling or cutting operations, which consequently can degrade the mechanical properties of the PCD table or cause failure. Additionally, some of the diamond grains can undergo a chemical breakdown or back-conversion to graphite via interaction with the solvent catalyst. At elevated high temperatures, portions of the diamond grains may transform to carbon monoxide, carbon dioxide, graphite, or combinations thereof, causing degradation of the mechanical properties of the PCD table.
One conventional approach for improving the thermal stability of PDCs is to at least partially remove the solvent catalyst from the PCD table of the PDC by acid leaching.
In another conventional approach for forming a PDC, a sintered PCD table may be separately formed and then leached to remove the solvent catalyst from interstitial regions between bonded diamond grains. The leached PCD table may be simultaneously HPHT bonded to a cemented carbide substrate and infiltrated with silicon and cobalt from the substrate in a separate HPHT process. The silicon may infiltrate the interstitial regions of the leached PCD table from which the solvent catalyst has been leached and react with the diamond grains to form silicon carbide. The cobalt may also infiltrate the interstitial regions of the leached PCD table from which the solvent catalyst has been leached to form a bond with the cemented carbide substrate. PDCs sold under the trade name Terracut were fabricated by the foregoing process.
Despite the availability of a number of different PDCs, manufacturers and users of PDCs continue to seek PDCs that exhibit improved toughness, wear resistance, thermal stability, or combinations thereof.
Embodiments of the invention relate to methods of manufacturing PDCs by infiltrating an at least partially leached PCD table in a controlled manner in an HPHT process, and resultant PDCs. The temperature, pressure, and HPHT process time are chosen to control a depth to which an infiltrant partially infiltrates into the at least partially leached PCD table in the HPHT process.
In an embodiment, a method of fabricating a PDC includes forming a PCD table in the presence of a metal-solvent catalyst in a first HPHT process. The PCD table so formed includes a plurality of bonded diamond grains defining a plurality of interstitial regions, with at least a portion of the plurality of interstitial regions including the metal-solvent catalyst disposed therein. The plurality of bonded diamond grains exhibits an average grain size of about 40 μm or less. The method further includes at least partially leaching the PCD table to remove at least a portion of the metal-solvent catalyst therefrom. The method additionally includes subjecting the at least partially leached PCD table and a substrate to a second HPHT process under diamond-stable temperature-pressure conditions to partially infiltrate the at least partially leached PCD table with an infiltrant and attach the partially infiltrated PCD table to the substrate. A maximum temperature (T), a total process time (t), and a maximum internal cell pressure (P) of the second HPHT process are chosen so that β is about 2 to about 325° Celsius·hours/gigapascals (“° C.·h/GPa”), with β represented as β=T·t/P. The infiltrated polycrystalline diamond table includes a first region adjacent to the substrate including the infiltrant disposed in at least a portion of the interstitial regions thereof and a second region extending inwardly from an exterior working surface to a selected depth of at least about 700 μm. The second region is substantially free of the infiltrant.
In an embodiment, a PDC includes a substrate, and a pre-sintered PCD table bonded to the substrate. The pre-sintered PCD table includes an exterior working surface, at least one lateral surface, and a chamfer extending between the exterior working surface and the at least one lateral surface. The pre-sintered PCD table includes a plurality of bonded diamond grains defining a plurality of interstitial regions. The plurality of bonded diamond grains exhibits an average grain size of about 40 μm or less. The pre-sintered PCD table further includes a first region and a second region. The first region is adjacent to the substrate, and at least a portion of the interstitial regions of the first region include an infiltrant disposed therein. The second region is adjacent to the first region and extends inwardly from the exterior working surface to a selected depth of at least about 700 μm. The interstitial regions of the second region are substantially free of the infiltrant. A nonplanar interface is located between the first and second regions.
Other embodiments include applications utilizing the disclosed PDCs in various articles and apparatuses, such as, rotary drill bits, bearing apparatuses, machining equipment, and other articles and apparatuses.
Features from any of the disclosed embodiments may be used in combination with one another, without limitation. In addition, other features and advantages of the present disclosure will become apparent to those of ordinary skill in the art through consideration of the following detailed description and the accompanying drawings.
The drawings illustrate several embodiments of the invention, wherein identical reference numerals refer to identical elements or features in different views or embodiments shown in the drawings.
Embodiments of the invention relate to methods of manufacturing PDCs by infiltrating an at least partially leached PCD table in a controlled manner in an HPHT process, and resultant PDCs. The temperature, pressure, and HPHT process time are chosen to control a depth to which an infiltrant partially infiltrates into the at least partially leached PCD table in the HPHT process. The disclosed PDCs may be used in a variety of applications, such as rotary drill bits, machining equipment, and other articles and apparatuses.
The diamond grains of the PCD table 102 may exhibit an average grain size of about 40 μm or less, such as about 30 μm or less, about 25 μm or less, or about 20 μm or less. For example, the average grain size of the diamond grains may be about 10 μm to about 18 μm, about 8 μm to about 15 μm, about 9 μm to about 12 μm, or about 15 μm to about 18 μm. In some embodiments, the average grain size of the diamond grains may be about 10 μm or less, such as about 2 μm to about 5 μm or submicron. The diamond grain size distribution of the diamond grains may exhibit a single mode, or may be a bimodal or greater grain size distribution.
