KR100359643B1 - A manufacturing process of ultra-granule tungsten carbide dust by soppy system mixing - Google Patents
A manufacturing process of ultra-granule tungsten carbide dust by soppy system mixing Download PDFInfo
- Publication number
- KR100359643B1 KR100359643B1 KR1020000055365A KR20000055365A KR100359643B1 KR 100359643 B1 KR100359643 B1 KR 100359643B1 KR 1020000055365 A KR1020000055365 A KR 1020000055365A KR 20000055365 A KR20000055365 A KR 20000055365A KR 100359643 B1 KR100359643 B1 KR 100359643B1
- Authority
- KR
- South Korea
- Prior art keywords
- tungsten carbide
- mixing
- raw material
- solution
- tungstic acid
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/90—Carbides
- C01B32/914—Carbides of single elements
- C01B32/949—Tungsten or molybdenum carbides
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/60—Particles characterised by their size
- C01P2004/62—Submicrometer sized, i.e. from 0.1-1 micrometer
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Carbon And Carbon Compounds (AREA)
Abstract
본 발명은 습식혼합 방법에 의해 초미립 탄화텅스텐 분말을 제조하는 방법에 관한 것으로, 원료합성 과정이 습식으로 진행됨에 착안하여 원료합성 후 습식상태에서 바로 부원료와 혼합하여 건조함으로써 Milling 공정없이 균일도를 높이고 건조 후에도 성형공정을 생략할 수 있도록 함을 목적으로 하는 것이다.The present invention relates to a method for producing ultra-fine tungsten carbide powder by a wet mixing method, focusing on the raw material synthesis process in a wet manner, and after mixing the raw material in a wet state immediately after synthesis of the raw material to increase the uniformity without milling process It is an object to make it possible to omit the molding step even after drying.
그 방법으로는 미립 WC분말을 제조하기 위한 원료로써, 분말상태의 텅스텐화합물(CaWO4, APT-Ammonium Para Tungstate) 혹은 함중석용액(Na2WO4, (NH)4WO4용액 등)을 1.5∼2.0당량의 무기산 용액에 가하는 방법으로 입자를 성장시켜, Colloid화가 되는 것을 방지하여 텅스텐산(H2WO4, Tungstic Acid)을 제조하는 공정과,As a raw material for the production of fine WC powders, powdered tungsten compounds (CaWO 4 , APT-Ammonium Para Tungstate) or heavy stone solutions (Na 2 WO 4 , (NH) 4 WO 4 solution, etc.) 1.5 To grow tungstic acid (H 2 WO 4 , Tungstic Acid) by growing the particles by adding them to a solution of -2.0 equivalents to prevent colloidation;
상기 제조된 텅스텐산 Slurry에 탄소를 첨가하여 습식혼합하는 공정과,Wet mixing by adding carbon to the prepared tungstic acid slurry;
상기 혼합물을 건조하여 덩어리 상태 그대로 1.2차 반응시키는 공정으로 이루어지는 것을 특징으로 하는 것이다.It is characterized in that it comprises a step of drying the mixture to react 1.2 times as it is in a lump.
본 발명에 의하면 원료 합성 후 습식상태에서 바로 부원료와 혼합하여 건조하므로 기존 건식 혼합시 필수 공정인 Milling 및 성형공정이 없이 탄화 텅스텐분말을 제조할 수 있어서 종래보다 경제적으로 처리할 수 있게 되는 효과가 있다.According to the present invention, it is possible to manufacture tungsten carbide powder without milling and molding process, which is an essential process for conventional dry mixing, since it is mixed with the subsidiary material in a wet state immediately after synthesis of raw materials, thereby making it economically effective. .
Description
본 발명은 습식혼합방법에 의해 초미립 탄화텅스텐 분말을 제조하는 방법에 관한 것이다.The present invention relates to a method for producing ultrafine tungsten carbide powder by a wet mixing method.
기존의 제조방법에 의하면 원료분말과 부원료분말을 혼합하는 건식혼합방법이므로 균일도를 높이기 위하여 장시간 밀링(MILLING)이 필요하며 혼합 후에도 분말의 비산을 막기 위하여 성형(Pellet화 하기 위함)공정이 추가되어야 하는 폐단이 있었다.According to the existing manufacturing method, it is a dry mixing method of mixing the raw powder and the sub-raw powder. Therefore, milling is required for a long time to increase the uniformity, and a molding (to pelletize) process must be added to prevent the powder from scattering after mixing. There was a dissolution.
