JPS5918402B2 - Manufacturing method for lubricating oil additives - Google Patents

Manufacturing method for lubricating oil additives

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Publication number
JPS5918402B2
JPS5918402B2 JP49044348A JP4434874A JPS5918402B2 JP S5918402 B2 JPS5918402 B2 JP S5918402B2 JP 49044348 A JP49044348 A JP 49044348A JP 4434874 A JP4434874 A JP 4434874A JP S5918402 B2 JPS5918402 B2 JP S5918402B2
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JP
Japan
Prior art keywords
formula
acid
mol
same
substituted
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
Application number
JP49044348A
Other languages
Japanese (ja)
Other versions
JPS5030905A (en
Inventor
スコツチフオ−ド エリオツト ジヨン
テレンス デイビス ブライアン
マ−チン ホウレツト リチヤ−ド
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Edwin Cooper and Co Ltd
Original Assignee
Edwin Cooper and Co Ltd
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Filing date
Publication date
Application filed by Edwin Cooper and Co Ltd filed Critical Edwin Cooper and Co Ltd
Publication of JPS5030905A publication Critical patent/JPS5030905A/ja
Publication of JPS5918402B2 publication Critical patent/JPS5918402B2/en
Expired legal-status Critical Current

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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M133/00Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing nitrogen
    • C10M133/52Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing nitrogen having a carbon chain of 30 or more atoms
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C59/00Compounds having carboxyl groups bound to acyclic carbon atoms and containing any of the groups OH, O—metal, —CHO, keto, ether, groups, groups, or groups
    • C07C59/40Unsaturated compounds
    • C07C59/58Unsaturated compounds containing ether groups, groups, groups, or groups
    • C07C59/64Unsaturated compounds containing ether groups, groups, groups, or groups containing six-membered aromatic rings
    • C07C59/66Unsaturated compounds containing ether groups, groups, groups, or groups containing six-membered aromatic rings the non-carboxylic part of the ether containing six-membered aromatic rings
    • C07C59/68Unsaturated compounds containing ether groups, groups, groups, or groups containing six-membered aromatic rings the non-carboxylic part of the ether containing six-membered aromatic rings the oxygen atom of the ether group being bound to a non-condensed six-membered aromatic ring
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    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
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    • C10M2207/282Esters of (cyclo)aliphatic oolycarboxylic acids
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    • C10M2215/00Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant compositions
    • C10M2215/02Amines, e.g. polyalkylene polyamines; Quaternary amines
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    • C10M2219/08Thiols; Sulfides; Polysulfides; Mercaptals
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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Lubricants (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Description

【発明の詳細な説明】 本発明は潤滑油添加剤として有用な化合物の製法に関す
る。
DETAILED DESCRIPTION OF THE INVENTION This invention relates to a process for making compounds useful as lubricating oil additives.

潤滑油、ことに自動車用潤滑油に配合される各種の添加
剤の中には、各種表面活性剤がある。
Among the various additives added to lubricating oils, especially automotive lubricating oils, there are various surfactants.

炭素粒子や他の不溶性物質、たとえば分解生成物および
燃料酸化生成物などに、潤滑油の主構成成分の油媒体中
に分散させるためには、分散剤、ことに無灰分分散剤が
用いられる。かくして不溶性物質は油媒体中に分散され
、エンジンの作動を劣化させる付着物の形成を防ぐこと
ができる。前記のごとき目的に用いられる無灰分分散剤
として、長鎖アルキルフエノールとアルデヒドおよびポ
リアルキレンとを反応させてえられるある種のマンニツ
ヒ塩基誘導体が提案されている。
Dispersants, especially ashless dispersants, are used to disperse carbon particles and other insoluble substances, such as decomposition products and fuel oxidation products, in the oil medium of the main constituent of lubricating oils. Insoluble substances are thus dispersed in the oil medium and can prevent the formation of deposits that degrade engine operation. As ashless dispersants used for the above purpose, certain Mannitz base derivatives obtained by reacting long-chain alkylphenols with aldehydes and polyalkylenes have been proposed.

これらの化合物はすぐれた分散剤であつて、それを配合
することによりその潤滑油にある程度の酸化耐性を付与
する。しかしながら、それらは一般に熱安定性に劣り、
またジーゼルに適用したばあいに油の性能が低下する傾
向がある。本発明は、潤滑油添加剤として有用な式:〔
式中、各R1は同一または異なつて、少なくとも30個
の炭素原子を有するポリブチル、ポリイソブチルまたは
ポリプロピル、R2は無しか、または式:(式中、mは
Oまたは整数、R1は前記と同じ、5、 /0R
5および−C は後記と同じ)で示される基、\.R
4は水素、 メチルまたは式:一z{;〕(式中、 Zは硫黄またはメチレン、R1は前記と同じ)で示され
る基、各R5は同一または異なつて、水素、/0メチル
または−CH2Cl−]2C\.で示される基、各/″
C は同一または異なつてアミド基を意味す\,
〜る〕 で示される化合物の製法を提供するものである。
These compounds are excellent dispersants and their inclusion imparts a certain degree of oxidation resistance to the lubricating oil. However, they generally have poor thermal stability;
Furthermore, when applied to diesel, the performance of the oil tends to decrease. The present invention describes the formula useful as a lubricating oil additive:
where each R1 is the same or different and is polybutyl, polyisobutyl or polypropyl having at least 30 carbon atoms, R2 is absent or of the formula: (wherein m is O or an integer, R1 is the same as above) ,5, /0R
5 and -C are the same as below), \. R
4 is hydrogen, methyl or a group represented by the formula: -Z{;] (wherein Z is sulfur or methylene, R1 is the same as above), each R5 is the same or different and is hydrogen, /0methyl or -CH2Cl -]2C\. Each group represented by /″
C is the same or different and means an amide group\,
-ru] Provides a method for producing a compound represented by the following.

本発明の化合物において、R1基は、少なくとも30、
好ましくは50〜200個の炭素原子を有するポリイソ
ブチルまたはポリプロピル基である。これらは、分子量
700〜3000、好ましくは900〜2000、とく
に約1000のポリイソブチレンまたはポリプロピレン
から誘導される。式〔1〕の化合物は該ポリイソブチル
またはポリプロピル置換フエノールを、グリオキシル酸
、ピルビン酸および2−オキソグルタール酸からなる群
から選ばれるカルボニル置換化合物と反応させビス(フ
エノール置換)カルボン酸を形成させ、これを、N−ア
ミノエチルエタノール、ビスーアミノプロピルピペラジ
ン、ビス−ヘキサメチレントリアミン、ジプロピレント
リアミン、ジメチルアミノプロピルアミン、エチレンポ
リアミンおよIV−1−工1,)ノ醪11マぐ)JL?
シS7マ〜ノ一》マご[ぐl爪口応生成物からなる群か
ら選ばれるアミンと反応させて対応するアミドに導くこ
とにより製造される。
In the compounds of the invention, the R1 group comprises at least 30,
Preferably it is a polyisobutyl or polypropyl group having 50 to 200 carbon atoms. These are derived from polyisobutylene or polypropylene with a molecular weight of 700 to 3000, preferably 900 to 2000, especially about 1000. The compound of formula [1] is obtained by reacting the polyisobutyl or polypropyl substituted phenol with a carbonyl substituted compound selected from the group consisting of glyoxylic acid, pyruvic acid and 2-oxoglutaric acid to form a bis(phenol substituted) carboxylic acid. This was added to N-aminoethylethanol, bis-aminopropylpiperazine, bis-hexamethylene triamine, dipropylene triamine, dimethylaminopropylamine, ethylene polyamine and IV-1-Product 1,) Nomomi 11 Mag) JL ?
It is produced by reacting with an amine selected from the group consisting of S7 reaction products to form the corresponding amide.

