The present invention relates to methods of making and purifying nanodiamonds.
Nanoscale diamond particles (with a size below 1 μm), generally known as nanodiamonds (NDs), have several outstanding material qualities, offering a wide range of potential for basic science and industrial applications. In particular, a number of optically addressable impurity defects, such as nitrogen-vacancy (NV) centers residing in the diamond lattice, have been deployed for next-generation quantum technologies due to their unique spin properties.
Currently, there are mainly two methods for the large-scale fabrication of NDs: “bottom-up” detonation NDs and “top-down” milling of bulk high-pressure high-temperature (HPHT) diamond. It is well known that the raw ND powders (i.e., detonation or HPHT) contain a considerable amount of unwanted impurities [e.g., ultrasmall (<10 nm)-sized NDs, disordered carbons, metal, and metal oxides], which are naturally introduced during synthesis and processing. However, previous reports have demonstrated that the non-diamond phases present at the surface of NDs are detrimental to the properties of embedded quantum defects (e.g., NV centers). Therefore, the removal of these impurities becomes a critical step before the ultimate applications of the NDs. For example, the fluorescence lifetime and spin-coherence time (T 2) of NV centers in NDs could be significantly improved by cleaning the surface quenchers (e.g., fluorescent graphitic carbon). This has proven to be quite beneficial for potential applications in photonics, quantum sensing, and imaging. Moreover, a sufficiently clean and uniform surface of NDs, desired for favorable nanobiointeractions, is a prerequisite for potential biomedical applications in drug delivery, biolabeling, and biosensing.
At present, the most commonly used method of removing non-diamond carbons involves the surface oxidization of raw NDs in the presence of air at 400-600° C. for several hours. The resultant oxygenated functional groups on the surface of the NDs have been shown to stabilize the NV charge states, increase the colloidal stability in aqueous solution, and prolong the NV spin coherence times. However, the conventional air oxidation approach is to put NDs powder alone in furnace for calcination, and a considerable amount of impurities are associated with such a process. The impurities are mainly amorphous carbon nanoparticles with a size range in a few tens of nm, which are difficult to remove. The impurities are mainly amorphous carbon nanoparticles due to calcination of crystalline NDs in air, with a size range in a few tens of nm. Those nanoparticles are impossible to remove by separation methods such as centrifugation at low speed (e.g., 1,000 rcf), and might be gradually removed by multiple rounds of high-speed centrifugation (e.g., 10,000 rcf). The additional centrifugation steps not only lead to more waste of the NDs sample, but also facilitate the severe negative issue of ND agglomeration.
Alternatively, wet chemical treatments (e.g., HNO3/H2SO4/HClO4) have also been adopted to remove both non-diamond carbons and metallic impurities in NDs. However, the use of these liquid phase protocols is costly, and the employment of hazardous chemicals carries environmental risks. Despite the considerable effort devoted to overcoming these challenges, it is still difficult to obtain NDs with a well-defined surface, especially when examined at the individual particle level.
In accordance with the well-established procedure for the liquid etching of bulk diamonds, the NDs have already been intensively etched with molten potassium nitrate (KNO3), that is, heated at 500-600° C. for several minutes. This intensive etching treatment has been shown to produce NDs with a much cleaner surface and more rounded morphology than those treated with gas oxidation methods. The rounded NDs also exhibit improved optical properties and excellent colloidal stability. However, this molten-salt process involves complicated procedures, requires professional protective equipment, and these disadvantages have so far prevented its general adoption.
Thus, there is a desire for a more convenient method that enables scale-up manufacturing of clean NDs.
It is the objective of the present invention to provide a highly efficient purification method for NDs.
The following presents a simplified summary of the invention in order to provide a basic understanding of some aspects of the invention. This summary is not an extensive overview of the invention. It is intended to neither identify key or critical elements of the invention nor delineate the scope of the invention. Rather, the sole purpose of this summary is to present some concepts of the invention in a simplified form as a prelude to the more detailed description that is presented hereinafter.
