TW200734275A - Process for preparing organically modified layered double hydroxide - Google Patents
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200734275 九、發明說明: 【發明所屬之技術領域】 本發明係關於用於製備層狀雙氫氧化物之方法。 【先前技術】 此等方法在此項技術中係已知的。Cavani等人(Catalysis Today,11 (1991),第173-301頁)報導用於產生層狀雙氫氧 化物之各種製備方法。所例證之製備方法皆於水中進行。200734275 IX. DESCRIPTION OF THE INVENTION: TECHNICAL FIELD OF THE INVENTION The present invention relates to a process for preparing a layered double hydroxide. [Prior Art] These methods are known in the art. Cavani et al. (Catalysis Today, 11 (1991), pp. 173-301) report various preparation methods for producing layered dihydrogen oxides. The exemplified preparation methods are all carried out in water.
Carlino(5WM /⑽/以,98 (1997),第 73-84 頁)描述主要 使用水溶液將緩酸插入層狀雙氫氧化物中之各種製備方 法。 用於製備層狀雙氫氧化物之多數方法係於水中進行,導 致最終乾燥產物含有大量水。而且,當具有羥基或有機陰 離子作為電荷平衡離子之層狀雙氫氧化物再分散於水中時 通常形成鹼性懸浮液。當將層狀雙氫氧化物摻和進聚合基 質中時,大量水及按習知方法製備之層狀雙氫氧化物之驗 度可能改變所得複合材料之機械與物理特性,例如,摻和 可能導致解聚合作用。 ^ 【發明内容】 此’本發明之-目的在於提供一種用於製備層狀雙氣 氧化,之新型方法’藉此可降低最終產物中之驗度及/或 水含量。進-步之目的在於提供新穎層狀雙氫氧化物。 ,該目的係藉由用於製備包含電荷平衡陰離子之層狀雙氫 乳化物之方法實現,該方法包含以下步驟: ⑷製備-前驅物懸浮液或溶液’丨包含二價金屬離子 116965.doc 200734275 源、三價金屬離子源、水及可與水混溶且其中可溶解 至少5 g/l電荷平衡陰離子前驅物之溶劑; ⑻處理該前驅物懸浮液或溶液,以得到該層狀雙氯氧化 物, 其中,該電荷平衡陰離子前驅物係在步驟(b)之前、期間或 之後添加於該懸浮液或溶液中,且其中,若電荷平衡卜離 子為有機陰離子’則以電荷平衡陰離子前㈣之^ 計,小於5 0重量%之電荷平衡^離 〜 子則驅物為鹽,限制條 件為该電何平衡陰離子不為碳酸根。 一溶劑於本發明方法中之使較得能夠產生含有相對低含 二:狀雙氫氧化物。該層狀雙氫氧化物通常具有改良 熱穩定性。 本發明方法尤其適合於製備含有有機陰離子作為電荷平 衡陰離子之層狀雙氫氧化物。該等經有機改質之層狀雙氫 氧化物具有降低之鹼度, ' 厣肿錐知^ /、以自知方式製備之習知 、ΓηΓ 減,#再分散於(料)水中時將具有較 :ΡΗ值。使用本發明方法可達成較高程度之有機陰離子之 插:。-般而言,層狀雙氣氧化物(且尤其是經有 =雙氫氧化物)將會具有與其所推入之聚合物之改良 、在本發明方法中,溶劑可為能與水混溶且其中可溶解至 少5糾電荷平衡陰離子前驅物之任何 溶可使用八8丁^4 D 1722_98钏〜^ 水之此 可取決於、、e A A °陰離子前驅物之溶解度 〜物之pH值及/或溫度。在本發明方法中,選 116965.doc 200734275 擇條件以使得(例如於反應溫度下)可溶解至少5 g/1電荷平 衡陰離子則驅物。此等溶劑之實例包括醇類,如甲醇、乙 醇、正丙醇、異丙醇、正丁醇、異丁醇及第三丁醇;烷烴 多兀醇類,如乙二醇'丙二醇及甘油;醚類,如二曱基 醚、二乙基醚或二丁基醚;烷烴多元醇之二醚類,二曱基 乙一醇一乙基乙二醇、二曱基丙二醇及二乙基丙二醇; 及如下式之烷氧基化醇類,Carlino (5WM / (10) /, 98 (1997), pp. 73-84) describes various preparation methods for mainly using an aqueous solution to insert a slow acid into a layered double hydroxide. Most of the methods used to prepare the layered double hydroxide are carried out in water, resulting in a final dried product containing a large amount of water. Moreover, an alkaline suspension is usually formed when a layered double hydroxide having a hydroxyl group or an organic anion as a charge balancing ion is redispersed in water. When a layered double hydroxide is incorporated into a polymeric matrix, the large amount of water and the degree of formation of the layered double hydroxide prepared by conventional methods may alter the mechanical and physical properties of the resulting composite, for example, blending may Lead to depolymerization. SUMMARY OF THE INVENTION [The present invention] It is an object of the present invention to provide a novel method for preparing layered double gas oxidation, whereby the degree of verification and/or water content in the final product can be reduced. The purpose of the further step is to provide a novel layered double hydroxide. This object is achieved by a process for preparing a layered dihydrogen emulsion comprising a charge-balancing anion comprising the steps of: (4) preparing a precursor suspension or solution '丨 comprising a divalent metal ion 116965.doc 200734275 a source, a source of trivalent metal ions, water, and a solvent miscible with water and capable of dissolving at least 5 g/l of charge-balanced anion precursor; (8) treating the precursor suspension or solution to obtain the layered dichloro-oxidation And the charge-balanced anion precursor is added to the suspension or solution before, during or after step (b), and wherein if the charge balance ion is an organic anion, then the charge balances the anion before (four) ^, the charge balance of less than 50% by weight is separated from the ~ sub-driver is a salt, the limitation is that the balance of the charge is not carbonate. A solvent in the process of the invention is relatively more capable of producing a relatively low di-containing: double hydroxide. The layered double hydroxide typically has improved thermal stability. The process of the invention is particularly suitable for the preparation of layered double hydroxides containing organic anions as charge balancing anions. The organically modified layered double hydroxides have a reduced alkalinity, and the 'swelling cone is known to be /, prepared in a self-conceived manner, ΓηΓ minus, #redistributed in (feed) water will have Compared with: depreciation. A higher degree of organic anion insertion can be achieved using the process of the invention: In general, a layered double gas oxide (and especially a = double hydroxide) will have an improvement with the polymer it is pushed into. In the process of the invention, the solvent may be miscible with water. And any solution in which at least 5 charge-correction anion precursors can be dissolved can be used. The water can be used depending on, the solubility of the e AA ° anion precursor, the pH of the substance, and/or Or temperature. In the process of the invention, 116965.doc 200734275 is selected such that, for example, at the reaction temperature, at least 5 g/1 of charge-balance anion is driven. Examples of such solvents include alcohols such as methanol, ethanol, n-propanol, isopropanol, n-butanol, isobutanol and tert-butanol; alkanol polyterpenes such as ethylene glycol 'propylene glycol and glycerol; Ethers such as dimethyl ether, diethyl ether or dibutyl ether; diethers of alkane polyols, dimercaptoethanol monoethyl glycol, dimercapto propylene glycol and diethyl propylene glycol; An alkoxylated alcohol of the formula
八中RACVCs烷基或苯基,&為氫或甲基且至$之 ?數;胺類,如三乙胺;非離子性聚合溶劑,如聚乙二 一聚丙一冑月桂基聚乙二醇;離子性液體;'•比咬類; 二甲亞砜;及吡咯啶酮類,如η-甲基吡咯啶酮。 在-個實施例中,溶劑為可與水形成共沸物之溶劑。在 本發明方法中使用共沸混合物使得更易於移除溶劑且更有 效地移除水。 溶劑較佳為具有_ 田# ^ 個&基之酵。此醇之實例為單醇,如 甲醇、乙醇、正丙醇、里%含 /、 ·子、正丁醇、異丁醇及第三丁 .,及如上所述之烷氧基化醇類。 在本發明之一個實施例中 ^ 合剎馮烷虱基化醇。此等烷 虱土化醇之實例為乙醇 1〜 聆早^基醚、乙二醇單乙基醚、乙 一酉予早正丙基醚、乙—醢罝 乙一知早異丙基醚、乙二醇單丁基醚、 116965.doc 200734275 乙二醇單第三丁基醚、乙二醇單己基醚、乙二醇單苯基 醚、乙二醇2-乙基己基醚、二乙二醇單甲基醚、二乙二醇 單乙基醚、二乙二醇單正丙基醚、二乙二醇單異丙基醚、 二乙二醇單丁基醚、丙二醇單甲基醚、丙二醇單乙基醚、 丙二醇單丙基醚、丙二醇單異丙基醚、丙二醇單丁基醚、 丙二醇單第三丁基醚、丙二醇單己基醚、丙二醇單苯基 醚、二丙二醇單甲基醚、二丙二醇單乙基醚、二丙二醇單 φ 正丙基醚、二丙二醇單異丙基醚及二丙二醇單丁基醚。該 等醇中,乙二醇單甲基醚及乙二醇單乙基醚係較少首選, 因為其會產生畸形且可能引起健康問題。 最佳之烷氧基化醇為丙二醇單甲基醚及丙二醇單乙基 鱗。溶劑可購自(例如)Shell(0xitol/Pr〇xit〇〇及D〇w (D_n〇1) 及 Union Carbide(Carbit〇l/Cell〇s〇lve)。亦設想使用兩種或 兩種以上溶劑於本發明方法中。另外預期使用另一種不與 水混溶且/或其中可溶解小於5 g/1電荷平衡陰離子前驅物之 φ 有機溶劑。此等有機溶劑之合適實例包括烷烴,如戊烷、 己烷及庚烷;酮類,如曱基戊基酮、甲基乙基酮、甲基異 丁基酮及環己酮;酯類,如乙酸乙酯及乙酸丁酯;不飽和 丙烯酸酯類,如丙烯酸丁酯、甲基丙烯酸曱酯、六亞曱基 一丙稀自曰及二羥甲基丙烧三丙稀酸酯;及芳族烴類,如 苯、甲苯及二甲苯。 本發明方法中所用之水及溶劑之量可在寬範圍内變化。 在本叙明之一個實施例中,以水與溶劑之總質量計,溶劑 之里小於50重量%,較佳小於40重量%,且最佳小於3〇重 116965.doc 200734275 量% 0 本發明方法中所用之二價金屬離子源及三價金屬離子源 可為熟悉此項技術者已知之任何來源。該等來源包括一價 及/或二價金屬離子之可溶性鹽以及不溶性或部分不溶性 二價及三價金屬離子源或其混合物。 金屬離子源之可溶性鹽包括硝酸鹽、氣酸鹽、高氯酸_ 以及銘酸鹽。不溶性或部分不溶性二價及三價金屬離子源 験一般包括二價或三價金屬離子之氧化物或氫氧化物、碳酸 鹽。該等來源較佳為不溶性或部分可溶性。最佳,一 ,一 1貝 及二^金屬離子源為氧化物或氫氧化物。 在本申請案之上下文中,”可溶性鹽”係指於室溫下完全 溶解且形成澄清溶液之二價及三價金屬離子源。在本申技 案之上下文中’術語”不溶性鹽或部分不溶性鹽”係指於室 溫下不完全溶解且形成懸浮液之來源。 二價金屬離子之實例為Zn2+、Mn2+、Ni2+、Cq2+、 _ Fe2+、Cy、Sn2+、Ba2+、Ca2+及 Mg2+。三價金屬離子之實 例為 A1 、Cr3+、Fe3+、Co3+、Mn3+、Ni3+、ce3 +及 Ga3+。 亦預期使用三種或三種以上不同金屬離子於利用本發明方 法所製備之層狀雙氫氧化物中。以上金屬離子中,首選 Mg2+與Al3 +之組合。 不溶性或部分不溶性之合適鎂源的實例包括氧化鎂、氫 氧化鎂、羥基碳酸鎂、碳酸氫鎂、白雲石(d〇1〇mite)及海 泡石(sepiolite)。亦預期兩種或兩種以上鎂源之組合。 不溶性或部分不溶性之鋁源通常為鋁之氫氧化物或氧化 116965.doc -10- 200734275 物此紹源之實例為二經基銘(如三水銘石(gibbsite)及三 $ 氧化銘(bayerite))、氧經基銘(aiuininiurn 〇x〇hydroxide)(如 軟水銘石(boehmite)、硬水鋁石(diasp〇re)或針鐵礦 (goethite))及過渡型氧化鋁,其為熟悉此項技術者已知。VIII RACVCs alkyl or phenyl, & hydrogen or methyl and up to the number; amines, such as triethylamine; nonionic polymerization solvent, such as polyethylene, polyacrylonitrile, lauryl Alcohol; ionic liquid; '• bite type; dimethyl sulfoxide; and pyrrolidone, such as η-methylpyrrolidone. In one embodiment, the solvent is a solvent that forms an azeotrope with water. The use of an azeotrope in the process of the invention makes it easier to remove the solvent and remove the water more efficiently. The solvent preferably has a leaven of _田#^& Examples of such alcohols are monoalcohols such as methanol, ethanol, n-propanol, 5%, n-butanol, isobutanol and tributyl, and alkoxylated alcohols as described above. In one embodiment of the invention, the fluorenyl hydrazinyl alcohol. Examples of such alkanoicated alcohols are ethanol 1~ lingsyl ether, ethylene glycol monoethyl ether, ethyl ketone to early n-propyl ether, ethyl bromide, isopropyl isopropyl ether, ethylene Alcohol monobutyl ether, 116965.doc 200734275 ethylene glycol mono-tert-butyl ether, ethylene glycol monohexyl ether, ethylene glycol monophenyl ether, ethylene glycol 2-ethylhexyl ether, diethylene glycol single Methyl ether, diethylene glycol monoethyl ether, diethylene glycol mono-n-propyl ether, diethylene glycol mono-isopropyl ether, diethylene glycol monobutyl ether, propylene glycol monomethyl ether, propylene glycol single Ethyl ether, propylene glycol monopropyl ether, propylene glycol monoisopropyl ether, propylene glycol monobutyl ether, propylene glycol mono-telebutyl ether, propylene glycol monohexyl ether, propylene glycol monophenyl ether, dipropylene glycol monomethyl ether, two Propylene glycol monoethyl ether, dipropylene glycol mono φ n-propyl ether, dipropylene glycol monoisopropyl ether and dipropylene glycol monobutyl ether. Among such alcohols, ethylene glycol monomethyl ether and ethylene glycol monoethyl ether are less preferred because they are deformed and may cause health problems. The most preferred alkoxylated alcohols are propylene glycol monomethyl ether and propylene glycol monoethyl scale. Solvents are commercially available, for example, from Shell (0xitol/Pr〇xit® and D〇w (D_n〇1) and Union Carbide (Carbit〇l/Cell〇s〇lve). It is also envisaged to use two or more solvents. In the process of the invention, it is further contemplated to use another φ organic solvent which is immiscible with water and/or which can dissolve less than 5 g/1 of charge-balance anion precursor. Suitable examples of such organic solvents include alkanes such as pentane. , hexane and heptane; ketones such as decyl amyl ketone, methyl ethyl ketone, methyl isobutyl ketone and cyclohexanone; esters such as ethyl acetate and butyl acetate; unsaturated acrylate Such as butyl acrylate, decyl methacrylate, hexamethylene propyl propylene and dimethyl propyl triacrylate; and aromatic hydrocarbons such as benzene, toluene and xylene. The amount of water and solvent used in the process of the invention may vary within wide limits. In one embodiment of the invention, less than 50% by weight, preferably less than 40% by weight, based on the total mass of water and solvent, And the best is less than 3 〇 weight 116965.doc 200734275 quantity % 0 the divalent gold used in the method of the invention The source of ions and the source of trivalent metal ions may be any source known to those skilled in the art. These sources include soluble salts of monovalent and/or divalent metal ions and insoluble or partially insoluble divalent and trivalent metal ion sources or Mixtures of the metal ion source include nitrates, gas salts, perchloric acid _ and methacrylates. Insoluble or partially insoluble divalent and trivalent metal ion sources generally include oxidation of divalent or trivalent metal ions. Or a hydroxide or a carbonate. The sources are preferably insoluble or partially soluble. Preferably, the source of one, one, and two metal ions is an oxide or hydroxide. In the context of the present application, "Soluble salt" means a source of divalent and trivalent metal ions that completely dissolves at room temperature and forms a clear solution. In the context of this application, the term 'insoluble salt or partially insoluble salt' means at room temperature It does not completely dissolve and forms a source of suspension. Examples of divalent metal ions are Zn2+, Mn2+, Ni2+, Cq2+, _Fe2+, Cy, Sn2+, Ba2+, Ca2+, and Mg2+. Examples are A1, Cr3+, Fe3+, Co3+, Mn3+, Ni3+, ce3+, and Ga3+. It is also contemplated to use three or more different metal ions in the layered double hydroxide prepared by the method of the present invention. Preferred combinations of Mg2+ and Al3+. Examples of suitable magnesium sources for insoluble or partially insoluble include magnesium oxide, magnesium hydroxide, magnesium hydroxycarbonate, magnesium hydrogencarbonate, dolomite (d〇1〇mite) and sepiolite. It is also expected to combine two or more kinds of magnesium sources. The insoluble or partially insoluble aluminum source is usually aluminum hydroxide or oxidized 116965.doc -10- 200734275 The example of this source is dijing Ming (such as Sanbi Mingshi (gibbsite) and three $bayerite, aiuininiurn 〇x〇hydroxide (such as boehmite, diasp〇re or goethite) Goethite)) and transition alumina, which are known to those skilled in the art.
