JPS592479B2 - Method for producing high-speed diesel fuel and lubricating oil from paraffin heavy oil - Google Patents
Method for producing high-speed diesel fuel and lubricating oil from paraffin heavy oilInfo
- Publication number
- JPS592479B2 JPS592479B2 JP7300779A JP7300779A JPS592479B2 JP S592479 B2 JPS592479 B2 JP S592479B2 JP 7300779 A JP7300779 A JP 7300779A JP 7300779 A JP7300779 A JP 7300779A JP S592479 B2 JPS592479 B2 JP S592479B2
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- Prior art keywords
- oil
- diesel fuel
- speed diesel
- lubricating oil
- treated
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Description
【発明の詳細な説明】
この出願の発明は原油もしくはその脱塩処理液の常圧蒸
留による180〜320°Cの範囲で所定に選択認定し
た温度範囲の留分をフルフラール処理しその抽残油より
高速デ゛イーゼル燃料及び潤滑油を製造する様にした方
7去に関するものであり、特に、該抽残油を活性白土処
理し、処理液に塩化アルミニウム処理、或は、超音波処
理を施してその処理液に含有されている不飽和炭化水素
を重合しパラフィン系重質油から高速ディーゼル燃料及
び潤滑油を比較的簡易な工程により製造する方法に係る
ものである。DETAILED DESCRIPTION OF THE INVENTION The invention of this application is to furfural-process a fraction in a predetermined selected temperature range of 180 to 320°C by atmospheric distillation of crude oil or its desalted liquid, and produce the raffinate oil. This article relates to a method for producing higher-speed diesel fuel and lubricating oil, and in particular, the raffinate oil is treated with activated clay, and the treated liquid is subjected to aluminum chloride treatment or ultrasonic treatment. The present invention relates to a method for producing high-speed diesel fuel and lubricating oil from paraffinic heavy oil through a relatively simple process by polymerizing unsaturated hydrocarbons contained in the treated liquid.
周知の如く、一般に原油はその産地や油井によって組成
や性状が著しく異なっているものである。As is well known, the composition and properties of crude oil generally vary significantly depending on its production area and oil well.
従って、当該原油の種類に応じてそれから製造する石油
製品の種類、製造工程を決定しなければならない。Therefore, the type of petroleum product to be manufactured from it and the manufacturing process must be determined depending on the type of crude oil.
例えば、近年、中国に於いては大慶石油の開発が進みそ
の工業化が図られているが、それから採取される原油は
パラフィン系の重質油であり、従来行なわれている精製
工程ではコスト高になる欠点があり経済的ロスが多く好
ましくない。For example, in recent years, Daqing Petroleum has been developed and industrialized in China, but the crude oil extracted from it is paraffinic heavy oil, and the conventional refining process is expensive. It is undesirable because it has the disadvantage of causing a lot of economic loss.
因みに大慶石油の性状を示すと次の第1表の通りである
。Incidentally, the properties of Daqing Oil are shown in Table 1 below.
この出願の発明の目的は上記の様なパラフィン系重質油
の特質及び在来製品製造の問題点に鑑みその利用に関し
て検討をするにその性状特質から高速ディーゼル燃料及
び潤滑油を得ることが最も有利な製品化であり、効果的
な経済的メリットが得られることに着目し、その可及的
簡易な製造方法を提供せんとするものである。The purpose of the invention of this application is to study the use of paraffinic heavy oil in view of the above-mentioned characteristics and problems in the production of conventional products. Focusing on the advantageous commercialization and the fact that effective economic benefits can be obtained, the present invention aims to provide a manufacturing method that is as simple as possible.
