TW200918661A - Lubrication oil compositions - Google Patents
Lubrication oil compositions Download PDFInfo
- Publication number
- TW200918661A TW200918661A TW097132311A TW97132311A TW200918661A TW 200918661 A TW200918661 A TW 200918661A TW 097132311 A TW097132311 A TW 097132311A TW 97132311 A TW97132311 A TW 97132311A TW 200918661 A TW200918661 A TW 200918661A
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- TW
- Taiwan
- Prior art keywords
- weight
- additive
- lubricating oil
- oil composition
- acid
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M169/00—Lubricating compositions characterised by containing as components a mixture of at least two types of ingredient selected from base-materials, thickeners or additives, covered by the preceding groups, each of these compounds being essential
- C10M169/04—Mixtures of base-materials and additives
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M107/00—Lubricating compositions characterised by the base-material being a macromolecular compound
- C10M107/20—Lubricating compositions characterised by the base-material being a macromolecular compound containing oxygen
- C10M107/30—Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- C10M107/32—Condensation polymers of aldehydes or ketones; Polyesters; Polyethers
- C10M107/34—Polyoxyalkylenes
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2207/00—Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
- C10M2207/02—Hydroxy compounds
- C10M2207/023—Hydroxy compounds having hydroxy groups bound to carbon atoms of six-membered aromatic rings
- C10M2207/026—Hydroxy compounds having hydroxy groups bound to carbon atoms of six-membered aromatic rings with tertiary alkyl groups
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2207/00—Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
- C10M2207/28—Esters
- C10M2207/287—Partial esters
- C10M2207/289—Partial esters containing free hydroxy groups
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2209/00—Organic macromolecular compounds containing oxygen as ingredients in lubricant compositions
- C10M2209/02—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- C10M2209/06—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing monomers having an unsaturated radical bound to an acyloxy radical of saturated carboxylic or carbonic acid
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2209/00—Organic macromolecular compounds containing oxygen as ingredients in lubricant compositions
- C10M2209/10—Macromolecular compoundss obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- C10M2209/102—Polyesters
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2209/00—Organic macromolecular compounds containing oxygen as ingredients in lubricant compositions
- C10M2209/10—Macromolecular compoundss obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- C10M2209/103—Polyethers, i.e. containing di- or higher polyoxyalkylene groups
- C10M2209/104—Polyethers, i.e. containing di- or higher polyoxyalkylene groups of alkylene oxides containing two carbon atoms only
- C10M2209/1045—Polyethers, i.e. containing di- or higher polyoxyalkylene groups of alkylene oxides containing two carbon atoms only used as base material
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2209/00—Organic macromolecular compounds containing oxygen as ingredients in lubricant compositions
- C10M2209/10—Macromolecular compoundss obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- C10M2209/103—Polyethers, i.e. containing di- or higher polyoxyalkylene groups
- C10M2209/105—Polyethers, i.e. containing di- or higher polyoxyalkylene groups of alkylene oxides containing three carbon atoms only
- C10M2209/1055—Polyethers, i.e. containing di- or higher polyoxyalkylene groups of alkylene oxides containing three carbon atoms only used as base material
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2215/00—Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant compositions
- C10M2215/02—Amines, e.g. polyalkylene polyamines; Quaternary amines
- C10M2215/06—Amines, e.g. polyalkylene polyamines; Quaternary amines having amino groups bound to carbon atoms of six-membered aromatic rings
- C10M2215/064—Di- and triaryl amines
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2215/00—Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant compositions
- C10M2215/02—Amines, e.g. polyalkylene polyamines; Quaternary amines
- C10M2215/06—Amines, e.g. polyalkylene polyamines; Quaternary amines having amino groups bound to carbon atoms of six-membered aromatic rings
- C10M2215/064—Di- and triaryl amines
- C10M2215/065—Phenyl-Naphthyl amines
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2215/00—Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant compositions
- C10M2215/22—Heterocyclic nitrogen compounds
- C10M2215/223—Five-membered rings containing nitrogen and carbon only
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2217/00—Organic macromolecular compounds containing nitrogen as ingredients in lubricant compositions
- C10M2217/02—Macromolecular compounds obtained from nitrogen containing monomers by reactions only involving carbon-to-carbon unsaturated bonds
- C10M2217/028—Macromolecular compounds obtained from nitrogen containing monomers by reactions only involving carbon-to-carbon unsaturated bonds containing monomers having an unsaturated radical bound to a nitrogen-containing hetero ring
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2219/00—Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions
- C10M2219/04—Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions containing sulfur-to-oxygen bonds, i.e. sulfones, sulfoxides
- C10M2219/044—Sulfonic acids, Derivatives thereof, e.g. neutral salts
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2219/00—Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions
- C10M2219/06—Thio-acids; Thiocyanates; Derivatives thereof
- C10M2219/062—Thio-acids; Thiocyanates; Derivatives thereof having carbon-to-sulfur double bonds
- C10M2219/066—Thiocarbamic type compounds
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2219/00—Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions
- C10M2219/10—Heterocyclic compounds containing sulfur, selenium or tellurium compounds in the ring
- C10M2219/104—Heterocyclic compounds containing sulfur, selenium or tellurium compounds in the ring containing sulfur and carbon with nitrogen or oxygen in the ring
- C10M2219/106—Thiadiazoles
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2223/00—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions
- C10M2223/02—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions having no phosphorus-to-carbon bonds
- C10M2223/04—Phosphate esters
- C10M2223/043—Ammonium or amine salts thereof
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2223/00—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions
- C10M2223/02—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions having no phosphorus-to-carbon bonds
- C10M2223/04—Phosphate esters
- C10M2223/045—Metal containing thio derivatives
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2223/00—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions
- C10M2223/02—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions having no phosphorus-to-carbon bonds
- C10M2223/04—Phosphate esters
- C10M2223/047—Thioderivatives not containing metallic elements
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2229/00—Organic macromolecular compounds containing atoms of elements not provided for in groups C10M2205/00, C10M2209/00, C10M2213/00, C10M2217/00, C10M2221/00 or C10M2225/00 as ingredients in lubricant compositions
- C10M2229/04—Siloxanes with specific structure
- C10M2229/041—Siloxanes with specific structure containing aliphatic substituents
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2010/00—Metal present as such or in compounds
- C10N2010/04—Groups 2 or 12
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2020/00—Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
- C10N2020/01—Physico-chemical properties
- C10N2020/02—Viscosity; Viscosity index
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2020/00—Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
- C10N2020/01—Physico-chemical properties
- C10N2020/04—Molecular weight; Molecular weight distribution
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- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
- C10N2030/02—Pour-point; Viscosity index
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- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
- C10N2030/06—Oiliness; Film-strength; Anti-wear; Resistance to extreme pressure
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- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
- C10N2030/08—Resistance to extreme temperature
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
- C10N2030/12—Inhibition of corrosion, e.g. anti-rust agents or anti-corrosives
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
- C10N2030/64—Environmental friendly compositions
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Emergency Medicine (AREA)
- Lubricants (AREA)
Abstract
Description
200918661 九、發明說明: 【發明所屬之技術領域】 本發明係關於包含⑴聚(三亞曱基-伸乙基醚)二醇及(ii) 包含某些指定添加劑組合之添加劑複合包之組合物及含有 該等組合物之满滑油。 . 本申請案與以下參考文獻有關:共同擁有之2006年11月 7 曰申請之題為"POLYTRIMETHYLENE ETHER GLYCOL ESTERS"的美國申請案第11/593,954號;共同擁有之與其 ( 同時申請之題為"LUBRICATION OIL COMPOSITIONS"的 美國臨時申請案第60/957,7 16號;共同擁有之與其同時申 請之題為"LUBRICATION OIL COMPOSITIONS"的美國臨 時申請案第60/957,725號(内部參考CL3886);及共同擁有 之與其同時申請之題為 "LUBRICATION OIL COMPOSITIONS”的美國臨時申請案第60/957,722號(内部 參考 CL3887)。 【先前技術】 ^ 某些聚三亞甲基醚二醇("P03G")(包括(但不限於)聚(三 亞甲基-伸乙基醚)二醇)以及其單酯及二酯("P03G酯")具有 一定特性而使其適用於各種領域,包括用作潤滑劑,此如 共同擁有之US7179769及2006年11月7日申請之題為 "POLYTRIMETHYLENE ETHER GLYCOL ESTERS"的美國 申請案第11/593,954號中所揭示。 由於該等特性,故希望調配基於P03G及P03G酯之潤滑 劑組合物。 134067.doc 200918661 【發明内容】 本發明係關於基於特定類型之P03G(聚(三亞甲基-伸乙 基_ )二酵-PTEEG)與特定添加劑組合之組合的組合物,該 等組合物具有一定特性而使其尤其適合於潤滑終端用途。 在一實施例中’提供一種潤滑油組合物,其包含⑴包含 在環境溫度下為流體之PTEEG之基本流體原料及(ii)包含 以下各物之添加劑複合包: (a) 抗磨添加劑複合包,其包含約〇·5重量%至約2.0重 量%(以組合物總重量計)之包含磷酸胺抗磨添加劑及硫代 磷酸酯(phosphorothionate)抗磨添加劑之混合物,及 (b) 約0.1重量%至約0.5重量%(以組合物總重量計)之充 當極壓添加劑、抗氧化添加劑或極壓添加劑與抗氧化添加 劑之添加劑。在較佳實施例中,充當極壓添加劑、抗氧化 添加劑或極壓添加劑與抗氧化添加劑之添加劑為亞甲基雙 (二烷基二硫代胺基甲酸酯)。 當PTEEG係基於生物學上所產生之ι,3-丙二醇時,可提 供具有極高可再生内容物之潤滑劑組合物。 【實施方式】 除非另作定義,否則本文中所用之所有技術及科學術語 均具有與熟習本發明所屬技術之一般技術者之通常理解相 同的意義。在矛盾之情況下,將以本說明書(包括定義)為 準。 ‘、、' 除非明確說明’否則商標均以大寫字母展示。 除非另有說明,否則所有百分比、份數、比率等均以重 134067.doc 200918661 量計。 當數量、濃度或其他值或參數係以範圍、較佳範圍或一 列上限較佳值與下限較佳值形式給出時,此應理解為具體 地揭不由任何範圍上限或較佳值與任何範圍下限或較佳值 之任何對形成之所有範圍,而與範圍是否分別地被揭示無 關。除非另有說明,否則當本文中描述一定範圍之數值 時,該範圍意欲包括其端點及該範圍内之所有整數及分 數。當界定一範圍時,本發明之範疇並不意欲受限於所述 特定值。 當使用術語”約”描述範圍之值或端點時,本揭示案應理 解為包括所指之特定值或端點。 如本文中所使用之術語"包含,,、”包括"、,,具有"或其任 何其他變體意欲涵蓋非排他性包括。舉例而言,包含一列 元件之製程、方法、製品或裝置並非必然僅限於彼等元 件’而可包括其他未明確列出之元件或該等製程、方法、 製品或裝置所固有之元件。此外,除非明確相反地說明, 否則”或”係指包括性之或而非排他性之或。舉例而言,以 下項中之任一項均滿足A4B狀況:A為真(或存在)且0為 假(或不存在);A為假(或不存在)且b為真(或存在);及八與 B均為真(或存在)。 使用,,一 ”用於描述本發明之元素及組份。此舉僅為方便 之故且給出本發明之一般含義。除非明顯意謂其他意義, 否則此描述應理解為包括一個或至少一個且單數亦包括複 數。 134067.doc 200918661 本文中之材料、方法及實例僅為說明性的且除如特別說 明以外’其並不意欲具限制性。儘管類似或等同於本文中 所述之彼等方法及材料的方法及材料可用於本發明之實踐 或測試,但本文中描述合適之方&及#_。 基本流體原料 如上所指不’適用於本發明之潤滑油組合物的基本流體 原料包含在環境溫度(25t)Ts流體之pteeg。該基液原 料亦可包含其他天然及/或合成流體辅潤滑劑。 天然流體輔潤滑劑之實例包括4常來源於植物且通常由 甘油三酯組成之植物油基潤滑劑。一般而言,此等者在室 溫下為液體。儘管植物之許多不同部分可產生油,但在實 務中通常主要自油籽植物之種子提取油。該等油包括可食 用與不可食用油,且包括(例如)高油酸葵花籽油、菜籽 油、大豆油、蓖麻油及其類似物,以及改質油,諸如 US6583302(脂肪酸酯)及 L Maichev,"plant 〇il Based200918661 IX. Description of the Invention: [Technical Field of the Invention] The present invention relates to a composition comprising (1) poly(trimethylene-ethyl ether) diol and (ii) an additive composite package comprising certain specified additive combinations and A full lubricating oil containing the compositions. This application is related to the following reference: commonly owned U.S. Application No. 11/593,954 entitled "POLYTRIMETHYLENE ETHER GLYCOL ESTERS", filed November 7, 2006, co-owned; "LUBRICATION OIL COMPOSITIONS" US Provisional Application No. 60/957, 7 16; commonly owned US Provisional Application No. 60/957,725 (internal reference CL3886) entitled "LUBRICATION OIL COMPOSITIONS" And co-owned U.S. Provisional Application No. 60/957,722, entitled "LUBRICATION OIL COMPOSITIONS" (internal reference CL3887). [Prior Art] ^ Certain polytrimethylene ether glycols ("P03G") (including (but not limited to) poly(trimethylene-extended ethyl ether) diol) and its monoesters and diesters ("P03G esters") have certain properties that make them suitable for use in a variety of applications. Including the use of lubricants, such as US 7179769, co-owned, and US application entitled "POLYTRIMETHYLENE ETHER GLYCOL ESTERS", filed on November 7, 2006 It is disclosed in the No. 11/593,954. Because of these characteristics, it is desirable to formulate a lubricant composition based on P03G and P03G esters. 