JP2509263B2 - Method for producing mixed overbased sulfonate - Google Patents
Method for producing mixed overbased sulfonateInfo
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- JP2509263B2 JP2509263B2 JP62314665A JP31466587A JP2509263B2 JP 2509263 B2 JP2509263 B2 JP 2509263B2 JP 62314665 A JP62314665 A JP 62314665A JP 31466587 A JP31466587 A JP 31466587A JP 2509263 B2 JP2509263 B2 JP 2509263B2
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- Prior art keywords
- sulfonate
- mineral oil
- mixed
- overbased
- composition
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- Lubricants (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は混合過塩基価スルホン酸塩の製造方法に関
し、詳しくはアルキルベンゼンと特定の性状を有する鉱
油を原料とし、各種潤滑油基油対する溶解性のすぐれた
混合過塩基価スルホン酸塩の効率のよい製造方法に関す
る。TECHNICAL FIELD The present invention relates to a method for producing a mixed overbasic sulfonate, and more specifically, it uses an alkylbenzene and a mineral oil having specific properties as a raw material and dissolves it in various lubricating base oils. The present invention relates to a method for efficiently producing a mixed overbased sulfonate having excellent properties.
従来、アルキルベンゼンスルホン酸塩や過塩基価スル
ホン酸塩を製造する方法としては、各種の方法が知られ
ている。例えば、合成アルキルベンゼンを直接スルホン
化する方法(米国特許第2676925号明細書,同第2924618
号明細書)、合成アルキルベンゼンと芳香族成分をほと
んど含まない精製度の高い鉱油を原料として用い、これ
をスルホン化する方法(米国特許第3470097号明細書,In
dustrial & Engineering Chemistry Vol.50,No.7,p99
7)、さらには合成アルキルベンゼンをスルホン化し、
そのスルホン酸塩をさらに過塩基価して過塩基価アルキ
ルベンゼンスルホン酸塩を製造する方法(特開昭54−14
919号公報)などがある。Conventionally, various methods are known as methods for producing alkylbenzene sulfonates and overbased sulfonates. For example, a method in which a synthetic alkylbenzene is directly sulfonated (US Pat. Nos. 2,676,925 and 2,924,618).
No. 3470097), a method of using a highly refined mineral oil containing almost no synthetic alkylbenzene and an aromatic component as a raw material and sulfonation thereof (US Pat. No. 3470097).
dustrial & Engineering Chemistry Vol.50, No.7, p99
7), further sulfonation of synthetic alkylbenzene,
A method for producing an overbased alkylbenzene sulfonate by further overbasing the sulfonate (JP-A-54-14)
No. 919 bulletin).
しかし、上述した如き方法により得られたアルキルベ
ンゼンスルホン酸塩や過塩基価アルキルベンゼンスルホ
ン酸塩は、いずれも潤滑油基油に対する溶解性が充分で
ないため、潤滑油用の添加剤としては様々な問題があっ
た。However, the alkylbenzene sulfonates and the overbased alkylbenzene sulfonates obtained by the method as described above have various problems as additives for lubricating oils because they have insufficient solubility in lubricating base oils. there were.
そこで本発明者は、上記従来技術の欠点を解消し、す
ぐれた性状の過塩基価スルホン酸塩を開発すべく鋭意研
究を重ねた。Therefore, the present inventor has conducted intensive studies to solve the above-mentioned drawbacks of the prior art and develop an overbased sulfonate having excellent properties.
その結果、原料として合成アルキルベンゼンと芳香族
分含量の高い鉱油の混合物、あるいはこの混合物のスル
ホン酸を用いて得られるスルホン酸塩や過塩基価スルホ
ン酸塩が、上記目的を達成できるものであることを見出
した。本発明はかかる知見に基づいて完成したものであ
る。As a result, a mixture of synthetic alkylbenzene and mineral oil having a high aromatic content as a raw material, or a sulfonate or an overbased sulfonate obtained by using a sulfonic acid of this mixture can achieve the above object. Found. The present invention has been completed based on such findings.