上記目的に沿うこの出願の発明の構成は原油もしくはそ
の脱塩処理液の常圧蒸留による180〜320℃の範囲
で適宜に選択された温度範囲の留分をフルフラール処理
し、その抽残油を活性白土処理し、該処理液に塩化アル
ミニウムを加えるかもしくは5〜500 KHzで超音
波処理を施して該処理液中に含有されている不飽和炭化
水素を重合処理した後、常圧蒸留により180〜320
℃の範囲で適宜に選択された温度範囲の留分を取り出し
て高速ディーゼル燃料を得、残留分を潤滑油とする様に
してパラフィン系重質油から高速ディーゼル燃料及び潤
滑油を得る様にしたことを要旨とするものである。The structure of the invention of this application in accordance with the above-mentioned object is to furfural-treat the fraction in an appropriately selected temperature range of 180 to 320°C by atmospheric distillation of crude oil or its desalted liquid, and extract the raffinate oil. After treating the treated solution with activated clay, adding aluminum chloride to the treatment solution or subjecting it to ultrasonic treatment at 5 to 500 KHz to polymerize the unsaturated hydrocarbons contained in the treatment solution, it is distilled to 180% by atmospheric distillation. ~320
A high-speed diesel fuel was obtained by extracting a fraction in a temperature range appropriately selected within the temperature range of ℃, and the residual fraction was used as a lubricating oil to obtain a high-speed diesel fuel and a lubricating oil from a paraffinic heavy oil. The gist of this is that
次にこの出願の発明の実施例を各工程に従って説明すれ
ば以下の通りである。Next, an embodiment of the invention of this application will be described below according to each step.
まず、この出願の発明に於いては、前記大慶石油に性状
類似タイプの原油もしくはその脱塩処理液を常圧蒸留し
て180〜320°Cの範囲で適宜に選択された温度範
囲の留分を取り出す。First, in the invention of this application, a crude oil having properties similar to those of Daqing Petroleum or its desalted liquid is distilled under normal pressure to obtain a distillate having a temperature range appropriately selected from 180 to 320°C. Take out.
而して、該温度範囲は好ましくは200〜300℃であ
り、200〜280℃が更に好ましい。The temperature range is preferably 200 to 300°C, more preferably 200 to 280°C.
蓋し、2000C未満の温度範囲、そして、300℃を
越える温度範囲の留分を含む場合は良質な高速ディーゼ
ル燃料を得ることが出来ない。If the distillate contains fractions in the temperature range below 2000C and above 300C, high-quality high-speed diesel fuel cannot be obtained.
次に上記留分に対して従来から行なわれている通常の方
法によるフルフラール抽出法を適用してこれを処理する
。Next, the above-mentioned fraction is processed by applying a conventional furfural extraction method.
例えば、上記留分にフルフラールを加えると共に常温、
或は、加温下で充分に混合撹拌した後静置して抽出液と
抽残液とに分離し抽残、/l!に水を加えて2〜3回水
洗し、抽残液から水を除くことにより行なわれる。For example, while adding furfural to the above fraction, at room temperature,
Alternatively, after sufficient mixing and stirring under heating, the extract is separated into an extract and a raffinate by being left to stand, and the raffinate is separated into a raffinate, /l! This is done by adding water to the solution, washing with water two to three times, and removing water from the raffinate.
該プロセスによってナフテン族炭化水素、芳香IS炭化
水素その他各種環状炭化水素類、酸素、窒素、硫黄、及
び金属の有機化合物類その他の有色物質、樹脂類等を抽
出し、原料油からバラフイニツク成分を分離する。Through this process, naphthenic hydrocarbons, aromatic IS hydrocarbons, various cyclic hydrocarbons, organic compounds of oxygen, nitrogen, sulfur, and metals, other colored substances, resins, etc. are extracted, and barafinic components are separated from the raw oil. do.
尚、この留分とフルフラールとの混合割合は、留分4容
に対しフルフラール3容となる様にするのが好ましい。The mixing ratio of this fraction and furfural is preferably such that 4 volumes of the fraction are mixed with 3 volumes of furfural.
次に、この抽残液を活性白土処理するが、該処理には従
来処理方法が適用可能であり、例えば、上記抽残液を1
. O0〜260°Cに加熱し、活性白土と接触させた
後白土を濾過除去することによって行なわれる。Next, this raffinate is treated with activated clay, and a conventional treatment method can be applied to this treatment. For example, the raffinate can be treated with activated clay.
.. This is carried out by heating to 0 to 260°C, contacting with activated clay, and then filtering off the clay.
而して、活性白土の使用量は上記抽残液に対し4重量程
度度、処理時間は30分程度が好ましく処理温度は12
0℃程度がより好ましい。Therefore, the amount of activated clay used is about 4% by weight based on the raffinate, and the treatment time is preferably about 30 minutes, and the treatment temperature is 12.