134067.doc 200918661 [Summary of the Invention] The present invention relates to a specific type of P03G (poly (Sanya) A combination of methyl-extended ethyl-)-fermentation-PTEEG) in combination with a particular additive, the compositions having properties that make them particularly suitable for lubricating end uses. In one embodiment, 'providing a lubricating oil a composition comprising (1) a base fluid feedstock comprising PTEEG fluid at ambient temperature and (ii) an additive composite package comprising: (a) an antiwear additive composite package comprising from about 5% by weight to About 2.0% by weight (based on the total weight of the composition) comprising a mixture of a phosphate amine antiwear additive and a phosphorothionate antiwear additive, and (b) from about 0.1% to about 0.5% by weight (by composition) The total weight of the additive acts as an extreme pressure additive, an antioxidant additive or an extreme pressure additive and an antioxidant additive. In a preferred embodiment, it acts as an extreme pressure additive, an antioxidant additive. Extreme pressure additive or additives of antioxidant additives is methylene bis (dialkyldithiocarbamate urethane). When PTEEG is based on a biologically produced i-, 3-propanediol, a lubricant composition having a very high reproducible content can be provided. [Embodiment] All technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which the invention pertains, unless otherwise defined. In case of conflict, the present specification (including definitions) will prevail. ‘,, ' Unless otherwise stated, the trademarks are displayed in capital letters. All percentages, parts, ratios, etc., are by weight 134067.doc 200918661 unless otherwise stated. When a quantity, a concentration, or other value or parameter is given by a range, a preferred range, or a list of upper and lower preferred values, this should be understood to specifically exclude any range of upper or preferred values and any range. All ranges formed by any pair of lower or preferred values are independent of whether the ranges are disclosed separately. Unless otherwise stated, when a range of values are recited herein, the range is intended to include its endpoints and all integers and fractions within the range. When a range is defined, the scope of the invention is not intended to be limited to the particular value. When the term "about" is used to describe a value or an endpoint of the range, the disclosure is to be understood to include the particular value or endpoint. The term "includes,," includes ",, has " or any other variation thereof as used herein to cover a non-exclusive include. For example, a process, method, article or device comprising a list of components. They are not necessarily limited to the elements of the invention, and may include other elements that are not specifically listed or elements that are inherent to such processes, methods, articles, or devices. In addition, unless expressly stated to the contrary, "or" Or not exclusive or. For example, any of the following satisfies the A4B condition: A is true (or exists) and 0 is false (or non-existent); A is false (or non-existent) and b True (or exist); and eight and B are true (or present). Use, "," is used to describe the elements and components of the present invention. This is for convenience only and gives the general meaning of the invention. This description should be understood to include one or at least one and singular and plural. 134067.doc 200918661 The materials, methods, and examples herein are illustrative only and are not intended to be limiting unless otherwise indicated. Although methods and materials similar or equivalent to those of the methods and materials described herein can be used in the practice or testing of the present invention, suitable squares & and ## are described herein. The basic fluid feedstock as indicated above does not apply to the base fluid feedstock of the lubricating oil composition of the present invention comprising pteeg at ambient temperature (25t) Ts fluid. The base stock may also contain other natural and/or synthetic fluid auxiliary lubricants. Examples of natural fluid auxiliary lubricants include 4 vegetable oil based lubricants which are often derived from plants and which are typically composed of triglycerides. Generally, these are liquid at room temperature. Although many different parts of the plant produce oil, in practice the oil is typically extracted primarily from the seeds of the oilseed plants. Such oils include edible and inedible oils and include, for example, high oleic sunflower oil, rapeseed oil, soybean oil, castor oil and the like, as well as modified oils such as US6583302 (fatty acid esters) and L Maichev,"plant 〇il Based
Lubricants”(購自 Department of Plant Agriculture,0ntari〇Lubricants" (purchased from Department of Plant Agriculture, 0ntari〇
Agriculture College, University of Guelph, 50 Stone Road W.,Guelph,Ontario, Canada NIG 2W1)中所揭示。 合成流體輔潤滑劑(除P〇3G及P〇3G酯之外)包括潤滑 油,諸如烴油,諸如聚丁烯、聚丙烯、丙稀-異丁烯共聚 物;聚氧基伸烷基二醇聚合物(除P03G之外)及其衍生物, 諸如氧化乙烯與氧化丙烯共聚物;以及二羧酸與各種醇之 酯,諸如己二酸二丁酯、癸二酸二(2-乙基己基)酯、反丁 烯二酸二-己酯、癸二酸二辛酯、壬二酸二異辛酿、壬二Agriculture College, University of Guelph, 50 Stone Road W., Guelph, Ontario, Canada NIG 2W1). Synthetic fluid auxiliary lubricants (except P〇3G and P〇3G esters) include lubricating oils such as hydrocarbon oils such as polybutene, polypropylene, propylene-isobutylene copolymers; polyoxyalkylene glycol polymers (except P03G) and its derivatives, such as copolymers of ethylene oxide and propylene oxide; and esters of dicarboxylic acids with various alcohols, such as dibutyl adipate, di(2-ethylhexyl) sebacate , di-hexyl fumarate, dioctyl sebacate, diisosaccharide azelaic acid, bismuth
134067.doc Q 200918661 酸二異癸酯、鄰苯二甲酸二辛酯、鄰苯二曱酸二癸酯及亞 麻油酸二聚體之2-乙基己二酯。 除PTEEG以外之P03G以及P〇3G酯通常(包括(但不限 於)PTEEG醋)亦可用作合成流體輔潤滑劑。 Ο134067.doc Q 200918661 Diisodecyl phthalate, dioctyl phthalate, dinonyl phthalate and 2-ethylhexyl dimer of linoleic acid dimer. P03G and P〇3G esters other than PTEEG are usually (including but not limited to) PTEEG vinegar and can also be used as a synthetic fluid auxiliary lubricant. Ο
較佳地’基料包含大量PTEEG(以基料之重量計大於50 重量°/〇)。在一些實施例中,基料可包含以基本流體原料之 總重量計約66重量。/。或66重量%以上,或約75重量%或75 重量°/。以上,或約9〇重量%或9〇重量%以上,或約95重量0/〇 或95重量%以上之量的pTEEG。在一些較佳實施例中,基 本流體原料僅(或大體上僅)包含PTEEG。 一部分PTEEG可以pTEEG酯替換,且以上所提及之量可 用於PTEEG加上pTEEG酯之組合。在一實施例中, PTEEG/PTEEG S旨在基本流體原料中之重量比率為1:丨或大 於1:1(PTEEG為主要組份),或約1 5:1或1.5:1以上,或約 2:1或2:1以上,或約5:1或5:1以上,或約2〇:1或2〇:1以上。 又,重量比率較佳為約25:1或25:1以下,或約20:1或20:1 以下’或約1 0:1或1 1以下。 潤滑油組合物較佳包含以潤滑油組合物之總重量計約5〇 重畺°/。或5 0重量%以上之量的基油原料。在各種實施例 中’潤滑油可包含以潤滑油組合物之總重量計約75重量〇/〇 或75重量%以上’或約9〇重量%或9〇重量%以上,或約95 重里/ό或95重置%以上之量的基料。 通用之聚三亞曱基鲢二醇(p〇3G) 出於本發明之目的,P03G(包括PTEEG)為募聚或聚合醚 134067.doc • 10- 200918661 二醇’其中至少50%之重複單元為三亞曱基醚單元。 P03G較佳係藉由使包含1,3-丙二醇之單體較佳在酸性催 化劑存在下縮聚來製備,由此產生含有-(ch2ch2ch2o)-鍵 (例如三亞甲基醚重複單元)之聚合物或共聚物。如上所指 示’至少50%之重複單元為三亞甲基醚單元。 . 當使用硫基酸性催化劑(諸如硫酸)來製備P03G時,所得 產物較佳含有小於約20 ppm、更佳小於約1 〇 ppm之硫。 除二亞甲基醚単元之外,可存在較少量之其他單元,諸 (:) 如其他聚伸烷基醚重複單元。在本揭示案之内容中,術語 ”聚三亞曱基醚二醇”涵蓋由基本上純的1,3-丙二醇製備之 P03G以及含有達約50重量。/。之共聚單體的彼等寡聚物及聚 合物(包括PTEEG及其他下述者)。 對於PTEEG而言,其他聚伸烷基醚重複單元主要為伸乙 基驗单元。 用於製備P03G之1,3-丙二醇可藉由各種熟知化學途徑中 之任一者或藉由生化轉化途徑獲得。較佳途徑如(例 Q 如)US5015789、US5276201、US5284979、US5334778、 US5364984 、 US5364987 、 US5633362 、 US5686276 、 US5821092 、 US5962745 、 US6140543 、 US6232511 、 US6235948 、 US6277289 、 US6297408 、 US6331264 、 US6342646 、 US7038092 、 US7084311 、 US7098368 、 US7009082 及 US20050069997A1 中所述。1,3-丙二醇較佳 是生化上得自可再生來源Γ生物衍生” 1,3_丙二醇)。 1,3-丙二醇之尤佳來源為經由醱酵製程使用可再生生物 來源。作為來自可再生來源之起始物質的說明性實例’已 134067.doc 11 200918661 描述1,3-丙二醇(PDO)之生化途徑,其利用由生物學及可 再生資源產生之原料(諸如玉米原料)。舉例而言,克雷伯 氏菌(ΑΓ/ehW/a)、擰檬酸桿菌(Cz7r〇^cier)、梭狀芽孢桿 菌(C/⑽的·山及乳酸桿菌⑽)種中發現能夠將 甘油轉化為1,3-丙二醇之菌株。若干公開案中揭示該技 術該等&開案包括US5633362 、US5686276及 刪21〇92。其中US5821〇92揭示一種使用重組生物體自 甘油以生物干法產生1,3-丙二醇之製程。該製程併有以對 於1,2-丙二醇具有特異性之異源_二醇脫水酶基因轉化之 大腸桿⑽·使經轉化之大腸桿菌在作為碳源之甘 油存在下生長且自生長培養基分離出U3_丙二醇。由於細 菌與酵母均可將葡萄糖(例如玉米糖)或其他碳水化合物轉 化為甘油,故該等公開案中所揭示之製程提供丙二醇 早體之快速、廉價且對環境負#的來源。 以生物學方法得到之 所提之製程所產生者,含有來自^ /藉由上文所述及 m 3有來自組成用於產生1)3_丙 =料的植物所併有之大氣二氧化碳之碳。以此方式,較 ==於本發日月之情形心生物學方法㈣ 碳,而非化石燃料基或石油基碳。因此利用 境且有^ 之^醇之P咖及基於其之醋對環 ==影響’此係因為組合物中所用…二: 肩耗正逐漸減少之化石燃 和不 氣中以再次為植物所使用。因此 ^後將碳釋放回大 為與包含石油基二醇之類似組二: = 物可表徵 子日比較天然且具有較少 134067.doc 12 200918661 環境影響。Preferably, the binder comprises a substantial amount of PTEEG (greater than 50 weight percent per gram based on the weight of the binder). In some embodiments, the binder can comprise about 66 weight based on the total weight of the base fluid feed. /. Or 66% by weight or more, or about 75% by weight or 75% by weight. Above, or about 9% by weight or more than 9% by weight, or about 95% by weight or more than 95% by weight of pTEEG. In some preferred embodiments, the basic fluid feedstock contains only (or substantially only) PTEEG. A portion of the PTEEG can be replaced with a pTEEG ester, and the amounts mentioned above can be used in combination with PTEEG plus pTEEG ester. In one embodiment, PTEEG/PTEEG S is intended to have a weight ratio of substantially 1 : 丨 or greater than 1:1 (PTEEG is the primary component), or about 1 5:1 or greater than 1.5:1, or about 2:1 or 2:1 or more, or about 5:1 or 5:1 or more, or about 2〇:1 or 2〇:1 or more. Further, the weight ratio is preferably about 25:1 or 25:1 or less, or about 20:1 or 20:1 or less or about 10:1 or less. The lubricating oil composition preferably comprises about 5 Torr and/or based on the total weight of the lubricating oil composition. Or a base oil raw material in an amount of 50% by weight or more. In various embodiments, the lubricating oil may comprise about 75 weights 〇/〇 or more than 75% by weight or about 9% by weight or more, or about 95% by weight, based on the total weight of the lubricating oil composition. Or 95 to reset the amount of the base above %. General purpose polytrimethylene decanediol (p〇3G) For the purposes of the present invention, P03G (including PTEEG) is a polymeric or polymeric ether 134067.doc • 10-200918661 diol' wherein at least 50% of the repeating units are Trimethylene ether unit. P03G is preferably prepared by polycondensing a monomer comprising 1,3-propanediol preferably in the presence of an acidic catalyst, thereby producing a polymer containing a -(ch2ch2ch2o)-bond (eg, a trimethylene ether repeating unit) or Copolymer. As indicated above, at least 50% of the repeating units are trimethylene ether units. When a sulfur-based acidic catalyst such as sulfuric acid is used to prepare P03G, the resulting product preferably contains less than about 20 ppm, more preferably less than about 1 〇 ppm of sulfur. In addition to the dimethylene ether oxime, there may be minor amounts of other units, such as other polyalkylene ether repeating units. In the context of the present disclosure, the term "polytrimethylene ether glycol" encompasses P03G prepared from substantially pure 1,3-propanediol and contains up to about 50 weights. /. The oligomers and polymers of the comonomers (including PTEEG and others described below). For PTEEG, the other polyalkylene ether repeating units are mainly exo-ethylation units. The 1,3-propanediol used to prepare P03G can be obtained by any of a variety of well known chemical routes or by biochemical conversion routes. Preferred methods are as follows: (for example, Q) US5015789, US5276201, US5284979, US5334778, US5364984, US5364987, US5633362, US5686276, US5821092, US5962745, US6140543, US6232511, US6235948, US6277289, US6297408, US6331264, US6342646, US7038092, US7084311, US7098368, US7009082 And as described in US20050069997A1. Preferably, the 1,3-propanediol is biochemically derived from a renewable source, a biologically derived "1,3-propanediol". A particularly preferred source of 1,3-propanediol is the use of a renewable biological source via a fermentation process. Illustrative example of a starting material of origin '134067.doc 11 200918661 describes a biochemical pathway of 1,3-propanediol (PDO) that utilizes raw materials (such as corn raw materials) produced from biological and renewable resources. It is found that Klebsiella (ΑΓ/ehW/a), bacterium of the genus C. citrinum (Cz7r〇^cier), Clostridium (C/(10), and Lactobacillus (10)) can convert glycerol into 1 , a strain of 3-propanediol. The disclosure of the technology is disclosed in several publications, including US Pat. No. 5,633,362, US Pat. No. 5,686,276, and No. 21,92, wherein US Pat. No. 5,821,92 discloses the use of recombinant organisms to produce 1,3 from glycerol by biological dry processes. - a process for propylene glycol. The process has a large intestine rod (10) transformed with a heterologous diol dehydratase gene specific for 1,2-propanediol. The transformed Escherichia coli is grown in the presence of glycerol as a carbon source and Self-growth medium U3_propanediol. Since bacteria and yeast can convert glucose (such as corn sugar) or other carbohydrates into glycerol, the processes disclosed in the publications provide fast, inexpensive, and environmentally friendly propylene glycol precursors. Source. The process produced by the biologically derived process, containing from the above / and m 3 from the composition of the plant used to produce 1) 3 - C = material and atmospheric carbon dioxide Carbon in this way, compared to == in the case of the current day and month, the heart biological method (4) carbon, not fossil fuel-based or petroleum-based carbon. Therefore, the use of the environment and the phenolic coffee and based on it Vinegar on the ring == influence 'This system is used in the composition... Two: The fossil burning and the non-gas in which the shoulder consumption is gradually decreasing is used again for the plant. Therefore, the carbon is released back to the large and contains petroleum-based A similar group of alcohols: = The object can be characterized by a sub-day that is more natural and has less environmental impact. 134067.doc 12 200918661
以生物學方法得到之1,3-丙二醇、p〇3G及p〇3G酯可藉 由雙重奴同位素指紋法而與由石化來源或化石燃料碳產生 之類似化合物區分開來。該方法有效區分化學上相同之物 質,且根據生物圈(植物)組份之生長來源(且可能為年齡) 解析共聚物中之碳。同位素i4C及為該問題帶來補充資 訊。核半衰期為5730年之放射性碳定年同位素(mc)明確地 使得可在化石("死")與生物圈("活")原料之間解析標本碳 (Currie, L. A. "Source Apportionment of Atmospheric Particles,'' Characterization of Environmental Particles, J. Buffle及 H.P. van Leeuwen編輯,IUPAC Environmental Analytical Chemistry Series(Lewis Publishers,Inc)第 1卷第 1部分(1992) 3-74)。放射性碳定年中之基本假設為大氣中 之C濃度之恆定性引起活有機體中之i4c之恆定性。當處 理經分離之樣品時,樣品之年齡可大致藉由以下關係推 斷: t=(-5730/0.693)ln(A/A〇), 其中t=年齡,5730年為放射性碳之半衰期,且八及〜分別 為樣品及現代標準之特定i4c^m(Hsieh,Y.,s〇n Sci. St)C.The biologically obtained 1,3-propanediol, p〇3G and p〇3G esters can be distinguished from similar compounds produced by petrochemical sources or fossil fuel carbon by double slave isotope fingerprinting. The method effectively distinguishes between chemically identical materials and resolves the carbon in the copolymer based on the source of growth (and possibly age) of the biosphere (plant) component. The isotope i4C adds additional information to the problem. Radiocarbon dating (mc) with a nuclear half-life of 5730 clearly allows for the analysis of specimen carbon between fossils ("dead") and biosphere ("live") materials (Currie, LA "Source Apportionment of Atmospheric Particles, '' Characterization of Environmental Particles, edited by J. Buffle and HP van Leeuwen, IUPAC Environmental Analytical Chemistry Series (Lewis Publishers, Inc) Vol. 1 Part 1 (1992) 3-74). The basic assumption in radiocarbon dating is that the constancy of C concentration in the atmosphere causes the constancy of i4c in living organisms. When processing an isolated sample, the age of the sample can be roughly inferred by the following relationship: t = (-5730 / 0.693) ln (A / A 〇), where t = age, 5730 is the half-life of radiocarbon, and eight And ~ respectively for the sample and modern standard specific i4c^m (Hsieh, Y., s〇n Sci. St) C.
