TW391955B - Process for the preparation of acetals - Google Patents

Process for the preparation of acetals Download PDF

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TW391955B
TW391955B TW87103695A TW87103695A TW391955B TW 391955 B TW391955 B TW 391955B TW 87103695 A TW87103695 A TW 87103695A TW 87103695 A TW87103695 A TW 87103695A TW 391955 B TW391955 B TW 391955B
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Taiwan
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catalyst
heterogeneous
item
scope
reaction
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TW87103695A
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Chinese (zh)
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Juergen Kanand
Rocco Paciello
Michael Roeper
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Basf Ag
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C41/00Preparation of ethers; Preparation of compounds having groups, groups or groups
    • C07C41/48Preparation of compounds having groups
    • C07C41/50Preparation of compounds having groups by reactions producing groups
    • C07C41/54Preparation of compounds having groups by reactions producing groups by addition of compounds to unsaturated carbon-to-carbon bonds

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

A process for the preparation of acetals by reacting allyl ethers with alcohols, wherein an allyl ether is reacted with an alcohol in the liquid phase in the presence of a homogeneous catalyst comprising an organometallic compound of the platinum metals, ruthenium, rhodium, palladium, platinum, osmium and/or iridium or in the presence of a heterogeneous catalyst which contains one or more of the elements chromium, molybdenum, tungsten, rhenium, ruthenium, cobalt, nickel, rhodium, iridium, osmium, palladium and/or platinum of the Periodic Table of Elements, under essentially anhydrous conditions.

Description

五、發明説明( A7 B7 經濟部中央標準局員工消費合作社印製 本發明係關於一種藉由缔丙醚與醇之反應以製備縮醛之 方法。 縮醒係經廣泛地使用於王業界巾,例如#作藉由水解縮 醛製備對應醛的起始材料’或者當作自醛或酮藉由轉化縮 醛反應製備縮醛之試劑。在香水之製備中,縮醛係以芳香劑[請參考 Riechstoffe,Aromen,K〇smetika u (197乃, 71]。 , 縮醛通常係自對應之醛或酮在酸性觸媒下與醇反應而得 [Riechstoffe,Aromen,Kosmetika.27 (1977),71]。在許多情況 中,相關的醛無法從天然來源中得到所欲之數量]或 來自天然原料之醛的價格是如此之高,以致於這些醛無法 廣泛地在工業上供不同目的使用。因此,業界需要一種可 自石化原料中經濟地製得縮链之方法。 US-A 4 788 325和張氏[J. 〇rganomet Chem 燈(1995) 31] 描述了烯丙醚與醇在氫及一氧化碳的存在下、使用八羰基 二話(C〇2(CO)8)作為觸媒所進行之反應,其可直接地用於反 應中作為觸媒’或在反應混合物中以話鹽與一氧化碳在 壓下進行碳基化反應而於原處製得。在反應條件下,八 基二鈷係以氫轉化成四羰基氫化钴(HCo(CO)4),其係實 具催化反應活性之物種。此方法之缺點在於,所用的羰 姑化合物相當容易揮發,而且當產物逐步蒸餾時,會有 分P过縮酸排出,因此,在進一步使用、例如當作芬芳劑 觔’該縮酸必須在昂貴的去钴階段中自包含於其中之羰 钴釋出。因此’該方法並不經濟。 US-A 4 658 069係關於將另外含甲醯基或羧基之烯丙醚 (請先閱讀背面之注意事項再填寫本頁)V. Description of the invention (A7 B7 Printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs This invention is about a method for preparing acetals through the reaction of propyl ether and alcohol. Awakening is widely used in king industry towels, For example, # as a starting material for preparing the corresponding aldehyde by hydrolyzing acetal 'or as a reagent for preparing acetal from aldehyde or ketone by converting the acetal reaction. In the preparation of perfume, acetal is based on a fragrance [Please refer to Riechstoffe, Aromen, Kosmetika u (197, 71). Acetals are usually obtained by reacting corresponding aldehydes or ketones with alcohols under acidic catalysts [Riechstoffe, Aromen, Kosmetika. 27 (1977), 71] In many cases, the relevant aldehydes cannot be obtained in the desired quantity from natural sources] or the prices of aldehydes from natural raw materials are so high that they cannot be widely used industrially for different purposes. Therefore, There is a need in the industry for a method for the economical production of chain shrinkage from petrochemical feedstocks. US-A 4 788 325 and Zhang's [J. Organomet Chem Lamp (1995) 31] describe the presence of allyl ethers and alcohols in hydrogen and carbon monoxide Next, use eight The reaction of carbonyl two words (C0 (CO) 8) as a catalyst can be used directly as a catalyst in the reaction or in a reaction mixture by a salt and carbon monoxide under pressure to perform a carbonation reaction. It is prepared in situ. Under the reaction conditions, octadecylcobalt is converted to cobalt tetracarbonylcobalt hydride (HCo (CO) 4) with hydrogen, which is a species with catalytic activity. The disadvantage of this method is that the used The carbohydrate compounds are relatively easy to volatilize, and when the product is gradually distilled, the P-peracetic acid will be discharged. Therefore, in further use, for example, as a fragrance agent, the acid must be self-contained in the expensive decobalization stage. Among them, cobalt carbonyl is released. Therefore, 'this method is not economical. US-A 4 658 069 is about allyl ether containing methylamido or carboxyl groups (please read the precautions on the back before filling this page)

訂 高 V山 叛 際基部 之基 .轉 4- 本紙張尺度適用中國國家標準(_ CMS ) A4規格(210 X 297公釐) > It— ϋΒ Bn A7 經濟部中央標準局員工消費合作社印製 五、發明説明(2 益f < 方法,其在第一階段中,烯丙醚係在 =二:Λ下與垸醇反應,然後將該反應所得的水去除,在 又裡將第一接段裡所得的烯丙醚縮醛在齒化釕觸 烷醇的辅助下轉化成飽合二縮醛。其他適合的觸媒為 ,、錄、鐵、免和刪化物。因為舶金屬…= 2件下不夠安定而且容易使相關的舶金屬沉積在反應裝 f 土上’導致貴錢金屬損失,此方法在工業規模上並不 經濟。 JP-A 25 i 14/1972係關於一種在氯化衝⑽觸媒之存在下, 將#丙醚與烷醇反應製以備縮醛之方法。在該申請案之實 =中’ 1_甲氧基·2,7_辛二缔係與甲醇反應,在氮氣氛 中,經由RuC13,而得到u-二甲氧基辛_[烯。該方法亦具 有觸媒穩定性很差之缺點。 本發月之目的係k供一種可製備埽丙醚縮醛、然卻沒有 先别技術缺點之經濟方法。 傾發現此目料藉由-種以醇與埽丙鍵反應來製備縮醛 的方法而達成,其中烯丙醚係與醇在液相裡,於包括元 週期表中之第VIA及/或¥111八族元素之有機金屬化合物的, 相觸媒存在下,或在包含一或多個元素週期表中之第via VIIA及/或VIIIA族金屬之多相觸媒的存在下,於基本上 水之條件下反應。 本發明新穎方法中所用之起始材料係具式烯丙醚 ri^^^\〇_r2 J 其中R1是氫或有機基’特別是1到17,較佳1到10個碳原子 請 先 閲 讀 背 ώ 之 注 意 事 項 再 貪 訂 素 均 無 -5- 本纸張尺度適用中國國家標準(CNS ) Α4規格(210 X 297公釐)Set the base of the high mountain base of V. Turn 4- This paper size applies to the Chinese National Standard (_ CMS) A4 size (210 X 297 mm) > It— ϋΒ Bn A7 Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs V. Description of the invention (2) In the first stage, the allyl ether is reacted with methanol at a ratio of two: Λ, and then the water obtained by the reaction is removed, and the first connection The allyl ether acetal obtained in the paragraph is converted into a saturated diacetal with the aid of dentified ruthenium alkanol. Other suitable catalysts are, ruthenium, iron, exemption, and deletion compounds. Because the foreign metal ... = 2 This method is not stable enough and it is easy to cause the relevant foreign metals to be deposited on the soil of the reaction container, which leads to the loss of precious metals. This method is not economical on an industrial scale. JP-A 25 i 14/1972 is a方法 In the presence of a catalyst, a method in which #propyl ether is reacted with an alkanol to prepare an acetal. The actual application of this application = 中 '1_methoxy · 2,7_octane system reacts with methanol, In a nitrogen atmosphere, u-dimethoxyoctyl- [ene is obtained via RuC13. This method also has poor catalyst stability. Disadvantages. The purpose of this article is to provide an economical method for the preparation of acetal ether acetal, but without the disadvantages of other technologies. It is found that this item prepares an acetal by reacting an alcohol with an acetal bond. Method, in which allyl ether and alcohol are in the liquid phase, in the presence of organometallic compounds of Group VIA and / or ¥ 111 group eight elements in the periodic table, in the presence of a catalyst, or In the presence of heterogeneous catalysts of via VIIA and / or group VIIIA metals in the periodic table or elements, the reaction is performed under substantially water conditions. The starting material used in the novel method of the present invention is allyl. Ether ri ^^^ \ 〇_r2 J where R1 is hydrogen or an organic group ', especially 1 to 17, preferably 1 to 10 carbon atoms, please read the precautions of the back first, and then there are no -5- Paper size applies Chinese National Standard (CNS) Α4 specification (210 X 297 mm)

的環狀’直鏈或支鏈煙基。此等烴基的例子是燒基,雙鍵 較佳不與烯丙基共軛的C3_C|7_烯基’芳基,例如苯基或乂 基,c3-c8:環烷基,烷芳基和芳烷基。因其大小而異,這: 烴基可=被1到3個於反應條件下為惰性之取代基、例如酯 基或烷氧基或芳氧基所取代。Rl較佳為直鏈、支鏈或環狀 的烷基。式I之缔丙醚中之R2是具有1到2〇、較佳1到1〇個 碳原子的有機基團。R2較佳為烴基,例如直鏈或支鏈c_ c20-燒基,較佳CrC|〇_燒基,C3_C8_環燒基,c3_c^缔基,車^ 佳q-Cf婦基,或crc8_環烯基(該烯基的雙鍵較佳不存在 於烯丙醚之氧原子的α位置上)’。64。_芳基,例如苯基或 荅基,或C7-Cn-芳烷基或烷芳基。R2較佳經由—級或二級 碳原子鍵結到烯丙醚〗的氧原子。特別較佳的R2是直鏈或支 鏈烷基或烯基。因其大小而定,有機基R2可以載有i或2個 於反應:件下為惰性之取代基、例如Ci_c丨。_烷氧基。因其 大小而異,R2亦可被!或2個羥基取代。然而,Μ較佳係不 載有其它取代基。 ” 二適&在本發明中作為起始材料之.晞丙醚I列舉如下, 但只為說明之目的:缔丙基甲基醚’烯丙基乙基醚,婦丙 基正丙基醚,烯丙基正丁基醚,二烯丙醚,(丁_2_烯基)甲 基醚,(丁 -2-烯基)乙基醚,(丁 _2_埽基)正丙基醚,(丁 _2_ 烯基)正丁基醚,二(丁 _2_烯基)醚,辛'7_二烯基甲基 醚’辛-2,7-二婦基正丁基醚,二(辛'7_二烯基)醚和卜丁 氧基十二-2,7,11-三烯。 在本發明用來根據方程式⑴製造縮醛πι的醇r3〇h 11中Cyclic 'straight or branched chain nicotyl. Examples of such hydrocarbon radicals are alkyl radicals, preferably C3_C | 7_alkenyl'aryl radicals whose double bonds are not conjugated to allyl, such as phenyl or fluorenyl, c3-c8: cycloalkyl, alkylaryl and Aralkyl. Depending on their size, this: The hydrocarbyl group may be substituted with 1 to 3 substituents which are inert under the reaction conditions, such as an ester or alkoxy or aryloxy group. R1 is preferably a linear, branched or cyclic alkyl group. R2 in the allyl ether of formula I is an organic group having 1 to 20, preferably 1 to 10 carbon atoms. R2 is preferably a hydrocarbon group, such as a linear or branched c_c20-alkyl group, preferably CrC | O_alkyl group, C3_C8_cycloalkyl group, c3_c ^ alkenyl group, car ^ q-Cf alkyl group, or crc8_ Cycloalkenyl (the double bond of the alkenyl is preferably not present at the alpha position of the oxygen atom of the allyl ether) '. 64. -Aryl, such as phenyl or fluorenyl, or C7-Cn-aralkyl or alkaryl. R2 is preferably bonded to the oxygen atom of the allyl ether via a carbon atom of the first or second order. Particularly preferred R2 is a linear or branched alkyl or alkenyl group. Depending on its size, the organic group R2 can carry i or 2 in the reaction: the substituent is inert under the component, such as Ci_c 丨. _Alkoxy. Depending on its size, R2 can also be used! Or 2 hydroxy substituted. However, M is preferably free of other substituents. "Dim & is used as the starting material in the present invention. The propyl ether I is listed below, but for the purpose of illustration only: allyl methyl ether 'allyl ethyl ether, propyl propyl n-propyl ether , Allyl n-butyl ether, diallyl ether, (but-2-enyl) methyl ether, (but-2-enyl) ethyl ether, (but_2_fluorenyl) n-propyl ether , (But_2_alkenyl) n-butyl ether, bis (but_2_alkenyl) ether, oct'7_dienyl methyl ether 'oct-2,7-dienyl n-butyl ether, di (Oct'7_dienyl) ether and butoxydodecyl-2,7,11-triene. In the alcohol r3Oh 11 used in the present invention for the production of acetals in accordance with equation VII.

