USH736H - Process for making boron nitride using sodium cyanide and boron - Google Patents
Process for making boron nitride using sodium cyanide and boron Download PDFInfo
- Publication number
- USH736H USH736H US07/019,835 US1983587A USH736H US H736 H USH736 H US H736H US 1983587 A US1983587 A US 1983587A US H736 H USH736 H US H736H
- Authority
- US
- United States
- Prior art keywords
- boron
- boron nitride
- making
- sodium cyanide
- reaction
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
- 229910052582 BN Inorganic materials 0.000 title claims abstract description 23
- PZNSFCLAULLKQX-UHFFFAOYSA-N Boron nitride Chemical compound N#B PZNSFCLAULLKQX-UHFFFAOYSA-N 0.000 title claims abstract description 23
- 238000000034 method Methods 0.000 title claims abstract description 17
- KXZJHVJKXJLBKO-UHFFFAOYSA-N chembl1408157 Chemical compound N=1C2=CC=CC=C2C(C(=O)O)=CC=1C1=CC=C(O)C=C1 KXZJHVJKXJLBKO-UHFFFAOYSA-N 0.000 title claims abstract description 5
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 title description 4
- 229910052796 boron Inorganic materials 0.000 title description 4
- 238000006243 chemical reaction Methods 0.000 claims abstract description 23
- 229910000149 boron phosphate Inorganic materials 0.000 claims abstract description 13
- YZYDPPZYDIRSJT-UHFFFAOYSA-K boron phosphate Chemical compound [B+3].[O-]P([O-])([O-])=O YZYDPPZYDIRSJT-UHFFFAOYSA-K 0.000 claims abstract description 7
- 239000000203 mixture Substances 0.000 claims abstract description 6
- 238000010438 heat treatment Methods 0.000 claims abstract description 4
- 238000002156 mixing Methods 0.000 claims abstract description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 9
- 229910052757 nitrogen Inorganic materials 0.000 claims description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 4
- 239000006227 byproduct Substances 0.000 claims description 3
- 239000007858 starting material Substances 0.000 claims description 3
- 229910052786 argon Inorganic materials 0.000 claims description 2
- 239000007789 gas Substances 0.000 claims description 2
- 239000001307 helium Substances 0.000 claims description 2
- 229910052734 helium Inorganic materials 0.000 claims description 2
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 claims description 2
- 239000011261 inert gas Substances 0.000 claims description 2
- 150000001875 compounds Chemical class 0.000 abstract description 2
- 239000000843 powder Substances 0.000 abstract description 2
- 239000000047 product Substances 0.000 description 10
- 239000000376 reactant Substances 0.000 description 8
- XFXPMWWXUTWYJX-UHFFFAOYSA-N Cyanide Chemical compound N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 description 7
- MNWBNISUBARLIT-UHFFFAOYSA-N sodium cyanide Chemical compound [Na+].N#[C-] MNWBNISUBARLIT-UHFFFAOYSA-N 0.000 description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 5
- 239000007787 solid Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 239000010439 graphite Substances 0.000 description 3
- 229910002804 graphite Inorganic materials 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- VXEGSRKPIUDPQT-UHFFFAOYSA-N 4-[4-(4-methoxyphenyl)piperazin-1-yl]aniline Chemical compound C1=CC(OC)=CC=C1N1CCN(C=2C=CC(N)=CC=2)CC1 VXEGSRKPIUDPQT-UHFFFAOYSA-N 0.000 description 2
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 2
- 229910019142 PO4 Inorganic materials 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 150000001639 boron compounds Chemical class 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 229910052681 coesite Inorganic materials 0.000 description 2
- 229910052906 cristobalite Inorganic materials 0.000 description 2
- 150000002825 nitriles Chemical class 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 235000021317 phosphate Nutrition 0.000 description 2
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 239000011574 phosphorus Substances 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 239000005049 silicon tetrachloride Substances 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 229910052682 stishovite Inorganic materials 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 229910052905 tridymite Inorganic materials 0.000 description 2
- 229910015133 B2 O3 Inorganic materials 0.000 description 1
- 229910003887 H3 BO3 Inorganic materials 0.000 description 1
- 229910004748 Na2 B4 O7 Inorganic materials 0.000 description 1
- 239000004115 Sodium Silicate Substances 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 229910021538 borax Inorganic materials 0.000 description 1
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 1
- 239000004327 boric acid Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- -1 compound boron nitride Chemical class 0.000 description 1
- 239000012611 container material Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 238000010574 gas phase reaction Methods 0.000 description 1