The PCD table 102 exhibits a thickness “t” of at least about 0.040 inch, such as about 0.045 inch to about 0.100 inch, about 0.050 inch to about 0.090 inch, about 0.065 inch to about 0.080 inch, or about 0.070 inch to about 0.080 inch. The infiltrated polycrystalline diamond table 102 includes a first region 110 adjacent to the substrate 108 that extends from the interfacial surface 109 an average selected infiltration distance “h” and includes an infiltrant disposed in at least a portion of the interstitial regions thereof. The infiltrant may be chosen from iron, nickel, cobalt, and alloys of the foregoing metals. For example, the infiltrant may be provided from the substrate 108 (e.g., a cobalt from a cobalt-cemented carbide substrate) or provided from another source such as a metallic foil and/or powder. The PCD table 102 includes a second region 112 that extends inwardly from the working surface 106 to an average selected depth “d.” The depth “d” may be at least about 700 μm, about 700 μm to about 2100 μm, about 750 μm to about 2100 μm, about 750 μm to about 1500 μm, about 1000 μm to about 1750 μm, about 1000 μm to about 2000 μm, about 1500 μm to about 2000 μm, about a third of the thickness of the PCD table 102, about half of the thickness of the PCD table 102, or about more than half of the thickness of the PCD table 102. The interstitial regions of the second region 112 are substantially free of the infiltrant.
As the PCD table 102 was fabricated from an at least partially leached PCD table that was subsequently partially infiltrated with the infiltrant, the second region 112 may still include some residual metal-solvent catalyst used to initially form the diamond-to-diamond bonds in the PCD table 112 that was not removed in the leaching process. For example, the residual metal-solvent catalyst in the interstitial regions of the second region 112 may be about 0.5% to about 2% by weight, such as about 0.9% to about 1% by weight. Even with the residual amount of the metal-solvent catalyst in the second region 112, the interstitial regions of the second region 112 may be considered to be substantially void of material.
The substrate 108 comprises a plurality of tungsten carbide or other carbide grains (e.g., tantalum carbide, vanadium carbide, niobium carbide, chromium carbide, and/or titanium carbide) cemented together with a metallic cementing constituent, such as cobalt, iron, nickel, or alloys thereof. For example, in an embodiment, the cemented carbide substrate is a cobalt-cemented tungsten carbide substrate. In some embodiments, the substrate 108 may include two or more different carbides (e.g., tungsten carbide and titanium carbide).
The inventors currently believe that the infiltration depth “h” is primarily governed by capillary action, which depends heavily on the viscosity, surface energy, and contact angle of the infiltrant (e.g., cobalt), as well as the time period over which the HPHT conditions are maintained. For example, according to one theory, the infiltration depth “h” is approximated by the mathematical expression below:
where:
h=infiltration depth;
r=radius of the interstitial regions of the PCD table 102;
t=time;
ϑ=contact angle of the infiltrant with the at least partially leached PCD table 102;
γ=surface energy of the infiltrant; and
υ=viscosity (which depends on temperature and pressure) of the infiltrant.
According to one theory, the porosity of the PCD table 102 draws the infiltrant further into the PCD table 102 as a result of capillary action. The infiltration depth “h” is not simply a function of pressure, as increased pressure would be expected to drive more complete penetration of the infiltrant through the PCD table 102. Rather, as shown by working examples 1-4 below, infiltration depth “h” appears to be governed by capillary action so that at a given pressure for which substantially full infiltration occurs, higher pressures (and the same temperature and HPHT process time) will result in less infiltration. According to one theory, infiltration occurs through capillary action rather than a pressure differential. The viscosity of the infiltrant increases at increased pressures, causing less infiltration to occur than at lower pressures, all else being equal. Viscosity is also affected by temperature, i.e., as temperature increases, viscosity decreases, so that at higher temperatures, increased infiltration results. Infiltration may also be affected by process time. Increased processing times result in increased depth of infiltration.
The temperature, pressure, and time period during the HPHT process used for attachment of the PCD table 102 to the substrate 108 may be controlled so as to provide for a desired infiltration depth “h.” Partial infiltration of the PCD table 102 may provide the same or better wear resistance and/or thermal stability characteristics of a leached PCD table integrally formed on a substrate (i.e., a one-step PDC) without actual leaching having to be performed, as the infiltrant does not fully infiltrate to the working surface 106 of the PCD table 102. Examples of such an embodiment are described in working examples 3 and 4, below. In some embodiments, the PCD table 102 may be leached to remove a portion of the infiltrant from the first region 110 to improve the uniformity of infiltrant in the first region 110, thermal stability, wear resistance, or combinations of the foregoing. Examples of such embodiments are described in working examples 5-7, below.
It is noted that an irregular nonplanar interface 114 is present between the first region 110 and the second region 112. One effect of this characteristic is that this nonplanar interface 114 between the first region 110 and the second region 112 differs from an otherwise similarly appearing PDC, but in which a region similar to second region 112 (in that it is substantially void of infiltrant) is formed by leaching, particularly if the PCD table 102 includes a chamfer formed therein. In such instances, the leaching profile advances from the outer surfaces exposed to the leaching acid. For example, leaching typically progresses from the exterior surfaces downward and/or inward so that any chamfer or end exposed to the acid affects the leaching profile. The incomplete infiltration operates by a different mechanism in which infiltration occurs from the “bottom up,” so that the presence of the chamfer 107 in the PCD table 102 does not affect the infiltration profile of the infiltrant. Additionally, if the infiltrant had infiltrated the entire PCD table 102 so that the interstitial regions of the second region 112 were also occupied by the infiltrant and subsequently removed in a leaching process to the depth “d,” a boundary between the first region 110 and the second region 112 would be indicative of being defined by a leaching process as opposed to being relatively irregular.