As described herein, a highly efficient purification method for NDs (with a size below 1 μm) by salt-assisted air oxidation (SAAO) is explained. With the methods described herein, the pure NDs (without any detectable amorphous carbon nanoparticles) can be produced by one-step processing (e.g., centrifugation at 1,000 rcf for 5 minutes) after air oxidation, without the need for any further centrifugation acts. Furthermore, the developed SAAO method enables facile scale-up manufacturing of clean NDs, with a rounded shape transformed from the original shard-like shape, which is impossible to achieve using any existing purification method.
Disclosed herein are methods of purifying NDs comprising mixing NDs with at least one salt to form a mixture; heating the mixture at a temperature from 200° C. to 1,000° C. for a time from 10 minutes to 10 hours; and combining a liquid with the heated mixture and centrifuging at a speed of 30 rcf to 25,000 rcf for a time from 10 seconds to 60 minutes to provide purified NDs.
Also disclosed are methods of making essentially pure NDs comprising mixing NDs with at least one salt to form a mixture; heating the mixture at a temperature from 200° C. to 1,000° C. for a time from 10 minutes to 10 hours; and combining a liquid with the heated mixture and centrifuging at a speed of 30 rcf to 25,000 rcf for a time from 10 seconds to 60 minutes to provide essentially pure NDs with less than 0.01% by weight impurities.
Purification of NDs is the primary step to realize most of their quantum applications, e.g., surface oxidization (i.e., aerobic, or anaerobic triacid oxidation) methods have been commonly used for removing the surface-covering non-diamond structures (e.g., sp2 carbon, sp2 clusters). The conventional method for this is air oxidation treatment of NDs at 400-600° C. (to put NDs power alone in a furnace for calcination). However, there are a considerable amount of impurities associated with such a process. The impurities are mainly amorphous carbon nanoparticles due to calcination of crystalline NDs in air, with a size range in a few tens of nm. Those nanoparticles are impossible to remove by separation methods such as centrifugation at low speed (e.g., 1,000 rcf), and might be gradually removed by multiple rounds of high-speed centrifugation (e.g., 10,000 rcf). The additional centrifugation steps not only lead to more waste of the NDs sample, but also facilitate the severe negative issue of ND agglomeration. As described herein, a highly efficient purification method for NDs by SAAO is explained. With the novel systems and methods described herein, pure NDs (without any (or barely any) detectable amorphous carbon nanoparticles) can be produced by one-step processing (centrifugation at 1,000 rcf for 5 minutes) after air oxidation, no need for any further centrifugation steps.
The following description and the drawings set forth in detail certain illustrative aspects and implementations of the invention. These are indicative, however, of but a few of the various ways in which the principles of the invention may be employed. Other objects, advantages and novel features of the invention will become apparent from the following detailed description of the invention when considered in conjunction with the drawings.
In order to explain the embodiments of the present invention or the technical solutions in the prior art more clearly, drawings required for the description of the embodiments of the present invention will be briefly described below. Obviously, the drawings in the following description are only some embodiments of the present invention.
In general, the method of purifying NDs according to the invention comprises the following steps:
NDs are initially mixed with a suitable amount of salt before heating. In one embodiment, a unit weight of NDs is mixed with 0.1 to 100 times an amount of a salt. In another embodiment, a unit weight of ND is mixed with 0.5 to 50 times an amount of a salt. In yet another embodiment, a unit weight of ND is mixed with 1 to 10 times an amount of a salt.
The salt is any salt that facilitates surface oxidation of NDs. A salt is an ionic compound having an anion and cation. General examples of salts that can be employed include one or more of alkaline earth metal halogens, sulfates, persulfates, nitrates, phosphates, and the like; alkali metal halogens, sulfates, persulfates, nitrates, phosphates, and the like; transition metal halogens, sulfates, persulfates, nitrates, phosphates, and the like; ammonium halogens, sulfates, persulfates, nitrates, phosphates, and the like; quaternary alkyl ammonium halogens, sulfates, persulfates, nitrates, phosphates, and the like. Specific examples of salts that can be employed include one or more of sodium chloride, magnesium chloride, potassium chloride, calcium chloride, ammonium chloride, sodium sulfate, magnesium sulfate, potassium sulfate, calcium sulfate, ammonium sulfate, and the like.