以上不溶性或部分可溶性二價金屬離子及三價金屬離子 源於本發明方法中之使用提供一種更環保之方法,因為更 少的鹽(若存在)殘留於得自該方法之廢物流中。而且,二 價及二價金屬離子源且尤其是鎂源及鋁源與層狀雙氫氧化 物製備中普遍使用之相應鹽相比而言一般較不昂貴。此 外,本發明之方法通常更簡單,因為其需要較少步驟且/ 或不需要對廢物流進行後處理。而且,與習知方法相比而 言,該等方法可以短很多之時間進行,而又可導致更高產 率之經有機改質之層狀雙氫氧化物。 在本發明之一較佳實施例中,不溶性或部分可溶性二價 及/或二價金屬離子源且尤其是鎂源及/或鋁源在步驟卬)之 前研磨。在本發明方法中,二價及/或三價金屬離子源一 般具有小於20 μπι之d50值及小於50 pm2d9〇值。較佳地, d50值小於15 pmad90值小於40 μιη,更佳地,d5〇值小於 10 μηι且d90值小於30 μιη,甚佳地,㈣值小於8 _且_ 值小於20 μηι,且最佳地,d50值小於6 μιη且d9〇值小於ι〇 μπι。粒度分佈可使用熟悉此項技術者已知之方法(例如雷 射繞射法)依據DIN 13320測定。此研磨步驟使得層狀雙氫 氧化物之形成更快地進行。若二價及三價金屬離子源為鎂 源及鋁源,則該步驟可進一步降低如三水鋁石或水鎂石 116965.doc 200734275 (brucite)之雜質含量。The use of the above insoluble or partially soluble divalent metal ions and trivalent metal ions from the process of the present invention provides a more environmentally friendly process because less salt, if any, remains in the waste stream from the process. Moreover, divalent and divalent metal ion sources, and especially magnesium sources and aluminum sources, are generally less expensive than the corresponding salts commonly used in the preparation of layered double hydroxides. Moreover, the process of the present invention is generally simpler because it requires fewer steps and/or does not require post treatment of the waste stream. Moreover, compared to conventional methods, such methods can be carried out in a much shorter period of time, which in turn leads to higher yields of organically modified layered double hydroxides. In a preferred embodiment of the invention, the insoluble or partially soluble divalent and/or divalent metal ion source and especially the magnesium source and/or aluminum source are ground prior to step 卬). In the process of the invention, the source of divalent and/or trivalent metal ions generally has a d50 value of less than 20 μm and a value of less than 50 pm2d9. Preferably, the d50 value is less than 15 pmad90 value is less than 40 μηη, more preferably, the d5〇 value is less than 10 μηι and the d90 value is less than 30 μηη, and preferably, the (four) value is less than 8 _ and the _ value is less than 20 μηι, and the best Ground, the d50 value is less than 6 μηη and the d9〇 value is less than ι〇μπι. The particle size distribution can be determined according to DIN 13320 using methods known to those skilled in the art, such as laser diffraction. This grinding step allows the formation of the layered double hydroxide to proceed more quickly. If the divalent and trivalent metal ion source is a magnesium source and an aluminum source, this step can further reduce the impurity content such as gibbsite or brucite 116965.doc 200734275 (brucite).
在本申咕案之上下文中’術語’’處理”及”經處理之,,,如 步驟(b)之處理,係指在高溫下處理懸浮液。此處理可為熱 處理或溶劑熱(solvothermal)處理。在本申請案之上下文 中,術語”熱處理"及”用熱方法”係指在大氣壓力下於3〇它 與前驅物懸浮液或溶液沸點之間的溫度下處理前驅物懸浮 液或溶液。該溫度通常為4(rc至12(rc,較佳為5〇。〇至 100°C且最佳為60°C至90°c。 又,術語"溶劑熱處理"及"用溶劑熱方法”係指在大氣壓 力以上之壓力下及—般為大氣壓力下前驅物懸浮液或溶液 之沸點以上之溫度下處理前驅物懸浮液或溶液。該壓力通 常為1巴至200巴,較佳為2巴至15〇巴,且最佳為3巴至_ 巴。該溫度通常為loot或更高,較佳為1〇〇。(:至3〇〇。〇,更 佳為litre至25(TC,且最佳為120。〇至200。(:。 本發明方法可在前驅物懸浮液中無c〇2或任何碳酸鹽存 在下進打,以確保無碳酸鹽併入層狀雙氫氧化物中作 荷平衡陰離子。 ' ’ 本發明方法亦適合於製備含有有機陰離子作為電 層狀雙氯氧化物。該等層狀雙氯氧化物稱為”經 ?吳之層狀雙氫氧化物"或”有機黏土 (。rgan〇c㈣”。 ^發明之-個實施例中,有機陰離子係於步驟⑻之前 ^八進行的同時添加至前驅物懸浮液或溶液中。以 ί ’經有機改質之層狀雙氫氧化物以-個步驟製備,此、· 吊使得該方法i簡單且更迅速且因此更經濟。 、 116965.doc 12 200734275In the context of this application, the terms 'process' and 'processed', as in the treatment of step (b), refer to the treatment of the suspension at elevated temperatures. This treatment can be a heat treatment or a solvothermal treatment. In the context of this application, the terms "heat treatment" and "thermal method" refer to the treatment of a precursor suspension or solution at atmospheric pressure at a temperature between it and the precursor suspension or the boiling point of the solution. The temperature is usually 4 (rc to 12 (rc, preferably 5 〇. 〇 to 100 ° C and most preferably 60 ° C to 90 ° C. Again, the term "solvent heat treatment " &" with solvent heat "Method" means treating a precursor suspension or solution at a pressure above atmospheric pressure and at a temperature above the boiling point of the precursor suspension or solution at atmospheric pressure. The pressure is usually from 1 bar to 200 bar, preferably It is from 2 bar to 15 bar, and most preferably from 3 bar to _ bar. The temperature is usually loot or higher, preferably 1 〇〇. (: to 3 〇〇. 〇, more preferably litre to 25 ( TC, and most preferably 120. 〇 to 200. (: The process of the invention can be carried out in the presence of no c〇2 or any carbonate in the precursor suspension to ensure that no carbonate is incorporated into the layered double hydroxide The substance is equilibrated as an anion. ' ' The method of the invention is also suitable for preparing an organic anion as an electrolayered dichloride The layered bis(oxychloride) is referred to as "layered double hydroxide" or "organic clay (.rgan〇c(4)". In an embodiment, the organic anion is in the step (8) Simultaneous addition to the precursor suspension or solution. The organically modified layered double hydroxide is prepared in a step-by-step manner, which makes the method i simple and faster. Therefore more economical. 116965.doc 12 200734275
电何十衡陰離卞別驅物可為驗金屬或驗土金屬H 及/或三價金屬離子之鹽或酸或其混合物。在本發= 中,以電荷平衡陰離子前驅物之總質量計,小㈣重量% 之電荷平衡陰離子以鹽形式引人懸浮液中。為減少廢物& 中之鹽量,首選使用有機陰離子之酸及二價及/或三價2 屬離子與有機陰離子之鹽或有機陰離子之酸之混合物。士 上所述’以電荷平衡陰離子前驅物之總質量計二於:重σ 量%之電荷平衡陰離子以鹽形式使用,較佳小於3〇重量% 之電荷平衡陰離子為鹽,且更佳地小於1〇重量%之電荷平° 衡陰離子為鹽。亦設想本發明方法中不存在電荷平衡陰離 子之鹽,以減少廢物流及/或甚至最終產物中之鹽量。 在本發明之-個實施例中’電荷平衡陰離子為有機陰離 子。有機陰離子之前驅物可為鹼金屬或鹼土金屬鹽或二價 及/或三價金屬離子之鹽或酸或其混合物。有機陰離子可 以上述量使用。 有機陰離子之酸之適當實例包括乙酸、琥珀酸、對苯二 曱酸、苯甲酸、辛酸、癸酸、月桂酸、肉豆蘿酸、掠搁 酉夂硬月曰S文花生酸、壬酸、癸稀酸(decenoic acid)、棕 搁稀酸(palmitoleic acid)、油酸、亞麻油酸(lin〇leic acid)、次亞麻油酸(iin〇ienicacid)及松香。 亦設想在步驟(b)之前或期間添加部分有機陰離子且在形 成層狀雙氫氧化物之後添加其餘部分。 或者’在層狀雙氫氧化物形成之後添加有機陰離子,在 此情況下’層狀雙氫氧化物包含選自由以下各物組成之群 116965.doc • 13 - 200734275 的電荷平衡陰離子:氫氧根、硝酸根、裹 机雕子、溴離子、 磷酸根、膦酸根、磺酸根、硫酸根、硫 & 敬^虱根或其混合 物。本發明係關於如上所述之方法,Α谁— ”一步包含以下步 驟: (〇製備懸浮介質及層狀雙氫氧化物之懸 〜,予液,該層狀雙 氫氧化物包含選自由以下各物組成之 八义拜的電荷平衡陰 離子:氫氧根、硝酸根、磷酸根、膦酸根、磺酸根、 | 硫酸根、硫酸氫根及鹵離子; (d)處理該懸浮液,以得到經有機改質之層狀雙氫氧化 物, 其中,有機陰離子前驅物係在步驟(c)或(d)期間添加。 較佳地,步驟(C)中所用之層狀雙氫氧化物之電荷平衡陰 離子係選自由以下各物組成之群:氫氧根、硝酸根、氣離 子、溴離子或其混合物。該電荷平衡陰離子可易於與有機 陰離子進行交換。相比於類似方法中使用水,該交換係藉 Φ 由使用本發明溶劑而得以有利提高。 或者,本發明係關於一種製備包含有機陰離子作為電荷 平衡陰離子之層狀雙氫氧化物之方法,該方法包含以下步 驟: (a) 製備層狀雙氫氧化物、溶劑及視情況之水之懸浮液, 該層狀雙氫氧化物包含選自由以下各物組成之群的電 何平衡陰離子:氫氧根、硝酸根、磷酸根、膦酸根、 石黃酸根、硫酸根、硫酸氫根及鹵離子; (b) 處理該前驅物懸浮液或溶液,以獲得層狀雙氫氧化 H6965.doc -14- 200734275 物 其中’該有機降雜1义 π子則驅物係於步驟(勾戋 懸浮液中,且其中#、货 < (h月間添加至 ,、中忒/谷劑可與水混溶且 gM有機陰離子前驅物。 八 岭解至少5 所用之層狀雙氫氧化物 u平奶』為根據本發明方 狀雙氫氧化物,或者該声 所1備之層 法製備。 J 1尤用白知製備方The electric Hehengheng yin and the dynasty may be the salt or acid or a mixture thereof of the metal or soil metal H and/or trivalent metal ion. In the present invention, a small (four) weight percent of the charge-balancing anion is introduced into the suspension in the form of a salt based on the total mass of the charge-balanced anion precursor. In order to reduce the amount of salt in the waste &amp; it is preferred to use an organic anionic acid and a mixture of a divalent and/or trivalent 2 genus ion with an organic anion salt or an organic anion acid. The above description is based on the total mass of the charge-balanced anion precursor. The charge-balance anion of the weight % is used in the form of a salt, preferably less than 3% by weight. The charge-balance anion is a salt, and more preferably less than 1 〇% by weight of the charge is equal to the salt. It is also envisaged that no salt of charge-balanced anions will be present in the process of the invention to reduce the amount of salt in the waste stream and/or even in the final product. In one embodiment of the invention, the charge balancing anion is an organic anion. The organic anion precursor may be an alkali metal or alkaline earth metal salt or a salt or acid of a divalent and/or trivalent metal ion or a mixture thereof. The organic anion can be used in the above amounts. Suitable examples of the acid of the organic anion include acetic acid, succinic acid, terephthalic acid, benzoic acid, octanoic acid, citric acid, lauric acid, myristic acid, chlorpyrifos, sulphuric acid, citric acid, Decenoic acid, palmitoleic acid, oleic acid, lin〇leic acid, iin〇ienic acid, and rosin. It is also contemplated to add a portion of the organic anion before or during step (b) and to add the remainder after forming the layered double hydroxide. Or 'adding an organic anion after the formation of the layered double hydroxide, in which case the layered double hydroxide comprises a charge-balanced anion selected from the group 116965.doc • 13 - 200734275: hydroxide , nitrate, wrapper, bromide, phosphate, phosphonate, sulfonate, sulfate, sulfur & The present invention relates to the method as described above, and the one-step comprises the following steps: (〇 preparing a suspension medium and a layered double hydroxide suspension, a liquid, the layered double hydroxide comprising selected from the following a charge-balance anion of the composition of the eight yiyi: hydroxide, nitrate, phosphate, phosphonate, sulfonate, | sulfate, hydrogen sulfate and halide; (d) treating the suspension to obtain organic a modified layered double hydroxide, wherein the organic anion precursor is added during step (c) or (d). Preferably, the charge-balance anion of the layered double hydroxide used in step (C) It is selected from the group consisting of hydroxide, nitrate, gas ion, bromide ion or a mixture thereof. The charge-balancing anion can be easily exchanged with an organic anion. Compared to water used in a similar method, the exchange system By Φ is advantageously improved by the use of the solvent of the invention. Alternatively, the invention relates to a process for preparing a layered double hydroxide comprising an organic anion as a charge-balancing anion, the method comprising The following steps: (a) preparing a layered double hydroxide, a solvent and optionally a suspension of water, the layered double hydroxide comprising an electrohepatic anion selected from the group consisting of: hydroxide, Nitrate, phosphate, phosphonate, rhein, sulfate, hydrogen sulfate and halide; (b) treatment of the precursor suspension or solution to obtain layered double hydroxide H6965.doc -14- 200734275 Wherein 'the organic hypomixed 1 π sub-driver is attached to the step (hooking in the suspension, and wherein #, the goods < (added to, during the month, the sorghum / gluten can be miscible with water and gM organic Anionic precursor. The layered double hydroxide u flat milk used in at least 5 of Bailing solution is prepared according to the square double hydroxide of the present invention or the layer method prepared by the sound system. square
若本發明方法包含於層狀雙氣氧化物形成之後“ 平衡陰離子與有機,離早 、何 物)形成步驟及交換步驟可田也+ 飞氧化 換乂驟可用熱方法或溶劑熱方法執行, 或者形成步驟可用埶方、本袖> , 财法執仃而交換步驟用水熱方法執 行,反之亦然。 轨 在本申清案之上下文中,術語"電荷平衡陰離子"係指補 償結晶聰薄片之靜電荷不足之陰離子。由於顧通常且 有層狀結構’因此電荷平衡陰離子可位於堆疊ldh層之爽 層内、邊緣上或外表面上。位於堆疊ldh層之夾層内之陰 離子稱為插入離子。 β 包含有機陰離子或有機黏土之堆疊LDH亦可(例如)於聚 合基質中分層或剝離。在本說明書之上下文中,術語,,分 層係定義為因LDH結構之至少部分脫層引起之lDH粒子 之平均堆疊私度之降低,進而產生每體積含有顯著更多單 獨LDH薄片之材料。術語,,剝離"係定義為完全分層,亦 即,垂直於LDH薄片方向上之週期性消失,導致單獨層於 介質中之隨機分散,進而完全失去堆疊次序。 116965.doc -15· 200734275 LDH之溶脹或膨脹·亦叫做ldh之插入-可藉由χ光繞射 (XRD)觀察,因為底面反射(亦即,d(〇〇1)反射)之位置指示 層間距離,此距離在插入時增加。 平均堆疊程度之降低可觀察為XRD反射之加寬直至消失 或係藉由底面反射(〇〇1)之漸增非對稱性觀察。 完全分層(亦即剝離)之表徵仍有待分析,但一般而言亦 可根據原始LDH之非-(hkO)反射之完全消失進行。 φ 層之有序化及由此之分層範圍可進一步利用穿透電子顯 微鏡(TEM)目測。 本發明之LDH可為熟悉此項技術者已知之任何ldh,只 是形態學及物理化學特性可能不同。通常,_ldh為能 夠膨脹或溶漲之礦物LDH。此等LDH具有包含帶電荷結晶 薄片(亦稱為單獨LDH層)以及夾帶於其中之電荷平衡陰離 子的層狀結構。術語”膨脹”及”溶漲”於本申請案上下文中 係私帶電荷結晶薄片之間距離的增加。可膨脹可於適 • 當溶劑(如水)中溶漲且可藉由交換電荷平衡離子與其他(有 機)電荷平衡離子而進一步膨脹且改質,該改質於此項技 術中亦稱為插入。 本發明進一步係關於藉由本發明方法所獲得之層狀雙氫 氧化物。與在水中製備之層狀雙氫氧化物相比而言,本發 月之層狀雙氫氧化物且尤其是經有機改質之層狀雙氫氧化 物具有低水含量、降低之驗度及改良熱穩定性。本發明之 ldh通㊉具有與聚合物之改良相容性,且可於廣泛範圍之 聚合物中使用,尤其是可於一旦LDH摻和進來便會惡化之 116965.doc • 16 · 200734275 ^ 6物中使用。在此等情況下,所得聚合物通常會具有較 低解聚合程度、較低脫色程度及/或降低之抗氧化劑退化 程度。 由於所得有機改質層狀雙氫氧化物之較低鹼度,當其應 用於硫縮合(slllfur-con(ienzation)橡膠化合物中時,與未改 質層狀雙氫氧化物相比而言,對焦化時間之影響降低。If the method of the present invention comprises the step of "equalizing anions and organics, from the early stage, and what matter" after the formation of the layered double gas oxide, the step of the formation and the exchange step may be performed by a thermal method or a solvothermal method, or The formation step can be used for the side, the sleeve, the financial method, and the exchange step is performed by the hydrothermal method, and vice versa. In the context of this application, the term "charge balance anion" An anion with insufficient static charge of the sheet. Since it usually has a layered structure', the charge-balanced anion can be located in the layer, on the edge or on the outer surface of the stacked ldh layer. The anion located in the interlayer of the stacked ldh layer is called an insertion. Ion. β Stacked LDH comprising organic anions or organic clays may also be layered or stripped, for example, in a polymeric matrix. In the context of this specification, the term, layered is defined as the at least partial delamination of the LDH structure. The reduction in the average stacking of the lDH particles results in a material containing significantly more individual LDH flakes per volume. Terminology, stripping " The system is defined as a complete stratification, that is, a periodic disappearance perpendicular to the direction of the LDH sheet, resulting in a random dispersion of the individual layers in the medium, thereby completely losing the stacking order. 