As will be discussed in more detail below, the PCD table 102 is formed separately from the substrate 108, and the PCD table 102 is subsequently attached to the substrate 108. For example, in an embodiment, the PCD table 102 may be integrally formed with a first cemented carbide substrate, after which the first substrate is removed, the separated PCD table is at least partially leached, and the at least partially leached PCD table is then attached to the substrate 108 in a second HPHT process. In another embodiment, the PCD table 102 may be formed without using a cemented carbide substrate (e.g., by subjecting diamond particles and a metal-solvent catalyst to a HPHT process), after which the formed PCD table is at least partially leached and attached to the substrate 108.
When attaching the PCD table 102 to substrate 108 in a second HPHT process, the HPHT process conditions (e.g., maximum temperature, maximum pressure, and total process time) are specifically chosen to result in only partial infiltration of the PCD table 102. As a result of this second HPHT process, the infiltrant within the substrate 108 (e.g., cobalt from a cobalt-cemented tungsten carbide) infiltrates from the substrate 108 into at least some of the interstitial regions of PCD table 102 in the first region 110.
In an embodiment, the diamond particles of the one or more layers of diamond particles 150 may exhibit an average particle size of about 40 μm or less, such as about 30 μm or less, about 25 μm or less, or about 20 μm or less. For example, the average particle size of the diamond particles may be about 10 μm to about 18 μm, about 8 μm to about 15 μm, about 9 μm to about 12 μm, or about 15 μm to about 18 μm. In some embodiments, the average particle size of the diamond particles may be about 10 μm or less, such as about 2 μm to about 5 μm or submicron.
The diamond particle size distribution of the diamond particle may exhibit a single mode, or may be a bimodal or greater grain size distribution. In an embodiment, the diamond particles of the one or more layers of diamond particles 150 may comprise a relatively larger size and at least one relatively smaller size. As used herein, the phrases “relatively larger” and “relatively smaller” refer to particle sizes (by any suitable method) that differ by at least a factor of two (e.g., 30 μm and 15 μm). According to various embodiments, the diamond particles may include a portion exhibiting a relatively larger average particle size (e.g., 50 μm, 40 μm, 30 μm, 20 μm, 15 μm, 12 μm, 10 μm, 8 μm) and another portion exhibiting at least one relatively smaller average particle size (e.g., 6 μm, 5 μm, 4 μm, 3 μm, 2 μm, 1 μm, 0.5 μm, less than 0.5 μm, 0.1 μm, less than 0.1 μm). In an embodiment, the diamond particles may include a portion exhibiting a relatively larger average particle size between about 10 μm and about 40 μm and another portion exhibiting a relatively smaller average particle size between about 1 μm and 4 μm. In some embodiments, the diamond particles may comprise three or more different average particle sizes (e.g., one relatively larger average particle size and two or more relatively smaller average particle sizes), without limitation.
It is noted that the as-sintered diamond grain size may differ from the average particle size of the diamond particles prior to sintering due to a variety of different physical processes, such as grain growth, diamond particles fracturing, carbon provided from another carbon source (e.g., dissolved carbon in the metal-solvent catalyst), or combinations of the foregoing.
The first cemented carbide substrate 105 and the one or more layers of diamond particles 150 may be placed in a pressure transmitting medium, such as a refractory metal can embedded in pyrophillite or other pressure transmitting medium. The pressure transmitting medium, including the first cemented carbide substrate 105 and the one or more layers of diamond particles 150 therein, may be subjected to a first HPHT process using an ultra-high pressure press to create temperature and pressure conditions at which diamond is stable. The temperature of the first HPHT process may be at least about 1000° C. (e.g., about 1200° C. to about 1600° C.) and the pressure of the first HPHT process may be at least 4.0 GPa (e.g., about 5.0 GPa to about 12.0 GPa) for a time sufficient to sinter the diamond particles to form the PCD table 150′. For example, the pressure of the first HPHT process may be about 5 GPa to about 7 GPa and the temperature of the first HPHT process may be about 1150° C. to about 1450° C. (e.g., about 1200° C. to about 1400° C.).
During the first HPHT process, the metal-solvent catalyst cementing constituent from the first cemented carbide substrate 105 may be liquefied and may infiltrate into the diamond particles of the one or more layers of diamond particles 150. The infiltrated metal-solvent catalyst cementing constituent functions as a catalyst that catalyzes initial formation of directly bonded-together diamond grains to form the PCD table 150′.
In an alternative to using the first cemented carbide substrate 105 during sintering of the diamond particles, the PCD table 150′ may be formed by placing the diamond particles along with a metal-solvent catalyst (e.g., cobalt powder and/or a cobalt disc) in a pressure transmitting medium, such as a refractory metal can embedded in pyrophyllite or other pressure transmitting medium. The pressure transmitting medium, including the diamond particles and metal-solvent catalyst therein, may be subjected to a first HPHT process using an ultra-high pressure press to create temperature and pressure conditions at which diamond is stable. Such a process will result in the formation of a PCD table 150′ separate from any cemented carbide substrate 105.
In embodiments in which the PCD table 150′ is formed so as to be metallurgically bonded to a cemented carbide substrate, the PCD table 150′ may then be separated from the first cemented carbide substrate 105, as shown in
Whether the first cemented carbide substrate 105 is employed during formation of the PCD table 150′ or not, the metal-solvent catalyst may be at least partially removed from the PCD table 150′ by immersing the PCD table 150′ in an acid, such as aqua regia, nitric acid, hydrofluoric acid, mixtures thereof, or other suitable acid, to form a porous at least partially leached PCD table 150″ that allows fluid to flow therethrough (e.g., from one side to another side). For example, the PCD table 150′ may be immersed in the acid for about 2 to about 7 days (e.g., about 3, 5, or 7 days) or for a few weeks (e.g., about 4-6 weeks) depending on the process employed. In some embodiments, a residual amount of the metal-solvent catalyst used to catalyze formation of the diamond-to-diamond bonds of the PCD table 150′ may still remain even after leaching. For example, the residual metal-solvent catalyst in the interstitial regions may be about 0.5% to about 2% by weight, such as about 0.9% to about 1% by weight.