Am J·,56,460,(1992))。然而,由於自1950以來之大氣層 核測試及自1 850年以來之化石燃料燃燒,ιγ獲得第二地 球化學時間特徵。其在大氣C〇2中且因此在活生物圈中之 濃度在核測試高峰期(在二十世紀六十年代中期)約為雙 倍。此後其逐漸回復至約l_2xi 〇·12之穩態宇生(大氣)基線 I34067.doc •13· 200918661 同位素比率(14c/12c) ’其中近似弛緩”半衰期”(relaxati〇n half· life)為7-10年。(此後面之半衰期不可自字面上理解; 相反地,必須使用詳細之大氣核輸入/衰變函數來追縱自 核時代開始以來大氣及生物圈14C之變化)。正是此後面之 生物圈14C時間特徵支持新近生物圈碳之年度定年前景。 14C可藉由加速器質譜(AMS)量測,其結果以”現代碳分數 "(fM)單位給出。fM係以國家標準與技術研究所(Nati〇nalAm J., 56, 460, (1992)). However, due to atmospheric nuclear testing since 1950 and fossil fuel combustion since 1850, ιγ obtained the second geochemical time characteristics. Its concentration in the atmosphere C〇2 and therefore in the living biosphere is approximately doubled during the peak of the nuclear test (in the mid-1960s). Thereafter, it gradually returns to a steady-state (atmospheric) baseline of about l_2xi 〇·12. I34067.doc •13· 200918661 Isotope ratio (14c/12c) 'The approximate relaxation half-life' (relaxati〇n half· life) is 7 -10 years. (The latter half-life cannot be understood literally; instead, a detailed atmospheric nuclear input/decay function must be used to track changes in the atmosphere and the biosphere 14C since the beginning of the nuclear era). It is this 14C time feature of the biosphere that supports the annual dating of the new biosphere carbon. 14C can be measured by Accelerator Mass Spectrometry (AMS) and the results are given in "Modern Carbon Fractions" (fM). fM is based on the National Institute of Standards and Technology (Nati〇nal).
ΟΟ
Institute of Standards and Technology,NIST)標準參考物質 (Standard Reference Material,SRM)4990B及 499〇c(分別稱 為草酸標準物!1加1及11加11)定義。基本定義係指〇95乘 H〇xI之〗4C/i2C同位素比率(參考AD 195〇)。此大致等於經 衰變校正之工業革命前木材。對於當前活生物圈(植物物 質)而言,fM= 1 · 1。 穩定碳同位素比率严C)提供來源辨別及解析之補充 途徑。所給生物來源物質中之13c/12c比率為固定二氧化碳 時大氣二氧化碳中之丨3C/12c比率之結果,且亦反映精確之 代謝路徑。亦存在區域性變化。石油、C3植物(闊葉樹卜 ^植物(草)及海相碳酸鹽均顯示13C/12C及相應fc值之顯 '此外,C3及C4植物之脂質物質的分析結果由於代 謝路k之故與來源於相同植物之碳水化合物組份之物質不 同。在量測精度範圍内,】3C由於同位素分餾效應而顯示 較大變化,對於太恭 _ 、卷月而S,同位素分餾效應中最顯著者 :光合機制。植物中碳同位素比率差異之主要原因與植物 先合碳代謝路徑、尤其初級幾基化(亦即,初始大氣co2 134067.doc 14 200918661 固疋)期間發生之反應之差異密切相關。植物之兩大類為 併有"CV(或卡爾文-本森(Calvin-Benson))光合循環之彼等 者及併有"CV’(或哈奇-斯萊克(Hatch-Slack))光合循環之彼 等者。C3植物(諸如闊葉樹及針葉樹)主要在溫帶氣候區。 在A植物中’初級C〇2固定或羧基化反應涉及酶核酮 糖-1,5-二磷酸羧化酶,且第一穩定產物為3_碳化合物。另 一方面,C4植物包括諸如熱帶草、玉米及甘蔗之植物。在 C4植物中’涉及另一種酶磷酸烯醇式_丙酮酸羧化酶之另 一叛基化反應為初級羧基化反應。第一穩定碳化合物為4_ 碳氫酸(carbon acid),隨後4·碳氫酸被脫羧基化。由此釋 放之C02藉由C3循環再固定。 C4與C3植物均展現一定範圍之nc/12c同位素比率,但典 型值為每密耳(C4)約-10至-14及每密耳((:3)_21至_26(|吡“ 等人,J. Agric· Food Chem.,45, 2942 (1997))。煤及石油 通常屬於此後面之範圍内。nc量測尺度最初係以用皮迪 箭石(pee dee belemnite)(PDB)石灰石設定之零來界定其 值係以與該物質之每一千偏差之份數給出。值係以 每一千(每密耳)之份數計(縮寫%),且如下計算: (-χ1000°/〇 由於測參考物質(RM)已耗4,故已與副A、USGS、 NIST及其他所選國際同位素實驗室合作開發—系列替代 RM。對與PDB之每密耳偏差的表示為以。藉由對質量 44、45及46之分子離子進行高精度穩定比率質譜測定 134067.doc 15 200918661 (stable ratio mass spectrometry,IRMS)對 C02進行量測。 因此,以生物學方法得到之1,3-丙二醇及包含以生物學 方法得到之1,3-丙二醇之組合物可基於14C(fM)及雙重碳同 位素指紋與其石化來源對應物完全區分開來,從而指示物 質之新組成。區分該等產品之能力有益於商業上追蹤該等 • 物質。舉例而言,可將包含”新π與"舊"碳同位素概況之產 . 品與僅由”舊”物質製成之產品區分開來。因此,本發明之 物質可在商業上基於其獨特概況且為確認競爭性、確定存 C ' 放期及尤其為評估環境影響之目的而進行跟蹤。 較佳地,用作反應物或用作反應物之組份之1,3-丙二醇 如藉由氣相層析分析所測定應具有大於約99重量%且更佳 大於約99.9重量%之純度。尤佳者為如US7038092、 US7098368 、 US7084311及 US20050069997A1 中所揭示之 經純化1,3-丙二醇以及如US20050020805A1中所揭示由其 製備之P03G。 經純化1,3-丙二醇較佳具有以下特徵: 〇 (1) 在220 nm下之紫外線吸收小於約0.200,且在250 nm 下之紫外線吸收小於約0.075,且在275 nm下之紫外線吸 收小於約0.075 ;及/或 (2) L*a*b*”b*” 色值小於約 0.15(ASTM D6290)且在 270 nm下之吸光度小於約0.075之組成;及/或 (3) 小於約10 ppm之過氧化物組成;及/或 (4) 如由氣相層析法所量測,小於約400 ppm、更佳小於 約3 00 ppm且更佳小於約1 50 ppm之總有機雜質(除1,3 -丙二 134067.doc •16· 200918661 醇之外的有機化合物)濃度。Institute of Standards and Technology, NIST) Standard Reference Material (SRM) 4990B and 499〇c (referred to as oxalic acid standards! 1 plus 1 and 11 plus 11 respectively). The basic definition refers to the 4C/i2C isotope ratio of 〇95 times H〇xI (refer to AD 195〇). This is roughly equal to the pre-industrial wood that was decay-corrected. For the current living biosphere (plant matter), fM = 1 · 1. Stable Carbon Isotope Ratios C) Provide complementary pathways for source identification and analysis. The 13c/12c ratio in the given biosourced material is the result of the 丨3C/12c ratio in atmospheric carbon dioxide at fixed carbon dioxide and also reflects the precise metabolic pathway. There are also regional changes. Oil, C3 plants (broadleaf trees, plants (grass) and marine carbonates show 13C/12C and corresponding fc values'. In addition, the analysis results of lipid substances in C3 and C4 plants are due to the metabolic pathway The carbohydrate content of the same plant is different. Within the range of measurement accuracy, 3C shows a large change due to the isotope fractionation effect. For the Taigong _, the moon and the S, the most significant of the isotope fractionation effects: photosynthetic mechanism The main reason for the difference in carbon isotope ratios in plants is closely related to the difference in the plant's carbon-metabolic pathway, especially the primary grouping (ie, the initial atmospheric co2 134067.doc 14 200918661 疋). The majority are those who have a "CV (or Calvin-Benson) photosynthetic cycle and have a "CV' (or Hatch-Slack) photosynthetic cycle C3 plants (such as broad-leaved trees and conifers) are mainly in the temperate climate zone. In the A plant, the 'primary C〇2 fixation or carboxylation reaction involves the enzyme ribulose-1,5-bisphosphate carboxylase, and the first The stable product is 3_ Compounds. On the other hand, C4 plants include plants such as tropical grass, corn, and sugar cane. In C4 plants, another dephosphorylation reaction involving another enzyme, phosphoenol-pyruvate carboxylase, is a primary carboxylation reaction. The first stable carbon compound is 4_carbon acid, and then the hydrocarbon is decarboxylated. The CO2 thus released is re-fixed by C3 cycle. Both C4 and C3 plants exhibit a certain range of nc/ 12c isotope ratio, but typical values are about -10 to -14 per mil (C4) and per mil ((:3)_21 to _26 (|Py, et al., J. Agric. Food Chem., 45, 2942 (1997)). Coal and oil usually fall within the scope of this. The nc measurement scale was originally defined by the zero of the pee dee belemnite (PDB) limestone to define its value with the substance. The fraction of each thousand deviation is given. The value is in parts per thousand (per mil) (abbreviation %) and is calculated as follows: (-χ1000°/〇 because the reference material (RM) has been consumed 4, it has been developed in cooperation with Deputy A, USGS, NIST and other selected international isotope laboratories - a series of replacement RM. For each with PDB The mil bias is expressed as a measure of CO 2 by high-precision stable ratio mass spectrometry of molecular ions of masses 44, 45, and 46. 134067.doc 15 200918661 (stable ratio mass spectrometry, IRMS) The 1,3-propanediol obtained by the method and the composition comprising the biologically obtained 1,3-propanediol can be completely distinguished from the petrochemical source counterpart based on the 14C (fM) and the double carbon isotope fingerprint, thereby indicating the substance New composition. The ability to distinguish between these products is beneficial for the commercial tracking of such substances. For example, a product containing a "new π and "old" carbon isotope profile can be distinguished from a product made only from "old" materials. Thus, the materials of the present invention can be commercially based on A unique overview and tracking for the purpose of confirming competitiveness, determining C's release and especially for assessing environmental impact. Preferably, 1,3-propanediol used as a reactant or as a component of the reactants Purified by gas chromatography analysis should have a purity of greater than about 99% by weight and more preferably greater than about 99.9% by weight. Particularly preferred are purified 1,3-propanediols as disclosed in US Pat. No. 7,038,092, US Pat. No. 7,098,368, US Pat. P03G prepared therefrom as disclosed in US20050020805A1. Purified 1,3-propanediol preferably has the following characteristics: 〇(1) has a UV absorption of less than about 0.200 at 220 nm and an ultraviolet absorption of less than about 0.075 at 250 nm. And the UV absorption at 275 nm is less than about 0.075; and/or (2) the L*a*b*"b*" color value is less than about 0.15 (ASTM D6290) and the absorbance at 270 nm is less than about 0.075. ; and / or (3) less than about 10 ppm The peroxide composition; and/or (4) total organic impurities (excluding 1) of less than about 400 ppm, more preferably less than about 300 ppm, and more preferably less than about 150 ppm as measured by gas chromatography. , 3 - Propylene 134067.doc • 16· 200918661 Organic compounds other than alcohol) concentration.