(請先閱讀背面之注意事項再填寫本頁) 1Γ 經濟部中央標隼局員工消費合作杜印製 -6-(Please read the notes on the back before filling out this page) 1Γ Consumption Cooperation by Employees of the Central Bureau of Standards, Ministry of Economic Affairs -6-

A7 B7 五、發明説明(4 OR3A7 B7 V. Description of the invention (4 OR3

(1) III ⑽+ R3〇H觸⑹^(1) III ⑽ + R3〇H contact ^

1 II 其中推測該反應係經由缔醇醚!同分異構化成中間產物…而 發生 取代基R3可以與含於所用之缔丙基醚中之 不同。較佳使用一級或二級醇R3〇H,特別較佳使用一級醇 R3OH。三級醇R3〇h也可以使用,但是因取代基尺2的笨重程 度而足地’位阻現象可能在反應過程發生。因此,較佳係 選擇醇R 0H,因為R2不會造成位阻現象。特別較佳係使用 脂族CrC4_醇當作R3〇h,特別是甲醇、乙醇、正丙醇、異 丁醇和正丁醇。所用的醇R3〇h當然也可以是多元醇,例如 乙二醇,1,2-丙二醇,1,3_丙二醇,1>4_ 丁二醇或込、己二 醇。如果R2包含羥基自由基,則可與雙鍵進行分子内或分 子間之反應’而形成環或丙晞系縮醛,即,此係指存在於 取代基R2中之羥基作為醇r3〇H用之情沉而言。 經濟部中央橾準局員工消費合作衽印製 許多過渡金屬元素的有機金屬化合物,特別是元素週期 表中第VIA和VIIIA族元素’較佳是鉬,鐵,姑,鎳,尤其 是鉑金屬釕,鍺,鈀,鉑,鉞及銥,特別較佳釕,姥,銥 或餓的有機金屬化合物’可於本發明中作為縮醛化烯丙基 随Π ’以得到縮醛III的均相觸媒。為了本發明的應用,有 機金屬化合物應暸解係指過渡金屬與包含配位基,例如 _ ’銻,砷,氮,硫及/或氧的錯合物,而且經由自由的電 -7- 本紙張尺度適用中國國家標準(CNS ) A4g ( 210X297公釐)1 II where it is speculated that the reaction is via associated ether! Isomerization to intermediates ... and the occurrence of the substituent R3 may be different from that contained in the allyl ether used. The primary or secondary alcohol R3OH is preferably used, and the primary alcohol R3OH is particularly preferably used. The tertiary alcohol R3oh can also be used, but due to the bulkiness of the substituent rule 2, steric hindrance may occur during the reaction. Therefore, the alcohol R 0H is preferred because R 2 does not cause steric hindrance. Particularly preferred is the use of an aliphatic CrC4-alcohol as R30h, especially methanol, ethanol, n-propanol, isobutanol and n-butanol. The alcohol R30h used may of course also be a polyhydric alcohol, such as ethylene glycol, 1,2-propylene glycol, 1,3-propanediol, 1 > butanediol or fluorene, hexanediol. If R2 contains a hydroxyl radical, it can be reacted intra- or intermolecularly with a double bond to form a ring or propionyl acetal, that is, the hydroxyl group present in the substituent R2 is used as the alcohol r3OH. In terms of sentiment. Consumption cooperation with employees of the Central Bureau of Standards of the Ministry of Economic Affairs prints many organometallic compounds of transition metal elements, especially Group VIA and VIIIA elements in the Periodic Table of the Elements, preferably molybdenum, iron, nickel, nickel, especially platinum metal ruthenium , Germanium, palladium, platinum, osmium, and iridium, particularly preferably ruthenium, osmium, iridium, or hungry organometallic compounds' can be used as acetalized allyl groups in the present invention to obtain homogeneous contact of acetal III Media. For the application of the present invention, organometallic compounds should be understood to refer to complexes of transition metals and containing ligands such as _'antimony, arsenic, nitrogen, sulfur, and / or oxygen, and via free electricity. Applicable to China National Standard (CNS) A4g (210X297 mm)

經濟部中央標準局員工消費合作社印製 子對與過渡金屬配位共價,舉例Λ 率例而έ像有機胺配位基,有 機騰配位基,整合物配位基,例如乙龜丙酮和二的,像是 二甲基二肪,糠偶醯二肋或笨偶驢二肪,尿素或硫脲,8經 基奎林’單配位基或多配位基’特別是二配位基有基騰和 有機亞磷酸鹽配位基,有機胂和有機脎配位基,和芳族含 氮配位基((-N = C-C=N-)的構造是使其作為錯合劑的原因), 舉例來說2,2Ί咬或i,10_啡,林,以及經由取代作用而自這 些母質衍生之配位基’例如三級吡啶。這些錯合物可以以 中性錯合物存在,或可以帶有電荷並且可以與陰離子形成 鹽。另一方面,這*過渡金屬與例如幾酸、碳酸或氫氨酸 之不包含任一種上述有機配位基的簡單鹽類,係不考慮當 作本發明目的所用之化合物。同樣地,過渡金屬的羧^ 鹽、氰基或羰基錯合物,例如八羰基二鈷(c〇2(c〇)s)或四羰 基氫化钴(HCo(CO)4)也不包含上述的有機配位基。另一方 面,金屬與上述有機配位基的錯合物_其另外包含羧酸鹽, 醇酸鹽,氰化物,碳酸鹽之或以錯合物形式結合之羰基配 位基,或包含羧酸鹽,醇酸鹽,氰化物,碳酸鹽或硫酸鹽 作為過渡金屬之正電有機金屬錯合物的陰離子_係涵蓋有& 金屬化合物的定義範圍内。 所用的配位基可為單配位基或多配位基,例如二配位基 膦配位基。適當的膦配位基為,例如三烷基膦,三芳^ 膦,烷基二芳基膦’芳基二烷基膦,芳基二膦,燒基二騰 和芳基燒基二膦。載有烷基的膦配位基可以包含相同的或 不同的CVC2。-垸基,較佳係crcs_烷基,或環烷基。載有芳 基的膦配位基可以包含相同的或不同的C(5_C12_芳基,特別 -8 - 本紙張尺度適用中國國家標準(CNS ) A4規格(2丨0X297公釐) (請先閲讀背面之注意事項再填寫本I)Printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs on covalent coordination with transition metal coordination. For example, Λ is similar to organic amine ligands, organic free ligands, and complex ligands, such as acetone and acetone. Two, such as dimethyl difat, bran, or rib, diuretic, urea or thiourea, 8 via Kikulin 'single or multi-ligand', especially di-ligand Gite and organic phosphite ligands, organic amidines and organic amidine ligands, and aromatic nitrogen-containing ligands ((-N = CC = N-) structure is the reason for making it a complexing agent) For example, 2,2 bite or i, 10-morphine, Lin, and ligands such as tertiary pyridine derived from these parent materials through substitution. These complexes can exist as neutral complexes, or they can be charged and can form salts with anions. On the other hand, these simple transition metals and simple salts of, for example, a few acids, carbonic acid, or hydrogenic acid, which do not contain any of the above-mentioned organic ligands, are not considered as compounds used for the purpose of the present invention. Similarly, carboxylates, cyano, or carbonyl complexes of transition metals, such as cobalt dioctacarbonyl (c0 (c0) s) or cobalt tetrahydrocarbon hydride (HCo (CO) 4), do not include the above Organic ligands. On the other hand, a complex of a metal with the above-mentioned organic ligand_ which additionally contains a carboxylic acid salt, an alcoholate, a cyanide, a carbonate or a carbonyl ligand bound in the form of a complex, or contains a carboxylic acid The anions of salts, alcoholates, cyanides, carbonates or sulfates as transition metal positively charged organometallic complexes are included within the definition of & metal compounds. The ligand used may be a single ligand or a multi-ligand, such as a di-ligand phosphine ligand. Suitable phosphine ligands are, for example, trialkylphosphine, triarylphosphine, alkyldiarylphosphine ' aryldialkylphosphine, aryldiphosphine, alkyldipentyl, and aryldiphosphine. The alkyl-supported phosphine ligand may contain the same or different CVC2. -Fluorenyl, preferably crcs_alkyl, or cycloalkyl. Phosphine ligands carrying aryl groups may contain the same or different C (5_C12_aryl groups, especially -8-This paper size applies to China National Standard (CNS) A4 specifications (2 丨 0X297 mm) (Please read first (Notes on the back please fill out this I)

經濟部中央標準局員工消費合作社印製 Α7 Β7 五、發明説明(6 ) 疋苯基或奈基,和二苯基。可以用於錯化第VIA族或VIIIA 狹兀素的其他膦配位基係為載有雜環脂族基,例如吡咯 啶,咪唑啉,六氫吡啶,嗎啉,噁唑啶,六氫吡啩或三唑 淀基’或雜芳基’例如吡咯,咪唑,噁唑,啕哚,吡啶, 喳啉,嘧啶,吡唑,吡畊,或噠嗪基,與其它烷基或芳基 的膦配位基。配位基的烷基或芳基可以為未經取代的或可 以載有於反應條件下為惰性之取代基,例如C「C4_@氧基或 二-crC4_烷基胺基,crc6_烷基,硝基,氰基或磺酸鹽。適 當之碩酸鹽化膦配位基的例子為,特別是三苯基膦三磺酸 鹽(TPPTS)和三苯基膦單磺酸鹽(TppMS)(Angew.Printed by the Consumer Cooperatives of the Central Bureau of Standards of the Ministry of Economic Affairs A7 B7 V. Description of the Invention (6) Phenyl or naphthyl, and diphenyl. Other phosphine ligands that can be used to misinterpret VIA or VIIIA catenins are heterocyclic aliphatic groups such as pyrrolidine, imidazoline, hexahydropyridine, morpholine, oxazoline, hexahydropyridine Hydrazone or triazolyl 'or heteroaryl' such as pyrrole, imidazole, oxazole, pyridine, pyridine, perylene, pyrimidine, pyrazole, pyrenyl, or pyridazinyl, and other alkyl or aryl phosphines Ligand. The alkyl or aryl group of the ligand may be unsubstituted or may carry a substituent that is inert under the reaction conditions, such as C, C4_ @ oxy or di-crC4_alkylamino, crc6_alkyl , Nitro, cyano or sulfonate. Examples of suitable phosphonate ligands are, in particular, triphenylphosphine trisulfonate (TPPTS) and triphenylphosphine monosulfonate (TppMS) (Angew.