116965.doc -15· 200734275 Swelling or swelling of LDH • Also known as the insertion of ldh - can be observed by Xenon diffraction (XRD) because the position of the bottom reflection (ie, d(〇〇1) reflection) indicates the distance between the layers, which increases at the time of insertion. The decrease can be observed as the broadening of the XRD reflection until it disappears or is observed by the increasing asymmetry of the bottom reflection (〇〇1). The characterization of the complete layering (ie, stripping) remains to be analyzed, but in general It can be performed according to the complete disappearance of the non-(hkO) reflection of the original LDH. The ordering of the φ layer and thus the stratification range can be further visualized by a transmission electron microscope (TEM). The LDH of the present invention can be familiar with this item. Any ldh known to the skilled artisan may only have different morphological and physicochemical properties. Typically, _ldh is a mineral LDH that can swell or swell. These LDHs contain charged crystalline flakes (also known as individual LDH layers) and a layered structure of charge-balanced anions entrained therein. The terms "expansion" and "swell up" are in the context of the present application an increase in the distance between the privately-charged crystalline sheets. The swell can be adapted to the solvent (eg water) The medium melts up and can be further expanded and modified by exchanging charge balancing ions with other (organic) charge balancing ions, which is also referred to as insertion in the art. The invention further relates to the method obtained by the method of the invention Layered double hydroxide. The layered double hydroxide of the present month and especially the organically modified layered double hydroxide have a lower ratio than the layered double hydroxide prepared in water. Water content, reduced degree of inspection and improved thermal stability. The invention has improved compatibility with polymers and can be used in a wide range of polymers, especially when LDH is incorporated. 116965.doc • 16 · 200734275 ^ 6 Used in. In such cases, the resulting polymer will generally have a lower degree of depolymerization, a lower degree of discoloration, and/or a reduced degree of degradation of the antioxidant. Due to the lower alkalinity of the resulting organically modified layered double hydroxide, when applied to a sulfur condensation (slllfur-con (ienzation) rubber compound, compared to the unmodified layered double hydroxide, The effect of the focus time is reduced.
在本發明之一個實施例中,可製備具有不同於習知LDH 之形態學的LDH。LDH或有機改質LDH中單獨片晶之平均 長度與直徑之比率(L/D比率)可超過2〇〇,較佳地L/D比率 至夕300,更佳為至少5〇〇,且甚佳為至少丨〇〇〇。比率 可使用電子顯微鏡測定,如掃描電子顯微鏡(sem)及/或 TEM。該長度為片晶在垂直於堆疊方向之方向上的最大尺 寸,而直徑係指黏土粒子於堆疊方向上之厚度。若黏土分 層及/或剝離,則直徑可如一個層之厚度般大。 本毛明之層狀雙氫氧化物具有對應於以下通式之層狀結 構, [M;Mn3+(〇H) 2m+2n JXn/;-bH20 (|) 其中,M2+ 為如 Zn2+、Mn2+、Ni2+、c〇2+、Fe2+、、 Sn2+、Ba2+、Ca2+、Mg2+之二價金屬離子,m3 +為如 ai3+、 \N〜e3 + w +之三價金屬離 子,m及η具有使得^^丨至⑺之值,且b具有〇至1〇範圍内 之值。X為熟悉此項技術者已知之電荷平衡陰離子。電荷 平衡陰離子可為有機陰離子或無機陰離子。設想使用一或 116965.doc •17- 200734275 多種有機陰離子及/或一或多種無機陰離子。 此項技術中已知之無機陰離子之實例包括:氫氧根、碳 酸根、碳酸氫根、硝酸根、氯離子、溴離子、磺酸根、硫 酸根、硫酸氫根、釩酸根、鎢酸根、硼酸根、磷酸根;= 撐離子(pillaring anion),如HV〇4-、V2〇74-、HV2〇i24-、V办3·、 V1〇〇286-、Μ〇7〇2Λ、PWl2(V-、Β(〇Η)4·、B4〇5_429In one embodiment of the invention, an LDH having a morphology different from that of the conventional LDH can be prepared. The ratio of the average length to the diameter of the individual lamellae in the LDH or organically modified LDH (L/D ratio) may exceed 2 〇〇, preferably L/D ratio to 夕300, more preferably at least 5 〇〇, and even Good for at least 丨〇〇〇. The ratio can be determined using an electron microscope such as a scanning electron microscope (sem) and/or TEM. The length is the maximum size of the platelets in the direction perpendicular to the stacking direction, and the diameter refers to the thickness of the clay particles in the stacking direction. If the clay is layered and/or peeled off, the diameter can be as large as the thickness of one layer. The layered double hydroxide of the present invention has a layered structure corresponding to the following formula, [M; Mn3 + (〇H) 2m + 2n JXn /; - bH20 (|) wherein M2+ is such as Zn2+, Mn2+, Ni2+, a divalent metal ion of c〇2+, Fe2+, Sn2+, Ba2+, Ca2+, Mg2+, m3+ is a trivalent metal ion such as ai3+, \N~e3 + w + , m and η have such a ^^丨 to (7) The value, and b has a value in the range of 〇 to 1〇. X is a charge balancing anion known to those skilled in the art. The charge balancing anion can be an organic anion or an inorganic anion. It is envisaged to use one or 116965.doc • 17- 200734275 multiple organic anions and/or one or more inorganic anions. Examples of inorganic anions known in the art include: hydroxide, carbonate, bicarbonate, nitrate, chloride, bromide, sulfonate, sulfate, hydrogen sulfate, vanadate, tungstate, borate Phosphate; = pillaring anion, such as HV〇4-, V2〇74-, HV2〇i24-, V3, V1〇〇286-, Μ〇7〇2Λ, PWl2(V-, Β(〇Η)4·, B4〇5_429
[B3〇3(〇H)4]-、[B3〇3(OH)5]2·、_?·、HGa〇32_、⑽广;及 Kegghl離子。較佳地,無機陰離子係選自由以下各4物組成 之群·虱氧根、碳酸根、碳酸氫根、石肖酸根、氯離子、漠 離子、%酸根、硫酸根、硫酸氫根或其混合物。 本發明方法中所用之有機陰離子可為熟悉此項技術者已 知之:何有機陰離子。可適用於本發明方法中之有機陰離 子可何生自有機陰離子之鹽或酸。如硬脂酸自旨之驗金屬鹽 之鹽衍生有機陰離子之使用可因其與相應酸衍生有機陰離 子相比於溶劑中更具穩定性而有利。或者 子之使用可有因為鹽離子將不被引入廢物流中= 廢物流不需要額外處理以移除鹽離子,使該方法更廉價且 更簡單。 ' 此等有機陰離子包括·· -、二或多元叛酸、確酸、膦酸 及硫酸。較佳地,有機陰離子包含至少2個碳原子,更佳 山 眾子甚佳至少10個碳原子,且最佳至少12個 厌原子’且有機陰離子包含至多個碳原子,較佳至多 5〇0個奴原+,更佳至多1GG個碳原子,且最佳至多50個碳 116965.doc 200734275 利用本發明方法製備之經有機改質之層狀雙氫氧化物較 佳具有1.5 nm以上之單獨層間距離。此在該等經有機改質X 之層狀雙氫氧化物之使用中具有優勢,例如若其於聚合基 質中使用時。在聚合基質中(例如於奈米複合材料或塗^ 組合物中),較大層間距離使得本發明之層狀雙氫氧2物 於聚合基質中可易於加工’且其進一步使得層狀雙氫氧化 物易於分層及/或剝離,致使經改質之層狀雙氫氧化物與 φ 聚合物基質之混合物具有改良物理特性。較佳地,本發明 之LDH之層間距離為至少丨.5 nm,更佳至少】6 nm,甚佳 至少1.8 nm,且最佳至少2 nm。單獨層間之距離可使用χ 光繞射及穿透電子顯微鏡(TEM)測定,如上所概述。 進一步預期,電荷平衡有機陰離子包含一或多種官能 基,如經基、胺、竣酸及乙稀基。若此等經有機改質之 LDH用於聚合基質中,則該等官能基可與聚合物相互作用 或反應。 籲 本舍明有機陰離子之適當實例為一元叛酸,如脂肪酸, 及松香基離子(rosin-based ion) 〇 在一個實施例中,有機陰離子為具有8至22個碳原子至 脂肪酸或其鹽。此脂肪酸或其鹽可為飽和或不飽和脂肪 酸。此等脂肪酸或其鹽之適當實例係衍生自辛酸、癸酸、 月桂酸、肉豆蔻酸、棕櫚酸、硬脂酸、花生酸、癸烯酸、 棕櫚烯酸、油酸、亞麻油酸、次亞麻油酸及其混合物。 在本發明之另一個實施例中,有機陰離子為松香或其 鹽。松香得自天然來源,易於購得,且與合成有機陰離子 116965.doc -19- 200734275 相比而言相對便宜。松香天然來源之典型實例為松香膠、 木松香及高油松香。松香通常為一般含有約2〇個碳原子之 單幾酸三環松香酸之多種不同異構體的懸浮液。各種松香 酸之三環結構之不同之處主要在於雙鍵之位置。通常,松 香為包含左海松脂酸(lev〇pimaric acid)、新松香酸 (neoabietic acid)、長葉松酸(palustric acid)、松香酸 (abietic acid)、脫氫松香酸(dehydr〇abietic acid)、斷脫氫 Φ 松香酸(seco-dehydroabietic add)、四氫松香酸(tetrahydroabietic acid)、一氯松香酸(dihydr〇abietic acid)、海松脂酸(pharic acid)及異海松脂酸(is〇pimaric acid)之物質的懸浮液。得自 天然來源之松香亦包括松香,亦即,松香懸浮液,其尤其 藉由聚合作用、異構化作用、歧化作用、氮化作用及與丙 烯酸、酸酐及丙烯酸酯之迪爾_阿德(Diels_Alder)反應改 質。藉由該等方法獲得之產物稱為改質松香。天然松香亦 可藉由熟悉此項技術者已知之任何方法化學改變,該等方 # 法如松香上之竣基與金屬氧化物、金屬氫氧化物或鹽反應 以形成松香皂或鹽(所謂之樹脂酸鹽(resinate》。此等經化 學改變之松香稱為松香衍生物。 松香可藉由引人有機基團、陰離子性基團或陽離子性基 團進行改質或化學改變。有機基團可為具有工至利個碳原 子之厶取代或未經取代脂族或芳族烴。陰離子性基團可為 熟悉此項技術者已知之任何陰離子性基團,如缓酸根或續 酸根。[B3〇3(〇H)4]-, [B3〇3(OH)5]2·, _?·, HGa〇32_, (10) broad; and Kegghl ion. Preferably, the inorganic anion is selected from the group consisting of the following four substances: oxime, carbonate, hydrogencarbonate, lithothate, chloride, ion, % acid, sulfate, hydrogen sulfate or a mixture thereof . The organic anions used in the process of the invention are known to those skilled in the art: what organic anions. The organic anion which is suitable for use in the process of the invention can be derived from a salt or acid of an organic anion. The use of an organic anion derived from a salt of a metal salt such as stearic acid may be advantageous because it is more stable than the corresponding acid-derived organic anion in a solvent. Alternatively, the use of salt ions will not be introduced into the waste stream = the waste stream does not require additional treatment to remove salt ions, making the process cheaper and simpler. 'The organic anions include ···, di- or poly-repulsive, acid, phosphonic acid and sulfuric acid. Preferably, the organic anion comprises at least 2 carbon atoms, more preferably at least 10 carbon atoms, and preferably at least 12 anatomical atoms' and the organic anion comprises up to a plurality of carbon atoms, preferably at most 5 〇0 More than 1 GG carbon atoms, and most preferably up to 50 carbons 116965.doc 200734275 The organically modified layered double hydroxide prepared by the method of the present invention preferably has a single layer of 1.5 nm or more. distance. This is advantageous in the use of such layered double hydroxides which have been organically modified X, for example if they are used in a polymeric matrix. In a polymeric matrix (e.g., in a nanocomposite or coating composition), the greater interlayer distance allows the layered dihydrogen oxyhydroxides of the present invention to be readily processed in a polymeric matrix' and which further renders layered dihydrogen The oxide is susceptible to delamination and/or exfoliation, resulting in improved physical properties of the modified layered double hydroxide and φ polymer matrix mixture. Preferably, the interlayer distance of the LDH of the present invention is at least 丨.5 nm, more preferably at least -6 nm, very preferably at least 1.8 nm, and most preferably at least 2 nm. The distance between the individual layers can be determined using a ray diffraction and a transmission electron microscope (TEM), as outlined above. It is further contemplated that the charge-balanced organic anion comprises one or more functional groups such as a trans-base, an amine, a citric acid, and an ethylene group. If such organically modified LDH is used in a polymeric matrix, the functional groups can interact or react with the polymer. A suitable example of an organic anion of Benbenming is a monobasic acid, such as a fatty acid, and a rosin-based ion. In one embodiment, the organic anion has from 8 to 22 carbon atoms to a fatty acid or a salt thereof. The fatty acid or a salt thereof may be a saturated or unsaturated fatty acid. Suitable examples of such fatty acids or salts thereof are derived from octanoic acid, citric acid, lauric acid, myristic acid, palmitic acid, stearic acid, arachidic acid, decenoic acid, palmitoleic acid, oleic acid, linoleic acid, sub- Linoleic acid and its mixtures. In another embodiment of the invention, the organic anion is rosin or a salt thereof. Rosin is obtained from natural sources and is readily available and relatively inexpensive compared to synthetic organic anions 116965.doc -19- 200734275. Typical examples of natural sources of rosin are rosin gum, wood rosin and high oil rosin. The rosin is typically a suspension of a plurality of different isomers of a mono-acid tricyclic rosin acid generally having about 2 carbon atoms. The three ring structure of various rosin acids differ mainly in the position of the double bond. Usually, the rosin contains lev〇pimaric acid, neoabietic acid, palustric acid, abietic acid, dehydr〇abietic acid, Dehydro-hydrogen pyridine rosinic acid (seco-dehydroabietic add), tetrahydroabietic acid, dihydr〇abietic acid, pharic acid and is〇pimaric acid a suspension of the substance. Rosin derived from natural sources also includes rosin, that is, a rosin suspension, which is especially by polymerization, isomerization, disproportionation, nitriding and Deer_Ade with acrylic acid, acid anhydride and acrylate ( Diels_Alder) The reaction was modified. The product obtained by these methods is called modified rosin. Natural rosin can also be chemically altered by any method known to those skilled in the art, such as the rosin group on rosin reacting with a metal oxide, metal hydroxide or salt to form a rosin soap or salt (so-called Resinate. These chemically modified rosins are called rosin derivatives. Rosin can be modified or chemically altered by introducing an organic group, an anionic group or a cationic group. The substituted or unsubstituted aliphatic or aromatic hydrocarbon is a hydrazine having a working carbon atom. The anionic group may be any anionic group known to those skilled in the art, such as a tallow or a sulphate.