About 0°C is more preferable.
該処理によって脱色、脱臭、脱湿、或は、懸濁物、樹脂
、アスファルト物質、酸素化合物、窒素化合物及びある
種の硫黄化合物などを除去するこさが出来る。This treatment can decolorize, deodorize, dehumidify, or remove suspended solids, resins, asphalt materials, oxygen compounds, nitrogen compounds, and certain sulfur compounds.
次に上記処理液に塩化アルミニウムを加えるか、或は、
超音波処理を施してこの抽出液中の不飽和炭化水素の重
合処理する。Next, add aluminum chloride to the above treatment solution, or
The unsaturated hydrocarbons in this extract are polymerized by ultrasonication.
上記塩化アルミニラt、による重合処理は、前記処理液
に塩化アルミニウムを添加し、加温下で処理した後にこ
の処理液を水洗することにより行なわれる。The polymerization treatment using aluminum chloride is carried out by adding aluminum chloride to the treatment solution, treating it under heating, and then washing the treatment solution with water.
当該処理に於いて、塩化アルミニウムの量は白土処理液
に対し2〜10重量係、処理温度は120〜150℃、
処理時間は30分程度が好ましい。In this treatment, the amount of aluminum chloride is 2-10% by weight of the clay treatment solution, the treatment temperature is 120-150°C,
The processing time is preferably about 30 minutes.
一方、超音波による重合処理は約5〜500KHzの超
音波により行なわれる。On the other hand, the ultrasonic polymerization treatment is performed using ultrasonic waves of about 5 to 500 KHz.
これによって、白土処理液中の不飽和炭化水素が重合し
、潤滑油となるべき成分が生成される。As a result, the unsaturated hydrocarbons in the clay treatment liquid are polymerized, and components to become lubricating oil are produced.
尚、この重合に使用される超音波は5KHz以下及び5
00 KHz以上では重合が所望に行なわれない。In addition, the ultrasonic waves used for this polymerization are 5 KHz or less and 5 KHz or less.
Above 0.00 KHz, polymerization does not occur as desired.
最後に、上記重合処理液を常圧蒸留し、180〜320
℃の範囲で所定に選択された温度範囲の留分を取り出し
て高速ディーゼル・燃料を得、残留分を潤滑油の基油と
する。Finally, the above polymerization solution was distilled under normal pressure to give a
A fraction in a predetermined temperature range of 0.degree. C. is extracted to obtain high-speed diesel fuel, and the residue is used as a base oil for lubricating oil.
但し、上記温度範囲は200〜3008Cが好ましく、
200〜280℃が更に好ましい。However, the above temperature range is preferably 200 to 3008C,
200-280°C is more preferable.
200℃未満の温度範囲及び300°Cを越える温度範
囲の留分が含まれる場合は、良質な高速ディーゼル燃料
が得られない。If fractions in the temperature range below 200°C and above 300°C are included, high-quality high-speed diesel fuel cannot be obtained.
次に具体的実施例を挙げて以下にその態様を説明する。Next, specific examples will be given and the aspects thereof will be explained below.
実施例 1
大慶石油から常圧蒸留により200〜280°Cの留分
を取り出す。Example 1 A 200-280°C fraction was extracted from Daqing Petroleum by atmospheric distillation.
該留分は原油の11.5容量係で、留分4容に対しフル
フラール3容を加えて常温で充分に混合撹1半した後、
静置して抽出液と抽残液とに分離し抽残液に水を加えて
2〜3回水洗する。The fraction was 11.5 volumes of crude oil, and 3 volumes of furfural was added to 4 volumes of the fraction, and the mixture was thoroughly mixed and stirred at room temperature for 1 and a half hours.
The extract is left to stand and separated into an extract and a raffinate, water is added to the raffinate, and the extract is washed with water 2 to 3 times.
而して、該抽残液を活性白土4重量係使用して120℃
、60分間処理し、使用済白土は濾別して無色透明な処
理液を得る。Then, the raffinate was heated at 120°C using 4 parts by weight of activated clay.
, for 60 minutes, and the used clay was filtered off to obtain a colorless and transparent treatment solution.
