TW294684B - - Google Patents
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- TW294684B TW294684B TW082105473A TW82105473A TW294684B TW 294684 B TW294684 B TW 294684B TW 082105473 A TW082105473 A TW 082105473A TW 82105473 A TW82105473 A TW 82105473A TW 294684 B TW294684 B TW 294684B
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G69/00—Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G69/00—Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
- C08G69/02—Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids
- C08G69/08—Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids derived from amino-carboxylic acids
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G69/00—Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
- C08G69/02—Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids
- C08G69/08—Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids derived from amino-carboxylic acids
- C08G69/10—Alpha-amino-carboxylic acids
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G73/00—Macromolecular compounds obtained by reactions forming a linkage containing nitrogen with or without oxygen or carbon in the main chain of the macromolecule, not provided for in groups C08G12/00 - C08G71/00
- C08G73/06—Polycondensates having nitrogen-containing heterocyclic rings in the main chain of the macromolecule
- C08G73/10—Polyimides; Polyester-imides; Polyamide-imides; Polyamide acids or similar polyimide precursors
- C08G73/1046—Polyimides containing oxygen in the form of ether bonds in the main chain
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G73/00—Macromolecular compounds obtained by reactions forming a linkage containing nitrogen with or without oxygen or carbon in the main chain of the macromolecule, not provided for in groups C08G12/00 - C08G71/00
- C08G73/06—Polycondensates having nitrogen-containing heterocyclic rings in the main chain of the macromolecule
- C08G73/10—Polyimides; Polyester-imides; Polyamide-imides; Polyamide acids or similar polyimide precursors
- C08G73/1092—Polysuccinimides
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- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Macromolecular Compounds Obtained By Forming Nitrogen-Containing Linkages In General (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Polyamides (AREA)
- Polyethers (AREA)
- Polyesters Or Polycarbonates (AREA)
Description