/等权香基材料之其他詳細資料可見於^^⑽^及L 116965.doc -20- 200734275Other details of the /equal scent-based materials can be found in ^^(10)^ and L 116965.doc -20- 200734275
Russe\\(Naval Stores, production-chemistry-utilization, 1989,New York,第 II節,第 9章)及 J_B. Class(’’Resins,Natural,’’第 1 章:’’Rosin and Modified Rosins,’’ 〇/ C/zemka/ ,在線刊登日期:2000年12月4日)中。 在一個實施例中,插入陰離子為脂肪酸與松香之混合 物。 一般而言,本發明之LDH類型中插入離子總量之至少 10%為有機陰離子,較佳為至少30%,更佳為至少60%, 且最佳為至少90%。在一較佳實施例中,插入陰離子總量 之至少10%為脂肪酸衍生陰離子或松香基陰離子或兩者之 懸浮液,較佳為至少30%,更佳為至少60%,且最佳為至 少 90% 0 有機改質LDH之製備中所用之LDH中所含之電荷平衡陰 離子與鋁的莫耳比率可為所希望之任意值。此比率可處在 10:1至1:10範圍内,較佳為5:1至1:5,且最佳為2:1至1:2。 預期使用1之比率。 本發明之LDH包括水滑石及類水滑石陰離子性LDH。此 等LDH之實例為水滑石及類水滑石材料、透鎂鋁石 (meixnerite)、水鎮紹石(manasseite)、碳鎮鐵礦(pyroaurite)、 水碳鐵鎂石(sj6grenite)、碳鎂鉻礦(stichtite)、水碳鉻鎂石 (barbertonite)、水 I呂錄石(takovite)、水碳鐵錄石(reevesite)及 水碳猛鎂石(desautelsite)。較佳之LDH為水滑石,其為具 有對應於以下通式之層狀結構之LDH, 116965.doc -21 - 200734275 (II) [Mg^Aln3+(OH) 2m+2n K2/;-bH20 其中,m及n具有使得111/11=1至1〇(較佳為工至㈧之值,且1^具 有0至10範圍内之值,通常為2至6之值,且經常為約4之 值。X為如上所述之電荷平衡離子。 首選m/n應具有2至4之值,更尤其為接近3之值。 LDH可為熟悉此項技術者已知之任何晶體形式,如 Cavani 等人(Catalysis Today, 11 (1991),第 173_3〇1頁)或 B〇〇kir^A(LDHSandLDHMinerals,(1993)i4g(5), 第558-564頁)所述者。若LDH為水滑石,則該水滑石可為 具有(例如)3Ηι、3H2、3R!或3R2堆疊之多型體。 本發明之LDH可用作以下物質中之成分:塗覆組合物、 (印刷)油墨調配物、黏合劑增黏劑、樹脂基組合物、橡膠 組合物、清洗調配物、鐵井流體及水泥、叾膏調配物、不 織布、纖維、料體1、定向塑膠縳件⑽㈣流 ㈣t)、(前)陶究材料,及雜合有機_無機複合材料,如聚合 物基奈米複合物。本發明LDH可進—步用於聚合反應中, 如溶液聚合反應、乳液聚合反應及懸浮液聚合反應。有機 黏土可進一步用作半晶質聚合物(如聚丙缔)中:結晶助 劑。本發明之LDH可進-步用於其中可組合單獨功能之 LDH及有機陰離子之應用中,如於造紙製程或清潔劑工業 中:又’本發明之LDH可用於供醫藥、殺轰劑及/或肥料 之受控釋放應用中’且可用作有機化合物(如污畅、著 色劑等)之吸附劑。 116965.doc -22- 200734275 入天月$纟係關於包含聚合物及本發明之LDH之奈米 子才料其中LDH包含具有至少8個破原子之有機陰離 二般^ ’經有機改質之咖具有相當高程度之剝離 或分層’且經微米尺寸化改質之LDH之含量一般較低Russe\\ (Naval Stores, production-chemistry-utilization, 1989, New York, Section II, Chapter 9) and J_B. Class(''Resins,Natural,''Chapter 1:''Rosin and Modified Rosins, '' 〇 / C/zemka/, online publication date: December 4, 2000). In one embodiment, the intercalated anion is a mixture of fatty acid and rosin. In general, at least 10% of the total amount of intercalated ions in the LDH type of the invention is an organic anion, preferably at least 30%, more preferably at least 60%, and most preferably at least 90%. In a preferred embodiment, at least 10% of the total amount of intercalated anions is a suspension of a fatty acid-derived anion or a rosin-based anion or both, preferably at least 30%, more preferably at least 60%, and most preferably at least 90% 0 The molar ratio of the charge-balance anion to aluminum contained in the LDH used in the preparation of the organically modified LDH may be any desired value. This ratio may range from 10:1 to 1:10, preferably from 5:1 to 1:5, and most preferably from 2:1 to 1:2. It is expected to use a ratio of 1. The LDH of the present invention includes hydrotalcite and hydrotalcite-like anionic LDH. Examples of such LDHs are hydrotalcite and hydrotalcite-like materials, meixnerite, manasseite, pyroaurite, sj6grenite, carbon magnesium chrome Sthottite, barbertonite, takovite, reevesite, and desautelsite. Preferably, the LDH is hydrotalcite, which is an LDH having a layered structure corresponding to the following general formula, 116965.doc -21 - 200734275 (II) [Mg^Aln3+(OH) 2m+2n K2/; -bH20 wherein m And n has a value such that 111/11 = 1 to 1 Torr (preferably, working to (eight), and 1^ has a value in the range of 0 to 10, usually a value of 2 to 6, and often a value of about 4. X is a charge balancing ion as described above. Preferred m/n should have a value of 2 to 4, more particularly a value close to 3. LDH can be any crystal form known to those skilled in the art, such as Cavani et al. (Catalysis Today, 11 (1991), pp. 173_3〇1) or B〇〇kir^A (LDHS and LDHMinerals, (1993) i4g(5), pp. 558-564). If LDH is hydrotalcite, the water The talc may be a polytype having, for example, a 3 Η, 3H2, 3R! or 3R2 stack. The LDH of the present invention can be used as a component in a coating composition, a (printing) ink formulation, and a binder viscosifying agent. Agent, resin-based composition, rubber composition, cleaning formulation, iron well fluid and cement, paste preparation, non-woven fabric, fiber, material body 1, oriented plastic fastener (10) (4) ㈣t), (former) study ceramic materials, and hybrid organic-inorganic composite material _, Ji Naimi as polymer composites. The LDH of the present invention can be further used in a polymerization reaction such as solution polymerization, emulsion polymerization, and suspension polymerization. Organic clay can be further used as a crystallization aid in semi-crystalline polymers such as polypropylene. The LDH of the present invention can be further used in applications where LDH and organic anions of separate functions can be combined, as in the papermaking process or detergent industry: and the LDH of the present invention can be used for pharmaceuticals, bombicides and/or Or a controlled release application of fertilizers' and can be used as an adsorbent for organic compounds (eg, stains, colorants, etc.). 116965.doc -22- 200734275 入天月$纟 relates to the nano-particles containing the polymer and the LDH of the present invention, wherein the LDH comprises an organic anion having at least 8 broken atoms and an organically modified coffee. The content of LDH with a relatively high degree of peeling or delamination' and micron-sized modification is generally lower
或甚至為零。奈米複合材料中完全剝離及/或分層之LDH 可使該材料具有可見光穿透性,且因此使其適用於光學應 用0 術語"奈米複合材料"係指其中至少—種組分包含具有處 =1至1GG奈米範圍内之至少—個維度之無機相的複合材 特别適σ用於本發明之奈米複合材料中之包含電荷 平衡有機陰離子混合物中至少一者經化學改變以與聚合物 基質更相容或對其更具反應性之電荷平衡有機陰離子混合 物。此使得LDH與聚合物基f之間的相互作用得以改良, 產生改良機械特性及/或黏彈特性。更相容之有機陰離子 可包含具有個碳原子之經取代或未經取代脂族或芳 族烴。或者或另外,有機陰離子中之至少―者可包含選自 由以下各物組成之群的反應性基團:丙烯酸根、甲基丙烯 酸根、經基、氣離子、胺、環氧化物、硫醇、乙稀基、二 硫化物及多硫化物、氨基甲酸根、銨、磺酸根、亞磺酸 根、疏、鱗(Ph〇Sph〇nium)、膦酸根、異氰酸根、疏基、、經 苯基、氫化物、乙醯氧基及酸酐。 可適當用於本發明之奈米複合材料中之聚合物可為孰舞 此項技術者已知之任何聚合物基質。在本說明書中,術語 116965.doc -23 - 200734275 π聚合物”係指且士 守曰具有至少兩種構建塊(亦即,單體) 物,因此包括寘取触 機 枯养I體、共聚體及聚合樹脂。適合用於人 物基質中之聚人% & π …口 曰物為聚加成物及聚縮合物兩者。該等聚人 物可另外為均聚物或共聚物。較佳地,聚合基質具有至,丨、 20之聚合度,#乂土 夕 更佳為至少5 0。在此關係中,對於聚合度之 定義參見PJ ^ • Fl〇ry5 Principles of Polymer Chemistry^ NewOr even zero. The fully exfoliated and/or layered LDH in the nanocomposite allows the material to be visible to light, and thus makes it suitable for optical applications. 0 Terminology "Nanocomposite" means at least one of these components A composite comprising an inorganic phase having at least one dimension in the range of from 1 to 1 GG nanometer is particularly suitable for use in the nanocomposite comprising a charge-balanced organic anion in the nanocomposite of the invention chemically altered A charge-balanced organic anion mixture that is more compatible or more reactive with the polymer matrix. This improves the interaction between the LDH and the polymer group f, resulting in improved mechanical properties and/or viscoelastic properties. More compatible organic anions may contain substituted or unsubstituted aliphatic or aromatic hydrocarbons having one carbon atom. Alternatively or additionally, at least one of the organic anions may comprise a reactive group selected from the group consisting of acrylate, methacrylate, thiol, gas ion, amine, epoxide, thiol, Ethylene, disulfide and polysulfide, carbamate, ammonium, sulfonate, sulfinate, sparse, scale (Ph〇Sph〇nium), phosphonate, isocyanate, sulfhydryl, phenyl , hydride, ethoxylated and anhydride. The polymer which can be suitably used in the nanocomposite of the present invention can be any polymer matrix known to those skilled in the art. In the present specification, the term 116965.doc -23 - 200734275 π polymer" means that the scorpion has at least two building blocks (ie, monomers), and thus includes the contact of the contactor, the copolymerization Body and polymeric resin. Suitable for use in the matrix of the human body. The & 曰 曰 曰 为 为 为 为 为 为 为 为 为 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 Preferably, the polymeric matrix has a degree of polymerization of 丨, 20, and more preferably at least 50. In this relationship, for the definition of degree of polymerization, see PJ ^ • Fl〇ry5 Principles of Polymer Chemistry^ New
York, 1953 。 ’ 適田聚合物之實例為:聚烯烴類,如聚乙烯或聚丙烯; 乙烯基聚合物類,#聚苯乙烯、聚甲基丙烯酸曱酯、聚氣 乙稀聚偏一氣乙稀或聚偏二氟乙稀;飽和聚酯類,如聚 對苯二甲酸乙二西旨、聚乳酸或聚(ε_己内醋);不飽和聚醋 樹脂類、丙烯酸醋樹脂類、甲基丙烯酸醋樹脂類、聚醯亞 胺類、環氧樹脂類、齡曱酸樹脂類、尿素甲酸樹脂類、三 聚氰胺甲醛樹脂類、聚胺酯樹脂類、聚碳酸酯類、聚芳基 敗類聚颯類、聚硫醚類、聚醯胺類、聚醚醯亞胺類、聚 醚醋類、聚醚酮類、聚醚醋酮類、聚矽氧烷類、聚胺醋 類、聚環氧化物類,及兩種或兩種以上聚合物之摻和物。 較佳者為聚烯烴類、乙烯基聚合物類、聚醋類、聚碳酸醋 類、聚醯胺類、聚胺酯類或聚環氧化物類。 本發明之有機黏土尤其適用於熱塑性聚合物中,如聚乙 烯、聚丙烯、聚苯乙烯或乙縮醛(共)聚合物(如聚曱醛 (polyoxymethylene ’ ΡΟΜ));及橡膠中如天然橡膠 (NR)、苯乙烯-丁二烯橡膠(SBR)、聚異戊二烯橡膠(IR)、 聚丁二烯橡膠(BR)、聚異丁烯橡膠(IIR)、鹵化聚異丁烯橡 116965.doc -24- 200734275 膠、丁腈橡膠(NBR)、鹵化丁腈橡膠(HNBR)、苯乙烯-異 戊二烯-苯乙烯橡膠(SIS)及類似苯乙烯嵌段共聚物、聚(表 氣醇)橡膠(CO、ECO、GPO)、聚矽氧橡膠(Q)、氯丁二烯 橡膠(CR)、乙烯丙烯橡膠(EPM)、乙烯丙烯二烯橡膠 (EPDM)、聚硫橡膠(T)、氟橡膠(FKM)、乙烯-乙酸乙烯酯 橡膠(EVA)、聚丙烯酸酯橡膠(ACM)、聚降莰烯橡膠 (polynorbornene,PNR)、聚胺酯橡膠(AU/EU),及聚酯 /醚 熱塑性彈性體。 尤其較佳者為藉由聚合至少一種烯系不飽和單體所獲得 之聚合物或共聚物。此等聚合物之實例為聚烯烴及改質聚 烯烴,其為熟悉此項技術者所知。聚烯烴或改質聚烯烴可 為均聚物或共聚物。此等(改質)聚烯烴之適當實例為:聚 乙烯、聚丙烯、聚丁烯、聚苯乙烯、聚氣乙稀、聚偏二氯 乙烯,及乙烯-丙烯橡膠、丙烯-丁烯共聚物、乙烯-氣乙烯 共聚物、乙烯-乙酸乙烯酯共聚物、丙烯腈-丁二烯-苯乙烯 共聚物(ABS)、丙烯腈-丙烯酸酯-苯乙烯共聚物(AAS)、甲 基丙烯酸甲酯-丁二烯-苯乙烯共聚物(MBS)、氯化聚乙 烯、氯化聚丙烯、乙烯-丙烯酸酯共聚物、氣乙烯-丙烯共 聚物,及其混合物。甚佳之聚合物為聚乙烯、聚丙烯、聚 苯乙烯及聚氣乙稀。 聚乙烯之具體實例為高密度聚乙烯、低密度聚乙烯、直 鏈低密度聚乙烯、超低密度聚乙烯,及超高分子量聚乙 烯。乙烯基聚合物之實例為乙烯-乙酸乙烯酯共聚物 (EVA)、乙烯-丙烯酸乙酯共聚物(EEA)、乙烯-丙稀酸甲g旨 116965.doc -25- 200734275 共聚物(EMA)及乙烯-丙烯酸共聚物(Eaa)。 最佳之t合物為聚丙稀。此項技術中已知之任何聚丙稀 將適用於本發明。