該処理液に対し2〜3分間、250 KHzの超音皮処
理を施しその処理液中の不飽和炭化水素の垂片処理をす
る。The treatment solution is subjected to ultrasonic treatment at 250 KHz for 2 to 3 minutes to remove unsaturated hydrocarbons in the treatment solution.
次いで、重合処理液を常圧蒸留して200〜280°C
の留分を取り出し高速ディーゼル燃料を浸ると共に残留
分として潤滑油の基油を得る。Next, the polymerization treatment solution was distilled at normal pressure to 200-280°C.
The fraction is taken out and immersed in high speed diesel fuel to obtain the base oil for lubricating oil as a residual fraction.
上記高速ディーゼル燃料の性状を示せば次の第2表の通
りであり、又、潤滑油の性状を示せば第3表の通りであ
る。The properties of the high-speed diesel fuel are shown in Table 2 below, and the properties of the lubricating oil are shown in Table 3.
実施例 2
同じく大慶石油の常圧蒸留による200〜280°C゛
の留分を取り・出し上記実施例1と同様にフルフラール
処理、活性白土処理(ただし処理時間は30分)する。Example 2 Similarly, the 200-280°C fraction obtained by atmospheric distillation of Daqing Petroleum was taken out and treated with furfural and activated clay in the same manner as in Example 1 (however, the treatment time was 30 minutes).
処理液に対して塩化アルミニウムを2重量係加え、12
0℃、30分間混合撹拌しこの処理液中の不飽和炭化水
素を重合させた後処理液を水洗する。Add 2 parts by weight of aluminum chloride to the treatment solution, and add 12 parts by weight of aluminum chloride.
The mixture was mixed and stirred at 0° C. for 30 minutes to polymerize unsaturated hydrocarbons in the treated solution, and the treated solution was then washed with water.
該重合水洗処理液を常圧蒸留して2’00〜280°C
の留出分を取り出し、この留出分を高速ディーゼル燃料
油きし留残分を潤滑油の基油とする。The polymerization water washing solution was distilled at normal pressure to 2'00 to 280°C.
This distillate is extracted from high speed diesel fuel and the distillate is used as a base oil for lubricating oil.
実施例 3
処理プロセスは実施例2とほぼ同様であるが、活性白土
処理時間を60分として実施する。Example 3 The treatment process is almost the same as in Example 2, but the activated clay treatment time is 60 minutes.
実施例 4
同じく大慶石油を常圧蒸留して2oo〜280℃の留分
を得る。Example 4 Similarly, Daqing Petroleum was distilled under normal pressure to obtain a fraction of 20°C to 280°C.
この該留分に実施例1と同様なフルフラール処理、活性
白土処理を施した後、対処理液2重量係の塩化アルミニ
ウムを加えて150℃、30分混合撹拌して不飽和炭化
水素を重合させた後、水洗いして塩化アルミニウムを除
去する。After subjecting this fraction to the same furfural treatment and activated clay treatment as in Example 1, aluminum chloride in an amount of 2 parts by weight of the treated liquid was added and mixed and stirred at 150°C for 30 minutes to polymerize unsaturated hydrocarbons. After that, wash with water to remove aluminum chloride.
該不飽和炭化水素重合処理液を常圧蒸留して200〜2
50℃の留出分を取り出し、留出分である高速ディーゼ
ル燃料油と留残分である潤滑油を得る。The unsaturated hydrocarbon polymerization solution is distilled at atmospheric pressure to give a
The distillate at 50°C is taken out to obtain a high-speed diesel fuel oil as a distillate and a lubricating oil as a distillate.
実施例 5
処理プロセスは実施例4とほぼ同様であるが、活性白土
処理時間を60分とし、塩化アルミニウム添加量を4重
量係として実施する。Example 5 The treatment process is almost the same as in Example 4, except that the activated clay treatment time is 60 minutes and the amount of aluminum chloride added is 4 parts by weight.
実施例 6
処理プロセスは実施例5とほぼ同様であるが塩化アルミ
ニウム添加量を10重重量出して実施する。Example 6 The treatment process is almost the same as in Example 5, except that aluminum chloride is added in an amount of 10% by weight.