본 발명은 이러한 종래의 단점을 보완하기 위하여 원료합성(H2WO4) 과정이 습식으로 진행됨에 착안하여 원료합성 후 습식상태에서 바로 부원료와 혼합하여 건조함으로써 Milling 공정없이 균일도를 높이고 건조 후에도 성형공정을 생략할 수 있도록 함을 목적으로 하는 것이다.The present invention focuses on the raw material synthesis (H 2 WO 4 ) process in order to make up for the disadvantages of the prior art by mixing with the raw material immediately in the wet state after the synthesis of raw materials to increase the uniformity without milling process and molding process after drying The purpose is to be able to omit.
본 발명의 구체적인 방법을 살펴보면 다음과 같다.Looking at the specific method of the present invention.
미립 WC분말을 제조하기 위한 원료로써, 분말상태의 텅스텐화합물(CaWO4, APT-Ammonium Para Tungstate) 혹은 함중석용액(Na2WO4, (NH)4WO4용액 등)과 무기산 1.5∼2.0당량을 반응시킨 후 입자를 결정화시켜 Colloid화가 되는 것을 방지하여 제조한 텅스텐산(H2WO4, Tungstic Acid) Slurry를 사용한다.As a raw material for preparing fine WC powders, 1.5 to 2.0 equivalents of tungsten compounds in powder form (CaWO 4 , APT-Ammonium Para Tungstate) or a solution containing sodium stones (Na 2 WO 4 , (NH) 4 WO 4 solution, etc.) and inorganic acids After reacting, tungstic acid (H 2 WO 4 , Tungstic Acid) slurry prepared by crystallizing particles to prevent colloidation is used.
적정량의 시약(무기산)을 반응성이 가장 좋도록 활성화시킨 다음, 사용원료(함중석 물질)를 투입해 가면서 결정화를 시키기 때문에 기존방법 대비 적은 량(2당량 이하)의 시약으로 높은 수율의 텅스텐산을 합성할 수 있다(표 1 참조).Since the appropriate amount of reagent (inorganic acid) is activated to have the best reactivity, the crystallization is carried out by adding the used raw material (heavy stone material). Can be synthesized (see Table 1).
이와 같은 방법으로 제조된 텅스텐산 침전물을 Decantation 방법으로 4∼6차례 완전히 세척하여 Slurry 상태로 제조한다. 이 중 일정 소량을 채취하여 건조하는 방법으로 Slurry 중 WO3의 함량을 측정한다. 측정된 WO3함량에 대해 2.5∼4.5당량의 탄소를 첨가하여 증류수 1:0.3∼1.5 부피비를 첨가한 다음, Ball Mill Jar에 Ball을 넣고 혼합한 후, 100∼200℃에서 건조하여 덩어리(Ingot) 상태로 만든다.Tungstic acid precipitate prepared in this manner is washed 4 to 6 times by Decantation method to prepare a slurry state. Among them, a small amount is taken and dried to measure the content of WO 3 in the slurry. 2.5 to 4.5 equivalents of carbon was added to the measured WO 3 content to add 1: 0.3 to 1.5 volume ratio of distilled water. Then, Ball was added to the Ball Mill Jar, mixed, and dried at 100 to 200 ° C. to ingot. Make it state.
이 덩어리 상태 그대로 진공분위기 중 900∼1200℃에서 1차 반응시킨 후, 연속해서 수소분위기중 1200∼1600℃에서 반응시켜 조대한 입자가 없는 평균 0.2∼0.5㎛크기의 미립 WC분말을 제조할 수 있다는 것이다.After the first reaction at 900-1200 ° C. in a vacuum atmosphere as it is in the form of agglomerates, the reaction can be continued at 1200-1600 ° C. in a hydrogen atmosphere to produce an average 0.2-0.5 μm fine WC powder without coarse particles. will be.
실시예 1Example 1
① APT 혹은 CaWO4분말의 WO3에 대한 염산 반응당량의 약 1.5∼2.0당량의 용액을 순수를 첨가하여 적정농도로 희석한다.① A solution of about 1.5 to 2.0 equivalents of hydrochloric acid reaction equivalent to WO 3 of APT or CaWO 4 powder is diluted to the appropriate concentration by adding pure water.
