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TWI359160B - Polytrimethylene ether glycol with excellent quali - Google Patents

Polytrimethylene ether glycol with excellent quali Download PDF

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Publication number
TWI359160B
TWI359160B TW93112823A TW93112823A TWI359160B TW I359160 B TWI359160 B TW I359160B TW 93112823 A TW93112823 A TW 93112823A TW 93112823 A TW93112823 A TW 93112823A TW I359160 B TWI359160 B TW I359160B
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Taiwan
Prior art keywords
propanediol
less
polytrimethylene ether
glycol
color
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TW93112823A
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Chinese (zh)
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TW200508278A (en
Inventor
Hari Babu Sunkara
Howard Chung-Ho Ng
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Du Pont
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Description

1359160 九、發明說明: 優先權 本申請案係訴請2003年5月6曰申請之美國優先申請案序 號60/468,228及2003年8月5曰申請之美國優先申請案序號 1〇/634,61 1之優先權,此二者均併列為本文之參考。 【發明所屬之技術領域】 本發明涉及生產具優異質地,特別是其顏色與功能性, 之聚三亞甲醚二醇之同質及共聚喊類,其係藉由使用^ 丙二醇,較佳為獲取自可再生性生物來源者。 【先前技術】 1,3·丙二醇(下文中亦稱為”pD〇")係為一種可用於各種聚 合物,包括.聚酯類、聚胺酯類、聚醚類和環狀化合物之 生產之單體。聚三亞甲醚二醇(下文中亦稱為"p〇3G")之同 質和共聚謎類即為此等聚合物之實例。該聚合物最終可用 於各種應用’包括:纖維、薄膜等。 產生丨,3_丙二醇之化學途徑已為人知曉。例如:1,3-丙 二醇可製備自: 1.環氧乙⑨,在催化劑和磷化氫、水、一氧化碳、氫和 一種酸之存在之下(”氫曱醯化途徑") 2·丙烯醛之催化溶液相水合作用再進行還原作用丙烯 醛途徑") 此兩種生成1,3-丙二醇之途徑均涉及令間產物3_羥基丙 醛(下文中稱為"ΗΡΑ”)之合成。在最後之催化性氫化步驟 中將ΗΡΑ還原成PDO。隨後之最終純化涉及數個程序,包 93144.doc 1359160 括真空蒸發。 生成1,3-丙二醇之生化途徑已被說明’其係利用生物生 產之原料及可再生性資源,例如:玉米原料。此等pD〇於 下文中稱之為”生化PDO"。舉例言之,可將甘油轉化成 1,3-丙二醇之細菌菌株已發現於例如··克雷氏菌屬 (Klebsiella)、擰檬酸菌屬(Citr〇bacter)、克氏梭桿菌屬 (Clostridium)和乳桿菌屬(Lactobacillus)。該技術揭示於數 篇專利中,包括:美國專利第5,633,362、5,686,276和最近 之5,821,〇92號,其均併列為本文之參考。在 中,Nagarajan等人尤其揭示一種使用重組生物自甘油生產 1,3-丙二醇之生物方法。該方法併用經異質性pdu二醇氫化 酶基因轉形,對丨,2-丙二醇具有專—性之大腸桿菌 (E.coh)。使該經轉形之大腸桿菌生長於以甘油作為碳源之 培養基中並自該生長培養基分離丙二醇。因為細菌與 酵母菌二者均可轉化葡萄糖(例如:玉米糖)或其他碳水化 合物成為甘油,故該發明之方法可提供一種快速、不貴且 環保之可用於聚酯類、聚醚及其他聚合物之生產之丨,3-丙 二醇單體之來源。 自觸年代早期’沉澱法(例如:以❻丙二醇和緩化物 或其他材料)即已被用以自所欲產物(例如:酵素)中分離出 有色及有味成份以獲取純化製品。自發酵液中沉澱高分子 量構成物,再以還原劑將此等成份漂白(DE39i7645)已為 人所知。此外,微㈣後再奈米過據以去除殘留化合物亦 已知有所助益(聽7529),其中分子量高於分離大小之物 93l44.doc 1359160 ^可被去m,奈米過_會很快被阻塞且其成本頗 高。 各種處理方法已揭示於先前技藝以存在於pD〇t之去除 顏色前驅物,然而,該等方法費力、昂貴且會增加聚合物 之成本。例如·· Kelsey,美國專利第5,527,973號揭示一種 用以提供經純化1,3-丙二醇之方法,其可做為淺色聚酯之 起始材料。該方法具有數個缺點,包括:冑用多種涉備且 需要以大量水加以稀釋,其又難以自產物中去除。 Sunkara等人,美國專利第6,235 948號中揭示一種藉由預 熱,用以自1,3-丙二醇中去除產生顏色之雜質之方法,其 較佳為以異質酸摧化劑,例如:過氟化離 將催化劑遽除,並再分離之以丙二醇,較佳為^ =空 蒸餾。自純化之二醇中製得之聚三亞甲醚二醇之入?11八值 為30-40,然而,未述及該聚合物之分子量。 聚亞烷基醚二醇之製備通常係藉由自相對應之亞烷基二 醇鲛催化性消去水或亞烷基氧化物之催化性開環。舉例言 之’聚三亞甲謎二醇之製備可藉由丙二醇之脫水或藉 由使用可溶性酸催化劑之二氧己烷之開環聚合。使用硫 酸,自甘油製造P03G之方法完整說明於美國專利公開^ 請案2002/0007043A1和2〇〇2/〇〇1〇374A1中,其均併列為本 文之參考。以此法製得之聚醚二醇可藉由此項技藝中已知 之方法加以純化。用於聚三亞甲醚二醇之純化方法典型係 包括.(1) 一個將聚合期間生成之酸酯類水解之水解步驟 (2)去除酸催化劑 '未反應單體、低分子量線形寡體和環醚 93l44.doc 類之募體之水萃 襞’以將存在之酸中(3)驗處理’典型係以氫氧化約 以去除殘餘之林2並㈣,及(4)將聚合物乾燥並過遽 咸已熟知由13 三亞甲驗二醇具有。二質酸催化性聚合縮合所生產之聚 上接受。聚合之t::!,特別是:其顏色無法為工業 = σ豸通常取決於原料·· PDO之品質。除了1359160 IX. INSTRUCTIONS: PRIORITY This application is filed on May 6, 2003, US Priority Application No. 60/468,228 and August 5, 2003. US Priority Application No. 1〇/634,61 Priority 1 is hereby incorporated by reference in its entirety. BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to the production of homotrim and copolymerization of polytrimethylene ether glycol having an excellent texture, particularly its color and functionality, which is preferably obtained by using propylene glycol. Renewable biological source. [Prior Art] 1,3·propanediol (hereinafter also referred to as "pD〇") is a single product which can be used for the production of various polymers including polyesters, polyurethanes, polyethers and cyclic compounds. The homogeneous and copolymeric mystery of polytrimethylene ether glycol (hereinafter also referred to as "p〇3G") is an example of such a polymer. The polymer can be used in a variety of applications, including: fibers, films. Et. The chemical route for the production of hydrazine, 3_propanediol is known. For example: 1,3-propanediol can be prepared from: 1. Ethylene oxide 9, in the catalyst and phosphine, water, carbon monoxide, hydrogen and an acid In the presence of ("hydroquinone pathway") 2) acrolein catalytic solution phase hydration and then reduction of acrolein pathway ") Both of these pathways for the formation of 1,3-propanediol involve interproducing products Synthesis of 3-hydroxypropanal (hereinafter referred to as "ΗΡΑ"). Reduction of hydrazine to PDO in the final catalytic hydrogenation step. Subsequent final purification involves several procedures, including 93144.doc 1359160 including vacuum evaporation. Biochemical pathway for the production of 1,3-propanediol It has been stated that it utilizes bio-raw raw materials and renewable resources, such as corn raw materials. These pDs are referred to hereinafter as "biochemical PDO". For example, bacterial strains which convert glycerol to 1,3-propanediol have been found, for example, in the genus Klebsiella, Citr〇 bacter, Clostridium. And Lactobacillus. This technique is disclosed in a number of patents, including U.S. Patent Nos. 5,633,362, 5,686,276, and 5,821, the entire disclosure of each of each of In particular, Nagarajan et al. disclose a biological method for producing 1,3-propanediol from glycerol using recombinant organisms. The method uses a heterogeneous pdu diol hydrogenase gene transformation, which has a specific Escherichia coli (E. coh) for hydrazine and 2-propanediol. The transformed Escherichia coli was grown in a medium containing glycerol as a carbon source and propylene glycol was separated from the growth medium. Since both bacteria and yeast can convert glucose (eg, corn sugar) or other carbohydrates to glycerol, the method of the invention provides a fast, inexpensive, and environmentally friendly polyester, polyether, and other polymerization. The