The ND/salt mixture is then heated at a suitable temperature for a suitable period of time to facilitate surface oxidation of NDs. In one embodiment, the ND/salt mixture is heated at a temperature from 200° C. to 1,000° C. for a time from 10 minutes to 10 hours. In another embodiment, the ND/salt mixture is heated at a temperature from 300° C. to 800° C. for a time from 30 minutes to 8 hours. In yet another embodiment, the ND/salt mixture is heated at a temperature from 400° C. to 600° C. for a time from 1 hour to 5 hours.
The oxidized mixture is then added to a liquid and subjected to machine separation, such as centrifugation at a low as possible speed for a suitable period of time. Examples of the liquid include water, deionized water, or an organic liquid such as an alcohol. The machine separation separates the salt from the NDs, enabling the collection of the purified NDs. The low speed is employed to minimize/reduce damage to and/or minimize/reduce agglomeration of the NDs. In one embodiment, the oxidized mixture is centrifuged at a speed of 30 rcf to 25,000 rcf for a time from 10 seconds to 60 minutes. In another embodiment, the oxidized mixture is centrifuged at a speed of 100 rcf to 10,000 rcf for a time from 30 seconds to 30 minutes. In yet another embodiment, the oxidized mixture is centrifuged at a speed of 500 rcf to 5,000 rcf for a time from 1 minute to 15 minutes.
Purified NDs are collected. The NDs are characterized in that very little to no detectable impurities are present and/or the size distribution of the purified NDs is relatively narrow, especially compared to similar oxidation-centrifugation process when a salt is not used. The NDs are essentially pure; meaning the collected NDs are at least 99.9% by weight NDs, with less than 0.1% by weight impurities such as amorphous carbon nanoparticles. In another embodiment, the collected NDs are at least 99.95% by weight NDs, with less than 0.05% by weight impurities such as amorphous carbon nanoparticles. In yet another embodiment, the collected NDs are at least 99.99% by weight NDs, with less than 0.01% by weight impurities such as amorphous carbon nanoparticles.
According to the method of the present invention, the purified NDs are not agglomerated.
In another aspect, the present invention provides a method of making essentially pure NDs which comprises the following steps:
In the method of making essentially pure NDs according to the present invention, wherein the raw NDs includes impurities comprising ultra-small (<10 nm) sized NDs, amorphous carbon nanoparticles, metal, and metal oxides.
NDs are initially mixed with a suitable amount salt before heating. In one embodiment, a unit weight of NDs is mixed with 0.5 to 50 times an amount of a salt. In yet another embodiment, a unit weight of ND is mixed with 1 to 10 times an amount of a salt.
The salt is any salt that facilitates surface oxidation of NDs. A salt is an ionic compound having an anion and cation. General examples of salts that can be employed include one or more of alkaline earth metal halogens, sulfates, persulfates, nitrates, phosphates, and the like; alkali metal halogens, sulfates, persulfates, nitrates, phosphates, and the like; transition metal halogens, sulfates, persulfates, nitrates, phosphates, and the like; ammonium halogens, sulfates, persulfates, nitrates, phosphates, and the like; quaternary alkyl ammonium halogens, sulfates, persulfates, nitrates, phosphates, and the like. Specific examples of salts that can be employed include one or more of sodium chloride, magnesium chloride, potassium chloride, calcium chloride, ammonium chloride, sodium sulfate, magnesium sulfate, potassium sulfate, calcium sulfate, ammonium sulfate, and the like.
The ND/salt mixture is then heated at a suitable temperature for a suitable period of time to facilitate surface oxidation of NDs. In one embodiment, the ND/salt mixture is heated at a temperature from 300° C. to 800° C. for a time from 30 minutes to 8 hours. In another embodiment, the ND/salt mixture is heated at a temperature from 400° C. to 600° C. for a time from 1 hour to 5 hours.
