JPH01502193A - Propoxylated Guerbet alcohol and its esters - Google Patents

Propoxylated Guerbet alcohol and its esters

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Publication number
JPH01502193A
JPH01502193A JP63501592A JP50159288A JPH01502193A JP H01502193 A JPH01502193 A JP H01502193A JP 63501592 A JP63501592 A JP 63501592A JP 50159288 A JP50159288 A JP 50159288A JP H01502193 A JPH01502193 A JP H01502193A
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Japan
Prior art keywords
group
acid
compound according
product
alcohol
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.)
Pending
Application number
JP63501592A
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Japanese (ja)
Inventor
オッレニック・ジュニア・アンソニー・ジェー
ビルボ・レイモンド・イー
Original Assignee
ジーエーエフ・コーポレーション
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Priority claimed from US07/011,771 external-priority patent/US4731190A/en
Application filed by ジーエーエフ・コーポレーション filed Critical ジーエーエフ・コーポレーション
Publication of JPH01502193A publication Critical patent/JPH01502193A/en
Pending legal-status Critical Current

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Abstract

(57)【要約】本公報は電子出願前の出願データであるため要約のデータは記録されません。 (57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 プロポキシル化 ゲルベ アルコールおよびそのエステル本発明は一つの面にお いてゲルベ(guerbet)アルコールから誘導した新規な化合物に関するも のである。別の面において前記新規な化合物の製造方法に関するものであり、他 の面において前記新規な化合物を含有する組成物および該組成物を潤滑剤として 使用することに関するものである。[Detailed description of the invention] Propoxylated Guerbet alcohol and its ester The present invention has one aspect. Regarding novel compounds derived from guerbet alcohol. It is. Another aspect relates to a method for producing the novel compound, and others. A composition containing the novel compound and the composition as a lubricant It is about using.

発明の背景 鉱油または不飽和脂肪油のような水不溶性油は冷却効率の観点から金属加工用に 完全に受け入れられている訳ではないことはよく知られている。フリス(Fli s)の米国特許第3、929.656号(1975年12月30日)のような初 期の特許は鉱油60〜90%、不飽和脂肪油5〜30%およびパラフィン油3〜 15%からなる系に基づく代表的な油を開示している。このような油を主成分と するエマルジョン型潤滑剤はアルミニウムの熱間圧延、絞り成型およびアイアニ ング(ironing)によるアルミニウム缶の製造、鋼の冷間圧延などを包含 する塑性変形処理に従来から使用されている。これらの従来のエマルジョンは乳 化剤として陰イオン石鹸、非イオン界面活性剤例えばアルコキシ化アルコールの ソルビトールエステル、および他の添加剤を含有している。これらの処理に使用 される生成物の代表的なものは周囲温度において液体であり、所要の潤滑特性を 付与するような高い分子量を有する。効果が大きくて液体である潤滑性物質を得 るのに、興味ある生成物はオレイン酸、レルン酸、およびトール油酸のような不 飽和疎水性物質に基づいている。スギャの米国特許第3.945.930号(1 976年3月23日)は非イオン脂肪酸エトキシレートおよび油溶性不飽和脂肪 トリグリセリドとリン酸エステル腐食防止剤とからなる代表的なエマルジョン系 を開示している。米国特許第4.042.515号および同第4.075.39 3号には金属潤滑用エマルジョン系に使用されるダイマー酸不飽和脂肪酸エステ ルが記載されている。Background of the invention Water-insoluble oils such as mineral oils or unsaturated fatty oils are preferred for metalworking due to their cooling efficiency. It is well known that it is not completely accepted. Fli No. 3,929,656 (December 30, 1975) The period patent covers 60-90% mineral oil, 5-30% unsaturated fatty oil and 3-30% paraffin oil. A representative oil based on a system consisting of 15% is disclosed. This kind of oil is the main ingredient Emulsion type lubricants are used for hot rolling, drawing and ironing of aluminum. Includes manufacturing of aluminum cans by ironing, cold rolling of steel, etc. It has been traditionally used for plastic deformation processing. These traditional emulsions are milk anionic soaps, nonionic surfactants such as alkoxylated alcohols, Contains sorbitol esters, and other additives. used for these processes Typical products are liquids at ambient temperature and exhibit the required lubricating properties. It has such a high molecular weight. Obtain a lubricating substance that is highly effective and is a liquid. However, the products of interest are oleic acid, leruric acid, and tall oil acid. Based on saturated hydrophobes. Sugya U.S. Patent No. 3.945.930 (1 March 23, 976) are nonionic fatty acid ethoxylates and oil-soluble unsaturated fats. Typical emulsion system consisting of triglyceride and phosphate ester corrosion inhibitor is disclosed. U.S. Patent Nos. 4.042.515 and 4.075.39 No. 3 contains dimer acid unsaturated fatty acid ester used in emulsion systems for metal lubrication. is listed.

予め成形したアルミニウムに疎水性コーティングを被着させることは米国特許第 4.243.537号、同第4.362.634号および同第4.581.15 2号に記載されており、この際に水分散性不飽和脂肪酸アルコキシレートおよび アルカノールアミン石鹸が絞り成形用化合物(drawing compoun d)中に使用されている。Applying a hydrophobic coating to preformed aluminum is covered by U.S. Patent No. 4.243.537, 4.362.634 and 4.581.15 No. 2, in which water-dispersible unsaturated fatty acid alkoxylates and Alkanolamine soap is a drawing compound. d) used in

上述の物質は潤滑剤として可成り良好に作用するが、酸化され悪臭を発生する。The above-mentioned substances act fairly well as lubricants, but they oxidize and give off bad odors.

また、所望の流動性にとって必要な二重結合が酸化して低分子量アルデヒド、ケ トンおよび縮合生成物を生成し、これらの生成物は反応して副生物を生成し、不 都合な色、臭および味を与える。ppm程度の僅かな微小濃度において副生物に よって生じるこれらの有害な結果は、繰返し洗浄した後でも残る。このような不 都合な性質は、製造処理中にこのような合成潤滑剤を使用して成形した金属容器 内に飲料または他の食料品を充填する用途では、特に受け入れることができない 。醸造工業では最近になって金属容器の製造中に合成潤滑剤として使用される物 質に対して3■/gのKOHの沃素価で示される最大不飽和レベルを採用した。Additionally, the double bonds necessary for the desired fluidity may be oxidized to form low molecular weight aldehydes, ton and condensation products, and these products react to produce by-products and Provides a pleasant colour, odor and taste. At a very small concentration of ppm, it becomes a by-product. These harmful consequences therefore remain even after repeated cleaning. Such failure Advantageous properties include molded metal containers using such synthetic lubricants during the manufacturing process. Particularly unacceptable for filling beverages or other foodstuffs . In the brewing industry, synthetic lubricants have recently been used as synthetic lubricants during the manufacture of metal containers. The maximum unsaturation level indicated by the iodine value of KOH of 3/g was taken for the quality.

従って、本発明の目的は上述の潤滑剤の欠点を克服し、金属成形中の潤滑のため に好都合で有効な経済的方法を提供することにある。Therefore, the object of the present invention is to overcome the drawbacks of the above-mentioned lubricants and to provide a suitable solution for lubrication during metal forming. The objective is to provide a convenient and effective economical method for

本発明の他の目的は優れた潤滑特性および低い不飽和レベルを有する一群の化合 物を提供することにある。Another object of the invention is to provide a group of compounds with excellent lubrication properties and low unsaturation levels. It's about providing things.

本発明の他の目的は金属加工に適当な温度において流動性を保持する比較的高分 子量の潤滑剤を提供することにある。Another object of the present invention is to provide a relatively high-quality material which retains fluidity at temperatures suitable for metal processing. The objective is to provide a small amount of lubricant.

本発明のさらに他の目的はアルミニウム缶および金属薄板の製造に特に有用な潤 滑剤組成物を提供することにある。Yet another object of the invention is to provide a lubricant particularly useful in the manufacture of aluminum cans and sheet metal. An object of the present invention is to provide a lubricant composition.

発明 本発明においては、次式: (式中のRおよびR1はそれぞれ別個に1〜20個の炭素原子を有するアルキル 基を示し、かつR+R’の全炭素原子数は4個以上であり;yは1〜20の数を 示し:整数Xと整数2との和はO〜20であり;R2は水素原子、アルキル基ま たは−COR3基を示し、かつR3は水素原子、未置換のアルキル基またはアル ケニル基、あるいはカルボキシル基、COR’基または次式: で表わされるシクロヘキセニル基で置換されたアルキル基またはアルケニル基を 示し、かつmは1〜3の数を示し:nはθ〜10の数を示し:pおよびrはそれ ぞれθ〜1の数を示し:R3は水酸基または次式: で表わされるアルコキシル化ゲルベ基を示し:Rsは1〜10個の炭素原子を有 するアルキル基またはアルケニル基を示す)で表わされるプロポキシル化ゲルベ  アルコールおよびそのエステルを提供する。これらの化合物は純粋な状態にお いて単独あるいは混合物の形態で潤滑剤として使用することができ、また鉱油、 水、アルコキシル化または未アルコキシル化パラフィン油およびエステルなどの ような不活性溶媒を含有する組成物に配合することができる。また、潤滑剤組成 物は式Aで表わされるゲルベ誘導体化合物の全体に対して50重量%以下の未反 応ゲルベ アルコールおよびカニツァロ石鹸副生物を含有することができる。invention In the present invention, the following formula: (wherein R and R1 are each independently an alkyl group having 1 to 20 carbon atoms) group, and the total number of carbon atoms of R + R' is 4 or more; y is a number from 1 to 20; Indication: The sum of integer X and integer 2 is O~20; R2 is a hydrogen atom, an alkyl group, or or -COR3 group, and R3 is a hydrogen atom, an unsubstituted alkyl group, or an alkyl group. Kenyl group, carboxyl group, COR' group or the following formula: An alkyl group or alkenyl group substituted with a cyclohexenyl group represented by and m represents a number from 1 to 3: n represents a number from θ to 10: p and r represent that Each represents the number of θ to 1: R3 is a hydroxyl group or the following formula: represents an alkoxylated Guerbet group represented by: Rs has 1 to 10 carbon atoms; (indicating an alkyl or alkenyl group) Provides alcohol and its esters. These compounds are in their pure state. It can be used as a lubricant alone or in the form of a mixture, and mineral oil, such as water, alkoxylated or unalkoxylated paraffin oils and esters. It can be blended into a composition containing an inert solvent such as. Also, lubricant composition The substance contains less than 50% by weight of the Guerbet derivative compound represented by formula A. It may contain guerbet alcohol and Cannizzaro soap by-products.

式Aで表わされる化合物は7未満、好ましくは2未満の沃素価で示される低い不 飽和度を有する化合物である。本発明化合物のうち最も好ましいものは不飽和を 有していない化合物およびほぼ零の沃素価を有する化合物である。本発明化合物 中にプロピレンオキシドが存在しているのは重要なことである。その理由は、プ ロピレンオキシドが潤滑剤に所要の高い流動性を与え、周囲温度およびこれより 低い温度において液体状態を保持させるからである。このように、プロピレンオ キシド(PO)単位の存在は、エチレンオキシド(EO)のみでアルコキシル化 されたゲルベ誘導体生成物に有意により大きい流動性を付与する。EO単位およ びPO単位は主としてブロック状に分布して存在しているが、重合体鎖中に間隔 をおいてランダムに存在させることができる。金属成形の際に使用するのに好ま しい化合物は有意量のP口単位を含有する化合物である。The compounds of formula A have a low impurity value with an iodine value of less than 7, preferably less than 2. It is a compound with a degree of saturation. The most preferred compounds of the present invention have unsaturation. Compounds that have no iodine value and compounds that have an iodine value of almost zero. Compound of the present invention The presence of propylene oxide in it is important. The reason is that Lopylene oxide gives the lubricant the required high fluidity and allows it to withstand ambient temperatures and above. This is because it maintains a liquid state at low temperatures. In this way, propylene oil The presence of oxide (PO) units indicates that alkoxylation occurs only with ethylene oxide (EO). impart significantly greater fluidity to the purified Guerbet derivative product. EO units and Although the PO units are mainly distributed in blocks, there are intervals in the polymer chain. can be made to exist randomly. Preferred for use in metal forming New compounds are those containing significant amounts of P units.