すなわち、本発明はアルギルベンゼンスルホン酸
(A)と40℃における動粘度が100〜500cSt以上で芳香
族分含量が3%以上の鉱油のスルホン酸(B)との混合
物の過塩基価スルホン酸塩を主成分とする混合過塩基価
スルホン酸塩を提供するものである。また、本発明はこ
の混合過塩基価スルホン酸塩を製造する方法として、ア
ルキルベンゼン及び40℃における動粘度が100〜500cSt
以上で芳香族分含量が3%以上の鉱油の混合物を、スル
ホン化し、次いでアルカリ化合物で中和処理してスルホ
ン酸塩とし、しかる後に該スルホン酸塩の少なくとも一
部を過剰のアルカイ化合物と共に炭酸ガスと接触させて
過塩基価スルホン酸塩とすることにより混合過塩基価ス
ルホン酸塩を製造する方法をも提供するものである。That is, the present invention relates to an overbased sulfonic acid of a mixture of argylbenzene sulfonic acid (A) and sulfonic acid (B) of mineral oil having a kinematic viscosity at 40 ° C. of 100 to 500 cSt or more and an aromatic content of 3% or more. A mixed overbased sulfonate having a salt as a main component is provided. The present invention also provides a method for producing this mixed overbased sulfonate, which has a kinematic viscosity of 100 to 500 cSt at alkylbenzene and 40 ° C.
Above, a mixture of mineral oils having an aromatic content of 3% or more is sulfonated and then neutralized with an alkali compound to give a sulfonate, after which at least a part of the sulfonate is carbonated with an excess of an alky compound. It also provides a method for producing a mixed overbased sulfonate by contacting with gas to form an overbased sulfonate.
本発明の方法により製造された混合過塩基価スルホン
酸塩は、上記の如く(A),(B)の両スルホン酸の過
塩基価スルホン酸塩を主成分とするものである。ここで
(B)成分である鉱油のスルホン酸の原料となる鉱油と
しては、40℃における動粘度が100〜500cStであって、
芳香族分含量(n−d−M法による%CA)が3%以上、
好ましくは5〜60%のものである。この40℃における動
粘度が100cSt未満のものあるいは芳香族分含量が3%未
満のものでは、得られる混合過塩基価スルホン酸塩の潤
滑油基油に対する溶解性が充分でない。このような鉱油
は、上記性状を有するものであれば特に制限はないが、
例えばパラフィン基系、中間基系、ナフテン基系の原油
を常圧蒸溜,減圧蒸溜して得られる留出油を各種精製法
で処理した精製油が用いられる。The mixed overbased sulfonate prepared by the method of the present invention is mainly composed of the overbased sulfonate of both sulfonic acids (A) and (B) as described above. Here, as the mineral oil which is a raw material of the sulfonic acid of the mineral oil which is the component (B), the kinematic viscosity at 40 ° C. is 100 to 500 cSt,
(% By n-d-M method C A) aromatic content content of 3% or more,
It is preferably 5 to 60%. When the kinematic viscosity at 40 ° C. is less than 100 cSt or the aromatic content is less than 3%, the solubility of the obtained mixed overbasic sulfonate in the lubricating base oil is insufficient. Such mineral oil is not particularly limited as long as it has the above properties,
For example, a refined oil obtained by treating a distillate obtained by distilling a paraffin-based, intermediate-based or naphthene-based crude oil under atmospheric pressure or under reduced pressure by various refining methods is used.
また、本発明の混合過塩基価スルホン酸塩の種類とし
ては、特に制限はないが、通常はカルシウム塩,マグネ
シウム塩,バリウム塩,銅塩,ナトリウム塩,カリウム
塩,リチウム塩などがあり、そのうちカルシウム塩が好
ましい。In addition, the kind of the mixed overbased sulfonate of the present invention is not particularly limited, but usually includes calcium salt, magnesium salt, barium salt, copper salt, sodium salt, potassium salt, lithium salt, etc. Calcium salts are preferred.
本発明の混合過塩基価スルホン酸塩は、上記(A),
(B)の両スルホン酸混合物の過塩基価スルホン酸塩を
主成分とし、その割合は適宜定めればよいが、通常は
(A)成分/(B)成分=1/4〜4/1(重量比)の範囲に
なるように選定すればよい。The mixed overbased sulfonate of the present invention has the above (A),
The overbased sulfonate of the mixture of both sulfonic acids of (B) is the main component, and the ratio may be appropriately determined, but usually (A) component / (B) component = 1/4 to 4/1 ( The weight ratio may be selected within the range.