本発明の方法で用いられる出発物質のビス(フエノール
置換)カルボン酸またはその誘導体は、好ましくは、本
出願人の英国特許明細書第1446435号に記載の縮
合生成物である。
The starting bis(phenol-substituted) carboxylic acids or derivatives thereof used in the process of the invention are preferably the condensation products described in the Applicant's British Patent Specification No. 1,446,435.

該英国特許明細書第1446435号に記載の生成物は
、(1)アルキル置換基が少なくとも8個の炭素原子を
有するアルキル置換モノヒトリックフェノールと(2)
グリオキサル酸、ピルビン酸、レブリン酸、3−オキソ
グルタール酸、2−オキソグルタール酸およびそれらの
エステル類から選ばれるカルボニル置換化合物との縮合
生成物である。英国特許明細書第1446435号には
また一般式:または〔式中、各R1は同一または異なつ
て少なくとも8個の炭素数を有するアルキル;R2は無
しまたはや 7,0〕(式中、
mはOまたは整数、R4,R5,Yおよびnは後記と同
じ)で示される基;Wは無しまたは式(式中、pおよび
qは同一または異なつて0または整数、R4,R5,Y
およびnは後記と同じ)で示される基;各R4は同一ま
たは異なつて無しまたは式−Z−R6(式中、Zは硫黄
または2個以上の硫黄鎖あるいは無し、R6はアルキル
、ヒドロキシ置換アリール、アラルキルまたはアルキル
アリール基:各R5は同一または異なつて水素、メチル
または一(CH2)rl−C\ ;nは同一または異な
つてOまたは1〜2の整数;各Yは同一または異なつて
ヒドロキシまたはアルコキシ基である〕で示される化合
物も記載される。
The product described in GB 1446435 comprises (1) an alkyl-substituted monohydric phenol in which the alkyl substituent has at least 8 carbon atoms; and (2)
It is a condensation product with a carbonyl-substituted compound selected from glyoxalic acid, pyruvic acid, levulinic acid, 3-oxoglutaric acid, 2-oxoglutaric acid, and esters thereof. British Patent Specification No. 1,446,435 also describes the general formula: or in which each R1 is the same or different alkyl having at least 8 carbon atoms; R2 is none or less than 7,0;
m is O or an integer, R4, R5, Y and n are the same as below); W is none or a group represented by the formula (wherein p and q are the same or different and 0 or an integer, R4, R5, Y
and n is the same as below); each R4 is the same or different, or a group represented by the formula -Z-R6 (wherein Z is sulfur or two or more sulfur chains or none, R6 is alkyl, hydroxy-substituted aryl , aralkyl or alkylaryl group: each R5 is the same or different and is hydrogen, methyl or one (CH2)rl-C\; n is the same or different and is O or an integer from 1 to 2; each Y is the same or different and is hydroxy or is an alkoxy group] are also described.

前記式中、R3が式〔C〕の基であるばあいは、式で示
される基はいかなる順序で配列されていてもよい。
In the above formula, when R3 is a group of formula [C], the groups represented by the formula may be arranged in any order.

たとえば、これらは互いにランダムに点在してもよく、
プロツクとして配列されている必要はない。前記縮合生
成物の場合、出発物質のアルキル置換フエノールはその
芳香環上に、前記式〔A〕および〔B〕の化合物におけ
るR4に対応する1個以上の他の置換基を有していても
よい。
For example, these may be randomly interspersed with each other,
It does not need to be arranged as a block. In the case of the above condensation product, the starting material alkyl-substituted phenol may have one or more other substituents on its aromatic ring corresponding to R4 in the compounds of the above formulas [A] and [B]. good.

アルキル置換基以外に置換基が無い場合は、R4が水素
のものに対応する。アルキル置換基は、式〔A〕および
〔B〕におけるR1に対してパラ位にあることが好まし
い。他の置換基がある場合には、それらは、少なくとも
1つのオルト位が非置換で、その位置にてフエノールが
カルボニル化合物と縮合しフエノール残基が式〔A〕お
よび〔B〕に示されるようにオルト位に結合されるごと
くなりうるように置換されているのが好ましい。基R4
または縮合生成物の場合はそれに対応する置換基は、前
記したごとく、無しでもまたは式Z−R6であつてもよ
い。
If there are no substituents other than alkyl substituents, this corresponds to R4 being hydrogen. Preferably, the alkyl substituent is in the para position to R1 in formulas [A] and [B]. If other substituents are present, they are unsubstituted in at least one ortho position, at which position the phenol is fused with the carbonyl compound and the phenol residue is as shown in formulas [A] and [B]. is preferably substituted so that it can be bonded in the ortho position. group R4
Alternatively, in the case of a condensation product, the corresponding substituent may be absent or of the formula Z-R6, as described above.

好ましい態様ではR4は無しである。それはすなわち、
R4または縮合生成物の場合はその対応する置換基が水
素であることを意味する。そのような化合物は、アルキ
ル置換基以外の置換基を有しないアルキルフエノールか
ら誘導される。他の態様では、R4または縮合生成物の
場合はその対応する置換基は、式−ZR6(式中、Zは
無しかまたは硫黄または2個以上、好ましくは2〜4個
の硫黄原子の鎖である。この態様の場合、Zが無しのと
きは、R6は炭素数1〜8個、好ましくは1〜4個の短
鎖アルキル基であるか、または式−CHR7(式中、R
7は水1t素またはアルキル;R8は少なくとも1個の
ヒドロキシ置換基を有するアリールまたはアラルキル基
)で示される基である。
In a preferred embodiment R4 is absent. That is,
In the case of R4 or a condensation product, it means that the corresponding substituent is hydrogen. Such compounds are derived from alkylphenols having no substituents other than alkyl substituents. In another embodiment, R4, or its corresponding substituent in the case of a condensation product, has the formula -ZR6, where Z is none or a chain of sulfur or 2 or more, preferably 2 to 4 sulfur atoms. In this embodiment, when Z is absent, R6 is a short-chain alkyl group having 1 to 8 carbon atoms, preferably 1 to 4 carbon atoms, or has the formula -CHR7 (wherein R
7 is water or alkyl; R8 is an aryl or aralkyl group having at least one hydroxy substituent.

一方、この態様でZが硫黄または2以上の硫黄鎖のとき
は、R6はヒドロキシ置換基を有するアリールまたはア
ルキルアリール基であるのが好ましい。本発明の製法に
用いる出発物質は、式〔A〕および〔B〕におけるR1
が少なくとも30個の炭素原子を有するポリイソブチル
またはポリプロピルである前記英国特許明細書第144
6435号に記載の新規化合物またはR5が水素、メチ
ルまたは一CH2CH2C<8である前記縮合生成物で
ある。
On the other hand, when Z is sulfur or two or more sulfur chains in this embodiment, R6 is preferably an aryl or alkylaryl group having a hydroxy substituent. The starting materials used in the production method of the present invention are R1 in formulas [A] and [B].
is polyisobutyl or polypropyl having at least 30 carbon atoms.
6435 or said condensation products in which R5 is hydrogen, methyl or -CH2CH2C<8.

これらの出発物質を前記のごとくアミンまたはアミンの
混合物と反応させる。存在するアミノ基が/″カルボキ
シル基と反応して−C1 のアミド基を形成する。
These starting materials are reacted with an amine or mixture of amines as described above. The amino group present reacts with the /'' carboxyl group to form an amide group of -C1.

本発明の製法で用いる出発物質のアミンは、前記のごと
く、N−アミノエチルエタノール、ビスーアミノプロピ
ルピペラジン、ビス−ヘキサメチレントリアミン、ジプ
ロピレントリアミン、ジメチルアミノプロピルアミン、
エチレンポリアミンおよびエチレンポリアミンとジシア
ンジアミドとの反応生成物からなる群から選ばれる。
As mentioned above, the starting amines used in the production method of the present invention include N-aminoethylethanol, bis-aminopropylpiperazine, bis-hexamethylenetriamine, dipropylenetriamine, dimethylaminopropylamine,
selected from the group consisting of ethylene polyamines and reaction products of ethylene polyamines and dicyandiamide.