Chem. 105 (1993), 1588)。 原則上’此等於本發明中用以錯化第VIA族或νΠΙΑ族元 素之配位基的適用性並沒有限制。然而,為了成本因素, 較佳係使用可利用簡單方式製得之配位基。 此等配位基之某些僅以舉例說明之例子如下:三甲基 膦’二乙基膦,三丙基膦,三異丙基膦,三丁基膦,三辛 基膦’三癸基膦,三環戊基膦,三環己基膦,三苯基膦, 二甲苯基膦,環己基二苯基膦,四苯基二膦,丨,2_雙(二苯 基膦基)乙烷,四甲基二膦基甲烷,四乙基二膦基甲烷, 1,3-雙(二苯基膦基)丙烷,丨,4_雙(二苯基膦基)丁烷,四_ 二級丁基二膦基甲烷,L2-雙(二甲基膦基)乙烷,152_雙 (二乙基膦基)乙烷,1;2_雙(二丙基膦基)乙烷,丨,2_雙(二 異丙基膦基)乙烷’ 1,2-雙(二丁基膦基)乙烷,;ι,2_雙(二-二級丁基膦基)乙烷,1,1_雙(二環己基膦基)甲烷,〗,2_雙 (二環己基膦基)乙烷’ 1,4_雙(二環己基膦基)丁烷和ΕΡ-Α 9- 本紙張尺度適用中國國家標準(CNS ) Α4規格(210χ297公瘦) ..----------- (請先閲讀背面之注意事項再填寫本頁) 訂 經濟部中央標準局員工消費合作社印製 A7 B7 _ 五、發明説明(7 ) 279 018,EP-A 311 619,W〇 90/06810和 EP-A 71 281所述的 雙膦配位基。除三苯基騰(縮窝為PPh3)之外較佳的膦配位 基,係經由cvc4-伸烷基键結和具有下列通式之二配位基膦 配位基Chem. 105 (1993), 1588). In principle, this is equivalent to the applicability of the ligands used to misinterpret the group VIA or νΠΙΑ element in the present invention. However, for cost reasons, it is preferable to use a ligand that can be prepared in a simple manner. Some of these ligands are by way of example only: trimethylphosphine'diethylphosphine, tripropylphosphine, triisopropylphosphine, tributylphosphine, trioctylphosphine'tridecyl Phosphine, tricyclopentylphosphine, tricyclohexylphosphine, triphenylphosphine, xylylphosphine, cyclohexyldiphenylphosphine, tetraphenyldiphosphine, 2-bis (diphenylphosphino) ethane , Tetramethyldiphosphinomethane, tetraethyldiphosphinomethane, 1,3-bis (diphenylphosphino) propane, 4-bis (diphenylphosphino) butane, tetra-secondary Butyl diphosphinomethane, L2-bis (dimethylphosphino) ethane, 152_bis (diethylphosphino) ethane, 1; 2-bis (dipropylphosphino) ethane, 丨, 2_bis (diisopropylphosphino) ethane '1,2-bis (dibutylphosphino) ethane, 1,2, bis (di-secondary butylphosphino) ethane, 1, 1_bis (dicyclohexylphosphino) methane, 2_bis (dicyclohexylphosphino) ethane, 1,4-bis (dicyclohexylphosphino) butane and EP-Α 9- paper size Applicable to China National Standard (CNS) Α4 specification (210x297 male thin) ..----------- (Please read the notes on the back first (Fill in this page again) Order A7 B7 printed by the Consumer Cooperatives of the Central Bureau of Standards of the Ministry of Economic Affairs _ V. Description of the invention (7) 279 018, EP-A 311 619, W90 / 06810 and EP-A 71 281 Phosphine ligand. Preferred phosphine ligands other than triphenylpentene (condensation is PPh3) are via a cvc4-alkylene bond and a phosphine ligand having the following two formulae:

A\ /A P- (CH2) η - Ρ / \A \ / A P- (CH2) η-Ρ / \

A A 其中η是整數1到4,而基團Α是相同的或不同的q-C^-烷基 或Cr或C6-環烷基’其一些典型的例子係已在上述中提及。 除了以上述專利申請案所述之方法製備以外,烷基-或芳 基膦配位基可以利用已知之方法製備,例如Houben-Weyl,A A where η is an integer of 1 to 4, and the groups A are the same or different q-C ^ -alkyl or Cr or C6-cycloalkyl '. Some typical examples have been mentioned above. In addition to the methods described in the aforementioned patent applications, alkyl- or arylphosphine ligands can be prepared using known methods, such as Houben-Weyl,

Methoden der Organischen Che.mie,第 XII/1冊,第 4 版第 17-65 頁和第 18.2-186 頁’ Thieme,Stuttgart, 1963,和第 E 1冊, 第 4 版第 106-199 頁,Thieme, Stuttgart, 1982。 適當之磷酸鹽配位基為,例如三烷基磷酸鹽,烷基二芳 基磷酸鹽’三芳基磷酸鹽,烷基.二亞磷酸鹽,芳基二亞磷 酸鹽和坑基芳基二亞磷酸鹽。載有燒基的磷酸鹽配位基可 以包含相同的或不同的cvc!。-烷基,較佳係crc6-烷基,或 環坑基。載有芳基·的稱酸鹽配位基可以包含相同的或不同 的cvCf芳基’特別是苯基或茶基,和二苯基或二苯基。 可以用來做錯化過渡金屬的其他磷酸鹽配位基是載有雜環 脂族基’例如吡咯啶,咪唑啶,六氫吡啶,嗎啉,嗔也 啶’六氫吡畊或三啶基’或雜芳基,例如吡咯,咪唑,噪 吐,'^丨p木’ p比淀,p奎p林,p密咬,ρ比ρ坐,?比°井,或'達嗅基, 與其它烷基或芳基的的配位基。磷酸鹽配位基的烷基或芳 -10- 本纸張尺度適用中6國家標準(CNS )八4麟(210X297公楚) ':-- ~丨 --------聲! (請先閲讀背面之注意事項再填寫本頁) 訂 Ά. fgE§ 經濟部中央標準局員工消費合作社印製 A7 B7 五、發明説明(8 ) 基可為未取代的或可為載有於反應條件下為惰性之取代 基’例如crcv烷氧基,二_crc4-垸基胺基,Crc6_烷基,羥 基’確基’氰基或橫酸鹽。經橫酸鹽取代的磷酸鹽配位基 及其錯合物大體上是可溶於水的。適合之磷酸鹽配位基 為’例如二甲基鱗酸.鹽,二乙基鱗酸鹽,三丙基鱗酸鹽, 三異丙基磷酸鹽,三丁基磷酸鹽,三環戊基磷酸鹽,三環 己基磷酸鹽’三苯基磷酸鹽和EP-A 472 071,EP-A 213 639,EP -A 214 622,DE-A 2 733 796,EP-A 2261,EP-A 2821,EP-A 9115,EP-A 155 508,EP-A 353 770,US-A 4 318 845,US-A 4 204 997和US_A 4 362 830所述的單-及雙亞磷酸 鹽配位基。 除膦或磷酸鹽配位基以外,經烷基-或芳基-取代或融化 之2,2’-二吡啶或或1,1〇_啡啉衍生物-包含造成2,2,_二吡啶或 1,10-啡啉配位基有配位基形成性質的(_N=c_C=N-)基,例如 2,2’-二喳啉,4,7-二苯基-ΐ,ι〇-啡啉,2,9-二甲基-4,7-二苯 基-1,10-啡p林,4,5-重氮芴’二吡咯[3,2-a : 2,,3,-c]吩嗪, 2,2’,6 1,2 ” -三聯吡啶等的2,2,-二吡啶或1,10-啡啉配位基, 也可以用於本發明之方法中。這些配位基其中一些可為市 售品,例如2,2’-二吡啶或1,10-啡啉,以及其他利用Synthesis 1 (1976)或 Aust_ J. Chem_ 23 (1970),1023 所述的方法製備。 可用於本發明之VIA族或VIIIA族元素之此等錯合物可於 原處在混合物中製得,或者預先形成,然後再加入反應混 合物中。就這些錯合物地就製造的情況而言,大體上化合 物第VIA族或VIIIA族元素的化合物,例如其鹵化物,較佳 為其氯化物,溴化物或碘化物,硝酸鹽,氰化物或硫酸鹽 -11 - 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) (請先閑讀背面之注意事項再填寫本頁〕Methoden der Organischen Che.mie, Book XII / 1, 4th edition, pages 17-65 and 18.2-186 'Thieme, Stuttgart, 1963, and Book E 1, 4th edition, pages 106-199, Thieme , Stuttgart, 1982. Suitable phosphate ligands are, for example, trialkyl phosphates, alkyl diaryl phosphates' triaryl phosphates, alkyl. Diphosphites, aryl diphosphites, and pit aryl diimides Phosphate. Carbyl-loaded phosphate ligands may contain the same or different cvc !. -Alkyl, preferably crc6-alkyl, or cyclopityl. The aryl group-bearing acid salt ligand may contain the same or different cvCf aryl's, especially phenyl or theophyl, and diphenyl or diphenyl. Other phosphate ligands that can be used to make the transition metal are heterocyclic aliphatic groups such as pyrrolidine, imidazolidine, hexahydropyridine, morpholine, pyrimidine, hexahydropyridine or tripyridyl 'Or heteroaryl, such as pyrrole, imidazole, vomiting,' ^ 丨 p 木 'pibidian, pkui plin, p dense bite, ρ than ρ sitting ,? Bi wells, or 'daphnosyl,' are ligands for other alkyl or aryl groups. Alkyl or aryl of phosphate ligands -10- This paper size applies to 6 National Standards (CNS) 8 4 Lin (210X297) Chu ':-~ 丨 -------- Sound! (Please read the precautions on the back before filling out this page) Order. FgE§ Printed by the Consumer Standards Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs A7 B7 V. Description of the invention (8) The base may be unsubstituted or may be contained in the reaction Substituents that are inert under conditions such as crcv alkoxy, di-crc4-fluorenylamino, Crc6-alkyl, hydroxy, acyl, cyano, or transacid. Phosphonate substituted phosphate complexes and their complexes are generally water-soluble. Suitable phosphate ligands are 'e.g. dimethylscale acid. Salt, diethylscale acid salt, tripropylscale acid salt, triisopropyl phosphate, tributyl phosphate, tricyclopentyl phosphate Salt, tricyclohexyl phosphate 'triphenyl phosphate and EP-A 472 071, EP-A 213 639, EP-A 214 622, DE-A 2 733 796, EP-A 2261, EP-A 2821, EP -A 9115, EP-A 155 508, EP-A 353 770, US-A 4 318 845, US-A 4 204 997 and US_A 4 362 830 as described in the mono- and bisphosphite ligands. In addition to phosphine or phosphate ligands, alkyl- or aryl-substituted or fused 2,2'-dipyridines or or 1,10-morpholine derivatives-containing 2,2, -dipyridines Or 1,10-morpholine ligands have (_N = c_C = N-) groups that have ligand-forming properties, such as 2,2'-dioxoline, 4,7-diphenyl-pyrene, ι〇- Phenanthroline, 2,9-dimethyl-4,7-diphenyl-1,10-morphine, 4,5-diazopyridine's dipyrrole [3,2-a: 2,3,- c] Phenazine, 2,2 ', 6 1,2 "-terpyridine, 2,2, -dipyridine or 1,10-morpholine ligands can also be used in the method of the present invention. These compounds Some of the bases can be commercially available, such as 2,2'-dipyridine or 1,10-morpholine, and others can be prepared by the method described in Synthesis 1 (1976) or Aust_ J. Chem_ 23 (1970), 1023 These complexes of Group VIA or Group VIIIA elements which can be used in the present invention can be prepared in the mixture in situ, or they can be formed beforehand and then added to the reaction mixture. As far as the complexes are concerned, the manufacturing conditions In other words, compounds of Group VIA or VIIIA elements, such as their halides, are preferably chlorinated. , Bromide or iodide, nitrate, cyanide or sulfate -11-- Precautions This paper scales applicable Chinese National Standard (CNS) A4 size (210X297 mm) (Please read the back of the idle and then fill this page]

