Abstract:
화학식 (I) 에따른킬레이트제의제조법으로서: R-CH(COOX)-N(CHCOOX)(I) [식중, R은수소, C-C-알킬, 페닐, 벤질, CHOH, 및 CHCHCOOX로부터선택되고, X는 (MH) 이고 (이때, M 은알칼리금속으로부터선택됨), x 는 0.6 내지 1 의범위임] 하기단계를포함하는제조법: (a) 화학식 (II a) 에따른화합물의고체, 슬러리또는용액을제공하는단계: R-CH(COOX)-N(CHCN)(II a) [식중, X는 (MH) 이고, (이때, M 은알칼리금속으로부터선택됨) y 는 0 내지 1 범위임] (b) 상기고체또는슬러리또는용액을, 알칼리금속히드록시드의수성용액과접촉시키는단계로서, 이때알칼리금속이온대 니트릴기의몰비는 0.6:1 내지 0.95:1 의범위인단계, (c) 화학식 (II a) 에따른상기화합물을상기알칼리금속히드록시드와반응시키는단계.
Abstract translation:根据通式(I),R1-CH(COOX1)-N(CH2COOX1)2制备螯合剂的方法,其中R1选自氢,C1-C4-烷基,苯基,苄基,CH2OH和CH2CH2COOX1,X1 是(M 1 H 1-x),M选自碱金属,x在0.6至1的范围内,所述方法包括以下步骤:(a)提供根据一般化合物的固体,浆液或溶液 其中X2是(MyH1-y),M选自碱金属,y在0-1的范围内,(b)使所述固体与式(IIa)R1-CH 或浆液或溶液与碱金属氢氧化物的水溶液反应,其中碱金属离子与腈基团的摩尔比在0.6:1至0.95:1的范围内,(c)使所述通式(II)的化合物与通式 a)与所述碱金属氢氧化物反应。
Abstract:
Process for making a chelating agent according to the general formula (I), R1-CH(COOX1)-N(CH2COOX1)2 wherein R1 is selected from hydrogen, C1-C4-alkyl, phenyl, benzyl, CH2OH, and CH2CH2COOX1, X1 is (ΜχΗ1-χ), M being selected from alkali metal, x is in the range of from 0.6 to 1, said process comprising the following steps: (a) providing a solid, a slurry or a solution of a compound according to general formula (II a) R1-CH(COOX2)-N(CH2CN)2 wherein X2 is (MyH1-y), M being selected from alkali metal, y is in the range of from zero to 1, (b) contacting said solid or slurry or solution with an aqueous solution of alkali metal hydroxide, wherein the molar ratio of alkali metal ions to nitrile groups is in the range of from 0.6:1 to 0.95:1, (c) reacting said compound according to general formula (II a) with said alkali metal hydroxide.
Abstract:
Process for making a chelating agent according to the general formula (I), R1-CH(COOX1)-N(CH2COOX1)2 wherein R1 is selected from hydrogen, C1-C4-alkyl, phenyl, benzyl, CH2OH, and CH2CH2COOX1, X1 is (???1-?), M being selected from alkali metal, x is in the range of from 0.6 to 1, said process comprising the following steps: (a) providing a solid, a slurry or a solution of a compound according to general formula (II a) R1-CH(COOX2)-N(CH2CN)2 wherein X2 is (MyH1-y), M being selected from alkali metal, y is in the range of from zero to 1, (b) contacting said solid or slurry or solution with an aqueous solution of alkali metal hydroxide, wherein the molar ratio of alkali metal ions to nitrile groups is in the range of from 0.6:1 to 0.95:1, (c) reacting said compound according to general formula (II a) with said alkali metal hydroxide.