以下に特記しない限り温度は℃で示し、パーセントおよび比は重量基準で示し、 圧力はkg/cm”絶対圧(psia)で示す。ゲルベ アルコールはベーター 炭素原子に分枝を有する化合物で、次式: (式中のRおよびR1は上述のものと同一のものを示す)で表わされる。Unless otherwise specified below, temperatures are given in °C and percentages and ratios are given by weight; Pressure is expressed in kg/cm" absolute pressure (psia). Guerbet alcohol is beta A compound having a branch on a carbon atom, with the following formula: (R and R1 in the formula are the same as those described above).

本発明の好適な生成物は、RおよびR’が6〜15個の炭素原子を有するアルキ ル基を示し;yが1〜lOの数、最も好ましくは2〜8の数を示し; X+Zの 合計が2〜20の数、最も好ましくは4〜10の数を示し;沃素価で示される化 合物の不飽和度が2未満である化合物である。大部分の場合に、20部分が優位 を占めることはできないが、20部分の存在は化合物における流動性、洗浄性お よび耐酸化性にとって重要である。また、上述の式Aにおいて、R2が有機基を 示し、この基が4個以上の炭素原子を有するのが好ましい。Preferred products of the invention are alkyl radicals in which R and R' have from 6 to 15 carbon atoms. represents a group; y represents a number of 1 to 1O, most preferably a number of 2 to 8; represents a number whose sum is from 2 to 20, most preferably from 4 to 10; A compound whose degree of unsaturation is less than 2. In most cases, the 20 part is dominant However, the presence of the 20-moiety improves the fluidity, detergency, and important for oxidation resistance and oxidation resistance. Furthermore, in the above formula A, R2 represents an organic group. and preferably this group has 4 or more carbon atoms.

上述のように、本発明化合物は単独または配合物として、金属容器の成形、自動 車の計器板の流し込成型、特にRIM法による自動車のバンパーの成形、および ゴムタイヤの流し込成型のような、金属、熱可塑性プラスチックおよびゴム材料 の成形、流し体成形および押出成形に使用することができる。容器を成形する際 に伴われる操作としては、カッピング(cupping) 、キャンニング(c anning) 、圧延、鍛造、アイアニング、絞り成形、波形加工(wrin kling)などがある。これらの操作のすべてにおいて、本発明化合物は外部 潤滑剤として作用し、変形を受ける金属あるいは熱可塑性プラスチックまたはゴ ムを注入する成形型に塗布して成形品を迅速かつ清浄に脱型させることができる 。熱可塑性プラスチックおよびゴムを流し体成形する際のこのような操作に使用 する場合の本発明化合物の利点は、本発明化合物が外部でその作用を行いかつ金 型基板に直接付着させることができることである。従って、流し込成形品を脱型 するための液体組成物に異質の汚染性添加剤を添加する必要がない。一般的に、 上述の範囲内の下限に近い部分におけるアルコキシル化がプラスチックおよびゴ ムの流し体成形に有利であることが分った。゛ 金属容器、特にアルミニウム缶を形成する一例では、潤滑剤は親水性と親油性と が平衡している組成を有するエマルジョンを形成するアルコール混合物からなる 。例えば、このようなマルマジョンは、20%以上のEOを含有する水溶性アル コキシル化ゲルベ アルコール約10〜約60%と、油溶性アルコキシル化ゲル ベ アルコール約10〜約40%と、未アルコキシル化ゲルベ アルコール約O 〜約20%トヲ組み合わせることにより生成する。この混合物は鉱油を含有して いない低粘度および高被洗浄性(rinsability)を有する系を提供す る。親水性と親油性との比率(HLB)が大きい場合には、この物質は水溶性で あるが、小さいHLBは油溶性物質であることを示す、肛BをEO混入量によっ て変えて水に対する溶解度を変えることができる。As mentioned above, the compounds of the present invention, alone or as a combination, can be used for molding metal containers, automatic Cast molding of car instrument panels, especially car bumper molding by RIM method, Metals, thermoplastics and rubber materials, such as cast molding of rubber tires It can be used for molding, fluid molding and extrusion molding. When forming containers The operations involved in this include cupping, canning, and anning), rolling, forging, ironing, drawing, corrugating (wrin kling) etc. In all of these operations, the compound of the invention is Metal or thermoplastic or rubber that acts as a lubricant and is subject to deformation. It is possible to quickly and cleanly demold the molded product by applying it to the mold to be injected. . Used in such operations when pouring thermoplastics and rubbers The advantage of the compound of the present invention is that the compound of the present invention performs its action externally and It is possible to attach it directly to the mold substrate. Therefore, demolding the cast molded product There is no need to add extraneous contaminating additives to the liquid composition for use. Typically, Alkoxylation near the lower end of the above range is important for plastics and rubbers. This method was found to be advantageous for fluid molding of molds.゛ In one example of forming metal containers, particularly aluminum cans, the lubricant has both hydrophilic and oleophilic properties. consisting of an alcohol mixture forming an emulsion with a composition in equilibrium with . For example, such marmagions are water-soluble alcohols containing 20% or more EO. Coxylated Guerbet Approximately 10 to 60% alcohol and oil-soluble alkoxylated gel About 10% to about 40% Guerbet alcohol and about 0% non-alkoxylated Guerbet alcohol It is produced by combining ~20%. This mixture contains mineral oil This provides a system with low viscosity and high rinsability. Ru. If the hydrophilic-to-lipophilic ratio (HLB) is large, the substance is water-soluble. However, small HLB indicates that it is an oil-soluble substance. can be changed to change its solubility in water.

他の例では、上述の混合物中の未アルコキシル化成分を、純度の比較的低いゲル ベ アルコールから本発明の生成物を誘導した場合のように、50%以下とする ことができる。In other examples, the unalkoxylated components in the mixtures described above can be combined into gels of relatively low purity. 50% or less, as in the case of deriving the products of the invention from base alcohols. be able to.

驚くべきことには、このような不純なゲルベ アルコールをアルコキシル化およ び/または次のエステル化に使用する場合に、優れた被洗浄性が達成される。関 連する不純物°はゲルベ反応における未反応アルコールであり、これは必然的に 低分子量で、例えば、ゲルベ アルコール生成物およびカニツァロ石鹸副生物中 に存在するような炭素原子数が半分のものである。これらの不純物はゲルベ ア ルコール生成物と混合した状態で約50重量%以下、普通約30重量%以下の分 量で存在することができる。従って、金属加工用の好ましい組成物は50重量% 以下、好ましくは少量の線状低分子量アルコールを含有しており、このアルコー ルは本発明のアルコキシル化ゲルベ生戊物を生成する反応中に全体的または部分 的にアルコキシル化および/またはエステル化されることがある。Surprisingly, such impure Guerbet alcohol can be alkoxylated and Excellent washability is achieved when used for subsequent esterification and/or subsequent esterification. Seki A related impurity is the unreacted alcohol in the Guerbet reaction, which necessarily Low molecular weight, e.g. in Guerbet alcohol products and Cannizzaro soap by-products It has half the number of carbon atoms as exists in . These impurities are Up to about 50% by weight, usually up to about 30% by weight when mixed with the alcohol product Can exist in amounts. Therefore, a preferred composition for metalworking is 50% by weight The following preferably contains a small amount of linear low molecular weight alcohol; during the reaction to produce the alkoxylated Guerbet material of the present invention. may be alkoxylated and/or esterified.

また、上述のアルコキシル化ゲルベ生戊物またはその混合物のエマルジョンまた は溶液は、水、鉱油、アルコキシル化および未アルコキシル化パラフィン系化合 物、エーテル、脂肪酸ケトンなどを包含する種々の溶媒および/または懸濁化剤 を使用して作ることができる。このような希釈を行う場合には、希釈剤と生成物 または生成物混合物との比を約20=1〜約1:20 、好ましくは約10:1 〜約1:10にする。Also, emulsions or mixtures of the alkoxylated Guerbet raw materials or mixtures thereof described above may be used. The solution is water, mineral oil, alkoxylated and non-alkoxylated paraffinic compounds. Various solvents and/or suspending agents including compounds, ethers, fatty acid ketones, etc. It can be made using . When making such dilutions, the diluent and product or product mixture in a ratio of about 20=1 to about 1:20, preferably about 10:1. ~ about 1:10.

普通、本発明のゲルベ生成物は、金属表面が他の表面と接触して摩擦を生じる際 に、この金属表面に潤滑性を付与するのに十分な分量で、吹付け、浸漬または他 の好都合な方法によって金属基板に付着させる。潤滑剤の特定の付着量は使用す る個々の操作および処理温度によって左右される。従って、1kgの金属に対し て0.0001 g程度の少量ないし3g程度の比較的多量の本発明の生成物を 使用することができる。飲料用アルミニウム缶の成形には1 kgめ金属に対し て約0.001〜約1gの本発明の生成物を使用することが比較的多い。Typically, the Guerbet products of the present invention are useful when a metal surface comes into contact with another surface to create friction. be sprayed, dipped or otherwise applied in an amount sufficient to provide lubricity to the metal surface. attached to the metal substrate by any convenient method. A specific amount of lubricant must be used. depends on the particular operation and processing temperature. Therefore, for 1 kg of metal A small amount of about 0.0001 g to a relatively large amount of about 3 g of the product of the present invention is can be used. For forming aluminum beverage cans, 1 kg of metal is required. It is relatively common to use from about 0.001 to about 1 g of the product of the invention.

本発明の生成物を潤滑剤として使用することにより多くの有利な結果が達成され る。この潤滑剤は酸化および悪臭に対する抵抗性が大きいほか、周囲温度におい て流動性を保持する。さらに、このような生成物は成形処理条件下に金属表面に 良好な付着性(substantivity)を示すが、水で洗浄することによ って容易に除去されて油膜残留物または斑点のほとんど存在しない清浄な金属表 面を生成する。本発明生成物が洗浄によって完全に除去されることは、食料品用 金属容器を成形する際に極めて望ましいことである。Many advantageous results are achieved by using the products of the invention as lubricants. Ru. This lubricant is highly resistant to oxidation and odor, and is resistant to ambient temperatures. maintain liquidity. Furthermore, such products can be deposited on metal surfaces under forming processing conditions. Shows good substantivity, but can be removed by washing with water. Clean metal surfaces with virtually no oil slick residue or spots that are easily removed Generate a surface. The fact that the product of the invention can be completely removed by washing is This is highly desirable when forming metal containers.

その理由は、本発明の生成物が後で容器の白味を汚染する分解性残留物を全く残 さないからである。このような性質は、濃度の極めて低い汚染性物質によっても 汚染され易い飲料に使用するアルミニウム缶を成形する際に必要である。The reason is that the products of the invention leave no degradable residues that later contaminate the whiteness of the container. This is because they do not. These properties can be maintained even by extremely low concentrations of pollutants. Necessary when molding aluminum cans for beverages that are easily contaminated.

