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Superabrasive particle synthesis with growth control

a technology of superabrasives and growth control, which is applied in the direction of crystal growth process, chemical/physical process, gel state, etc., can solve the problems of affecting the thermal stability of diamond grit, requiring a much longer growth time, and diamonds with a lower amount of inclusions

Inactive Publication Date: 2008-02-28
SUNG CHIEN MIN
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0155] In one detailed aspect of the present invention, the crystalline seed can be from about 10% to about 30% of the desired grown diamond particle size. Depending on the growth conditions and the size of the crystalline seed, the grown superabrasive particles can have a particle size from about 100 μm to about 2 mm. Most common superabrasive particles sizes can range from about 18 mesh to about 60 mesh. Even larger superabrasive particles can be grown if larger crystalline seeds are used. Typically, grown superabrasive particles useful in many abrasive and cutting applications can have a particle size from about 210 μm to about 1 mm. One advantage of the present invention is the uniformity of grown superabrasive particle sizes. The predetermined pattern and orientation of layers allows for substantially uniform nucleation and growth of diamond and cBN. Therefore, the grown superabrasive particles of the present invention have a very narrow size distribution and improved quality when compared to particles grown from randomly nucleated and seeded precursors. For example, the size distributions using the present invention are typically less than half the standard deviation of conventional random seeded methods. Typically, the grown superabrasive particles of the present invention also have inclusion levels which are typically not noticeable under unaided visual inspection. Typically, yields of from about 30% to about 90% conversion of carbon to diamond can be expected when using the present invention. Further, the percent of high quality diamond can range from 50% to about 90%, with over 70% being a typical yield. In some embodiments of the present invention, the yield of high quality diamonds can range from about 2 carat / cm3 to about 5 carat / cm3, and preferably from about 3.5 carat / cm3 to about 4.5 carat / cm3. FIG. 18 shows an assembly of grown diamond particles in accordance with the present invention. In FIG. 18, the diamond particles are substantially uniform in size and exhibit uniform euhedral crystal shapes. In this example, the diamond separation was predetermined at 0.9 mm.

Problems solved by technology

The amount of defects (e.g. metal inclusion) will also affect the thermal stability of the diamond grit.
Diamonds having a lower amount of inclusions can also wear slower at the cutting tips where heat is generated.
Because the saw grits are much larger than grinding grits, they require much longer growth time.
As the time for diamond growth increases, the more difficult it is to control pressure and temperature.
However, under ultrahigh pressure conditions during crystal growth, the pressure tends to continually decay due to the volume contraction associated with diamond formation.
Hence, it is very difficult to maintain optimal conditions of pressure and temperature for homogeneous growth of diamond grits.
Consequently, saw diamond grits are very difficult to grow, particularly those having high quality.
These difficulties partially account for the abundance of companies which can grow saw grits, while very few companies are capable of growing high grade saw grits having larger sizes.
As a result, very few companies can master the technology of growing coarse saw grits, in particular, those with high quality, high impact strength, and high thermal stability.
Unfortunately, typical processes also result in the crystals having external flaws, e.g., rough surfaces, and undesirable inclusions, e.g., metal and carbon inclusions.
Therefore, increased costs are incurred in segregating acceptable high strength diamonds from weaker, poor quality diamonds.
Random nucleation methods typically allow some regions of raw materials to be wasted while other regions are densely packed with diamond crystals having a high percentage of defects.
Some diamond synthesis methods have improved nucleation uniformity somewhat; however, during diamond growth local changes in pressure can occur.
If heating is accomplished by passing electrical current directly through the reaction cell, then diamond growth can also interfere with the electrical current used to control heating.
The results of such interference are non-uniformities and fluctuations in the temperature and pressure gradients across the reaction cell and thus a wide distribution of crystal sizes, crystal shapes, and inclusion levels.
This marginal yield still wastes large amounts of raw materials, reduces production efficiencies, and leaves considerable room for improvement.
However, such materials are intrinsically heterogeneous.
However, powdered mixture methods can be difficult to control.
For example, the density of graphite and metal catalyst materials differ significantly, making uniform mixing very difficult.
In addition, powdered mixture methods generally require even more strict control of process conditions than in layered methods.

Method used

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  • Superabrasive particle synthesis with growth control
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Examples

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example 1

[0157] A circular mold having a diameter of 28 mm was filled with powdered natural graphite having an average size of about 20 μm, low resistivity of about 5 μΩ-cm, and a degree of graphitization of 0.8. The graphite was purified to be substantially free of oil, organic binders, ash, or other non-carbon materials. The graphite was cold pressed at 150 MPa to form a particulate compact disk having a thickness of 0.7 mm and a density of 2 g / cm3 (12% porosity). High purity INVAR (Fe-35Ni with a mesh size of less than 40 μm) was placed on top of the graphite layer and cold pressed at 300 MPa to form a particulate catalyst layer having a thickness of 0.2 mm and a density of 6 / cm3 (about 20% porosity). A thin layer of adhesive was sprayed onto the particulate catalyst layer. A template similar to that shown in FIG. 2B, having apertures spaced 0.8 mm apart (center-to-center) and apertures 130 μm in diameter was placed on the catalyst layer. The template was covered in uncoated diamond seeds...