エチレンポリアミンの例としては、エチレンジアミン、
ジエチレントリアミン、トリエチレンテトラミン、テト
ラエチレンペンタミン、ペンタエチレンヘキサミンおよ
びより高級のポリエチレンポリアミン混合物が挙げられ
る。これらのエチレンポリアミンを英国特許第1068
235号に記載のようなジシアンジアミドと反応させた
反応生成物も使用できる。有用な高級ポリアミン類は3
00〜1000または50001好ましくは400〜6
00の分子量を有し、とくにエチレンイミンの重合によ
つてえられるものがよい。
Examples of ethylene polyamines include ethylene diamine,
Mention may be made of diethylenetriamine, triethylenetetramine, tetraethylenepentamine, pentaethylenehexamine and higher polyethylenepolyamine mixtures. These ethylene polyamines are covered by British Patent No. 1068.
Reaction products reacted with dicyandiamide, such as those described in No. 235, can also be used. There are 3 useful higher polyamines
00-1000 or 50001 preferably 400-6
Particularly preferred are those having a molecular weight of 0.00 and obtained by polymerization of ethyleneimine.

エチレンイミドを重合すると広範囲の分子量を有するポ
リアルキレンポリアミン類の混合物がえられる。それら
は、本発明にもつとも有用な分子量範囲のものに分割し
てもよい。アミンはほぼ等モルのビス(フエノール置換
)カルボン酸またはその誘導体と反応される。
Polymerization of ethyleneimide yields a mixture of polyalkylene polyamines having a wide range of molecular weights. They may be divided into molecular weight ranges useful in this invention. The amine is reacted with approximately equimolar amounts of bis(phenol-substituted) carboxylic acid or derivative thereof.

この態様において、最初2以上の第1級アミノ基を含有
する好ましいアルキレンポリアミン反応剤または他のア
ミン類を用いたときは、反応生成物は1個以上の残留第
1級アミノ基を含んでいる。また、好ましい線状アルキ
レンポリアミン類を用いたときは、アミンは2倍モル比
までのビス(フエノール置換)カルボン酸またはその誘
導体と反応する。得られた本発明の化合物は潤滑油添加
剤として有用であり、また、該化合物をさらに他の反応
剤と反応させて潤滑油添加剤として有用な誘導体とする
こI−もでAる一仔1レば−アミン景上γドビスし、公
知の方法にしたがつて、1以上の残留アミノ基はカルボ
ン酸と反応して、アミン塩、アミド、イミド、イミダゾ
リンを形成し、あるいは、アルデヒド、ケトンまたはそ
の混合物と反応し、あるいはアルデヒドとケトンの混合
物と反応してマンニツヒ塩基を形成する。また他の別法
として、アミンが適当モルのカルボン酸とまず反応して
残留第1級または第2級アミノ基を有するイミド、アミ
ドまたはアミン塩を生成し、ついでそのイミド、アミド
またはアミン塩がビス(フエノール置換)カルボン酸ま
たはその誘導体と反応する。
In this embodiment, when a preferred alkylene polyamine reactant or other amines initially containing two or more primary amino groups is used, the reaction product contains one or more residual primary amino groups. . Also, when using the preferred linear alkylene polyamines, the amine reacts with up to a two-fold molar ratio of bis(phenol-substituted) carboxylic acids or derivatives thereof. The resulting compounds of the present invention are useful as lubricating oil additives, and the compounds can also be further reacted with other reactants to give derivatives useful as lubricating oil additives. One or more residual amino groups react with a carboxylic acid to form an amine salt, amide, imide, imidazoline, or aldehyde, ketone, according to known methods. or mixtures thereof, or with mixtures of aldehydes and ketones to form Mannitz bases. Another alternative is to first react the amine with a suitable mole of carboxylic acid to form an imide, amide or amine salt with residual primary or secondary amino groups; Reacts with bis(phenol-substituted) carboxylic acids or their derivatives.

本発明の他の態様においては、アミンが1個の第1級ア
ミノ基を有するポリアミンで、それが、等モルのビス(
フエノール置換)カルボン酸またはその誘導体と反応す
る前または後に、アルキル置換基が8〜200個の炭素
原子を有するアルキル置換こはく酸またはその無水物と
反応する。そのような置換基は、イソブチレンまたはプ
ロピレンなどの比較的低分子量のオレフインまたはその
ようなオレフインのオリゴマ一の残基であるのが好まし
い。本発明の方法は、反応剤を一諸に加熱することによ
り容易に行なわれる。
In another embodiment of the invention, the amine is a polyamine having one primary amino group, and it is a polyamine having an equimolar amount of bis(
Before or after reacting with the phenol-substituted) carboxylic acid or its derivative, it is reacted with an alkyl-substituted succinic acid or its anhydride in which the alkyl substituent has from 8 to 200 carbon atoms. Preferably, such substituent is the residue of a relatively low molecular weight olefin, such as isobutylene or propylene, or an oligomer of such an olefin. The method of the invention is easily carried out by heating the reactants together.

好ましい反応温度は50〜250℃、好ましくは130
〜220℃、もつとも好ましくは180〜220℃であ
る。キシレン、トルエンまたは鉱油などの不活性溶媒を
用いてもよい。反応は大気に開放した容器で行なうのが
便利である。しかし、所望なら、真空下、低圧力下また
は窒素気流中で行なつてもよい。反応は通常1〜6時間
で完結し、もつとも普通には2〜4時間で終る。本発明
の化合物、その誘導体またはこれらの混合物を組成物全
重量に対して0.3〜15重量%、好ましくは1〜6重
量%の割合で潤滑油に添加することにより、潤滑油組成
物が得られる。
The preferred reaction temperature is 50-250°C, preferably 130°C.
The temperature is preferably 180 to 220°C, preferably 180 to 220°C. Inert solvents such as xylene, toluene or mineral oil may also be used. The reaction is conveniently carried out in a container open to the atmosphere. However, if desired, it may also be carried out under vacuum, low pressure or a stream of nitrogen. The reaction is usually completed in 1 to 6 hours, and most commonly in 2 to 4 hours. By adding the compound of the present invention, its derivative or a mixture thereof to the lubricating oil in a proportion of 0.3 to 15% by weight, preferably 1 to 6% by weight based on the total weight of the composition, the lubricating oil composition can be improved. can get.

かかる組成物には他の潤滑油添加剤を加えてもよく、添
加剤濃厚物、添加剤パツケージとすることもできる。用
いる潤滑油は、ジオクチルセバケートなどの公知の合成
エステル油のいずれでもよいが、周知のタイプの潤滑油
粘度を有する鉱油が好ましい。かかる潤滑油組成物にお
いては、ことに、ポリイソブチル基が分子量900〜2
000を有するポリイソブチルフエノールをグリオキシ
ル酸と反応させ、得られた中間体を平均4〜6個のアミ
ノ基を有するポリエチレンポリアミンと反応させ(反応
剤のモル比が1.0〜2.0:1:0.5〜1.0)で
得られる本発明の化合物を用いることがもつとも好まし
い。つぎに本発明を実施例をあげてさらに具体的に説説
明する。
Other lubricating oil additives may be added to such compositions and may also be in the form of additive concentrates, additive packages. The lubricating oil used may be any of the known synthetic ester oils such as dioctyl sebacate, but mineral oils having lubricating oil viscosities of known types are preferred. In such lubricating oil compositions, in particular, the polyisobutyl group has a molecular weight of 900 to 2.
000 is reacted with glyoxylic acid and the resulting intermediate is reacted with a polyethylene polyamine having an average of 4 to 6 amino groups (the molar ratio of the reactants is 1.0 to 2.0:1). :0.5 to 1.0) is preferably used. Next, the present invention will be explained in more detail with reference to Examples.