本発明の生成物は、出発物質であるゲルベ アルフールをアルコキシル化し、次 いで所要に応じてエステル化することにより生成する。ゲルベ アルコールおよ びその製造方法はよく知られており、例にっていさらに説明する必要はないと考 える。本発明方法に使用する好ましいゲルベアルコールとしては、2−エチル− ヘキサン−1−オール、2−へキシル−エイコサン−1−オール、2−ヘキシル −デカン−1−オール、2−オクチル−ドデカン−1−オール、2−ブチル−オ クタン−1−オール、2−デシル−デカン−1−オール、2−ミリスチル−エイ コサン−1−オール、2−カブリルーエイコサン−1−オール、2−ココ−コシ ン−1−オール(2−coco−cocan−1−ol)、2−クロウ−オクタ デカン−1−オール、イソセチルアルコール、2−ヘキサゾシルーオクタデカン −1−オールなどがある。The products of the present invention are obtained by alkoxylating the starting material Guerbet Alfur and then It is produced by esterification as required. Guerbet alcohol and The method of manufacturing them is well known and we do not consider it necessary to explain further by way of example. I can do it. The preferred Guerbet alcohol used in the method of the invention is 2-ethyl- Hexan-1-ol, 2-hexyl-eicosan-1-ol, 2-hexyl -Decan-1-ol, 2-octyl-dodecane-1-ol, 2-butyl-o Cutan-1-ol, 2-decyl-decane-1-ol, 2-myristyl-A Cosan-1-ol, 2-cabryl-eicosan-1-ol, 2-coco-cosi 2-coco-cocan-1-ol, 2-crow-octa Decan-1-ol, isocetyl alcohol, 2-hexazosyl-octadecane -1-ol and the like.

これらのゲルベ アルコールおよび他のゲルベ アルコールは、生成物中の単位 として次式: (式中のR,R’、 x、 yおよびZは上述のものと同一のものを示す)で表 わされる対応するアルコキシル化ゲルベ アルコールを生成するのに望ましい量 のアルキレンオキシドと反応させることにより、アルコキシル化される。ゲルベ 分子中に導入されたアルコキシレート単位はプロピレンオキシド単位またはプロ ピレンオキシド単位とエチレンオキシド単位との混合物を含有する。アルコキシ レート単位は一層ランダムまたは不均一な分布構造になるよう混合物として導入 することができ、あるいはPO単位およびEO単位は一層ブロック様分布をする ように段階的に添加することができる。アルコキシル化プロセスは約り0℃〜約 200℃の温度、好ましくは約110℃〜175℃の温度において、約0.14 kg/cm”絶対圧(2psia)〜約14.06 kg/c+++絶対圧(2 00psia) 、好ましくは約2.81kg/cm ”絶対圧<40 psi a) 〜約4、22kg/cm ”絶対圧(60psia)の圧力下に行う。こ の発熱反応を除熱効率およびPOおよびEOの両方またはを)ずれか一方の添加 量に応じて約4時間〜約25時間、一層普通には約5時間〜約10時間行う。E O:POの比は約O:1〜約20:1の間、好ましくは約1=4〜約4:1の間 で変えることができる。上述のように、生成物は完全にプロポキシ化することが でき、あるいはエチレンオキシド単位とプロピレンオキシド単位との混合物を含 有することができる。アルコキシル化単位の混合物が望ましい場合には、ゲルベ  アルコールを先ず所望量のエチレンオキシドと接触させ、次いで所望量のプロ ピレンオキシドと接触させるのが望ましい。次いで、エトキシル化−プロポキモ ル化ゲルベを再度追加量のEOと接触させて代表的ブロック様構造を生成する。These Guerbet alcohols and other Guerbet alcohols have units in the product As the following formula: (In the formula, R, R', x, y and Z are the same as above) the desired amount to produce the corresponding alkoxylated Guerbet alcohol. is alkoxylated by reacting with an alkylene oxide. Guerbet The alkoxylate unit introduced into the molecule is a propylene oxide unit or a propylene oxide unit. Contains a mixture of pyrene oxide units and ethylene oxide units. Alkoxy Rate units are introduced as a mixture for a more random or non-uniform distribution structure or the PO and EO units have a more block-like distribution It can be added in stages. The alkoxylation process ranges from approximately 0℃ to approx. At a temperature of 200°C, preferably from about 110°C to 175°C, about 0.14 kg/cm” absolute pressure (2 psia) ~ approx. 14.06 kg/c+++ absolute pressure (2 psia) 00 psia), preferably about 2.81 kg/cm" absolute pressure <40 psi a) Performed under a pressure of ~4.22 kg/cm” absolute pressure (60 psia). The exothermic reaction of the heat removal efficiency and the addition of PO and/or EO Depending on the amount, the time is from about 4 hours to about 25 hours, more usually from about 5 hours to about 10 hours. E The O:PO ratio is between about O:1 and about 20:1, preferably between about 1=4 and about 4:1. You can change it with As mentioned above, the product can be fully propoxylated. or contain a mixture of ethylene oxide and propylene oxide units. can have If a mixture of alkoxylated units is desired, the gel base The alcohol is first brought into contact with the desired amount of ethylene oxide, then the desired amount of the product. Preferably, it is contacted with pyrene oxide. Then ethoxylation-propochymo The rubberized Guerbet is again contacted with an additional amount of EO to produce a typical block-like structure.

アルコキシル化反応は塩基性条件下に、望ましくは全反応混合物に対し約0.0 5〜約0.5重量%、好ましくは約0.1〜約0.3重量%の量の水酸化カリウ ム、水酸化ナトリウム、ナトリウムメチレート、炭酸ストロンチウムなどを添加 して実施する。The alkoxylation reaction is carried out under basic conditions, preferably about 0.0 Potassium hydroxide in an amount of 5 to about 0.5% by weight, preferably about 0.1 to about 0.3% by weight. Addition of aluminum, sodium hydroxide, sodium methylate, strontium carbonate, etc. and implement it.

反応生成物は蒸溜によって回収し、直接潤滑剤として使用するか、あるいは適当 なエステル化剤と反応させることにより対応するエステルに転化することができ る。The reaction product can be recovered by distillation and used directly as a lubricant or as a suitable can be converted to the corresponding ester by reacting with a suitable esterifying agent. Ru.

エステル化は約1=4〜約300℃の温度、好ましくは140℃〜約210℃の 温度において大気圧または10mmhのような僅かな減圧下に行う。この反応を 約2時間〜約24時間の間、好ましくは約4時間〜約12時間の間行って対応す るエステル化生成物を生成する。エステル化反応中に水が生成する。この水は直 接蒸留たまはプロセス中に二成分共沸混合物を使用することにより除去するのが 好都合である。The esterification is carried out at a temperature of from about 1=4 to about 300°C, preferably from 140°C to about 210°C. It is carried out at atmospheric pressure or under a slight vacuum, such as 10 mmh, at temperature. This reaction The treatment is carried out for about 2 hours to about 24 hours, preferably for about 4 hours to about 12 hours. produces an esterified product. Water is produced during the esterification reaction. This water is directly It can be removed by direct distillation or by using a binary azeotrope during the process. It's convenient.

適当なエステ化剤は、例えば、オレフィン系不飽和酸、芳香族カルボン酸、アル コキシ置換基を有するカルボン酸またはシクロヘキセン基で置換されたカルボン 酸であり、これらの酸としては一塩基酸(monoacid)、ダイマー酸、お よびトリマー酸がある。エステル化に使用できる有機酸の特定例としては、アク リル酸、アコニット酸、安息香酸、トルイル酸、キシリル酸、メタクリル酸、ア ジピン酸、酪酸、カプリン酸、カプロン酸、ケイ皮酸、シトラコン酸、クエン酸 、クレソチン酸、エライジン酸、グルタル酸、グリコール酸、乳酸、リヴリン酸 、マレイン酸、マロン酸、バルミチン酸、フタル酸、プロピオン酸、サリチル酸 、ステアリン酸、スペリン酸、コハク酸、酒石酸、リルン酸、オレイン酸、ピメ リン酸、アゼライン酸、セバシン酸、ナフタール酸、トリメリット酸、プロパン −トリカルボン酸、エチルジカルボン酸およびミリスチン酸およびこれらの混合 物がある。ジーまたはトリー有機酸を使用する場合には、エステル化反応をカル ボキシル単位の全部または一部が対応するエステルに転化するまで続けることが できる。Suitable esterifying agents include, for example, olefinically unsaturated acids, aromatic carboxylic acids, alkali Carboxylic acids with koxy substituents or carboxylic acids substituted with cyclohexene groups These acids include monoacids, dimer acids, and and trimer acids. Specific examples of organic acids that can be used for esterification include Lylic acid, aconitic acid, benzoic acid, toluic acid, xylylic acid, methacrylic acid, Dipic acid, butyric acid, capric acid, caproic acid, cinnamic acid, citraconic acid, citric acid , cresotic acid, elaidic acid, glutaric acid, glycolic acid, lactic acid, livric acid , maleic acid, malonic acid, valmitic acid, phthalic acid, propionic acid, salicylic acid , stearic acid, superic acid, succinic acid, tartaric acid, lylunic acid, oleic acid, pime Phosphoric acid, azelaic acid, sebacic acid, naphthalic acid, trimellitic acid, propane -tricarboxylic acid, ethyldicarboxylic acid and myristic acid and mixtures thereof There are things. When using di- or tri-organic acids, the esterification reaction is can be continued until all or part of the boxyl units have been converted to the corresponding ester. can.

エステル化に使用するシクロヘキセニル酸は次式=(式中のnは1〜3の数:n は0〜10の数;R4は1〜15個の炭素原子を有するアルキル基またはアルケ ニル基、1pおよびrはいずれも0〜1の数を示す)で表わされる。Cyclohexenylic acid used for esterification is expressed by the following formula = (in the formula, n is a number from 1 to 3: n is a number from 0 to 10; R4 is an alkyl group or alkyl group having 1 to 15 carbon atoms; Nyl group, 1p and r each represent a number from 0 to 1).

このようなシクロヘキセン置換アルキル酸またはアルケニル酸の例としては、次 式: %式% でit)さtLる6−(ヘプト−1−エニル)−5−ペンチル−3−シクロヘキ セン−1,2−シ゛ノニル酸、次式二で表わされる5、6−シプチルー1. 2 .4a、5. 6.8a−ヘキサヒドロ−1,2−ナフタレンシカプリル酸、お よび次式: で表わされる1、2. 3. 4.4a、5. 6.8a−オクタヒドロ−5, 6−シメチルー1.2−ナフタレンジプロピオン酸がある。普通、プロペニルア ルコールからこれらの環式化合物を生成する反応は、非環式化合物と単環式化合 物と二環式化合物との混合物を生成する。粘土触媒の存在下にリルン酸とオレイ ン酸とは反応して化合物りと化合物Mと次式: で表わされる9−ノニリデンー10−ペンチル−1,18−オクタデカンジカル ボン酸との混合物を生成する。Examples of such cyclohexene-substituted alkyl or alkenylic acids include: formula: %formula% 6-(hept-1-enyl)-5-pentyl-3-cyclohexyl Sen-1,2-cynonylic acid, 5,6-cyptyl group represented by the following formula 2: 1. 2 .. 4a, 5. 6.8a-hexahydro-1,2-naphthalene caprylic acid, and the following formula: 1, 2. 3. 4.4a, 5. 6.8a-octahydro-5, There is 6-dimethyl-1,2-naphthalene dipropionic acid. Normal, Propenilua The reaction that produces these cyclic compounds from alcohol is a process that produces both acyclic and monocyclic compounds. and a bicyclic compound. lyric acid and olei in the presence of clay catalyst The compound M reacts with phosphoric acid to form the following formula: 9-nonylidene-10-pentyl-1,18-octadecanedical represented by Produces a mixture with bonic acid.