なお、本発明の混合過塩基価スルホン酸塩は、(A)
成分であるアルキルベンゼンスルホン酸と(B)成分で
ある鉱油のスルホン酸との混合物を過塩基価スルホン酸
塩としたものでなければならず、(A),(B)の両ス
ルホン酸をそれぞれ別々に過塩基価スルホン酸塩とし、
それらを混合して調製したものでは、本発明の目的とす
る性能を発現することはできない。The mixed overbased sulfonate of the present invention is (A)
A mixture of an alkylbenzene sulfonic acid as a component and a sulfonic acid of mineral oil as a component (B) must be an overbased sulfonic acid salt, and both sulfonic acids of (A) and (B) are separated from each other. With overbased sulfonate,
A product prepared by mixing them cannot exhibit the desired performance of the present invention.
本発明の混合過塩基価スルホン酸塩は、様々な方法に
より製造することができるが、前述した方法によれば、
極めて効率よくしかもすぐれた性能の混合スルホン酸塩
が得られる。The mixed overbased sulfonate of the present invention can be produced by various methods. According to the above-mentioned method,
A mixed sulfonate having extremely high efficiency and excellent performance can be obtained.
本発明の方法では、原料としてのアルキルベンゼンと
前述した40℃における動粘度が100〜500cSt以上で芳香
族分含量が3%以上の鉱油とを適宜割合で配合、好まし
くは前者/後者=1/4〜4/1(重量比)の範囲で配合した
混合物を、まず発煙硫酸等のスルホン化剤を用いてスル
ホン化してスルホン酸とし、これを必要に応じて100〜1
50ニュートラルオイルなどで希釈(但し、スルホン酸に
対して等重量以下で配合することが好ましい。)した
後、アルカリ化合物、例えば水酸化カルシウム,水酸化
マグネシウム,水酸化バリウム,水酸化銅等の水酸化物
あるいはこれらの金属の酸化物などを用いて中和して、
スルホン酸塩とすれば、混合スルホン酸塩が得られる。
また、スルホン酸を水酸化ナトリウム等で中和して、ス
ルホン酸ナトリウム等のアルカリ金属塩とした後、アル
カリ土類金属のハロゲン化物(例えば塩化カルシウム)
で複分解しても、同様に好適な混合スルホン酸塩を得る
ことができる。In the method of the present invention, alkylbenzene as a raw material and the above-mentioned mineral oil having a kinematic viscosity at 40 ° C. of 100 to 500 cSt or more and an aromatic content of 3% or more are blended at an appropriate ratio, preferably the former / latter = 1/4. ~ 4/1 (weight ratio), the mixture is mixed first with a sulfonating agent such as fuming sulfuric acid to give sulfonic acid.
After diluting with 50 neutral oil or the like (however, it is preferable to add it in an amount equal to or less than the weight of sulfonic acid), and then use an alkaline compound such as water such as calcium hydroxide, magnesium hydroxide, barium hydroxide or copper hydroxide. Neutralize using oxides or oxides of these metals,
With sulfonates, mixed sulfonates are obtained.
Also, after neutralizing sulfonic acid with sodium hydroxide or the like to form an alkali metal salt such as sodium sulfonate, an alkaline earth metal halide (eg, calcium chloride)
Even when the metathesis is carried out with, a similarly suitable mixed sulfonate can be obtained.
なお、この方法を行う際のスルホン化処理ならびに中
和処理の条件は、特に制限はなく常法によればよい。The conditions for the sulfonation treatment and the neutralization treatment when carrying out this method are not particularly limited and may be conventional methods.