In embodiments employing the cemented carbide substrate 105, it is noted that because the metal-solvent catalyst is infiltrated into the diamond particles from the cemented carbide substrate 105 including tungsten carbide or other carbide grains cemented with a metal-solvent catalyst (e.g., cobalt, nickel, iron, or alloys thereof), the infiltrated metal-solvent catalyst may carry tungsten therewith, tungsten carbide therewith, another metal therewith, another metal carbide therewith, or combinations of the foregoing. In such embodiments, the PCD table 150′ and the at least partially leached PCD table 150″ may include such material(s) disposed interstitially between the bonded diamond grains. The tungsten therewith, tungsten carbide therewith, another metal therewith, another metal carbide therewith, or combinations of the foregoing may be at least partially removed by the selected leaching process or may be relatively unaffected by the selected leaching process.
As shown in
As an alternative to using the cemented carbide substrate 108 as an infiltrant source, an infiltrant layer (e.g., a cobalt disc) may be disposed between the cemented carbide substrate 108 and the PCD table 150″. In such an embodiment, the infiltrant layer may liquefy and infiltrate into the PCD table 150″ during the second HPHT process.
The infiltration depth “h” may be controlled by selection of the maximum temperature, maximum pressure, and total process time of the second HPHT process during which the PCD table 150″ attaches to substrate 108. As used herein, total process time includes the time to ramp-up to the maximum temperature, the soak time at the maximum temperature, and the cool down time from the maximum temperature. The second HPHT process conditions are controlled so that the infiltrant from the substrate 108 only partially infiltrates the PCD table 150″ to form the PCD table 102 having the first region 110 and the second region 112, respectively in which the interstitial regions of the second region 112 remain unfilled by the infiltrant infiltrated from the substrate 108.
An HPHT process parameter β may be defined to characterize the second HPHT process during which the PCD table 150″ attaches to substrate 108. β is defined as β=T·t/P, where:
T is a maximum temperature of the second HPHT process;
t is the total process time (t) of the second HPHT process; and
P is a maximum internal cell pressure in the pressure transmitting medium used in the second HPHT process.
β may be about 2° C.·h/GPa to about 325° C.·h/GPa, about 5° C.·h/GPa to about 100° C.·h/GPa, about 5° C.·h/GPa to about 35° C.·h/GPa, about 7.5° C.·h/GPa to about 25° C.·h/GPa, about 10° C.·h/GPa to about 20° C.·h/GPa, about 20° C.·h/GPa to about 30° C.·h/GPa (e.g., 24-26° C.·h/GPa), about greater than 28° C.·h/GPa, about 30° C.·h/GPa to about 100° C.·h/GPa, about 50° C.·h/GPa to about 75° C.·h/GPa, about 75° C.·h/GPa to about 150° C.·h/GPa, or about 100° C.·h/GPa to about 200° C.·h/GPa. By controlling T, t, and P of the second HPHT process, the infiltration depth “h” may be controlled so that the PCD table 150″ is only partially infiltrated. For a given thickness of the PCD table 150″, the infiltration depth “h” may be decreased by increasing P, decreasing T, decreasing t, or combinations thereof. Thus, for a given thickness of the PCD table 150″, the infiltration depth “h” may be decreased by decreasing β and increased by increasing β.
In the second HPHT process, in some embodiments, P is about 6 GPa to about 10 GPa, T is about 1250° C. to about 3250° C., and t is about 60 seconds to about 1 hour. In other more specific embodiments for the second HPHT process that will result in partial infiltration of a 3.5-5 mm thick PCD table 150″, P is about 6 GPa to about 8 GPa (e.g., about 6.1 GPa to about 7.0 GPa), T is about 1250° C. to about 1500° C., and t is about 60 seconds to about 7 minutes (e.g., about 200-450 seconds) that results in the depth “d” of the second region 112 of the PCD table 102 being at least about a third of the PCD table thickness, about half of the PCD table thickness, or more than half of the PCD table thickness. The time (t) for the second HPHT process is typically longer when a high-pressure belt press is used to apply pressure as opposed to a high-pressure cubic press. Typical times used with a high-pressure cubic pressure are about 200-450 seconds, such as about 300-400 seconds of total process time.
The inventors have unexpectedly found that increasing the pressure (P) during the second HPHT process results in decreased infiltration. As explained above, one theory is infiltration occurs through capillary action, and that the increased pressure (P) increases the viscosity of the infiltrant, allowing the infiltrant to infiltrate into the PCD table 150″ a relatively less extent than if a higher pressure (P) is employed. For example, in an embodiment the first HPHT process may be carried out at a pressure of about 6 GPa, while in order to achieve partial infiltration, the second HPHT process may be carried out at a pressure between about 6.2 GPa and about 10 GPa (e.g., about 6.3 GPa to about 8.5 GPa, or about 6.3 GPa to about 7 GPa). The temperature and time period of the first and second processes may otherwise be the same (e.g., 1400° C. for about 400 seconds). Higher pressures may be employed to further decrease the infiltration depth “h” for a given temperature (T), time (t), and thickness of the PCD table 150″. In other words, as the pressure (P) increases, the infiltration will be less complete.