エステル化剤として二塩基酸を使用する例は、アルコキシル化ゲルベ アルコー ルと、例えば、シクロヘキサノールを硝酸で酸化することによって生成する次式 :%式% で表わされる化合物との反応によって例示される。An example of using a dibasic acid as an esterifying agent is alkoxylated gel base alcohol. For example, the following formula is produced by oxidizing cyclohexanol with nitric acid: :%formula% This is exemplified by the reaction with the compound represented by

この場合にはカルボキシル基の一方または両方がアルコールによってエステル化 されて、反応に使用した酸の割合および反応時間に応じてモノ−またはジ−エス テルを生成する。普通このようなモノエステルとジエステルとの混合物が得られ る。同様に、アルコキシル化ゲルベ アルコールと三塩基酸、例えば、石炭を硝 酸で酸化することにより生成する次式: で表わされる化合物との反応はモノエステル、ジエステルまたはトリエステル、 普通これらの混合物を生成する。その理由は、アルコキシル化ゲルベ アルコー ルに対する酸量に応じて、1個、2個または3個のカルボキシル基がエステル化 されるからである。他のポリカルボン酸およびその製造方法は米国特許第4.0 75.393号:同第4.042.515号:同第2.482.761号:同第 2.793.219号;同第3.076、003号;および同第3.100.7 84号に開示されている。普通、ポリカルボン酸の製造はモンモリロナイト粘度 のような触媒の存在下における不飽和脂肪酸の熱的縮合を必然的に伴う。In this case, one or both carboxyl groups are esterified with alcohol. Depending on the proportion of acid used in the reaction and the reaction time, mono- or Generate tell. Usually a mixture of such monoesters and diesters is obtained. Ru. Similarly, alkoxylated Guerbet alcohols and tribasic acids, e.g. The following formula is produced by oxidation with acid: The reaction with the compound represented by is monoester, diester or triester, Usually a mixture of these is produced. The reason is that alkoxylated gelbean alcohol Depending on the amount of acid relative to the molecule, 1, 2 or 3 carboxyl groups are esterified This is because it will be done. Other polycarboxylic acids and methods for their production are disclosed in U.S. Patent No. 4.0 75.393: Same No. 4.042.515: Same No. 2.482.761: Same No. 2.793.219; 3.076, 003; and 3.100.7 No. 84. Normally, polycarboxylic acid is manufactured using montmorillonite viscosity. It entails thermal condensation of unsaturated fatty acids in the presence of catalysts such as.

第1図は本発明化合物におけるプロピレンオキシドの影響および低温で流動性を 保持できる能力を示す。第1図のグラフにおいて、種々のアルコキシル化された 基を有する2−デシル−デカン−1−オール アルコールの融点をアルコキシル 化された単位の全モル数に対して測定した。曲線Xはエチレンオキシドのみを含 有するアルコキシル化ゲルベを示す。曲線Zは8066%およびPO34%を含 有するアルコキシル化ゲルベを示す。最後に、曲線Oは8050%およびPO5 0%を含有するアルコキシル化ゲルベを示す。Figure 1 shows the influence of propylene oxide on the compounds of the present invention and the fluidity at low temperatures. Demonstrates ability to hold. In the graph of Figure 1, various alkoxylated The melting point of 2-decyl-decane-1-ol alcohol with the alkoxyl group It was measured based on the total number of moles of converted units. Curve X contains only ethylene oxide. 1 shows alkoxylated Guerbet with Curve Z contains 8066% and PO34%. 1 shows alkoxylated Guerbet with Finally, curve O is 8050% and PO5 The alkoxylated Guerbet containing 0% is shown.

これらの曲線を比較することによって分るように、合計8モルのアルコキシル化 された単位が種々の化合物中に含有されている場合には、PO50%を含有する アルコキシル化ゲルベは0℃より低い温度においても流動性を保持するが、6口 のみを含有する化合物において同程度のアルコキシル化が行われている場合には 、融点が有意に高くなる。これらの化合物はいずれも通常液体であるが、EO単 位のみを含有するアルコキシル化ゲルベは耐酸性が有意に小さくなり、油溶性が 小さくなる。白線ZおよびOによって示される化合物の融点が低いことは、これ らの化合物を種々の配合物中に容易に混入できので、望ましい。このような性質 は、これらの化合物が高分子量であることを考えると、全く予期できぬことであ る。従って、同一化合物において優れた潤滑性に寄与する高分子量と配合の容易 さとが達成される。As can be seen by comparing these curves, a total of 8 moles of alkoxylation If the unit is contained in various compounds, it contains 50% of PO. Alkoxylated Guerbet retains fluidity even at temperatures below 0°C; If the same degree of alkoxylation is carried out in a compound containing only , the melting point becomes significantly higher. All of these compounds are normally liquid, but EO alone Alkoxylated Guerbet containing only becomes smaller. The low melting point of the compound indicated by the white lines Z and O is due to this These compounds are desirable because they can be easily incorporated into a variety of formulations. This kind of property is completely unexpected considering the high molecular weight of these compounds. Ru. Therefore, high molecular weight and ease of formulation contribute to excellent lubricity in the same compound. Sato is achieved.

米国特許第4.425.458号は塑性潤滑剤として未アルコキシ化ゲルベアル コールニ塩基酸エステルを使用することを開示している。しかし、これらのエス テルは親油性が大きすぎるので金属容器の絞り加工およびアイアニングには有用 でない。さらに、塑性潤滑の機構も金属成形を含む処理とは全く似ていない。特 に上述の特許およびその他のものに開示されている塑性潤滑は、ポリマーメルト 中に溶解する性能に依存しており、すなわち内部潤滑剤として作用する。これに 対し、金属成形においては潤滑剤は溶解しないが、摩擦を軽減するために金属表 面に薄いフィルムとして被着させる。本発明の物質をプラスチックの流し込み成 形用潤滑剤として使用する場合には、この物質はポリマーメルト中に溶解しない が、成形品を迅速に脱型するために成形型の表面に被着させる。従って、本発明 のアルコキシル化ゲルベ生成物は溶融混合物中に異質の物質を導入しないので、 従来の塑性潤滑剤より優れた多くの利点を有する。U.S. Pat. No. 4,425,458 describes unalkoxylated gelbearing as a plastic lubricant. The use of colnibasic acid esters is disclosed. However, these Because tel is too lipophilic, it is useful for drawing and ironing metal containers. Not. Moreover, the mechanism of plastic lubrication is also not at all similar to processes involving metal forming. Special Plastic lubrication, as disclosed in the above-mentioned patents and others, It relies on its ability to dissolve in the liquid, i.e. act as an internal lubricant. to this On the other hand, in metal forming, lubricants do not dissolve, but are used on the metal surface to reduce friction. It is applied as a thin film to the surface. The substance of the present invention is poured into plastic. When used as a molding lubricant, the material does not dissolve in the polymer melt. is applied to the surface of the mold in order to quickly demold the molded product. Therefore, the present invention Since the alkoxylated Guerbet products do not introduce foreign materials into the molten mixture, It has many advantages over traditional plastic lubricants.

本発明を一般的に説明したが、以下に好適例を示す次の実施例について本発明を 説明する。これらの実施例は本発明の範囲を限定するものではない。Having described the present invention generally, the present invention will now be described with reference to the following examples, which are preferred embodiments. explain. These examples are not intended to limit the scope of the invention.

実施例1 2立四頚ガラス反応フラスコ中のデシルアルコール967gに、水酸化ナトリウ ム30gおよびニッケル2.0gをかきまぜながら添加した。この混合物を23 0〜250℃に加熱し、反応で生成した水を蒸留によって除去しながら6時間か きまぜた。次いで反応器内容物を冷却し、生成物である1−デシル−デカン−1 −オールを90%より大きい収率で回収した。蒸留によって精製した生成物は気 液分配クロマトグラフィ(GLC)によって確認した。Example 1 Sodium hydroxide was added to 967 g of decyl alcohol in a 2-stand, four-necked glass reaction flask. 30 g of aluminum and 2.0 g of nickel were added with stirring. Add this mixture to 23 Heat to 0 to 250°C and heat for 6 hours while removing water produced by the reaction by distillation. I mixed it up. The reactor contents are then cooled and the product 1-decyl-decane-1 -ol was recovered in greater than 90% yield. Products purified by distillation are Confirmed by liquid partition chromatography (GLC).

上述の一般的な操作を以下の実施例2〜10のすべてにおいて使用した。The general procedure described above was used in all Examples 2-10 below.

実施例2 デシルアルコール510gおよびラウリルアルコール510gに、水酸化カリウ ム20.0gおよび亜鉛1.0gを、よくかきまぜながら添加した。生成した混 合物を、反応で生成した水を留出させながら、230〜250℃に加熱した。Example 2 Add potassium hydroxide to 510 g of decyl alcohol and 510 g of lauryl alcohol. 20.0 g of aluminum and 1.0 g of zinc were added with good stirring. The generated confusion The mixture was heated to 230-250° C. while distilling off the water produced in the reaction.

反応を進行させ、次いでGLC分析を行い、ゲルベアルコール生成物である2− ラウリル−デカン−1−オールを90%より大きい収率で得た。次いで反応生成 物を蒸留して高純度のゲルベ生成物を得た。The reaction was allowed to proceed, followed by GLC analysis, and the Guerbet alcohol product, 2- Lauryl-decan-1-ol was obtained in greater than 90% yield. Then reaction production The product was distilled to obtain a highly pure Guerbet product.

実施例3 デシルアルコール500gおよびオクチルアルコール500gに、水酸化カリウ ム30.0gおよびニッケル2.0gを、よくかきまぜながら添加した。生成し た混合物を、反応で生成した水を蒸留によって除去しながら、230〜250℃ に加熱した。Example 3 Add potassium hydroxide to 500 g of decyl alcohol and 500 g of octyl alcohol. 30.0 g of aluminum and 2.0 g of nickel were added with good stirring. generate The mixture was heated at 230 to 250°C while removing the water produced by the reaction by distillation. heated to.

反応を進行させ、次いでGLC分析を行い、ゲルベ−アルコール生成物である2 −デシル−オクタン−1−オールを90%より大きい収率で得た。反応生成物は 蒸留して精製した。The reaction was allowed to proceed, followed by GLC analysis, and the Guerbet-alcohol product, 2 -decyl-octan-1-ol was obtained in greater than 90% yield. The reaction product is Purified by distillation.

実施例4 オクチルアルコール1000gに炭酸カリウム30.0gおよびニッケル1.0 gをよくかきまぜながら添加した。生成した混合物はよくかきまぜながら220 〜240℃に加熱した。反応で生成した水は留出させた。Example 4 Octyl alcohol 1000g, potassium carbonate 30.0g and nickel 1.0 g was added while stirring well. The resulting mixture was heated to 220 ml while stirring well. Heated to ~240°C. Water produced in the reaction was distilled off.

反応を進行させ、次いでGLC分析を行った。CI6ゲルベーアルコールの収率 は90%より大きかった。反応生成物を蒸留して高純度ゲルベアルコールを得た 。The reaction was allowed to proceed and then subjected to GLC analysis. Yield of CI6 Guerbet alcohol was greater than 90%. High purity Guerbet alcohol was obtained by distilling the reaction product. .

