JPH0526869B2 - - Google Patents
Info
- Publication number
- JPH0526869B2 JPH0526869B2 JP15769686A JP15769686A JPH0526869B2 JP H0526869 B2 JPH0526869 B2 JP H0526869B2 JP 15769686 A JP15769686 A JP 15769686A JP 15769686 A JP15769686 A JP 15769686A JP H0526869 B2 JPH0526869 B2 JP H0526869B2
- Authority
- JP
- Japan
- Prior art keywords
- transition metal
- benzene
- carbide
- titanium tetrachloride
- carbide film
- 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.)
- Expired - Lifetime
Links
- 229910052723 transition metal Inorganic materials 0.000 claims description 13
- 150000003624 transition metals Chemical class 0.000 claims description 13
- 150000002430 hydrocarbons Chemical class 0.000 claims description 8
- 239000000758 substrate Substances 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 4
- 238000005979 thermal decomposition reaction Methods 0.000 claims description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 36
- 238000006243 chemical reaction Methods 0.000 description 13
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 12
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 description 12
- 239000007789 gas Substances 0.000 description 11
- 238000000034 method Methods 0.000 description 10
- 239000010408 film Substances 0.000 description 9
- 229910052786 argon Inorganic materials 0.000 description 6
- 238000000576 coating method Methods 0.000 description 6
- 238000005229 chemical vapour deposition Methods 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- -1 saturated fatty acid hydrocarbon Chemical class 0.000 description 5
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000010453 quartz Substances 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- MTPVUVINMAGMJL-UHFFFAOYSA-N trimethyl(1,1,2,2,2-pentafluoroethyl)silane Chemical compound C[Si](C)(C)C(F)(F)C(F)(F)F MTPVUVINMAGMJL-UHFFFAOYSA-N 0.000 description 3
- QPUYECUOLPXSFR-UHFFFAOYSA-N 1-methylnaphthalene Chemical compound C1=CC=C2C(C)=CC=CC2=C1 QPUYECUOLPXSFR-UHFFFAOYSA-N 0.000 description 2
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 2
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 description 2
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 239000012159 carrier gas Substances 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000010790 dilution Methods 0.000 description 2
- 239000012895 dilution Substances 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 150000001247 metal acetylides Chemical class 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000000197 pyrolysis Methods 0.000 description 2
- NXHILIPIEUBEPD-UHFFFAOYSA-H tungsten hexafluoride Chemical compound F[W](F)(F)(F)(F)F NXHILIPIEUBEPD-UHFFFAOYSA-H 0.000 description 2
- WSWMGHRLUYADNA-UHFFFAOYSA-N 7-nitro-1,2,3,4-tetrahydroquinoline Chemical compound C1CCNC2=CC([N+](=O)[O-])=CC=C21 WSWMGHRLUYADNA-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 229910021552 Vanadium(IV) chloride Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- MVPPADPHJFYWMZ-UHFFFAOYSA-N chlorobenzene Chemical compound ClC1=CC=CC=C1 MVPPADPHJFYWMZ-UHFFFAOYSA-N 0.000 description 1
- ZLMUYRIFFZDBSE-UHFFFAOYSA-H chromium hexafluoride Chemical compound F[Cr](F)(F)(F)(F)F ZLMUYRIFFZDBSE-UHFFFAOYSA-H 0.000 description 1
- 229910021567 chromium(VI) fluoride Inorganic materials 0.000 description 1
- 239000011247 coating layer Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002003 electron diffraction Methods 0.000 description 1
- 238000000921 elemental analysis Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 1
- 150000004820 halides Chemical class 0.000 description 1
- PRVOBRCYHYXCMU-UHFFFAOYSA-H hexafluorotechnetium Chemical compound F[Tc](F)(F)(F)(F)F PRVOBRCYHYXCMU-UHFFFAOYSA-H 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 238000007733 ion plating Methods 0.000 description 1
- 229910001092 metal group alloy Inorganic materials 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 238000004544 sputter deposition Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 235000021122 unsaturated fatty acids Nutrition 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
- JTJFQBNJBPPZRI-UHFFFAOYSA-J vanadium tetrachloride Chemical compound Cl[V](Cl)(Cl)Cl JTJFQBNJBPPZRI-UHFFFAOYSA-J 0.000 description 1
- 238000001947 vapour-phase growth Methods 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Landscapes
- Chemical Vapour Deposition (AREA)
- Inorganic Insulating Materials (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は遷移金属炭化物膜の製法に関する。[Detailed description of the invention] (Industrial application field) The present invention relates to a method for producing a transition metal carbide film.
(従来の技術)
一般に炭化物は高硬度で耐摩耗性、耐食性に富
み、金属あるいは金属合金材料等の被覆膜として
広く利用されている。(Prior Art) Generally, carbides have high hardness, wear resistance, and corrosion resistance, and are widely used as coating films for metals or metal alloy materials.