次に、上記で得た混合スルホン酸塩の少なくとも一
部、即ち一部乃至全部を過剰のアルカリ化合物と共に炭
酸ガスと接触させて過塩基価スルホン酸塩(つまり、混
合スルホン酸塩の一部を過塩基化すれば、スルホン酸塩
と過塩基価スルホン酸塩との混合物が得られ、混合スル
ホン酸塩の全部を過塩基化すれば、全てが過塩基価スル
ホン酸塩となる。)を得るものである。ここで、スルホ
ン酸塩を過塩基価物に変換するにあたっては、通常は上
記混合スルホン酸塩を、水と有機溶剤(メタノールなど
のアルコール等)との混合溶剤にアルカリ化合物ととも
に加えて撹拌しながら、炭酸ガスを導入して接触処理
し、さらに必要に応じてアルカリ化合物を反応させるこ
とによって行われる。この際の処理条件は特に制限はな
く、適宜状況に応じて定めればよい。Next, at least a part of the mixed sulfonate obtained above, that is, a part or all of the mixed sulfonate is brought into contact with carbon dioxide gas together with an excess of an alkali compound to give an overbased sulfonate (that is, a part of the mixed sulfonate is Overbasing gives a mixture of sulfonates and overbased sulfonates, and overbasing all of the mixed sulfonates yields all overbased sulfonates.) It is a thing. Here, in converting the sulfonate into an overbased compound, usually, the mixed sulfonate is added to a mixed solvent of water and an organic solvent (alcohol such as methanol) together with an alkali compound while stirring. It is carried out by introducing carbon dioxide gas, carrying out a contact treatment, and further reacting an alkali compound as necessary. The processing condition at this time is not particularly limited, and may be appropriately set according to the situation.
次に、本発明を実施例及び比較例によりさらに詳しく
説明する。Next, the present invention will be described in more detail with reference to Examples and Comparative Examples.
実施例1 アルキルベンゼンボトム325gと第1表に示す325gの鉱
油IIIを反応フラスコに秤り取り、撹拌した。得られた
混合物を20℃以下に冷却した後、25%発煙硫酸216mlを
約30分間かけて滴下した。この際、混合物の温度は38℃
に保持されるように滴下速度を調節した。滴下終了後、
混合物の温度を36〜38℃に3時間保った。スルホン化反
応終了後、スルホン酸溶液と硫酸スラッジを分離した。Example 1 325 g of alkylbenzene bottom and 325 g of mineral oil III shown in Table 1 were weighed in a reaction flask and stirred. After the obtained mixture was cooled to 20 ° C. or lower, 216 ml of 25% fuming sulfuric acid was added dropwise over about 30 minutes. At this time, the temperature of the mixture is 38 ° C.
The dropping rate was adjusted so that After the dropping is completed,
The temperature of the mixture was kept at 36-38 ° C for 3 hours. After the completion of the sulfonation reaction, the sulfonic acid solution and the sulfuric acid sludge were separated.
このスルホン酸250g及び100ニュートラル鉱油50gを反
応容器に秤取し、トルエン200gおよび水酸化カルシウム
20gを加えて1時間撹拌した。その後、固形物を分離し
て清澄液(スルホン酸カルシウムのトルエン溶液)にメ
タノール120g,水15gおよび水酸化カルシウム90gを加え
て撹拌しながら炭酸ガス44gを4時間かけて導入した。
その後、水酸化カルシウムを15g加えて30分間撹拌後、
溶剤を留去し、150℃で30分保持後、冷却した。混合物
の温度が室温近くに下った時点で、トルエン300gを加え
て30分間撹拌し、これを遠心分離にかけて上澄液を集め
た。さらに上澄液を蒸溜して過塩基価スルホン酸カルシ
ウムを含む組成物を得た。このものの塩基価(TBN)は3
15mgKOH/gであった。また、この組成物の性状を第2表
に示す。250 g of this sulfonic acid and 50 g of 100 neutral mineral oil were weighed into a reaction vessel, and 200 g of toluene and calcium hydroxide were added.
20 g was added and stirred for 1 hour. Thereafter, the solid matter was separated, and 120 g of methanol, 15 g of water and 90 g of calcium hydroxide were added to a clear solution (a toluene solution of calcium sulfonate), and 44 g of carbon dioxide gas was introduced over 4 hours while stirring.
Then, after adding 15 g of calcium hydroxide and stirring for 30 minutes,
The solvent was distilled off, and the mixture was kept at 150 ° C for 30 minutes and then cooled. When the temperature of the mixture had dropped to near room temperature, 300 g of toluene was added and stirred for 30 minutes, and this was centrifuged to collect the supernatant. Further, the supernatant was distilled to obtain a composition containing calcium overbased sulfonate. The base number (TBN) of this product is 3
It was 15 mg KOH / g. The properties of this composition are shown in Table 2.