經濟部t央標準局員工消費合作社印製 394684 a7 _B7_/五、發明説明(1 .) 本發明供鼷於一種製造聚琥珀β亞胺之方法,詳細而 言,本發明傈鼷於一種由馬來醯胺酸及聚(亞《二酵)製造 聚琎珀醒亞胺之方法。 已知有數種習用方法可製取聚躭珀醯亞胺,並予以水 解形成可供多種用途之聚(胺基酸),包括作為吸附_,硬 表面淸潔劑,鍋爐及冷卻塔用之水處理添加薄,及作為肋 洗雨,抗膜爾,分散爾,掩護劑及結垢'抑制薄等去垢添加 劑。然而,所有製迪聚琥珀S亞胺之習知方法均有反應時 間過長,起始材料昂貴,或涉及業界所面對之多種困難之 固體材料之處理間題。 Koskan氏之美國專利案第5 , 057 , 597號掲述一種在至 少18QO之溫度及氮氣面氛下攪拌約三至六小時以使胺基 酸流臞化而製成聚琥珀醸亞胺之固相製法。所生成之聚琥 珀醛亞胺繼後被水解成為聚(胺基酸)。 8〇611丨1^氏等人之美國專利案第4,839,461號掲述一 種聚(丁氛二酸)之製造方法,該法將馬來酸或馬來酸酐輿 氛溶液以1:1-1.5之克分子董比例混合。然後将該混合物 加熱至120- 1501C,繼之將銨Si與馬來酸之生成溶蒸發, 餘留下結晶軟塊。隨邸使结晶軟塊熔化,同時将鐘合與结 晶之水皤除,製得聚(丁®二酸)之多孔性塊臞。 整傾程序需時六至八小時。 典』111〇11<^〇公司之日本專利案第52-00 88 773 8號掲 述聚(丁®二酸)之溶»粂製造方法。該專利案僳使用丁氛 二酸野之氫鹵酸鹽於一或多種有檐溶劑中。所掲示之溶》 -4- (請先閲讀背面之注意事項再填寫本頁) .I- 1 ^^1 J—»· .裝· -線· 本紙張尺度適用中國國家標準(CNS ) Α4規格(2丨0X297公釐) A7 B7 經濟部中央標隼局員工消費合作社印裝 五、發明説明(2 ) 像諸如丙酸,丁酸及戊酸等之有機酸;諸如第三丁酵及第 三戊酵等之酵;諸如醋酸乙酯及醋酸丁酯等之醋;諸如甲 基異丁基酮及環己酵等之83;諸如四氫呋喃及二氣雜環己 烷等之醮;諸如二氛化乙烯及二氛苯等之鹵化烀;諸如甲 苯,二甲苯及系烷等之烴類;及諸如二甲替甲醯胺等之醯 胺。逭些溶劑將付出更大之危險性,更高之成本,更«烈 之奥味及籌性,及更褀雜之去除步霣以取得最終産品。 聚琥珀醯亞胺與聚(胺基酸)之傳統合成方法均極為耗 時,複雜或需使用大量之揮發性有機溶ϋ或惟性氣鱅。本 文中”聚琥珀醒亞胺(複數)”一詞僳指在聚醱«中含有琥珀 酵亞胺組份及其他組份之聚合物質,而”聚琥珀醯亞胺(單 數)”像指僅含有琥珀醒亞胺組份之聚合物質。 本發明之一目的僳提供一種裂造聚琥珀醒亞胺之溶劑 法。 本發明之另一目的傷提供一種不需要分離産物步驟之 製造聚躭珀睡亞胺之溶爾法。 本發明僳採取下列步*製造聚琥珀酵亞胺: a) 由聚(亞烴二酵)及馬來醯胺酸形成聚合混合物; b) 将混合物加熱至一昇高溫度;及 〇) 使混合物維持於該昇溫下以形成聚琥珀醯亞胺。 適用於本發明之聚(亞烴二醇)偽在反應溫度下流龌化 者。適當之聚(亞烴二酵)包括聚(四亞甲基二酵),聚(乙 二醇),及聚(丙二酵聚(亞烴二酵)之一雇或兩値末端 基可為羧酸,1至30餹碩原子之烷基,或胺,或1至10
本紙張尺度適用t國國家標準(CNS ) Α4規格(210X297公釐) ------.—丨n 装-- (請先閲讀背面之注意事項再填寫本頁) 訂 經濟部中央標準局員工消費合作社印裝 294684 A7 B7 五、發明説明(3 ) 但硪原子之烷基胺,或上逑之任何組合。最好聚(亞《二 酵)傜二乙二酵醚,聚(乙二酵),末端甲基聚(乙二酵), 或聚(丙二酵)。聚(亞®二酵)之分子Λ可离達約30,000, 最好為3 0 0至20, 00 0左右•以約1 , 0 0 0至15,000更可取 。聚(亞烴二酵)以相對於馬來睡胺酸之2至約90重量% ,約20至90更佳,約30至85重量%最可取之量添加於 聚合反瓤混合物中。 — 除了馬來醯胺酸以外,聚琥珀醯亞胺亦可依本發明之 方法添加高逹80重(以馬來醣胺酸之重量計)之一或多 種其他醯胺基酸製成。通用之其他醯胺基酸包括甲基寓馬 酸,亞甲基丙二酸,分解烏頭酸,順式甲基丁烯二酸,烏 頭酸,烷基馬來酸,烯基琥珀酸,聚(甲基丙烯酸)之一乙 烯条不飽和齊聚鱷,丁烯-1,3,4 -三羧酸,一甲基馬來酸醣, 一甲基分解烏頭酸酯,丙烯酸,甲基丙烯酸,及巴亘酸之 釅胺基酸。在使用時,該一或多種其他醯胺基酸最好僳用 佔馬來醯胺酸重量之5至約70%,最好為約10至60重量% 之董。 聚合反應之圍氛宜實質上不含氧氣,包括空氣中之* 氣。因於聚縮合反應發生之溫度下,聚(亞烴二酵)將會被 氣化,楢色或降解,故团氛宜為無氧。達至無氣之園氛之 適當方式偽以梅氣,最好為氰氣,匾罩,掃流或吹氣於反 應器,或在減壓下實施聚合作用。 本發明之昇高通度匾足以提供聚缩合作用。較可取之 溫度視操作條件而定。例如,當馬來醯胺酸及一或多種其 本紙張尺度適用中國國家標準(CNS ) Α4規格(210 X 297公釐) I U 一 裝 — ϋ 訂 I ^ (請先聞讀背面之注意事項再填寫本頁) 經濟部中央標準局貞工消費合作杜印製 Α7 Β7 五、發明説明(4 ) 他酵胺基酸對聚(亞《二酵)之比例增加,或聚禳合進行之 壓力增加時,較可取之溫度将會增高。然而,例如在共沸 溶爾存在下,較可取溫度將會降低。一般而言.較可取之 昇溫傜大約120至25〇υ。 聚琥珀醏亞胺僳由縮合反應製成。因此最好能将所産 生之諸如水或酵等副産物去除以驅使反臁完成。埵當之去 水方法包括将諸如甲苯,二甲苯或Γ, 2 ,ϋ -四氳化綦等之 一或多種共沸溶W添加於聚合作用混合物中,再將共沸物 從聚合作用混合物皤除。另一種去水方法换添加諸如矽酸 鋁等之一或多種乾燥劑於聚合作用混合物中。再一種去水 方法傜將愔氣吹入聚合混合物内,或使梅氣播流於聚合混 合物之表面。又一種方法則在滅壓下實施聚合作用。 聚合作用可以分批或連缅方式進行。適用之反«器包 括分批槽反臁器,連鑛攪拌槽反應器,活塞式流動反應器, 管式反應器及刮壁式反麻器等。反應器之溫度必須足以将 縮合反慝所釋出之水去除。此溫度將隨是否使用共沸溶_ 及實施聚合作用之壓力,包括真空計壓力,大氣壓力,超 計大氣壓,而改變。 由本發明之方法所形生之産物偽聚琥珀酾亞胺於聚(亞 烴二酵)中之溶液,懸浮液或分散液。聚(亞烴二醇)可有 效應用於聚(琥珀醛亞胺)之多種用途,例如在清潔劑配製 方面之應用。