經濟部中央標準局員工消費合作社印製 A7 _B7 _ 五、發明説明(9 ) 或’特別較佳是這些金屬的錯合物,例如乙醯基醋酮酸 鹽’幾酸鹽,幾基錯合物’或錦τ煙錯合物,例如乙婦或丁 二烯錯合物,係一起和相關的配位基進料至反應混合物 中,因此反應錯合物裡形成可用於本發明之錯合物。一般 而言,相關配位基在此的莫耳比例為基於第VIA族或VIIIA 族元素之1到200,較佳係1到5 0,特佳係i到! 〇。 在上述過渡金屬的有機金屬化合物之中,包括含磷配位 基,特別是膦配位基之鉑金屬羧基錯合物,例如 HRh(PPh3)3(CO) ’ IrCl(CO)(PPh3)3 , [Ir(環辛二烯 基)pph3)2]PF6 ’ HRuCl(PPh3)3(CO),HRu(CO)(CH3COO) (PPh3)2, H2Ru(CO)(PPh3)3,HRuCl(CO)(己基二苯基膦)3,ruh2(pph3)4, RuCl2(CO)2(PPh3)3 或 RuH(CO)(C9H19CO〇)(pph3)2 ,其中Printed by A7 _B7 _ of the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs. 5. Description of the invention (9) or 'especially preferred is a complex of these metals, such as acetamacetate', and several bases. Substances or bromide smoke complexes, such as ethene or butadiene complexes, are fed into the reaction mixture together with related ligands, so the complexes formed in the reaction complexes can be used in the present invention Thing. Generally speaking, the molar ratio of the relevant ligands here is based on 1 to 200 of Group VIA or Group VIIIA elements, preferably 1 to 50, particularly preferably i to! 〇. Among the above-mentioned organometallic compounds of transition metals, there are platinum metal carboxyl complexes containing phosphorus-containing ligands, especially phosphine ligands, such as HRh (PPh3) 3 (CO) 'IrCl (CO) (PPh3) 3 , [Ir (cyclooctadienyl) pph3) 2] PF6 'HRuCl (PPh3) 3 (CO), HRu (CO) (CH3COO) (PPh3) 2, H2Ru (CO) (PPh3) 3, HRuCl (CO) (Hexyldiphenylphosphine) 3, ruh2 (pph3) 4, RuCl2 (CO) 2 (PPh3) 3 or RuH (CO) (C9H19CO〇) (pph3) 2, where