用於製備P03G之起始物質將視所要P03G、起始物質可 用性、催化劑、設備等而定且包含"1,3-丙二醇反應物"。 "1,3·丙二醇反應物"意謂ι,3-丙二醇,以及較佳聚合度為2 至9之1,3-丙二醇之寡聚物及預聚物,及其混合物。在一些 情況下,可能希望使用達10%或10%以上之低分子量寡聚 物(在其可獲得之情況下)。因此,較佳地,起始物質包含 1,3-丙二醇以及其二聚物及三聚物。尤佳之起始物質以 1,3-丙二醇反應物之重量計含有約9〇重量%或9〇重量❶/。以上 1,3-丙二醇,且更佳含有99重量%或99重量%以上1,3_丙二 醇。 P03G可經由此項技術中已知之多種製程製備,諸如 US697729i及US672〇459中所揭示之製程。較佳製程如 US7074969 、 US7157607 、 US7161045 及 US7164046 中所 述0 如上所指示,除三亞曱基醚單元之外,P03G可含有較 乂量之其他聚伸院基醚重複單元。因此,用於製備p〇3G 之單體除1,3-丙二醇反應物之外可含有至多5〇重量%之共 聚单體多元醇。適用於該製程中之共聚單體多元醇包括脂 族一醇,例如乙二醇、丨’6·己二醇、丨’了-庚二醇、1,8_辛二 醇、1,9-壬二醇 1,1〇-癸二醇、1,12-十二烷二醇、 3,3,4,4,5,5-六 n,% 戊三醇、2,23,3,4,4,5,5_/U,6j ^-81^3,3,4,4,5,5,6,6,7,7,8,8,9,9,10,10--1- 烷二醇;環脂族二醇,例如M_環己二醇、“4•環己烷二 134067.doc -17· 200918661 甲醇及異山梨醇;《經基化合物,例如甘油、三經甲基 丙烧及異戊四1共聚單體二醇之較佳族群係選自由以下 各物組成之群:乙二醇、2_甲基-丨^丙二醇、22_二甲 基丙二醇、2,2-二乙基{3-丙二醇、2_乙基_2侧甲 基)·1,3·丙二醇、cvc丨〇二醇(諸如丨,6_己二醇、丨兀辛二醇 及U0-癸二醇)及異山梨醇以及其混合物。除丨,3丙二醇之 外,尤佳之二醇為乙二醇,且C6_C10二醇亦可為尤其適用 的0The starting materials used to prepare P03G will depend on the desired P03G, starting material availability, catalyst, equipment, etc. and will include "1,3-propanediol reactant". "1,3·propanediol reactant" means i-, 3-propanediol, and oligomers and prepolymers of preferred 1,3-propanediol having a degree of polymerization of 2 to 9, and mixtures thereof. In some cases, it may be desirable to use up to 10% or more of the low molecular weight oligomer (where it is available). Accordingly, preferably, the starting material comprises 1,3-propanediol and dimers and trimers thereof. More preferably, the starting material contains about 9% by weight or 9 Å by weight based on the weight of the 1,3-propanediol reactant. The above 1,3-propanediol, and more preferably 99% by weight or 99% by weight or more of 1,3 - propylene glycol. P03G can be prepared by a variety of processes known in the art, such as those disclosed in U.S. Patent No. 6,977,729 and U.S. Patent No. 6,672,459. The preferred processes are as described above in U.S. Patent Nos. 7,074,969, US Pat. No. 7,157,607, U.S. Patent No. 7,716,045, and U.S. Patent No. 7,174,046. As indicated above, P03G may contain, in addition to the tris-decyl ether unit, a greater amount of other extended excipient ether repeating units. Thus, the monomer used to prepare p〇3G may contain up to 5% by weight of the comonomer polyol in addition to the 1,3-propanediol reactant. Comonomer polyols suitable for use in the process include aliphatic monoalcohols such as ethylene glycol, 丨'6·hexanediol, 丨'h-heptanediol, 1,8-octanediol, 1,9-壬diol 1,1〇-nonanediol, 1,12-dodecanediol, 3,3,4,4,5,5-hexa,% pentatriol, 2,23,3,4, 4,5,5_/U,6j ^-81^3,3,4,4,5,5,6,6,7,7,8,8,9,9,10,10--1-alkane Alcohol; cycloaliphatic diol, such as M_cyclohexanediol, "4•cyclohexane II 134067.doc -17· 200918661 methanol and isosorbide; "base group compounds, such as glycerol, trimethyl ketone And a preferred group of isoprene 1-4 comonomer diols are selected from the group consisting of ethylene glycol, 2-methyl-hydrazine propylene glycol, 22 dimethyl propylene glycol, 2,2-diethyl Base {3-propanediol, 2-ethyl-2 side methyl)·1,3·propanediol, cvc decanediol (such as hydrazine, 6-hexanediol, octyl octanediol and U0-decanediol) And isosorbide and mixtures thereof. In addition to hydrazine, 3 propylene glycol, a particularly preferred diol is ethylene glycol, and C6_C10 diol may also be particularly suitable.
適用於本發明之合適PTEEG(例如)如US2〇〇4〇〇3〇〇95ai 中所述。較佳PTEEG係藉由酸催化之50莫耳%至約99莫耳 % (較佳為約6 0莫耳%至約9 8莫耳%,且更佳為約7 〇莫耳% 至約98莫耳,3_丙二醇與至多5〇莫耳%至約i莫耳%(較佳 為約40莫耳%至約2莫耳%,且更佳為約3〇莫耳%至約二莫 耳/ί>)乙一醇的縮聚來製備。 較佳地,純化之後的PTEEG基本上無酸性催化劑端基, 但可含有極低含量之在約〇 〇〇3至約〇 〇3 meq/g範圍内的不 飽和端基,主要為烯丙基端基。可認為此類PTEEG包含具 有以下式(I)及(II)之化合物(基本上由該等化合物組成): H0-((CH2)30)m((CH2)20)n-H (I) H0-((CH2)3-0)m((CH2)20)nCH2CH=CH2 (II), 其中m及η在一定範圍内以使]^11(數量平均分子量)在約2〇〇 至約10000之範圍内,其中式(ΙΠ)化合物以一定量存在以 使烯丙基端基(較佳所有不飽和端或端基)以約〇 〇〇3至約 0.03 meq/g範圍内之量存在。 134067.doc -18- 200918661 PTEEG可為無規或嵌段共聚物,且式(I)及式(II)意欲覆 蓋兩種變體。 適用於本發明之較佳P〇3G(PTEEG)具有至少約250、更 佳至少約1000且更佳至少約2000之Μη(數量平均分子量)。 Μη較佳小於約10000,更佳小於約5000,且更佳小於約 • 3500。亦可使用P03G之摻合物。舉例而言,P03G可包含 較高與較低分子量之Ρ03G之摻合物,較佳地,其中較高 分子量之P〇3G具有約1000至約5000之數量平均分子量, 且較低分子量之P03G具有約200至約950之數量平均分子 量。經換合ΡΟ3 G之Μη較佳應仍處於上述範圍内。 較佳用於本文中之P03G通常為多分散的,其具有較佳 約1_0至約2.2、更佳約1.2至約2.2且更佳約1.5至約2.1之多 分散性(亦即Mw/Mn)。多分散性可藉由使用P03G之摻合 物來調節。 適用於本發明之P03G較佳具有小於約100 APHA且更佳 小於約50 APHA之色值,及較佳在40°C下為約1〇〇 cS或100 cS以上之黏度。 P03G 酯 在一些實施例中,P03G酯包含一或多種式(III)化合 物: 〇 R1-C——Ο——Q——Ο——R2 (III) 其中Q表示P03G在去除羥基之後的殘基,R2為Η或R3CO, 134067.doc -19- 200918661 且Ri及Rs中之每一者單獨地為含有4至個碳原子、較佳 至少6個碳原子、更佳至少8個碳原子之經取代或未經取代 之芳族、飽和脂族、不飽和脂族或環脂族有機基團。在一 二實施例中’ R丨及r3中之每一者均具有2〇個或個以下之 碳原子,且在一些實施例中具有10個或10個以下之碳原 子。在一些較佳實施例中,Ri及R3中之每一者均具有8個 碳原子。 P〇3GSa較佳係藉由使主要包含1,3-丙二醇之含羥基單體 (3有2或2個以上羥基之單體)縮聚形成p⑴g(如下所揭 示)、’膣而以單鲮酸(或等效物)酯化來製備,如2〇〇6年丨J月Suitable PTEEGs suitable for use in the present invention are, for example, as described in U.S. Patent 4, 4, 3, 95,. Preferably, PTEEG is from 50 mole % to about 99 mole % by acid catalysis (preferably from about 60 mole % to about 98 mole %, and more preferably from about 7 mole % to about 98) Mohr, 3-propylene glycol and up to 5 mole % to about i mole % (preferably from about 40 mole % to about 2 mole %, and more preferably from about 3 mole % to about two moles) Preferably, the purified PTEEG is substantially free of acidic catalyst end groups, but may contain very low levels ranging from about 〇〇〇3 to about me3 meq/g. Unsaturated end groups, mainly allyl end groups. Such PTEEGs are considered to comprise (substantially consist of) compounds having the following formulae (I) and (II): H0-((CH2)30) m((CH2)20)nH (I) H0-((CH2)3-0)m((CH2)20)nCH2CH=CH2 (II), where m and η are within a certain range to make [^11] The average molecular weight) is in the range of from about 2 Torr to about 10,000, wherein the compound of the formula (ΙΠ) is present in an amount such that the allyl end group (preferably all unsaturated ends or end groups) is about 〇〇〇3 to Amounts in the range of about 0.03 meq/g are present. 134067.doc -18- 200918661 PTEE G may be a random or block copolymer, and formula (I) and formula (II) are intended to cover both variants. Preferred P〇3G (PTEEG) suitable for use in the present invention has at least about 250, more preferably at least about 1000 and more preferably at least about 2000 数量 (number average molecular weight). Μη is preferably less than about 10,000, more preferably less than about 5,000, and still more preferably less than about 3.500. A blend of P03G may also be used. For example, P03G A blend of higher and lower molecular weight Ρ03G may be included, preferably wherein the higher molecular weight P〇3G has a number average molecular weight of from about 1000 to about 5,000, and the lower molecular weight P03G has from about 200 to about 950. The number average molecular weight. The Μ η of the ΡΟ 3 G is preferably still within the above range. P03G preferably used herein is generally polydisperse, preferably having from about 1_0 to about 2.2, more preferably about 1.2 to Polydispersity (i.e., Mw/Mn) of from about 2.2 and more preferably from about 1.5 to about 2.1. Polydispersity can be adjusted by using a blend of P03G. P03G suitable for use in the present invention preferably has less than about 100 APHA. And more preferably less than about 50 APHA, and preferably about 1 〇〇 cS or 100 cS at 40 ° C P03G Ester In some embodiments, the P03G ester comprises one or more compounds of formula (III): 〇R1-C-Ο-Q-Ο-R2 (III) wherein Q represents the removal of hydroxyl groups by P03G Subsequent residues, R2 is hydrazine or R3CO, 134067.doc -19- 200918661 and each of Ri and Rs is independently 4 to carbon atoms, preferably at least 6 carbon atoms, more preferably at least 8 A substituted or unsubstituted aromatic, saturated aliphatic, unsaturated aliphatic or cycloaliphatic organic group of a carbon atom. In the second embodiment, each of 'R丨 and r3 has 2 or less carbon atoms, and in some embodiments, 10 or less carbon atoms. In some preferred embodiments, each of Ri and R3 has 8 carbon atoms. P〇3GSa is preferably formed by polycondensation of a hydroxyl group-containing monomer mainly comprising 1,3-propanediol (3 monomers having 2 or more hydroxyl groups) to form p(1)g (as disclosed below), and a monodecanoic acid (or equivalent) esterification to prepare, such as 2〇〇6年丨J月
7 日申《月之題為 POLYTRIMETHYLENE ETHER GLYCOL ESTERS,,的美國巾請案第1 1/593,954號中所揭示。 由此所製備之P03G醋為以酯之總重量計較佳包含約5〇 重量/。至100重罝%、更佳約75重量%至刚重量%之二酯及 0至約50重量%、更佳〇至約25重量%之單酯的組合物。較 佳地,該等單酯及二酯為2_乙基己酸之酯。 用於製備該醋之P〇3G無需與基本流體原料之p〇3G共組 份相同。 酸及等效物 P〇3G之酯化係藉由與酸及/或等效物(較佳單羧酸及/或 等效物)反應而進行。 ”单緩酸等效物”意謂在與聚合二醇反應時大體上如軍叛 酸般執仃之化合物’此如通常由一般熟習相關技術者所識 別。出於本發明之目的,單羧酸等效物包括(例如)單羧酸 134067.doc •20- 200918661 之酯及酯形成衍生物,諸如酸齒化物(例如酸氯化物)及酸 肝0 較佳地,使用具有式R_COOH之單羧酸,其中R為含有6 至40個碳原子的經取代或未經取代之芳族1旨族或環脂族 有機部分。 不同單鲮酸及/或等效物之混合物亦合適。 如上所指示,單羧酸(或等效物)可為芳族、脂族或環脂 族。就此而言’ ”芳族"單M錢基與苯環系統中之碳原 子連接之單羧酸,諸如下述彼等單羧酸。”脂族”單羧酸為 缓基與完全飽和之碳原子連接或與為婦煙雙鍵之部分的碳 原子連接之單Μ。若碳原子處於環中,料效物為"環 脂族"。 單羧酸(或等效物)可含有任何取代基或其組合(諸如,如 醯胺、胺、《、鹵素、經基等之官能基),只要該等取 代基不干擾酯化反應或不會不利地影響所得酯產物之特性 即可。 單緩酸及等效物可來自任何來源,{旦較佳纟源於天然來 源或生物來源。 以下酸及其衍生物尤其較佳:月桂酸、肉豆蔻酸、棕櫚 酸、硬脂酸、花生酸、苯甲酸、辛酸、芥子酸、標搁油 酸、十五烧酸、十七烧酸、十九烧酸、亞麻油酸、花生四 稀酸、油豸、戊酸、己酸、癸酸及2_乙基己酸以及其混合 物。尤佳之酸或其衍生物為2_乙基己酸、苯甲酸、硬月°旨 酸、月桂酸及油酸。 134067.doc 200918661 酯化製程 為製備該等酯,可在約l〇〇C>c ^ ^ 約 275 C、較佳約 125t:至 、⑽C乾圍内之溫度下’較佳在惰性氣體存在下,使 、〇3G與早幾酸接觸。該製程可在大氣屬力下或在真空下 2订。在接觸期間形成水,且其可在惰性氣體流中或在真 空下移除以驅使反應完成。 為促進P03G與羧酸之反應,通常使用醋化催化劑,較 佳為無機酸催化劑。無機酸催化劑之實例包括(但不限於) 硫酸、鹽酸、鱗酸、氫礙酸及異質催化劑,諸如彿石、雜 多酸、大孔樹脂及離子交換樹脂。較佳之醋化酸備化劑係 選自由硫酸、鱗酸、鹽酸及氫蛾酸組成之群。尤佳無機酸 催化劑為硫酸。 所用催化劑之量可為反應混合物之約〇 . 〇丨重量%至約1 〇 重量/。,較佳為反應混合物之〇丨重量%至約5重量%,且更 佳為約0.2重量%至約2重量〇/0。 可使用羧酸或其衍生物與二醇羥基之任何比率。酸與羥 基之較佳比率為約3:1至約1:2,其中比率可經調節以改變 產物中單酯與二酯之比率。一般而言,為有利於二酯產 生,使用略大於1 :1之比率。為有利於單酯產生,使用酸 與羥基之0.5:1或0.5:1以下之比率。 醋化之較佳方法包含使用無機酸催化劑使丨,3_丙二醇反 應物縮聚為P〇3G,隨後在不分離及純化p〇3G的情況下添 加羧酸及進行酯化。在該方法中,將U3_丙二醇反應物醚 化或縮聚形成P03G係使用如US6977291及US6720459中所 134067.doc -22- 200918661 揭不之酸催化劑進行。鍵化反應亦可使用如jp測_ 182974A巾料之含有酸錢之縮㈣化劑進行。持續縮 聚或鱗化反應直至達至所要分子量,且隨後將計算量之單 幾酸添加至反應混合物中。繼續反應,同時將水副產物移 除。在此階段時,醋化㈣化反應同時進行。因此,在此 較佳:旨化方法中’用於使二醇縮聚之酸催化劑亦用於醋 化右有必要蚪,在酯化階段可添加其他酯化催化劑。 在此程序中,所得產物之黏度(分子量)係藉由添加叛酸 之時間來控制。 在一替代性程序十,醋化反應可針對經純化P03G藉由 添加酯化催化劑及叛酸,繼而加熱且移除水而進行。在此 程序中,所得產物之黏度主要為所用_之分子量的函 數。 無論醋化程序繼之以何程序,在_化步驟之後,均將任 何副產物移除’且隨後移除縮聚及/或酯化反應剩餘之摧 化劑殘餘物以獲得穩定(尤其在高溫下)之§旨產物。此可藉 由在約80 C至約1〇〇。〇下將粗醋產物經由以水處理而水解 足以在不顯著影響缓酸酉旨之情況下水解來源於催化劑之任 何殘餘酸酯的時間來實現。所需時間可自約丨小時至約8小 時變化。若在壓力下進行水解,則可能為較高溫度及相應 較短之時間。在此點上,視反應條件而定,產物可含有二 醋、單醋或二醋與單醋之組合’及少量酸催化劑、未反應 之叛酸及二醇。將經水解之聚合物藉由已知習知技術(諸 如水洗、鹼中和、過遽及/或蒸餾)進一步純化以移除水、 134067.doc -23- 200918661 酸催化劑及未反應之羧酸。未反應之二醇及酸催化劑可 (例如)藉由以去離子水洗滌來移除。亦可(例如)藉由以去 離子水或驗水溶液洗滌或藉由真空汽提移除未反應之羧 酸。 水解通常繼之以一或多個水洗步驟以移除酸催化劑,及 乾燥(較佳在真空下)以獲得酯產物。水洗亦用來移除未反 應之二醇。所存在之任何未反應之單羧酸亦可在水洗中移 除’但亦可藉由以鹼水溶液洗滌或藉由真空汽提來移除。 若需要時’產物可藉由在減壓下分餾而進一步分餾以分 離低分子量|旨。 可使用質子NMR及波長χ_射線螢光光譜法來鑑別及定量 聚合物中所存在之任何殘餘催化劑(諸如硫)。質子Nmr可 (例如)鑑別聚合物鏈中所存在之硫酸酯基,且波長χ_射線 榮光法可測定聚合物中所存在之總硫(無機及有機硫)。本 發明之由上述製程製得之酯大體上不含硫且因此適用於高 、、田處 ra ✓皿厲用 〇 較佳地,純化之後的P〇3G酯基本上無酸性催化劑端 基’但可含有極低含量之在約〇 003至約〇 〇3 meq/g範圍内 的不飽和端基,主要為烯丙基端基。可認為該p〇3G酯包 含具有以下式(IV)及(V)之化合物(基本上由該等化合物組 成): R.