実施例5 イソデシルアルコール967gおよびトリデシルアルコール500gに、水酸化 ナトリウム30.0gおよび亜クロム酸銅(copper chromite)  2.0gを、よくかきまぜながら添加した。Example 5 967 g of isodecyl alcohol and 500 g of tridecyl alcohol were hydroxylated. 30.0g of sodium and copper chromite 2.0 g was added while stirring well.

生成した混合物を、反応で生成した水を蒸留により除去しながら、230〜25 0℃に加熱した。The resulting mixture was heated to 230 to 25 Heated to 0°C.

ゲルベアルコール生成物を90%より大きい収率で回収した。生成物を蒸留して 高純度のゲルベ生物物を得た。Guerbet alcohol product was recovered in greater than 90% yield. Distill the product High purity Guerbet organisms were obtained.

実施例6 1 m (Coco)アルコール(CI2〜C4s混合物> 967gに水酸化 カリウム30.0gおよびニッケル2.0gをよくかきまぜながら添加した。生 成した混合物を、反応で生成した水を蒸留により除去しながら、230〜250 ℃に加熱した。Example 6 1 m (Coco) alcohol (CI2-C4s mixture> Hydroxylated to 967 g 30.0 g of potassium and 2.0 g of nickel were added with good stirring. Living The resulting mixture was heated to 230-250 ml while removing the water produced by the reaction by distillation. heated to ℃.

ゲルベ生成物への転化率%は90%より大きかった。生成物を蒸留してC24〜 C32混合ゲルベアルコールからなる高純度生成物を得た。The % conversion to Guerbet product was greater than 90%. Distill the product to produce C24~ A high purity product consisting of C32 mixed Guerbet alcohol was obtained.

実施例7 デシルアルコール967gに水酸化カリウム30.0gおよびニッケル2.0g を、よくかきまぜながら添加した。生成した混合物を、反応で生成した水を蒸留 により除去しながら、230〜250℃に加熱した。Example 7 Decyl alcohol 967g, potassium hydroxide 30.0g and nickel 2.0g was added while stirring well. The water produced in the reaction is distilled from the resulting mixture. The mixture was heated to 230-250° C. while being removed by.

反応を進行させ、次いでGLC分析を行った。2−デシル−デカン−1−オール 量が60%の収率になった際に、反応混合物を冷却し、濾過してゲルベアルコー ルおよび未反応デシルアルコールを含有する混合生成物を回収した。The reaction was allowed to proceed and then subjected to GLC analysis. 2-decyl-decane-1-ol When the amount reached 60% yield, the reaction mixture was cooled and filtered with Guerbet alcohol. A mixed product containing alcohol and unreacted decyl alcohol was recovered.

実施例8 デシルアルコール500gおよびラウリルアルコール500gに、水酸化カリウ ム30.0gおよび亜鉛粉末2.0gを、よくかきまぜながら添加した。生成し た混合物を、反応で生成した水を留出させながら、230〜250℃に加熱した 。Example 8 Add potassium hydroxide to 500 g of decyl alcohol and 500 g of lauryl alcohol. 30.0 g of aluminum powder and 2.0 g of zinc powder were added with good stirring. generate The mixture was heated to 230-250°C while distilling off the water produced in the reaction. .

反応を進行させ、次いでGLC分析を行い、ゲルベ生成物の収率が75%に達し た際に、反応混合物を冷却し、濾過して生成物2−ラウリル−デカン−1−オー ルおよび未反応のデシルアルコールおよびラウリルアルコールヲ得り。The reaction was allowed to proceed, followed by GLC analysis, and the yield of Guerbet product reached 75%. Upon reaction, the reaction mixture was cooled and filtered to remove the product 2-lauryl-decane-1-o and unreacted decyl alcohol and lauryl alcohol.

実施例9 デシルアルコール500gおよびオクチルアルコール500gに、水酸化ナトリ ウム30.0gおよびニッケル2.0gを、よくかきまぜながら添加した。生成 した混合物を、反応で生成した水を留出させながら、230〜250℃に加熱し た。Example 9 Add sodium hydroxide to 500 g of decyl alcohol and 500 g of octyl alcohol. 30.0 g of aluminum and 2.0 g of nickel were added with good stirring. Generate The resulting mixture was heated to 230 to 250°C while distilling off the water produced in the reaction. Ta.

反応を進行させ、次いでGLC分析を行った。2−オクチル−デカン−1−オー ルのゲルベが70%に達した際に、反応混合物を冷却し、ゲルベアルコールおよ び未反応のオクチルアルコールおよびデジルアコールを含有する生成物を回収し た。The reaction was allowed to proceed and then subjected to GLC analysis. 2-octyl-decane-1-o When the Guerbet in the alcohol reaches 70%, the reaction mixture is cooled and added with Guerbet alcohol and Collect the product containing unreacted octyl alcohol and desyl alcohol. Ta.

実施例10 オクチルアルコール1000gに、水酸化カリウム30.0gおよびニッケル2 .0gを、よくかきまぜながら添加した。生成した混合物を、反応で生成した水 を還流アルコールから分離し、反応混合物から除去しながら、230〜250℃ に加熱した。次いで還流アルコールを反応器に再循環させた。Example 10 To 1000 g of octyl alcohol, 30.0 g of potassium hydroxide and 2 nickel .. 0 g was added with good stirring. The resulting mixture is mixed with the water produced in the reaction. at 230-250°C while separating it from the refluxing alcohol and removing it from the reaction mixture. heated to. The refluxing alcohol was then recycled to the reactor.

反応を進行させ、次いでGLC分析を行った。CI6ゲルベアルコールの収率が 80%になった際に、反応混合物を冷却し、ゲルベ生成物を未反応オクチルアル コールと共に回収した。The reaction was allowed to proceed and then subjected to GLC analysis. The yield of CI6 Guerbet alcohol is At 80%, the reaction mixture was cooled and the Guerbet product was removed from the unreacted octyl alcohol. Collected with Cole.

実施例11 A、実施例1のゲルベアルコール748.5gに、KOH2gおよびエチレンオ キシド249gを2時間にわたって添加した。発熱反応が生起し、混合物は3. 16kg / cm 2ゲージ圧(45psig)の圧力下に125℃の温度に なった。エトキシル化生成物を真空下にストリップし、次いで冷却し、生成物A として回収した。Example 11 A. To 748.5 g of Guerbet alcohol from Example 1, add 2 g of KOH and ethylene oxide. 249 g of oxide was added over 2 hours. An exothermic reaction occurs and the mixture becomes 3. 16 kg/cm at a temperature of 125°C under a pressure of 2 gauge pressure (45 psig) became. The ethoxylated product was stripped under vacuum, then cooled and the product A It was recovered as.

B、実施例2のゲルベアルコール748.5gに、KOH2gおよびエチレンオ キシド500gを2時間にわたって添加した。B. To 748.5 g of Guerbet alcohol from Example 2, add 2 g of KOH and ethylene oxide. 500 g of oxide was added over 2 hours.

その結果生じた発熱反応によって3.52 kg/cm ’ゲージ圧(50ps ig)の圧力下に温度は180℃になった。エトキシル化生成物を真空下にス)  IJフプし、冷却し、生成物Bとして回収した。The resulting exothermic reaction produced a pressure of 3.52 kg/cm (50 ps) ig) and the temperature reached 180°C. ethoxylated product under vacuum) IJ pumped, cooled and collected as Product B.

C0実施例11Aのエトキシル化ゲルベアルコール748.5gに、KOH2g およびプロピレンオキシド250gを、2時間にわたって添加した。次いで同じ ような期間にわたってエチレンオキシド250gを添加した。発熱反応によって 温度は約175℃になった。主としてブロック分布をしているエトキシル化−プ ロポキシル化−エトキシル化生成物を真空下にストリップし、冷却し、生成物C として回収した。To 748.5 g of ethoxylated Guerbet alcohol from C0 Example 11A, 2 g of KOH and 250 g of propylene oxide were added over 2 hours. then the same 250 g of ethylene oxide was added over a period of time. by an exothermic reaction The temperature reached approximately 175°C. Ethoxylated polymers with mainly block distribution The lopoxylated-ethoxylated product was stripped under vacuum, cooled and the product C It was recovered as.

D、生成物Bを製造する際に行った操作を繰り返した。D. The operations performed in preparing product B were repeated.

ただし、実施例1のゲルベアルコールを実施例2のゲルベアルコールの代りに使 用した。また、プロピレンオキシド500gをエチレンオキシド500gの代り に使用した。生成したプロポキシル化生成物を生成物りとして回収した。However, if the Guerbet alcohol of Example 1 is used instead of the Guerbet alcohol of Example 2, used. Also, replace 500g of propylene oxide with 500g of ethylene oxide. used for. The resulting propoxylated product was recovered as product.

E、生成物Cを製造する際に行った操作を繰り返した。E, the operations performed in preparing product C were repeated.

ただし、ゲルベアルコールを最初にエチレンオキシド500gと、次いでプロピ レンオキシド500gと接触させ、最後のエチレンオキシドとの接触は行わなか った。さらに、実施例2のゲルベアルコールを実施例11Aのエトキシル化ゲル ベアルコールの代りに使用した。生成したブロック分布をしているエキキシル化 −プロポキシル化生成物を生成物Eとして回収した。However, Guerbet alcohol must first be mixed with 500 g of ethylene oxide and then propylene oxide. Contact with 500 g of ethylene oxide, without final contact with ethylene oxide. It was. Furthermore, the Guerbet alcohol of Example 2 was added to the ethoxylated gel of Example 11A. Used in place of bear alcohol. Exilization with generated block distribution -Propoxylation product was recovered as Product E.

F、実施例1のゲルベアルコール748.5gに、KOH2gおよびエチレンオ キシド250gとプロビレオンオキシド250gとの混合物を、2時間にわたっ て添加した。発熱反応によって約170℃になった。不均一なアルコキシル化分 布をしているエトキシル化−プロポキシル化生成物を真空下にストリップし、冷 却し、生成物Fとして回収した。F. To 748.5 g of Guerbet alcohol from Example 1, 2 g of KOH and ethylene oxide were added. A mixture of 250 g of oxide and 250 g of provireon oxide was added over a period of 2 hours. and added. The exothermic reaction brought the temperature to about 170°C. Heterogeneous alkoxylation content The ethoxylated-propoxylated product is stripped under vacuum and cooled. The product was collected as Product F.

上述した生成物A−Fの性質を1 (不可(poor))〜5(秀)の評点で評 価した。評価結果は次の第1表に示す通りであった。The properties of the products A-F described above were evaluated on a scale of 1 (poor) to 5 (excellent). I valued it. The evaluation results were as shown in Table 1 below.

第1表 BCDEF 揮発性’ 123443 被洗浄性’ 234445 潤滑性’ 233443 流動性’ 214544 1、200℃の炉で24時間。Table 1 BCDEF Volatile’ 123443 Washability’ 234445 Lubricity’ 233443 Liquidity' 214544 1. 24 hours in a 200℃ oven.

2、21.1℃(70°F)の水で洗浄。2. Wash with 70°F (21.1°C) water.

3、ロスチャイルド摩擦試験機。3. Rothschild friction tester.

4.20℃における値。4. Value at 20°C.

エトキシル化アルコール生成物は直接潤滑剤として使用することができ、あるい は以下に実施例に示すようにアルコキシル化アルコールとC4〜C20有機脂肪 酸とを反応させることによりエトキシル化アルコール生成物の全部または一部を 対応するエステルに転化することができる。Ethoxylated alcohol products can be used directly as lubricants or is an alkoxylated alcohol and a C4-C20 organic fat as shown in the examples below. All or part of the ethoxylated alcohol product by reaction with acid It can be converted to the corresponding ester.