実施例 1 (a) PIBフエノールーグリオキシル酸中間体の調
製英国特許明細書第1446435号の実施例1記載の
分子量1000のポリイソブチレンから調製したポリイ
ソブチルフエノール6929(0.7モル)、グリオキ
シル酸1水化物64.49(0.7モル)およびp−ト
ルエンスルホン酸59をトルエン500meに溶解した
溶液を、窒素雰囲気下、デイーンおよびスターク(De
anおよびStark)水分離器にとりつけたフラスコ
中で水の発生がやむまで還流温度で加熱する(34蔵の
水を捕集)。
Example 1 (a) Preparation of PIB phenol-glyoxylic acid intermediate Polyisobutylphenol 6929 (0.7 mol) prepared from polyisobutylene of molecular weight 1000 as described in Example 1 of British Patent Specification No. 1446435, glyoxylic acid A solution of monohydrate 64.49 (0.7 mol) and p-toluenesulfonic acid 59 dissolved in 500 me of toluene was mixed with Deen and Stark under a nitrogen atmosphere.
an and Stark) Heat at reflux temperature in a flask attached to a water separator until water evolution ceases (34 volumes of water collected).

生じた溶液を蒸留し、溶媒を溜去して赤色の粘稠液75
09を得る。酸価=40巧KOH/9、ケン化価−96
mw.0(b)ジアミドの調製前記(a)項の生成物3
06.49をテトラエチレンペンタ ミン27.99と
混合し、窒素雰囲気下、200℃で4時間加熱する。
The resulting solution was distilled to remove the solvent and a red viscous liquid 75
Get 09. Acid value = 40 KOH/9, saponification value -96
mw. 0(b) Preparation of diamide Product 3 of section (a) above
06.49 is mixed with 27.99% of tetraethylenepentamine and heated at 200° C. for 4 hours under nitrogen atmosphere.

鉱油589で稀釈後、生成物を済過助剤を用いて淵過す
る。酸価=6Tf1fK0Y1/g(計算値0)、全ア
ルカリ価−52m7K0Yv9(計算値60)、窒素%
=2.3(計算値2.5)実施例 2 中間体を分離しない場合のジアミドの調製ポリイソブチ
ルフエノール8909(1.0モル)、グリオキシル酸
1水化物929(1.0モル)およびp−ト,ルエンス
ルホン酸79をトルエン600r11eに洛解した溶液
を、窒素雰囲気下、デイーンおよびスターク水分離器に
とりつけたフラスコ中で水の発生がやむまで環流温度で
加熱する(41meの水を捕集)。
After dilution with mineral oil 589, the product is filtered using filter aid. Acid value = 6Tf1fK0Y1/g (calculated value 0), total alkali value -52m7K0Yv9 (calculated value 60), nitrogen %
= 2.3 (calculated value 2.5) Example 2 Preparation of diamide without separation of intermediates Polyisobutylphenol 8909 (1.0 mol), glyoxylic acid monohydrate 929 (1.0 mol) and p- A solution of toluene sulfonic acid 79 in toluene 600r11e is heated at reflux temperature under a nitrogen atmosphere in a flask attached to a Dean and Stark water separator until water evolution ceases (41me of water is collected). ).

この溶液を数℃まで放冷し、ついでテトラエチレンペン
タミン94.59(0.5モル)を加える。溶媒溜去し
た後、該混合物を、窒素雰囲気下、200℃で4時間加
熱する。生成物を鉱油で稀釈した後、淵過する(収量1
819、理論的濃度85%)。酸価=12巧KO旦/9
(計算値0)、全アルカリ価−567n(VKOH/9
(計算値65)、窒素%=2.4(計算値2.7)実施
例 3〜11前記実施例2の一般的方法により、中間体
を分離することなく多くのアミド類が調製される。
This solution is allowed to cool to several degrees centigrade, and then 94.59 (0.5 mol) of tetraethylenepentamine is added. After evaporation of the solvent, the mixture is heated at 200° C. for 4 hours under a nitrogen atmosphere. The product is diluted with mineral oil and filtered (yield 1
819, theoretical concentration 85%). Acid value = 12 Takumi KOdan/9
(calculated value 0), total alkali number -567n (VKOH/9
(calc. 65), Nitrogen % = 2.4 (calc. 2.7) Examples 3-11 By the general method of Example 2 above, many amides are prepared without separation of intermediates.

一般的方法はつぎのとおりである。ポリイソブチルフエ
ノールおよびグリオキシル酸1水化物をトリエンまたは
キシレンに溶解し、p−トルエンスルホン酸(反応溶液
の重量に基づき、0.1%)を加え攪拌し、窒素雰囲気
下、デイーンおよびスターク分離器で水を捕集し、水の
発生が実質的にやむまで還流温度で加熱する。
The general method is as follows. Polyisobutylphenol and glyoxylic acid monohydrate were dissolved in triene or xylene, p-toluenesulfonic acid (0.1% based on the weight of the reaction solution) was added and stirred, and the mixture was purified in a Dean and Stark separator under a nitrogen atmosphere. The water is collected and heated at reflux temperature until water evolution substantially ceases.

この溶液を80〜100℃に冷却し、テトラエチレンペ
ンタアミン(TEPA)を加える。溶媒を溜去し、反応
を200℃で4時間継続させる。生成物を冷却し、鉱油
および石油エーテル(沸点62〜68℃)で稀釈し、淵
過助剤を用いて沢過する。170℃以下の温度で真空蒸
溜して石油エーテルを除去する。
Cool the solution to 80-100°C and add tetraethylenepentamine (TEPA). The solvent is distilled off and the reaction is continued at 200° C. for 4 hours. The product is cooled, diluted with mineral oil and petroleum ether (boiling point 62-68°C) and filtered using deep filter aid. The petroleum ether is removed by vacuum distillation at a temperature below 170°C.

収率は一般に少なくとも90%である。残りの酸価は低
く、最高7m7K0H/9である。さらに、該調製法の
詳細をつぎの第1表に示す。実施例10のチオビスPl
Bフエノール出発物質はつぎのように調製する:ポリイ
ソブチルフエノール(例えば、分子量1000PIB)
571.59(0.5モノ(ハ)を硫黄16.09(0
.5グラム原子)および水酸化ナトリウム4.09の存
在下、窒素雰囲気下、195℃で攪拌する。
Yields are generally at least 90%. The remaining acid values are low, up to 7m7K0H/9. Furthermore, details of the preparation method are shown in Table 1 below. Thiobis Pl of Example 10
The B phenol starting material is prepared as follows: polyisobutylphenol (e.g., molecular weight 1000 PIB)
571.59 (0.5 mono(c) to sulfur 16.09 (0
.. 5 grams atom) and 4.09 grams of sodium hydroxide at 195° C. under a nitrogen atmosphere.

硫化水素が発生し、その発生量は20時間後に著るしく
減少する。ついで反応を停止させ、生成物を石油エーテ
ル(沸点62〜68℃)で稀釈する。この溶液を水−メ
タノール(1:9)250r!Leで2回洗滌し、真空
蒸溜して溶媒を除去する。収量=5639(97%)、
硫黄%=1。5(計算値1.4) 実施例11のメチレン−ビス−PIBフエノール出発物
質はつぎのように調製される,:ポリイソブチルフエノ
ール(例えば、分子量1000PIB)102.6g(
0.1モル)、40%ホルマリン4.19(0.05モ
ル)、濃塩酸1m1およびトルエン60meの混合物を
攪拌し、デイーンおよびスターク水分離器中で3.9d
(計算値4.1r11e)の水が捕集されるまで還流温
度で加熱する(4時間)。
Hydrogen sulfide is generated and its amount decreases significantly after 20 hours. The reaction is then stopped and the product diluted with petroleum ether (boiling point 62-68°C). This solution was mixed with water-methanol (1:9) at 250 ml. Wash twice with Le and remove the solvent by vacuum distillation. Yield = 5639 (97%),
% Sulfur = 1.5 (calc. 1.4) The methylene-bis-PIB phenol starting material of Example 11 is prepared as follows: 102.6 g of polyisobutylphenol (e.g., 1000 PIB) (
0.1 mol), 40% formalin 4.19 (0.05 mol), 1 ml of concentrated hydrochloric acid and 60 me of toluene was stirred for 3.9 d in a Dean and Stark water separator.
Heat at reflux temperature until (calc. 4.1r11e) of water is collected (4 hours).