-C(0)-0-((CH2)30)m((CH2)20)n-R2 (IV)U.S. Patent Application Serial No. 1 1/593,954, the entire disclosure of which is incorporated herein by reference. The P03G vinegar thus prepared preferably contains about 5 Å by weight based on the total weight of the ester. A composition of up to 100% by weight, more preferably from about 75% by weight to just wt% of the diester and from 0 to about 50% by weight, more preferably from about 25% by weight of the monoester. Preferably, the monoesters and diesters are esters of 2-ethylhexanoic acid. The P〇3G used to prepare the vinegar does not need to be the same as the p〇3G co-component of the basic fluid feedstock. Acids and Equivalents The esterification of P〇3G is carried out by reaction with an acid and/or an equivalent (preferably a monocarboxylic acid and/or an equivalent). "Single-acid equivalents" means a compound that is substantially ruthenium-like when reacted with a polymeric diol' as is generally recognized by those of ordinary skill in the art. For the purposes of the present invention, monocarboxylic acid equivalents include, for example, ester and ester forming derivatives of monocarboxylic acids 134067.doc • 20-200918661, such as acid dentates (eg, acid chlorides) and acid livers 0 Preferably, a monocarboxylic acid having the formula R_COOH wherein R is a substituted or unsubstituted aromatic 1 group or a cycloaliphatic organic moiety having 6 to 40 carbon atoms is used. Mixtures of different monoterpenic acids and/or equivalents are also suitable. As indicated above, the monocarboxylic acid (or equivalent) can be an aromatic, aliphatic or cycloaliphatic group. In this regard, the 'monomeric' monocarboxylic acid is bonded to a carbon atom in the benzene ring system, such as the following monocarboxylic acids. The "aliphatic" monocarboxylic acid is a slow base and fully saturated. a carbon atom that is attached to or linked to a carbon atom that is part of a double bond of a woman's cigarette. If the carbon atom is in the ring, the effect is "cycloaliphatic". The monocarboxylic acid (or equivalent) may contain Any substituent or combination thereof (such as a functional group such as a guanamine, an amine, a "halogen, a thiol group, etc.") as long as the substituents do not interfere with the esterification reaction or adversely affect the properties of the resulting ester product. The mono-acids and equivalents may be derived from any source, and the preferred acids are derived from natural or biological sources. The following acids and derivatives are particularly preferred: lauric acid, myristic acid, palmitic acid, stearic acid, Arachidonic acid, benzoic acid, octanoic acid, sinapic acid, tartaric acid, fifteen-burning acid, heptadecanoic acid, cinnamic acid, linoleic acid, peanut tetrabasic acid, oil quinone, valeric acid, caproic acid, hydrazine Acid and 2-ethylhexanoic acid and mixtures thereof. Particularly preferred acid or its derivative is 2-ethylhexanoic acid, benzene Acid, hard moon acid, lauric acid and oleic acid. 134067.doc 200918661 The esterification process for preparing the ester can be about 1 〇〇C> c ^ ^ about 275 C, preferably about 125 t: to, (10) C At a temperature within the dry perimeter, it is preferred to contact 〇3G with an earlier acid in the presence of an inert gas. The process can be formulated under atmospheric force or under vacuum. Water is formed during contact and can be The reaction is carried out in an inert gas stream or under vacuum to drive the reaction to completion. To promote the reaction of P03G with a carboxylic acid, a acetation catalyst, preferably a mineral acid catalyst, is generally used. Examples of inorganic acid catalysts include, but are not limited to, sulfuric acid, Hydrochloric acid, squaric acid, hydrogen sulphate and heterogeneous catalysts, such as fossil, heteropoly acid, macroporous resin and ion exchange resin. Preferably, the acetal acid preparation agent is selected from the group consisting of sulfuric acid, scaly acid, hydrochloric acid and hydromoxic acid. The preferred inorganic acid catalyst is sulfuric acid. The amount of the catalyst used may be from about 〇.% by weight to about 1 〇 by weight of the reaction mixture, preferably from about 5% by weight to about 5% by weight of the reaction mixture. And more preferably about 0.2% by weight to About 2 weights 〇 / 0. Any ratio of carboxylic acid or its derivative to diol hydroxyl group can be used. A preferred ratio of acid to hydroxyl group is from about 3:1 to about 1:2, wherein the ratio can be adjusted to change the product The ratio of monoester to diester. In general, to facilitate diester production, a ratio of slightly more than 1:1 is used. To facilitate monoester production, a ratio of acid to hydroxyl of 0.5:1 or less is used. A preferred method of acetalization comprises polycondensation of a ruthenium, 3-propanediol reactant to P〇3G using a mineral acid catalyst, followed by addition of a carboxylic acid and esterification without isolation and purification of p〇3G. The etherification or polycondensation of the U3_propylene glycol reactant to form the P03G system is carried out using an acid catalyst as disclosed in U.S. Patent 6,977,291 and U.S. Patent 6,720,459, the disclosure of which is incorporated herein by reference. The keying reaction can also be carried out using an acid-containing sizing agent such as jp _ 182974A. The reaction is continued to be polycondensed or squashed until the desired molecular weight is reached, and a calculated amount of monoacid is then added to the reaction mixture. The reaction is continued while the water by-product is removed. At this stage, the acetation (four) reaction proceeds simultaneously. Therefore, it is preferred herein that the acid catalyst for polycondensing the diol is also used for acetification, and other esterification catalysts may be added during the esterification stage. In this procedure, the viscosity (molecular weight) of the resulting product is controlled by the time of addition of tracing. In an alternative procedure, the acetification reaction can be carried out on purified P03G by adding an esterification catalyst and tareric acid, followed by heating and removal of water. In this procedure, the viscosity of the resulting product is primarily a function of the molecular weight used. Regardless of the procedure followed by the acetalization process, any by-products are removed after the _chemical step and the remaining catalyzed residue of the polycondensation and/or esterification reaction is subsequently removed to obtain stability (especially at elevated temperatures) ) § product. This can be borrowed from about 80 C to about 1 〇〇. The crude vinegar product is hydrolyzed by treatment with water for a time sufficient to hydrolyze any residual acid ester derived from the catalyst without significantly affecting the acid retardation. The time required can vary from about 丨 hours to about 8 hours. If the hydrolysis is carried out under pressure, it may be a higher temperature and a correspondingly shorter time. In this regard, depending on the reaction conditions, the product may contain a combination of diacetic acid, monoacetic acid or diacetic acid and monoacetic acid' and a small amount of acid catalyst, unreacted toxaic acid and diol. The hydrolyzed polymer is further purified by known techniques (such as water washing, alkali neutralization, percolation and/or distillation) to remove water, 134067.doc -23-200918661 acid catalyst and unreacted carboxylic acid . The unreacted diol and acid catalyst can be removed, for example, by washing with deionized water. Unreacted carboxylic acid can also be removed, for example, by washing with deionized water or an aqueous solution or by vacuum stripping. The hydrolysis is typically followed by one or more water washing steps to remove the acid catalyst, and drying (preferably under vacuum) to obtain the ester product. Washing is also used to remove unreacted diol. Any unreacted monocarboxylic acid present may also be removed in a water wash' but may also be removed by washing with an aqueous base or by vacuum stripping. If desired, the product can be further fractionated by fractional distillation under reduced pressure to separate the low molecular weight. Proton NMR and wavelength chirped ray spectroscopy can be used to identify and quantify any residual catalyst (such as sulfur) present in the polymer. The proton Nmr can, for example, identify the sulfate groups present in the polymer chain, and the wavelength χ-ray glory method can determine the total sulfur (inorganic and organic sulfur) present in the polymer. The ester prepared by the above process of the present invention is substantially free of sulfur and is therefore suitable for use in high, high-quality fields. Preferably, the P〇3G ester after purification is substantially free of acidic catalyst end groups' It may contain very low levels of unsaturated end groups in the range of from about 〇003 to about me3 meq/g, primarily allyl end groups. The p〇3G ester may be considered to comprise a compound having the following formulae (IV) and (V) consisting essentially of: R.-C(0)-0-((CH2)30)m((CH2) ) 20) n-R2 (IV)
Ri-C(0)-〇-((CH2)3-〇)m((CH2)20)nCH2CH=CH2 (V), 其中R·2為Η或1<:(0);心及尺3中之每一者單獨地為含有6至 134067.doc •24- 200918661 4〇個碳原子之經取代或未經取代之芳族、飽和脂族、不飽 和脂族或環脂族有機基團;„!及η在一定範圍内以使Mn在 約200至約loooo範圍内;且其中式(ΠΙ)化合物以—定量存 在以使烯丙基端基(較佳所有不飽和端或端基)以約〇〇〇3至 約0.03 meq/g之範圍内的量存在。 較佳地’ P03GS旨具有小於P03G黏度之黏度。p〇3G酯之 較佳黏度在40。(:下在約20 cS至約150 cS之範圍内,且更 佳為約100 CS或1〇〇 c§以下。 基於關於P03G本身之上述較佳項,可確定p〇3G酯之其 他較佳特性。舉例而言,較佳分子量及多分散性係基於該 酯之P03G組份之較佳分子量及多分散性。 通用添加劑 本發明之合成潤滑油組合物包含基料與一或多種添加劑 之混合物,其中各添加劑係為了改良基料在其所欲應用 (例如作為液壓液、齒輪油、制動液、壓縮機潤滑劑、紡 織°°及壓延機潤滑劑、金屬加工液、冷凍潤滑劑、二衝程 引擎潤滑劑及/或曲軸箱潤滑劑)中之效能及特性之目的而 採用。 、添加劑it常可基於添加劑之類型及添加劑效應之所要水 準以通常可由熟習相關技術者確定之量添加。 較佳地,添加劑可混溶於P〇3G與P〇3G酯之一者或兩者 中。 較佳地,潤滑油添加劑包含以下各物中之至少一者:無 灰分散劑、金屬清潔劑、黏度改質劑、抗磨劑、抗氧化 134067.doc -25- 200918661 劑、摩擦改質劑、傾點下降劑 乳化劑、防鱗劑及其混合物。…、腐餘抑制劑、脫 當潤滑油組合物用作冷凍潤滑劑時, 包含以下各物令之至,丨、一 μ油添加劑較佳 赦禮a ω· t •極愿及抗磨添加劑、氧介芬 熱穩疋性改進劑、腐蝕抑制 齊丨乳化及 降劑、絮凝》: nr 11夂'又a數改進劑、傾點下 ㈣I凝點下降劑、清潔劑、消 混合物。 1黏度調節劑及其 單獨使用或與—戋多箱 4夕種其餘指定添加劑組合使用任何一 次夕種指疋添加劑音欲屬於 命4 屬於本發明之範嘴内。單獨使用或 與—或多種J:侦it中、夭4, 平调Μ史用或 制劑組合)使用一籀以卜紅彳4t 次夕種腐蝕抑 用種以上任何指定添加劑(例如一或多 擦改質劑)亦屬於本發明之範疇内。 可將個別添加劑以任何便利方式併人基料中。因此,1 =二:各者可直接藉由將其以所要濃度水準分散或= =基料中而添加至基料中。該摻合可在環境溫度下或在 南im下進行。 或者’該等添加劑中之全部或一些可摻合於濃縮物或添 口劑複合包(additive package)中’隨後摻合於基料中以製 備成品潤滑劑。濃縮物通常將經調配而含有適當量之添加 劑以在濃縮物與預定量之基本潤滑劑組合時在調配物中提 供所要濃度。 各種添加劑之非限制性、說明性實例如下。 無灰分散劑包含具有能夠與欲分散粒子結合之官能基的 聚合煙主鏈。通常,分散劑包含與聚合物主鏈通常經由橋 134067.doc •26- 200918661 基連接之胺、醇、酿胺及/或酯極性部分。無灰分散劑可 (例如)選自長鏈烴取代單羧酸及二羧酸及/或其酸酐之鹽、 知、私基g旨、醯胺、醯亞胺及喔。坐琳、長鍵烴之硫代敌酸 醋衍生物、多元胺直接與之連接之長鏈脂族烴,及藉由長 鏈取代酴與甲醛及聚伸烷基多元胺縮合形成之曼尼希縮合 (Mannich condensation)產物。 黏度改質劑(VM)發揮賦予潤滑油高溫及低溫可操作性 之作用。所用之VM可具有彼單一功能或可具有多功能。 亦已知亦充當分散劑之多功能黏度改質劑。說明性黏度 改質劑為聚異丁稀、乙烯與丙烯與高碳心烯烴之共聚物、 聚甲基丙烯酸酯、聚甲基丙烯酸烷基酯、曱基丙烯酸酯共 聚物、不飽和二羧酸與乙烯基化合物之共聚物、苯乙烯與 丙烯酸酯之互聚物,及苯乙烯/異戊二烯、苯乙烯/ 丁二烯 及異戊二烯/ 丁二烯之部分氫化共聚物,以及丁二烯及異 戊二烯及異戊二烯/二乙烯基苯之部分氫化均聚物。 含金屬或灰分形成清潔劑既充當清潔劑減少或移除沈積 物,亦充當酸中和劑或防銹劑,由此減少磨損及腐蝕且延 長引擎壽命。清潔劑通常包含極性頭部與長疏水性尾部, 其中極性頭部包含酸有機化合物之金屬鹽。該等鹽可含有 大體上化學計量之量的金屬,其中通常將其描述為正鹽或 中性鹽,且如可藉由ASTM D-2896所量測通常將具有〇至 約80之總鹼值(TBN)。有可能藉由使過量金屬化合物(諸如 氧化物或氫氧化物)與酸性氣體(諸如二氧化碳)反應而包括 大里金屬驗。所得高驗性清潔劑包含經中和清潔劑作為金 134067.doc 200918661 屬基(例如碳酸鹽)膠束之外層。該等高鹼性清潔劑可具有 約150或150以上且通常約250至約450或450以上之TBN。 說明性清潔劑包括中性及高鹼性磺酸鹽、苯酚鹽、硫化 苯酚鹽、硫代膦酸鹽、水楊酸鹽及環烷酸鹽及其他油溶性 金屬(尤其驗金屬或驗土金屬,例如納、鉀、鐘、約及鎮) 羧酸鹽。最普遍使用之金屬為鈣及鎂,其可存在於潤滑劑 中所用之清潔劑中;以及鈣及/或鎂與鈉之混合物。尤其 便利之金屬清潔劑為TBN為約20至約450之中性及高鹼性 磺酸鈣,以及TBN為約50至約450之中性及高鹼性苯酚約 及硫化苯酚鹽。 通常將二烴基二硫代磷酸金屬鹽用作抗磨劑及抗氧劑。 金屬可為鹼金屬或鹼土金屬,或鋁、鉛、錫、鉬、錳、錄 或銅。鋅鹽最普遍係以潤滑油組合物之總重量計以約〇. i 重量%至約1 0重量%、較佳約0.2重量%至約2重量%之量用 於满滑油中。其可根據已知技術,藉由通常經由使一或多 種醇或酚與pzS5反應首先形成二烴基二硫代磷酸(DDPA)且 隨後以鋅化合物中和所形成之DDPA而製備。舉例而言, 二硫代磷酸可藉由使第一醇與第二醇之混合物反應來製 備。或者,可製備多個二硫代磷酸,其中一者上之烴基在 性質上完全為第二級且其他者上之烴基在性質上完全為第 一級。為製備鋅鹽,可使用任何鹼性或中性鋅化合物,但 最通常採用氧化物、氫氧化物及碳酸鹽。商業添加劑由於 反應中使用過量驗性鋅化合物而通常含有過量鋅。 然而,在一實施例中,潤滑油組合物較佳大體上不含 134067.doc -28- 200918661 鋅。 氧化抑制劑或抗氧化劑降低基料在使用中變壞之趨勢, 該變壞可由氧化產物(諸如金屬表面上之淤渣及清漆樣沈 積物)及由黏度增長所證明。該等氧化抑制劑包括受阻 酴、較佳具有C5至c!2烷基側鏈之烷基酚硫酯之鹼土金屬 鹽、壬基酚硫化鈣、無灰油溶性苯酚鹽及硫化苯酚鹽、磷 硫化或硫化烴、填酯、金屬硫代胺基曱酸鹽、如 US4867890中所述之油溶性銅化合物,及含鉬化合物。