source of the production of 3-propylene glycol monomer. The early precipitation method (e.g., propylene glycol and delayed or other materials) has been used to separate colored and odorous ingredients from desired products (e.g., enzymes) to obtain purified preparations. The precipitation of high molecular weight constituents from the fermentation broth and the bleaching of these components with a reducing agent (DE 39i7645) are known. In addition, micro (four) and then nanometer to remove residual compounds is also known to help (listen 7529), which molecular weight is higher than the separation size of 93l44.doc 1359160 ^ can be gone m, nano too _ will be very It is blocked quickly and its cost is high. Various processing methods have been disclosed in the prior art to remove color precursors present in pD〇t, however, such methods are laborious, expensive, and add to the cost of the polymer. For example, Kelsey, U.S. Patent No. 5,527,973 discloses a method for providing purified 1,3-propanediol which can be used as a starting material for light colored polyester. This method has several drawbacks, including: the use of a variety of preparations and the need to dilute with large amounts of water, which is difficult to remove from the product. A method for removing color-producing impurities from 1,3-propanediol by preheating, which is preferably a heterogeneous acid catalyzing agent, for example, perfluorination, is disclosed in U.S. Patent No. 6,235,948. The catalyst is removed by crystallization and further separated by propylene glycol, preferably ^ = empty distillation. The addition of polytrimethylene ether glycol prepared from the purified diol? 11 octagonal value is 30-40, however, the molecular weight of the polymer is not mentioned. The polyalkylene ether glycols are typically prepared by catalytically eliminating the catalytic ring opening of water or alkylene oxides from the corresponding alkylene glycol oxime. For example, the preparation of polytrimethylene glycol can be carried out by dehydration of propylene glycol or by ring opening polymerization of dioxane using a soluble acid catalyst. The use of sulphuric acid to produce P03G from glycerol is fully described in U.S. Patent Publication No. 2002/0007043 A1 and U.S. Patent Application Serial No. 2,374, the entire disclosure of each of which is incorporated herein by reference. The polyether diols prepared in this manner can be purified by methods known in the art. The purification method for polytrimethylene ether glycol typically includes: (1) a hydrolysis step for hydrolyzing an acid ester formed during polymerization (2) removal of an acid catalyst 'unreacted monomer, low molecular weight linear oligomer and ring The water extract of the ether of the 93l44.doc class is treated with the acid in the presence of the acid (3), which is typically treated with hydroxide to remove residual forest 2 and (4), and (4) the polymer is dried and passed. It is well known that it has 13 trimethacrylates. The polycondensation produced by the catalytic polymerization of the dicarboxylic acid is accepted. Polymerization t::!, in particular: its color cannot be industrial = σ豸 usually depends on the quality of the raw material · PDO. apart from

原枓之外,聚人 貝陈J 某種程产之柏二,之條件和聚合物之安定性亦與變色有 木m枉度之相關性。 _ _ '在聚二亞曱醚二醇之例中,聚醚In addition to the original sputum, the conditions of the cypress and the stability of the polymer are also related to the discoloration. _ _ 'In the case of polydiethylene ether glycol, polyether

—醇傾向具有I®科+ & A 欲。_ _ s工 顏色,此特性為許多終端用途所不 t二亞甲喊二醇作六 醇艮今易因與氧或空氣接觸而變色,特 別疋在向溫之下,始a ▲ 將聚&作用於通氮氣之下進行並將聚 趟一醇貯存於純氣存. 、在之下。另一種預防方法、為加入低濃 1 之適當抗氧化劑。較佳者為丁基㈣f苯(BHT,2,6-第—丁基_4-甲基酚),其濃度為1〇〇5〇〇微克/公克聚 ii| 〇 、再者,藉由傳統方式以減輕聚三亞甲醚二醇的顏色之嘗 試並無太多成功的例子。例如:M〇rris等人,美國專利第 2’520,733號指出在酸催化劑存在之下,自pD〇聚合生成聚 一亞甲醚二醇時之獨特變色傾向。他們嘗試之許多方法均 無法改善聚三亞甲醚二醇之顏色,包括使用活性碳、活性 鋁、矽膠、單獨過濾和單獨氫化。結果,他們研發出一種 用以於酸催化劑(2.5至6%重量比;)存在且溫度為約175°c至 200 C之下,將自ι,3-丙二醇製得之聚醇純化之方法。該純 化方法,步及將t合物通過漂白土earth)過遽,再 93144.doc 1359160 加以氫化。此等大量純化方法可得到淡黃色之終產物,事 實上,此权序製得之聚三亞甲醚二醇(其中之實例χι)之顏 色僅降至8號色度(Gardner),其色質相當於ΑρΗΑ值>3〇〇且 總體上不適於現今之需求。- Alcohol tends to have I® family + & A desire. _ _ s work color, this feature is not used for many end uses. The second propylene diol is used as the hexahydrin. It is easy to change color due to contact with oxygen or air, especially when it is under temperature, a ▲ will be poly & The action is carried out under nitrogen and the polydecyl alcohol is stored in pure gas. Another preventive method is to add a low concentration of appropriate antioxidant. Preferred is butyl (tetra)f benzene (BHT, 2,6-butyl- 4-methylphenol), the concentration of which is 1 〇〇 5 〇〇 microgram / gram poly ii | 〇, again, by tradition There are not many successful examples of ways to reduce the color of polytrimethylene ether glycol. For example, M 〇rris et al., U.S. Patent No. 2,520,733, teaches a unique tendency to discolor from the polymerization of pD oxime to form polymethylene ether glycol in the presence of an acid catalyst. Many of the methods they tried did not improve the color of polytrimethylene ether glycol, including the use of activated carbon, activated aluminum, silicone, separate filtration, and separate hydrogenation. As a result, they developed a method for purifying a polyol prepared from i,3-propanediol in the presence of an acid catalyst (2.5 to 6% by weight;) at a temperature of about 175 ° C to 200 ° C. The purification process, stepwise and passing the t compound through the bleaching earth earth, is then hydrogenated by 93144.doc 1359160. Such a large number of purification methods can give a pale yellow final product. In fact, the color of the polytrimethylene ether glycol (in which example ι) obtained by this weighting is only reduced to the No. 8 color (Gardner), and its color quality. Equivalent to ΑρΗΑ value>3〇〇 and generally not suitable for today's needs.