聚丙烯類之實例見於R b.York, 1953. Examples of suitable polymers are: polyolefins, such as polyethylene or polypropylene; vinyl polymers, #polystyrene, polymethyl methacrylate, polyethylene ethylene, ethylene oxide or polyethylene Difluoroethylene; saturated polyesters, such as polyethylene terephthalate, polylactic acid or poly(ε_hexine vinegar); unsaturated polyester resin, acrylic vinegar resin, methacrylic resin Classes, polyimines, epoxy resins, aged phthalic acid resins, urea formic acid resins, melamine formaldehyde resins, polyurethane resins, polycarbonates, polyaryl saponins, polythioethers , polyamines, polyether oximines, polyether vinegars, polyether ketones, polyether ketones, polyoxyalkylenes, polyamines, polyepoxides, and two or a blend of two or more polymers. Preferred are polyolefins, vinyl polymers, polyesters, polycarbonates, polyamines, polyurethanes or polyepoxides. The organic clay of the present invention is especially suitable for use in thermoplastic polymers such as polyethylene, polypropylene, polystyrene or acetal (co)polymers (such as polyoxymethylene 'ΡΟΜ); and rubber such as natural rubber (NR), styrene-butadiene rubber (SBR), polyisoprene rubber (IR), polybutadiene rubber (BR), polyisobutylene rubber (IIR), halogenated polyisobutylene rubber 116965.doc -24 - 200734275 Glue, nitrile rubber (NBR), halogenated nitrile rubber (HNBR), styrene-isoprene-styrene rubber (SIS) and similar styrenic block copolymers, poly(gas alcohol) rubber ( CO, ECO, GPO), polyoxyxene rubber (Q), chloroprene rubber (CR), ethylene propylene rubber (EPM), ethylene propylene diene rubber (EPDM), polysulfide rubber (T), fluororubber ( FKM), ethylene vinyl acetate rubber (EVA), polyacrylate rubber (ACM), polynorbornene (PNR), polyurethane rubber (AU/EU), and polyester/ether thermoplastic elastomer. Particularly preferred are polymers or copolymers obtained by polymerizing at least one ethylenically unsaturated monomer. Examples of such polymers are polyolefins and modified polyolefins, which are known to those skilled in the art. The polyolefin or modified polyolefin can be a homopolymer or a copolymer. Suitable examples of such (modified) polyolefins are: polyethylene, polypropylene, polybutene, polystyrene, polyethylene oxide, polyvinylidene chloride, and ethylene-propylene rubber, propylene-butene copolymer , ethylene-gas ethylene copolymer, ethylene-vinyl acetate copolymer, acrylonitrile-butadiene-styrene copolymer (ABS), acrylonitrile-acrylate-styrene copolymer (AAS), methyl methacrylate - Butadiene-styrene copolymer (MBS), chlorinated polyethylene, chlorinated polypropylene, ethylene-acrylate copolymer, ethylene-propylene copolymer, and mixtures thereof. Very good polymers are polyethylene, polypropylene, polystyrene and polyethylene. Specific examples of the polyethylene are high density polyethylene, low density polyethylene, linear low density polyethylene, ultra low density polyethylene, and ultra high molecular weight polyethylene. Examples of vinyl polymers are ethylene-vinyl acetate copolymer (EVA), ethylene-ethyl acrylate copolymer (EEA), ethylene-acrylic acid methyl ketone 116965.doc -25- 200734275 copolymer (EMA) and Ethylene-acrylic acid copolymer (Eaa). The best t compound is polypropylene. Any polypropylene known in the art will be suitable for use in the present invention. Examples of polypropylenes are found in R b.
LiebeYman(Kirk_Othmer Encyclopedia of Chemical Technology,在 線刊登曰期:2000年12月4曰)之”P〇lypropyiene,,第j章_ "Properties"中。本發明之聚丙烯之一特殊種類藉由所謂之 熱塑性聚烯烴(TPO)形成,該等聚烯烴包括聚丙烯與 橡膠之摻和物或反應堆級。 本發明之奈米複合材料可進一步包含此項技術中普遍使 用之添加劑。此等添加劑之實例為顏料、染料、UV穩定 劑、熱穩定劑、抗氧化劑、填料(如滑石、白堊、石灰、 羥磷灰石、矽石、碳黑、玻璃纖維、天然與合成聚合纖維 及其他(有機)無機填料)、阻燃劑、成核劑、抗衝擊改質 ㈣增塑劑、流變改質劑、交聯劑、偶聯劑及除氣劑。 该等可選附加物及其相應量可根據需要選擇。 以混合物總重計,LDH於奈米複合材料中之量較佳為 0.01-75重量%’更佳為〇〇5_5〇重量%,甚佳為〇丄3〇重量 篁。或更少,較佳1-1〇重量%,更佳卜5重量%之 LM量尤其有利於製備聚合物基奈米複合材料,亦即含。有 丄刀層-直至經剝離_有機改質LDH之本發明之含聚人 組合物。 口 ^〈 1〇-7〇重量❶、更佳1〇-5〇重量%之而量尤 所謂之母料,亦即,用於(例如)聚合物混合之高濃度添: 116965.doc -26- 200734275 劑預混合料。儘管此等母料中之黏土-般而言不完全分層 及/或剝離,但在摻和母料與其他聚合物以獲得真實聚合 物基奈米複合物時,^需要,則可在後面階段達成進一步 分層及/或剝離。 本發明之奈米複合材料可根據熟悉此項技術者已知之任 何方法製備。熟悉此項技術者可(例如)藉由使用熔融摻和 技術密切混合聚合物基質與本發明之有機黏土。該方法為 φ 首選,因為其簡單、節省成本且易於應用於現有設備中。 亦設想於單體及/或募聚體經聚合以形成聚合物基質之 前、同時或之後於聚合物基質存在下或於單體及/或寡聚 體存在下製備本發明之黏土。聚丙烯之製備及加工之其他 詳細資料可見於R.B. LiebermanWd-OAma 心 〇/ C/zewka/仏以⑽/%;;,在線刊登曰期:2000年12月4日)之 ’’Polypropylene” 第 2章」’Manufacture” 中。 本發明之奈米複合材料可用於其中按習知使用該等複合 鲁材料之任何應用中。奈米複合材料可適當地用於地毯、汽 車部件、容器封口、午餐盒、蓋板、醫療裝置、家庭用 品、食物容器、洗碗機、戶外傢具、吹模瓶、可棄式不織 布、電纜與電線,及包裝中。關於聚丙烯之其他詳細資料 可見於 R.B· Lieberman(Kirk-Othmer Encyclopedia of Chemical Technology,在線刊登日期:2000年12月4曰)之 "Polypropylene” 第 5 章-’’Uses” 中及 Basell 標題為 ’’Polypropylene: Textile、Rigid Packaging,Consumer,Film, Automotive,Electrical/Electronics and Home Appliances,,之 -27- 116965.doc 200734275 小冊子022 PPe 10/01中。 包含橡膠之奈米複合材料可適當地用於輪胎製造中,如 綠色輪胎、卡車輪胎、牵引車輪胎、工程機械用 road)輪胎及飛機輪胎,用於冬天用輪胎(wint^ 勾中; 用於乳膠產品中,包括手套、保險套、氣球、導液管、乳 膠絲、泡沫體、地毯底布及橡膠化椰棕及毛髮,用於鞋襪 中,用於土木工程產品中,如橋支承、橡膠·金屬_壓層支 承;用於包帶及軟管中;用於非輪胎汽車應用中,包括引 擎底座、橡膠支承、密封墊、索環、墊圈及防護罩;用於 電線與電纜中;及用於管道密封件、醫療閉合件、滚筒、 小固體輪胎、家用及商用器具之座架、橡膠球及管形材 料、擠奶器以及其他農業應用中。 若橡膠為聚矽氧橡膠且經改質之層狀雙氫氧化物為根據 本發明之經改質層狀雙氫氧化物,則該等奈米複合材料可 適當地用於塗覆產物中,包括壓敏黏合劑、塑性硬塗層及 防水塗層;用於纖維加工應用(包括紡織品)及頭髮護理應 用、密封劑、黏合劑、封囊劑及太陽能電池單元中。 【實施方式】 本發明進一步以以下實例加以說明。 實例 使用以下化學品:Liebe Yman (Kirk_Othmer Encyclopedia of Chemical Technology, online publication: December 4, 2000) "P〇lypropyiene,, Chapter j_", "Properties". One of the special types of polypropylene of the present invention is called Thermoplastic polyolefin (TPO) is formed, which includes a blend of polypropylene and rubber or a reactor grade. The nanocomposite of the present invention may further comprise additives commonly used in the art. Examples of such additives are Pigments, dyes, UV stabilizers, heat stabilizers, antioxidants, fillers (such as talc, chalk, lime, hydroxyapatite, vermiculite, carbon black, glass fiber, natural and synthetic polymeric fibers and other (organic) inorganic fillers ), flame retardant, nucleating agent, impact modified (4) plasticizer, rheology modifier, crosslinker, coupling agent and deaerator. The optional additives and their corresponding amounts can be as needed Preferably, the amount of LDH in the nanocomposite is preferably from 0.01 to 75% by weight, more preferably from 5 to 5 % by weight, even more preferably from 3 to 5% by weight, or less, based on the total weight of the mixture. Preferred 1 -1% by weight, more preferably 5% by weight of LM is particularly advantageous for the preparation of polymer based nanocomposites, that is to say. There is a boring layer - up to the stripping - organically modified LDH of the present invention The composition of the human body. The mouth is more than 1 〇 〇 〇 ❶ 更 更 更 更 更 更 更 更 尤 尤 尤 尤 尤 尤 尤 尤 116 116 116 116 116 116 116 116 116 116 116 116 116 116 116 116 116 116 116 116 .doc -26- 200734275 Premixes. Although the clay in these masterbatches is generally not fully layered and/or stripped, the masterbatch and other polymers are blended to obtain the true polymer base. In the case of a composite, further delamination and/or exfoliation may be achieved at a later stage. The nanocomposite of the present invention may be prepared according to any method known to those skilled in the art. Those skilled in the art may, for example, The polymer matrix is intimately mixed with the organic clay of the present invention by using a melt blending technique. This method is preferred because it is simple, cost effective, and easy to apply to existing equipment. Also contemplated as monomers and/or polymerizers. Before polymerization, to form a polymer matrix, simultaneously or The clay of the invention is then prepared in the presence of a polymer matrix or in the presence of monomers and/or oligomers. Additional details of the preparation and processing of the polypropylene can be found in RB Lieberman Wd-OAma 〇/C/zewka/仏(10)/%;;, published online: December 4, 2000) in ''Polypropylene'' Chapter 2 ''Manufacture''. The nanocomposite of the present invention can be used in the conventional use of such composite For any application of materials, nanocomposites can be suitably used in carpets, automotive parts, container closures, lunch boxes, covers, medical devices, household goods, food containers, dishwashers, outdoor furniture, blow molded bottles, Discarded non-woven fabrics, cables and wires, and packaging. Additional details on polypropylene can be found in RB· Lieberman (Kirk-Othmer Encyclopedia of Chemical Technology, online publication date: December 4, 2000) in "Polypropylene" Chapter 5 - ''Uses' and Basell titled ''Polypropylene: Textile, Rigid Packaging, Consumer, Film, Automotive, Electrical/Electronics and Home Appliances, pp. -27-116965.doc 200734275 booklet 022 PPe 10/01. Rubber-containing nanocomposites can be suitably used in tire manufacturing, such as green tires, truck tires, tractor tires, roads for construction machinery, tires and aircraft tires, for winter tires (wint^ hook; used for Latex products, including gloves, condoms, balloons, catheters, latex, foam, carpet backing and rubberized coir and hair, used in footwear, for civil engineering products, such as bridge support, Rubber·Metal_Laminated support; used in straps and hoses; used in non-tire automotive applications, including engine mounts, rubber supports, gaskets, grommet, gaskets and shields; used in wires and cables; And for pipe seals, medical closures, rollers, small solid tires, mounts for household and commercial appliances, rubber balls and tubular materials, milkers and other agricultural applications. If the rubber is polyoxyxene rubber and The modified layered double hydroxide is a modified layered double hydroxide according to the present invention, and the nano composite materials can be suitably used in coating products, including pressure sensitive adhesives, plastic hard coatings. And waterproof coating; used in fiber processing applications (including textiles) and hair care applications, sealants, adhesives, sealants, and solar cells. [Embodiment] The present invention is further illustrated by the following examples. Chemicals:
Kortacid® PH05 ·· —種棕櫚酸與硬脂酸之摻和物,由 Oleochemicals GmbH(Akzo Nobel Chemicals之公司)供應。Kortacid® PH05 · a blend of palmitic acid and stearic acid supplied by Oleochemicals GmbH (a company of Akzo Nobel Chemicals).