Ri-C(0)-〇-((CH2)3-〇)m((CH2)20)nCH2CH=CH2 (V), where R·2 is Η or 1<:(0); heart and ruler 3 Each of which is individually substituted or unsubstituted aromatic, saturated aliphatic, unsaturated aliphatic or cycloaliphatic organic group containing from 6 to 134067.doc •24 to 200918661 4 carbon atoms; And η are within a range such that Mn is in the range of from about 200 to about loooo; and wherein the compound of formula (ΠΙ) is present in a quantitative amount such that the allyl end group (preferably all unsaturated ends or end groups) is about An amount in the range of from 〇〇〇3 to about 0.03 meq/g is present. Preferably, 'P03GS has a viscosity less than P03G. The preferred viscosity of the p〇3G ester is 40. (: at about 20 cS to about Within the range of 150 cS, and more preferably about 100 CS or 1 〇〇 c § below. Based on the above preferences for P03G itself, other preferred properties of the p〇3G ester can be determined. For example, preferred molecular weight And polydispersity is based on the preferred molecular weight and polydispersity of the P03G component of the ester. General Purpose Additives The synthetic lubricating oil compositions of the present invention comprise a mixture of a binder and one or more additives, each of which is added. The agent is used to improve the base material (for example, as hydraulic fluid, gear oil, brake fluid, compressor lubricant, textile ° and calender lubricant, metalworking fluid, refrigeration lubricant, two-stroke engine lubricant) And / or crankcase lubricants are used for the purpose of performance and characteristics. The additive it can often be added in an amount which can usually be determined by a person skilled in the art based on the type of additive and the desired effect of the additive effect. Preferably, the additive It may be miscible in one or both of P〇3G and P〇3G ester. Preferably, the lubricating oil additive comprises at least one of the following: an ashless dispersant, a metal detergent, a viscosity modifier Antiwear agent, anti-oxidation 134067.doc -25- 200918661 agent, friction modifier, pour point depressant emulsifier, antiscaling agent and mixtures thereof...., residual inhibitor, deodorized lubricating oil composition When chilling lubricants, the following items are included. 丨, one μ oil additive is better 赦 a a ω · t • Extreme and anti-wear additives, oxy- fen thermal stability improver, corrosion inhibition 丨 emulsification And lowering agent Flocculation: nr 11夂' and a number of improvers, pour point (four) I pour point depressant, detergent, a mixture. 1 viscosity modifier and its use alone or in combination with - 戋 multi-box 4 eve other specified additives Any one-night fingertip additive sounds belong to life. It belongs to the mouth of the invention. It can be used alone or with - or a variety of J: Detective, 夭4, Μ Μ history or preparation combination) It is also within the scope of the invention to treat any of the above specified additives (e.g., one or more wipe modifiers). Individual additives can be incorporated into the human base in any convenient manner. Thus, 1 = two: each can be added to the base directly by dispersing it at the desired concentration level or = = base. The blending can be carried out at ambient temperature or under Southern im. Alternatively, all or some of the additives may be blended into a concentrate or an additive package' subsequently blended into the base to prepare a finished lubricant. The concentrate will typically be formulated to contain an appropriate amount of additive to provide the desired concentration in the formulation when the concentrate is combined with a predetermined amount of the base lubricant. Non-limiting, illustrative examples of various additives are as follows. The ashless dispersant comprises a polymeric tobacco backbone having functional groups capable of binding to the particles to be dispersed. Typically, the dispersant comprises an amine, alcohol, amine and/or ester polar moiety that is attached to the polymer backbone, typically via a bridge 134067.doc • 26-200918661. The ashless dispersant may, for example, be selected from the group consisting of long chain hydrocarbon-substituted monocarboxylic acids and salts of dicarboxylic acids and/or anhydrides thereof, known as decylamine, quinoneimine and hydrazine. a long-chain aliphatic hydrocarbon directly linked thereto by a thiol, a long-chain hydrocarbon, and a Mannich formed by condensation of a long-chain substituted hydrazine with formaldehyde and a polyalkylene polyamine. Mannich condensation product. The viscosity modifier (VM) functions to impart high temperature and low temperature operability to the lubricating oil. The VM used may have a single function or may have multiple functions. Multifunctional viscosity modifiers which also act as dispersants are also known. Illustrative viscosity modifiers are polyisobutylene, copolymers of ethylene and propylene with high carbon olefins, polymethacrylates, polyalkyl methacrylates, mercapto acrylate copolymers, unsaturated dicarboxylic acids Copolymer with vinyl compound, interpolymer of styrene and acrylate, and partially hydrogenated copolymer of styrene/isoprene, styrene/butadiene and isoprene/butadiene, and Partially hydrogenated homopolymer of dienes and isoprene and isoprene/divinylbenzene. Metal- or ash-forming detergents act as both cleaners to reduce or remove deposits and also act as acid neutralizers or rust inhibitors, thereby reducing wear and corrosion and extending engine life. Detergents typically comprise a polar head and a long hydrophobic tail, wherein the polar head comprises a metal salt of an acid organic compound. The salts may contain a substantially stoichiometric amount of a metal, which is generally described as a normal or neutral salt, and will generally have a total base number of from about 80 to about 80 as measured by ASTM D-2896. (TBN). It is possible to include a large metal test by reacting an excess of a metal compound such as an oxide or a hydroxide with an acid gas such as carbon dioxide. The resulting highly detrimental cleaner comprises a neutralized cleaner as a gold 134067.doc 200918661 genus (e.g., carbonate) micelle outer layer. The overbased detergents can have a TBN of about 150 or more and typically from about 250 to about 450 or more. Illustrative cleaners include neutral and overbased sulfonates, phenates, sulfurized phenates, thiophosphonates, salicylates and naphthenates, and other oil-soluble metals (especially metals or soils) For example, sodium, potassium, bell, about and town) carboxylates. The most commonly used metals are calcium and magnesium, which may be present in the detergent used in the lubricant; and calcium and/or a mixture of magnesium and sodium. Particularly convenient metal cleaners are from about 20 to about 450 neutral and overbased calcium sulfonates having a TBN, and from about 50 to about 450 neutral and overbased phenolic and sulfurized phenates of TBN. A metal salt of a dihydrocarbyl dithiophosphate is generally used as an antiwear agent and an antioxidant. The metal may be an alkali metal or alkaline earth metal, or aluminum, lead, tin, molybdenum, manganese, copper or copper. The zinc salt is most commonly used in a full lubricating oil in an amount of from about 0.1% by weight to about 10% by weight, preferably from about 0.2% by weight to about 2% by weight, based on the total weight of the lubricating oil composition. It can be prepared according to known techniques by first forming a dihydrocarbyl dithiophosphoric acid (DDPA) by first reacting one or more alcohols or phenols with pzS5 and subsequently neutralizing the formed DDPA with a zinc compound. For example, dithiophosphoric acid can be prepared by reacting a mixture of a first alcohol and a second alcohol. Alternatively, a plurality of dithiophosphoric acids may be prepared, one of which is completely second in nature and the other of which is completely first in nature. For the preparation of zinc salts, any basic or neutral zinc compound can be used, but oxides, hydroxides and carbonates are most commonly employed. Commercial additives typically contain an excess of zinc due to the use of excess zinc compounds in the reaction. However, in one embodiment, the lubricating oil composition preferably does not substantially contain 134067.doc -28-200918661 zinc. The oxidation inhibitor or antioxidant reduces the tendency of the binder to deteriorate during use, as evidenced by oxidation products such as sludge and varnish-like deposits on the metal surface and by viscosity growth. The oxidation inhibitors include hindered oxime, alkaline earth metal salts of alkyl phenol thioesters preferably having a C5 to c! 2 alkyl side chain, nonyl phenol calcium sulfide, ashless oil soluble phenates, and sulfurized phenates, phosphorus Sulfurized or sulfurized hydrocarbons, ester-filled, metal thioamino phthalates, oil-soluble copper compounds as described in U.S. Patent 4,867,890, and molybdenum-containing compounds.
可包括摩擦改質劑以改良燃料經濟性。吾人熟知油溶性 烷氧基化單胺及二胺改良邊界層潤滑性。該等胺可以原樣 使用或以與硼化合物(諸如氧化硼、_化硼、偏硼酸鹽、 硼酸或侧酸單烷基醋、爛酸二烷基醋或删酸三烷基醋)之 加合物或反應產物形式使用。 已知其他摩擦改質劑。在該等者中有藉由㈣酸及酸軒 與烷醇反應形成之醋。其他習知摩擦改質劑通常由與親油 烴鏈共價結合之極性端基(例如綾基或羥基)組成。 腦7〇285〇中描述幾酸及酸酐與院醇之醋。另一習知摩擦 改質劑之實例為有機金屬鉬。 + 其Γ月性防錄劑係選自以下各物之群··非離子聚氧基伸烧 基夕元醇及其酯、聚氧基伸烧㈣及陰離子燒基碍酸。 = 吏用含銅及錯之腐#抑制劑。通常,該等化 子…”硫化物、其衍生物及其聚 I ,、他添加劑為噻二唾之硫代亞磺醯胺及多硫基亞於 酿胺,諸㈣κ丨測㈣所敎彼等者。料 134067.doc -29- 200918661 亦屬於此類添加劑。 j乳化組份之—說明性實例如队A侧522中所述。其 糸藉由使氧化稀與藉由使雙環氧化物與多元醇 之加合物反應而獲得。 ^熳侍 傾點下降劑(或者稱為濁滑油改進劑)降低流體可流動或 :被傾倒時之最低溫度。該等添加劑為吾人所熟知。改良 流體之低溫流純之典型彼等添加劑扣及〜二炫基反 丁歸·-酸醋/乙酸乙、说妒-U取此 βFriction modifiers can be included to improve fuel economy. It is well known that oil-soluble alkoxylated monoamines and diamines improve the boundary layer lubricity. The amines may be used as such or in combination with a boron compound such as boron oxide, boron boride, metaborate, boric acid or oleic acid monoalkyl vinegar, rotten acid dialkyl vinegar or acid-cutting trialkyl vinegar. Used as a substance or as a reaction product. Other friction modifiers are known. Among these, there are vinegar formed by reacting (iv) acid and acid with an alkanol. Other conventional friction modifiers typically consist of polar end groups (e.g., sulfhydryl or hydroxy) covalently bonded to the oleophilic hydrocarbon chain. The brain 7 〇 285 描述 describes several acids and anhydrides and vinegar. Another example of a conventional friction modifier is organometallic molybdenum. + The lunar anti-recording agent is selected from the group consisting of non-ionic polyoxyalkylene extended calcinol and its ester, polyoxyalkylene extended (four) and anionic burning base acid. = Use copper and wrong rot # inhibitor. Usually, the sulphide, its derivatives and its poly-I, the additive is thiadisulfide thiosulfinamide and polythiol amide, and the (four) κ 丨 (4) Etc. 134067.doc -29- 200918661 Also pertaining to such additives. j. Emulsifying components - illustrative examples are as described in Panel A, Side 522. The ruthenium is made by diluting the oxidizing agent with Obtained by the reaction of the polyol adduct. The pour point depressant (or known as the turbid oil improver) reduces the flow of the fluid or: the lowest temperature at which it is poured. These additives are well known to us. The low temperature flow is pure and the other additives are deducted and ~2 炫基反丁归·- vinegar/acetic acid B, saying 妒-U take this β
乙烯酉曰共聚物、聚甲基丙烯酸烷基酯及 其類似物。 泡沫控制可由包括聚矽氧烷型消泡齊“例如矽油或聚二 甲基矽氧烷)之多種化合物提供。 -些上述添加劑可提供多種效應;因此,例如,單一添 加劑可充當分散劑-氧化抑制劑。該方法為吾人所熟知且 無需進一步詳細描述。 特定用於壓縮冷凍系統之添加劑之說明性、非限制性實 例如下。Vinyl ruthenium copolymer, polyalkyl methacrylate, and the like. Foam control may be provided by a variety of compounds including polyoxyalkylene type defoaming "e.g., eucalyptus or polydimethyl siloxane" - some of the above additives may provide a variety of effects; thus, for example, a single additive may act as a dispersant - oxidation Inhibitors. This method is well known and need not be described in further detail. Illustrative, non-limiting examples of additives specifically for use in compression refrigeration systems are as follows.