この溶液を13『C/20m7tLで真空蒸溜し生成物
を沢過する。収量=82f!、水酸価=58.2即KO
H/9(計算値54.5)実施例12〜17(参考例)
前記実施例3〜11(第1表)記載の方法で多くのTE
PAの重合体(モノアミド類)が調製される。
This solution was vacuum distilled at 13° C/20 m 7 tL and the product was filtered off. Yield = 82f! , hydroxyl value = 58.2 immediate KO
H/9 (calculated value 54.5) Examples 12 to 17 (reference example)
Many TEs were prepared by the methods described in Examples 3 to 11 (Table 1) above.
Polymers (monoamides) of PA are prepared.

これらはさらに他の反応体と反応し、こはく酸イミド類
、アミド類、マンニツヒ塩基およびシツフの塩基を形成
する。これらの調製法の詳細をつぎの第2表に示す。他
の反応体としてアルケニルこはく酸無水物を用いる場合
は、アミド化の最終段階で加え、生成物を稀釈および濾
過する前に、反応を200℃でチ時間継続させる。
These further react with other reactants to form succinimides, amides, Mannitz bases and Schiff bases. Details of these preparation methods are shown in Table 2 below. If alkenylsuccinic anhydride is used as the other reactant, it is added in the final step of amidation and the reaction is allowed to continue at 200° C. for an hour before diluting and filtering the product.

アミド/マンニツヒ塩基の混合物を調製するためには、
該アミドを冷却し、トルエンで再稀釈し、アルキルフエ
ノールを加え、40%ホルムアルデヒド(ホルマリン)
水溶液を90〜95℃で滴下する。
To prepare the amide/Mannitzig base mixture,
The amide was cooled, rediluted with toluene, alkylphenol added, and 40% formaldehyde (formalin) added.
Add the aqueous solution dropwise at 90-95°C.

この温度を1時間保持し、ついで溶液を還流温度で加熱
し、水をデイーンおよびスターク分離器中に除去する。
稀釈油を加えた後、前記のように、生成物を稀釈し、濾
過する。実施例 18〜25 ポリイソブチルフエノール(例えば、分子量1000P
1B)11439(0.1モル)をp−トルエンスルホ
ン酸2,0f1の存在下、デイーンおよびスターク分離
器中の水の捕集がやむまで(47d捕集)還流キシレン
800me中でグリオキシル酸1水化物92g(1.0
モル)と反応させる。
This temperature is maintained for 1 hour, then the solution is heated to reflux temperature and the water is removed into a Dean and Stark separator.
After adding the diluent oil, the product is diluted and filtered as described above. Examples 18-25 Polyisobutylphenol (e.g., molecular weight 1000P
1B) 11439 (0.1 mol) was dissolved in glyoxylic acid 1 hydrate in 800 me of refluxing xylene in the presence of p-toluenesulfonic acid 2,0 f 1 until water collection in the Dean and Stark separators ceased (47 d collection). 92g (1.0
mol).

ついで、溶媒を17『C以下の温度で真空蒸留して除去
する。生じた中間体を、第3表に詳記するように、つぎ
の一般的方法により、多くの種々のアミンと反応させる
:該中間体1189(0.1モル)を、窒素雰囲気下、
凝縮器をつけないフラスコ中で、゛発生する水を留去さ
せながら、200℃でアミンと共に攪拌する。
The solvent is then removed by vacuum distillation at a temperature below 17°C. The resulting intermediate is reacted with a number of different amines, as detailed in Table 3, by the following general method: The intermediate 1189 (0.1 mol) is reacted with a
In a flask without a condenser, stir with amine at 200° C. while distilling off the generated water.

生成物を鉱油で稀釈し85%濃度とし、石油エーテル(
沸点62〜68℃)で稀釈し、濾過助剤を用いて濾過し
、180℃以下で真空蒸留して溶媒を除去する。より揮
発性のアミン類の場合は、最初にやや異なつた方法を用
いる:(a)ジプロピレントリアミン(実施例19)の
場合、該反応剤を、先ず170〜180℃で0.5時間
、200℃で2時間、ついで凝縮器をはずして20『C
で2時間加熱還流する。
The product was diluted with mineral oil to a concentration of 85% and purified with petroleum ether (
The solution is diluted at a boiling point of 62-68°C), filtered using a filter aid, and the solvent is removed by vacuum distillation at a temperature below 180°C. For more volatile amines, a slightly different method is used initially: (a) For dipropylene triamine (Example 19), the reactants are first heated at 170-180° C. for 0.5 h at 200° C. ℃ for 2 hours, then remove the condenser and heat to 20℃.
Heat under reflux for 2 hours.

(b)エチレンジアミン(実施例20)の場合、該反応
剤を還流トルエン25d中で0.5時間加熱し、溶媒を
留去し、反応を200℃で4時間継続させる。
(b) In the case of ethylenediamine (Example 20), the reactants are heated in 25 d of refluxing toluene for 0.5 h, the solvent is distilled off and the reaction is continued at 200° C. for 4 h.

(c)ジメチルアミノプロピルアミン(実施例22)の
場合、100%過剰を用い、還流条件下、150℃で3
時間反応させ、過剰のアミンを21『C以下で留去し、
反応を200℃で4時間継続させる。
(c) For dimethylaminopropylamine (Example 22), 100% excess was used and 3
react for an hour, distill off excess amine at below 21°C,
The reaction is continued for 4 hours at 200°C.

実施例 26 油溶液中のアミンの調製 PIBフエノール(例えば、分子量1300PIB)1
31.7f1(0.1モル)、グリオキシル酸1水化物
4,6g(0.05モル)、p−トルエンスルホン酸0
.16gおよび鉱油25。
Example 26 Preparation of amine in oil solution PIB phenol (e.g. molecular weight 1300 PIB) 1
31.7f1 (0.1 mol), glyoxylic acid monohydrate 4.6 g (0.05 mol), p-toluenesulfonic acid 0
.. 16g and mineral oil 25g.

3gの混合物を窒素雰囲気下、140℃で1.5時間撹
拌する。
3 g of the mixture is stirred at 140° C. for 1.5 hours under nitrogen atmosphere.

発生した水は蒸発させる。混合物を80℃に放冷し、テ
トラエチレンペンタアミン9.59(0.05モル)を
加え、反応を200℃で4時間継続させる。最後に、生
成物を石油エーテル中に濾過する。窒素%=1.7(計
算値1.9)、TBN=49m銀0旦/実施例 27ポ
リイソブチルフエノール(例えば、分子量1000PI
B)267g(0.25モル)をp−トルエンスルホン
酸0.49の存在下、水の発生がやむまで還流トルエン
1507rLe中で、グリオキシル酸1水化物239(
0.25モル)と反応させる(12r11e捕集)。
The generated water is evaporated. The mixture is allowed to cool to 80°C, 9.59 (0.05 mol) of tetraethylenepentamine is added and the reaction is continued at 200°C for 4 hours. Finally, the product is filtered into petroleum ether. Nitrogen % = 1.7 (calculated value 1.9), TBN = 49m silver 0 days/Example 27 Polyisobutylphenol (e.g. molecular weight 1000PI
B) 267 g (0.25 mol) of glyoxylic acid monohydrate 239 (
0.25 mol) (12r11e collection).