上記の様にこの出願の発明に、よれば、比較的簡易な工
程でパラフィン系重質油から良質の高速ディーゼル燃料
を製造することが可能であり、パラフィン系重質油の有
効な利用方法を提供すると共に工業的にも経済的にも有
利な方法を提供することが出来る。As mentioned above, according to the invention of this application, it is possible to produce high-quality high-speed diesel fuel from paraffinic heavy oil in a relatively simple process, and it is possible to effectively utilize paraffinic heavy oil. At the same time, it is possible to provide an industrially and economically advantageous method.
試験例
大慶原油を常圧蒸留し、その200〜280°Cの留分
を取り出し、フルフラール及び活性白土処理を施す。Test Example Daqing crude oil is distilled under normal pressure, and the fraction at 200-280°C is taken out and treated with furfural and activated clay.
次に塩化アルミニウムを10重量係上天、温度を120
℃に保ちながら撹拌を行なう。Next, add aluminum chloride to 10% by weight, and reduce the temperature to 120%.
Stir while maintaining the temperature at °C.
その後塩化アルミニウムを水洗いにより除去し、これを
再び常圧蒸留して温度280°C以北の留分を取り出し
、寸ンブル/16.1とする。Thereafter, aluminum chloride was removed by washing with water, and this was distilled again under normal pressure to take out the fraction with a temperature north of 280°C, which was designated Dimble/16.1.
大慶原油を常圧蒸留し、その280〜300°Cの留分
を取り出し、フルフラール及び活性白土処理を施す。Daqing crude oil is distilled under atmospheric pressure, and the 280-300°C fraction is extracted and subjected to furfural and activated clay treatment.
次に周波数28 KHz、出力600Wの超音波を2分
間照射し、これを再び常圧蒸留して温度300℃以上の
留分を取り出し、サンプル扁2とする。Next, ultrasonic waves with a frequency of 28 KHz and an output of 600 W are irradiated for 2 minutes, and this is again distilled under normal pressure to take out a fraction with a temperature of 300° C. or higher, which is used as sample plate 2.
大慶原油を常圧蒸留し、その200〜280°Cの留分
を取り出し、フルフラール及び活性白土処理を施す。Daqing crude oil is distilled under atmospheric pressure, and the 200-280°C fraction is extracted and subjected to furfural and activated clay treatment.
次に周波数28 KHz、出力600Wの超音波を5分
間照射し、これを再び常圧蒸留して温度300 ’C以
上の留分を取り出し、サンプル/I63とする。Next, ultrasonic waves with a frequency of 28 KHz and an output of 600 W are irradiated for 5 minutes, and this is distilled again under normal pressure to take out a fraction with a temperature of 300'C or higher, which is designated as sample /I63.
大慶原油を常圧蒸留し、その200〜280℃の留分を
取り出し、フルフラール及び活性白土処理を施してサン
プル/I64とする。Daqing crude oil is distilled under atmospheric pressure, and the fraction at 200-280°C is taken out and subjected to furfural and activated clay treatment to obtain sample/I64.
以上のサンプル/V;1〜4をガスクロマトグラフ法に
より分析すると、サンプル/i61からはCI3〜C3
1成分が、サンプル扁2からはCI4〜0331戊分が
、サンプル扁3からはCI3〜C3□成分が、サンプル
/I64からはC8〜C28成分が検出される。When the above samples /V; 1 to 4 were analyzed by gas chromatography, CI3 to C3 were found from sample /i61.
1 component is detected from sample plate 2, CI4 to 0331 components are detected from sample plate 3, CI3 to C3□ components are detected from sample plate 3, and C8 to C28 components are detected from sample /I64.
また、各成分の含量については、サンプル/161〜3
はいずれもサンプル/164と比較して、質量数の大き
な成分が増加している。In addition, regarding the content of each component, sample/161-3
In both cases, the components with large mass numbers are increased compared to sample/164.
このように超音波処理又は塩化アルミニウム添加により
、重合反応が生起されることがわかる。Thus, it can be seen that a polymerization reaction is caused by ultrasonic treatment or addition of aluminum chloride.
而して、この出願の発明により製造さ几る高速ディーゼ
ル燃料は高速ディーゼルエンジンに最適のものであり、
又、潤滑油は良質精密機械油として効果的に使用し得る
ものである。Therefore, the high-speed diesel fuel produced by the invention of this application is optimal for high-speed diesel engines,
Furthermore, the lubricating oil can be effectively used as a high-quality precision machine oil.