このような炭化物の被覆膜、特に金属炭化物の
被膜は、通常炭素源としてメタン、プロパンで代
表される飽和脂肪酸炭化水素と金属源として四塩
化チタン、六フツ化タングステン等の化合物を用
い、化学気相成長法(CVD法)によつて行なわ
れている。 Such carbide coatings, especially metal carbide coatings, are usually made by chemical treatment using a saturated fatty acid hydrocarbon such as methane or propane as a carbon source and a compound such as titanium tetrachloride or tungsten hexafluoride as a metal source. This is done using the vapor phase growth method (CVD method).
しかしながら、上記の被覆法では、使用される
原料ガスの熱分解温度が高く、例えば1000℃を越
す温度で処理しなければならず、基材となる金属
母材の性能の低下を招く。 However, in the above-mentioned coating method, the thermal decomposition temperature of the raw material gas used is high, and the treatment must be performed at a temperature exceeding 1000°C, for example, resulting in a decrease in the performance of the metal base material.
基材の温度を上げずに処理する方法、例えばイ
オンプレーテイング法、スパツタリング法等も考
えられているが、これらはいずれも物理的な付着
を用いたもので、基材と被覆層との間の強度が極
めて小さく、被膜として適当ではない。また、被
膜自体の結晶性も殆んどなく、硬度、耐食性等が
劣る。 Methods of processing without raising the temperature of the base material, such as ion plating and sputtering methods, are being considered, but these all use physical adhesion and do not cause any damage between the base material and the coating layer. Its strength is extremely low, making it unsuitable as a coating. Furthermore, the coating itself has almost no crystallinity, and its hardness, corrosion resistance, etc. are inferior.
(発明の目的)
本発明は、上記従来の方法に鑑みてなされたも
ので、熱分解CVD(化学気相成長)法により、
1000℃以下の比較的低温で、結晶性の優れた炭化
物膜を基材上に形成する技術を提供することを目
的とする。(Object of the Invention) The present invention has been made in view of the above-mentioned conventional methods, and uses a pyrolytic CVD (chemical vapor deposition) method.
The purpose of the present invention is to provide a technology for forming a carbide film with excellent crystallinity on a substrate at a relatively low temperature of 1000°C or less.
(発明の内容)
即ち、本発明は不飽和基含有炭化水素化合物お
よび遷移金属ハロゲン化物の蒸気を同時に導入
し、600〜1000℃で加熱分解して基材上に遷移金
属炭化物膜を形成することを特徴とする遷移金属
炭化物膜の製法を提供する。(Contents of the invention) That is, the present invention involves simultaneously introducing vapors of an unsaturated group-containing hydrocarbon compound and a transition metal halide, and thermally decomposing them at 600 to 1000°C to form a transition metal carbide film on a substrate. Provided is a method for producing a transition metal carbide film characterized by the following.
本発明は、遷移金属炭化物を合成するため、不
飽和基含有炭化水素化合物と遷移金属ハロゲン化
物の同時熱分解法を利用し、熱分解温度の低い炭
化水素化合物を用いることにより、600〜1000℃
の低温で結晶性の優れた炭化物膜を形成すること
が可能で、従来の実用上処理温度の下限を400℃
以上低下させることができる。 In order to synthesize a transition metal carbide, the present invention utilizes a simultaneous thermal decomposition method of an unsaturated group-containing hydrocarbon compound and a transition metal halide, and uses a hydrocarbon compound with a low thermal decomposition temperature.
It is possible to form a carbide film with excellent crystallinity at a low temperature of 400°C, exceeding the lower limit of the conventional practical processing temperature.
or more.
本発明に用いる不飽和基含有炭化水素化合物
は、芳香族炭化水素、例えばベンゼン、トルエ
ン、キシレン、ナフタレン、α−メチルナフタレ
ン等;不飽和脂肪酸炭化水素、例えばエチレン、
プロピレン、ブチレン、2−ブチン、アセチレン
等;ジエン系化合物、例えばブタジエン、イソプ
レン等;またはこれらのハロゲン置換体、例えば
p−クロロベンゼン、1,2−ジクロロエチレ
ン、1,2−ジブロモエチレン等が挙げられる。 The unsaturated group-containing hydrocarbon compounds used in the present invention include aromatic hydrocarbons such as benzene, toluene, xylene, naphthalene, α-methylnaphthalene, etc.; unsaturated fatty acid hydrocarbons such as ethylene,
Propylene, butylene, 2-butyne, acetylene, etc.; diene compounds, such as butadiene, isoprene, etc.; or halogen-substituted products thereof, such as p-chlorobenzene, 1,2-dichloroethylene, 1,2-dibromoethylene, etc.