- 229910021397 glassy carbon Inorganic materials 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- BHEPBYXIRTUNPN-UHFFFAOYSA-N hydridophosphorus(.) (triplet) Chemical compound [PH] BHEPBYXIRTUNPN-UHFFFAOYSA-N 0.000 description 1
- 238000009533 lab test Methods 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910001463 metal phosphate Inorganic materials 0.000 description 1
- 239000000615 nonconductor Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 235000019351 sodium silicates Nutrition 0.000 description 1
- 235000010339 sodium tetraborate Nutrition 0.000 description 1
- BSVBQGMMJUBVOD-UHFFFAOYSA-N trisodium borate Chemical compound [Na+].[Na+].[Na+].[O-]B([O-])[O-] BSVBQGMMJUBVOD-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B21/00—Nitrogen; Compounds thereof
- C01B21/06—Binary compounds of nitrogen with metals, with silicon, or with boron, or with carbon, i.e. nitrides; Compounds of nitrogen with more than one metal, silicon or boron
- C01B21/064—Binary compounds of nitrogen with metals, with silicon, or with boron, or with carbon, i.e. nitrides; Compounds of nitrogen with more than one metal, silicon or boron with boron
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/60—Optical properties, e.g. expressed in CIELAB-values
Definitions
- This invention relates to a process for making the compound boron nitride and was developed pursuant to a contract with the U.S. Department of Energy.
- Hexagonal Boron Nitride is used in many applications that require container material stable at high temperature or a high resistance electrical insulator. This material is also a very soft solid and has a tendency to flake and can be used as a solid lubricant similar to graphite.
- Oxide compounds of boron most frequently used are B 2 O 3 , H 3 BO 3 and Na 2 B 4 O 7 which are reacted directly with NaCN or in conjunction with a sodium acceptor such as SiO 2 .
- This process has the disadvantage of having a hydrated reactant, the oxygen containing boron compound, which must be dried in order to remove the water of hydration. Additionally, some of the boron is converted to sodium borate thereby lowering the boron nitride yield.
- a further object of this invention is to maximize the yield of boron nitride from the boron containing starting material.
- a final object of this invention is to provide a simple process for making boron nitride that is suitable for commercialization.
- boron nitride that consists of mixing NaCN and BPO 4 and heating the mixture to a temperature sufficient to cause the reactants to react.
- the preferred temperature is about 1,050° C.
- the product BN can be separated from the phosphorus-containing by-products by extraction of the phosphates with water. Excess reactants remaining will also be extracted in the water wash.
- the preferred temperature of the water wash is 25° C. or more.
- the chemical boron phosphate has little common usage in the chemical arts. In the past it has been used as a catalyst or catalyst support and in chemical research to make metal phosphates, but other useful applications of this chemical are not found in the literature.
- boron phosphate to make boron nitride is significant considering its otherwise lack of utility and the ease with which boron phosphate is made by simply mixing boric acid and phosphoric acid and heating the mixture to reaction. It can also be purchased commercially from Alfa Products (Danvers, MA, 01923), STREM (Newburyport, MA, 01950) and Atomergic Chemetals Corp. (Plainview, NY, 11801), among others.
- the reaction for making BN is very simple requiring only that the reactants be mixed together and heated to reaction temperature. Isolating the product is simple as well since the by-products are all soluble in water leaving the solid boron nitride product.
- the only reaction conditions that require care are the composition of the crucible and the reaction atmosphere.
- the crucible cannot be metal or quartz due to cyanide's tendency to attack these materials.
- vitreous carbon graphite, BN and perhaps high fired alumina are suitable materials for the reaction crucible.
- the inert atmosphere is provided by an inert gas such as argon, helium or diatomic gas such as nitrogen.
- the reaction cannot be performed in a vacuum, however, because the sodium cyanide will evaporate.
- the applicants did several studies to determine the optimum ratio of NaCN to BPO 4 . Whenever the cyanide and the boron phosphate are brought together and heated to reaction temperature, a reaction will take place; therefore, there is no minimum or maximum ratio of reactants required. However, the optimum ratio is one that will minimize the presence of free phosphorus and drive a maximum amount of the cyanide to form product, since both phosphorous and cyanide are dangerous elements that are best removed from the system. Additionally, expending all the cyanide will increase the yield relative to the cyanide reactant.