The oxidized mixture is then added to a liquid and subjected to machine separation, such as centrifugation at a low as possible speed for a suitable period of time. Examples of the liquid include water, deionized water, or an organic liquid such as an alcohol. The machine separation separates the salt from the NDs, enabling collection of the purified NDs. The low speed is employed to minimize/reduce damage to and/or minimize/reduce agglomeration of the NDs. In one embodiment, the oxidized mixture is centrifuged at a speed of 100 rcf to 10,000 rcf for a time from 30 seconds to 30 minutes. In another embodiment, the oxidized mixture is centrifuged at a speed of 500 rcf to 5,000 rcf for a time from 1 minute to 15 minutes.
The liquid is selected from the group consisting of water, deionized water, an organic liquid, such as methanol, ethanol, and combination thereof.
The resulting essentially pure NDs are collected. The NDs are characterized in that very little to no detectable impurities are present and/or the size distribution of the purified NDs is relatively narrow, especially compared to similar oxidation-centrifugation process when a salt is not used. The NDs are essentially pure meaning that the collected NDs are at least 99.9% by weight NDs, with less than 0.1% by weight impurities such as amorphous carbon nanoparticles. In another embodiment, the collected NDs are at least 99.95% by weight NDs, with less than 0.05% by weight impurities such as amorphous carbon nanoparticles. In yet another embodiment, the collected NDs are at least 99.99% by weight NDs, with less than 0.01% by weight impurities such as amorphous carbon nanoparticles.
Desirably, the essentially pure NDs made by the method according to the present invention are not agglomerated.
The present invention will be further illustrated with reference to the detailed examples below. It is necessary to state that, the embodiments below are only for illustration, but not for limitation of the present invention. Various alterations that are made by a person skilled in the art in accordance with teaching from the present invention should be within the scope claimed by the claims of the present invention.
Salt-Assisted Air Oxidation Method (SAAO Method)
NDs with a mean particle size of 200 nm (HPHT, PolyQolor, China) were used as the starting material.
(1) 0.5 g of NDs were mixed with 2.5 g of sodium chloride (NaCl, 99.5%, Sigma-Aldrich), and they were heated at 500° C. for 5 hours in air.
(2) 600 mg of the resultant sample was dispersed in 1 mL of deionized water and sonicated for 1 hour, and the NDs were then purified with deionized water 3 times by centrifugation (first: 1,000 rcf, 5 minutes; second: 3,000 rcf, 5 minutes; third: 8,000 rcf, 10 minutes).
(3) The purified NDs were redispersed in deionized water and sonicated for 10 minutes to obtain well-dispersed ND suspension for further characterizations.
For comparison, conventional air oxidation of NDs was performed in parallel to Example 1, i.e., no NaCl added in the starting material.
(1) 0.5 g of NDs were heated at 500° C. for 5 hours in air.
(2) 100 mg of the resultant sample was dispersed in 1 mL of deionized water and sonicated for 1 h, and the NDs were then purified with deionized water 3 times by centrifugation (11,000 rcf, 10 minutes).
(3) The purified NDs were redispersed in 1 mL of deionized water and sonicated for 10 minutes to obtain well-dispersed ND suspension for further characterizations.