In a similar manner, the temperature (T) may be altered from the first process to the second process to achieve a similar result. For example, a decrease in temperature (T) provides a similar effect relative to infiltration depth “h” as an increase in pressure (P). Processing time (t) may also be altered from the first process to the second process to achieve a desired infiltration depth “h”. For example, increasing processing time (t) provides a similar effect relative to infiltration depth “h” as a decrease in pressure (P). More than one of the temperature (T), pressure (P), or processing time (t) variables may be changed to achieve a desired infiltration depth “h” and any of the resultant selected depths “d” disclosed herein.
In some embodiments, at least one of the P, T, or tin the second HPHT process are different than an associated P, T, or t used in the first HPHT process used to initially sinter the diamond particles that forms the PCD table 150′.
In some embodiments, the infiltrant that occupies the interstitial regions of the first region 110 of the PCD table 102 may be at least partially removed in a subsequent leaching process using an acid, such as aqua regia, nitric acid, hydrofluoric acid, mixtures thereof, or other suitable acid. Even though the second region 112 is already substantially free of the infiltrant, the inventors have found that leaching may improve the uniformity of the interface 114 between the first region 110 and the second region 112, which may improve thermal stability and/or wear resistance in the finished PDC 100.
The following working examples provide further detail in connection with the specific PDC embodiments described above.
A PDC was formed according to the following process. A layer of diamond particles was placed adjacent to a cobalt-cemented tungsten carbide substrate. The diamond particles and the substrate were positioned within a pyrophyllite cube, and HPHT processed at a temperature of about 1400° C. and a pressure of about 6 GPa for about 250 seconds of soak time (about 370 seconds total process time) at the 1400° C. temperature in a high-pressure cubic press to sinter the diamond particles and attach the resulting PCD table to the substrate. The thickness of the PCD table of the PDC was about 0.083 inch and an about 0.012 inch chamfer was machined in the PCD table.
The thermal stability of the conventional unleached PDC so-formed was evaluated by measuring the distance cut in a Sierra White granite workpiece prior to failure without using coolant in a vertical turret lathe test. The distance cut is considered representative of the thermal stability of the PDC. The conventional unleached PDC was able to cut a distance of only about 1000 linear feet in the workpiece prior to failure. The test parameters were a depth of cut for the PDC of about 1.27 mm, a back rake angle for the PDC of about 20 degrees, an in-feed for the PDC of about 1.524 mm/rev, and a cutting speed of the workpiece to be cut of about 1.78 m/sec. Evidence of failure of the conventional unleached PDC is best shown in
A PDC was formed according to the following process. A layer of diamond particles having the same particle size distribution as comparative example A was placed adjacent to a cobalt-cemented tungsten carbide substrate. The diamond particles and the substrate were positioned within a pyrophyllite cube, and HPHT processed at a temperature of about 1400° C. and a pressure of about 6 GPa for about 250 seconds of soak time (about 370 seconds total process time) at the 1400° C. temperature in a high-pressure cubic press to sinter the diamond particles and attach the resulting PCD table to the substrate. The PCD table was subsequently leached to remove cobalt from the interstitial regions between diamond grains within the PCD table to a depth of about 94 μm. The thickness of the PCD table of the PDC was about 0.088 inches and an about 0.012 inch chamfer was machined in the PCD table.
The thermal stability of the conventional leached PDC so-formed was evaluated by measuring the distance cut in the same Sierra White granite workpiece as Comparative Example A prior to failure without using coolant in a vertical turret lathe test and using the same test parameters. The distance cut is considered representative of the thermal stability of the PDC. The conventional leached PDC was able to cut a distance of about 3500 linear feet in the workpiece prior to failure. Evidence of failure of the conventional PDC is best shown in
Two PDCs were formed according to the following process. A layer of diamond particles having the same particle size distribution as comparative example A was placed adjacent to a first cobalt-cemented tungsten carbide substrate. The diamond particles and the first cobalt-cemented tungsten carbide substrate were positioned within a pyrophyllite cube, and HPHT processed at a temperature of about 1400° C. and a pressure of about 6 GPa for about 250 seconds of soak time (about 370 seconds total process time) at the 1400° C. temperature in a high-pressure cubic press to sinter the diamond particles and attach the resulting PCD table to the first cobalt-cemented tungsten carbide substrate. The PCD table was then separated from the first cobalt-cemented tungsten carbide substrate by grinding away the first cemented tungsten carbide substrate. The PCD table was subsequently leached to remove substantially all of the cobalt from the interstitial regions between diamond grains within the PCD table. The leached PCD table was then placed adjacent to a second cobalt-cemented tungsten carbide substrate. The PCD table and the second cobalt-cemented tungsten carbide substrate were positioned within a pyrophyllite cube, and HPHT processed at a temperature of about 1400° C. and a pressure of about 5.1 GPa for about 250 seconds of soak time (about 400 seconds total process time) at the 1400° C. in a high-pressure cubic press to attach the PCD table to the second tungsten carbide substrate. A scanning electron microscope image (
The thickness of the PCD table of one PDC was about 0.079 inch and an about 0.012 inch chamfer was machined in the PCD table. The thickness of the PCD table of the other PDC was about 0.080 inch and an about 0.013 inch chamfer was machined in the PCD table.