CgH^COO是癸酸陰離子’尤其較佳作為本發明方法裡的均 相觸媒。在這些均相觸媒之中,依次以無鹵素錯合物為較 佳’例如包含0-H-酸性’有機化合物之共軛鹼,當做配位 基的錯合物’ 0-H-酸性’有機化合物係指在水溶液中為酸 性的化合物’例如單羧酸,單磺酸或非螫合性酚類。較佳 源自單叛酸的Cj-C2。-碳酸陰離子,例如乙酸鹽,丙酸趟, 丁酸鹽,異丁酸鹽,戊酸鹽,特戊酸鹽,己酸鹽,i酸 S ’辛奴鹽’ 2-乙基己鹽’ 2-丙基戊酸鹽,癸酸鹽,月 桂酸鹽’肉豆蔻酸鹽’棕櫚鹽,硬脂酸鹽,油酸鹽,苯甲 ,酸鹽,烷基苯甲酸鹽,莕酸鹽和烷基萘酸鹽陰離子,或非 螫合性酚鹽陰離子或磺酸鹽陰離子,可以有利地作為1 ^ 配位基。 Μ 可以有利地作為有機過渡金屬化合物中的配位基所使用 -12- 本紙乐尺度適用中國國家標準(CNS ) Α4規格(210X297公楚;) (I先閲讀背面之注意事項再填寫本頁) 4 訂 A7 B7 經濟部中央標準局員工消費合作社印製 五、發明説明(1〇 ) 之酚鹽,係例如在芳核上以於反應條件下為惰性之取代基 取代的酚鹽,和莕酸鹽陰離子及酚鹽和苯酸鹽陰離子,= ^經烷基取代的,較佳係經CrCiG_烷基取代的酚鹽或 萘酸鹽,像是甲基酚鹽,壬基酚鹽,2,6_二_三級丁基酚鹽 或2,6-二-三級丁基-4-甲基酚鹽陰離子。 可以有利地供本發明目的使用之磺酸鹽配位基係,舉例 來說,烷績酸鹽,例如甲烷磺酸鹽,辛烷磺酸鹽,十二燒 磺酸鹽,十八烷磺酸鹽或三氟甲烷磺酸鹽陰離子,或芳基 磺酸鹽,例如甲苯磺酸鹽陰離子。 包含源自酸性有機化合物之配位基及可用於本發明的均 相觸媒的製備係以上述釕錯合物作為其它過渡金屬之類似 錯合物的典型例子簡短地概略說明如下: 這些包含羧酸鹽配位基的錯合物可以例如從可獲得的 RuH2 (PPh3)3(CO)作為起始物根據uttley等人於’’無機合成” 乙書中第XVII冊(1977)第125頁所述,藉由與對應的叛酸反 應,類似 Robinson 等人 J_ Chem. Soc_,Dalton Trans. (1973) 1912, Frediani 等人,同前,(1990)第 165 頁,同前(1990)第 1705 頁,同前(1990)第 3663 頁,和 Frediani 等人,j Organomet Chem· 454, C17-C19 (1993)所提的方法而製得。 包含酚鹽配位基的對應錯合物可以藉由相似 H2Ru(CO)(PPh3)3的方式與相關的酚反應而獲得。包含續酸 鹽配位基的錯合物可利用例如US-A 4 892 955所述的方法獲 得。含有鹵素之均相觸媒可以利用例如Uttley等人無機合成 第XV冊(1974),45所述的方法,由RuC13與曱酸反應而得。 上述觸媒可以同樣地加入反應批次或-特別是應用在包含 -13 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) (請先聞讀背面之注意事項再填寫本頁} 訂 東. A7 B7 經濟部中央標準局員工消費合作衽印製 五、發明説明(Ή ) 羧酸鹽或酚鹽配位基之均相觸媒_在反應混合物中於原處藉 由RuH2 (PPh3)3(CO)與相關的酚反應而製得。 此外’由於源自無氫化物基或羰基配位基的錯合物,因 而包含氫化物基及羰基配位基的錯合物可以在反應混合物 中於原處藉由在分子態氫及/或一氧化碳強迫混合而產生。 此等以羧酸鹽,磺酸鹽或酚鹽配位基改質並且另外地包 含括含磷配位基,特別是膦或磷酸鹽配位基,較佳膦配位 基’必要時有羰基配位基的有機過渡金屬化合物,特別是 有機銜化合物,係以其高活性及選擇性以及以高安定性, 因而可長期操作的特性,為本發明方法選作作縮醛化催化 用的均相觸媒。 這些均相觸媒的有利性質可以另外地藉由在大於形成相 關過渡金屬羧酸鹽或酚鹽錯合物所需之化學計量更大的數 量的相關酸性化合物存在下,以致於自由態之相關酸性化 合物與作為均相觸媒之有機過渡金屬化合物呈平衡的方式 進行縮酸化作用而改良。為了該目的,所用的酸性化合物 係有利地相同於鍵結到有機過渡金屬化合物裡之過渡金屬 的化合物,但是其他的酸性有機化合物同樣地以此方式加 入。在如此的程序裡,酸性有機化合物通常的用量為基於 作為均相觸媒之有機過渡金屬化合物1 : 1莫耳比。 雖然縮趁化反應不一定要把氫加入反應混合物,但是加 入少量的氫,如果必要時,與少量一氧化碳—起加入,當 使用含奴基之均相觸媒時,可以使這些均相觸媒的使用時 間壽命延長。於實務中,合成氣體可以供該目的使用。於 此需注意的是,因所用的反應溫度和所用的部分壓力而 -14- 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) -*i»r» —Mi n n n HB m rn 4—=ttRνϋ tK « .m c請先聞讀背面之注意事項再填寫本頁} 訂 I - A 7 _;_______ B7_. 五、發明説明(12 ) 走,氳及/或一氧化碳係與在反應混合物裡以均相觸媒存在 I過渡金屬錯合物反應,由於其氫化物基及羰基配基數不 同的多種催化活性有機金屬過渡金屬錯合物之故,可能在 這些條件下於反應混合物中彼此達成平衡。 為了要改良均相觸媒特別是包括含磷之配位基的均相觸 媒的活性、選擇性和穩定性,膦或磷酸鹽通常加入2到1〇〇 倍’較佳係2到2 0倍,特別較佳2到丨〇倍過渡金屬之膦或 磷酸鹽錯合物莫耳數的數量。如果作為均相觸媒之過渡金 屬錯合物於原處在反應混合物中製得,則有利地將基於相 關過渡金屬之對應極過量的膦或磷酸鹽配位基加入。 均勻溶解於反應介質裡的過渡金屬觸媒通常的用量為基 於進料土反應器之烯丙酸_ I 〇.〇〇 1到1,較佳〇·〇 1到1莫耳 %。對於熟習本項技藝者而言顯而易知,均相觸媒的加入 里係視每個情況之均相觸媒的觸媒活性而定。因所用之均 相觸媒的類型而定’較大或較小量的觸媒因此也可以有利 地加入反應混合物。每個情況裡所用之均相觸媒的最適宜 數量係有利地以初步實驗決定。 經濟部中央標隼局員工消費合作社印製 (請先閲讀背面之注意事項再填寫本頁) 輔以上述均相觸媒而進行的縮醛化反應可以以批次式, 例如在攪拌壺裡,或連續式,例如在環狀反應器或攪拌壺 階式路發器裡進行,其溫度大體上為2 〇到2〇〇t,較佳6 〇 到180 c ’特別8 0到160°C,而壓力大體上為1到100 ,較佳i 到6 0巴。縮醛化反應可以在所加入之溶劑,例如脂族或芳 族烴類,像是甲苯,苯或環己烷,醚,例如二丁基醚’四 氫呋喃或二氧六圜,或液體低分子量的聚烷二醇類,鹵化 的脂族或芳族烴類,例如氯仿,二氯甲烷,氯苯或二氯 -15- ^:尺⑯用?ΐ國家標準(CNS) A7 A7 經濟部中夬標準局員工消費合作社印製 五、發明説明(13 ) 笨,亞颯或颯,例如二甲亞砜或五環磺氧烷的存在 下進行。 本發明的縮醛化反應係在本質上為無水的條件下,即在 缺乏對技術有效之數量的水之下進行,因為水的存在對 駿化反應的結果有不利的影響。顯然可知地,痕量水 在對於產率沒有可測量的影響,而 本效應所容忍。纟^ ^可為本發明方法的成 、不用在這些傳統的溶劑裡進行,以醚1得到祕m的同 刀丹構化和縮醛化反應也可以在膦熔融液裡進行。該程 可以有利地在含膦均相觸媒的情況裡。大體上,實: =劑的膦原則上可以自由地選擇,但是溶融液裡㈣的 择較隹為當做均相觸媒之過渡金屬錯合物裡發揮配位基 用的騰。 醇R3〇Hn的加入量的範圍很廣。形成縮醛ιπ所 也可以超過。大體上,醇R3〇Hi1係請為基 於所用u希丙醚w1:im〇0:1,較佳1:1到1〇: 1 . 1到5 . 1的莫耳比加入。以婦丙醚丨 醇R3〇:H II通常沒有對反岸壯果达ώ 4 的CgH ^ COO is a capric acid anion 'and is particularly preferred as a homogeneous catalyst in the method of the present invention. Among these homogeneous catalysts, halogen-free complexes are preferred in sequence, for example, conjugate bases containing 0-H-acidic organic compounds, and complexes '0-H-acidic' as ligands. An organic compound refers to a compound that is acidic in an aqueous solution, such as a monocarboxylic acid, a monosulfonic acid, or a non-binding phenol. Cj-C2 which is derived from mono-acid acid is preferred. -Carbonic acid anions, such as acetate, propionate, butyrate, isobutyrate, valerate, pivalate, hexanoate, sulphonic acid 'Sinu salt' 2-ethylhexyl salt '2 -Propylvalerate, caprate, laurate 'myristic acid' palm salt, stearates, oleates, benzoates, acid salts, alkyl benzoates, phosphonates and alkanes A naphthonate anion, or a non-coupled phenate or sulfonate anion, can be advantageously used as a 1 ^ ligand. Μ can be advantageously used as a ligand in organic transition metal compounds. -12- This paper scale is applicable to China National Standard (CNS) A4 specifications (210X297); (I read the precautions on the back before filling this page) 4 Order A7 B7 Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs 5. The phenate of invention description (1) is, for example, a phenate substituted on an aromatic nucleus with a substituent that is inert under the reaction conditions, and osmic acid Salt anion and phenate and benzoate anion, = ^ alkyl substituted, preferably CrCiG_ alkyl substituted phenate or naphthate, such as methyl phenate, nonyl phenate, 2, 6-di-tertiary butyl phenate or 2,6-di-tertiary butyl-4-methyl phenate anion. Sulfonate ligand systems which can be advantageously used for the purpose of the present invention, for example, alkanoates such as methane sulfonate, octane sulfonate, dodecyl sulfonate, octadecanesulfonic acid Salt or trifluoromethanesulfonate anion, or arylsulfonate, such as tosylate anion. The preparation of the homogeneous catalyst containing the ligand derived from the acidic organic compound and the homogeneous catalyst which can be used in the present invention is a typical example of the above-mentioned ruthenium complex as a similar complex of other transition metals. These are briefly described as follows: The complexes of the acid salt ligands can be obtained, for example, from available RuH2 (PPh3) 3 (CO) as starting material according to Uttley et al. In "Inorganic Synthesis", Book XVII (1977), page 125 It is similar to Robinson et al. J_Chem. Soc_, Dalton Trans. (1973) 1912, Frediani et al., By reacting with the corresponding acid reaction, ibid. (1990) p. 165, ibid. (1990) p. 1705 , Ibid. (1990), p. 3663, and the method proposed by Frediani et al., J Organomet Chem. 454, C17-C19 (1993). Corresponding complexes containing phenate ligands can be made similarly H2Ru (CO) (PPh3) 3 can be obtained by reacting with related phenols. The complexes containing a continuous acid salt ligand can be obtained by the method described in US-A 4 892 955, for example. For example, the method described in Uttley et al. Inorganic Synthesis Book XV (1974), 45 It is obtained by the reaction between RuC13 and osmic acid. The above catalysts can be added to the same reaction batch or-especially if it contains -13 paper sizes that are applicable to the Chinese National Standard (CNS) A4 (210X297 mm) (please listen first) Read the notes on the back and fill in this page again} Ding Dong. A7 B7 Consumption Cooperation with Employees of the Central Standards Bureau of the Ministry of Economic Affairs 衽 Printing 5. Description of Invention (Ή) Homogeneous catalysts of carboxylate or phenate ligands_ 在 反应The mixture is prepared in situ by the reaction of RuH2 (PPh3) 3 (CO) with the relevant phenol. In addition, 'Hydride and carbonyl groups are included because they are derived from complexes without hydride or carbonyl ligands. Ligand complexes can be generated in situ in the reaction mixture by forced mixing in molecular hydrogen and / or carbon monoxide. These are modified with carboxylate, sulfonate or phenate ligands and additionally The organic transition metal compounds containing phosphorus-containing ligands, especially phosphine or phosphate ligands, and preferably carbonyl ligands, if necessary, are particularly preferred because of their high activity. And selectivity and high stability, so The characteristics of long-term operation are the homogeneous catalysts selected by the method of the present invention as acetalization catalysts. The advantageous properties of these homogeneous catalysts can additionally be formed by the complexation of the transition metal carboxylate or phenate in the relevant transition metal. In the presence of a greater amount of the relevant acidic compound in stoichiometry, the acidification is improved in such a way that the related acidic compound in the free state is balanced with the organic transition metal compound as a homogeneous catalyst. For this purpose, the acidic compound used is advantageously the same as the transition metal compound bonded to the organic transition metal compound, but other acidic organic compounds are added in the same manner. In such procedures, acid organic compounds are generally used in an amount of 1: 1 molar ratio based on the organic transition metal compound as a homogeneous catalyst. Although it is not necessary to add hydrogen to the reaction mixture, it is necessary to add a small amount of hydrogen, if necessary, with a small amount of carbon monoxide. When a homogeneous catalyst containing a slave group is used, these homogeneous catalysts can be made. Life time is extended. In practice, syngas can be used for this purpose. It should be noted here that due to the reaction temperature used and the partial pressure used, -14- This paper size applies to the Chinese National Standard (CNS) A4 specification (210X297 mm)-* i »r» —Mi nnn HB m rn 4— = ttRνϋ tK «.mc Please read the notes on the back before filling out this page} Order I-A 7 _; _______ B7_. V. Description of the invention (12) Go, 氲 and / or carbon monoxide and the reaction mixture In the presence of a homogeneous catalyst, a transition metal complex reaction exists. Due to its multiple catalytically active organometallic transition metal complexes with different numbers of hydride groups and carbonyl ligands, it may be possible to reach each other in the reaction mixture under these conditions. balance. In order to improve the activity, selectivity and stability of homogeneous catalysts, especially homogeneous catalysts including phosphorus-containing ligands, phosphine or phosphate is usually added 2 to 100 times, preferably 2 to 20 Times, particularly preferably 2 to 10 times the molar number of phosphine or phosphate complexes of transition metals. If the transition metal complex as a homogeneous catalyst is prepared in situ in the reaction mixture, it is advantageous to add a correspondingly excessive excess of phosphine or phosphate ligands based on the relevant transition metal. The transition metal catalyst uniformly dissolved in the reaction medium is usually used in an amount of 1 to 1, preferably 1 to 1 mole% based on the allyl acid_I 0.001 in the feed soil reactor. It is obvious to those skilled in this art that the addition of homogeneous catalyst depends on the catalytic activity of the homogeneous catalyst in each case. Depending on the type of homogeneous catalyst used, a larger or smaller amount of catalyst can therefore also be advantageously added to the reaction mixture. The optimum amount of homogeneous catalyst used in each case is advantageously determined by preliminary experiments. Printed by the Consumers' Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs (please read the precautions on the back before filling this page). The acetalization reaction with the above-mentioned homogeneous catalyst can be performed in batches, for example, in a mixing tank, Or continuous, for example, in a ring reactor or a stirred tank stepped hair dryer, the temperature is generally 20 to 200 t, preferably 60 to 180 c 'particularly 80 to 160 ° C, The pressure is generally 1 to 100, preferably i to 60 bar. The acetalization reaction can be carried out in a solvent such as an aliphatic or aromatic hydrocarbon such as toluene, benzene or cyclohexane, an ether such as dibutyl ether 'tetrahydrofuran or dioxane, or a liquid low molecular weight Polyalkanediols, halogenated aliphatic or aromatic hydrocarbons, such as chloroform, dichloromethane, chlorobenzene or dichloro-15- ^: What is used for? ΐNational Standards (CNS) A7 A7 Printed by the Consumer Cooperatives of the 夬 Standards Bureau of the Ministry of Economic Affairs 5. Description of the invention (13) Stupid, thallium or thorium, such as dimethyl sulfoxide or pentasulfoxane. The acetalization reaction of the present invention is carried out under essentially anhydrous conditions, i.e., in the absence of a technically effective amount of water, because the presence of water adversely affects the results of the chemical reaction. Obviously, trace water has no measurable effect on yield, and this effect is tolerated. The method of the present invention can be performed without using these conventional solvents. The isodanization and acetalization reactions in which ether 1 is used to obtain m can also be performed in a phosphine melt. This process can be advantageous in the case of phosphine-containing homogeneous catalysts. Generally speaking, in principle, the phosphine of the agent can be freely selected in principle, but the choice of tritium in the solution is more important as a ligand for the transition metal complex used as a homogeneous catalyst. The range of the amount of alcohol R3OHn added is wide. The acetal formation can also be exceeded. Generally, the alcohol R30Hi1 is added based on the molar ratio of u-propyl ether w1: im00: 1 used, preferably 1: 1 to 10: 1.1 to 5.1. Take fenprofen 丨 alcohol R3〇: H II usually does not have