極壓添加劑為熟習此項技術者所已知的且用於向在相對 極面壓力下發生之應用中的金屬表面提供保護。說明性極 壓及抗磨添加劑包括磷酸鹽、磷酸酯(磷酸二曱苯酯)、亞 磷酸鹽、硫代磷酸鹽(二有機二硫代磷酸鋅)氣化蠟、硫化 脂肪及烯烴、有機鉛化合物、脂肪酸、鉬錯合物、函素取 代之有機矽化合物、硼酸鹽、有機酯、_素取代之磷化合 物、硫化Diels Alder加合物、有機硫化物、含有氯及硫之 化合物、有機酸之金屬鹽。 134067.doc -30. 200918661 w S 氧化及熱穩定性改進劑包括空間位阻酚(bht)、 芳族胺、二硫代磷酸鹽、亞磷酸鹽、硫化物及二硫代酸之 金屬鹽。 說月I·生腐蝕抑制劑包括有機酸、有機胺、有機磷酸鹽、 有機醇、I屬磺酸鹽&有機亞磷酸鹽。 黏度心數為點度隨溫度變化之量度,且高數值表明黏度 隨溫度之變化最小。鑒於本發明之潤滑油組合物之高黏度 才曰數,有可旎調配無黏度指數改進劑之潤滑油組合物。然 而’可月&存在希望進一步改良黏度指數之應用。說明性黏 度指數改進劑包括聚異丁烯、聚甲基丙烯酸酯及聚烷基苯 乙烯。 說明性傾點及/或絮凝點下降劑包括聚曱基丙烯酸酯乙 烯-乙酸乙烯共聚物、琥珀醯胺酸_烯烴共聚物、乙烯_α_烯 烴共聚物及蠟與萘或酚之弗瑞德-克來福特縮合(Friedel_Extreme pressure additives are known to those skilled in the art and are used to provide protection to metal surfaces in applications where relative pole pressure occurs. Illustrative extreme pressure and anti-wear additives include phosphate, phosphate (diphenyl phenyl phosphate), phosphite, thiophosphate (zinc dithiophosphate) gasification wax, sulfurized fat and olefin, organic lead Compounds, fatty acids, molybdenum complexes, elemental substituted organotelluric compounds, borate, organic esters, phosphine-substituted phosphorus compounds, sulfurized Diels Alder adducts, organosulfides, compounds containing chlorine and sulfur, organic acids Metal salt. 134067.doc -30. 200918661 w S Oxidation and thermal stability improvers include sterically hindered phenol (bht), aromatic amines, dithiophosphates, phosphites, sulfides and metal salts of dithioacids. Said month I. Raw corrosion inhibitors include organic acids, organic amines, organic phosphates, organic alcohols, I sulfonates & organic phosphites. The number of viscosities is a measure of the change in point with temperature, and the high value indicates that the viscosity changes minimally with temperature. In view of the high viscosity of the lubricating oil composition of the present invention, there is a lubricating oil composition which can be formulated with a non-viscosity index improver. However, there is a desire to further improve the viscosity index. Illustrative viscosity index improvers include polyisobutylene, polymethacrylate, and polyalkyl styrene. Illustrative pour point and/or flocculation point depressants include polydecyl acrylate ethylene-vinyl acetate copolymers, succinyl amide copolymers, ethylene _α olefin copolymers, and waxes with naphthalene or phenol - Cladding condensate (Friedel_
Crafts condensation)產物。 說明性清潔劑包括績酸鹽、經長鏈烧基取代之芳族續 酸、膦酸鹽、硫代膦酸鹽、酚鹽、烷基酚之金屬鹽、烷基 硫化物、烷基酚-醛縮合產物、經取代之水楊酸鹽之金屬 鹽、來自不飽和酸酐及胺之反應產物的N—取代募聚物或聚 合物,及併有聚酯鍵之共聚物(諸如乙酸乙稀酯_順丁烯二 酸酐共聚物)。 說明性消泡劑為矽氧烷聚合物。 說明性黏度調節劑包括聚異丁稀、聚甲基丙烯酸酯、聚 烷基苯乙稀、環烷油、烷基苯油、石躐油、聚酯、聚氣乙 134067.doc •31 200918661 烯及聚磷酸鹽。 在本發明中’添加劑應至少可部分(大於約50重量%)混 溶於基料中。-般而言,此意謂所用添加劑至少在某種程 度上,且較佳在大體程度上具有油溶性。 因此潤滑油組合物應較佳為大體上均勻之混合物,其中 組份大體上無沈降或相分離。 潤滑油組合物以潤滑油組合物之總重量計較佳包含小於 50重量%之量的添加劑。在各種實施例中,以潤滑油組合 物之總重量計’潤滑油可包含約25重量%或25重量%以 下,或約10重量%或10重量%以下,或約5重量%或5重量% 以下之量的添加劑。 特定添加劑複合包 在一些實施例中,潤滑油組合物含有包含至少三種不同 添加劑之組合的添加劑複合包(重量%以組合物總重量 計): (a) 抗磨添加劑複合包,其包含約0.5重量%至約2.0重 量%之包含磷酸胺抗磨添加劑及硫代磷酸酯抗磨添加劑之 混合物,及 (b) 約〇·〇5重量%至約0.5重量%之亞曱基雙(二烷基二硫 代胺基曱酸酯)。亞甲基雙(二烷基二硫代胺基曱酸酯)可充 當極壓添加劑及/或抗氧化劑。 在替代性實施例中,潤滑油組合物中之抗磨添加劑複合 包含有約0.5重量%至約1 ·〇重量%之包含磷酸胺抗磨添加劑 及硫代構酸酯抗磨添加劑的混合物。 134067.doc -32· 200918661 在替曰代性實施例中,添加劑複合包含有約(Μ重量%至約 〇.3重量%之亞甲基雙(二絲二硫代胺基甲酸醋)。 在-較佳實施例中,潤滑油組合物另外包含以下各物中 之一或多者(重量%以組合物總重量計” (c)約0.05重量%至約2 〇重量%,或者約〇 〇5重量%至 :1.0重量%,或者約〇1重量%至約〇 5重量。之曱苯三唑抗 乳化劑/金屬鈍化劑添加劑;及/或 ⑷約0.05重篁%至約1〇重量%,或者約。」重量%至約 1.0重里% ’或者約〇」重量%至約〇 75重量%之選自由以下 各物”且成之群之主抗氧化添加劑複合包:受阻胺抗氧化 劑、受阻酚抗氧化劑及其混合物,及/或 0)約0.05重1; %至約〇 3重量。/。,或者約〇 〇5重量%至 約0.2重量%之磺酸鈣腐蝕抑制劑;及/或 (f)約0重量%至約2.0重量。/。,或者約〇.〇5重量%至 約1.0重量%,或者約0」重量%至約G 5重量%之嗓二嗤金屬 鈍化劑及二硫化物金屬鈍化劑之一者或組合。 齒輪/液壓湖滑劑 本發明之潤滑劑組合物之較佳用途係作為齒輪/液壓潤 滑劑。此類潤滑劑之例示性配方如下(重量%以總組合物 計): (a) 約90重量❶/。至99重量。/❶,或者約95重量%至約98.5重 量%之在環境溫度下為流體的pTEEG,或1>丁££(3與在環境 溫度下為流體之PTEEG酯之混合物; (b) 抗磨添加劑複合包,其包含約0.5重量%至約2 〇重 134067.doc •33- 200918661 量% ’或者約0.5重量%至約1 .〇重量%之包含磷酸胺抗磨添 加劑及硫代磷酸酯抗磨添加劑之混合物; (c) 約0.05重量%至約0.5重量%,或者約〇.1重量%至約 0.3重量〇/〇之亞曱基雙(二烷基二硫代胺基甲酸酯)極壓/抗氧 化添加劑; (d) 〇至約2.0重量%,或者約0.05重量%至約2.0重量 %,或者約0.05重量%至約1 _〇重量%,或者約〇. 1重量。/〇至 約0.5重量%之曱苯三唑抗氧化劑/金屬鈍化劑添加劑; (e) 約〇重量%至約1.0重量%,或者約0.05重量%至約 1 ·〇重量°/° ’或者約〇. 1重量°/❶至約1.0重量%,或者約〇. 1重 量%至約0.75重量°/。之選自由以下各物組成之群之主抗氧 化添加劑複合包:受阻胺抗氧化劑、受阻酚抗氧化劑及其 混合物, (f) 約〇至約〇.3重量%,或者約〇.〇5重量。/〇至約0·3重量 % ’或者約0.05重量°/。至約〇.2重量%之磺酸鈣腐蝕抑制 劑;及/或 (g) 〇至約2.0重量%,或者約o.oi重量%至約2.0重量 °/〇,或者約0.05重量%至約1·〇重量。/。,或者約〇丨重量%至 約0.5重量%之噻二唑金屬鈍化劑及二硫化物金屬鈍化劑之 一者或組合。 實例 除非另有說明’否則所有份數、百分比等係以重量計。 分別使用ASTM方法D445-83及ASTM方法D792-91來測 定聚合物之動力學黏度及密度。 134067.doc -34- 200918661 所用其他ASTM方法如下文表格中所列。 將本發明之物質在有及無潤滑油添加劑複合包的情況下 進行測試。測試期間所用之複合劑包含表1中所列之組份。 表1Crafts condensation) product. Illustrative detergents include acid salt, aromatic acid extended by long chain alkyl groups, phosphonates, thiophosphonates, phenates, metal salts of alkyl phenols, alkyl sulfides, alkyl phenols - An aldehyde condensation product, a metal salt of a substituted salicylate, an N-substituted merging polymer or polymer derived from a reaction product of an unsaturated acid anhydride and an amine, and a copolymer having a polyester bond (such as ethylene glycol) _ Maleic anhydride copolymer). An illustrative antifoaming agent is a siloxane polymer. Illustrative viscosity modifiers include polyisobutylene, polymethacrylate, polyalkyl styrene, naphthenic oil, alkyl benzene oil, eucalyptus oil, polyester, polygas 134067.doc •31 200918661 olefin And polyphosphates. In the present invention, the additive should be at least partially (greater than about 50% by weight) miscible in the binder. In general, this means that the additives used are at least to some extent, and preferably are generally oil soluble. Accordingly, the lubricating oil composition should preferably be a substantially homogeneous mixture wherein the components are substantially free of settling or phase separation. The lubricating oil composition preferably comprises an additive in an amount of less than 50% by weight based on the total weight of the lubricating oil composition. In various embodiments, the lubricating oil may comprise about 25% by weight or less by weight, or about 10% by weight or less, or about 5% by weight or 5% by weight, based on the total weight of the lubricating oil composition. The following amounts of additives. Specific Additive Composite Package In some embodiments, the lubricating oil composition contains an additive composite package (wt% by weight of the total composition) comprising a combination of at least three different additives: (a) an antiwear additive composite package comprising about 0.5 5% by weight to about 2.0% by weight of a mixture comprising a phosphate amine antiwear additive and a phosphorothioate antiwear additive, and (b) from about 5% by weight to about 0.5% by weight of a fluorenyl bis(dialkyl group) Dithioamino phthalate). Methylene bis(dialkyldithioamino phthalate) can be used as an extreme pressure additive and/or an antioxidant. In an alternative embodiment, the antiwear additive composite in the lubricating oil composition comprises from about 0.5% to about 1% by weight of a mixture comprising a phosphate amine antiwear additive and a thioate antiwear additive. 134067.doc -32· 200918661 In an alternative embodiment, the additive composite comprises about (from about 5% by weight to about 3% by weight of methylene bis(dioxadithiocarbamic acid vinegar). In a preferred embodiment, the lubricating oil composition additionally comprises one or more of the following (% by weight based on the total weight of the composition) (c) from about 0.05% by weight to about 2% by weight, or about 〇〇 5% by weight to: 1.0% by weight, or from about 1% by weight to about 5% by weight. The benzotriazole anti-emulsifier/metal deactivator additive; and/or (4) from about 0.05% by weight to about 1% by weight , or about."% by weight to about 1.0% by weight 'or about 5% by weight to about 75% by weight of the main antioxidant additive package selected from the group consisting of: a hindered amine antioxidant, blocked a phenolic antioxidant and mixtures thereof, and/or 0) from about 0.05 by weight; from about 1% to about 3% by weight, or from about 5% by weight to about 0.2% by weight of a calcium sulfonate corrosion inhibitor; and/or (f) from about 0% by weight to about 2.0% by weight, or from about 5% by weight to about 1.0% by weight, or about 0% "% by weight to about 5% by weight of the bismuth metal passivator and the disulfide metal passivating agent or combination. Gear / hydraulic lake slip agent The preferred use of the lubricant composition of the present invention is as a gear / Hydraulic Lubricants. Exemplary formulations of such lubricants are as follows (% by weight based on total composition): (a) from about 90 weights 。/. to 99 weight% ❶, or from about 95% to about 98.5% by weight a pTEEG that is fluid at ambient temperature, or a mixture of 1> and a PTEEG ester that is fluid at ambient temperature; (b) an antiwear additive composite package comprising from about 0.5% to about 2 weights 134067.doc •33- 200918661 Amount %' or from about 0.5% by weight to about 1.% by weight of a mixture comprising a phosphate amine antiwear additive and a phosphorothioate antiwear additive; (c) from about 0.05% by weight to about 0.5% % by weight, or about 11. 1% by weight to about 0.3% by weight of hydrazine/bisindole bis(dialkyldithiocarbamate) extreme pressure/antioxidant additive; (d) 〇 to about 2.0 weight %, or from about 0.05% to about 2.0% by weight, or from about 0.05% to about 1% by weight %, or about 〇. 1 重量./〇 to about 0.5% by weight of benzotriazole antioxidant/metal deactivator additive; (e) from about 5% by weight to about 1.0% by weight, or from about 0.05% by weight to about 1 · 〇 weight ° / ° 'or about 1. 1 weight ° / ❶ to about 1.0% by weight, or about 1. 1% by weight to about 0.75 weight ° /. selected from the group consisting of the following main antioxidant Additive compound package: hindered amine antioxidant, hindered phenol antioxidant and mixtures thereof, (f) from about 〇 to about 3% by weight, or about 〇. /〇 to about 0. 3 wt% or about 0.05 wt. Up to about 2% by weight of a calcium sulfonate corrosion inhibitor; and/or (g) 〇 to about 2.0% by weight, or about o. oi% by weight to about 2.0% by weight, or about 0.05% by weight to about 1·〇 weight. /. Or one or a combination of about 5% by weight to about 0.5% by weight of the thiadiazole metal deactivator and the disulfide metal deactivator. EXAMPLES Unless otherwise stated, all parts, percentages, etc. are by weight. The dynamic viscosity and density of the polymer were determined using ASTM method D445-83 and ASTM method D792-91, respectively. 134067.doc -34- 200918661 Other ASTM methods used are listed in the table below. The materials of the present invention were tested with and without a lubricating oil additive composite package. The complex used during the test contained the components listed in Table 1. Table 1