因此當産物用於淸潔劑用途時不需分離步思 将聚(琥珀醯亞胺)自聚(亞烴二醇)中離析。若情況需要可 藉任何傳統方式水解聚(琥珀酵亞胺)以形成相對之聚(胺 本紙張尺度適用中國國家橾準(CNS ) A4規格(210X297公釐) ------:ITJ 裝-- (請先閲讀背面之注意事項再填寫本頁) 訂 2^4684 a? B7 五、發明説明(5 ) 基酸),諸如聚(丁氨二酸較可取之水解方式傈使産物 與諸如氳氣化納或磺酸納等水性齡溶液接觸。 賁施例1:聚(琥珀匿亞胺)之製備 於一装配有磁性攪拌棒,回流冷襄器,及氰氣入口輿 出口之100毫升裝三頸園底燒瓶中加入5.0克之馬甲醯胺 酸及分子量為8,000之5.0克之聚(乙二酵以《氣持鑛 播流燒瓶及將其浸入保持在19〇υ之油槽中達3.5小時, 再冷卻至室溫。由1Η HHR光譜分析顯示無馬來醏胺酸留存 。以稀轘水性硪酸銷水解聚琥珀醯亞胺以形成聚 (丁第二 酸)β 1Η UUR光譜之分析證實聚(丁氨二酸)之形成β 實施例2 重覆實施例1之步想,唯使用分子量為350之聚(乙 二酵)一甲基醚;將燒瓶浸入保持在1 5 0 - 1 6 0 *〇之油槽中 逹1小時。由1Η NMR光譜分析顯示無馬來醯按酸留存及證 實聚琥珀醯亞胺之形成。 ------:—; —^衣------訂 (請先閲讀背面之注意^項再填寫本頁) 經濟部中央標準局—工消费合作社印製 -8 - 本紙張尺度適用中國國家標準(CNS ) Α4規格(210Χ297公釐)
Claims (1)
- 4:伽 | I < ·申請專利範圍 1. 一種聚琥珀醒亞胺之製造方法,其步*包括: 1)由馬來醯胺酸及選自二乙二酵醚、聚乙二酵、末 端甲基聚乙二酵及聚丙二酵蘧出之一種聚亞烴二酵形成聚 合反醮混合物,而此混合物中含有相對於馬來醯胺酸之重 置之2〜90重最%之聚亞烴二酵; 2 )將該混合物加熱至1 2 0〜2 5 0 *〇之較高溫度;及 3)將該混合物保持於該較高溫度,以形成聚琥珀醯 亞胺》 2. 如申請專利範麵第1項之方法,其中該聚亞《二 酵傜聚乙二酵。 3· 如申請專利範匾第1項之方法,其中該聚合反廛 混合物含有相對於馬來醯胺酸之重*之30〜85重董%之 聚亞烴二酵。 Ml.I-Μ (請先閲讀背面之注意事項再填寫本頁) 經濟部中央標準局貝工消費合作社印製 物 合 混 該 中 其 法 方 之 項 〇 1 下 第境 国琛 範溫 利高 專之 讅氣 申無 如質 實 5 於 持 保 本紙張尺度逋用中國國家標準(CNS )八1 2規格(210X297公釐) 1 如申請專利範匾第1項之方法,該方法進一步包 2 括將聚琥珀醛亞胺水解形成對應之聚胺基酸之步B。
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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US07/911,865 US5371177A (en) | 1992-07-10 | 1992-07-10 | Process for preparing polysuccinimides from maleamic acid |
Publications (1)
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TW294684B true TW294684B (zh) | 1997-01-01 |
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TW082105473A TW294684B (zh) | 1992-07-10 | 1993-07-09 |
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US (2) | US5371177A (zh) |
EP (1) | EP0578450B1 (zh) |
JP (1) | JPH06211983A (zh) |
KR (1) | KR940005712A (zh) |
CN (1) | CN1035191C (zh) |
AT (1) | ATE162204T1 (zh) |
AU (1) | AU666195B2 (zh) |
BR (1) | BR9302724A (zh) |
CA (1) | CA2099461A1 (zh) |
DE (1) | DE69316277T2 (zh) |
ES (1) | ES2112390T3 (zh) |
MX (1) | MX9303792A (zh) |
MY (1) | MY108917A (zh) |
NZ (1) | NZ247843A (zh) |
TW (1) | TW294684B (zh) |
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US5380817A (en) * | 1992-07-10 | 1995-01-10 | Rohm And Haas Company | Process for preparing polysuccinimides from aspartic acid |
US5371177A (en) * | 1992-07-10 | 1994-12-06 | Rohm And Haas Company | Process for preparing polysuccinimides from maleamic acid |
US5393868A (en) * | 1992-10-13 | 1995-02-28 | Rohm And Haas Company | Production of polysuccinimide by thermal polymerization of maleamic acid |