Claims (1)
0〜320℃の範囲で所定に選択された温度範囲の留分
をフルフラール処理し、その抽残油よりパラフィン系重
質油からの高速ディーゼル燃料及び潤滑油を製造する方
法において、該抽残油を活性白土処理し、該処理液に塩
化アルミニウムを加えてこの処理液が含有している不飽
和炭化水素を重合処理した後、この処理液から常圧蒸留
により180〜320°Cの範囲で所定に選択された温
度範囲の留分を取り出して高速ディーゼル・燃料を得、
残留分を潤滑油とすることを特徴とするパラフィン系重
質油からの高速ディーゼル燃料咬び潤滑油の製造方法。 2 原油もしくはその脱塩処理液の常圧蒸留ζこよる1
80〜320℃の範囲で所定に選択された温度範囲の留
分2フルフラール処理し、その抽残油よりパラフィン系
重質油からの高速ディーゼル・燃料及び潤滑油を製造す
る方法において、該抽残油を活性白土処理し、該処理液
に超音波処理を施してその処理液が含有している不飽和
炭化水素を重合処理した後、この処理液から常圧蒸留に
より180〜320℃の範囲で所定に選択された温度範
囲の留分を取り出して高速ディーゼル燃料を得。 残留分を潤滑油とすることを特徴とするパラフィン系重
質油からの高速ディーゼル燃料及び個滑油の製造方法。[Claims] 1.18 by atmospheric distillation of crude oil or its desalted liquid
In a method for producing high-speed diesel fuel and lubricating oil from paraffinic heavy oil by treating a fraction in a predetermined temperature range of 0 to 320°C with furfural treatment, the raffinate oil is is treated with activated clay, aluminum chloride is added to the treated solution to polymerize the unsaturated hydrocarbons contained in the treated solution, and then the treated solution is distilled at a specified temperature in the range of 180 to 320°C under atmospheric pressure. extracting fractions in selected temperature ranges to obtain high-speed diesel fuel;
A method for producing a high-speed diesel fuel lubricating oil from paraffinic heavy oil, characterized in that the residue is used as a lubricating oil. 2 Atmospheric distillation of crude oil or its desalted liquid
A method for producing high-speed diesel fuel and lubricating oil from paraffinic heavy oil by treating the fraction 2 with furfural in a predetermined temperature range of 80 to 320°C and using the raffinate from the raffinate. The oil is treated with activated clay, the treated liquid is subjected to ultrasonic treatment to polymerize the unsaturated hydrocarbons contained in the treated liquid, and then the treated liquid is distilled under atmospheric pressure at a temperature of 180 to 320°C. High-speed diesel fuel is obtained by extracting the fraction in a predetermined selected temperature range. A method for producing high-speed diesel fuel and solid lubricating oil from paraffinic heavy oil, characterized in that the residual content is used as a lubricating oil.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7300779A JPS592479B2 (en) | 1979-06-12 | 1979-06-12 | Method for producing high-speed diesel fuel and lubricating oil from paraffin heavy oil |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7300779A JPS592479B2 (en) | 1979-06-12 | 1979-06-12 | Method for producing high-speed diesel fuel and lubricating oil from paraffin heavy oil |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS55165992A JPS55165992A (en) | 1980-12-24 |
JPS592479B2 true JPS592479B2 (en) | 1984-01-18 |
Family
ID=13505848
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7300779A Expired JPS592479B2 (en) | 1979-06-12 | 1979-06-12 | Method for producing high-speed diesel fuel and lubricating oil from paraffin heavy oil |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS592479B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0574426B2 (en) * | 1985-11-06 | 1993-10-18 | Rohm Kk |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2576006B2 (en) * | 1992-10-26 | 1997-01-29 | 三菱重工業株式会社 | Power generation method |
-
1979
- 1979-06-12 JP JP7300779A patent/JPS592479B2/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0574426B2 (en) * | 1985-11-06 | 1993-10-18 | Rohm Kk |
Also Published As
Publication number | Publication date |
---|---|
JPS55165992A (en) | 1980-12-24 |
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