Kortacid® PKGH : C12至C22脂肪酸之摻和物,由 116965.doc -28- 200734275Kortacid® PKGH: a blend of C12 to C22 fatty acids, from 116965.doc -28- 200734275
Oleochemicals GmbH(Akzo Nobel Chemicals之公司)供應。 脫氫松香:購自 Hexion Specialty Products 氫化松香:Foral® AX-E,購自 Eastman Chemical Prifac® 7990 :改質脂肪酸(購自Uniqema) 使用以下溶劑: 異丙醇(賭自Acros)Oleochemicals GmbH (a company of Akzo Nobel Chemicals) is available. Dehydrogenated rosin: purchased from Hexion Specialty Products Hydrogenated rosin: Foral® AX-E, available from Eastman Chemical Prifac® 7990: Modified fatty acid (purchased from Uniqema) The following solvents were used: Isopropanol (bet from Acros)
Ethyl proxitol® :乙氧基丙-2-醇(購自 Shell)Ethyl proxitol® : Ethoxypropan-2-ol (purchased from Shell)
Dowanol® DPNP :丙氧基2-甲基乙氧基丙-2-醇(購自DowDowanol® DPNP: propoxy 2-methylethoxypropan-2-ol (purchased from Dow)
Chemicals)Chemicals)
Dowanol DPM :二丙二醇甲基醚(購自 Dow Chemicals)Dowanol DPM: Dipropylene glycol methyl ether (available from Dow Chemicals)
Dowanol PMA :丙二醇甲基醚乙酸酉I (購自Dow Chemicals)Dowanol PMA: propylene glycol methyl ether acetate 酉I (available from Dow Chemicals)
Dowanol PPh ·丙二醇苯基醚(購自 Dow Chemicals)Dowanol PPh · Propylene Glycol Phenyl Ether (available from Dow Chemicals)
Butyl Carbi to 1 :二乙二醇單丁基醚(購自 Acros) 實例1 將20重量%具有2之Mg/Al比率及羥基作為電荷平衡陰離 子之根據式II之類水滑石層狀雙氫氧化物之250公克水性懸 浮液及250公克異丙醇(購自Acros)潰入配備有高速攪拌器 之1公升玻璃反應容器中且加熱至80°C。接著將於250公克 異丙醇中之90公克Kortacid® PH05經45分鐘添加至該反應 容器中。添加前,將脂肪酸摻和物加熱至80°C。酸添加 後,將反應容器再保持於80°C歷時3小時。接著將反應容 器冷卻至約50°C且移出所得漿料。然後將漿料於4000 rpm 下離心約20分鐘。傾析出液體且將固體於真空下於80°C於 116965.doc -29- 200734275 烘箱中乾燥隔夜。所得包含脂肪酸摻和物之類水滑石黏土 用X光繞射分析,以測定坑道間距(inter-gallery spacing)4 晶格間距(d-spacing)。如上述製備之類水滑石黏土的xrd 圖案顯示次要水滑石相關非_(hk0)反射,表明陰離子性黏 土之插入。該插入物展示2Θ=1·72之特徵性d(〇〇l)值。 如藉由熱重分析(TGA)所量測,該經有機改質之層狀雙 氫氧化物之熱分解起始點為270°C。 $ 實例2 將20重量%具有2之Mg/Al比率及羥基作為電荷平衡陰離 子之根據式II之類水滑石層狀雙氫氧化物之3丨·25公克水性 懸洋液及200公克ethyl proxit〇l(購自SheU)潰入配備有高速 攪拌器之500 ml玻璃反應容器中且加熱至8〇t。接著將於 10 公克 ethyl proxitol 中之 7·5 公克 K〇rtaci# 1>11〇5經15 分鐘 添加至該反應容器中。添加前,將脂肪酸摻和物加熱至 80。。。酸添加後,加熱反應容器,同時蒸餾出水化邮 • pr〇xito1共沸物直至達到130。〇之溫度。接著將反應容器冷 卻至約5吖且移出所得漿料。然後將聚料於2,5〇〇柳下離 心約ίο分鐘。傾析出液體且將固體於真空下於8〇t於烘箱 中乾燥3小時。 所得包含脂肪酸摻和物之類水滑石黏土用χ光繞射分 析,以測定坑道間距或晶格間距。如上述製備之類水滑石 黏土的XRD圖案顯示次要水滑石相關非他〇)反射,表明 陰離子性黏土之插人m物展示46^之特徵性d(〇叫 116965.doc -30· 200734275 實例3 將20重量%具有2之Mg/Al比率及羥基作為電荷平衡陰離 子之根據式II之類水滑石層狀雙氫氧化物之34.5公克水性 懸浮液及200公克Dowanol DPNP潰入配備有高速攪拌器之 5 00 ml玻璃反應容器中且加熱至80°C。接著將於10公克 Dowanol DPNP 中之 7.5 公克 Kortacid® PH05 經 15 分鐘添加 至該反應容器中。添加前,將脂肪酸摻和物加熱至80°C。 酸添加後,加熱反應容器,同時於130°C溫度下蒸餾出水 /Dowanol DPNP混合物。將乾產物冷卻至室溫且將固體於 真空下於80°C於烘箱中乾燥3小時。 如上述製備之類水滑石黏土的XRD圖案顯示次要水滑石 相關非-(hkO)反射,表明陰離子性黏土之插入。該插入物 展示47.0A之特徵性d(001)值。 實例4 將20重量%具有2之Mg/Al比率及羥基作為電荷平衡陰離 子之根據式II之類水滑石層狀雙氫氧化物之3 1.25公克水性 懸浮液及200公克Dowanol DPM潰入配備有高速攪拌器之 5 00 ml玻璃反應容器中且加熱至80°C。接著將6.0公克 Kortacid® PKGH加熱至80°C且添加至該反應容器中。酸添 加後,加熱反應容器,同時於130°C溫度下蒸餾出水/Dowanol DPM混合物。將乾產物冷卻至室溫且將固體於真空下於 80°C於烘箱中乾燥3小時。 如上述製備之類水滑石黏土的XRD圖案顯示次要水滑石 相關非-(hkO)反射,表明陰離子性黏土之插入。該插入物 116965.doc 31 200734275 展示32A之特徵性d(001)值。 實例5 將20重量%具有2之Mg/Al比率及羥基作為電荷平衡陰離 子之根據式Π之類水滑石層狀雙氫氧化物之3 1.25公克水性 懸浮液及200公克Dowanol PMA潰入配備有高速攪拌器之 5 00 ml玻璃反應容器中且加熱至80°C。接著將6.0公克 Kortacid® PKGH添加至該反應容器中。添加前,將脂肪酸 摻和物加熱至80°C。酸添加後,加熱反應容器,同時於 130°C溫度下蒸餾出水/Dowanol PMA混合物。然後將反應 容器冷卻至約50°C,且移出所得漿料。然後將漿料於2,500 rpm下離心約10分鐘。傾析出液體且將固體於真空下於 80°C於烘箱中乾燥3小時。 如上述製備之類水滑石黏土的XRD圖案顯示次要水滑石 相關非-(hkO)反射,表明陰離子性黏土之插入。該插入物 展示48A之特徵性d(001)值。 實例6 將20重量%具有2之Mg/Al比率及羥基作為電荷平衡陰離 子之根據式II之類水滑石層狀雙氫氧化物之3 1.25公克水性 懸浮液及200公克Dowanol PPh潰入配備有高速攪拌器之 500 ml玻璃反應容器中且加熱至80°C。接著將6.0公克 Kortacid® PKGH添加至該反應容器中。添加前,將脂肪酸 摻和物加熱至80°C。酸添加後,加熱反應容器,同時於 130°C溫度下蒸餾出水/Dowanol PPh混合物。然後將反應容 器冷卻至約50°C,且移出所得漿料。然後將漿料於4,000 116965.doc -32- 200734275 rpm下離心約10分鏢。移出透明液體且將固體(漿料頂層) 及凝膠(漿料底層)用丙酮洗條且於真空下於8 〇。〇於烘箱中 乾燥3小時。 如上述製備之類水滑石黏土的XRD圖案顯示次要水滑石 相關非-(hkO)反射,表明陰離子性黏土之插入。該插入物 展示29A之特徵性d(001)值。 實例7 0 將20重量%具有2之Mg/Al比率及羥基作為電荷平衡陰離子 之根據式II之類水滑石層狀雙氫氧化物之3 1 ·25公克水性懸浮 液及200公克Butyl Carbitol潰入配備有高速攪拌器之5〇〇 ml 玻璃反應容器中且加熱至80°C。接著將6·0公克Kortacid® PKGH添加至該反應容器中。添加前,將脂肪酸摻和物加熱 至80°C。酸添加後,加熱反應容器,同時於12(rc溫度下蒸 餾出水/Butyl Carbitol混合物。然後將反應容器冷卻至約 5 0°C,且移出所得漿料。然後將漿料於4,〇〇〇 rpm下離心約1〇 ^ 分鐘。移出透明液體及固體(漿料頂層)且將凝膠(漿料底層) 用丙酮洗滌且於真空下於80°C於烘箱中乾燥3小時。 如上述製備之類水滑石黏土的XRD圖案顯示次要水滑石 相關非-(hkO)反射,表明陰離子性黏土之插入。該插入物 展示30A之特徵性d(001)值。 實例8 將20重量%具有2之Mg/A1比率及經基作為電荷平衡陰離 子之根據式II之類水滑石層狀雙氫氧化物之3丨·25公克水性 懸浮液及200公克Dowanol PPh潰入配備有高速攪拌器之 116965.doc -33- 200734275 5 00 ml玻璃反應容器中且加熱至8(rc。接著將9·75公克脫 氫松香添加至該反應容器中。添加前,將松香加熱至 80°C。酸添加後,加熱反應容器,同時於13〇它溫度下蒸 顧出水/Dowanol PPh混合物。然後將反應容器冷卻至約 50 C ’且移出所得漿料。然後將漿料於4,〇〇〇 rpm下離心約 10分鐘。移出透明液體,且將凝膠(漿料底層)用丙酮洗滌 且於真空下於80°C於烘箱中乾燥3小時。 φ 如上述製備之類水滑石黏土的XRD圖案顯示次要水滑石 相關非-(hkO)反射,表明陰離子性黏土之插入。該插入物 展示25A之特徵性d(〇〇l)值。 實例9 將20重量%具有2之Mg/Al比率及羥基作為電荷平衡陰離 子之根據式π之類水滑石層狀雙氫氧化物之62 5公克水性 懸浮液及150公克ethyl proxit〇l(購自Shell)潰入配備有高速 擾拌器之500 ml玻璃反應容器中且加熱至85。〇。接著將 • 4·06公克Kwtaci# PKGH及12.1 8公克氫化松香添加至該反 應容器中。添加前,將脂肪酸/松香摻和物加熱至8 5。〇。此 外,添加50公克ethyl proxit〇i。摻和物添加後,加熱反應 谷器,同時蒸餾出水/ethyi proxit〇i共沸物直至達到12〇。〇 之溫度。然後將反應容器冷卻至約5〇〇c,添加1〇〇公克 ethyl proxito卜且移出所得漿料。然後將漿料於2,5〇〇叩仿 下離心約10分鐘。傾析出液體,且將固體用丙酮洗滌且於 真空下於80°C於烘箱中乾燥隔夜。 如上述製備之類水滑石黏土的XRD圖案顯示次要水滑石 116965.doc -34- 200734275 相關非-(hkO)反射,表明陰離子性黏土之插入。該插入物 展示29A之特徵性d(001)值。 實例10 將20重量%具有2之Mg/Al比率及羥基作為電荷平衡陰離 子之根據式II之類水滑石層狀雙氫氧化物之62 · 5公克水性 懸浮液及150公克ethyl proxitol(購自Shell)潰入配備有高速 攪拌器之500 ml玻璃反應容器中且加熱至85。〇。接著將 12.15 公克 Kortacid⑧ PKGH及 100公克 ethyl proxitol添加至 該反應容器中。添加前,將脂肪酸摻和物加熱至8 5。在 脂肪酸摻和物/ethyl proxitol添加後,加熱反應容器,同時 蒸餾出水/ethyl proxitol共沸物直至達到12〇。(:之溫度。將 另外100公克ethyl proxitol添加至漿料中。然後將反應容器 冷卻至約50°C,且移出所得漿料。然後將漿料於2,5〇〇 rpm 下離心約10分鐘。傾析出液體,且將固體用丙酮洗滌且於 真空下於8〇°C於烘箱中乾燥6小時。 如上述製備之類水滑石黏土的XRD圖案顯示次要水滑石 相關非-(hkO)反射,表明陰離子性黏土之插入。該插入物 展示28A之特徵性d(001)值。 實例11 將20重量%具有2之Mg/Al比率及經基作為電荷平衡陰離 子之根據式II之類水滑石層狀雙氫氧化物之62 5公克水性 懸浮液及150 ml 2-(2-乙基己氧基)乙醇潰入配備有高速攪 拌器之500 ml玻璃反應容器中且加熱至85。〇。接著將ι215 公克Kortacid® PKGH添加至該反應容器中。添加前,將脂 116965.doc -35- 200734275 肪酸摻和物加熱至85它。在脂肪酸摻和物添加後,加熱反 應容器,同時蒸餾出水/2_(2-乙基己氧基)乙醇共沸物直至 達到125 C之溫度。然後將反應容器冷卻至約5〇它,且移 出所传漿料。然後將漿料於4,〇〇〇 rpm下離心約1 〇分鐘。傾 析出液體’且將固體用丙酮洗務且於真空下於8〇。〇於烘箱 中乾燥5小時。 如上述製備之類水滑石黏土的XRD圖案顯示次要水滑石 φ 相關非-(hk0)反射,表明陰離子性黏土之插入。該插入物 展示30A之特徵性d(〇〇i)值。 實例12 將20重量。/〇具有2之Mg/Al比率及羥基作為電荷平衡陰離 子之根據式II之類水滑石層狀雙氫氧化物之3 1.25公克水性 懸浮液及200公克ethyi pr〇xit〇1(購自SheU)潰入配備有高速 攪拌器之500 ml玻璃反應容器中且加熱至85。〇。接著將 5.78公克Kortacid® PKGH及0·28公克胺基十二烷酸添加至 # 該反應容器中。添加前,將脂肪酸/胺基十二烷酸摻和物 加熱至85°C。在摻和物添加後,加熱反應容器,同時蒸餾 出水/ethyl proxitol共沸物直至達到12〇。〇之溫度。將1〇〇公 克ethyl proxitol添加至漿料中。然後將反應容器冷卻至約 50°C ’且移出所得漿料。然後將漿料於4,〇〇〇 rpjn下離心約 10分鐘。傾析出液體,且將固體用丙酮洗滌且於真空下於 80°C於烘箱中乾燥隔夜。 如上述製備之類水滑石黏土的XRD圖案顯示次要水滑石 相關非_(hk0)反射,表明陰離子性黏土之插入。該插入物 116965.doc -36- 200734275 展示25A之特徵性d(001)值。 實例13 將20重量%具有2之Mg/Al比率及羥基作為電荷平衡陰離 子之根據式II之類水滑石層狀雙氫氧化物之3 1.25公克水性 懸浮液及200公克ethyl proxitol潰入配備有高速授拌器之 5 00 ml玻璃反應容器中且加熱至85°C。接著將3.75公克 Kortacid® PH05及4.87公克脫氫松香添加至該反應容器 中。添加前,將脂肪酸/松香摻和物加熱至8 5 °C。在摻和物 添加後,添加1 50公克ethyl proxitol,且加熱反應容器,同 時蒸餾出水/ethyl proxitol共沸物直至達到120°C之溫度。 然後將反應容器冷卻至約50°C,且移出所得漿料。然後將 漿料於4,000 rpm下離心約1 0分鐘。傾析出液體,且將固體 於真空下於80°C於烘箱中乾燥5小時。 如上述製備之類水滑石黏土的XRD圖案顯示次要水滑石 相關非-(hkO)反射,表明陰離子性黏土之插入。該插入物 展示29A之特徵性d(001)值。 實例14 將20重量%具有2之Mg/Al比率及羥基作為電荷平衡陰離 子之根據式II之類水滑石層狀雙氫氧化物之50公克水性懸 浮液及1 50公克ethyl proxitol(購自Shell)潰入配備有高速授 拌器之500 ml玻璃反應容器中且加熱至85°C。接著將於50 公克 ethyl proxitol 中之 6·3 公克 Kortacid® PKGH及 6.3 公克 氫化松香經1 5分鐘添加至該反應容器中。添加前,將脂肪 酸/松香換和物加熱至8 5 °C。在摻和物添加後,加熱反應容 116965.doc -37- 200734275 器’同時蒸館出水/ethyl proxitol共沸物直至達到i2〇°C之 溫度。然後將反應容器冷卻至約5(rc,添加1〇〇公克ethyl proxitol ’且移出所得漿料。然後將漿料於2,5〇〇 rpm下離 心約10分鐘。傾析出液體,且將固體用丙酮洗滌且於真空 下於80°C於烘箱中乾燥隔夜。 如上述製備之類水滑石黏土的XRD圖案顯示次要水滑石 相關非-(hkO)反射,表明陰離子性黏土之插入。該插入物 展示29A之特徵性d(〇〇i)值。 實例15 將20重量%具有2之Mg/Al比率及羥基作為電荷平衡陰離 子之根據式II之類水滑石層狀雙氫氧化物之1〇〇公克水性懸 浮液及21公克ethyl proxit〇l(購自Shell)潰入配備有高速攪 拌器之500 ml玻璃反應容器中且加熱至85°C。接著將溶解Butyl Carbi to 1 : Diethylene glycol monobutyl ether (available from Acros) Example 1 20% by weight of hydrotalcite layered double hydroxide according to formula II having a Mg/Al ratio of 2 and a hydroxyl group as a charge-balance anion 250 g of the aqueous suspension and 250 g of isopropyl alcohol (available from Acros) were broken into a 1 liter glass reaction vessel equipped with a high speed stirrer and heated to 80 °C. Next, 90 grams of Kortacid® PH05 in 250 grams of isopropanol was added to the reaction vessel over 45 minutes. The fatty acid blend was heated to 80 °C prior to addition. After the acid addition, the reaction vessel was kept at 80 ° C for another 3 hours. The reaction vessel was then cooled to about 50 ° C and the resulting slurry was removed. The slurry was then centrifuged at 4000 rpm for about 20 minutes. The liquid was decanted and the solid was dried overnight at 80 ° C in a 116965.doc -29-200734275 oven under vacuum. The resulting hydrotalcite clay containing fatty acid blends was analyzed by X-ray diffraction to determine the inter-gallery spacing of 4 d-spacing. The xrd pattern of hydrotalcite clay prepared as described above shows a secondary hydrotalcite-related non-(hk0) reflection indicating the insertion of an anionic clay. The insert exhibits a characteristic d(〇〇l) value of 2Θ=1·72. The thermal decomposition starting point of the organically modified layered double hydroxide was 270 ° C as measured by thermogravimetric analysis (TGA). $ Example 2 20% by weight of a hydrotalcite layered double hydroxide of a hydrotalcite layered double hydroxide having a ratio of Mg/Al of 2 and a hydroxyl group as a charge-balanced anion, and 200 g of ethyl proxit〇 l (purchased from SheU) was broken into a 500 ml glass reaction vessel equipped with a high speed stirrer and heated to 8 〇t. This was then added to the reaction vessel at 7 g of K 〇rtaci # 1 > 11 〇 5 in 10 g of ethyl proxitol. The fatty acid blend is heated to 80 prior to addition. . . After the acid addition, the reaction vessel was heated while distilling off the hydrated pr〇xito1 azeotrope until it reached 130. The temperature of 〇. The reaction vessel was then cooled to about 5 Torr and the resulting slurry was removed. Then concentrate the material under 2,5 〇〇 willows for about ίο minutes. The liquid was decanted and the solid was dried in an oven at 8 Torr for 3 hours under vacuum. The resulting hydrotalcite clay containing fatty acid blends was analyzed by calender diffraction to determine the tunnel pitch or lattice spacing. The XRD pattern of the hydrotalcite clay prepared as described above shows the secondary hydrotalcite-related non-tank reflection, indicating that the anionic clay is inserted into the m-characteristic display 46^ characteristic d (howling 116965.doc -30· 200734275 example 3 20% by weight of a 34.5 gram aqueous suspension of hydrotalcite layered double hydroxide according to formula II, having a Mg/Al ratio of 2 and a hydroxyl group as a charge-balanced anion, and 200 gram of Dowanol DPNP broken into a high-speed stirrer 5 00 ml glass reaction vessel and heated to 80 ° C. Then add 7.5 g of Kortacid® PH05 in 10 g Dowanol DPNP to the reaction vessel over 15 minutes. Add the fatty acid blend to 80 before adding. After the acid addition, the reaction vessel was heated while distilling off the water/Dowanol DPNP mixture at a temperature of 130 ° C. The dry product was cooled to room temperature and the solid was dried in an oven at 80 ° C for 3 hours under vacuum. The XRD pattern of the hydrotalcite clay prepared above shows a minor hydrotalcite-related non-(hkO) reflection indicating the insertion of an anionic clay. The insert exhibits a characteristic d(001) value of 47.0 A. Example 4 The amount % has a Mg/Al ratio of 2 and the hydroxyl group as a charge-balanced anion. 