example 2

[0158] A circular mold having a diameter of 28 mm was filled with powdered natural graphite having an average size of about 20 μm, low resistivity of about 5 μΩ-cm, and a degree of graphitization of 0.8. The graphite was purified to be substantially free of oil, organic binders, ash, or other non-carbon materials. The graphite was mixed with high purity INVAR (Fe-35Ni with a mesh size of less than 40 μm). The weight ratio of graphite to metal catalyst was 1:1.5. The mixture was then cold pressed at 250 MPa to form a particulate compact disk having a thickness of 0.7 mm and a density of 2 g / cm3 (12% porosity). The particulate compact disk was coated with a thin layer of adhesive. A template similar to that shown in FIG. 2B, having apertures spaced 0.8 mm apart (center-to-center) and apertures 130 μm in diameter was placed on the compact disk. The template was covered in uncoated diamond seeds having a mesh size of 120 / 140 (about 115 μm in diameter) such that the apertures were filled...

example 3

[0159] Graphite disks were prepared by pressing natural graphite powder having a grain size of about 20 microns into disks 37 mm in diameter and 0.8 mm in thickness at about 400 MPa. The porosity of the resulting graphite disks was about 15%. Ni coated diamond seeds (precoated diameter of about 65-75 microns) having a coated diameter of about 105-125 microns were planted into the graphite disks in a grid pattern having a pitch of about 0.8 mm to form seeded graphite disks. The seeded graphite disks were alternated with INVAR (Fe65-Ni35) disks and loaded into a steel container to make a final growth cell of 38.8 mm in diameter and 30 mm in height. One hundred of these growth cells were pressed in a 2500 ton cubic press with a ram size of 600 mm to attain a pressure of about 5.2 GPa and temperature of about 1250° C. The pressure and temperature were maintained for 50 minutes and then the pressure was reduced and the temperature gradually decreased. The pressed growth cells were broken...

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Abstract

An improved method for synthesizing superabrasive particles provides high quality industrial superabrasive particles with high yield and a narrow size distribution. The synthesis method can include forming a growth precursor of a substantially homogeneous mixture of raw material and catalyst material or layers of raw material and metal catalyst. The growth precursor can have a layer of adhesive over at least a portion thereof. A plurality of crystalline seeds can be placed in a predetermined pattern on the layer of adhesive. The growth precursor can be maintained at a temperature and pressure at which the superabrasive crystal is thermodynamically stable for a time sufficient for a desired degree of growth. Advantageously, the patterned placement of crystalline seeds and disclosed processes allow for production of various morphologies of synthetic diamonds, including octahedral and cubic diamonds, and improved growth conditions generally. As a result, the grown superabrasive particles typically have a high yield of high quality particles and a narrow distribution of particle sizes.

Description

RELATED APPLICATIONS [0001] This application is a continuation of U.S. patent application Ser. No. 11 / 175,017, filed Jul. 5, 2005, which is a continuation-in-part of U.S. patent application Ser. No. 10 / 926,576, filed Aug. 25, 2004, which is a continuation-in-part of U.S. patent application Ser. No. 10 / 791,300, filed Mar. 1, 2004, which is a continuation-in-part of U.S. patent application Ser. No. 10 / 259,168, filed Sep. 27, 2002, which is a continuation-in-part of U.S. patent application Ser. No. 09 / 935,204, filed Aug. 22, 2001, now issued as U.S. Pat. No. 6,679,243, which is a continuation-in-part of U.S. patent application Ser. No. 09 / 399,573, filed Sep. 20, 1999, now issued as U.S. Pat. No. 6,286,498, which is a continuation-in-part application of U.S. patent application Ser. No. 08 / 835,117, filed Apr. 4, 1997, now issued as U.S. Pat. No. 6,039,641, and of U.S. patent application Ser. No. 08 / 832,852, filed Apr. 4, 1997, now abandoned, all of which are incorporated herein by refere...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C30B1/02C30B1/00B01J3/06B23P15/28B24D3/08B24D7/06B24D99/00C04B35/52C22C1/05C22C26/00E21B10/56E21B10/567
CPCB01J3/062Y10T428/2991B01J2203/062B01J2203/0625B01J2203/0645B01J2203/0655B01J2203/066B01J2203/068B01J2203/0685B22F2005/001B22F2999/00B23D61/18B23D65/00B23P15/28B24D3/08B24D7/066B24D18/00B24D99/005C04B35/52C09K3/1409C09K3/1445C22C1/051C22C26/00C22C2204/00E21B10/5676B01J2203/061B22F2207/03B22F1/0011B22F3/004B22F2003/1046B24D2203/00B22F1/05
Inventor SUNG, CHIEN-MIN
Owner SUNG CHIEN MIN
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