Mason在美國專利第3,326,985號中揭示一種用以製備分 子里範圍為1200-U00且具有改善之顏色之程序,其藉由 於通氮之下,以真空抽除低分子量之聚三亞甲醚二醇。然 而,其色度並無定量且應無法達到上述需求。 【發明内容】 本發明提供一種方法,其包含使1,3-丙二醇與一種適當 之聚合催化劑接觸以產生聚三亞曱醚二醇,其中該丨,3-丙 二醇,於接觸之前,包含約1〇微克/公克或更少之過氧化 化合物,以1,3-丙二醇之重量為基準。較佳者,該^丙 二醇包含約1〇〇微克/公克或更少之羰基化合物,以pD〇之 重量為基準。亦較佳者,該u·丙二醇包含約1〇〇微克/公 克或更少之單官能基醇化合物,以PDO之重量為基準β 除非另有陳述,所以百分比、份數、比例等均為重量 比。商標顯示為大寫。 另外,若含量、濃度或其他數值或參數以範圍、較佳之 範圍Μ出較佳之較高值及較佳之較低值表示時,咸知其 係特疋揭7F由任意上㈣較佳值與任意下限或較佳值之任 〜配對之形成之所有範圍,無論該範圍 本發明係針對自經(酸)催化…二醇之聚:揭二生 產優異質地之聚三亞甲喊二醇。本發明者群目前發現自石 93144.doc 1359160 化途徑製造之丙二醇並不夠良好以生產高品質p⑽聚 合物:此乃因雜質之存在,例如:幾基化合物例如:經 基丙路、不確定構造之過氧化物生成性化合物 醇(例如:2·幾乙美η _条& 早Β此基 &乙基-1,3-一氧烷,下文中稱之為"hed”), 及可以PH測定谓測之酸性化合物。單官能基醇類在聚合做 X作為鏈終止劑,其可插人聚合物中作為可影響聚合物 吕月b丨生之終止端點"。單官能基醇類可能與顏色之生成有 :無關 '然而’一般而言,羰基化合物常與顏色體有關, 吾人可預期羰基數目愈多,則顏色會愈深。上述之某些 PDO中之雜質可在酸催化性聚合製程中產生顏色。 根據第一方面,本發明包含使^夂丙二醇與—種適當之 聚合催化劑接觸以生產聚三亞甲醚二醇,其中該丙二 醇於接觸之前,包含約10微克/公克或更少之過氧化化合 物,以1,3-丙二醇之重量為基準。一般而言,烯烴類、醚 類和烯丙基類易於形成過氧化物,且所形成之過氧化物之 測定可利用市售可購得之試片或藉由此項技藝中已知之碘 還原滴定法。 根據本發明之另一方面,1,3-丙二醇進一步包含約1〇〇微 克/公克或更少之羰基化合物’以PDO之重量為基準。較佳 者’該PDO包含約75微克/公克或更少,更佳為約5〇微克/ 公克或更少,最佳為約25微克/公克或更少之艘基化合 物’以PDO之重量為基準。幾基化合物之說明性實例為經 基丙醛和以縮醛形式存在之醛類,例如:由3·羥基丙駿與 1,3 -丙二醇反應而得之縮酿。幾基含量之測定可藉由以此 93144.doc 11 1359160 項技藝中已熟知之方式’將羰基化合物轉化成二硝基苯腙 之後再以uv偵測之。 根據本發明之另一方面,1,3-丙二醇進一步包含約1〇〇微 克/公克或更少之單官能基醇化合物,以PD〇之重量為基 準。較佳者,該PDO包含約75微克/公克或更少,更佳為約 50微克/公克或更少,最佳為約25微克/公克或更少之羰基 化合物’以PDO之重量為基準。單官能基醇化合物之說明 性實例為HED及3 -經基四氫η比鳴。 根據本發明之另一方面,1,3 -丙二醇包含至少99.95%之 該二醇,即:其純度至少為99.95%。 根據本發明之另一方面,1,3 _丙二醇與等重量之水之混 合物之PH("50/50 pH")界於6.0至7·5,較佳為界於6〇及 7.0 〇 根據本發明之另一方面,本發明提供—種方法,其包含 使一種生化衍生之1,3 -丙二醇與一種適當之聚合催化劑接 觸以產生聚三亞曱醚二醇,其中該^·丙二醇之5〇/5〇 pH 為6.0-7.5且包含約1〇0微克/公克或更少之羰基化合物、約 1〇微克/公克或更少之過氧化化合物和約1〇〇微克/公克或更 少之單官能基醇化合物,以PDO之重量為基準。 本發明已發現,若以含低量之此等雜質,特別是彼等低 於本文中才曰出之下限者作為起始原料,可實質上整體減少 或消除PDO和P〇3G之後續處理之需求。較佳者,該pD〇係 為生化衍生的PDO(生化衍生性p最佳者,使用於根據本 發明之方法中之PD0係衍生自上述之生物性及可再生性來 93J44.doc -12- 1359160 源,即.係製備自發酵製程及玉米原料。 根據本發明之另一方面,一種組合物包含·生化衍生之 1,3丙一醇’其中該匕弘丙二醇包含約⑺^微克/公克或更少 之Ik基化合物、約10微克/公克或更少之過氧化化合物和 約1〇〇微克/公克或更少之單官能基醇化合物,以u丙二 醇之重里為基準。根據本發明之再另一方面,聚三亞甲醚 二醇係衍生自生化魅之m醇之聚合作用。 較佳者,根據本發明所使用之1,3-丙二醇之色值低於約 10APHA。較佳者,根據本發明所使用之u-丙三醇之色值 低於約5APHA。APHA顏色之測定係說明於下文之試驗方 法1中。 一種簡單之程序可提供確認用於P03G生產之PDO品質 之快速方法,其可不需使用耗時之步驟生產p〇3G。該方 法端賴於發現PD〇中可造成P〇3G之顏色生成之雜質會在 加速性酸熱試驗(AAHT,試驗方法6)之溫和條件之下快速自 我顯現。AAHT法涉及一段與硫酸(PD〇重量之1%)短暫共 熱之時期。該加熱時間為1〇分鐘,在17〇〇c之下。因此, AAHT法可將顏色前驅物轉化成顏色,但不發生顯著之聚 醚二醇生成。較佳者,PD〇經AAHT後之色值低於約15 APHA。較佳者,PDCmAAHT後之色值低於約ι〇 ApHA。 從本發明之PDO製得之P03G可為同型或共聚物。舉例 言之’ PDO可與其他雙醇類(如下)聚合以製造共聚物。 可用於本發明之PD〇共聚物可含有至多為5〇%重量比(較 佳為20%重量比或更少)之除丨,3_丙二醇之外之共聚單體二 93144.doc 13 1359160 醇及/或其暴體。適用於此方 戍甲之共聚單體_ 肪族二醇,例如:乙烯二醇 蒞―%包括脂 1,〇-己一醇、1 7 I* π辛二醇…二醇、U〇-癸二醇、U2= 知 3’3’4’4’5’54U,5j:,'2,2,3:~ 1,6-己二醇、’,W-八虱- 丨ί ,7’7’8,8,9,9,10,1〇,-十丄蠢 1,12-十二烷二醇,璜灿t ’丁 虱-A procedure for preparing a molecular weight in the range of 1200-U00 and having an improved color is disclosed in U.S. Patent No. 3,326,985, the disclosure of which is incorporated herein by reference. However, its chromaticity is not quantitative and should not meet the above requirements. SUMMARY OF THE INVENTION The present invention provides a process comprising contacting 1,3-propanediol with a suitable polymerization catalyst to produce a polytrimethylene ether glycol, wherein the oxime, 3-propanediol comprises about 1 Torr prior to contacting. Micrograms per gram or less of peroxidic compound based on the weight of 1,3-propanediol. Preferably, the propylene glycol comprises a carbonyl compound of about 1 μg/g or less, based on the weight of pD〇. Also preferably, the u-propanediol comprises a monofunctional alcohol compound of about 1 μg/g or less, based on the weight of the PDO. Unless otherwise stated, the percentages, parts, ratios, etc. are weights. ratio. Trademarks are shown in uppercase. In addition, if the content, concentration or other value or parameter is expressed by a range, a preferred range, and preferably a higher value, and preferably a lower value, it is known that it is a preferred value and an arbitrary value. The lower limit or the preferred value is any range of the formation of the pairing, regardless of the range. The present invention is directed to the production of a polytrimethylene diol which is excellent in texture by the polymerization of a (acid) catalyzed diol. The present inventors have found that propylene glycol produced from the stone 93144.doc 1359160 process is not good enough to produce high quality p(10) polymers: this is due to the presence of impurities, such as: a few base compounds such as: propyl group, uncertain structure a peroxide-forming compound alcohol (for example, 2···································· The acidic compound can be measured by pH. The monofunctional alcohol is polymerized as X as a chain terminator, and its insertable polymer can be used as a terminating end point which can affect the polymer Lu Yue b. Monofunctional group Alcohols may be associated with color formation: nothing. However, in general, carbonyl compounds are often associated with color bodies. The more we can expect the number of carbonyl groups, the darker the color. The impurities in some of the above PDOs can be in acid. The color is produced in a catalytic polymerization process. According to a first aspect, the invention comprises contacting propylene glycol with a suitable polymerization