- Equations I, II, and III are representative of the reactions that take place under varying ratios of NaCN to BPO 4 . ##EQU1##
- boron nitride will be obtained from NaCN and BP04 when both are present in the reactor regardless of the ratio, the preferred ratio of NaCN/BPO 4 is one or greater and the optimum ratio is in the range from 1 to 1.2 since no or insignificant amounts of phosophorus are evolved when the reactants are present in these proportions. Higher ratio values of 1.71 to 2 leave a residue of carbon mixed with boron nitride resulting in grey cast to the final product.
- the product boron nitride appears to consist of irregularly shaped particles of one micrometer or less in the longest direction as observed in the scanning electron microscope.
- the BN product has significant commercial use and this reaction provides a very simple inexpensive process for making the powder and can be easily adapted to commercialization.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Ceramic Products (AREA)
Abstract
This a very simple process for making boron nitride by mixing sodium cyanide and boron phosphate and heating the mixture in an inert atmosphere until a reaction takes place. The product is a white powder of boron nitride that can be used in applications that require compounds that are stable at high temperatures and that exhibit high electrical resistance.
Description
This invention relates to a process for making the compound boron nitride and was developed pursuant to a contract with the U.S. Department of Energy.
Hexagonal Boron Nitride (BN) is used in many applications that require container material stable at high temperature or a high resistance electrical insulator. This material is also a very soft solid and has a tendency to flake and can be used as a solid lubricant similar to graphite.
Due to the significant industrial interest in BN, a very large number of reactions have been reported for its synthesis. Examples include a solid-gas phase reaction involving nitrogen or gaseous ammonia and silicon tetrachloride which has the disadvantages of being a very expensive reaction and requiring silicon tetrachloride which is difficult to make.
Another method involves the reaction of oxygen-containing boron compounds with cyanides. Such reactions take advantage of the strong reducing conditions created by the cyanides as well as their ability to provide nitrogen to the medium. Oxide compounds of boron most frequently used are B2 O3, H3 BO3 and Na2 B4 O7 which are reacted directly with NaCN or in conjunction with a sodium acceptor such as SiO2. This process has the disadvantage of having a hydrated reactant, the oxygen containing boron compound, which must be dried in order to remove the water of hydration. Additionally, some of the boron is converted to sodium borate thereby lowering the boron nitride yield. Also, if SiO2 is used as a sodium acceptor, it is difficult to purify the product since some sodium silicates are insoluble in water. Therefore, there is a need to provide a process for making boron nitride that is simple and efficient and inexpensive.
In view of the above described needs, it is an object of this invention to provide a process for making boron nitride without using a reactant that forms a hydrate, thus requiring rigorous drying prior to the reaction.
It is also an object of this invention to provide an inexpensive process for making boron nitride.
A further object of this invention is to maximize the yield of boron nitride from the boron containing starting material.
A final object of this invention is to provide a simple process for making boron nitride that is suitable for commercialization.
Upon further study of this specification and appended claims further objects and advantages of this invention will become apparent to those skilled in the arts.
These objects have been achieved by providing a process for making boron nitride that consists of mixing NaCN and BPO4 and heating the mixture to a temperature sufficient to cause the reactants to react. The preferred temperature is about 1,050° C. The product BN can be separated from the phosphorus-containing by-products by extraction of the phosphates with water. Excess reactants remaining will also be extracted in the water wash. The preferred temperature of the water wash is 25° C. or more.
The chemical boron phosphate has little common usage in the chemical arts. In the past it has been used as a catalyst or catalyst support and in chemical research to make metal phosphates, but other useful applications of this chemical are not found in the literature. Using boron phosphate to make boron nitride is significant considering its otherwise lack of utility and the ease with which boron phosphate is made by simply mixing boric acid and phosphoric acid and heating the mixture to reaction. It can also be purchased commercially from Alfa Products (Danvers, MA, 01923), STREM (Newburyport, MA, 01950) and Atomergic Chemetals Corp. (Plainview, NY, 11801), among others.
The reaction for making BN is very simple requiring only that the reactants be mixed together and heated to reaction temperature. Isolating the product is simple as well since the by-products are all soluble in water leaving the solid boron nitride product. The only reaction conditions that require care are the composition of the crucible and the reaction atmosphere.
The crucible cannot be metal or quartz due to cyanide's tendency to attack these materials. However, vitreous carbon graphite, BN and perhaps high fired alumina, are suitable materials for the reaction crucible.