実施例12〜18 第2表に示す量の特定のアルコキシル化ゲルベアルコールに、第2表に示す量の 第2表に示す脂肪酸を添加した。Examples 12-18 The amounts of specified alkoxylated Guerbet alcohols shown in Table 2 are added to the amounts shown in Table 2. The fatty acids shown in Table 2 were added.

約140℃において水を留出させながら5mmHgの圧力下に160〜180℃ の温度に加熱することによりエステル化反応を行った。酸価が1■/g未満のK OHに達するまで反応を続けた。副生物である水を連続的に除去することにより 高純度のエステル化生成物を回収した。160-180°C under a pressure of 5 mmHg while distilling water at about 140°C. The esterification reaction was carried out by heating to a temperature of . K with acid value less than 1■/g The reaction continued until OH was reached. By continuously removing water as a by-product High purity esterification product was recovered.

第2表 12 カプリル(octanoic) (748,5g) 生成物B (145 3g)13 ラウリル(748,5g) 生成物C(2270g)14 ステア リン(748,5g) 生成物C(1613g)15 ココ (748,5g>  生成物D (1690g)16 カプリル(caprylic) (748, 5g) 生成物E (155,5g)17 ダイマー酸混合物’ (748,5 g) 生成物E (238,0g)18 ダイマー酸混合物” (748,5g ) 生成物E(119,0g)本化合物り、 Mおよび0を含有する混合物上述 のアルコキシル化ゲルベエステルのうち、実施例12のもののみが満足できる流 動性を示さず、アルミニウム缶の絞り成形の際に優れた潤滑性を示さなかった。Table 2 12 Caprylic (octanoic) (748,5g) Product B (145 3g) 13 Lauryl (748.5g) Product C (2270g) 14 Stare Phosphorus (748.5g) Product C (1613g) 15 Coco (748.5g> Product D (1690g) 16 caprylic (748, 5g) Product E (155,5g) 17 Dimer acid mixture’ (748,5 g) Product E (238,0g) 18 Dimer acid mixture” (748,5g ) Product E (119,0 g) This compound is a mixture containing M and 0 as described above. Of the alkoxylated Guerbet esters, only Example 12 had a satisfactory flow. It did not exhibit any dynamic properties and did not exhibit excellent lubricity during drawing forming of aluminum cans.

残りの生成物は良好な耐酸化性を有し、アルミニウム表面から容易に洗浄するこ とができ、優れた潤滑性を有し、これらの生成物を金属表面に吹付けて得たフィ ルムは金属に対し良好な付着性を示した。The remaining product has good oxidation resistance and can be easily cleaned from aluminum surfaces. The film obtained by spraying these products onto metal surfaces has excellent lubricity. lum showed good adhesion to metals.

他のダイマー酸混合物、例えば、次の第3表に示す組成のものを、実施例17お よび実施例18において、代りに使用して良好な流動性および優れた潤滑性を有 するエステルを得た。Other dimer acid mixtures, such as those shown in Table 3 below, were used in Example 17 and and in Example 18, it was used instead to have good fluidity and excellent lubricity. The resulting ester was obtained.

第3表 トール油脂肪酸 15 70 15 リルン酸 5 55 40 実施例19 ガラス反応器中の実施例11の生成物D 1815gに、かきまぜながらトリメ リット酸210gを添加した。この混合物を、かきまぜかつ水を蒸発させながら 、6時間にわたって170℃の温度に加熱し、しかる後にこの混合物を冷却し、 化合物り、 MおよびOの一塩基酸、二塩基酸および非環式エステルを含有する トリエステル生成物を回収した。混合生成物は酸価が1.5■/g未満のKOH であった。生成物は優れた金属潤滑性、良好な耐酸化性および高度の金属付着性 を示した。Table 3 Tall oil fatty acid 15 70 15 Rilunic acid 5 55 40 Example 19 To 1815 g of the product D of Example 11 in a glass reactor was added the trimester with stirring. 210 g of lithic acid was added. Stir this mixture and evaporate the water. , to a temperature of 170° C. for 6 hours, after which the mixture is cooled, Compounds containing monobasic acids, dibasic acids and acyclic esters of M and O The triester product was collected. The mixed product is KOH with an acid value of less than 1.5 /g Met. The product has excellent metal lubricity, good oxidation resistance and high metal adhesion showed that.

実施例20〜25 0スチャイルド摩擦試験機を使用して次の実験を行って、本発明化合物と他の商 業的に使用されている化合物、例えば、アルカラブ(Alkalube、商品名 ’) GE−3(3EO単位の2−デシル−デカン−1−オール);アルカラブ GE−5(5EO単位の2−デシル−デカン−1−オール)およびアルカラブG E−20(20EO単位の2−デシル−デカン−1−オール)とについて摩擦性 を測定し、比較した。これらの商業的製品を実施例15.16および18の生成 物と比較した。Examples 20-25 The following experiment was conducted using a 0 Schchild friction tester to test the compounds of the present invention and other commercial products. Compounds used commercially, such as Alkalube (trade name) ’) GE-3 (2-decyl-decan-1-ol with 3 EO units); Alcarab GE-5 (2-decyl-decan-1-ol with 5 EO units) and Alcalab G Friction properties for E-20 (2-decyl-decane-1-ol with 20 EO units) were measured and compared. These commercial products were produced in Examples 15.16 and 18. compared to things.

供試潤滑剤をイソプロパツールに溶解した1%溶液をガラスビューレット中で作 ることにより試験を行った。この溶液を1時間かきまぜてから一夜静置し、しか 後にアトラブ(Atlab、商品名)・フィニツシユ・アプリケーターに導入し 、該アプリケーターから前記溶液を150デニールで32フイブリルのポリエス テル繊維に、該繊維の重量に対し1重量%の量で被着させた。被覆された繊維を 37.8℃(100’ F)のAI/SS ドラム上に通してイソプロパツール を除去し、次いでSSスプール上に巻き取り、22.2℃(72°F)の一定温 度および60%の相対湿度において24時間貯蔵した。この平衡化期間の後に、 100〜300m/分で動作しているロスチャイルド摩擦試験機に繊維を導入し 、2個のトランスジューサの間で繊維の摩擦を測定した。繊維金属界面における 摩擦係数(μm)を記録し、次の第4表に示した。Prepare a 1% solution of the test lubricant in isopropanol in a glass burette. The test was conducted by Stir this solution for 1 hour, then let it stand overnight. Later introduced into Atlab (product name) finish applicator. , apply the solution from the applicator to a 150 denier, 32 fibril polyester The fibers were coated in an amount of 1% by weight, based on the weight of the fibers. coated fibers Pass the isopropanol onto an AI/SS drum at 37.8°C (100’F) was removed and then wound onto an SS spool and kept at a constant temperature of 72°F (22.2°C). and 60% relative humidity for 24 hours. After this equilibration period, The fibers were introduced into a Rothschild friction tester operating at 100-300 m/min. , measured the fiber friction between two transducers. at the fiber-metal interface The coefficient of friction (μm) was recorded and shown in Table 4 below.

補正書の写しく翻訳文)提出書(特許法第184条の7第1項)昭和63年10 月 6日 ■ハ 特許庁長官 吉 1) 文 毅 殿 1、特許出願の表示 PCT/US8B100278 2、発明の名称 プロポキシル化 ゲルベ アルコールおよびそのエステル3、特許出願人 住 所 アメリカ合衆国ニューシャーシー州07470 ウニインアルプス ロ ード1361 名称 ジ−ニーエフ・コーポレーション代表者 ウォード・ジョシュア・ジエイ 国 籍 アメリカ合衆国 4、代 理 人 1988年 6月20日 6、添付書類の目録 訂正した請求の範囲 (式中のRおよびR1はそれぞれ別個に6〜15個の炭素原子を有するアルキル 基を示し;yは1〜20の整数を示し;整数Xおよび2の和はO〜20であり; R2は水素原子、未置換のアルキル基またはアルケニル基、あるいはカルボキシ ル基、CUR’基または次式:で表わされるシクロへキセニル基で置換されたア ルキル基またはアルケニル基を示し、かつmは1〜3の数を示し;nはいずれの 場合にも0〜10の整数を示し;pおよびrはそれぞれ0〜1の数を示し;R5 はいずれの場合にも水酸基または次式: で表わされるアルコキシル化された基を示し;R6は1〜10個の炭素原子を有 するアルケニル基またはアルキル基を示す)で表わされることを特徴とするアル コキシル化化合物。Copy and translation of amendment) Submission (Article 184-7, Paragraph 1 of the Patent Act) October 1988 Month 6th ■Ha Director General of the Patent Office Yoshi 1) Takeshi Moon 1. Display of patent application PCT/US8B100278 2. Name of the invention Propoxylated Guerbet Alcohol and Its Esters 3, Patent Applicant Address: Uniin Alps, New Chassis, USA 07470 code 1361 Name: Genf Corporation Representative: Ward Joshua G.I. Nationality: United States of America 4. Deputy manager June 20, 1988 6. List of attached documents Amended scope of claims (wherein R and R1 are each independently an alkyl group having 6 to 15 carbon atoms) represents a group; y represents an integer of 1 to 20; the sum of integers X and 2 is O to 20; R2 is a hydrogen atom, an unsubstituted alkyl group or alkenyl group, or a carboxy aryl group, CUR' group or cyclohexenyl group represented by the following formula: represents alkyl group or alkenyl group, and m represents a number from 1 to 3; n represents any also represents an integer from 0 to 10; p and r each represent a number from 0 to 1; R5 is in each case a hydroxyl group or the following formula: represents an alkoxylated group represented by; R6 has 1 to 10 carbon atoms; (representing an alkenyl group or an alkyl group) Coxylated compounds.

3、R2は水素原子を示す請求項1記載の化合物。3. The compound according to claim 1, wherein R2 represents a hydrogen atom.

6、R3は次式: で表わされる基を示す請求項4記載の化合物。6, R3 is the following formula: 5. The compound according to claim 4, which has a group represented by:

7.2未満の沃素価を有する請求項1記載の化合物。2. A compound according to claim 1 having an iodine number of less than 7.2.

8、RおよびR’は同じものを示す請求項1記載の化合物。8. The compound according to claim 1, wherein R and R' represent the same thing.

求項1記載の化合物。A compound according to claim 1.

12、x、yおよび/または2はいずれも1〜15の数である請求項1記載の化 合物。12, x, y and/or 2 are all numbers from 1 to 15. Compound.

たものであり、請求項1記載の化合物は対応するポリエステルを含有している請 求項1記載の化合物。and the compound according to claim 1 contains the corresponding polyester. A compound according to claim 1.

14、前記化合物がモノ−、ジーおよびトリーエステルの混合物である請求項1 3記載の化合物。14. Claim 1, wherein said compound is a mixture of mono-, di- and tri-esters. 3. The compound described in 3.

22、さらに次式: で表わされる未アルコキシル化ゲルベアルコールを含有する請求項20記載の組 成物。22, and further the following formula: 21. The set according to claim 20, containing an unalkoxylated Guerbet alcohol represented by A product.

23、前記未アルコキシル化ゲルベアルコールが約50重量%以下の量で存在す る請求項22記載の組成物。23. said unalkoxylated Guerbet alcohol is present in an amount of about 50% by weight or less 23. The composition according to claim 22.

24、前記未アルコキシル化ゲルベアルコールが約30重量%以下の量で存在す る請求項23記載の組成物。24. said unalkoxylated Guerbet alcohol is present in an amount of about 30% by weight or less 24. The composition according to claim 23.