The thermal stability of the unleached PDCs so-formed was evaluated by measuring the distance cut in the same Sierra White granite workpiece as Comparative Example A prior to failure without using coolant in a vertical turret lathe test using the same test parameters. The distance cut is considered representative of the thermal stability of the PDC. One of the unleached PDCs was able to cut a distance of about 2000 linear feet in the workpiece prior to failure. The other unleached PDC was able to cut a distance of about 2500 linear feet in the workpiece prior to failure. Evidence of failure of each PDC is best shown in
Two PDCs were formed according to the following process. A layer of diamond particles having the same particle size distribution as comparative example A was placed adjacent to a first cobalt-cemented tungsten carbide substrate. The diamond particles and the first cobalt-cemented tungsten carbide substrate were positioned within a pyrophyllite cube, and HPHT processed at a temperature of about 1400° C. and a pressure of about 6 GPa for about 250 seconds of soak time (about 370 seconds total process time) at the 1400° C. temperature in a high-pressure cubic press to sinter the diamond particles and attach the resulting PCD table to the first cobalt-cemented tungsten carbide substrate. The PCD table was then separated from the first tungsten carbide substrate by grinding away the first cemented tungsten carbide substrate. The PCD table was leached to remove substantially all of the cobalt from the interstitial regions between diamond grains within the PCD table. The leached PCD table was then placed adjacent to a second cobalt-cemented tungsten carbide substrate. The PCD table and the second cobalt-cemented tungsten carbide substrate were positioned within a pyrophyllite cube, and HPHT processed at a temperature of about 1400° C. and a pressure of about 5.7 GPa for about 250 seconds of soak time (about 400 seconds total process time) at the 1400° C. temperature in a high-pressure cubic press to attach the PCD table to the second cobalt-cemented tungsten carbide substrate. A scanning electron microscope image (
The thickness of the PCD table of the first PDC was about 0.081 inch and an about 0.012 inch chamfer was machined in the PCD table. The thickness of the PCD table of the second PDC was about 0.079 inch and an about 0.012 inch chamfer was machined in the PCD table.
The thermal stability of the unleached PDC so-formed was evaluated by measuring the distance cut in the same Sierra White granite workpiece as Comparative Example A prior to failure without using coolant in a vertical turret lathe test and using the same test parameters. The distance cut is considered representative of the thermal stability of the PDC. One of the unleached PDCs was able to cut a distance of about 1000 linear feet in the workpiece prior to failure. The other was able to cut a distance of about 2000 linear feet in the workpiece prior to failure. Evidence of failure of each PDC is best shown in
Two PDCs were formed according to the following process. A layer of diamond particles having the same particle size distribution as comparative example A was placed adjacent to a first cobalt-cemented tungsten carbide substrate. The diamond particles and the first cobalt-cemented tungsten carbide substrate were positioned within a pyrophyllite cube, and HPHT processed at a temperature of about 1400° C. and a pressure of about 6 GPa for about 250 seconds of soak time (about 370 seconds total process time) at the 1400° C. temperature in a high-pressure cubic press to sinter the diamond particles and attach the resulting PCD table to the first cobalt-cemented tungsten carbide substrate. The PCD table was then separated from the first cobalt-cemented tungsten carbide substrate by grinding away the first cemented tungsten carbide substrate. The PCD table was leached to remove substantially all of the cobalt from the interstitial regions between diamond grains within the PCD table. The leached PCD table was then placed adjacent to a second cobalt-cemented tungsten carbide substrate. The PCD table and the second cobalt-cemented tungsten carbide substrate were positioned within a pyrophyllite cube, and HPHT processed at a temperature of about 1400° C. and a pressure of about 6.3 GPa for about 250 seconds of soak time (about 400 seconds total process time) at the 1400° C. temperature in a high-pressure cubic press to attach the PCD table to the second cobalt-cemented tungsten carbide substrate. A scanning electron microscope image (
The thickness of the PCD table of the first PDC was about 0.081 inch and an about 0.013 inch chamfer was machined in the PCD table. The thickness of the PCD table of the second PDC was about 0.082 inch and an about 0.013 inch chamfer was machined in the PCD table.
The thermal stability of the unleached PDC so-formed was evaluated by measuring the distance cut in the same Sierra White granite workpiece as Comparative Example A prior to failure without using coolant in a vertical turret lathe test and using the same test parameters. The distance cut is considered representative of the thermal stability of the PDC. One of the unleached PDCs was able to cut a distance of about 5500 linear feet in the workpiece without failing and without using coolant. The other was able to cut a distance of about 9000 linear feet in the workpiece without failing and without using coolant. This is best shown in
Two PDCs were formed according to the following process. A layer of diamond particles having the same particle size distribution as comparative example A was placed adjacent to a first cobalt-cemented tungsten carbide substrate. The diamond particles and the first cobalt-cemented tungsten carbide substrate were positioned within a pyrophyllite cube, and HPHT processed at a temperature of about 1400° C. and a pressure of about 6 GPa for about 250 seconds of soak time (about 370 seconds total process time) at the 1400° C. temperature in a high-pressure cubic press to sinter the diamond particles and attach the resulting PCD table to the first cobalt-cemented tungsten carbide substrate. The PCD table was then separated from the first cobalt-cemented tungsten carbide substrate by grinding away the first cemented tungsten carbide substrate. The PCD table was subsequently leached to remove substantially all of the cobalt from the interstitial regions between diamond grains within the PCD table. The leached PCD table was then placed adjacent to a second cobalt-cemented tungsten carbide substrate. The PCD table and the second cobalt-cemented tungsten carbide substrate were positioned within a pyrophyllite cube, and HPHT processed at a temperature of about 1400° C. and a pressure of about 7 GPa for about 250 seconds of soak time (about 400 seconds total process time) at the 1400° C. temperature in a high-pressure cubic press to attach the PCD table to the second cobalt-cemented tungsten carbide substrate. A scanning electron microscope image (
The thickness of the PCD table of the first PDC was about 0.075 inch and an about 0.013 inch chamfer was machined in the PCD table. The thickness of the PCD table of the second PDC was about 0.077 inch and an about 0.013 inch chamfer was machined in the PCD table.