catalyst to produce polytrimethylene ether glycol, wherein the propylene glycol comprises about 10 micrograms per gram prior to contacting. or A small amount of peroxidic compound based on the weight of 1,3-propanediol. In general, olefins, ethers and allyls are easy to form peroxides, and the peroxides formed are commercially available. Commercially available test strips or by iodine reduction titration known in the art. According to another aspect of the invention, the 1,3-propanediol further comprises about 1 microgram per gram or less of carbonyl compound The weight of the PDO is based on. Preferably, the PDO comprises about 75 micrograms per gram or less, more preferably about 5 micrograms per gram or less, and most preferably about 25 micrograms per gram or less of the base compound. 'Based on the weight of PDO. Illustrative examples of a few base compounds are acetal aldehydes and aldehydes in the form of acetals, for example, the reaction of 3 hydroxypropyl and 1,3-propanediol The determination of the number of bases can be detected by uv after conversion of the carbonyl compound to dinitrophenylhydrazine in a manner well known in the art of 93144.doc 11 1359160. According to another aspect of the invention, 1,3-propanediol further comprises about 1 μg/m Or less monofunctional alcohol compound based on the weight of PD. Preferably, the PDO comprises about 75 micrograms per gram or less, more preferably about 50 micrograms per gram or less, most preferably about 25 μg/g or less of the carbonyl compound 'based on the weight of the PDO. Illustrative examples of the monofunctional alcohol compound are HED and 3-tetrahydropyrene oxime. According to another aspect of the invention, 1, 3-propanediol comprises at least 99.95% of the diol, i.e., has a purity of at least 99.95%. According to another aspect of the invention, the pH of the mixture of 1,3-propanediol and an equal weight of water ("50/50 pH" The invention is in the range of 6.0 to 7.5, preferably 6 〇 and 7.0 〇. According to another aspect of the invention, the invention provides a method comprising the step of formulating a biochemically derived 1,3 -propanediol The polymerization catalyst is contacted to produce polytrimethylene ether glycol, wherein the propylene glycol has a pH of 6.0 to 7.5 and contains about 10,000 micrograms per gram or less of carbonyl compound, about 1 microgram/ a gram or less peroxy compound and a monofunctional alcohol of about 1 μg/g or less Thereof, with reference to the weight of the PDO. The present inventors have discovered that the subsequent treatment of PDO and P〇3G can be substantially reduced or eliminated substantially as a starting material with a low amount of such impurities, particularly those lower than those specified herein. demand. Preferably, the pD oxime is a biochemically derived PDO (biochemically derived p-optimal, the PD0 system used in the method according to the invention is derived from the above-mentioned biological and regenerative properties 93J44.doc -12- 1359160 Source, ie, prepared from a fermentation process and corn raw material. According to another aspect of the invention, a composition comprises a biochemically derived 1,3 propanol wherein the hydrazine propylene glycol comprises about (7) μg/g or Fewer Ik-based compounds, about 10 μg/g or less peroxy compound, and about 1 μg/g or less of a monofunctional alcohol compound based on the weight of u-propanediol. According to the present invention In another aspect, the polytrimethylene ether glycol is derived from the polymerization of a biol of the biochemical. Preferably, the 1,3-propanediol used in accordance with the present invention has a color value of less than about 10 APHA. Preferably, according to The color value of u-glycerin used in the present invention is less than about 5 APHA. The determination of the color of APHA is described in Test Method 1 below. A simple procedure provides a rapid method for confirming the quality of PDO for P03G production, It does not require time-consuming steps Production of p〇3G. This method relies on the discovery that the impurities in the PD〇 which can cause the color generation of P〇3G will rapidly manifest themselves under the mild conditions of the accelerated acid heat test (AAHT, Test Method 6). The AAHT method involves A period of transient heat-up with sulfuric acid (1% of PD〇 weight). The heating time is 1 〇 minutes, below 17 〇〇c. Therefore, the AAHT method can convert the color precursor into color, but does not occur significantly. Preferably, the color value of the PD 〇 after AAHT is less than about 15 APHA. Preferably, the color value after PDCmAAHT is less than about ι ApHA. P03G obtained from the PDO of the present invention. It may be a homo- or copolymer. For example, 'PDO may be polymerized with other diols (see below) to produce a copolymer. The PD-based copolymer useful in the present invention may contain up to 5% by weight (preferably 20) % by weight or less), comonomer other than 3_ propylene glycol II 93144.doc 13 1359160 Alcohol and / or its violent body. Suitable for the comonomer of this side armor _ aliphatic diol, For example: ethylene glycol-% includes fat 1, 〇-hexanol, 17 I* π octanediol... diol, U 〇 -decanediol, U2= know 3'3'4'4'5'54U, 5j:, '2,2,3:~ 1,6-hexanediol, ',W-gossip- 丨ί ,7 '7'8,8,9,9,10,1〇,- 十丄 stupid 1,12-dodecanediol, 璜灿 t '丁虱-