US5389303A (en) * | 1993-09-10 | 1995-02-14 | Srchem Incorporated | Mixtures of polyamino acids and citrate |
CA2132112A1 (en) * | 1993-09-21 | 1995-03-22 | David Elliott Adler | Acid catalyzed process for preparing amino acid polymers |
EP0650995B1 (de) * | 1993-11-02 | 2000-01-05 | Bayer Ag | Verfahren zur Herstellung von Asparaginsäure-haltigen Polymeren |
US5491213A (en) * | 1994-01-28 | 1996-02-13 | Donlar Corporation | Production of polysuccinimide |
US6005069A (en) * | 1996-12-18 | 1999-12-21 | Donlar Corporation | Production of polysuccinimide and derivatives thereof in a sulfur-containing solvent |
US5981691A (en) * | 1997-04-23 | 1999-11-09 | University Of South Alabama | Imide-free and mixed amide/imide thermal synthesis of polyaspartate |
US6136950A (en) | 1997-09-23 | 2000-10-24 | Mbt Holding Ag | Highly efficient cement dispersants |
US6076997A (en) * | 1997-12-03 | 2000-06-20 | Mbt Holding Ag | Deep mix soil stabilization method |
DE19822604A1 (de) | 1998-05-20 | 1999-11-25 | Goldschmidt Ag Th | Kondensationsprodukte enthaltend polyethermodifizierte Monoester und/oder -amide alpha, beta-ungesättigter Dicarbonsäuren, ihre Herstellung und Verwendung |
CN100343305C (zh) * | 2002-12-31 | 2007-10-17 | 尼克塔治疗亚拉巴马公司 | 马来酰胺酸聚合物衍生物及其生物轭合物 |
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US3846380A (en) * | 1972-10-31 | 1974-11-05 | M Teranishi | Polyamino acid derivatives and compositions containing same |
IT1000589B (it) * | 1972-12-26 | 1976-04-10 | Ajinomoto Kk | Procedimento per preparare un poli amminoacido |
JPS528873A (en) * | 1975-07-09 | 1977-01-24 | Matsushita Electric Ind Co Ltd | Maximum demand monitor indication unit |
JPS60203636A (ja) * | 1984-03-28 | 1985-10-15 | Fuso Kagaku Kogyo Kk | コポリアミノ酸の製造法 |
DE3626672A1 (de) * | 1986-08-07 | 1988-02-11 | Bayer Ag | Polyasparaginamidsaeure |
DD262665A1 (de) * | 1987-06-17 | 1988-12-07 | Akad Wissenschaften Ddr | Verfahren zur herstellung von polyaspartimid |
US5057597A (en) * | 1990-07-03 | 1991-10-15 | Koskan Larry P | Process for the manufacture of anhydro polyamino acids and polyamino acids |
DE4023463C2 (de) * | 1990-07-24 | 1999-05-27 | Roehm Gmbh | Verfahren zur Molekulargewichtserhöhung bei der Herstellung von Polysuccinimid |
US5221733A (en) * | 1991-02-22 | 1993-06-22 | Donlar Corporation | Manufacture of polyaspartic acids |
JP3153326B2 (ja) * | 1992-04-08 | 2001-04-09 | 株式会社トーキン | 衝突センサ |
US5319145A (en) * | 1992-07-10 | 1994-06-07 | Rohm And Haas Company | Method for preparing polysuccinimides with a rotary tray dryer |