Characterizations
Comparison of NDs of Example 1 and Comparative Example 1
(I) Unremoved Impurities Associated with Conventional Air Oxidation
To evaluate the performance of the conventional air oxidation approach (
Surprisingly, there seemed to be some newly generated portions (<nm) after the conventional air oxidation treatment, as indicated by the significantly broadened DLS spectrum of the resultant NDs powder directly dispersed in deionized water (
(II) Clean and Rounded NDs by the SAAO Method
The failure to remove the adsorbed impurities on the surface of NDs was due partly to the close packing of ND powder, and partly to deficiencies (e.g., incomplete or spontaneous oxidation) in the oxidation process. To overcome this, the so-called SAAO method, i.e., mixing NDs with salt crystals (i.e., NaCl or KCl) before the thermal treatment was proposed. In a typical experiment, the raw ND powder was mixed well with NaCl crystals with a mass ratio of 1:5, and the mixture was then routinely processed (heated at 500° C. in a furnace for 5 hours in air), as depicted in
To further evaluate the performance of this novel method, the detailed morphology features of individual NDs was carefully characterized using a TEM-AFM correlated microscopy imaging technique (
(III) Crystallinity and Surface Chemistry Characterizations of NDs
The XRD results (
(IV) The Newly Generated “Impurities” During Conventional Oxidation
As indicated from the abovementioned results (
On the other hand, a time-dependent oxidation study (
(V) The Mechanism of the SAAO Method
To investigate the underlying mechanisms of the developed SAAO method, the mixtures of NDs and NaCl (after oxidation) were firstly checked to see if the cleanliness of NDs on salt particles changed directly without any further cleaning processes (e.g., washing and centrifugation). As shown in
To verify this, an air oxidation experiment (
The above results indicate that the NaCl might also be involved in the oxidation process of NDs, not just acting like spacers. Inspired by the well-known fact that the chloride salts (e.g., NaCl and KCl) could extensively corrode metals or alloys at the temperature of 400-700° C. due to the generated highly corrosive gases, therefore, the “etching atmosphere” generated by NaCl at high temperature (
The Cleaning Process of the SAAO Methods
NDs with a mean particle size of 200 nm were used as starting material.
(1) 0.5 g of NDs were mixed with 2.5 g of NaCl (99.5%, Sigma-Aldrich), and they were heated at 500° C. for 2 hours in air.
(2) 600 mg of the resultant sample was dispersed in 1 mL of deionized water and sonicated for 1 hour, and the NDs were then purified with deionized water 1 time by centrifugation (1,000 rcf, 5 minutes).
(3) The purified NDs were redispersed in deionized water and sonicated for 10 minutes to obtain well-dispersed ND suspension for further characterizations.
For comparison, conventional air oxidation of NDs was performed in parallel to Example 2, i.e., no NaCl added in the starting material.
(1) 0.5 g of NDs were heated at 500° C. for 2 hours in air.
(2) 100 mg of the resultant sample was dispersed in 1 mL of deionized water and sonicated for 1 h, and the NDs were then purified with deionized water 1 time by centrifugation (1,000 rcf, 10 minutes).
(3) The purified NDs were redispersed in 1 mL of deionized water and sonicated for 10 minutes to obtain well-dispersed ND suspension for further characterizations.
Characterizations
The procedures of the SAAO of NDs in Example 2 and conventional (no salt added) air oxidation of NDs in Comparative Example 2 are shown in
As can be seen from
From the DLS measurement of
The above examples demonstrate the cleaning process of the SAAO method is much easier than that of the conventional method, i.e., pure NDs (without any detectable impurity nanoparticles) can be produced by one-step processing (centrifugation at 1,000 rcf for 5 minutes) after air oxidation, no need for any further centrifugation steps.
The Suitable SAAO Conditions for 200 nm NDs
NDs with a mean particle size of 200 nm were used as starting material.
(1) 0.5 g of NDs were mixed with 2.5 g of NaCl (99.5%, Sigma-Aldrich), and they were heated at 400° C. for 2 hours in air.
(2) 0.5 g of NDs were mixed with 2.5 g of NaCl (99.5%, Sigma-Aldrich), and they were heated at 500° C. for 1 hour in air.
(3) 0.5 g of NDs were mixed with 2.5 g of NaCl (99.5%, Sigma-Aldrich), and they were heated at 500° C. for 2 hours in air.
(4) 0.5 g of NDs were mixed with 2.5 g of NaCl (99.5%, Sigma-Aldrich), and they were heated at 500° C. for 10 hours in air.
(5) 0.5 g of NDs were mixed with 2.5 g of NaCl (99.5%, Sigma-Aldrich), and they were heated at 500° C. for 20 hours in air.
(6) 0.5 g of NDs were mixed with 2.5 g of NaCl (99.5%, Sigma-Aldrich), and they were heated at 600° C. for 2 hours in air.