比較例1 第1表に示す鉱油IIIに代えて鉱油Iを用いたこと以
外は、実施例1と同様に操作を行って、組成物を得た。
このもののTBNは300mgKOH/gであった。また、この組成
物の性状を第2表に示す。Comparative Example 1 A composition was obtained in the same manner as in Example 1 except that Mineral Oil I was used instead of Mineral Oil III shown in Table 1.
The TBN of this product was 300 mg KOH / g. The properties of this composition are shown in Table 2.
比較例2 第1表に示す鉱油IIIに代えて鉱油IIを用いたこと以
外は、実施例1と同様の操作を行って、組成物を得た。
このもののTBNは320mgKHO/gであった。また、この組成
物の性状を第2表に示す。Comparative Example 2 A composition was obtained by performing the same operation as in Example 1 except that the mineral oil II was used instead of the mineral oil III shown in Table 1.
The TBN of this product was 320 mgKHO / g. The properties of this composition are shown in Table 2.
実施例2 第1表に示す鉱油IIIに代えて鉱油IVを用いたこと及
び水を15gから10gに変えたこと以外は、実施例1と同様
の操作を行って、組成物を得た。このもののTBNは315mg
KOH/gであった。また、この組成物の性状を第2表に示
す。Example 2 A composition was obtained by performing the same operation as in Example 1 except that mineral oil IV was used instead of mineral oil III shown in Table 1 and that water was changed from 15 g to 10 g. This product has a TBN of 315 mg
It was KOH / g. The properties of this composition are shown in Table 2.
実施例3 第1表に示す鉱油IIIに代えて鉱油Vを用いたこと及
び水を15gから10gに変えたこと以外は、実施例1と同様
の操作を行って、組成物を得た。このもののTBNは300mg
KOH/gであった。また、この組成物の性状を第2表に示
す。Example 3 A composition was obtained in the same manner as in Example 1 except that mineral oil V was used instead of mineral oil III shown in Table 1 and that water was changed from 15 g to 10 g. This product has a TBN of 300 mg
It was KOH / g. The properties of this composition are shown in Table 2.
実施例4 第1表に示す鉱油IIIに代えて鉱油VIを用いたこと及
び水を15gから10gに変えたこと以外は、実施例1と同様
の操作を行って、組成物を得た。このもののTBNは300mg
KOH/gであった。また、この組成物の性状を第2表に示
す。Example 4 A composition was obtained in the same manner as in Example 1 except that mineral oil VI was used instead of mineral oil III shown in Table 1 and that water was changed from 15 g to 10 g. This product has a TBN of 300 mg
It was KOH / g. The properties of this composition are shown in Table 2.
実施例5 実施例3の過程で得られたスルホン酸150g,100ニュー
トラル鉱油150g及び水10gを用い、以下実施例1と同様
にして過塩基化を行った。得られた組成物のTBNは300mg
KOH/gであった。また、この組成物の性状を第2表に示
す。Example 5 Using 150 g of sulfonic acid obtained in the process of Example 3, 150 g of 100 neutral mineral oil and 10 g of water, overbasing was carried out in the same manner as in Example 1 below. TBN of the obtained composition is 300 mg
It was KOH / g. The properties of this composition are shown in Table 2.
比較例3 第1表に示す鉱油IIIに代えて鉱油VIIを用いたこと以
外は、実施例1と同様の操作を行って、組成物を得た。
このもののTBNは270mgKOH/gであった。また、この組成
物の性状を第2表に示す。Comparative Example 3 A composition was obtained by performing the same operation as in Example 1 except that the mineral oil VII shown in Table 1 was used in place of the mineral oil VII.
The TBN of this product was 270 mg KOH / g. The properties of this composition are shown in Table 2.
比較例4 アルキルベンゼンボトム325gを、実施例1にしたがっ
てスルホン化した後、鉱油1を325gに加えて希釈した。
以下、実施例1と同様にして過塩基化を行った。得られ
た組成物のTBNは270mgKOH/gであった。また、この組成
物の性状を第2表に示す。Comparative Example 4 325 g of alkylbenzene bottom was sulfonated according to Example 1 and mineral oil 1 was then added to 325 g for dilution.