US5371177A (en) * | 1992-07-10 | 1994-12-06 | Rohm And Haas Company | Process for preparing polysuccinimides from maleamic acid |
US5296578A (en) * | 1992-09-18 | 1994-03-22 | Donlar Corporation | Production of polysuccinimide and polyaspartic acid from maleic anhydride and ammonia |
US5219952A (en) * | 1992-09-18 | 1993-06-15 | Donlar Corporation | Production of high molecular weight polysuccinimide and high molecular weight polyaspartic acid from maleic anhydride and ammonia |
US5393868A (en) * | 1992-10-13 | 1995-02-28 | Rohm And Haas Company | Production of polysuccinimide by thermal polymerization of maleamic acid |
-
1992
- 1992-07-10 US US07/911,865 patent/US5371177A/en not_active Expired - Fee Related
-
1993
- 1993-06-10 NZ NZ247843A patent/NZ247843A/en unknown
- 1993-06-10 AU AU40157/93A patent/AU666195B2/en not_active Ceased
- 1993-06-21 JP JP5149001A patent/JPH06211983A/ja not_active Withdrawn
- 1993-06-24 MY MYPI93001226A patent/MY108917A/en unknown
- 1993-06-24 MX MX9303792A patent/MX9303792A/es not_active IP Right Cessation
- 1993-06-30 BR BR9302724A patent/BR9302724A/pt not_active Application Discontinuation
- 1993-06-30 CA CA002099461A patent/CA2099461A1/en not_active Abandoned
- 1993-07-02 ES ES93305213T patent/ES2112390T3/es not_active Expired - Lifetime
- 1993-07-02 DE DE69316277T patent/DE69316277T2/de not_active Expired - Fee Related
- 1993-07-02 AT AT93305213T patent/ATE162204T1/de not_active IP Right Cessation
- 1993-07-02 EP EP93305213A patent/EP0578450B1/en not_active Expired - Lifetime
- 1993-07-09 TW TW082105473A patent/TW294684B/zh active
- 1993-07-09 KR KR1019930012926A patent/KR940005712A/ko not_active Application Discontinuation
- 1993-07-10 CN CN93108566A patent/CN1035191C/zh not_active Expired - Fee Related
-
1994
- 1994-08-25 US US08/296,081 patent/US5463017A/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
MX9303792A (es) | 1994-02-28 |
BR9302724A (pt) | 1994-03-01 |
EP0578450A2 (en) | 1994-01-12 |
CA2099461A1 (en) | 1994-01-11 |
ES2112390T3 (es) | 1998-04-01 |
CN1082066A (zh) | 1994-02-16 |
MY108917A (en) | 1996-11-30 |
JPH06211983A (ja) | 1994-08-02 |
CN1035191C (zh) | 1997-06-18 |
AU4015793A (en) | 1994-01-13 |
EP0578450A3 (en) | 1994-07-27 |
EP0578450B1 (en) | 1998-01-14 |
US5463017A (en) | 1995-10-31 |
AU666195B2 (en) | 1996-02-01 |
DE69316277T2 (de) | 1998-08-27 |
KR940005712A (ko) | 1994-03-22 |
ATE162204T1 (de) | 1998-01-15 |
US5371177A (en) | 1994-12-06 |
NZ247843A (en) | 1995-03-28 |
DE69316277D1 (de) | 1998-02-19 |
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