3 1.25 g of an aqueous suspension of hydrotalcite layered double hydroxide according to formula II and 200 g of Dowanol DPM broken into a high-speed stirrer 00 ml glass reaction vessel and heated to 80 ° C. Then 6.0 g of Kortacid® PKGH was heated to 80 ° C and added to the reaction vessel. After acid addition, the reaction vessel was heated while distilling off water at 130 ° C /Dowanol DPM mixture. The dry product was cooled to room temperature and the solid was dried in an oven at 80 ° C for 3 hours under vacuum. The XRD pattern of the hydrotalcite clay as described above shows the minor hydrotalcite-related non-(hkO Reflection, indicating the insertion of an anionic clay. The insert 116965.doc 31 200734275 shows the characteristic d(001) value of 32 A. Example 5 The basis of 20% by weight of a Mg/Al ratio of 2 and a hydroxyl group as a charge balancing anion 3 1.25 g of aqueous suspension of hydrotalcite layered double hydroxide and 200 g of Dowanol PMA were broken into a 500 00 glass reaction vessel equipped with a high-speed stirrer and heated to 80 ° C. Then 6.0 g Kortacid® PKGH was added to the reaction vessel. Prior to the addition, the fatty acid blend was heated to 80° C. After the acid addition, the reaction vessel was heated while distilling off the water/Dowanol PMA mixture at a temperature of 130° C. The reaction vessel was then Cool to about 50 ° C and remove the resulting slurry. The slurry was then centrifuged at 2,500 rpm for about 10 minutes. The liquid was decanted and the solid was dried in an oven at 80 ° C for 3 hours under vacuum. The XRD pattern of a hydrotalcite clay such as that described above shows a secondary hydrotalcite-related non-(hkO) reflection indicating the insertion of an anionic clay. The insert shows a characteristic d(001) value of 48A. Example 6 3 1.25 g of an aqueous suspension of a hydrotalcite layered double hydroxide having a ratio of 2% by weight of Mg/Al and a hydroxyl group as a charge-balanced anion, and 200 g of Dowanol PPh were equipped with a high speed. The stirrer was placed in a 500 ml glass reaction vessel and heated to 80 °C. Next, 6.0 grams of Kortacid® PKGH was added to the reaction vessel. The fatty acid blend was heated to 80 °C prior to addition. After the acid addition, the reaction vessel was heated while distilling off the water/Dowanol PPh mixture at a temperature of 130 °C. The reaction vessel was then cooled to about 50 ° C and the resulting slurry was removed. The slurry was then centrifuged at about 4,000 116965.doc -32 - 200734275 rpm for about 10 minutes. The clear liquid was removed and the solid (slurry top) and gel (slurry bottom) were washed with acetone and under vacuum at 8 Torr. Dry in an oven for 3 hours. The XRD pattern of a hydrotalcite clay such as that described above shows a secondary hydrotalcite-related non-(hkO) reflection indicating the insertion of an anionic clay. This insert shows the characteristic d(001) value of 29A. Example 7 0: 20% by weight of a hydrotalcite layered double hydroxide of a hydrotalcite layered double hydroxide having a ratio of Mg/Al of 2 and a hydroxyl group as a charge-balance anion; and a 200 gram of Butyl Carbitol It was placed in a 5 〇〇 ml glass reaction vessel equipped with a high speed stirrer and heated to 80 °C. Next, 0.000 grams of Kortacid® PKGH was added to the reaction vessel. The fatty acid blend was heated to 80 °C prior to addition. After the acid addition, the reaction vessel was heated while distilling off the water/Butyl Carbitol mixture at 12 (rc temperature. The reaction vessel was then cooled to about 50 ° C and the resulting slurry was removed. The slurry was then applied to 4, 〇〇〇 Centrifuge at rpm for about 1 〇 ^ minutes. Remove the clear liquid and solid (slurry top layer) and wash the gel (slurry bottom layer) with acetone and dry in an oven at 80 ° C for 3 hours under vacuum. The XRD pattern of a hydrotalcite-like clay shows a secondary hydrotalcite-related non-(hkO) reflection indicating the insertion of an anionic clay. The insert exhibits a characteristic d(001) value of 30 A. Example 8 20% by weight with 2 The Mg/A1 ratio and the base as a charge-balanced anion are 3 丨·25 g of an aqueous suspension of a hydrotalcite layered double hydroxide such as Formula II and 200 g of Dowanol PPh are broken into a 116965.doc equipped with a high-speed stirrer. -33- 200734275 5 00 ml glass reaction vessel and heated to 8 (rc. Then add 9.75 grams of dehydrogenated rosin to the reaction vessel. Before adding, heat the rosin to 80 ° C. After acid addition, heat Reaction vessel, while at 13 〇 it warms The steam/Dowanol PPh mixture was steamed down. The reaction vessel was then cooled to about 50 C' and the resulting slurry was removed. The slurry was then centrifuged at 4, rpm for about 10 minutes. The clear liquid was removed and the gel was removed. (Slurry bottom layer) was washed with acetone and dried in an oven at 80 ° C for 3 hours under vacuum. φ XRD pattern of hydrotalcite clay prepared as described above showed secondary hydrotalcite-related non-(hkO) reflection, indicating anion Insertion of a clay. The insert exhibits a characteristic d(〇〇l) value of 25 A. Example 9 20% by weight of a hydrotalcite layer having a ratio of Mg/Al of 2 and a hydroxyl group as a charge-balanced anion according to formula π 62 5 g of an aqueous suspension of double hydroxide and 150 g of ethyl proxit® (purchased from Shell) were broken into a 500 ml glass reaction vessel equipped with a high-speed stirrer and heated to 85 〇. Then 4 • 06 g of Kwtaci # PKGH and 12.1 g of hydrogenated rosin were added to the reaction vessel. Before the addition, the fatty acid/rosin blend was heated to 85. In addition, 50 g of ethyl proxit〇i was added. After the admixture was added , heating the reaction bar, while The distillate/ethyi proxit〇i azeotrope was reached until the temperature reached 12. The reaction vessel was then cooled to about 5 〇〇c, 1 gram of ethyl proxito was added and the resulting slurry was removed. The mixture was centrifuged for about 10 minutes, and the liquid was decanted, and the solid was washed with acetone and dried in an oven at 80 ° C under vacuum overnight. The XRD pattern of the hydrotalcite clay prepared as described above shows the minor hydrotalcite 116965.doc -34- 200734275 correlated non-(hkO) reflection, indicating the insertion of an anionic clay. This insert shows the characteristic d(001) value of 29A. Example 10 20 wt% of an aqueous suspension of hydrotalcite layered double hydroxide having a ratio of Mg/Al of 2 and a hydroxyl group as a charge-balance anion according to formula II and 150 g of ethyl proxitol (purchased from Shell) ) Crush into a 500 ml glass reaction vessel equipped with a high speed stirrer and heat to 85. Hey. Next, 12.15 g of Kortacid 8 PKGH and 100 g of ethyl proxitol were added to the reaction vessel. The fatty acid blend was heated to 85 prior to addition. After the addition of the fatty acid admixture /ethyl proxitol, the reaction vessel was heated while distilling off the water/ethyl proxitol azeotrope until it reached 12 Torr. (: Temperature. An additional 100 grams of ethyl proxitol was added to the slurry. The reaction vessel was then cooled to about 50 ° C and the resulting slurry was removed. The slurry was then centrifuged at 2,5 rpm for about 10 minutes. The liquid was decanted, and the solid was washed with acetone and dried in an oven at 8 ° C for 6 hours under vacuum. The XRD pattern of the hydrotalcite clay prepared as described above shows the minor hydrotalcite-related non-(hkO) reflection. , indicating the insertion of an anionic clay. The insert exhibits a characteristic d(001) value of 28 A. Example 11 20% by weight of a hydrotalcite according to formula II having a Mg/Al ratio of 2 and a radical as a charge-balancing anion 62 5 g of an aqueous suspension of layered double hydroxide and 150 ml of 2-(2-ethylhexyloxy)ethanol were broken into a 500 ml glass reaction vessel equipped with a high-speed stirrer and heated to 85 Torr. Add ι215 grams of Kortacid® PKGH to the reaction vessel. Prior to addition, the fat 116965.doc -35- 200734275 fatty acid blend is heated to 85. After the fatty acid blend is added, the reaction vessel is heated while distilling off the water. /2_(2-ethylhexyloxy)ethanol The boiler is allowed to reach a temperature of 125 C. The reaction vessel is then cooled to about 5 Torr and the transferred slurry is removed. The slurry is then centrifuged at 4 Torr for about 1 Torr. The liquid is decanted. The solid was washed with acetone and dried under vacuum for 8 hours. The mixture was dried in an oven for 5 hours. The XRD pattern of the hydrotalcite clay prepared as described above showed a minor hydrotalcite φ related non-(hk0) reflection, indicating anionic Insertion of clay. The insert exhibits a characteristic d(〇〇i) value of 30 A. Example 12 A hydrotalcite layer according to formula II with 20 weights/〇 having a Mg/Al ratio of 2 and a hydroxyl group as a charge balancing anion 3 1.25 g of aqueous suspension of double hydroxide and 200 g of ethyi pr〇xit〇1 (purchased from SheU) were broken into a 500 ml glass reaction vessel equipped with a high-speed stirrer and heated to 85. 接着. Then 5.78 Ktacid Kortacid® PKGH and 0·28 gram of aminododecanoic acid were added to the reaction vessel. The fatty acid/aminododecanoic acid blend was heated to 85 ° C before addition. After the admixture was added , heating the reaction vessel while distilling out water/ethyl proxitol azeotrope Up to 12 〇. The temperature of 〇. Add 1 gram of ethyl proxitol to the slurry. Then cool the reaction vessel to about 50 ° C ' and remove the resulting slurry. Then the slurry is at 4, 〇〇〇rpjn Centrifugation for about 10 minutes. The liquid was decanted, and the solid was washed with acetone and dried overnight in an oven at 80 ° C under vacuum. The XRD pattern of the hydrotalcite clay prepared as described above shows that the secondary hydrotalcite is not _( Hk0) reflection, indicating the insertion of an anionic clay. The insert 116965.doc -36- 200734275 shows the characteristic d(001) value of 25A. Example 13 2 1.25 g of an aqueous suspension of hydrotalcite layered double hydroxide according to formula II having 20% by weight of a Mg/Al ratio and a hydroxyl group as a charge-balanced anion, and 200 g of ethyl proxitol were equipped with a high speed The mixer was placed in a 500 00 glass reaction vessel and heated to 85 °C. Next, 3.75 grams of Kortacid® PH05 and 4.87 grams of dehydrogenated rosin were added to the reaction vessel. The fatty acid/rosin blend was heated to 85 ° C prior to addition. After the addition of the blend, 1 50 grams of ethyl proxitol was added and the reaction vessel was heated while distilling off the water/ethyl proxitol azeotrope until a temperature of 120 °C was reached. The reaction vessel was then cooled to about 50 ° C and the resulting slurry was removed. The slurry was then centrifuged at 4,000 rpm for about 10 minutes. The liquid was decanted and the solid was dried in an oven at 80 ° C for 5 hours under vacuum. The XRD pattern of a hydrotalcite clay such as that described above shows a secondary hydrotalcite-related non-(hkO) reflection indicating the insertion of an anionic clay. This insert shows the characteristic d(001) value of 29A. Example 14 20 g of an aqueous suspension of hydrotalcite layered double hydroxide according to formula II having 20% by weight of a Mg/Al ratio of 2 and a hydroxyl group as a charge balancing anion and 1 50 g of ethyl proxitol (purchased from Shell) It was broken into a 500 ml glass reaction vessel equipped with a high-speed agitator and heated to 85 °C. Then, 6.3 g of Kortacid® PKGH and 6.3 g of hydrogenated rosin in 50 g of ethyl proxitol were added to the reaction vessel over a period of 15 minutes. The fatty acid/rosin exchange was heated to 85 ° C before addition. After the admixture is added, the reaction volume is heated 116965.doc -37- 200734275' while steaming the effluent/ethyl proxitol azeotrope until the temperature of i2 〇 °C is reached. The reaction vessel was then cooled to about 5 (rc, 1 gram of ethyl proxitol' was added and the resulting slurry was removed. The slurry was then centrifuged at 2,5 rpm for about 10 minutes. The liquid was decanted and the solid was used. The acetone was washed and dried overnight in an oven at 80 ° C under vacuum. The XRD pattern of the hydrotalcite clay prepared as described above shows a minor hydrotalcite-related non-(hkO) reflection indicating the insertion of an anionic clay. The characteristic d(〇〇i) value of 29A is shown. Example 15 1% of a hydrotalcite layered double hydroxide according to formula II having 20% by weight of a Mg/Al ratio and a hydroxyl group as a charge balancing anion The gram aqueous suspension and 21 g of ethyl proxit〇l (purchased from Shell) were broken into a 500 ml glass reaction vessel equipped with a high-speed stirrer and heated to 85 ° C. Then dissolved