② 0.2∼0.3N 농도의 HNO3용액을 ①항의 용액과 동일 분량으로 준비하여 70∼80℃로 데운다.② Prepare HNO 3 solution with 0.2 ~ 0.3N concentration in the same amount as the solution in ① and warm it to 70 ~ 80 ℃.
③ ①항의 희석액을 잘 혼합하면서 준비된 APT 혹은 CaWO4분말을 30∼40 min정도의 속도로 투입하여 반응시킨다. 이때 반응온도를 85±5℃로 유지한다. 약 1시간 후 ②항의 용액을 첨가하여 1∼2시간 정도 추가 반응시킨다.③ APT or CaWO 4 powder prepared while mixing the dilutions of ① well at a rate of 30-40 min to react. At this time, the reaction temperature is maintained at 85 ± 5 ℃. After about 1 hour, the solution of ② is added and reacted for 1 to 2 hours.
④ 반응이 끝나면 침전물을 Decantation 방법으로 4∼5회 완전 세척하고 Slurry 중 일정부피(예: 10㎖)를 채취하여 증발접시에 넣어 150℃에서 시간 건조시켜 수분을 완전히 증발시킨 후 그 무게를 달아 H2WO4중 WO3의 함량을 계산한다.④ After the reaction is complete, wash the precipitate 4 ~ 5 times by Decantation method, take a certain volume (for example, 10ml) out of slurry, put it in an evaporating dish, dry it at 150 ℃ for time, evaporate the water completely and weigh it. 2 The content of WO 3 in WO 4 is calculated.
⑤ Slurry 전체 부피를 측정하여, WO3의 함량 기준으로 탄소를 4.2당량 첨가하고 증류수를 Slurry 부피의 0.5배 첨가하여 Ball Mill Jar내에서 8시간 동안 습식 혼합한다.⑤ Measure the total volume of slurry, add 4.2 equivalents of carbon based on the content of WO 3 and add 0.5 times the volume of distilled water to wet mix for 8 hours in the Ball Mill Jar.
⑥ H2WO4Slurry와 탄소분말의 혼합물을 건조기에 장입하여 150℃에서 4시간 동안 건조하면 덩어리 상태로 굳어진다. 이를 그 상태 그대로 Graphite Crusible에 장입하여 진공분위기중 1100℃, 3시간동안 1차 반응시킨 후, 연속해서 수소분위기중 1400℃에서 1시간 동안 2차 반응시켜 냉각하는 방법으로 조대입자가 없는 평균입도 0.25㎛의 미립 탄화텅스텐 분말을 제조할 수 있었다.⑥ Charge the mixture of H 2 WO 4 slurry and carbon powder into the dryer and dry at 150 ℃ for 4 hours to solidify into a lump. It is charged into Graphite Crusible as it is and reacted for 1 hour at 1100 ° C in a vacuum atmosphere for 3 hours, followed by 2 hours of reaction at 1400 ° C in a hydrogen atmosphere for 1 hour to cool. A micronized tungsten carbide powder of 탆 could be prepared.
실시예 2Example 2
① 함중석용액(Na2WO4용액 혹은 (NH4)2WO4용액)을 WO3기준으로 약400∼450g/ℓ의 농도로 준비한다.① Prepare the sodium hydroxide solution (Na 2 WO 4 solution or (NH 4 ) 2 WO 4 solution) at a concentration of about 400 to 450 g / l based on WO 3 .
② 함중석 용액의 WO3량에 대한 염산반응당량의 약1.5∼2.0당량의 용액을 순수를 첨가하여 적정농도로 희석한다.(2) Dilute the solution of about 1.5 to 2.0 equivalents of hydrochloric acid reaction equivalent to WO 3 of the barite solution to the appropriate concentration by adding pure water.
③ 0.2∼0.3N 농도의 HNO3용액을 ②항의 용액과 동일 분량으로 분비하여 80℃로 데운다.③ Heat HNO 3 solution with 0.2 ~ 0.3N concentration in the same amount as the solution in ② and warm it to 80 ℃.
④ ②항의 용액에 ①항의 용액을 40∼60min정도의 속도로 투입하여 반응시키는데, 반응온도는 85±5℃로 유지하고 1시간 정도 반응시킨 후 ③항의 용액을 첨가하여 1∼2시간 추가 반응시킨다.④ The solution of item ① is added to the solution of item ② at a rate of about 40 to 60 min. The reaction temperature is maintained at 85 ± 5 ° C. for 1 hour, and then the solution of item ③ is added for 1 to 2 hours. .