遷移金属のハロゲン化物の例としては、四塩化
チタン、四塩化バナジウム、六フツ化クロム、六
フツ化タングステン、六フツ化モリブデンまたは
六フツ化テクネチウム等が挙げられる。 Examples of transition metal halides include titanium tetrachloride, vanadium tetrachloride, chromium hexafluoride, tungsten hexafluoride, molybdenum hexafluoride, and technetium hexafluoride.
本発明の遷移金属炭化物膜の製法を図面および
実施例に基づいて説明する。 The method for producing a transition metal carbide film of the present invention will be explained based on drawings and examples.
(実施例)
第1図は本発明の実施例の説明に供する炭化物
生成装置のブロツク構成図である。(Embodiment) FIG. 1 is a block configuration diagram of a carbide generating apparatus for explaining an embodiment of the present invention.
上記の2種の原料ガスをキヤリヤガスで希釈し
て石英反応管4に導入する。石英反応管4への原
料供給方法は常圧バブラー法または減圧法を用い
る。いずれの方法でも後述する様にそれぞれの原
料の供給量を制御することにより、結晶性の優れ
た炭化物が得られる。常圧バブラー法では、キヤ
リヤガスとして水素またはアルゴンガスを使用す
る。第1図は常圧バブラー法を利用した装置構成
を示しているが、この装置で減圧CVD法を利用
することもできる。この場合には、炭化物の膜厚
を常圧バブラー法に比べてより均一に実現するこ
とが可能である。 The above two types of raw material gases are diluted with a carrier gas and introduced into the quartz reaction tube 4. The raw material is supplied to the quartz reaction tube 4 using an ordinary pressure bubbler method or a reduced pressure method. In either method, a carbide with excellent crystallinity can be obtained by controlling the supply amount of each raw material as described below. In the atmospheric bubbler method, hydrogen or argon gas is used as a carrier gas. Although FIG. 1 shows an apparatus configuration that uses the normal pressure bubbler method, it is also possible to use the reduced pressure CVD method with this apparatus. In this case, it is possible to achieve a more uniform carbide film thickness than in the normal pressure bubbler method.
原料の供給量は、使用する不飽和基含有炭化水
素化合物及び遷移金属ハロゲン化物の種類に強く
依存するが、炭化水素化合物の濃度は反応温度が
高い程少なくすることが望ましい。例えばベンゼ
ンと四塩化チタンを用いた場合、ベンゼンの濃度
は反応温度によつて下記に調整するのが効果的で
ある。 The amount of raw material supplied strongly depends on the type of unsaturated group-containing hydrocarbon compound and transition metal halide used, but it is desirable to reduce the concentration of the hydrocarbon compound as the reaction temperature increases. For example, when benzene and titanium tetrachloride are used, it is effective to adjust the concentration of benzene as shown below depending on the reaction temperature.
四塩化チタン1容(ガス)に対して、ベンゼン
は800〜900℃で10〜20容、900〜1000度では5〜
10容である。この濃度比以上に供給量を設定する
と、得られる炭化チタンの表面凹凸が激しくなり
スーチング発生する。 For one volume of titanium tetrachloride (gas), benzene is 10 to 20 volumes at 800 to 900℃, and 5 to 20 volumes at 900 to 1000℃.
It is 10 volumes. If the supply amount is set above this concentration ratio, the surface unevenness of the obtained titanium carbide becomes severe and sooting occurs.
真空蒸留による精製操作を行つたベンゼンおよ
び四塩化チタンが収納されたバブル容器1および
1′内にアルゴンガス制御系2よりアルゴンガス
を供給してベンセンおよび四塩化チタンを夫々独
立にバブルさせ、パイレツクスガラス管3を介し
て石英反応管4へベンセン分子および四塩化チタ
ン分子を同時に給送する。この際、バブル容器
1,1′内の液体ベンゼンおよび液体四塩化チタ
ンの温度を一定に保持してアルゴンガス流量をバ
ルブ5で夫々独立に調節し、ベンゼン分子および
四塩化チタン分子の反応管4内への供給量を夫々
一定制御する。一方、希釈ライン9よりアルゴン
を流し、反応管4へ給送されるベンゼン分子と四
塩化チタン混合ガスの数密度および流速を最適化
する。反応管4には成長用基板の載置された試料
台7が設置されており、反応管4の外周囲には加
熱炉8が設けられている。この加熱炉8によつて
反応管4内の成長用基板は1000℃以下の比較的低
温度に保持されている。 Argon gas is supplied from the argon gas control system 2 into the bubble containers 1 and 1' containing benzene and titanium tetrachloride that have been purified by vacuum distillation, and the benzene and titanium tetrachloride are bubbled independently. Benzene molecules and titanium tetrachloride molecules are simultaneously fed to the quartz reaction tube 4 through the Tx glass tube 3. At this time, the temperatures of liquid benzene and liquid titanium tetrachloride in the bubble containers 1 and 1' are kept constant, and the argon gas flow rate is adjusted independently with the valve 5. The amount of supply into each tank is controlled at a constant level. On the other hand, argon is flowed through the dilution line 9 to optimize the number density and flow rate of the benzene molecule and titanium tetrachloride mixed gas fed to the reaction tube 4. A sample stage 7 on which a growth substrate is mounted is installed in the reaction tube 4, and a heating furnace 8 is provided around the outer periphery of the reaction tube 4. The growth substrate in the reaction tube 4 is maintained at a relatively low temperature of 1000° C. or less by the heating furnace 8 .