耵反觅、'口果达成不利影響,但是醇R30H I有利的用量係如上所述。 以tit:束二後,產物通常進行蒸餘,而且均相觸媒可 、严、餾的殘留產物回A,必要時重複使用。如果 设使用觸媒,則可以有利地在蒸餘 形忐,,、t 田心則和沸點咼於反應所 形成又縮醛III的溶劑加入反應混合物。々 媒右节輪k Μ 如果所用的均相觸 入具熱安定性和化學安定性,則可以省略加 一點溶劑的步驟,而且均相觸媒可以回流到反應, -16^ 一 -__ 本‘氏張尺度適用中國國家標準(CNS ) A4祕(2!GX297公整) (請先閱讀背面之注意事項再填寫本頁) 訂 泉 A7 ----:----B7 五、發明説明(14 ) 例如在三苯基膦熔融液裡。 在本發明方法的另一具體實施例裡,烯丙醚I到縮醛III的 同分異構化和縮輕化反應係在使用均相觸媒下進行,該方 法有利地在液相裡進行。 傾發現’令人驚訝地,基本上不溶於反應介質之傳統多 相氯化作用觸媒可以作為將晞丙醚〗轉化成縮醛ΠΙ的觸媒。 在這些氫化作用觸媒之中’較佳為包含一或多個元素週期 表中第I Α族,VIA族,VIIA族或VIIIA族的元素,必要時連 同一或多個VA族的元素,特別是鉻,鉬,鎢,鍊,釕, 鈷,鎳,铑’銥,餓,鈀及鉑,必要時與鐵及/或銅併用的 觸媒。 經濟部中央標準局員工消費合作社印製 (請先閲讀背面之注意事項再填寫本頁) 在本發明之方法中’舉例來說,可以使用經沉澱之觸媒 7為非均相觸媒。此等觸媒可以從其鹽溶液,特別從其硝 馼鹽及/或乙酞鹽溶液,藉由添加鹼金屬及/或鹼土金屬氫 氧化物及/或碳酸鹽溶液,例如瞬間溶解性氫氧化物,水合 氧化物,鹼式鹽或碳酸鹽以使其催化活性化合物沉澱,然 後乾燥所得足沉澱物,接著通常在3〇〇_7〇(rc,特別 °c的溫度下烺燒使轉化成由例如在通常5〇_7〇〇t:,特別是 100-400°C下以還原劑,例如氫或含氫氣體還原至相關金屬 友/或還原至低氧化態之氧化化合物的相關氧化物,混合氧 化物及/或混合多價氧化物,再轉化成實際催化活性形式而 得。通常一直繼續進行還原反應,直到不再形成水。在製 造包含載體之經沉澱觸媒時,催化活性组份的沈澱作用可 在相關載體的存在下進行。然而,催化活性組份也可以有 利地同時與載體從相關鹽溶液一起沉澱,在該情況裡,例 -17- 本紙張尺度適用中國國家標準(CNS ) ( 210X297公楚) A7 B7 經濟部中央標準局員工消費合作社印製 五、發明説明(15 ) 如是在催化活性組份經由水玻璃溶液裡沉澱。 包含催化活性金屬或沉積在載體上之金屬化合物的觸媒 較佳用於本發明的方法裡。除上述也包含除催化活性乜份 以外之載體的經沉澱觸之外,大體上經負載之觸媒_並中催 化活性觸媒已藉由浸潰方式敷置在載體上-適用於本發明的 方法。 將催化活性觸媒敷置於載體上的方法通常不是決定性 的,而且可以多種方式進行。催化活性金屬可以藉由例如 以相關元素之鹽類或氧化物的溶液或懸 這些載體上’乾燥和經由還原劑,較佳用 聯氨將金屬化合物還原成低氧化態的相關金屬或氧化化合 物。將催化活性觸媒敷置於載體上的另一種可行方法是2 丈熱可迅速分解的鹽,例如硝酸鹽的溶液,或以受熱可迅 速分解的錯合化合物,例如催化活性金屬的羰基或^化物 基錯合物浸漬載體,並將以此方式浸潰的載體加熱至3〇〇到 60(TC以使經吸收的金屬化合物熱分解。該熱分解作用較佳 在惰性氣體大氣之下進行。適當的惰性氣體是’例如氮, 二氧化碳,氫或惰性氣體。此外,催化活性金屬可以藉由 咨汽沉積法或藉由噴焰法沉積在觸媒載體上。 這些負載觸媒裡催化活性金屬的含量原則上不是決定性 的,只要可以進行成功地進行本發明的方法。對於熟習此 項技藝者而言可顯而易知,這些負載觸媒裡含較高量的催 化活性金屬係使時空產率比催化活性金屬含量低較低者 高。然而,通常使用含有基於觸媒總重量〇」到8 〇,較佳 0.5到3 0重f %催化活性金屬的負載觸媒。因為這些所述的 -18- 本紙張尺度適用中國國家標隼(CNS )八4規格(_ΙΓ^Χ297公缝) (請先閲讀背面之注意事項再填寫本頁) 訂 ...泉. 五、發明説明(16 A7 B7 經濟部中央標準局貝工消費合作社印製 含量係觸媒總重量-包括載體-為 為基凌但疋不同載體具有 非常不同的岔度和表面穑屮,姑工u ^ 彻比然而也可以使用小於或大於 所述的數量而未對本發明方法的結果產生不利影^ ^ 也可以將數個催化活性金屬敷置於各別的載體上。此二, 催化活性金屬可以藉由例如DE_A 2 519 8i7,Ep_A⑷川 和EP-A 285 420的方法敷置在載體±。在上述公告案的觸媒 裡,催化活性金屬係以由上述金屬之鹽穫錯合物的教處理 及/還原作用而得的合金存在,其中該鹽或錯合物係藉由例 如浸潰法沉積於載體上。 大體上,鋁或鈦的氧化物,氧化锆,矽石,矽藻土,矽 膠,氧化鋁,例如蒙脫石,矽酸鹽,例如矽酸鎂或矽酸 鋁,沸石,例如ZSM-5或ZSM-10沸石,及活性碳可以作為 載體。較佳的載體是氧化鋁,二氧化鈦,氧化锆和活性 碳。當然也可以使用不同載體的混合物當做用於本發明之 觸媒的載體。 只行縮酸化反應之多相觸媒的例子是下列的觸媒: 氧化鉑,鈀/氧化鋁,鈀/矽石,鈀/硫酸鋇,鈀/氧化 锆,铑/活性碳,铑/氧化鋁,釕/矽石或釕/活性碳,鎳/矽 石姑/碎石’錄/氧化銘’羰_基鐵粉,鍊把/活性碳,鍊|白 /活性故’氧化銘-氧化錯混合物,舶飽/活性碳.,亞絡酸 銅’亞路酸鋇’氧化鎳-氧化鉻/氧化鋁,硫化鈷,硫 鎳’氧化銅/氧化鉬/氧化矽/氧化鋁觸媒,部分受到硒或 毒性的#巴/活性碳觸媒,及根據DE_a 3 932 332,US-A 3 445 ’ EP-A 44444,EP-A 147 219,DE-A 3 904 083,DE-: 321 1CU ’ eP-A 415 202,DE-A 2 366 264和EP-A 100 406的觸 化 鉛 449 -A 2 (請先閲讀背面之注意事項再填寫本頁) 訂 •X. 19- 本紙張尺度適用中國國家標準(CNS ) A4規格(21〇χ297公瘦) A7耵 Reverse search, 'mouth fruit reached an adverse effect, but the beneficial amount of alcohol R30H I is as described above. After taking tit: beam two, the product is usually subjected to distillation, and the homogeneous catalyst can return the residue to A, which can be reused if necessary. If it is assumed that a catalyst is used, it is advantageous to add the reaction mixture in the form of distillate, tantalum, and a solvent whose boiling point is formed by the reaction to form acetal III. If the homogeneous contact used has thermal and chemical stability, the step of adding a little solvent can be omitted, and the homogeneous catalyst can be refluxed to the reaction. -16 ^ 一 -__ 本 ' The Zhang scale is applicable to the Chinese National Standard (CNS) A4 secret (2! GX297 round) (Please read the precautions on the back before filling this page) Dingquan A7 ----: ---- B7 V. Description of the invention ( 14) For example in a triphenylphosphine melt. In another specific embodiment of the method of the present invention, the isomerization and lightening reaction of allyl ether I to acetal III is performed using a homogeneous catalyst, and the method is advantageously performed in the liquid phase. . It was found that, surprisingly, a conventional heterogeneous chlorination catalyst which is substantially insoluble in the reaction medium can be used as a catalyst for converting propyl ether to acetal II. Among these hydrogenation catalysts, it is preferable to include one or more elements of Group IA, VIA, VIIA, or VIIIA in the periodic table, and if necessary, the same or more elements of Group VA, especially It is a catalyst for chromium, molybdenum, tungsten, chain, ruthenium, cobalt, nickel, rhodium 'iridium, palladium and platinum, and iron and / or copper if necessary. Printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs (please read the notes on the back before filling this page) In the method of the present invention, for example, the precipitated catalyst 7 can be used as a heterogeneous catalyst. These catalysts can be obtained from their salt solutions, in particular from their nitrate and / or phthaloyl salt solutions, by adding alkali and / or alkaline earth metal hydroxides and / or carbonate solutions, such as instantaneous soluble hydroxide Compounds, hydrated oxides, basic salts or carbonates to precipitate their catalytically active compounds, and then the resulting foot precipitate is dried, and then converted to calcination, usually at a temperature of 300-700 (rc, particularly ° C). Relevant oxides from oxidizing compounds that are reduced to relevant metal friends / or to low oxidation states, for example, by reducing agents, such as hydrogen or hydrogen-containing gases, usually at 50-700 t: especially at 100-400 ° C. , Mixed oxides and / or mixed polyvalent oxides, and then converted into the actual catalytically active form. Usually the reduction reaction continues until water no longer forms. When the precipitated catalyst containing the carrier is produced, the catalytically active group The precipitation of the components can be carried out in the presence of the relevant carrier. However, the catalytically active components can also be advantageously precipitated together with the carrier from the relevant salt solution. In this case, Example -17- this paper scale applies to China Standards (CNS) (210X297 Gongchu) A7 B7 Printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 5. Description of the invention (15) If the catalytically active components are precipitated in a water glass solution. Contains catalytically active metals or is deposited on a carrier Catalysts of metal compounds are preferably used in the method of the present invention. In addition to the above-mentioned precipitated catalysts that also include carriers other than catalytically active catalysts, the supported catalysts and catalysts are generally supported. Application by impregnation on the carrier-suitable for the method of the invention. The method of applying the catalytically active catalyst to the carrier is generally not decisive and can be carried out in a variety of ways. The catalytically active metal can be, for example, related to Solution or suspension of salts or oxides of the elements on these supports' dried and via a reducing agent, preferably hydrazine, to reduce the metal compound to the relevant metal or oxidized compound in a low oxidation state. A catalytically active catalyst is placed on the support Another possible method is to quickly decompose salts, such as nitrate solutions, or complex compounds that decompose rapidly when heated. For example, the carbonyl or carbonyl complex of the catalytically active metal is impregnated with the support, and the support impregnated in this manner is heated to 300 to 60 ° C. to thermally decompose the absorbed metal compound. The thermal decomposition is better It is carried out under an atmosphere of an inert gas. A suitable inert gas is' for example nitrogen, carbon dioxide, hydrogen or an inert gas. In addition, the catalytically active metal can be deposited on the catalyst carrier by a vapor deposition method or by a flame spray method. These The content of catalytically active metals in supported catalysts is not critical in principle, as long as the method of the present invention can be successfully carried out. It will be apparent to those skilled in the art that these supported catalysts contain a relatively high amount of Catalytically active metals make the space-time yield higher than those with lower and lower catalytically active metals content. However, loading catalysts containing f% of catalytically active metals based on the total weight of the catalyst are preferably from 0 to 80, preferably from 0.5 to 30 weight percent. Media. Because these mentioned -18- this paper size is applicable to China National Standard (CNS) 8 4 specifications (_ΙΓ ^ × 297 common sewing) (Please read the precautions on the back before filling this page) Order ... Description of the invention (16 A7 B7 Printed content of the Central Bureau of Standards of the Ministry of Economic Affairs, Shellfish Consumer Cooperative, the total weight of the catalyst-including the carrier-is based on the base, but different carriers have very different degrees and surfaces. However, it is also possible to use smaller or larger amounts without adversely affecting the results of the method of the present invention. ^ Several catalytically active metals can also be deposited on separate supports. Second, the catalytically active metals can be borrowed The method is applied to a carrier ± by methods such as DE_A 2 519 8i7, Ep_A Takikawa, and EP-A 285 420. In the catalysts of the above-mentioned announcement, the catalytically active metals are taught to obtain complexes from the salts of the above-mentioned metals and / Reduction-derived alloys exist in which the salt or complex is deposited on the support by, for example, impregnation. In general, aluminum or titanium oxides, zirconia, silica, diatomaceous earth, silica gel, Alumina, such as montmorillonite, silicic acid Salts, such as magnesium silicate or aluminum silicate, zeolites, such as ZSM-5 or ZSM-10 zeolites, and activated carbon can be used as carriers. The preferred carriers are alumina, titania, zirconia, and activated carbon. Of course, it is also possible to use A mixture of different carriers is used as a carrier for the catalyst of the present invention. Examples of heterogeneous catalysts that perform only the acidification reaction are the following catalysts: platinum oxide, palladium / alumina, palladium / silica, palladium / barium sulfate , Palladium / zirconia, rhodium / activated carbon, rhodium / alumina, ruthenium / silica or ruthenium / activated carbon, nickel / silica / crushed stone 'Record / Oxide Ming' carbonyl iron powder, chain handle / active Carbon, Chain | White / Activity So 'Mixed Oxide-Oxidation Miscellaneous Mixture, Saturated / Activated Carbon ... / Molybdenum oxide / silicon oxide / alumina catalyst, # bar / activated carbon catalyst partially exposed to selenium or toxicity, and according to DE_a 3 932 332, US-A 3 445 'EP-A 44444, EP-A 147 219, DE-A 3 904 083, DE-: 321 1CU 'eP-A 415 202, DE-A 2 366 264, and EP-A 100 406 in contact with lead 449 -A 2 (Please read the note on the back first Please fill in this page again) X. 19- This paper size applies Chinese National Standard (CNS) A4 specification (21〇297 thin) A7