⑤ 반응이 끝나면 반응물을 Decantation 방법으로 5∼6회 완전 세척하고 Slurry 중 일정부피(예: 10㎖)를 채취하여 증발접시에 넣어 110℃에서 4시간 건조시켜 수분을 완전히 증발시킨 후 그 무게를 달아 H2WO4중 WO3의 함량을 계산한다.⑤ After the reaction, the reactants are thoroughly washed 5 ~ 6 times by Decantation method, take a certain volume (for example 10ml) out of slurry and put it in an evaporating dish and dry it at 110 ℃ for 4 hours to completely evaporate moisture and weigh it. The content of WO 3 in H 2 WO 4 is calculated.
⑥ Slurry 전체 부피를 측정하여 WO3의 함량 기준으로 탄소를 4.35당량 첨가하고 증류수를 Slurry 부피의 1.2배 첨가하여 Ball Mill Jar 내에서 12시간 동안 습식 혼합한다.⑥ Measure the total volume of slurry and add 4.35 equivalents of carbon based on the content of WO 3 and add 1.2 times of the volume of slurry to wet mix in Ball Mill Jar for 12 hours.
⑦ H2WO4Slurry와 탄소분말의 혼합물을 건조기에 장입하여 110℃에서 36시간 동안 건조하면 덩어리 상태로 굳어진다. 이를 그 상태 그대로 Graphite Crusilble에 장입하여 진공분위기중 1050℃, 4시간 동안 1차 반응시킨 후, 연속해서 수소분위기중 1300℃에서 1시간 동안 2차 반응시켜 냉각하는 방법으로 조대입자가 없는 평균입도 0.20㎛의 미립 탄화텅스텐 분말을 제조할 수 있었다.⑦ The mixture of H 2 WO 4 slurry and carbon powder is charged into a drier and dried at 110 ° C. for 36 hours to harden into a lump. It was loaded into Graphite Crusilble as it is and reacted for 1 hour at 1050 ° C. in a vacuum atmosphere for 4 hours, followed by a second reaction at 1300 ° C. in a hydrogen atmosphere for 1 hour to cool. A micronized tungsten carbide powder of 탆 could be prepared.
이상 설명한 바와 같은 본 발명에 의하면 원료 합성 후 습식상태에서 바로 부원료와 혼합하여 건조하므로 Milling 공정없이 균일도를 높일 수 있고 건조 후에도 혼합분말이 잉곳(Ingot)화 되므로 성형공정을 생략할 수 있게 된다.According to the present invention as described above, since the raw material is mixed with the subsidiary materials in a wet state immediately after synthesis, the uniformity can be increased without the milling process, and the mixed powder is ingot after the drying process, so that the molding process can be omitted.
따라서 본 발명은 기존 건식 혼합시 필수 공정인 Milling 및 성형공정이 없이 탄화 텅스텐분말을 제조할 수 있어서 종래보다 경제적으로 처리할 수 있게 되는 유용한 효과가 있는 발명인 것이다.Therefore, the present invention is an invention having a useful effect of being able to manufacture tungsten carbide powder without the milling and molding process, which is an essential step in the existing dry mixing, so that it can be economically processed.