It is also critical to conduct the reaction in an inert atmosphere because the cyanide will react with air. The inert atmosphere is provided by an inert gas such as argon, helium or diatomic gas such as nitrogen. The reaction cannot be performed in a vacuum, however, because the sodium cyanide will evaporate.
The applicants did several studies to determine the optimum ratio of NaCN to BPO4. Whenever the cyanide and the boron phosphate are brought together and heated to reaction temperature, a reaction will take place; therefore, there is no minimum or maximum ratio of reactants required. However, the optimum ratio is one that will minimize the presence of free phosphorus and drive a maximum amount of the cyanide to form product, since both phosphorous and cyanide are dangerous elements that are best removed from the system. Additionally, expending all the cyanide will increase the yield relative to the cyanide reactant.
Laboratory tests performed on the products of the reaction provided results that made it possible to define the stoichiometry of the reaction and select optimum parameters for the synthesis of boron nitride. Equations I, II, and III are representative of the reactions that take place under varying ratios of NaCN to BPO4. ##EQU1##
Although boron nitride will be obtained from NaCN and BP04 when both are present in the reactor regardless of the ratio, the preferred ratio of NaCN/BPO4 is one or greater and the optimum ratio is in the range from 1 to 1.2 since no or insignificant amounts of phosophorus are evolved when the reactants are present in these proportions. Higher ratio values of 1.71 to 2 leave a residue of carbon mixed with boron nitride resulting in grey cast to the final product.
Various ratios of NaCN and BPO4 in a combined weight of one to two grams were mixed by grinding and placed in crucibles, made preferably of graphite, that were tall to avoid expulsion of the mixture from the crucible during reaction and heated to a temperature of about 1,050° C. under flowing nitrogen for about twenty hours although reaction is complete within 3-5 hours at this temperature. The products were cooled and extracted with hot water to remove the soluble phosphates and unreacted starting materials and the solid residue was further washed with acetone and dried at 120° C. to a constant weight.
The product boron nitride appears to consist of irregularly shaped particles of one micrometer or less in the longest direction as observed in the scanning electron microscope.
The BN product has significant commercial use and this reaction provides a very simple inexpensive process for making the powder and can be easily adapted to commercialization.
Claims (6)
1. A process for making boron nitride comprising mixing sodium cyanide with boron phosphate and heating said mixture in a nonvacuum atmosphere of gas selected from the group nitrogen or an inert gas to a temperature and for a length of time suitable to cause reaction and subsequentialy extracting said by-products and unreacted starting material with water.
2. The process of claim 1 wherein said temperature is about 1,050° C. and said time is three hours or longer.
3. The process of claim 1 wherein said inert atmosphere is selected from the group argon and helium.
4. The process of claim 1 wherein the ratio of said sodium cyanide to said boron phosphate is 1 or greater.
5. The process of claim 4 wherein said ratio is from 1 to 1.2.
6. The process of claim 1 wherein said water is at a temperature 25° C. or more.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/019,835 USH736H (en) | 1987-02-27 | 1987-02-27 | Process for making boron nitride using sodium cyanide and boron |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/019,835 USH736H (en) | 1987-02-27 | 1987-02-27 | Process for making boron nitride using sodium cyanide and boron |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| USH736H true USH736H (en) | 1990-02-06 |
Family
ID=21795291
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US07/019,835 Abandoned USH736H (en) | 1987-02-27 | 1987-02-27 | Process for making boron nitride using sodium cyanide and boron |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | USH736H (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110577226A (en) * | 2019-10-18 | 2019-12-17 | 福州大学 | A kind of preparation method of boron nitride/boron phosphate sandwich type hollow sphere |