テトラエチレンペンタアミン47.39(0.25モル
)を加え、トルエンを留去し、20『Cで4時間反応を
継続してテトラエチレンペンタアミンの重合体(モノア
ミド)を得る。ノニルフエノール110g(0.5モル
)を前記と同様にトルエン中でグリオキシル酸23g(
0.25モル)と別々に反応させ12dの水を捕集する
。このトルエン溶液をすでに生成したアミドに加え、ト
ルエンを留去し、再び反応を200℃で4時間継続させ
る。鉱油79.89を加え、生成物を石油エーテル洛液
に濾過する。溶媒を除去して油3969を得る。窒素%
=2.5(計算値3.1)、TBN=64m9K0H/
9、TAN=8m9K0旦/実施例28(参考例)PI
Bフエノール(例えば、分子量1000PIB)243
.59(0.22モル)およびノニルフエノール48.
49(0.22モル)の混合物を還流トルエン300r
11e中で、水の発生がやむまで(207rLe捕集)
グリオキシル酸40.59(0.44モル)と反応させ
る。
47.39 (0.25 mol) of tetraethylenepentamine was added, toluene was distilled off, and the reaction was continued at 20°C for 4 hours to obtain a polymer (monoamide) of tetraethylenepentamine. 110 g (0.5 mol) of nonylphenol was mixed with 23 g (23 g) of glyoxylic acid in toluene in the same manner as above.
0.25 mol) and collect 12d of water. This toluene solution is added to the amide already formed, the toluene is distilled off, and the reaction is continued again at 200° C. for 4 hours. Add 79.89 g of mineral oil and filter the product into petroleum ether. Removal of solvent gives oil 3969. nitrogen%
=2.5 (calculated value 3.1), TBN=64m9K0H/
9, TAN=8m9K0dan/Example 28 (Reference example) PI
B phenol (e.g. molecular weight 1000 PIB) 243
.. 59 (0.22 mol) and nonylphenol 48.
49 (0.22 mol) was refluxed in toluene at 300 r.
11e until water generation stops (207rLe collection)
React with 40.59 (0.44 mol) of glyoxylic acid.

テトラエチレンペンタアミン41.69(0.22モル
)を加え、トルエンを留去し、反応を200℃で4時間
継続させる。
41.69 (0.22 mol) of tetraethylenepentamine are added, the toluene is distilled off and the reaction is continued at 200° C. for 4 hours.

生成物を冷却し、鉱油61.69で稀釈し、石油エーテ
ル溶液中に濾過する。収量=353g、窒素%−3.6
(計算値3.6)、TBN=74m7K0H/9、TA
N=7巧KOH/9実施例 29 前記実施例1の方法と同様にして、ポリプロピルフエノ
ール(触媒として三フツ化ホウ素を用い、フエノールを
分子量860のポリプロピレンでアルキル化して調製)
100.49(0.04モル)をグリオキシル酸3.7
f!(0.02モノ(ハ)と反応させる。
The product is cooled, diluted with 61.69 g of mineral oil and filtered into petroleum ether solution. Yield = 353g, Nitrogen% -3.6
(calculated value 3.6), TBN=74m7K0H/9, TA
N=7 KOH/9 Example 29 Polypropylphenol (prepared by alkylating phenol with polypropylene having a molecular weight of 860 using boron trifluoride as a catalyst) in the same manner as in Example 1 above.
100.49 (0.04 mol) to glyoxylic acid 3.7
f! (React with 0.02 mono(c).

生した中間体506.9(0.01モル)をトリエチレ
ンテトラアミン0.73g(0.005モル)と共に2
00℃で4時間加熱する。
The resulting intermediate 506.9 (0.01 mol) was mixed with 0.73 g (0.005 mol) of triethylenetetraamine.
Heat at 00°C for 4 hours.

鉱油9.059を加え、生成物を石油エーテル溶液に濾
過し、最後に、180℃で真空蒸留する。窒素%=0.
4(計算値0.5)実施例 30 前記実施例1の一般的方法を用い、ポリブチル0−クレ
ゾール(触媒として三フツ化ホウ素を用い、o−クレゾ
ールを分子量1000のポリブテンでアルキル化して調
製)66.79(0.05モル)をキシレン溶液60m
e中でグリオキシル酸2.3g(0.025モル)と反
応させる。
9.059 g of mineral oil is added, the product is filtered into petroleum ether solution and finally distilled under vacuum at 180°C. Nitrogen%=0.
4 (calculated value 0.5) Example 30 Using the general method of Example 1 above, polybutyl o-cresol (prepared by alkylating o-cresol with polybutene having a molecular weight of 1000 using boron trifluoride as a catalyst) 66.79 (0.05 mol) in 60ml of xylene solution
2.3 g (0.025 mol) of glyoxylic acid in e.g.

この中間体27.29(0.01モル)をペンタエチレ
ンヘキサアミン1.169(0.005モル)と共に2
00℃で4時間攪拌する。
27.29 (0.01 mol) of this intermediate was combined with 1.169 (0.005 mol) of pentaethylenehexamine in 2
Stir at 00°C for 4 hours.

稀釈油4.959を加え、生成物を石油エーテル溶液中
に濾過する。窒素%=1.0(計算値1.3)、TBN
=20TI1fK0H/9実施例 31 ポリブチルフエノール,(例えば、分子量1000PI
B)194.39(0.17モル)、2−オキソグルタ
ール酸27.2f!(0.17モル)、石油工ーテル(
沸点80〜100′C)14077!11および水30
m1の混合物に攪拌、冷却しながら濃硫酸125!RL
eを加える。
Add 4.959 g of diluted oil and filter the product into petroleum ether solution. Nitrogen% = 1.0 (calculated value 1.3), TBN
=20TI1fK0H/9 Example 31 Polybutylphenol, (e.g., molecular weight 1000PI
B) 194.39 (0.17 mol), 2-oxoglutaric acid 27.2f! (0.17 mol), oil factory (
boiling point 80-100'C) 14077!11 and water 30
ml of concentrated sulfuric acid while stirring and cooling 125! R.L.
Add e.

この混合物を室温で6日間攪拌し、さらに石油エーテル
で稀釈し、水−メタノール(1:9)200dで3回洗
滌する。160℃で真空蒸留して酸1489を得る。
The mixture is stirred at room temperature for 6 days, further diluted with petroleum ether and washed three times with 200 d of water-methanol (1:9). Vacuum distillation at 160° C. gives acid 1489.

ケン化価=20.4WIK0H/9前記の酸709を過
剰のテトラエチレンペンタミン109と共に200℃で
4時間加熱する。
Saponification number=20.4WIK0H/9 The above acid 709 is heated with excess tetraethylenepentamine 109 at 200° C. for 4 hours.

この混合物を冷却し、稀釈油139および石油エーテル
300meを加え、この溶液を水一メタノール(1:9
)40r11eで2回洗滌する。真空蒸留して生成物8
29を得る。窒素%=1.0、TBN=29WiK0H
/9実施例 32(参考例) 前記実施例26の生成物100,09(0.03モル)
をイソステアリン酸8.5g(0.03モル)と共に2
00℃で4時間加熱する。
The mixture was cooled, diluted oil 139 and petroleum ether 300 me were added, and the solution was dissolved in water-methanol (1:9
) Wash twice with 40r11e. Vacuum distillation produces product 8
Get 29. Nitrogen%=1.0, TBN=29WiK0H
/9 Example 32 (Reference Example) Product 100.09 (0.03 mol) of Example 26 above
with 8.5 g (0.03 mol) of isostearic acid.
Heat at 00°C for 4 hours.

酸価が低下し(5巧KOH/9)、TBNが49〜36
m(IKOH/9に低下すると反応はおおむね完了する
Acid value decreases (5 KOH/9), TBN is 49-36
m(IKOH/9), the reaction is almost complete.