添加劑 描述 功能 購自 IRGALUBE® TPPT 硫代磷酸三苯 酯,通常含有9% 磷及9.4%硫 抗磨劑/極壓 劑 Ciba Specialty Chemicals, Tarrytown, NY VANLUBE® 7723 亞甲基雙(二丁基 二硫代胺基曱酸 酯) 急參抗氧化 劑及極壓劑 RT Vanderbilt Company Inc., Norwalk, CT VANLUBE® 887E 甲苯三唑 抗氧化劑 RT Vanderbilt Company Inc., Norwalk, CT PANA 苯基α-萘胺 抗氧化劑 Akrochem, Akron, OH VANLUBE® RD 聚合1,2-二氫-2,2,4-三甲基喹啉 抗氧化劑 R.T. Vanderbilt Co., Inc., Norwalk, CT IRGANOX® 1135 受阻酚 抗氧化劑 Ciba Specialty Chemicals, Tarrytown, NY IRGALUBE® 349 胺磷酸鹽混合物 及腐 鍅抑制劑 Ciba Specialty Chemicals, Tarrytown,NY VANLUBE® 8912E 磺酸鈣 防銹劑 RT Vanderbilt Company Inc., Norwalk, CT CUVAN® 826 2,5-二巯基-1,3,4-噻二唑衍生物 f蝕抑制劑 $金屬鈍化 L#j RT Vanderbilt Company, Inc., Norwalk, CT IRGACORE®L12 腐餘抑制劑 Ciba Specialty Chemicals, Tarrytown, NY 聚二甲基矽氧烷 聚合物200cSt 消泡劑 Dow Coming, Midland, MI LUBRIZOL 889D 酯共聚物 —— 消泡劑 The Lubrizol Corporation, Wickliffe, OH 134067.doc 35· 200918661 實例1-5 實例1-5係藉由在50〇C下攪拌或在室溫下在罐型滚磨機 上之密封罐中將混合物旋轉經2至3日將固體成份(呈顆粒 形式)摻合於具有表2中所列之Μη的PTEEG(使用25莫耳 乙二醇製備)中來製備。顆粒形式之固體成份有助於避免 當使用粉末形式時發生之造成過量起泡之空氣夾帶。當在 敞口罐中製備混合物時,使用氮氣氣氛。將液體添加劑添 加至預混合摻合物中,從而確保無固體粒子未溶解° u下 表2概述該等實例之組成。 表2 :實例1-5 實例1 實例2 實例3 實例4 實例5 聚二甲基矽氧烷 聚合物 0.005 0.0025 0.0025 Lubrizol 889D 0.05 0.05 Vanlube® 7723 0.3 0.3 0.2 0.3 0.3 Vanlube® 887E 0.4 0.4 0.3 0.4 0.4 Irganox® 1135 0.2 0.2 0.2 0 Irgalube® TPPT 0.5 0.5 0.5 0.5 0.5 Irgalube® 349 0.4 0.4 0.4 0.4 0.4 Vanlube® 8912E 0.1 0 PANA 0.5 0 Vanlube® RD 0.25 0.25 0.5 0.5 Irgacore® L12 0.1 0 CUVAN® 826 0.1 0.1 0.1 0.1 0.1 PTEEG (Mn, SEC/GPC) 98.3 (993) 97.85 (1093) 97.95 (1093) 97 (1040) 97.8 (993) 134067.doc -36- 200918661 對該等實例中之組合物進行為建立關於工業上可接受之 抗磨齒輪/液壓油之標準規格所需之測試。結果如表3及表 4所示。 表3 :實例1-5之潤滑劑特性 特性 ASTM 實例1 實例2 實例3 實例4 實例5 黏度指數 D-2270 207 206 208 203 傾點,°c D-97 -45 -45 -48 -42 -48 閃點,°c D-92 272 288 286 302 294 四球磨痕, mm D-4172 0.3 0.37 0.4 0.59 0.45 摩擦係數 D-4172 0.042 0.033 0.032 0.044 0.051 負載磨損指 數 D-2783 50.13 61.5 77 77 42.28 最大無卡咬 負載(磨痕, mm) D-2783 126 (·49) 160 (.52) 200 (.54) 200 (.52) 100 (.43) 最大卡咬負 載(磨痕, mm) D-2783 160 kg (2.78) 無 無 無 160kg (2.37) 焊接負載, kg D-2783 200 200 250 250 200 法列克斯軸 銷及V型塊 (Falex Pin 及 V block)最大 負載,lb D-3233 4250 3000 3000 4250 3500 134067.doc -37- 200918661 表4-氧化及腐蝕測試結果(ASTM D4636-190C-24h) 特性 實例1 實例2 實例3 實例4 實例5 黏度變化 -11.7 1.49 0.97 6.731 6.5 酸值變化 (Mg/KOH/g) 0.7 0.07 0.09 0.3 0.3 黏度,在40°C下 初始,cSt 195.1 234.8 238.3 208.1 198.1 cSt 172.2 238.3 240.6 222.1 210.9 總酸# 初始,mg KOH/g 0.22 0.25 0.25 0.42 0.21 ,mg KOH/g 0.92 0.32 0.34 0.72 0.51 銅腐# Dull-lb Dull-lb Dull-lb Dull-lb Dull-lb 與其他實例相比,實例1含有最小量之抗氧化劑(如表2 所示)。此潤滑劑在氧化及腐蝕測試(ASTM D4636)期間如 由在190°C下運行24 h之後黏度降低(-11.7%)及酸值顯著變 化(0·7)所示顯示熱降解之跡象(如表4所示)。然而,此組 合物如由極低四球磨痕(0.3 mm-ASTM D4172-40 kgjj200 rpm,在75°C下)及法列克斯轴銷及V型塊測試(最大負載 4250 lb-ASTM D3233)所示顯示極佳抗磨及承載特性(如表 3所示)。 實例2含有複合抗氧化劑,其除第二抗氧化劑 (VANLUBE® 7723,二硫代胺基甲酸酯)之外,含有包括受 阻胺(VANLUBE® RD,0_25 重量 %)及受阻酚(IRGANOX® 1135,0.2重量%)之主抗氧化劑。如由ASTM D4636所測 試,此潤滑劑顯示極小之黏度變化及可忽略之酸值變化。 實例3含有磺酸鈣(VANLUBE® 8912E,0.1重量%)。同 134067.doc -38- 200918661 樣地,此添加劑複合包如由高"負載磨損指數”(77)所示顯 示極佳承載特性,儘管其含有較低數量之VANLUBE® 7723亦然。 含有0,5重量%或0.5重量%以上受阻胺(VANLUBE® RD 及PANA)之實例4及實例5與含有0·25重量% VANLUBE® RD之實例相比顯示高黏度增加,不過其均如法列克斯負 載(表3 )所指示顯示高承載特性。 在包括超過0.5%之受阻胺的情況下亦觀察到對抗磨特性 之負面影響(在無VANLUBE® RD的情況下"四球磨損"最 低)° 在VANLUBE® RD含量為0_25重量%時(不考慮其他組份) 觀察到低"摩擦係數”。 本發明之組合物提供高承載能力(法列克斯負載>3000 lb-表3)、低摩擦及磨損係數。 又,如該等實例所示,受阻酚與受阻胺之抗氧化劑組合 提供氧化及熱穩定性、防腐性及防錢性(銅腐钱-1 b)之最佳 結果。 含有0.25重量% VANLUBE® RD(受阻胺)及0.2重量% IRGANOX® 11 3 5 (受阻盼)之組合物就氧化及腐|虫穩定性測 試-ASTM D 4636(190°C-24 h)而言顯示最小黏度及酸值變 化。 134067.doc -39-Additive description function available from IRGALUBE® TPPT Triphenyl thiophosphate, usually containing 9% phosphorus and 9.4% sulfur antiwear/extreme pressure agent Ciba Specialty Chemicals, Tarrytown, NY VANLUBE® 7723 methylene bis (dibutyl bis) Thioamine phthalate) Acute antioxidants and extreme pressure agents RT Vanderbilt Company Inc., Norwalk, CT VANLUBE® 887E Tolutriazole Antioxidant RT Vanderbilt Company Inc., Norwalk, CT PANA Phenyl α-naphthylamine Oxidizing Agent Akrochem, Akron, OH VANLUBE® RD Polymerization 1,2-Dihydro-2,2,4-Trimethylquinoline Antioxidant RT Vanderbilt Co., Inc., Norwalk, CT IRGANOX® 1135 Hindered Phenol Antioxidant Ciba Specialty Chemicals, Tarrytown, NY IRGALUBE® 349 Amine Phosphate Mixture and Corrosion Inhibitor Ciba Specialty Chemicals, Tarrytown, NY VANLUBE® 8912E Calcium Sulfate Rust Preventive Agent RT Vanderbilt Company Inc., Norwalk, CT CUVAN® 826 2,5-II Mercapto-1,3,4-thiadiazole derivative f-etch inhibitor $metal passivation L#j RT Vanderbilt Company, Inc., Norwalk, CT IRGACORE® L12 corrosion inhibitor Ciba Specialty Chemicals, Tarrytown, NY Polydimethylsiloxane polymer 200cSt defoamer Dow Coming, Midland, MI LUBRIZOL 889D Ester Copolymer - Defoamer The Lubrizol Corporation, Wickliffe, OH 134067.doc 35· 200918661 Examples 1-5 Examples 1-5 The solid components (in the form of granules) are blended in the form listed in Table 2 by stirring the mixture at 50 ° C or at room temperature in a sealed can on a can roller mill for 2 to 3 days. It was prepared by PTEEG (prepared using 25 mol ethylene glycol). The solid form in particulate form helps to avoid entrainment of air that causes excessive foaming when using the powder form. When the mixture was prepared in an open can, a nitrogen atmosphere was used. A liquid additive is added to the premix blend to ensure that no solid particles are not dissolved. Table 2 summarizes the composition of the examples. Table 2: Examples 1-5 Example 1 Example 2 Example 3 Example 4 Example 5 Polydimethylsiloxane polymer 0.005 0.0025 0.0025 Lubrizol 889D 0.05 0.05 Vanlube® 7723 0.3 0.3 0.2 0.3 0.3 Vanlube® 887E 0.4 0.4 0.3 0.4 0.4 Irganox ® 1135 0.2 0.2 0.2 0 Irgalube® TPPT 0.5 0.5 0.5 0.5 0.5 Irgalube® 349 0.4 0.4 0.4 0.4 0.4 Vanlube® 8912E 0.1 0 PANA 0.5 0 Vanlube® RD 0.25 0.25 0.5 0.5 Irgacore® L12 0.1 0 CUVAN® 826 0.1 0.1 0.1 0.1 0.1 PTEEG (Mn, SEC/GPC) 98.3 (993) 97.85 (1093) 97.95 (1093) 97 (1040) 97.8 (993) 134067.doc -36- 200918661 The compositions of the examples are made for the establishment of industrially Tests required to accept the standard specifications for anti-wear gears/hydraulic oils. The results are shown in Tables 3 and 4. Table 3: Lubricant Characteristics of Examples 1-5 ASTM Example 1 Example 2 Example 3 Example 4 Example 5 Viscosity Index D-2270 207 206 208 203 Pour Point, °c D-97 -45 -45 -48 -42 -48 Flash point, °c D-92 272 288 286 302 294 Four-ball wear scar, mm D-4172 0.3 0.37 0.4 0.59 0.45 Friction coefficient D-4172 0.042 0.033 0.032 0.044 0.051 Load wear index D-2783 50.13 61.5 77 77 42.28 Maximum no card Bite load (wear marks, mm) D-2783 126 (·49) 160 (.52) 200 (.54) 200 (.52) 100 (.43) Maximum card bit load (wear marks, mm) D-2783 160 Kg (2.78) No or no 160kg (2.37) Welding load, kg D-2783 200 200 250 250 200 Falex pin and V block (Falex Pin and V block) maximum load, lb D-3233 4250 3000 3000 4250 3500 134067.doc -37- 200918661 Table 4 - Oxidation and Corrosion Test Results (ASTM D4636-190C-24h) Characteristic Example 1 Example 2 Example 3 Example 4 Example 5 Viscosity Change -11.7 1.49 0.97 6.731 6.5 Acid Value Change (Mg/ KOH/g) 0.7 0.07 0.09 0.3 0.3 Viscosity, initial at 40 ° C, cSt 195.1 234.8 238.3 208.1 198.1 cSt 172.2 238.3 240.6 222.1 210.9 Total Acid # Initial, mg KOH/g 0.22 0.25 0.25 0.42 0.21 , mg KOH/g 0.92 0.32 0.34 0.72 0.51 Copper rot # Dull-lb Dull-lb Dull-lb Dull-lb Dull-lb Example 1 compared to other examples Contains a minimum amount of antioxidant (as shown in Table 2). This lubricant showed signs of thermal degradation during oxidation and corrosion testing (ASTM D4636) as shown by a decrease in viscosity (-11.7%) and a significant change in acid value (0.7) after 24 hours of operation at 190 °C (eg Table 4)). However, this composition is tested by a very low four-ball wear mark (0.3 mm-ASTM D4172-40 kgjj200 rpm at 75 ° C) and a Falex pin and V-block test (maximum load 4250 lb-ASTM D3233) The figure shows excellent wear and load bearing properties (as shown in Table 3). Example 2 contains a composite antioxidant containing, in addition to the second antioxidant (VANLUBE® 7723, dithiocarbamate), a hindered amine (VANLUBE® RD, 0-25% by weight) and hindered phenol (IRGANOX® 1135). , 0.2% by weight of the main antioxidant. As tested by ASTM D4636, this lubricant exhibits minimal viscosity changes and negligible acid value changes. Example 3 contained calcium sulfonate (VANLUBE® 8912E, 0.1% by weight). As with 134067.doc -38- 200918661, this additive composite package exhibits excellent load carrying characteristics as shown by the high "load wear index" (77), although it also contains a lower number of VANLUBE® 7723. Example 4 and Example 5 of 5% by weight or more of hindered amines (VANLUBE® RD and PANA) showed a high viscosity increase compared to the example containing 0.255% by weight of VANLUBE® RD, but all of them were like Falek The high load-bearing characteristics are indicated by the load (Table 3). The negative effects of anti-wear properties were also observed in the case of more than 0.5% hindered amine (in the absence of VANLUBE® RD "four-ball wear "lowest) ° A low "coefficient of friction is observed when the VANLUBE® RD content is 0-25% by weight (regardless of other components). The compositions of the present invention provide high load carrying capacity (Farex load > 3000 lb - Table 3), low friction and wear coefficient. Again, as shown by these examples, the combination of hindered phenol and hindered amine antioxidant provides the best results for oxidation and thermal stability, corrosion resistance and anti-money properties (copper rot -1 b). The composition containing 0.25 wt% VANLUBE® RD (hindered amine) and 0.2 wt% IRGANOX® 11 3 5 (obstructed) is in terms of oxidation and rot resistance test - ASTM D 4636 (190 ° C - 24 h) Shows the minimum viscosity and acid value change. 134067.doc -39-
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2008
- 2008-08-21 MX MX2010002154A patent/MX2010002154A/en unknown
- 2008-08-21 KR KR1020107006366A patent/KR20100061813A/en not_active Application Discontinuation
- 2008-08-21 EP EP08828883A patent/EP2181184A1/en not_active Withdrawn
- 2008-08-21 AU AU2008293750A patent/AU2008293750A1/en not_active Abandoned
- 2008-08-21 CN CN200880103980A patent/CN101802149A/en active Pending
- 2008-08-21 CA CA2696367A patent/CA2696367A1/en not_active Abandoned
- 2008-08-21 JP JP2010522015A patent/JP2010537001A/en active Pending
- 2008-08-21 US US12/195,685 patent/US20090054280A1/en not_active Abandoned
- 2008-08-21 BR BRPI0815314A patent/BRPI0815314A2/en not_active IP Right Cessation
- 2008-08-21 WO PCT/US2008/073825 patent/WO2009029474A1/en active Application Filing
- 2008-08-22 TW TW097132311A patent/TW200918661A/en unknown
Also Published As
Publication number | Publication date |
---|---|
JP2010537001A (en) | 2010-12-02 |
MX2010002154A (en) | 2010-03-18 |
CA2696367A1 (en) | 2009-03-05 |
AU2008293750A1 (en) | 2009-03-05 |
EP2181184A1 (en) | 2010-05-05 |
WO2009029474A1 (en) | 2009-03-05 |
CN101802149A (en) | 2010-08-11 |
KR20100061813A (en) | 2010-06-09 |
BRPI0815314A2 (en) | 2017-05-09 |
US20090054280A1 (en) | 2009-02-26 |
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