25、請求項1記載のアルコキシル化化合物を製造するに当り、 (式中のRおよびR1はいずれも6〜15個の炭素原子を有するアルキル基を示 す)で表わされるゲルベアルコールを、プロピレンオキシドとプロピレンオキシ ドおよびエチレンオキシドとからなる群から選定されたアルキレンオキシドと、 アルコール対アルキレンオキシドのモル比的1:1〜約l:20において、約り 5℃〜約200℃の温度で接触させ、 所要に応じて生成したアルコキシル化生成物を有機酸によって、アルコキシル化 化合物対酸の重量比約1=5〜約5:1において、真空下に約1=5〜約250 ℃の温度でエステル化することを特徴とするアルコキシル化化合物の製造方法。25. In producing the alkoxylated compound according to claim 1, (R and R1 in the formula both represent an alkyl group having 6 to 15 carbon atoms. Guerbet alcohol represented by propylene oxide and propylene oxy an alkylene oxide selected from the group consisting of At a molar ratio of alcohol to alkylene oxide of 1:1 to about 1:20, about contact at a temperature of 5°C to about 200°C, Alkoxylate the generated alkoxylation product with an organic acid as required. At a compound to acid weight ratio of about 1=5 to about 5:1 under vacuum, about 1=5 to about 250 A method for producing an alkoxylated compound, characterized by esterification at a temperature of °C.

26、先ずゲルベアルコールをEOと接触させ、次いでPOと接触させて、Xと yとの和が1〜20であり、yが1〜15の数を示す実質的にブロック構造を有 する請求項1記載のアルコキシル化アルコール生成物を生成する請求項25記載 の方法。26. First contact Guerbet alcohol with EO, then contact with PO, and then with X. The sum with y is 1 to 20, and y has a substantially block structure in which y is a number of 1 to 15. Claim 25, wherein the alkoxylated alcohol product of Claim 1 is produced by: the method of.

27、ゲルベアルコールをEOとPOとの混合物と接触させ、不均一構造の生成 物を得る請求項25記載の方法。27. Contacting Guerbet alcohol with a mixture of EO and PO to generate a heterogeneous structure 26. The method of claim 25 for obtaining a product.

28、ゲルベアルコールをPOのみと接触させる請求項25記載の方法。28. The method of claim 25, wherein Guerbet alcohol is contacted only with PO.

(式中のRおよびR1はそれぞれ別個に1〜20個の炭素原子を有するアルキル 基を示し;かつR+R’における全炭素原子数は4個以上であり、yは1〜20 の数を示し;Xおよび2は整数であって、Xと2との和は0〜20であり;R3 は未置換のアルケニル基、あるいは−COOH基またはCOR’基で置換された 置換アルキル基または置換アルケニル基を示し、あるいはR3は次式:で表わさ れるシクロへキセニル基を示し、かつmは1〜3の数を示し:nはいずれの場合 にもO〜10の数を示し;pおよびrはいずれも0〜1の数を示し、R5はいず れの場合にも水酸基または次式: で表わされる基を示し、R6は1〜10個の炭素原子を有するアルケニル基また はアルキル基を示す)で表わされることを特徴とするアルコキシル化化合物。(wherein R and R1 are each independently an alkyl group having 1 to 20 carbon atoms) represents a group; and the total number of carbon atoms in R+R' is 4 or more, and y is 1 to 20 represents the number; X and 2 are integers, and the sum of X and 2 is 0 to 20; R3 is an unsubstituted alkenyl group, or substituted with a -COOH group or a COR' group represents a substituted alkyl group or a substituted alkenyl group, or R3 is represented by the following formula: represents a cyclohexenyl group, and m represents a number from 1 to 3; n is in either case also represents a number from 0 to 10; p and r both represent a number from 0 to 1, and R5 represents a number from 0 to 1. In both cases, hydroxyl group or the following formula: represents a group represented by R6 is an alkenyl group having 1 to 10 carbon atoms or represents an alkyl group).

36、x、yおよび/または2は少なくとも1の数を示す請求項35記載の化合 物。36. The compound according to claim 35, wherein x, y and/or 2 represent a number of at least 1. thing.

37、RおよびR’はいずれも6〜15個の炭素原子を有するアルキル基を示す 請求項35記載の化合物。37, R and R' each represent an alkyl group having 6 to 15 carbon atoms 36. A compound according to claim 35.

38、液体潤滑剤組成物において、約0.05重量%〜約1重量%の請求項35 記載の化合物、および水、鉱油、パラフィン系油、脂肪酸エステル、脂肪酸ケト ン、アルコキシル化エステル、アルコキシル化ケトンおよびこれらの混合物から なる群から選定した前記化合物のためのキャリアを含有することを特徴とする液 体潤滑剤組成物。38. In a liquid lubricant composition, from about 0.05% to about 1% by weight of claim 35 Compounds listed and water, mineral oil, paraffinic oil, fatty acid ester, fatty acid keto from alkoxylated esters, alkoxylated ketones and mixtures thereof. A liquid characterized by containing a carrier for the compound selected from the group consisting of: Body lubricant composition.

39、さらに次式; (式中のRおよびR1はいずれも1〜20個の炭素原子を有するアルキル基を示 す)で表わされる未アルコキシル化ゲルベアルコールを含有する請求項38記載 の組成物。39, further the following formula; (R and R1 in the formula both represent an alkyl group having 1 to 20 carbon atoms. Claim 38 containing unalkoxylated Guerbet alcohol represented by Composition of.

40、請求項35記載のアルコキシル化化合物を合成するに当(式中のRおよび R’はいずれも1〜20個の炭素原子を有するアルキル基を示す)で表わされる ゲルベアルコールを、プロピレンオキシドとプロピレンオキシドおよびエチレン オキシドとからなる群から選定したアルキレンオキシドと、アルコール対アルキ レンオキシドのモル比的1:1〜約1:20において、約り5℃〜約200℃の 温度で接触させて前記ゲルベアルコールのアルコキシル化付加物を生成し;生成 したアルコキシル化生成物を1〜20個の炭素原子を有する有機酸によって、ア ルコキシル化アルコール対酸の重量比的1:5〜約5=1において、真空下に約 り25℃〜約250℃の温度でエステル化し、この際前記有機酸として未置換の アルケニルカルボン酸あるいは−000)1基またはCOR’基で置換された脂 肪族アルキルカルボン酸およびアルケニルカルボン酸または次式;で表わされる シクロへキシルカルボン酸からなる群から選定され、mは1〜3の数を示し;n はいずれの場合にもO〜10の数を示し;rおよびpはいずれも0また番マ1の 数を示し、1li4は1〜15個の炭素原子を有するアルキル基またはアルケニ ル基を示し, RSはいずれの場合1こも水酸基または次式: で表わされる基を示し;R′は1〜10個の炭素原子を有するアルキル基または アルケニル基を示す有機酸を使用することを特徴とするアルコキシルターゲット 化合物の合成方法。40, for synthesizing the alkoxylated compound according to claim 35 (wherein R and R' is an alkyl group having 1 to 20 carbon atoms) Guerbet alcohol, propylene oxide and propylene oxide and ethylene an alkylene oxide selected from the group consisting of When the molar ratio of ren oxide is 1:1 to about 1:20, the temperature is about 5°C to about 200°C. contacting at a temperature to form an alkoxylated adduct of the Guerbet alcohol; The alkoxylated product is treated with an organic acid having 1 to 20 carbon atoms. At a weight ratio of 1:5 to about 5=1 of rukoxylated alcohol to acid, about esterification at a temperature of 25°C to about 250°C, in which unsubstituted organic acid is used as the organic acid. alkenylcarboxylic acid or -000) or fatty acid substituted with COR' group Aliphatic alkyl carboxylic acids and alkenyl carboxylic acids or represented by the following formula; selected from the group consisting of cyclohexylcarboxylic acids, m represents a number from 1 to 3; n indicates a number from 0 to 10 in each case; r and p are both 0 or the number ma1. 1li4 is an alkyl group or alkenyl group having 1 to 15 carbon atoms. In each case, RS represents a hydroxyl group or the following formula: represents a group represented by; R' is an alkyl group having 1 to 10 carbon atoms or Alkoxyl target characterized by using an organic acid exhibiting an alkenyl group Methods for synthesizing compounds.

41、先ずゲルベアルコールをEOと接触させ、次G)でPOと接触させて、X とyとの和が1〜20であり、yが1〜15の数を示す実質的にブロック構造を 有する請求項35記載のアルコキシル化アルコール生成物を生成する請求項40 記載の方法。41. First, contact Guerbet alcohol with EO, then contact with PO in G), The sum of and y is 1 to 20, and y is a number of 1 to 15. Claim 40 producing the alkoxylated alcohol product of Claim 35 having Method described.

42、ゲルベアルコールをEOとPOとの混合物と接触させ、不均一構造の生成 物を得る請求項40記載の方法。42. Contacting Guerbet alcohol with a mixture of EO and PO to generate a heterogeneous structure 41. The method of claim 40 for obtaining a product.

43、ゲルベアルコールをPOのみと接触させる請求項40記載の方法。43. The method of claim 40, wherein Guerbet alcohol is contacted only with PO.

44、絞り成形、鍛造、アイアニング、圧延、波形加工またはキャンニングのう ちの少なくとも1種の操作において金属を処理して金属容器を成形するに当たり 、成形前に操作中の摩擦を低下させるのに十分な潤滑作用を示す量の請求項35 記載の化合物と前記金属とを接触させることを特徴とする金属容器の成形方法。44. Drawing, forging, ironing, rolling, corrugating or canning in processing metal to form a metal container in at least one of the following operations: , in an amount exhibiting sufficient lubrication to reduce friction during operation prior to molding. A method for forming a metal container, comprising bringing the compound described above into contact with the metal.

45、RおよびR’はいずれも 6〜15個の炭素原子を有するアルキル基を示 す請求項44記載の方法。45, R and R' each represent an alkyl group having 6 to 15 carbon atoms. 45. The method according to claim 44.

46、xまたはyは平均して1〜約15である請求項44記載の方法。46. The method of claim 44, wherein x or y is on average from 1 to about 15.

47、x十zの和は少なくとも4である請求項44記載の方法。47. The method of claim 44, wherein the sum of x and z is at least 4.

48.2は少なくとも1である請求項44記載の方法。45. The method of claim 44, wherein 48.2 is at least 1.