Citations (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1135232A (en) | 1913-02-03 | 1915-04-13 | Gen Electric | Process of making boron nitrid. |
| US1157271A (en) | 1913-02-03 | 1915-10-19 | Gen Electric | Stable boron nitrid and the process of making the same. |
| US1464292A (en) | 1921-12-08 | 1923-08-07 | Willis G Waldo | Process of producing boron nitride |
| GB742326A (en) | 1952-05-17 | 1955-12-21 | Carborundum Co | Improvements relating to the production of moulded shapes of boron nitride |
| US2834650A (en) | 1955-10-04 | 1958-05-13 | Union Carbide Corp | Production of boron nitride |
| US2839366A (en) | 1953-06-18 | 1958-06-17 | Nat Distillers Chem Corp | Process for the manufacture of boron nitride |
| US2865715A (en) | 1955-03-03 | 1958-12-23 | Nat Distillers Chem Corp | Manufacture of boron compounds |
| US2922699A (en) | 1957-12-11 | 1960-01-26 | Union Carbide Corp | Production of boron nitride |
| US2959469A (en) | 1957-08-08 | 1960-11-08 | American Potash & Chem Corp | Process for production of boron nitride |
| US2974013A (en) | 1957-08-13 | 1961-03-07 | Union Carbide Corp | Boron nitride production |
| US3208824A (en) | 1961-08-11 | 1965-09-28 | Kempten Elektroschmelz Gmbh | Process for the continuous production of boron nitride |
| US3216666A (en) | 1962-02-06 | 1965-11-09 | Morgardshammars Mek Verkst Sa | Supporting system for rotary drums and the like |
| US3241919A (en) | 1960-01-25 | 1966-03-22 | Du Pont | Process for the production of boron nitride |
| FR1513791A (en) | 1966-03-09 | 1968-02-16 | Lonza Werke Gmbh | Improvements to manufacturing processes for hexagonal boron nitride |
| US3692474A (en) | 1969-11-26 | 1972-09-19 | United States Borax Chem | Preparation of metal nitrides |
| USRE27608E (en) | 1965-04-13 | 1973-04-03 | Production of boron nitride |
-
1987
- 1987-02-27 US US07/019,835 patent/USH736H/en not_active Abandoned
Patent Citations (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1135232A (en) | 1913-02-03 | 1915-04-13 | Gen Electric | Process of making boron nitrid. |
| US1157271A (en) | 1913-02-03 | 1915-10-19 | Gen Electric | Stable boron nitrid and the process of making the same. |
| US1464292A (en) | 1921-12-08 | 1923-08-07 | Willis G Waldo | Process of producing boron nitride |
| GB742326A (en) | 1952-05-17 | 1955-12-21 | Carborundum Co | Improvements relating to the production of moulded shapes of boron nitride |
| US2839366A (en) | 1953-06-18 | 1958-06-17 | Nat Distillers Chem Corp | Process for the manufacture of boron nitride |
| US2865715A (en) | 1955-03-03 | 1958-12-23 | Nat Distillers Chem Corp | Manufacture of boron compounds |
| US2834650A (en) | 1955-10-04 | 1958-05-13 | Union Carbide Corp | Production of boron nitride |
| US2959469A (en) | 1957-08-08 | 1960-11-08 | American Potash & Chem Corp | Process for production of boron nitride |
| US2974013A (en) | 1957-08-13 | 1961-03-07 | Union Carbide Corp | Boron nitride production |
| US2922699A (en) | 1957-12-11 | 1960-01-26 | Union Carbide Corp | Production of boron nitride |
| US3241919A (en) | 1960-01-25 | 1966-03-22 | Du Pont | Process for the production of boron nitride |
| US3208824A (en) | 1961-08-11 | 1965-09-28 | Kempten Elektroschmelz Gmbh | Process for the continuous production of boron nitride |
| US3216666A (en) | 1962-02-06 | 1965-11-09 | Morgardshammars Mek Verkst Sa | Supporting system for rotary drums and the like |
| USRE27608E (en) | 1965-04-13 | 1973-04-03 | Production of boron nitride | |
| FR1513791A (en) | 1966-03-09 | 1968-02-16 | Lonza Werke Gmbh | Improvements to manufacturing processes for hexagonal boron nitride |
| US3415625A (en) | 1966-03-09 | 1968-12-10 | Lonza Werke Gmbh | Preparation of hexagonal boron nitride |
| US3692474A (en) | 1969-11-26 | 1972-09-19 | United States Borax Chem | Preparation of metal nitrides |
Non-Patent Citations (4)
| Title |
|---|
| E. Tiede and H. Tomaschek, Z. Anorg, u. Allg. Chemie. 4Z (1925) pp. 111-122. |
| John H. Perry editor, Chemical Engineers'Handbook McGraw-Hill Book Company,nc., New York, 1950 p. 115. |
| Tiede and Buscher, Ber. 53, 2206 (1920). |
| Vasovic and Stoiakovic, J. Am. Ceram. Soc., C-23 (1987). |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110577226A (en) * | 2019-10-18 | 2019-12-17 | 福州大学 | A kind of preparation method of boron nitride/boron phosphate sandwich type hollow sphere |
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