醉%狀月曰肪族二醇H 醇、環己烧二甲醇和異山梨醇,多㈣7己二 如:甘油、三經甲基丙院和戊赤蘚糖醇。/聚單^物,例 較佳群組係選自由下列所組成之群組· 2^體-每之 醇、2,2-二甲基-^-丙二醇、22_二 土 _1,3-丙二 乙基-2-(羥甲基H,3_丙二醇、;一 :]’3-丙二醇、、 ι’ιο-癸二醇、異山梨醇’及其混合物。以 可用者。熱安定劑、抗氧k #ί 10—醇係特別 聚合混合物或最終聚合物中。 硯需要破加至 在一些例子中,可一 J月匕某要使用尚達10%或以上之 量寡體,倘若其可取犋。± -刀予 』取仵。因此,較佳之起始原料包 丙一酵與其雙體和三聚F β县J. —歎體。最佳之起始原料包含90%重 比或以上之1,3-丙二醇,較佳為99%重量比或以上。 用以自PDO生產+ + 座〇3G之方法為此項技藝中普遍已知 者。例如:美國專利第2,52〇,733號,其併列為本文之參 考,揭示聚三亞甲醚-轳 %之聚合物及共聚物及一種用以在 脫水催化^ ’例如:破、無機酸(例如:硫酸)和有機醆存 在之下’自1,3-丙二醇製備此等聚合物之方法。 ^亞曱鍵醇之製備係較佳藉由一種酸催化性之1,3 · 93144.doc •14- 1359160 丙二醇之聚合縮合作用,如說心美國公開專利申 腫_〜和2_㈣辦,此二者均併列為本文^ 參考。聚三亞甲醚二醇之製備亦可藉由環醚類、環氧烷之 開環聚合作用”ymer Sci,ρ〇1_⑽恤 28, 429_444(1985)之說明,其亦併列為本文之參考。i ^ 丙二醇之聚合縮合較佳為使用環氧貌。如需#,則藉由本 發明之方法製備之聚醚二醇可藉由此項技藝中已知之方式 進-步純化以去除存在之酸。咸應知道在某些應用中,該 產物可不需進一步純化而被使用。然而,純化程序可顯著 改善聚合物質地及功能性且其係由下列所組成:(1)一個在 聚合期間將酸酯類水解之水解步驟其(2)典型為⑷去除 酸、未反應之單體、低分子量線形寡體及環酯之寡體之水 萃取步驟,(b)—種固態鹼之處理以中和存在之殘餘酸和 (c)將聚合物乾燥及過滤以去除殘留之水和固體。 從本發明之PDO製造之P03G之色值較佳為低於約5〇 APHA。更佳者,該p〇3G之色值係低於約3〇 APHA。較佳 者,使用本之PDO單體/募體所製造之p〇3G產物之分子量 為約250至約5000,較佳為約5〇〇至約4〇〇〇,且最佳為約 1000至約 3000。 本發明之方法可提供具有改良之功能性及聚合物顏色之 聚三亞甲醚二醇》 材料及試驗方法 試驗方法1.APHA值之測定 使用 Hunterlab ColoQuest分光色度計(Reston, VA)測定 93144.doc -15 - 1359160 PD〇和聚合物之顏色。顏色號碼之測定係根據ASTM D-1209以APHA表示(鉑-鈷系統)。聚合之分子量係計算自其 藉由滴定法所得之羥基數目。 試驗方法2. n>〇含量和HED之測定(藉由氣相層析法) 將未..二稀釋之PD〇樣品注入裝有wax(例如:Phenomenex Zorbax Wax、DB-Wax、UP Innowax或同等物)毛細管柱及 火燄離子化偵測器(FID)之氣相層析儀中。FID會隨時間函 數產生與分析物之濃度呈正比之訊號,並將該訊號擷取至 積分儀或以x,y數據貯存於電腦中。各個被分離並偵測之 成份於sfl號對時間作圖時均呈現為一"波峰"。假設所有雜 質在FID上之重量%反應因子均與pD〇相同。%純度係以% 面積計算。偵測下限為:5微克/公克。 試驗方法3羰基含量之測定(藉由分光光度分析) 於分光光度計定量之前,先將羰基化合物轉化成二硝基 苯基腙。偵測下限為:2微克/公克。 試驗方法4過氧化物含量之測定 使用市售可購得之過氧化物試驗片,〇 5_25微克/公克 EM Quant®或碘還原滴定法測定pd〇中之過氧化物。滴定 法涉及將5公克之樣品加至5 〇毫升之2 _丙醇/醋酸溶液中並 再以0.01 N硫代硫酸鈉溶液滴定該溶液。偵測下限為:〇 5 微克/公克。若使用試驗片,則可藉由將樣品稀釋至5_25微 克/公克之範圍定量濃度大於25微克/公克者或者使用針對 較高濃度設計之試驗片。 試驗方法5 pH之測定(pH顯示對數標尺上之酸性雜質含量) 93144.doc -16- 1359160 使用PDO與蒸餾水50:50之混合物,以pH計測定該溶液 之pH。 試驗方法6 AAHT流程 將PDO( 150公克)及1.5公克之濃硫酸倒入250毫升之三頸 燒瓶中。於氮氣中,將該溶液進行機械性攪拌並再加熱至 1 70 °C 10分鐘。10分鐘之後,將該溶液冷卻至室溫並根據 試驗方法1測定其顏色。 【實施方式】 實例1_3 1,3-丙二醇可購自兩種石化途徑。杜邦公司從丙烯醛開 始製造1,3-丙二醇;PDO亦可得自環氧乙烷來源。杜邦亦 使用衍生自玉米之葡萄糖作為一種可再生性原料來製造 1,3-丙二醇。如上述方法之說明,分析來自各種合成途徑 之PDO樣品之PDO含量、2-羥乙基-1,3-二氧烷(HED)含 量、幾基含量、過氧化物含量和酸度。其結果顯示於表 1。測定PDO經AAHT程序之前和之後之APHA值並將其結 果顯示於表2。 表1 : 1,3-丙二醇之化學分析 實例 PDO之 原料 PDO 之純度 % HED 微克/公克 羰基 微克/公克 過氧化物 微克/公克 Ph 50/50 1 玉米 99.997 ND* ND* ND* 6.82 2 丙烯經 99.968 80 93 56 4.87 3 學氧乙烷 99.917 310 198 ND* 5.88 ND*不可測得(參見試驗方法之極限) 93144.doc 1359160 表1之結果指出:相較於衍生自石化途徑之PDO,源自 生化途徑之PDO具有最高之純度且含有最少之雜質。 表2· 1,3-丙二醇於i7〇°c之下以酸處理1〇分鐘之變色狀況 實例 PDO 之原料 AAHT之前 之PDO顏色 (APHA) AAHT之後 之PDO顏色 (APHA) 1 玉米 3 8 2 丙稀酸 3 50 3 環氧乙烷 4 14Intoxication of the genus Acacia diol H alcohol, cyclohexane dimethanol and isosorbide, more (four) 7 hexanes such as: glycerol, tri-methyl propyl acetate and erythritol. / 聚单物,优选优选的 groups are selected from the group consisting of: 2 ^ - each alcohol, 2,2-dimethyl-^-propanediol, 22_ two soil _1,3- Propyldiethyl-2-(hydroxymethyl H,3-propylene glycol, ; 1:] '3-propanediol, ι'ιο-decanediol, isosorbide' and mixtures thereof. Available. Thermal stabilizer , anti-oxidation k # 10 10 - alcohol in a special polymerization mixture or in the final polymer. 砚 need to be broken into, in some cases, a certain amount of oligos that can be used up to 10% or more, if可 刀 ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± ± The 1,3-propanediol, preferably 99% by weight or more. The method for producing + + 〇 3G from PDO is generally known in the art. For example, U.S. Patent No. 2, 52, 733 No., which is incorporated herein by reference, discloses a polytrimethylene ether-轳% polymer and copolymer and a catalyst for dehydration catalysis such as: broken, inorganic acid (eg sulfuric acid) and organic hydrazine 'Methods for preparing such polymers from 1,3-propanediol. ^Preparation of the hydrazine linkage is preferably carried out by polymerization condensation of an acid-catalyzed 1,3 · 93144.doc • 14-1359160 propylene glycol, such as Speaking of the US public patents, swollen _~ and 2_(four), both of which are listed as reference. The preparation of polytrimethylene ether glycol can also be achieved by ring-opening polymerization of cyclic ethers and alkylene oxides. , ρ〇1_(10) shirt 28, 429_444 (1985), which is also incorporated herein by reference. The polymerization condensation of i ^ propylene glycol is preferably the use of epoxy. If required, the polyether prepared by the method of the invention The diol can be further purified by methods known in the art to remove the acid present. It should be understood that in certain applications, the product can be used without further purification. However, the purification procedure can significantly improve the polymer quality. It is composed of the following: (1) a hydrolysis step for hydrolyzing an acid ester during polymerization, (2) typically (4) removal of acid, unreacted monomer, low molecular weight linear oligo and ring Water extraction step of ester oligo, (b) - The solid base is treated to neutralize the residual acid present and (c) the polymer is dried and filtered to remove residual water and