Claims (3)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020000055365A KR100359643B1 (en) | 2000-09-21 | 2000-09-21 | A manufacturing process of ultra-granule tungsten carbide dust by soppy system mixing |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020000055365A KR100359643B1 (en) | 2000-09-21 | 2000-09-21 | A manufacturing process of ultra-granule tungsten carbide dust by soppy system mixing |
Publications (2)
Publication Number | Publication Date |
---|---|
KR20020022847A KR20020022847A (en) | 2002-03-28 |
KR100359643B1 true KR100359643B1 (en) | 2002-11-04 |
Family
ID=19689663
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1020000055365A KR100359643B1 (en) | 2000-09-21 | 2000-09-21 | A manufacturing process of ultra-granule tungsten carbide dust by soppy system mixing |
Country Status (1)
Country | Link |
---|---|
KR (1) | KR100359643B1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR102648224B1 (en) * | 2023-10-30 | 2024-03-19 | (주)베사 | Method for preparing tungsten carbide using granular powder in a vacuum atmosphere |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SE526626C2 (en) * | 2003-08-12 | 2005-10-18 | Sandvik Intellectual Property | Ways to manufacture submicron cemented carbide |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62108731A (en) * | 1985-11-07 | 1987-05-20 | Nippon Mining Co Ltd | Production of water soluble tungsten compound crystal and high-purity tungstic acid crystal |
JPH03208811A (en) * | 1990-01-12 | 1991-09-12 | Tokyo Tungsten Co Ltd | Superfine wc powder and production thereof |
KR950008000A (en) * | 1993-09-03 | 1995-04-15 | 이진백 | Manufacturing method of tungstic acid (H2WO4) |
JPH10194717A (en) * | 1996-12-05 | 1998-07-28 | Nanodyne Inc | Generation of tungsten carbide particle |
KR100191277B1 (en) * | 1996-12-31 | 1999-06-15 | 최효병 | Method for producing wc and w powder |
-
2000
- 2000-09-21 KR KR1020000055365A patent/KR100359643B1/en not_active IP Right Cessation
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62108731A (en) * | 1985-11-07 | 1987-05-20 | Nippon Mining Co Ltd | Production of water soluble tungsten compound crystal and high-purity tungstic acid crystal |
JPH03208811A (en) * | 1990-01-12 | 1991-09-12 | Tokyo Tungsten Co Ltd | Superfine wc powder and production thereof |
KR950008000A (en) * | 1993-09-03 | 1995-04-15 | 이진백 | Manufacturing method of tungstic acid (H2WO4) |
JPH10194717A (en) * | 1996-12-05 | 1998-07-28 | Nanodyne Inc | Generation of tungsten carbide particle |
KR100191277B1 (en) * | 1996-12-31 | 1999-06-15 | 최효병 | Method for producing wc and w powder |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR102648224B1 (en) * | 2023-10-30 | 2024-03-19 | (주)베사 | Method for preparing tungsten carbide using granular powder in a vacuum atmosphere |
Also Published As
Publication number | Publication date |
---|---|
KR20020022847A (en) | 2002-03-28 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA1115487A (en) | Fibrous calcium sulfate | |
CN101423318B (en) | Red mud dealkalization method | |
KR100427005B1 (en) | Spheroidally Agglomerated Basic Cobalt(II) Carbonate and Spheroidally Agglomerated Cobalt(II) Hydroxide, Process for Their Production and Their Use | |
US20140145120A1 (en) | Iron (iii) orthophosphate-carbon composite | |
JP2009500268A (en) | Reducing agent for soluble chromate-containing material of cement and method for producing the same | |
JP2003335519A (en) | Method for producing magnesium potassium titanate and lithium potassium titanate | |
EP0328768A1 (en) | Continuous process for making granules of sodium perborate | |
KR100359643B1 (en) | A manufacturing process of ultra-granule tungsten carbide dust by soppy system mixing | |
JP5132225B2 (en) | Amorphous spherical aluminum silicate, method for producing the same, and preparation using the aluminum silicate. | |
CN101962209A (en) | Post treatment technique of iron oxide red for high-performance Mn-Zn soft magnetic ferrite | |
JP2683389B2 (en) | Flaky zinc oxide powder and method for producing the same | |
JP3384412B2 (en) | Method for producing crystalline zirconium phosphate | |
JPH11513657A (en) | Method for producing calcium borate | |
JPH0251847B2 (en) | ||
KR100495698B1 (en) | A preparation method of Ag-doped Nano Zirconium Phosphate powders with improved antimicrobial property | |
US6740300B1 (en) | Method for manufacturing crystalline layered sodium disilicate | |
JPH01131022A (en) | Production of highly dispersible magnesium hydroxide | |
JPS63260816A (en) | Manufacture of fine grain calcium sulfate | |
JPH03126621A (en) | Zirconium dioxide powder, preparation thereof, use thereof and sintered body prepared therefrom | |
JP3684585B2 (en) | Melamine cyanurate granule and method for producing the same | |
JPH02175604A (en) | Production of copper phosphite compound | |
JP4022938B2 (en) | Method for producing clay mineral organic composite | |
KR101334261B1 (en) | A preparation method of zinc oxide by wet precipitation | |
JP2001510135A (en) | Method for producing crystalline layered sodium disilicate | |
RU2165389C1 (en) | Method of preparing finely dispersed single-phase hydroxyl apatite |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A201 | Request for examination | ||
E701 | Decision to grant or registration of patent right | ||
GRNT | Written decision to grant | ||
FPAY | Annual fee payment |
Payment date: 20051026 Year of fee payment: 4 |
|
LAPS | Lapse due to unpaid annual fee |