(7) 600 mg of the above resultant samples were dispersed in 1 mL of deionized water and sonicated for 1 hour, respectively. And the NDs were then purified with deionized water 3 times by centrifugation (first: 1,000 rcf, 5 minutes; second: 3,000 rcf, 5 minutes; third: 8,000 rcf, 10 minutes).
(8) The purified NDs were redispersed in deionized water and sonicated for 10 minutes to obtain well-dispersed ND suspensions for further characterization.
For comparison, conventional air oxidation of NDs was performed in parallel to Example 3, i.e., no NaCl added in the starting material.
(1) 0.5 g of NDs were heated at 400° C. for 2 hours in air.
(2) 0.5 g of NDs were heated at 500° C. for 1 hour in air.
(3) 0.5 g of NDs were heated at 500° C. for 2 hours in air.
(4) 0.5 g of NDs were heated at 500° C. for 10 hours in air.
(5) 0.5 g of NDs were heated at 500° C. for 20 hours in air.
(6) 0.5 g of NDs were heated at 600° C. for 2 hours in air.
(7) 100 mg of the above resultant samples were dispersed in 1 mL of DI water and sonicated for 1 hour, respectively. And the NDs were then purified with deionized water 3 times by centrifugation (11,000 rcf, 10 minutes).
(8) The purified NDs were redispersed in 1 mL of deionized water and sonicated for 10 minutes to obtain well-dispersed ND suspensions for further characterizations.
Characterizations
As depicted in
The Universality of the SAAO Method (KCl-assisted Air Oxidation of 50 nm NDs)
NDs with a mean particle size of 50 nm (HPHT, PolyQolor, China) were used as starting material.
(1) 0.5 g of NDs were mixed with 2.5 g of potassium chloride (KCl, 99.5%, Sigma-Aldrich), and they were heated at 500° C. for 2 hours in air.
(2) 600 mg of the resultant sample was dispersed in 1 mL of deionized water and sonicated for 1 hour, and the NDs were then purified with deionized water 3 times by centrifugation (first: 1,000 rcf, 5 minutes; second: 3,000 rcf, 5 minutes; third: 8,000 rcf, 10 minutes).
(3) The purified NDs were redispersed in deionized water and sonicated for 10 minutes to obtain well-dispersed ND suspension for further characterizations.
Characterizations
In summary, a simple, reliable and reproducible purification method, namely the salt-assisted air oxidation (SAAO) treatment was developed, which requires only one additional pre-step, i.e., mixing NDs with a proper amount of salt crystals (e.g., sodium chloride) prior to conventional oxidation. The developed method enables scale-up manufacturing of clean NDs, with a rounded shape transformed from the original shard-like shape. The impurity particles adsorbed on NDs were found to be etched by “etching atmosphere” introduced by NaCl at high temperatures. These findings will significantly enhance the scope of these little gemstones in diverse scientific and industrial fields, particularly in demanding areas such as biomedical and quantum sensing requiring stable and sound surface functionalities.
Unless otherwise indicated in the examples and elsewhere in the specification and claims, all parts and percentages are by weight, all temperatures are in degrees Centigrade, and pressure is at or near atmospheric pressure.
With respect to any figure or numerical range for a given characteristic, a figure or a parameter from one range may be combined with another figure or a parameter from a different range for the same characteristic to generate a numerical range.
Other than in the operating examples, or where otherwise indicated, all numbers, values and/or expressions referring to quantities of ingredients, reaction conditions, etc., used in the specification and claims are to be understood as modified in all instances by the term “about”.
While the invention is explained in relation to certain embodiments, it is to be understood that various modifications thereof will become apparent to those skilled in the art upon reading the specification. Therefore, it is to be understood that the invention disclosed herein is intended to cover such modifications as fall within the scope of the appended claims.
Filing Document | Filing Date | Country | Kind |
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PCT/CN2021/125267 | 10/21/2021 | WO |
Number | Date | Country | |
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63109956 | Nov 2020 | US |