solids. The color value of P03G produced from the PDO of the present invention is preferably less than about 5 〇 APHA. More preferably, the p〇3G has a color value of less than about 3 APHA. Preferably, the p〇3G product produced using the PDO monomer/collector has a molecular weight of from about 250 to about 5,000. Preferably, it is from about 5 Torr to about 4 Torr, and most preferably from about 1000 to about 3000. The process of the present invention provides a polytrimethylene ether glycol material having improved functionality and polymer color. Test Method 1. Determination of APHA Value The color of 93144.doc -15 - 1359160 PD 〇 and polymer was determined using a Hunterlab ColoQuest spectrophotometer (Reston, VA). The color number is determined by APHA according to ASTM D-1209 (platinum-cobalt system). The molecular weight of the polymerization is calculated from the number of hydroxyl groups obtained by titration. Test Method 2. n> Determination of strontium content and HED (by gas chromatography) A sample of two diluted PD 注入 was injected into a wax (for example: Phenomenex Zorbax Wax, DB-Wax, UP Innowax or equivalent) In a gas chromatograph of a capillary column and a flame ionization detector (FID). The FID will generate a signal proportional to the concentration of the analyte over time and capture the signal to the integrator or store it in the computer with x, y data. Each component that is separated and detected appears as a "Crest" when the sfl number is plotted against time. It is assumed that the weight % response factor of all impurities on the FID is the same as pD〇. % purity is calculated in % area. The detection limit is: 5 μg / g. Test Method 3 Determination of carbonyl content (by spectrophotometric analysis) The carbonyl compound is converted to dinitrophenyl hydrazine prior to quantification by a spectrophotometer. The detection limit is: 2 μg / g. Test Method 4 Determination of peroxide content The peroxide in pd〇 was determined using a commercially available peroxide test piece, _ 5_25 μg/g EM Quant® or iodine reduction titration. The titration method involves adding a 5 gram sample to 5 mM of a 2-propanol/acetic acid solution and titrating the solution with a 0.01 N sodium thiosulfate solution. The detection limit is: 〇 5 μg / g. If a test piece is used, it can be quantified by diluting the sample to a concentration of 5-25 μg/g to a concentration greater than 25 μg/g or using a test piece designed for a higher concentration. Test Method 5 Determination of pH (pH shows the content of acidic impurities on a logarithmic scale) 93144.doc -16- 1359160 The pH of the solution was measured by a pH meter using a mixture of PDO and distilled water of 50:50. Test Method 6 AAHT Process PDO (150 g) and 1.5 g of concentrated sulfuric acid were poured into a 250 ml three-necked flask. The solution was mechanically stirred under nitrogen and heated to 1 70 ° C for 10 minutes. After 10 minutes, the solution was cooled to room temperature and its color was determined according to Test Method 1. [Examples] Example 1_3 1,3-propanediol was purchased from two petrochemical routes. DuPont manufactures 1,3-propanediol from acrolein; PDO can also be derived from ethylene oxide. DuPont also uses glucose derived from corn as a renewable raw material to make 1,3-propanediol. The PDO content, 2-hydroxyethyl-1,3-dioxane (HED) content, minority group content, peroxide content, and acidity of the PDO samples from various synthetic routes were analyzed as described in the above methods. The results are shown in Table 1. The APHA values of PDO before and after the AAHT procedure were determined and the results are shown in Table 2. Table 1: Chemical analysis of 1,3-propanediol Example PDO purity of raw material PDO % HED Microgram / gram carbonyl microgram / gram peroxide microgram / gram Ph 50 / 50 1 Corn 99.997 ND* ND* ND* 6.82 2 Propylene 99.968 80 93 56 4.87 3 Oxygenethane 99.917 310 198 ND* 5.88 ND* not measurable (see limits of test methods) 93144.doc 1359160 The results of Table 1 indicate: compared to PDO derived from the petrochemical pathway, derived from The biochemical pathway of PDO has the highest purity and contains the least amount of impurities. Table 2. Discoloration of 1,3-propanediol treated with acid at i7〇°c for 1 minute. Example PDO raw material PDO color before AAHT (APHA) PDO color after AAHT (APHA) 1 Corn 3 8 2 C Dilute acid 3 50 3 ethylene oxide 4 14

表2顯示實例1中之pD〇於AAHT試驗之後之變色最少, 其暗不當中並無顏色前驅物類雜質。丙烯醛基底性丨,3-丙 二醇之純度較環氧乙烷基底性二醇更高且含有較少之羰基 化合物(如表1所示)。然而,丙烯醛基底性二醇在aaht法 中之良色度較強,其代表相對較高濃度之顏色前驅物類雜 質之存在。由過氧化物之存在亦證明此等pD〇中含有過氧 化物生成性化合物。Table 2 shows that the pD in Example 1 has the least discoloration after the AAHT test, and there is no color precursor impurity in the dark. The acrolein-based oxime, 3-propanediol, is higher in purity than the ethylene oxide base diol and contains less carbonyl compound (as shown in Table 1). However, the acrolein-based diol has a stronger color in the aaht method, which represents the presence of a relatively high concentration of color precursor-type impurities. It was also confirmed by the presence of a peroxide that these pD〇 contained a peroxide-generating compound.