実施例 33 ポリイソブチルフエノール(例えば、分子量1000P
IB)69.39(0.07モル)、ピルビン酸6.2
f1(0.07モノ(ハ)およびp−トルエンスルホン
酸19をキシレンに溶解した溶液を水の発生がやむまで
(3.2me捕集)、還流条件下、沸騰させる。
Example 33 Polyisobutylphenol (e.g. molecular weight 1000P
IB) 69.39 (0.07 mol), pyruvic acid 6.2
A solution of f1 (0.07 mono(ha)) and p-toluenesulfonic acid 19 dissolved in xylene is boiled under reflux conditions until the generation of water stops (3.2 me collection).

この溶液を濾過し、真空蒸留して溶媒を除去し酸中間体
を得る。この中間体23.49(0,022モノ(ハ)
をテトラエチレンペンタアミン4.17g(0.022
モノ(ハ)と共に200℃で4時間加熱する。
The solution is filtered and vacuum distilled to remove the solvent and yield the acid intermediate. This intermediate 23.49 (0,022 mono(c)
4.17g (0.022g) of tetraethylenepentamine
Heat with mono (c) at 200°C for 4 hours.

稀釈油4.769を加え、生成物を石油エーテル中に濾
過する。窒素%=2.3、TBN=72mvK0H/f
l実施例 34前記実施例33の方法と同様に、ポリブ
チルフエノール(例えば、分子量1000PIB)11
4.3g(0.1モル)をp−トルエンスルホン酸0.
29の存在下、ピルビン酸4.49(0.05モル)と
反応させる。
Add 4.769 g of diluted oil and filter the product into petroleum ether. Nitrogen%=2.3, TBN=72mvK0H/f
l Example 34 Similar to the method of Example 33 above, polybutylphenol (e.g., molecular weight 1000 PIB) 11
4.3 g (0.1 mol) of p-toluenesulfonic acid.
4.49 (0.05 mol) of pyruvate in the presence of 29.

中間体は分離しない。テトラエチレンペンタアミン4.
739(0.025モル)を加え、溶媒を留去し、反応
を4時間継続させ、アミンを鉱油21.4gで稀釈し、
常法により濾過する。
Intermediates do not separate. Tetraethylenepentaamine4.
739 (0.025 mol) was added, the solvent was distilled off, the reaction was continued for 4 hours, the amine was diluted with 21.4 g of mineral oil,
Filter by conventional method.

収量=128f!、窒素%=1.1(計算値1.1)、
TBN=31m7K0H/9実施例 35ポリイソブチ
ルフエノール(例えば、分子量650PIB)87,5
9(0.1モル)、グリオキシル酸1水化物4.69(
0.05モル)およびp−トルエンスルホン酸0.16
9をキシレン807neに溶解した溶液を水の発生がや
むまで(1.9771e捕匍、還流温度で加熱する。
Yield = 128f! , nitrogen %=1.1 (calculated value 1.1),
TBN=31m7K0H/9 Example 35 Polyisobutylphenol (e.g. molecular weight 650PIB) 87.5
9 (0.1 mol), glyoxylic acid monohydrate 4.69 (
0.05 mol) and p-toluenesulfonic acid 0.16
A solution of 9 in xylene 807ne is heated at reflux temperature until the evolution of water stops (1.9771e).

放冷後、テトラエチレンペンタアミン4.739(0.
025モル)を加え、キシレンを留去し、混合物を、窒
素雰囲気下、200℃で4時間加熱する。
After cooling, tetraethylenepentamine 4.739 (0.
025 mol) is added, the xylene is distilled off and the mixture is heated at 200° C. for 4 hours under a nitrogen atmosphere.

生成物を鉱油16.69で稀釈して、石油工ーテル溶媒
中に濾過する。収量−1049、窒素%=1.8(計算
値1.5)本発明の生成物を潤滑油の無灰分分散剤とし
て使用する場合の適性をMS,ClヘッダーAV−Bエ
ンジンテスト、パネルコーカーテストおよびスポツトテ
ストにより調べた。
The product is diluted with 16.69 g of mineral oil and filtered into petroleum ether solvent. Yield - 1049, Nitrogen % = 1.8 (calculated value 1.5) The suitability of the product of the present invention for use as an ashless dispersant in lubricating oils was determined by MS, Cl header AV-B engine test, panel coker test. and a spot test.

Cテストは供試添加剤を含む2つの配合について、標準
法により行なつた。
The C test was conducted using standard methods on two formulations containing the test additives.

配合Aば市販の有用なスルホン酸金属清浄剤、粘度指数
改良剤および抗酸化剤/抗摩耗添加剤を含有する米国規
格MIL−L46l52に適合するように配合した10
W/30混合物で、通常含有する無灰分分散剤4.5%
を同量の供試添加剤でおきかえてある。
Formulation A is a commercially available sulfonic acid metal detergent formulated to meet US Standard MIL-L46152 containing a viscosity index improver and an antioxidant/anti-wear additive.
W/30 mixture typically contains 4.5% ashless dispersant
was replaced with the same amount of the test additive.

該混合物は硫酸塩灰分含量1%である。配合Bは前記配
合Aと同様であるが、硫酸塩灰分含量が0.5%で、無
灰分腐蝕防止剤を含有している。
The mixture has a sulfate ash content of 1%. Formulation B is similar to Formulation A above, but has a sulfate ash content of 0.5% and contains an ashless corrosion inhibitor.

テストの後、常法により、エンジンの状態に従い価値の
等級を付した。
After the test, the value was graded according to the condition of the engine according to the conventional method.

これらの等級はつぎのとおりである。付記した以外は、
全て供試添加剤の濃度は4.5%である。
These grades are as follows. Except as noted,
The concentration of all additives tested was 4.5%.

添加剤Xはポリイソブチルフエノールのマンニツヒ塩基
のホウ素化物からなる市販の有用な無灰分分散剤である
。ヘッダーAV−Bエンジンテストは常法に従つて行な
い、テスト後、テストエンジンの種々の部品の状態に従
い、常法により価値の等級(最高10)を付した。
Additive X is a useful commercially available ashless dispersant consisting of a boronated Mannitz base of polyisobutylphenol. Header AV-B engine tests were conducted according to conventional methods, and after testing, a value rating (maximum 10) was assigned according to the condition of the various parts of the test engine.

また、テストエンジンの溝におけるカーボンの付着を測
定した。溝のカーボンおよび全価値等級(最高100)
はつぎのとおりである:AV−Bテストに用いた試料混
合物は市販の有用なスルホン酸金属清浄剤、腐蝕防止剤
および抗酸化剤/抗摩耗添加剤を含有し、米国規格MI
L− L − 2104Cに適合するように配合したS
AE3O混合物で、付記した以外は通常含有する無灰分
分散剤3.5%を同量の供試添加剤でおきかえてある。
Carbon adhesion in the grooves of the test engine was also measured. Groove carbon and full value grade (up to 100)
The sample mixture used for the AV-B test contained commercially available useful sulfonate metal detergents, corrosion inhibitors and antioxidant/anti-wear additives, and was compliant with American Standard MI.
S formulated to comply with L-L-2104C
In the AE3O mixture, the 3.5% ashless dispersant normally contained was replaced with the same amount of the test additive, except as noted.

パネルコーカーテストはAV−Bテストに用いた同じ試
料混合物を用いて、通常の装置を少し改良して3.5時
間行なつた。
The panel coker test was run for 3.5 hours using the same sample mixture used in the AV-B test, using conventional equipment with minor modifications.