The thermal stability of the unleached PDC so-formed was evaluated by measuring the distance cut in the same Sierra White granite workpiece as Comparative Example A prior to failure without using coolant in a vertical turret lathe test and using the same test parameters. The distance cut is considered representative of the thermal stability of the PDC. Both of the unleached PDCs were able to cut a distance of about 13500 linear feet in the workpiece without failing and without using coolant. This is best shown in
Thermal stability tests as shown in
The wear resistance of the PDCs formed according to comparative examples A and B, as well as working examples 1-4 were evaluated by measuring the volume of the PDC removed versus the volume of a Sierra White granite workpiece removed in a vertical turret lathe with water used as a coolant. The test parameters were a depth of cut for the PDC of about 0.254 mm, a back rake angle for the PDC of about 20 degrees, an in-feed for the PDC of about 6.35 mm/rev, and a rotary speed of the workpiece to be cut of about 101 RPM.
As shown in
A PDC was formed according to the following process. A layer of diamond particles having the same particle size distribution as comparative example A was placed adjacent to a cobalt-cemented tungsten carbide substrate. The diamond particles and the substrate were positioned within a pyrophyllite cube, and HPHT processed at a temperature of about 1400° C. and a pressure of about 6 GPa for about 250 seconds of soak time (about 370 seconds total process time) at the 1400° C. temperature in a high-pressure cubic press to sinter the diamond particles and attach the resulting PCD table to the substrate.
The thickness of the polycrystalline diamond table of the PDC was about 0.086 inches and an about 0.012 inch chamfer was machined in the polycrystalline diamond table. The thermal stability of the conventional unleached PDC so-formed was evaluated by measuring the distance cut in a Sierra White granite workpiece prior to failure without using coolant in a vertical turret lathe test using the same test parameters as comparative example A. The distance cut is considered representative of the thermal stability of the PDC. The conventional unleached PDC was able to cut a distance of only about 1000 linear feet in the workpiece prior to failure. Evidence of failure of the conventional unleached PDC is best shown in
A PDC was formed according to the following process. A layer of diamond particles having the same particle size distribution as comparative example A was placed adjacent to a cobalt-cemented tungsten carbide substrate. The diamond particles and the substrate were positioned within a pyrophyllite cube, and HPHT processed at a temperature of about 1400° C. and a pressure of about 6 GPa for about 250 seconds of soak time (about 370 seconds total process time) at the 1400° C. temperature in a high-pressure cubic press to sinter the diamond particles and attach the resulting PCD table to the substrate. The PCD table was subsequently leached to remove the cobalt from the interstitial regions between diamond grains within the PCD table to a depth of 78 μm.
The thickness of the PCD table of the PDC was about 0.092 inches and an about 0.013 inch chamfer was machined in the polycrystalline diamond table. The thermal stability of the conventional PDC so-formed was evaluated by measuring the distance cut in the same Sierra White granite workpiece as Comparative Example C prior to failure without using coolant in a vertical turret lathe test. The distance cut is considered representative of the thermal stability of the PDC. The conventional leached PDC was able to cut a distance of about 2000 linear feet in the workpiece prior to failure. Evidence of failure of the conventional PDC is best shown in
A PDC was formed according to the following process. A layer of diamond particles having the same particle size distribution as comparative example A was placed adjacent to a first cobalt-cemented tungsten carbide substrate. The diamond particles and the first cobalt-cemented tungsten carbide substrate were positioned within a pyrophyllite cube, and HPHT processed at a temperature of about 1400° C. and a pressure of about 6 GPa for about 250 seconds of soak time (about 370 seconds total process time) at the 1400° C. temperature in a high-pressure cubic press to sinter the diamond particles and attach the resulting PCD table to the first cobalt-cemented tungsten carbide substrate. The PCD table was then separated from the first tungsten carbide substrate by grinding away the first cobalt-cemented tungsten carbide substrate. The PCD table was then placed adjacent to a second cobalt-cemented tungsten carbide substrate. The PCD table and the second cobalt-cemented tungsten carbide substrate were positioned within a pyrophyllite cube, and HPHT processed at a temperature of about 1400° C. and a pressure of about 6.1 GPa for about 250 seconds of soak time (about 400 seconds total process time) at the 1400° C. temperature in a high-pressure cubic press to attach the PCD table to the second cobalt-cemented tungsten carbide substrate. Scanning electron microscope images of the PDC so-formed showed incomplete infiltration of cobalt from the second cobalt-cemented tungsten carbide substrate into the PCD table. The PCD was electrically non-conductive prior to leaching. The PCD table was subsequently leached for about 2 hours in nitric acid so as to remove cobalt from the interstitial regions between diamond grains within the PCD table.
The thickness of the PCD table of the PDC was about 0.078 inch and an about 0.012 inch chamfer was machined in the PCD table. The thermal stability of the unleached PDC so-formed was evaluated by measuring the distance cut in the same Sierra White granite workpiece as Comparative Example C prior to failure without using coolant in a vertical turret lathe test. The distance cut is considered representative of the thermal stability of the PDC. The PDC was able to cut a distance of about 24000 linear feet in the workpiece without failing and without using coolant. This is best shown in
A PDC was formed according to the following process. A layer of diamond particles having the same particle size distribution as comparative example A was placed adjacent to a first cobalt-cemented tungsten carbide substrate. The diamond particles and the first cobalt-cemented tungsten carbide substrate were positioned within a pyrophyllite cube, and HPHT processed at a temperature of about 1400° C. and a pressure of about 6 GPa for about 250 seconds of soak time (about 370 seconds total process time) at the 1400° C. temperature in a high-pressure cubic press to sinter the diamond particles and attach the resulting PCD table to the first cobalt-cemented tungsten carbide substrate. The PCD table was then separated from the first tungsten carbide substrate by grinding away the first cemented tungsten carbide substrate. The PCD table was then placed adjacent to a second cobalt-cemented tungsten carbide substrate. The PCD table and the second cobalt-cemented tungsten carbide substrate were positioned within a pyrophyllite cube, and HPHT processed at a temperature of about 1400° C. and a pressure of about 6.1 GPa for about 250 seconds of soak time (about 400 seconds total process time) at the 1400° C. temperature in a high-pressure cubic press to attach the PCD table to the second tungsten carbide substrate. Scanning electron microscope images of the PDC so-formed showed incomplete infiltration of cobalt from the second cobalt-cemented tungsten carbide substrate into the PCD table. The PCD was electrically non-conductive prior to leaching. The PCD table was subsequently leached for about 2 hours in nitric acid to remove cobalt from the interstitial regions between diamond grains within the PCD table.