Thereafter, overbasing was carried out in the same manner as in Example 1. The TBN of the obtained composition was 270 mgKOH / g. The properties of this composition are shown in Table 2.
比較例5 実施例1において、鉱油IIIを用いないで得られたア
ルギルベンゼンスルホン酸カルシウム150gと市販の天然
スルホネート150gとの混合物を実施例1と同じ条件で過
塩基化を行った。得られた組成物のTBNは280mgKOH/gで
あった。また、この組成物の性状を第2表に示す。Comparative Example 5 A mixture of 150 g of calcium alginylbenzene sulfonate obtained without using Mineral Oil III and 150 g of commercially available natural sulfonate was overbasified under the same conditions as in Example 1. The resulting composition had a TBN of 280 mg KOH / g. The properties of this composition are shown in Table 2.
〔発明の効果〕 本発明の方法により製造された混合過塩基価スルホン
酸塩は、従来のアルキルベンゼンスルホン酸塩と比べ
て、潤滑油基油に対する溶解性や清浄性にすぐれてお
り、また外観も淡色であって良好である。したがって、
本発明の方法により製造された混合過塩基価スルホン酸
塩は、清浄分散剤、防錆剤などの各種潤滑油用添加剤と
して有効に利用される。また、本発明の方法によれば、
上記混合過塩基価スルホン酸塩を極めて効率よく、しか
も高性能のものを得ることができ、実用的価値の高いも
のである。 [Effect of the Invention] The mixed overbased sulfonate produced by the method of the present invention is superior in solubility and detergency to a lubricating base oil as compared with a conventional alkylbenzene sulfonate, and also has an appearance. Light color and good. Therefore,
The mixed overbased sulfonate produced by the method of the present invention is effectively utilized as an additive for various lubricating oils such as detergent dispersant and rust preventive. Further, according to the method of the present invention,
The mixed overbased sulfonic acid salt can be obtained with extremely high efficiency and high performance, and is of high practical value.
Claims (1)
が100〜500cStで芳香族分含量が3%以上の鉱油の混合
物を、スルホン化し、次いでアルカリ化合物で中和処理
してスルホン酸塩とし、しかる後に該スルホン酸塩の少
なくとも一部を過剰のアルカリ化合物と共に炭酸ガスと
接触させて過塩基価スルホン酸塩とすることを特徴とす
る混合過給基価スルホン酸塩の製造方法。1. A mixture of an alkylbenzene and a mineral oil having a kinematic viscosity at 40 ° C. of 100 to 500 cSt and an aromatic content of 3% or more is sulfonated, and then neutralized with an alkali compound to give a sulfonate. A method for producing a mixed supercharged valence sulfonate, which comprises contacting at least a part of the sulfonate with carbon dioxide together with an excess of an alkali compound to form an overbased sulfonate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62314665A JP2509263B2 (en) | 1987-12-12 | 1987-12-12 | Method for producing mixed overbased sulfonate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62314665A JP2509263B2 (en) | 1987-12-12 | 1987-12-12 | Method for producing mixed overbased sulfonate |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01157946A JPH01157946A (en) | 1989-06-21 |
JP2509263B2 true JP2509263B2 (en) | 1996-06-19 |
Family
ID=18056067
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62314665A Expired - Lifetime JP2509263B2 (en) | 1987-12-12 | 1987-12-12 | Method for producing mixed overbased sulfonate |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2509263B2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0735515B2 (en) * | 1990-03-30 | 1995-04-19 | 株式会社松村石油研究所 | Method for producing basic calcium sulfonate |
US20040248996A1 (en) * | 2003-06-09 | 2004-12-09 | Crompton Corporation | Sodium petroleum sulfonate blends as emulsifiers for petroleum oils |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE863376A (en) * | 1977-01-28 | 1978-07-27 | Exxon Research Engineering Co | PROCEDURE FOR PREPARING ALKYLAROMATIC COMPOUNDS, AND OIL-SOLUBLE SULDONIC ACIDS AND SULPHONATES DERIVED THEREOF |
JPS5840943B2 (en) * | 1980-04-15 | 1983-09-08 | 株式会社 松村石油研究所 | Method for producing oil-soluble sulfonate salts |
-
1987
- 1987-12-12 JP JP62314665A patent/JP2509263B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH01157946A (en) | 1989-06-21 |
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