国際調査報告 1mM11311IM−^qe−+1+4−9−10PCTzυ5g81002 7εinternational search report 1mM11311IM-^qe-+1+4-9-10PCTzυ5g81002 7ε

Claims (34)

【特許請求の範囲】[Claims] 1.次式: ▲数式、化学式、表等があります▼ (式中のRおよびR1はそれぞれ別個に1〜20個の炭素原子を有するアルキル 基を示し、かつR+R1の全炭素原子数は4個以上であり;yは1〜20の数を 示し;整数xおよびzの和は0〜20であり;R2は水素原子、アルキル基また は▲数式、化学式、表等があります▼基を示し、かつR3は水素原子、未置換の アルキル基またはアルケニル基、あるいはカルボキシル基、COR5基または次 式: ▲数式、化学式、表等があります▼ または ▲数式、化学式、表等があります▼ で表わされるシクロヘキセにル基で置換されたアルキル基またはアルケニル基を 示し、かつmは1〜3の数を示し;コはいずれの場合にも0〜10の整数を示し ;pおよびyはそれぞれ0〜1の数を示し;R5はいずれの場合にも水酸基また は次式: ▲数式、化学式、表等があります▼ で表わされるアルコキシル化された基を示す)で表わされることを特徴とするア ルコキシル化化合物。1. The following formula: ▲Contains mathematical formulas, chemical formulas, tables, etc.▼ (wherein R and R1 are each independently an alkyl group having 1 to 20 carbon atoms) group, and the total number of carbon atoms in R+R1 is 4 or more; y is a number from 1 to 20; The sum of integers x and z is 0 to 20; R2 is a hydrogen atom, an alkyl group, or ▲There are mathematical formulas, chemical formulas, tables, etc.▼Indicates a group, and R3 is a hydrogen atom, an unsubstituted Alkyl or alkenyl group, or carboxyl group, COR5 group or formula: ▲Contains mathematical formulas, chemical formulas, tables, etc.▼ or ▲Contains mathematical formulas, chemical formulas, tables, etc.▼ An alkyl group or alkenyl group substituted with a cyclohexyl group represented by and m represents a number from 1 to 3; ko represents an integer from 0 to 10 in both cases. ; p and y each represent a number of 0 to 1; R5 is a hydroxyl group or is the following formula: ▲Contains mathematical formulas, chemical formulas, tables, etc.▼ an alkoxylated group represented by) Lukoxylated compounds. 2.xおよび/またはzは少なくとも1の整数を示す請求項1記載の化合物。2. 2. A compound according to claim 1, wherein x and/or z represent an integer of at least 1. 3.R2は水素原子を示す請求項1記載の化合物。3. 2. The compound according to claim 1, wherein R2 represents a hydrogen atom. 4.R2は▲数式、化学式、表等があります▼基を示す請求項1記載の化合物。4. 2. The compound according to claim 1, wherein R2 represents a ▼ group having a mathematical formula, a chemical formula, a table, etc. 5.R3は−水素原子を示す請求項4記載の化合物。5. 5. The compound according to claim 4, wherein R3 represents -hydrogen atom. 6.R3は次式: ▲数式、化学式、表等があります▼ で表される基を示す請求項4記載の化合物。6. R3 is the following formula: ▲Contains mathematical formulas, chemical formulas, tables, etc.▼ 5. The compound according to claim 4, which has a group represented by: 7.2未満の沃素価を有する請求項1記載の化合物。2. A compound according to claim 1 having an iodine number of less than 7.2. 8.RおよびR1は同じものを示す請求項1記載の化合物。8. 2. The compound according to claim 1, wherein R and R1 represent the same thing. 9.RおよびR1は飽和基を示す請求項1記載の化合物。9. 2. A compound according to claim 1, wherein R and R1 represent saturated groups. 10.RおよびR1は2〜16個の炭素原子を有するアルキル基を示す請求項1 記載の化合物。10. Claim 1: R and R1 represent an alkyl group having 2 to 16 carbon atoms. Compounds described. 11.R2は水素原子と▲数式、化学式、表等があります▼基とが混り合ったも のを示す請求項1記載の化合物。11. R2 is a mixture of a hydrogen atom and a ▲mathematical formula, chemical formula, table, etc.▼ group. The compound according to claim 1, which exhibits the following. 12.x,yおよび/またはzはいずれも1〜15の数である請求項1記載の化 合物。12. The compound according to claim 1, wherein x, y and/or z are all numbers from 1 to 15. Compound. 13.R2は▲数式、化学式、表等があります▼基を示し、▲数式、化学式、表 等があります▼基は多塩基酸から得られたものであり、請求項1記載の化合物は 対応するポリエステルを含有する請求項1記載の化合物。13. R2 indicates a group that has a ▲ mathematical formula, chemical formula, table, etc. etc. The ▼ group is obtained from a polybasic acid, and the compound according to claim 1 is 2. A compound according to claim 1 containing a corresponding polyester. 14.前記化合物がモノ−、ジ−およびトリ−エステルの混合物である請求項1 3記載の化合物。14. Claim 1 wherein said compound is a mixture of mono-, di- and tri-esters. 3. The compound described in 3. 15.6−(ヘプト−1−エニル)−5−ベンチル−3−シクロヘキセン−1, 2−ジノニル酸エステルを含有する混合物である請求項1記載の化合物。15.6-(hept-1-enyl)-5-bentyl-3-cyclohexene-1, 2. The compound according to claim 1, which is a mixture containing a 2-dinonylic acid ester. 16.5,6−(ジブチル−ヘキサヒドロ−1,2−ナフタレンジカプリル酸エ ステルを含有する混合物である請求項1記載の化合物。16.5,6-(dibutyl-hexahydro-1,2-naphthalene dicaprylate) 2. A compound according to claim 1, which is a mixture containing stellates. 17.9−ノニリデン−10−ペンチル−1,18−オクタデカンジカルボン酸 エステルを含有する混合物である請求項1記載の化合物。17.9-nonylidene-10-pentyl-1,18-octadecanedicarboxylic acid 2. A compound according to claim 1, which is a mixture containing an ester. 18.エトキシル化−プロボキシル化−2−デシルデカノールのウラリルエステ ルである請求項1記載の化合物。18. Uralyl ester of ethoxylated-proboxylated-2-decyldecanol 2. The compound according to claim 1, which is 19.プロボキシル化−2−デシルデカノールのココエステルである請求項1記 載の化合物。19. Claim 1 which is a cocoester of proboxylated-2-decyldecanol. Compounds listed. 20.液体潤滑剤組成物において、約0.05重量%〜約1重量%の請求項1記 載の化合物、および水、鉱油、パラフィン系油、脂肪酸エステル、脂肪酸ケトン 、アルコキシル化エステル、アルコキシル化ケトンおよびこれらの混合物からな る群から選定した前記化合物のためのキャリアを含有する酸化および悪臭に対す る抵抗性の大きいことを特徴とする液体潤滑剤組成物。20. from about 0.05% to about 1% by weight in a liquid lubricant composition. and water, mineral oil, paraffinic oil, fatty acid esters, fatty acid ketones. , alkoxylated esters, alkoxylated ketones and mixtures thereof. containing a carrier for said compound selected from the group of A liquid lubricant composition characterized by high resistance to 21.前記キャリヤは水および鉱油からなる群から選定したキャリアであり、キ ャリア対前記アルコキシル化化合物の重量比が約20:1〜約1:20である請 求項20記載の組成物。21. The carrier is a carrier selected from the group consisting of water and mineral oil; The weight ratio of carrier to said alkoxylated compound is from about 20:1 to about 1:20. 21. The composition according to claim 20. 22.さらに次式: ▲数式、化学式、表等があります▼ で表わされる未アルコキシル化ゲルベアルコールを含有する請求項20記載の組 成物。22. Furthermore, the following formula: ▲Contains mathematical formulas, chemical formulas, tables, etc.▼ 21. The set according to claim 20, containing an unalkoxylated Guerbet alcohol represented by A product. 23.前記未アルコキシル化ゲルベアルコールが約50重量%以下の量で存在す る請求項22記載の組成物。23. the unalkoxylated Guerbet alcohol is present in an amount up to about 50% by weight; 23. The composition according to claim 22. 24.前記未アルコキシル化ゲルベアルコールが約30重量%以下の量で存在す る請求項23記載の組成物。24. the unalkoxylated Guerbet alcohol is present in an amount up to about 30% by weight; 24. The composition according to claim 23. 25.請求項1記載のアルコキシル化化合物を製造するに当り、 次式: ▲数式、化学式、表等があります▼ (式中のRおよびR1はいずれも1〜20個の炭素原子を有するアルキル基を示 す)で表わされるゲルベアルコールを、プロピレンオキシドとプロピレンオキシ ドおよびエチレンオキシドとからなる群から選定したアルキレンオキシドと、ア ルコール対アルキレンオキシドのモル比約1:1〜約1:20において、約85 ℃〜約200℃の温度で接触させ、 所要に応じて生成したアルコキシル化生成物を有機酸によって、アルコキシル化 化合物対酸の重量比約1:5〜約5:1において、真空下に約125℃〜約25 0℃の温度でエステル化することを特徴とするアルコキシル化化合物の製造方法 。25. In producing the alkoxylated compound according to claim 1, The following formula: ▲Contains mathematical formulas, chemical formulas, tables, etc.▼ (R and R1 in the formula both represent an alkyl group having 1 to 20 carbon atoms. Guerbet alcohol represented by propylene oxide and propylene oxy alkylene oxide selected from the group consisting of At a molar ratio of alcohol to alkylene oxide of about 1:1 to about 1:20, about 85 ℃~about 200℃, Alkoxylate the generated alkoxylation product with an organic acid as required. from about 125° C. to about 25° C. under vacuum at a weight ratio of compound to acid of about 1:5 to about 5:1. A method for producing an alkoxylated compound characterized by esterification at a temperature of 0°C . 26.先ずゲルベアルコールをEOと接触させ、次いでPOと接触させて、x, zまたはxとyとの和が1〜20であり、yが1〜15の数を示す実質的にブロ ツク構造を有する請求項1記載のアルコキシル化アルコール生成物を生成する請 求項25記載の方法。26. Guerbet alcohol is first contacted with EO and then with PO to produce x, z or the sum of x and y is from 1 to 20, and y is a number from 1 to 15. A method for producing an alkoxylated alcohol product according to claim 1 having a structure of The method according to claim 25. 27.ゲルベアルコールをEOとPOとの混合物と接触させ、不均一構造の生成 物を得る請求項25記載の方法。27. Contacting Guerbet alcohol with a mixture of EO and PO to generate a heterogeneous structure 26. The method of claim 25 for obtaining a product. 28.ゲルベアルコールをPOのみと接触させる請求項25記載の方法。28. 26. The method of claim 25, wherein Guerbet alcohol is contacted only with PO. 29.アルコキシル化ゲルベアルコールを、C1〜C20脂肪族カルボン酸、C 1〜C20芳香族カルボン酸、C1〜C20オレフィン系不飽和カルボン酸およ び次式:▲数式、化学式、表等があります▼ または ▲数式、化学式、表等があります▼ (式中のnおよびR5は請求項1に記載したもきと同一のものを示し;mは1〜 3の数を示し;rおよびpはいずれも0または1の数を示し;R4は1〜15個 の炭素原子を有するアルキル基またはアルケニル基を示す)で表わされるシクロ ヘキセニル有機酸からなる群から選定した1種の有機酸でエステル化する請求項 25記載の方法。29. The alkoxylated Guerbet alcohol is a C1-C20 aliphatic carboxylic acid, C 1-C20 aromatic carboxylic acid, C1-C20 olefinically unsaturated carboxylic acid and Bi-formula: ▲ Contains mathematical formulas, chemical formulas, tables, etc. ▼ or ▲Contains mathematical formulas, chemical formulas, tables, etc.▼ (n and R5 in the formula are the same as those described in claim 1; m is 1 to Represents the number 3; r and p both represent the number 0 or 1; R4 represents 1 to 15 cyclo, which represents an alkyl or alkenyl group having carbon atoms A claim of esterification with one type of organic acid selected from the group consisting of hexenyl organic acids. 25. The method described in 25. 30.請求項29記載の方法の生成物。30. 30. A product of the method of claim 29. 31.請求項25記載の方法の生成物。31. 26. A product of the method of claim 25. 32.前記有機酸がモノカルボン酸である請求項29記載の方法。32. 30. The method of claim 29, wherein the organic acid is a monocarboxylic acid. 33.前記有機酸がジカルボン酸である請求項29記載の方法。33. 30. The method of claim 29, wherein the organic acid is a dicarboxylic acid. 34.前記有機酸がトリカルボン酸である請求項29記載の方法。34. 30. The method of claim 29, wherein the organic acid is a tricarboxylic acid.
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