The thickness of the polycrystalline diamond table of the PDC was about 0.081 inch and an about 0.012 inch chamfer was machined in the polycrystalline diamond table. The thermal stability of the unleached PDC so-formed was evaluated by measuring the distance cut in the same Sierra White granite workpiece as comparative example C prior to failure without using coolant in a vertical turret lathe test. The distance cut is considered representative of the thermal stability of the PDC. The PDC was able to cut a distance of about 30000 linear feet in the workpiece without failing and without using coolant. This is best shown in
A PDC was formed according to the following process. A layer of diamond particles having the same particle size distribution as comparative example A was placed adjacent to a first cobalt-cemented tungsten carbide substrate. The diamond particles and the first cobalt-cemented tungsten carbide substrate were positioned within a pyrophyllite cube, and HPHT processed at a temperature of about 1400° C. and a pressure of about 6 GPa for about 250 seconds of soak time (about 370 seconds total process time) at the 1400° C. temperature in a high-pressure cubic press to sinter the diamond particles and attach the resulting PCD table to the first tungsten carbide substrate. The PCD table was then separated from the first cobalt-cemented tungsten carbide substrate by grinding away the first cemented tungsten carbide substrate. The PCD table was then placed adjacent to a second cobalt-cemented tungsten carbide substrate. The PCD table and the second cobalt-cemented tungsten carbide substrate were positioned within a pyrophyllite cube, and HPHT processed at a temperature of about 1400° C. and a pressure of about 6.1 GPa for about 250 seconds of soak time (about 400 seconds total process time) at the 1400° C. temperature in a high-pressure cubic press to attach the PCD table to the second cobalt-cemented tungsten carbide substrate. Scanning electron microscope images of the PDC so-formed showed incomplete infiltration of cobalt from the second cobalt-cemented tungsten carbide into the PCD table. The PCD was electrically non-conductive prior to leaching. The PCD table was subsequently leached for about 2 hours in nitric acid so as to remove cobalt from the interstitial regions between diamond grains within the PCD table.
The thickness of the polycrystalline diamond table of the PDC was about 0.082 inch and an about 0.012 inch chamfer was machined in the polycrystalline diamond table. The thermal stability of the unleached PDC so-formed was evaluated by measuring the distance cut in the same Sierra White granite workpiece as comparative example C prior to failure without using coolant in a vertical turret lathe test. The distance cut is considered representative of the thermal stability of the PDC. The PDC was able to cut a distance of about 22000 linear feet in the workpiece without using coolant prior to failing. This is best shown in
The wear resistance of PDCs formed according to comparative examples C and D, as well as working examples 5-7 was evaluated by measuring the volume of the PDC removed versus the volume of a Sierra White granite workpiece removed in a vertical turret lathe with water used as a coolant. The test parameters were a depth of cut for the PDC of about 0.254 mm, a back rake angle for the PDC of about 20 degrees, an in-feed for the PDC of about 6.35 mm/rev, and a rotary speed of the workpiece to be cut of about 101 RPM.
As shown in
The PDCs formed according to the various embodiments disclosed herein may be used as PDC cutting elements on a rotary drill bit. For example, in a method according to an embodiment of the invention, one or more PDCs may be received that were fabricated according to any of the disclosed manufacturing methods and attached to a bit body of a rotary drill bit.
In addition, if desired, in some embodiments, a number of the PDCs 312 may be conventional in construction. Also, circumferentially adjacent blades 304 define so-called junk slots 320 therebetween. Additionally, the rotary drill bit 300 includes a plurality of nozzle cavities 318 for communicating drilling fluid from the interior of the rotary drill bit 300 to the PDCs 312.
The PDCs disclosed herein (e.g., PDC 100 of
Thus, the embodiments of PDCs disclosed herein may be used in any apparatus or structure in which at least one conventional PDC is typically used. In one embodiment, a rotor and a stator, assembled to form a thrust-bearing apparatus, may each include one or more PDCs (e.g., PDC 100 of
While various aspects and embodiments have been disclosed herein, other aspects and embodiments are contemplated. The various aspects and embodiments disclosed herein are for purposes of illustration and are not intended to be limiting. Additionally, the words “including,” “having,” and variants thereof (e.g., “includes” and “has”) as used herein, including the claims, shall be open ended and have the same meaning as the word “comprising” and variants thereof (e.g., “comprise” and “comprises”).
This application is a divisional of U.S. application Ser. No. 14/178,118 filed on 11 Feb. 2014, which is a continuation of U.S. application Ser. No. 12/961,787 filed on 7 Dec. 2010, the disclosure of each of which is incorporated herein, in its entirety, by this reference.
Number | Date | Country | |
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Parent | 14178118 | Feb 2014 | US |
Child | 16385262 | US |
Number | Date | Country | |
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Parent | 12961787 | Dec 2010 | US |
Child | 14178118 | US |