於 21.85 公克 ethyl proxitol 中之 25.16 公克 Kortacid® PKGH 經30分鐘添加至該反應容器中。添加前,將脂肪酸摻和物 加熱至8 5 C。將所得混合物攪拌3小時。然後將反應容器 冷卻至約50°C,且移出所得漿料。然後將漿料於4,〇〇〇 rpm 下離心約1 0分鐘。傾析出液體,且將固體用水洗滌且於真 空下於80°c於烘箱中乾燥隔夜。 如上述製備之類水滑石黏土的XRD圖案顯示次要水滑石 相關非-(hkO)反射,表明陰離子性黏土之插入。該插入物 展示37.7A之特徵性d(001)值。 實例16 將20重量%具有2之Mg/Al比率及羥基作為電荷平衡陰離 116965.doc -38- 200734275 子之根據式π之類水滑石層狀雙氫氧化物之丨0〇公克水性懸 浮液及12.5公克ethyl proxitol(購自shell)潰入配備有高速 攪拌器之500 ml玻璃反應容器中且加熱至85。〇。接著將溶25.16 g of Kortacid® PKGH in 21.85 g of ethyl proxitol was added to the reaction vessel over 30 minutes. The fatty acid blend was heated to 85 C before the addition. The resulting mixture was stirred for 3 hours. The reaction vessel was then cooled to about 50 ° C and the resulting slurry was removed. The slurry was then centrifuged at 4, rpm for about 10 minutes. The liquid was decanted and the solid was washed with water and dried in an oven at 80 ° C overnight under vacuum. The XRD pattern of a hydrotalcite clay such as that described above shows a secondary hydrotalcite-related non-(hkO) reflection indicating the insertion of an anionic clay. The insert exhibits a characteristic d(001) value of 37.7A. Example 16 20% by weight of a Mg/Al ratio and a hydroxyl group as a charge balance anion 116965.doc -38- 200734275 according to the formula π, such as a hydrotalcite layered double hydroxide And 12.5 grams of ethyl proxitol (purchased from the shell) was broken into a 500 ml glass reaction vessel equipped with a high speed stirrer and heated to 85. Hey. Will dissolve
解於 12·5 公克 ethyl proxitol 中之 25.16 公克 Kortacid® PKGH 經3 0分鐘添加至該反應容器中。添加前,將脂肪酸摻和物 加熱至85°C。將所得混合物攪拌3小時。然後將反應容器 冷卻至約50°C,且移出所得漿料。然後將漿料於4,〇〇〇 rpm • 下離心約10分鐘。傾析出液體,且將固體用水洗滌且於真 空下於80 °C於供箱中乾燥隔夜。 如上述製備之類水滑石黏土的XRD圖案顯示次要水滑石 相關非-(hkO)反射,表明陰離子性黏土之插入。該插入物 展示38·4Α之特徵性d(001)值。 實例17 將 1,995 公克氧化鎂(Zolith,4〇,購自 Martin Marieua Magnesia Specialties LLC)及 mg公克氫氧化鋁(Alumiu φ F505)於7,500公克去礦質水中混合且研磨至1·5 μηι之平均 粒度do)。该漿料之部分用去礦質水稀釋至8·8重量%之固 含篁。將1.3 6 kg經稀釋漿料潰入配備有高速攪拌器之油加 熱咼壓釜内且加熱至80 °C。漿料添加前,將高壓爸潰入以 1.25 kg 2-乙氧基丙醇且加熱至8(rc。接著將高壓釜加熱至 120°C,且經 15 分鐘添加 354 公克 Kortacid® PH05 與 Prifac 7990之50/50(重量比)混合物。添加前,將脂肪酸摻和物加 熱至120 C。酸添加後,將高壓釜加熱至17(Γ(:且保持工小 時。然後將咼壓釜冷卻至約4〇°C,且移出所得漿料。過濾 116965.doc •39- 200734275 聚料且用丙酮大面積洗滌。所得物f於真空下於⑼。c於供 箱中乾燥隔夜。 所得包含脂肪酸摻和物之類水滑石黏土用乂光繞射分 析’以測定坑道間距或晶格間距。如上述製傷之類水滑石 黏土的XRD圖案顯示次要水滑石相關非_(hk〇)反射,表明 陰離子性黏土之插入。XRD顯示52A及3(^d(⑽U值。此 外,經洗滌之粉末的SEM分析展示所得矩形片晶之極高縱 橫比(L/D>l〇,〇〇〇)。 實例18 購自 Martin Marietta 將665公克氧化鎂(z〇lith〇® 4〇Solution to 12.5 grams of 12.5 grams of ethyl proxitol Kortacid® PKGH was added to the reaction vessel over 30 minutes. The fatty acid blend was heated to 85 °C prior to addition. The resulting mixture was stirred for 3 hours. The reaction vessel was then cooled to about 50 ° C and the resulting slurry was removed. The slurry was then centrifuged at 4 Torr rpm for approximately 10 minutes. The liquid was decanted and the solid was washed with water and dried overnight at 80 ° C in vacuo. The XRD pattern of a hydrotalcite clay such as that described above shows a secondary hydrotalcite-related non-(hkO) reflection indicating the insertion of an anionic clay. The insert exhibits a characteristic d(001) value of 38·4Α. Example 17 1,995 g of magnesium oxide (Zolith, 4 〇, available from Martin Marieua Magnesia Specialties LLC) and mg gram of aluminum hydroxide (Alumiu φ F505) were mixed in 7,500 g of demineralized water and ground to an average of 1.5 μm Particle size do). A portion of the slurry was diluted with demineralized water to 8% by weight solids. The 1.3 6 kg diluted slurry was broken into an oil-heated autoclave equipped with a high-speed stirrer and heated to 80 °C. Before the slurry was added, the high pressure dad was broken into 1.25 kg of 2-ethoxypropanol and heated to 8 (rc. The autoclave was then heated to 120 ° C, and 354 g of Kortacid® PH05 and Prifac 7990 were added over 15 minutes. 50/50 (by weight) mixture. Before the addition, the fatty acid blend was heated to 120 C. After the acid was added, the autoclave was heated to 17 (: (and kept for hours) and then the autoclave was cooled to about 4 ° ° C, and the resulting slurry was removed. Filtration 116965.doc • 39- 200734275 Aggregate and washed with acetone over a large area. The resulting material f was dried under vacuum in (9) c. overnight in a tank. Hydrotalcite-like clay is analyzed by calendering to determine the channel spacing or lattice spacing. The XRD pattern of the hydrotalcite clay such as the above-mentioned injury shows the secondary hydrotalcite-related non-(hk〇) reflection, indicating an anion. Insertion of clay. XRD shows 52A and 3 (^d((10)U values. In addition, SEM analysis of the washed powder shows the extremely high aspect ratio (L/D> l〇, 〇〇〇) of the resulting rectangular platelets. 18 from Martin Marietta will be 665 grams of magnesium oxide (z〇lith〇® 4〇
Magnesia Specialties LLC)及 576 公克氫氧化鋁(μ ⑽山 F505)於2,500公克去礦質水中混合且研磨至丨$ _之平均 粒,5。)。該漿料之部分用去礦質水稀釋至96重量%之固 含量。將229 g經稀釋漿料潰入配備有高速攪拌器之油加 <,、、门堊爸内j_加熱至9〇 c。敷料添加前,將高廢爸潰入以Magnesia Specialties LLC) and 576 grams of aluminum hydroxide (μ (10) Hill F505) were mixed in 2,500 grams of demineralized water and ground to an average of 丨$_, 5 . ). A portion of the slurry was diluted with demineralized water to a solids content of 96% by weight. 229 g of the diluted slurry was crushed into an oil equipped with a high-speed stirrer, and the door was heated to 9 〇 c. Before the dressing is added, the high waste dad will be broken into
2〇\ g 2-乙氧基丙醇且加熱至啊。接著將高慶爸加熱至 120C ’ X保持約15分鐘。然後將高壓爸加熱至”代且保 持1小時。反應後,將高壓釜冷卻至6(rc以下,且移出所 得聚料。過濾漿料且用丙酮大面積洗滌。所得物質於真空 下於80°C於烘箱中乾燥隔夜。 / & 戶二得之類水滑石黏土μ光繞射分析,以測定坑道間距 或日曰格間距。如上述製備之類水滑石黏土的XRD圖案顯示 水滑石結構典型之_)及_)反射及對應於水鎖石之— 些次要信號。 116965.doc2〇\ g 2-ethoxypropanol and heated to ah. Then heat the Gaoqing dad to 120C ’ X for about 15 minutes. The high pressure dad was then heated to "regeneration" for 1 hour. After the reaction, the autoclave was cooled to 6 (rc below, and the resulting polymer was removed. The slurry was filtered and washed extensively with acetone. The resulting material was at 80 ° under vacuum. C is dried overnight in an oven. / & Fluorescence analysis of hydrotalcite clay such as hushui to determine the pitch of the tunnel or the spacing of the grid. The XRD pattern of the hydrotalcite clay prepared as described above shows the typical hydrotalcite structure. _) and _) reflections and corresponding to the water lock stone - some secondary signals. 116965.doc
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CN102009959A (en) * | 2010-09-10 | 2011-04-13 | 北京理工大学 | Preparation method of organic acid anion intercalation hydrotalcite |
US9410031B2 (en) * | 2011-06-28 | 2016-08-09 | Flow Polymers, Llc | Organic functionalization of layered double hydroxides |
CN104379661B (en) * | 2012-05-15 | 2017-06-06 | 株式会社普利司通 | For the halogenation diene rubber of tire |
ITUD20130030A1 (en) * | 2013-03-01 | 2014-09-02 | Sumeet Kumar | HYBRID COMPOSITE NANOMATERIALS |
CN103359792B (en) * | 2013-07-22 | 2015-01-14 | 中国科学院青海盐湖研究所 | MgFe binary hydrotalcite-like compound with high iron content and preparation method thereof |
EP2933300A1 (en) * | 2014-04-16 | 2015-10-21 | BASF Coatings GmbH | Composition based on layered hydroxides and polyesters, method for preparing the composition and its use |
CN104192810B (en) * | 2014-08-15 | 2015-10-28 | 浙江大学 | A kind of preparation method of layered double-hydroxide of large interlamellar spacing |
WO2016110698A1 (en) * | 2015-01-06 | 2016-07-14 | Scg Chemicals Co., Ltd. | Sio2-layered double hydroxide microspheres and methods of making them |
GB201502832D0 (en) * | 2015-02-19 | 2015-04-08 | Scg Chemicals Co Ltd And Scg Cement Co Ltd | Process for preparing small size layered double hydroxide particles |
CA3007497C (en) * | 2015-12-18 | 2020-12-15 | Saint-Gobain Placo | Gypsum product composition, gypsum products, and a method for using a compound in gypsum board |
US11242460B2 (en) | 2016-11-15 | 2022-02-08 | Scg Chemicals Co., Ltd. | Surface modified layered double hydroxide |
GB201703558D0 (en) * | 2017-03-06 | 2017-04-19 | Univ Oxford Innovation Ltd | catalysts |
US10745606B2 (en) * | 2017-08-15 | 2020-08-18 | Saudi Arabian Oil Company | Oil-based drilling fluid compositions which include layered double hydroxides as rheology modifiers |
CN108948749A (en) * | 2018-07-06 | 2018-12-07 | 佛山市高明区爪和新材料科技有限公司 | A kind of bullet O-shaped rubber seal and preparation method thereof |
CN110641118B (en) * | 2019-10-17 | 2021-07-27 | 厦门长塑实业有限公司 | High-barrier scratch-resistant biaxially oriented polyamide film and preparation method thereof |
CN110639366B (en) * | 2019-10-26 | 2021-06-18 | 北京工业大学 | A method for preparing Fe-cage intercalated layered double metal hydroxide nanofiltration membrane |
CN113493225B (en) * | 2021-08-11 | 2023-11-10 | 洛阳理工学院 | Preparation method and application of Co/Fe layered double hydroxide nanosheets |
CN116162304A (en) * | 2023-03-02 | 2023-05-26 | 江苏馨德高分子材料股份有限公司 | Polyethylene sheath material prepared from modified montmorillonite and preparation method thereof |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5518704A (en) * | 1993-07-06 | 1996-05-21 | Aristech Chemical Corporation | Nickel and cobalt containing hydrotalcite-like materials having a sheet-like morphology and process for production thereof |
DE19836580A1 (en) * | 1998-08-12 | 2000-02-17 | Sued Chemie Ag | A compound material with a polymer matrix and a double layer hydroxide with anionic compounds between the layers useful for nano-composite-fillers in polymer matrixes avoids the use of expensive quaternary ammonium compounds |
WO2001004053A1 (en) * | 1999-07-08 | 2001-01-18 | Mizusawa Industrial Chemicals, Ltd. | Composite polybasic salt, process for producing the same, and use |
US6846870B2 (en) * | 2001-08-23 | 2005-01-25 | Sunoco, Inc. (R&M) | Hydrotalcites, syntheses, and uses |
US6979708B2 (en) * | 2001-08-23 | 2005-12-27 | Sunoco, Inc. (R&M) | Hydrotalcites, syntheses, and uses |
DE10235571A1 (en) * | 2002-08-03 | 2004-02-12 | Clariant Gmbh | New magnesium-aluminum hydroxide-carbonates with sebacic acid anions and use of foliated double hydroxide salt as charge regulator in electrophotographic toner or developer, powder lacquer, electret or electrostatic separation |
NO20035745D0 (en) * | 2003-12-19 | 2003-12-19 | Amersham Health As | Process |
JP4058767B2 (en) * | 2004-11-04 | 2008-03-12 | 船井電機株式会社 | Switching power supply |
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2006
- 2006-12-01 CN CN2006800452623A patent/CN101321691B/en not_active Expired - Fee Related
- 2006-12-01 CN CN2006800457383A patent/CN101321692B/en not_active Expired - Fee Related
- 2006-12-01 BR BRPI0619473-7A patent/BRPI0619473A2/en not_active IP Right Cessation
- 2006-12-01 ES ES06830271T patent/ES2385672T3/en active Active
- 2006-12-01 AT AT06830271T patent/ATE556031T1/en active
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- 2006-12-04 CN CNA2006800453838A patent/CN101321697A/en active Pending
- 2006-12-06 TW TW095145442A patent/TWI381991B/en not_active IP Right Cessation
- 2006-12-06 TW TW95145443A patent/TW200734387A/en unknown
- 2006-12-06 TW TW95145446A patent/TW200734275A/en unknown
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ES2385672T3 (en) | 2012-07-30 |
BRPI0619473A2 (en) | 2011-10-04 |
CN101360782A (en) | 2009-02-04 |
CN101321692B (en) | 2012-08-22 |
CN101321691A (en) | 2008-12-10 |
TW200736161A (en) | 2007-10-01 |
CN101321692A (en) | 2008-12-10 |
ATE556031T1 (en) | 2012-05-15 |
TWI398405B (en) | 2013-06-11 |
TW200734269A (en) | 2007-09-16 |
TWI381991B (en) | 2013-01-11 |
TW200734387A (en) | 2007-09-16 |
CN101321697A (en) | 2008-12-10 |
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