斯 矽 特 方 的 矽 經濟部中央標準局員工消費合作社印製 矽 易 1到 合 均 391955 五、發明説明(17 媒。 包含布忍斯特及/或路易斯酸中心 有利用於本發明的方法裡。 、虱化作用觸媒也可以 舉例來說,催化活性金屬 易斯酸中心,如果其在觸媒:身氯 地還原成相關金屬。這例 "0虱轧骹活化時不完全 如亞銘酸銅。此:,二=:亞路酸鹽的觸媒,例 可以經由所用的載體置人觸 5^斯故或驗式中心 , 句媒内包含布忍斯特或政黑 =中心之載體的例子是氧化銘,二氧化飲,易 石二夕酸;,氧化銘’“,混合的鎂/氧化銘和活:碳。 包含元素週期表中次^TA ^ θ -立 A , νϊ ’ Vn及/或VIII元素,特別 疋兀素週期表中次族νπ及VTTT分本.t 特另 或路易斯酸之載體上的备載觸=貝在視為布忍斯 、,+、“ 的負载觸媒因此較佳地用於本發明 :里田做JL化作用觸媒。特別有利的觸媒是,舉例來說 人上I化鋁上的釕’矽石上的釕 妨,氧化锆^銜,二氧化欽上的銜,氧化銘上=上 石上的免,乳化锆上的赵,疏酸鋼上的免和部份地 或鉛毒害之活性碳觸媒上的免。 布忍斯特或路易斯酸的組份,例如滞石,氧化銘或 石,磷酸或硫酸’可以加入本身沒有此等布忍斯特或路 "斤I中心的觸媒。其通常加入基於所用觸媒重量之〇 〇 5,軚佳0·05到0.5,特別較佳〇_1到0.4重量%的數量。 也通用於將烯丙醚丨轉化成縮醛m的是包含選自元素週期 表中VIA族及VIIIA族過渡金屬之非均相有機金屬錯合化 物的多相觸媒,例如其中相關金屬固定在聚合基質的非 20- 本紙張尺度適用中國國家標準(CNS ) A4規格(2I0X297公釐 (請先聞讀背面之注意事項再填寫本頁〕Silicone's Consumer Co-operative Society of the Silicon Economics Central Standards Bureau printed Siyi 1 to 391955 on average. V. Invention Description (17). Includes Brewster and / or Lewis Acid Center for use in the method of the present invention. Lice-activating catalysts can also be exemplified by catalytically active metal easy acid centers, if they are reduced to the relevant metals in the catalyst: Chlorine. This example is not completely as infective when activated. Copper. This :, two =: succinate catalysts, for example, can be placed on the carrier through the use of 5 ^ sigma or test center, the sentence media contains Bronst or Zhenghe = center of the example It is an oxide inscription, a dioxin, an osparic acid; an oxide inscription "", a mixed magnesium / oxidized inscription and a live: carbon. Includes ^ TA ^ θ-standing A, νϊ 'Vn and / in the periodic table Or element VIII, especially the subgroups νπ and VTTT in the periodic table. T Special or prepared on the carrier of the Lewis acid = Bei Zai is regarded as the load catalyst of Brenz ,, +, and ". It is best used in the present invention: Litian is used as a JL catalyst. The particularly advantageous catalyst is, For example, ruthenium on aluminum, ruthenium on silica, zirconia ^, zirconia, oxidizing inscription = free on the stone, emulsified zirconium on zirconium, on sparse acid steel Exemptions and exemptions on activated carbon catalysts that are partially or lead poisoned. Bronister or Lewis acid components, such as stagnation, oxidizing or stone, phosphoric acid or sulfuric acid 'can be added per se without these Bronister or The catalyst of the road center is usually added in an amount of 0.05 to 0.5, preferably 0 to 0.4% by weight based on the weight of the catalyst used. It is also commonly used for allyl. The ether 丨 converted to acetal m is a heterogeneous catalyst containing heterogeneous organometallic complexes selected from the group VIA and VIIIA transition metals in the periodic table of the elements, such as non-20- This paper size applies to China National Standard (CNS) A4 specifications (2I0X297 mm (please read the precautions on the back before filling in this page)

經濟部中央標準局員工消费合作社印製 391955 五、發明説明(18 ) 相觸媒,該錯化合物能用作該處理階段之均相催化作用。 此等聚合基質可以是樹脂,例如苯乙烯/二乙烯基苯樹脂 或酚/甲醛樹脂,苯乙婦/二乙埽基苯樹脂或酚/甲醛樹脂, 其中用來錯合過渡金屬元素之相關配位基較佳共價鍵結, 配位基依次地與相關過渡金屬形成錯合物,因而使這些相 關過渡金屬事實無法活動。 VIA族或VIIIA族元素的此等非均相鍵結聚合物之錯合 物’特別是鈀及鎳錯合物的複合物可以藉由例如Zhuangyu 等人的方法(反應性聚合物2_(1988),249)或根據王氏等人(j 〇rg. Chem.这(1994), 5358)的方法獲得。VIA族及VIIIA族元 素之不動的膦錯合物可以藉由例如Hartley,Adv. Organomet. Chem. (1977) .189,F_R. Hartley,經負載的金屬錯合物, Riedel,Dordrecht 1985 ’ Κ· Smith,有機合成的固體載體及觸 媒 ’ Ellis Horwood,Prentice Hall, N.Y. 1992 > C.H. Pittman,有機合成時反應負載的聚合物第249頁,wiley, Chichester 1980和 C.H. Pittmann J. Am. Chem. Soc. Μ (1976), 5407 及 Ann. N.Y. Acad. Sci· .245 (1977), 15 的方法。使用此 等非均相觸媒的優點在於特別是更容易及更溫和地從反應 產物分離出觸媒。該觸媒可以置於反應混合物流經的固定 床裡或可以懸浮在反應混合物裡並在反應結束後機械地分 離掉。 非均相觸媒可以用於在液態反應介質裡的懸浮液或,較 佳地置於一或多個固定床。當使用懸浮在液態反應介質裡 之非均相觸媒時,方法可以在例如攪拌壺或環狀反應器裡 進行。當使用置於固定床裡的非均相觸媒時,反應混合物 -21 - 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) (請先閱讀背面之注意事項再填寫本頁)Printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 391955 V. Description of the invention (18) Phase catalyst, this compound can be used for homogeneous catalysis in this processing stage. These polymeric matrices can be resins, such as styrene / divinylbenzene resin or phenol / formaldehyde resin, acetophenone / diethylfluorenylbenzene resin or phenol / formaldehyde resin, which are used to intermix the relevant components of transition metal elements. The positional groups are preferably covalently bonded, and the ligands sequentially form complexes with related transition metals, thus rendering these related transition metals virtually inactive. The complexes of these heterogeneous bonding polymers of group VIA or VIIIA elements, especially the complexes of palladium and nickel complexes, can be performed by, for example, the method of Zhuangyu et al. (Reactive Polymer 2_ (1988) 249) or according to Wang et al. (Jorg. Chem. This (1994), 5358). The immobilized phosphine complexes of Group VIA and Group VIIIA elements can be obtained, for example, by Hartley, Adv. Organomet. Chem. (1977). 189, F.R. Hartley, supported metal complexes, Riedel, Dordrecht 1985 'K · Smith, Solid Supports and Catalysts for Organic Synthesis' Ellis Horwood, Prentice Hall, NY 1992 > CH Pittman, Polymers Supported by Reactions in Organic Synthesis, p. 249, Wiley, Chichester 1980 and CH Pittmann J. Am. Chem. Soc M (1976), 5407 and Ann. NY Acad. Sci. 245 (1977), 15. The advantage of using such heterogeneous catalysts is, in particular, the easier and gentler separation of the catalyst from the reaction products. The catalyst may be placed in a fixed bed through which the reaction mixture flows or may be suspended in the reaction mixture and mechanically separated after the reaction is completed. Heterogeneous catalysts can be used in suspension in a liquid reaction medium or, preferably, in one or more fixed beds. When a heterogeneous catalyst suspended in a liquid reaction medium is used, the method can be performed in, for example, a stirred tank or a ring reactor. When using a heterogeneous catalyst placed in a fixed bed, the reaction mixture -21-This paper size applies to China National Standard (CNS) A4 (210X297 mm) (Please read the precautions on the back before filling this page)