實例4自生化衍生的pD〇製備p〇3G 如下述說明,使用自生化途徑取得之U3·丙二醇來 聚合物: 將 個22公升 現瓶接 個氮氣入口及 蒸館頭,並倒入8392公克之丨,3_丙二醇。以1〇公升/分舍 速度在液體中打人氮氣並進行約15分鐘之機械性授掉3 用以燒瓶下方之磁攪拌器驅動之攪拌子卜"分鐘之種 經由其卜接口以分液漏斗在至少5分鐘之時間内慢憎 93144.doc -18- 1359160 低加入76.35公克之«。完成之後,將15公克之pD〇加至 分液漏斗中並旋轉以去除任何殘留之硫酸。將其加入燒瓶 中。攪拌此愿合物並如上述吹氣並加熱至16〇t。藉由某 館去除反應之水並於聚合反應期間連續收^使該反應持 續38.5小時,之後將之冷卻(持續授拌及吹氣)至4代。所 得之粗聚合物以NMR測得之平均分子量為213〇且八舰顏 色為59。 將該粗物質如下述水解。將該粗聚合物與等體積之蒸館 水加至-個22公升之5頸圓底燒瓶中(接上冷凝器及機械性 攪拌器)。將此混合物進行機性授拌,以約i5G毫升/分鐘之 速度吹入氮氣’並加熱至1〇(rc。將之迴流4小時,之後, 關掉加熱並使該混合物冷卻至价。中_拌並將吹氣降 至最小。在冷卻期間發生相分離。將水溶液相之水移除並 丟棄。將與原來等體穑 積之蒸餾水加至留在燒瓶内之濕聚合 物中0混合、吹氣並再加敎 …、至100 c 1小日卞,之後,關掉加 …並使該物質如前述—般冷卻。將水相移除並吾棄。 藉由滴定法測定殘留夕β Μ β、 史留之硫酸並以過量之氫氧化鈣加以中 :“將聚合物於減麼之下以,c乾燥3小時並再通過預先 覆CELPURE C-65過遽助劑之^職滤紙加以過遽。 所得之純化聚合物以_測得之平均分子量為而且 APHA顏色為32。Example 4 Preparation of p〇3G from biochemically derived pD〇 As described below, the U3·propylene glycol obtained from the biochemical route was used to polymerize: a 22 liter bottle was placed in a nitrogen inlet and a steaming head, and poured into 8392 grams.丨, 3_ propylene glycol. The nitrogen is applied to the liquid at a speed of 1 liter liter per minute and mechanically transferred for about 15 minutes. 3 The magnetic stirrer driven by the flask is driven by a stirrer. The funnel is slowly raking 93144.doc -18- 1359160 for at least 5 minutes and adding 76.35 grams of «. After completion, 15 grams of pD was added to the separatory funnel and rotated to remove any residual sulfuric acid. Add it to the flask. The mixture was stirred and blown as above and heated to 16 Torr. The reaction was removed by a library and the reaction was continued for 38.5 hours during the polymerization, after which it was cooled (continuously stirred and blown) to 4 passages. The crude polymer obtained had an average molecular weight of 213 NMR and an eight-ship color of 59. This crude material was hydrolyzed as follows. The crude polymer and an equal volume of steamed water were added to a 22 liter 5-neck round bottom flask (with condenser and mechanical stirrer). The mixture was mechanically mixed, and nitrogen gas was blown at a rate of about i5 G ml/min and heated to 1 Torr (rc. It was refluxed for 4 hours, after which the heating was turned off and the mixture was cooled to a price. Mix and minimize the blowing. Phase separation occurs during cooling. The water of the aqueous phase is removed and discarded. The distilled water mixed with the original is added to the wet polymer remaining in the flask. Gas and add 敎..., to 100 c 1 day, then turn off the addition... and let the material cool as described above. Remove the water phase and discard it. Determine the residual ββ Μ β by titration , Shiliu sulphuric acid and an excess of calcium hydroxide: "The polymer is reduced, c dry for 3 hours and then passed through the CELPURE C-65 遽 遽 遽 遽 ^ 加以 加以 加以 加以 加以The resulting purified polymer had an average molecular weight of _ measured and an APHA color of 32.