反応管4内に導入されたベンゼンと四塩化チタ
ンの混合ガスは、1000℃以下の温度に加熱されて
それぞれのガスは同時に熱分解される。この際、
熱分解により生じたチタンと炭素原子は反応し
て、より自由エネルギーの低い炭化チタンを生成
する。 The mixed gas of benzene and titanium tetrachloride introduced into the reaction tube 4 is heated to a temperature of 1000° C. or less, and each gas is simultaneously thermally decomposed. On this occasion,
Titanium and carbon atoms produced by pyrolysis react to form titanium carbide, which has a lower free energy.
得られる炭化チタン薄膜はX線マイクロアナラ
イザーによる元素分析の結果、化学量論組成であ
ることが確かめられた。また、高速反射電子線回
折の結果、900〜1000℃の反応温度では、ベンゼ
ンの四塩化チタンに対する濃度比が5〜10の範囲
で多結晶から単結晶に移行することが確認され
た。 As a result of elemental analysis using an X-ray microanalyzer, it was confirmed that the titanium carbide thin film obtained had a stoichiometric composition. Further, as a result of high-speed reflection electron diffraction, it was confirmed that at a reaction temperature of 900 to 1000°C, the concentration ratio of benzene to titanium tetrachloride transitioned from polycrystal to single crystal in the range of 5 to 10.
なお、炭化物を形成する遷移金属ハロゲン化物
としては、四塩化チタン以外に他の低融点のハロ
ゲン化物を使用しても同様の結果が得られ、ま
た、ベンゼン以外の他の炭化水素化合物との組み
合わせも可能である。 Note that similar results can be obtained by using other low-melting-point halides other than titanium tetrachloride as transition metal halides that form carbides, and combinations with other hydrocarbon compounds other than benzene can also be used. is also possible.
(発明の効果)
以上の如く、本発明に係る炭化物合成法によれ
ば、熱分解CVD法を用いて、従来より低い反応
温度で合成することが可能で、その結果、基板と
なる母材の性能を損なうことなく、結晶性の優れ
た炭化物膜を形成することができる。(Effects of the Invention) As described above, according to the carbide synthesis method according to the present invention, synthesis can be performed at a lower reaction temperature than conventional methods using the pyrolysis CVD method. A carbide film with excellent crystallinity can be formed without impairing performance.
第1図は本発明の実施例の説明に供する炭化物
生成装置のブロツク構成図である。
1,1′……バブル容器、2……アルゴンガス
制御系、3……ガラス管、4……反応管、6,9
……希釈ライン、7……試料台、8……加熱炉。
FIG. 1 is a block diagram of a carbide generating apparatus for explaining an embodiment of the present invention. 1, 1'...Bubble container, 2...Argon gas control system, 3...Glass tube, 4...Reaction tube, 6,9
...Dilution line, 7...Sample stand, 8...Heating furnace.
Claims (1)
ハロゲン化物の蒸気を同時に導入し、600〜1000
℃で加熱分解して基材上に遷移金属炭化物膜を形
成することを特徴とする遷移金属炭化物膜の製
法。1. Steam of an unsaturated group-containing hydrocarbon compound and a transition metal halide is introduced at the same time, and
A method for producing a transition metal carbide film, which comprises forming a transition metal carbide film on a substrate by thermal decomposition at °C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15769686A JPS6314871A (en) | 1986-07-03 | 1986-07-03 | Production of transition metal carbide film |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15769686A JPS6314871A (en) | 1986-07-03 | 1986-07-03 | Production of transition metal carbide film |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6314871A JPS6314871A (en) | 1988-01-22 |
| JPH0526869B2 true JPH0526869B2 (en) | 1993-04-19 |
Family
ID=15655383
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15769686A Granted JPS6314871A (en) | 1986-07-03 | 1986-07-03 | Production of transition metal carbide film |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6314871A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2748881B2 (en) * | 1995-02-03 | 1998-05-13 | 日本電気株式会社 | Semiconductor manufacturing apparatus and manufacturing method |
-
1986
- 1986-07-03 JP JP15769686A patent/JPS6314871A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6314871A (en) | 1988-01-22 |
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