IJmlglMileitma..·:: .1 391^55 A7 五、發明説明( 19 經濟部中央標準局員工消費合作社印裝 通常藉由j相或液相或液淋床程序床通過固定的觸媒床。 一般而言,觸媒係以每小時每升觸媒〇 〇〇1到2,較佳 〇_〇1到丨.5 ’特別較佳0.05到!公斤反應混合物的空間速度裝 載液態混合物。當使用非均相觸媒時,反應可以在溶劑的 存在或不存在之下進行。所用的溶劑可以相同於可以用於 在均相觸媒下進行反應的溶劑。 ' 從烯丙醚I產生縮醛m的醇R3〇Hn的加入數量範圍很廣。 形成縮醛III所需之等莫耳數量必要時也可以超過。大體 上,醇R3OH II係以II/〗為基於該反應所用之烯丙醚〗的i :】 到100 . 1 ’較佳1:1到10:1,特別1:1到5:1的莫耳比加 入。以烯丙醚I為基礎之非常過量的醇R3〇H Η通常沒有 反應結果造成不利影響,但是醇R30H π有利的用量係如 所述。在液相非均相觸媒上得到縮醛ηι之烯丙醚的同分 構化和縮醛化反應通常在“到%。^,較佳50到280它, 別較佳8 0到250 c的溫度,和通常在i到1〇〇,較佳i到5 〇 特別2到1 0巴的壓力下進行。 來自孩反應階段的液態反應取出物通常以類似上述以 相觸媒進行該程續階段的方式進行蒸餾。當使用非均相㈣ 媒時,略觸媒的再循環,如同當使用均相觸媒時在特殊環 境下視為優點一般,當然可以省略。 縮醛可以經由本發明方法,從缔丙醚起始,以良好的 率和k擇性製知。尤其,本發明方法所用的觸媒係以其 反應產物的良好可分離性及以良好的穩定性為其特徵而 別之’結果可以克服先前技術的缺點。 實施例 對 上異特 均 觸 產 從 區 -22 (請先閱讀背面之注意事項再填寫本頁)IJmlglMileitma .. · :: .1 391 ^ 55 A7 V. Description of the Invention (19 The printing of the Consumer Cooperatives of the Central Bureau of Standards of the Ministry of Economic Affairs usually prints through a fixed catalyst bed through a j-phase or liquid or liquid bed process bed. General In terms of catalysts, the liquid mixture is loaded with a liquid mixture at a space velocity of 0.001 to 2, preferably 0.001 to .5 'per litre of catalyst per hour, and 0.05 to 100 kg of reaction mixture. When using non- In the case of a homogeneous catalyst, the reaction can be carried out in the presence or absence of a solvent. The solvent used can be the same as the solvent that can be used to carry out the reaction in the presence of a homogeneous catalyst. The amount of alcohol R3OHn is added in a wide range. The amount of moire required to form acetal III can also be exceeded if necessary. In general, the alcohol R3OH II is based on II /, based on the allyl ether used in the reaction. i:] to 100. 1 ', preferably from 1: 1 to 10: 1, especially from 1: 1 to 5: 1. A very excess alcohol R3OH based on allyl ether I is usually not available. The reaction results have an adverse effect, but the beneficial amount of alcohol R30H π is as described. On liquid phase heterogeneous catalysts The isomerization and acetalization of the allyl ether to acetal is usually at "to%. ^, Preferably 50 to 280, more preferably 80 to 250 c, and usually at i to 1 〇〇, preferably i to 50, especially at a pressure of 2 to 10 bar. The liquid reaction extract from the reaction stage is usually distilled in a manner similar to that described above for the subsequent stages with a catalyst. When using non- In the case of homogeneous catalysts, the recycling of the catalyst is slightly as if it is regarded as an advantage in a special environment when using homogeneous catalysts, and of course it can be omitted. The acetal can be started from propyl ether through the method of the present invention, and Good rate and selectivity. In particular, the catalyst used in the method of the present invention is characterized by good separability of its reaction products and good stability, which can overcome the shortcomings of the prior art. The examples are all on the production site from the -22 (please read the precautions on the back before filling this page)

391955 A7 B7 五、發明説明(20 ) 實施例1 玻璃壓熱器裡裝入0.022克觸媒HRuCl(CO) (PPh3)3,0.03 1 克三苯基膦,0.005克癸酸,3_18克(24_8毫莫耳)正丁醇和 1_83克(24·8愛莫耳)1-丁氧基丁 _2_稀。在自生壓力下i60°C 裡反應1 6個小時之後’經由校準氣相色層分析法分析反應 混合物。85%的轉化率,形成選擇性為85.1 %的1,1 -二丁氧 基丁烷及選择性為10.1%的1-丁氧基丁小烯。 實施例2 玻璃壓熱器裡裝入0.01克非均相觸媒鈀/活性碳(1 〇重量 %Pd),3.0克(24毫莫耳)1-丁氧基丁-2-烯和1.73克(24毫莫 耳)正丁醇。在氫大氣壓(1巴)下150 °c裡反應16個小時之 後,經由校準氣相色層分析法分析反應混合物。21%的轉 化率’形成選擇性為42%的U-二丁氧基丁烷,選擇性為 25%的二丁基醚及選擇性為22%的1-丁氧基丁小烯。 (請先閱讀背面之注意事項再填寫本頁)391955 A7 B7 5. Description of the invention (20) Example 1 0.022 g of catalyst HRuCl (CO) (PPh3) 3, 0.03 1 g of triphenylphosphine, 0.005 g of capric acid, 3-18 g (24_8) Millimoles) n-butanol and 1_83 grams (24.8 Emory) of 1-butoxybutane_2_ dilute. After 16 hours of reaction at i60 ° C under autogenous pressure, the reaction mixture was analyzed via calibrated gas chromatography. A conversion of 85% results in the formation of 1,1-dibutoxybutane with a selectivity of 85.1% and 1-butoxybutene with a selectivity of 10.1%. Example 2 A glass autoclave was charged with 0.01 g of heterogeneous catalyst palladium / activated carbon (10 wt% Pd), 3.0 g (24 mmol) of 1-butoxybut-2-ene and 1.73 g (24 mmol) n-butanol. After 16 hours of reaction at 150 ° C under hydrogen atmosphere (1 bar), the reaction mixture was analyzed by calibrated gas chromatography. A conversion of 21% 'forms U-dibutoxybutane with a selectivity of 42%, dibutyl ether with a selectivity of 25%, and 1-butoxybut small olefin with a selectivity of 22%. (Please read the notes on the back before filling this page)

訂 經濟部中央標準局員工消費合作社印製 23- 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐)Printed by the Consumer Cooperatives of the Central Bureau of Standards of the Ministry of Economic Affairs. 23- This paper size applies to the Chinese National Standard (CNS) A4 (210X297 mm).

Claims (1)

391955 齋 气修正丨 4 、申請專利範圍 1. 7種由醇與缔丙醚反應製備縮醛的方法,其 Μ辱在液相裡’於包括銘金屬類,舒、錄、免、舶、鉞― 及/或銥义有機金屬化合物的均机觸媒之存在 i含一或多種元素週期表.中之I、鉬、鎢、鍊、釕二: .末、铑、銥、餓、鈀及/或敘元素之非均相觸媒的存在 於基本質上無水之條件下反應。 2· ^據情專利範圍第」項之方法,其中牌用的均相觸媒 為鉑金—屬與單配鬼或多配位膦或亞鱗酸鹽配位基的錯合 物。 口 3 · t1 .法,其中、均相觸媒係 在反應介—賓:趣教原處製得。 板據申請專利範園第1項之方法,其中該非均相觸媒另 外包.含鐵_及/或銅。 根據申請專利蓋圍第1項之方法,其中所用的非均相緝 媒為一發責载觸媒。 根據申請專利範圍第1或'&項之方法,其中所用的非均 相觸媒為一種包含銘―二—— 氧H,轉L矽酸 盛’礬土沸石及./或活性碳作為截體的負載觸媒。 根據申請專利範圍第1或5項之方法,其_中使用包含免 的非均相觸媒。 -24- 本紙浪尺度適用國國家標準(CNS )㈣协(210><297公董) (請先閱讀背面之注意事項再填寫本頁)391955 Fasting Amendment 丨 4, the scope of application for patents 1. 7 methods for preparing acetals by the reaction of alcohols and allyl ethers, whose M is in the liquid phase, including metals such as Ming, Shu, Lu, Wu, Chu, Lu ― And / or the presence of a homogeneous catalyst for an iridium organometallic compound i containing one or more elements of the periodic table, I, molybdenum, tungsten, chain, ruthenium II:., Rhodium, iridium, starvation, palladium and / Or heterogeneous catalysts of element or element exist in the condition that they are essentially water-free to react. 2. ^ The method according to item "Scope of the Patent," in which the homogeneous catalyst used for the brand is platinum-a complex with a mono-coordinator or multi-coordination phosphine or lindenite ligand.口 3 · t1. Method, in which the homogeneous catalyst system is prepared in the reaction medium-Bin: Qujiao origin. The method according to item 1 of the patent application park, where the heterogeneous catalyst is separately outsourced, contains iron and / or copper. According to the method of covering the first item of the patent application, the heterogeneous anti-monitoring agent used is a responsible catalyst. According to the method of the scope of application for patents No. 1 or '&, the heterogeneous catalyst used is a kind of zeolite containing inscription-two-oxygen H, trans-L silicate Sheng' alumina zeolite and. Body load catalyst. The method according to item 1 or 5 of the scope of patent application, in which a heterogeneous catalyst containing exemption is used. -24- The national standard (CNS) of this paper is applicable to the standard (210 > < 297 public directors) (Please read the precautions on the back before filling this page) 經濟部中央標準局員工消費合作社印製 391955 齋 气修正丨 4 、申請專利範圍 1. 7種由醇與缔丙醚反應製備縮醛的方法,其 Μ辱在液相裡’於包括銘金屬類,舒、錄、免、舶、鉞― 及/或銥义有機金屬化合物的均机觸媒之存在 i含一或多種元素週期表.中之I、鉬、鎢、鍊、釕二: .末、铑、銥、餓、鈀及/或敘元素之非均相觸媒的存在 於基本質上無水之條件下反應。 2· ^據情專利範圍第」項之方法,其中牌用的均相觸媒 為鉑金—屬與單配鬼或多配位膦或亞鱗酸鹽配位基的錯合 物。 口 3 · t1 .法,其中、均相觸媒係 在反應介—賓:趣教原處製得。 板據申請專利範園第1項之方法,其中該非均相觸媒另 外包.含鐵_及/或銅。 根據申請專利蓋圍第1項之方法,其中所用的非均相緝 媒為一發責载觸媒。 根據申請專利範圍第1或'&項之方法,其中所用的非均 相觸媒為一種包含銘―二—— 氧H,轉L矽酸 盛’礬土沸石及./或活性碳作為截體的負載觸媒。 根據申請專利範圍第1或5項之方法,其_中使用包含免 的非均相觸媒。 -24- 本紙浪尺度適用國國家標準(CNS )㈣协(210><297公董) (請先閱讀背面之注意事項再填寫本頁)Printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 391955 Fasting Amendment 丨 4. Application for patent scope 1. 7 methods for preparing acetals by reacting alcohol with propyl ether, which are in the liquid phase. The existence of homogeneous catalysts for the organometallic compounds of Shu, Lu, Lu, Ship, 钺, and / or Iridium i contains one or more periodic table of elements. I, molybdenum, tungsten, chain, ruthenium II:. , Heterogeneous catalysts of rhodium, iridium, iridium, palladium, and / or elements are reacted in the presence of essentially anhydrous conditions. 2. ^ The method according to item "Scope of the Patent," in which the homogeneous catalyst used for the brand is platinum-a complex with a mono-coordinator or multi-coordination phosphine or lindenite ligand.口 3 · t1. Method, in which the homogeneous catalyst system is prepared in the reaction medium-Bin: Qujiao origin. The method according to item 1 of the patent application park, where the heterogeneous catalyst is separately outsourced, contains iron and / or copper. According to the method of covering the first item of the patent application, the heterogeneous anti-monitoring agent used is a responsible catalyst. According to the method of the scope of application for patents No. 1 or '&, the heterogeneous catalyst used is a kind of zeolite containing inscription-two-oxygen H, trans-L silicate Sheng' alumina zeolite and. Body load catalyst. The method according to item 1 or 5 of the scope of patent application, in which a heterogeneous catalyst containing exemption is used. -24- The national standard (CNS) of this paper is applicable to the standard (210 > < 297 public directors) (Please read the precautions on the back before filling this page) 經濟部中央標準局員工消費合作社印製Printed by the Consumer Cooperatives of the Central Bureau of Standards of the Ministry of Economic Affairs
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US4658069A (en) * 1985-07-02 1987-04-14 National Distillers And Chemical Corporation Conversion of allyl ethers to acetals
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