Abstract:
The present invention relates to a method for the production of aminodicarboxylic acid-N,N,diacetic acids of the general Formula I, wherein X independently of one another represents hydrogen or an alkali metal and n represents a number 1 or 2. Furthermore, the invention relates to aminodicarboxylic acid-N,N-diacetic acids of high purity. The inventive method comprises the following steps: a) reacting an aminodicarboxylic acid of the general Formula II, wherein X and n have the aforementioned meanings, with 0.8 to 1.2 mole equivalents of formaldehyde and with 0.8 to 1.2 mole equivalents of hydrocyanic acid; b) reacting the reaction products of step a) with 0.8 to 1.2 mole equivalents of hydrocyanic acid and with 0.8 to 1.2 mole equivalents of formaldehyde; c) hydrolyzing in the reaction product obtained in step b).
Abstract:
Isolating methyl glycine nitrile-N,N-diacetonitrile (MGDN) from an MGDN containing aqueous mixture, comprises at least one step of cooling the mixture with a cooling rate of at least 20 K/hour from the temperature above the freezing point of MGDN to a temperature below the freezing point of MGDN, where the method is carried out continuously.
Abstract:
The invention relates to a process for preparing low-by-product, light-color methylglycine-N,N-diacetic acid tri(alkali metal) salt by alkaline hydrolysis of methylglycinediacetonitrile (MGDN), comprising the steps in the sequence (a) to (f): (a) mixing of MGDN with aqueous alkali at a temperature of ≦̸30° C.; (b) allowing the aqueous alkaline MGDN suspension to react at a temperature in the range from 10 to 30° C. over a period of from 0.1 to 10 h to form a solution; (c) allowing the solution from step (b) to react at a temperature in the range from 30 to 40° C. over a period of from 0.1 to 10 h; (d) optionally allowing the solution from step (c) to react at a temperature in the range from 50 to 80° C. over a period of from 0.5 to 2 h; (e) optionally allowing the solution from step (c) or (d) to react at a temperature in the range from 110 to 200° C. over a period of from 5 to 60 min; (f) hydrolysis and removal of ammonia of the solution obtained in step (c), (d) or (e) by stripping at a temperature of from 90 to 105° C.
Abstract:
Procedimiento para la producción de ácidos N,N-diacéticos de ácido aminodicarboxílico de la fórmula general I,**Fórmula** representando X independientemente entre sí hidrógeno o metal alcalino e indicando n un número 1 o 2, comprendiendo los pasos: a) reacción de un ácido aminodicarboxílico de la fórmula general II**Fórmula** teniendo X y n los significados que se han mencionado anteriormente, con 0,8 a 1,2 equivalentes molares de formaldehído y con 0,8 a 1,2 equivalentes molares de ácido cianhídrico, comprendiendo la adición de formaldehído y ácido cianhídrico, disponiéndose el ácido aminodicarboxílico en el recipiente de reacción y añadiéndose formaldehído y ácido cianhídrico; se deja reaccionar durante un periodo de tiempo de un minuto hasta 5 horas, b) a continuación reacción del producto de reacción obtenido en el paso a) con 0,8 a 1,2 equivalentes molares de ácido cianhídrico y con 0,8 a 1,2 equivalentes molares de formaldehído; c) hidrólisis del producto de reacción obtenido en el paso b).
Abstract:
Aqueous solution containing in the range of from 60.5 to 75 % by weight of a mixture of trialkalimetal salts of the L-and D-enantiomers of methyl glycine diacetic acid (MGDA), said mixture containing predominantly the respective L-isomer with an enantiomeric excess (ee) in the range of from 3 to 97%, wherein said trialkali metal salts have the general formula (I) [CH3-CH(COO)-N(CH2-COO)2]K3-xNax (I) wherein x is in the range of from zero to 2.9.
Abstract:
Se provee un método para aislar metilglicinanitrilo-N,N-diacetonit rilo (MGDN) de una mezcla acuosa que comprende MGDN. El método comprende enfriar la mezcla acuosa en uno o más pasos. En uno de estos pasos, la mezcla se enfría a una velocidad de enfriamiento de por lo menos 20 K/h desde una temperatura arriba del punto de solidificación de MGDN a una temperatura debajo del punto de solidificación de MGDN. El método es implementado continuamente.