連続的に油をはねとばす代りに、油を600’Fに保持
したアルミニウム板に対し、45秒間隔で、15秒間ず
つはねとばした。さらに装置を改良し、油だめを通して
油表面の上部に2.31/時間の割合で湿潤空気を通気
させた。通常油中に浸漬していない油だめの部分につい
て、キヤタピラ1−Gテスト後のエンジンピストンに等
級を付すと同じ方法で清浄さの%に従つて価値の等級%
を付した(100=完全清浄)。このテストはキヤタピ
ラ1−Gエンジンテストとよく相関すると考えられる。
得られた等級はつぎのとおりである:スポツトテストに
おいては、供試添加剤を鉱油( V2,O= 3.5c
S)に4%溶解した。
Instead of continuously splashing the oil, the oil was splashed for 15 seconds at 45 second intervals against an aluminum plate held at 600'F. The equipment was further modified to vent humid air through the oil sump and above the oil surface at a rate of 2.31/hour. For parts of the sump that are not normally immersed in oil, the value grade % according to the % cleanliness in the same way that engine pistons are graded after the Caterpillar 1-G test.
(100=completely clean). This test is believed to correlate well with the Caterpillar 1-G engine test.
The grades obtained are as follows: In the spot test, the test additive was mixed with mineral oil (V2, O = 3.5c
4% dissolved in S).

カーボンブラツク(SpherOn9、例えば、Cal
OtCarbOnCOy、平均粒子径27mμ)1%を
加え、該混合物10gを5インチ×1インチ試験管中で
超音波発生器を用い1時間撹拌した。ついでこの試験管
を50℃に16時間貯蔵し、放冷した。試験管の上部0
.5インチから採取した油滴を細いガラス棒を用いてク
ロマトグラフイー用紙にスポツトした。ついでスポツト
を24時間展開させつぎのとおり等級を付した。
Carbon black (SpherOn9, e.g. Cal
1% of OtCarbOnCOy (average particle size 27 mμ) was added, and 10 g of the mixture was stirred for 1 hour using an ultrasonic generator in a 5 inch x 1 inch test tube. The test tube was then stored at 50° C. for 16 hours and allowed to cool. top of test tube 0
.. A drop of oil taken from a 5-inch tube was spotted onto chromatography paper using a thin glass rod. The spots were then developed for 24 hours and graded as follows.

A=カーボンが充分分散 B=カーボンが適度に分散 c=カーボンがわずかに分散 D=カーボンが分散しないA = Carbon is sufficiently dispersed B = Carbon is moderately dispersed c = carbon slightly dispersed D = Carbon does not disperse

Claims (1)

【特許請求の範囲】 1 (a)少なくとも30個の炭素原子を有するポリブ
チル、ポリイソブチルまたはポリプロピル置換基を有す
る置換フェノールを、グリオキシル酸、ピルビン酸およ
び2−オキソグルタール酸からなる群から選ばれるカル
ボニル置換化合物と、モル比1.0〜2.0:1.0に
て還流温度で、水を留去しながら反応させてビス(フェ
ノール置換)カルボン酸を形成させ、ついで、(b)こ
のビス(フェノール置換)カルボン酸を、50〜250
℃で、N−アミノエチルエタノール、ビス−アミノプロ
ピルピペラジン、ビス−ヘキサメチレントリアミン、ジ
プロピレントリアミン、ジメチルアミノプロピルアミン
、エチレンポリアミンおよびエチレンポリアミンとジシ
アンジアミドとの反応生成物からなる群から選ばれるア
ミン0.5〜1.0モルと反応させること、を特徴とす
る式: ▲数式、化学式、表等があります▼ 〔式中、各R^1は同一または異なつて、少なくとも3
0個の炭素原子を有するポリイソブチルまたはポリプロ
ピル、R^2は無しか、または式:▲数式、化学式、表
等があります▼(式中、mは0または整数、R^1は前
記と同じ、R^5および▲数式、化学式、表等がありま
す▼は後記と同じ)で示される基、R^4は水素、メチ
ルまたは式:▲数式、化学式、表等があります▼(式中
、Zは硫黄またはメチレン、R^1は前記と同じ)で示
される基、各R^5は同一または異なつて、水素、メチ
ルまたは▲数式、化学式、表等があります▼で示される
基、各▲数式、化学式、表等があります▼は同一または
異なつてアミド基を意味する〕で示される化合物の製法
Claims: 1. (a) a substituted phenol having polybutyl, polyisobutyl or polypropyl substituents having at least 30 carbon atoms selected from the group consisting of glyoxylic acid, pyruvic acid and 2-oxoglutaric acid; with a carbonyl-substituted compound in a molar ratio of 1.0 to 2.0:1.0 at reflux temperature while distilling off water to form a bis(phenol-substituted) carboxylic acid, and then (b) This bis(phenol-substituted) carboxylic acid has a concentration of 50 to 250
0 C, an amine selected from the group consisting of N-aminoethylethanol, bis-aminopropylpiperazine, bis-hexamethylenetriamine, dipropylenetriamine, dimethylaminopropylamine, ethylene polyamine and the reaction product of ethylene polyamine with dicyandiamide. A formula characterized by reacting with .5 to 1.0 mol: ▲There are mathematical formulas, chemical formulas, tables, etc.▼ [In the formula, each R^1 is the same or different, and at least 3
Polyisobutyl or polypropyl with 0 carbon atoms, R^2 is absent or formula: ▲ Numerical formula, chemical formula, table, etc. ▼ (where m is 0 or an integer, R^1 is the same as above) , R^5 and ▲There are mathematical formulas, chemical formulas, tables, etc. ▼ is the same as below), R^4 is hydrogen, methyl, or the formula: ▲There are mathematical formulas, chemical formulas, tables, etc.▼ (In the formula, Z is sulfur or methylene, R^1 is the same as above), each R^5 is the same or different, hydrogen, methyl, or a ▲ mathematical formula, chemical formula, table, etc. A group represented by ▼, each ▲ mathematical formula , chemical formulas, tables, etc. ▼ means the same or different amide group] Method for producing the compound shown.
JP49044348A 1973-04-19 1974-04-18 Manufacturing method for lubricating oil additives Expired JPS5918402B2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB1917373A GB1459403A (en) 1973-04-19 1973-04-19 Lubricant additives their preparation and compositions containing them
GB1917373 1973-04-19

Publications (2)

Publication Number Publication Date
JPS5030905A JPS5030905A (en) 1975-03-27
JPS5918402B2 true JPS5918402B2 (en) 1984-04-27

Family

ID=10124960

Family Applications (1)

Application Number Title Priority Date Filing Date
JP49044348A Expired JPS5918402B2 (en) 1973-04-19 1974-04-18 Manufacturing method for lubricating oil additives

Country Status (14)

Country Link
JP (1) JPS5918402B2 (en)
AR (1) AR205535A1 (en)
AT (1) AT346309B (en)
BE (1) BE813916A (en)
BR (1) BR7403100D0 (en)
CA (1) CA1042454A (en)
CH (1) CH605683A5 (en)
DE (1) DE2418760A1 (en)
FR (1) FR2226416B1 (en)
GB (1) GB1459403A (en)
IT (1) IT1012586B (en)
NL (1) NL7405266A (en)
SE (1) SE7405242L (en)
ZA (1) ZA742476B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102004005108A1 (en) 2004-02-02 2005-10-27 Basf Ag Process for the preparation of polyisobutenylphenols

Also Published As

Publication number Publication date
GB1459403A (en) 1976-12-22
AT346309B (en) 1978-11-10
FR2226416A1 (en) 1974-11-15
IT1012586B (en) 1977-03-10
FR2226416B1 (en) 1978-10-27
DE2418760A1 (en) 1974-11-07
ATA320274A (en) 1978-03-15
BE813916A (en) 1974-08-16
NL7405266A (en) 1974-10-22
CH605683A5 (en) 1978-10-13
BR7403100D0 (en) 1974-11-19
ZA742476B (en) 1975-12-31
CA1042454A (en) 1978-11-14
AU6805674A (en) 1975-10-23
JPS5030905A (en) 1975-03-27
AR205535A1 (en) 1976-05-14
SE7405242L (en) 1974-10-21

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