實例S自1,3-丙二醇製锖p〇3G 如實例4之說明製備取 _ 備^合物’除了所使用之1,3-丙二醇係 衍生自丙稀搭途經。 93144.doc -19- 1359160Example S from 1,3-propanediol 锖p〇3G Prepared as described in Example 4 except that the 1,3-propanediol used was derived from propylene. 93144.doc -19- 1359160

實例6自1,3-丙二醇製備P03G 如實例4之說明製備聚合物,除了所使用之1,3-丙二醇係 衍生自環氧乙烷途徑。 表3 : P03G聚合物顏色 實例 PDO 之原料 粗聚合物 經純化之聚合物 Μη 顏色(ΑΡΗΑ) Μη 顏色(ΑΡΗΑ) 4 玉米 2130 59 2229 32 5 丙烯醛 2256 185 2341 157 6 環氧乙烷 2157 102 2170 109 表3顯示衍生自實例1之PDO之經純化P03G與衍生自其 他PDO之聚合物相較,其具有最低之色度。 93144.doc 20-Example 6 Preparation of P03G from 1,3-propanediol A polymer was prepared as described in Example 4 except that the 1,3-propanediol used was derived from the ethylene oxide route. Table 3: P03G polymer color example PDO raw material crude polymer purified polymer Μ color (ΑΡΗΑ) Μη color (ΑΡΗΑ) 4 corn 2130 59 2229 32 5 acrolein 2256 185 2341 157 6 ethylene oxide 2157 102 2170 109 Table 3 shows that purified P03G derived from PDO of Example 1 has the lowest chroma compared to polymers derived from other PDOs. 93144.doc 20-

Claims (1)

135^160 100年10月14日 十、申請專利範圍: 1· 一種製備聚三亞曱醚二醇之方法,其包含以下步驟: 知:供一 1,3 -丙一醇,其中該1,3 -丙二醇包含以1,3_丙 一醇(PDO)之重罝為基準1〇微克/公克或更少之過氧化化 合物’及100微克/公克或更少之羰基化合物;及 使該1,3-丙二醇與一酸聚合催化劑接觸以產生聚三亞 甲鍵二醇;其中該聚三亞甲醚二醇之顏色低於5〇 APHA。 2. 如請求項1之方法,其中該1,3-丙二醇進一步包含以pD〇 之重ϊ為基準100微克/公克或更少之單官能基醇化合 物。 3. 如請求項1之方法,其中該1,3-丙二醇之純度至少為 99.95% 〇 4. 如明求項1之方法’其中該1,3 -丙二醇包含生化衍生之 1,3 ·丙二醇。 5如請求項4之方法,其中該1,3-丙二醇係衍生自利用一種 可再生性生物來源之發酵製程。 6. 如明求項1之方法’其中該込弘丙二醇以1重量%之硫酸於 17〇C之下處理10分鐘後之色值低於15 APHA。 7. 如°月求項1之方法,其中該聚三亞甲醚二醇之分子量為 250至 5〇〇〇 0 8如°月求項1之方法’其中該聚三亞甲醚二醇包含同質聚 合物及/或共聚物。 9.如。月求項1之方法,其中該聚三亞甲醚二醇包含1,3-丙二 10 10 π. 12. 13. 14. 15. 醇與至少一種其他C6至Cl2二醇之共聚物。 •如請求項i之方法,其中該U·丙二醇之5〇/5〇阳為60· 7.5。 —種製備產生聚三亞甲醚二醇之方法,其包含以下步 驟: 使生化衍生之L 3 _丙二醇與一酸聚合催化劑接觸以產 生聚三亞曱醚二醇,其特徵在於,該丨,3_丙二醇之5〇/5〇 卩《:為6.〇-7.5且包含以1,3_丙二醇之重量為基準1〇〇微克/ 公克或更少之羰基化合物、1〇微克/公克或更少之過氧化 化合物和100微克/公克或更少之單官能基醇化合物;且 該聚三亞甲醚二醇之顏色低於50 APHA。 如請求項1或11之方法,其中該153_丙:醇之顏色低於1〇 APHA ^ 一種聚三亞曱醚二醇,其係藉由提供1,3-丙二醇及聚合 催化劑並以該聚合催化劑將丨,3·丙二醇聚合以形成聚三 亞甲醚一醇而製得,其中該丨,3_丙二醇包含以1,3 -丙二醇 之重里為基準100微克/公克或更少之羰基化合物、10微 克/ △克或更少之過氧化化合物和1〇〇微克/公克或更少之 單官能基醇化合物。 如請求項13之聚三亞曱醚二醇,其中該丨,3_丙二醇係由 可再生性來源之碳水化合物製得之生化衍生之1,3-丙二 醇。 如請求項13之聚三亞甲醚二醇,其中該聚三亞曱醚二醇 之分子量為250至5000且具有低於30ΑΡΗΑ之顏色。135^160 October 14th, 100th, the scope of application for patents: 1. A method for preparing polytrimethylene ether glycol, comprising the following steps: know: for a 1,3-propanol, wherein the 1,3 - propylene glycol comprises a peroxo compound of 1 〇 microgram/g or less based on the weight of 1,3-propanol (PDO) and a carbonyl compound of 100 μg/g or less; and the 1,3 - Propylene glycol is contacted with an acid polymerization catalyst to produce a polytrimethylene glycol; wherein the polytrimethylene ether glycol has a color of less than 5 〇 APHA. 2. The method of claim 1, wherein the 1,3-propanediol further comprises a monofunctional alcohol compound having a basis weight of pD〇 of 100 μg/g or less. 3. The method of claim 1, wherein the 1,3-propanediol has a purity of at least 99.95% 〇 4. The method of claim 1 wherein the 1,3-propanediol comprises biochemically derived 1,3·propanediol. 5. The method of claim 4, wherein the 1,3-propanediol is derived from a fermentation process utilizing a renewable biological source. 6. The method of claim 1 wherein the hydrazine propylene glycol is treated with 1% by weight of sulfuric acid at 17 ° C for 10 minutes and has a color value of less than 15 APHA. 7. The method of claim 1, wherein the polytrimethylene ether glycol has a molecular weight of from 250 to 5 〇〇〇 0 8 such as the method of claim 1 wherein the polytrimethylene ether glycol comprises homopolymerization And/or copolymer. 9. For example. The method of claim 1, wherein the polytrimethylene ether glycol comprises 1,3-propane di 10 10 π. 12. 13. 14. 15. A copolymer of an alcohol and at least one other C6 to Cl2 diol. • The method of claim i, wherein the 5 〇 / 5 〇 〇 of the U propylene glycol is 60 · 7.5. A method for producing a polytrimethylene ether glycol, comprising the steps of: contacting a biochemically-derived L 3 -propanediol with an acid polymerization catalyst to produce a polytrimethylene ether glycol, characterized in that the hydrazine, 3_ 5 〇 / 5 丙 of propylene glycol: 6. 〇 - 7.5 and contains 1 〇〇 microgram / gram or less of carbonyl compound, 1 〇 microgram / gram or less based on the weight of 1,3 propylene glycol a peroxy compound and a monofunctional alcohol compound of 100 μg/g or less; and the polytrimethylene ether glycol has a color of less than 50 APHA. The method of claim 1 or 11, wherein the 153-propane: alcohol has a color lower than 1 〇 APHA ^ a polytrimethylene ether diol by providing 1,3-propanediol and a polymerization catalyst and using the polymerization catalyst Prepared by polymerizing hydrazine, 3· propylene glycol to form polytrimethylene ether monool, wherein the hydrazine, 3-propylene glycol comprises a carbonyl compound of 100 μg/g or less based on the weight of 1,3-propanediol, 10 μg / Δg or less peroxy compound and 1 〇〇 microgram / gram or less of a monofunctional alcohol compound. The polytrimethylene ether glycol of claim 13, wherein the hydrazine, 3-propylene glycol is a biochemically derived 1,3-propanediol prepared from a carbohydrate of renewable origin. The polytrimethylene ether glycol of claim 13, wherein the polytrimethylene ether glycol has a molecular weight of from 250 to 5,000 and a color of less than 30 Å.
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