首页> 外国专利> Biodegradable polyesters and polymers biodegradable moldable thermoplastic compositions processes for the preparation of biodegradable polyesters and polymers and biodegradable moldable thermoplastic compositions use of biodegradable plastic moldable compostable adhesives biodegradable mixtures process for the production of biodegradable mixtures use of biodegradable polymers and biodegradable polymers

Biodegradable polyesters and polymers biodegradable moldable thermoplastic compositions processes for the preparation of biodegradable polyesters and polymers and biodegradable moldable thermoplastic compositions use of biodegradable plastic moldable compostable adhesives biodegradable mixtures process for the production of biodegradable mixtures use of biodegradable polymers and biodegradable polymers

机译:可生物降解的聚酯和聚合物可生物降解的可塑热塑性组合物的制备方法,用于制备可生物降解的聚酯和聚合物以及可生物降解的热塑性组合物。

摘要

The following are claimed: (A) biodegradable polyester P1, preparable by reaction of a mixt. comprising: (a1) a mixt. comprising: (a11) 35-95 mol.% of adipic acid and/or one or more ester-forming derivs. of this, (a12) 5-65 mol.% of terephthalic acid and/or one or more ester-forming derivs. of this, and (a13) 0-5 mol.% of a cpd. contg. sulphonate gps., the total of mol.% in (a11)-(a13) being 100 mol.%; and (a2) a dihydroxy cpd. selected from 2-6C alkane-diols and 5-10C cycloalkane-diols. The molar ratio of (a1) to (a2) is 0.4-1.5:1. In addn., 0.01-5 mol.% (based on the molar amt. of component (a1)) of a cpd. D, which comprises at least three gps. capable of forming ester gps., are also used for prodn. of polyester P1. Polyester P1 has (a) a mol.wt. (Mn) of 5000-50000 g/mol; (b) a viscosity no. of 30-350 g/ml (measured in o-dichlorobenzene/phenol (wt. ratio 50/50) at 25 degrees C and a P1 concn. of 0.5 wt.%); and (c) a m.pt. of 50-170 degrees C. (B) biodegradable polyester P2, preparable by reaction of a mixt. comprising: (b1) mixt. comprising: (b11) 20-95 mol.% of adipic acid and/or one or more ester-forming deriv. of this, (b12) 5-80 mol.% of terephthalic acid and/or one or more ester- forming deriv. of this, and (b13) 0-5 mol.% of a cpd. contg. sulphonate gps., the total of mol.% in (b11)-(b13) being 100 mol.%; (b2) a dihydroxy cpd. as (a2) above; (b3) 0.01-100 wt.% (based on the amt. of component (b1) of a hydroxycarboxylic acid B1 which is of formula (Ia) or (Ib); and (b4) 0-5 mol.% (based on the amt. of component (b1)) of a cpd. D. The molar ratio of (b1) to (b2) is 0.4-1.25:1. Polyester P2 has (a) a mol.wt. (Mn) of 5000-80000 g/mol; (b) a viscosity no. of 30 - 450 g/ml (measured in o-dichlorobenzene/phenol (wt. ratio 50/50) at 25 degrees C and a P2 concn. of 0.5 wt.%); and (c) a m.pt. of 50-235 degrees C. p = a whole no. from 1-1500; r = a whole no. from 1-4; G = phenylene, (CH2)k, C(R)H and C(R)HCH2; k = 1-5; R = Me or Et. (C) biodegradable polyester Q1 which have: (a) a mol.wt. (Mn) of 5000-100000 g/mol; (b) a viscosity no. of 30-450 g/ml (measured in o-dichlorobenzene/phenol (wt. ratio 50/50) at 25 degrees C and a Q1 concn. of 0.5 wt.%); and (c) a m.pt. of 50-235 degrees C. Q1 are obtained by reaction of a mixt. comprising; (c1) polyester P1 and/or a polyester PWD; (c2) 0.01-50 wt.% (based on (c1)) of a hydroxycarboxylic acid B1; and (c3) 0-5 mol.% (based on the amt. of component (a1) used in prodn. of P1 and/or PWD) of a cpd. D. Polyester PWD is obtainable by reaction of components (a1) and (a2) in a molar ratio of (a1) to (a2) of 0.4-1.5:1. Polyester PWD have: (a) a mol.wt. (Mn) of 5000 - 50000 g/mol; (b) a viscosity no. of 30 - 350 g/ml (measured in o-dichlorobenzene/phenol (wt. ratio 50/50) at 25 degrees C and a PWD concn. of 0.5 wt.%); and (c) a m.pt. of 50-170 degrees C. (D) biodegradable polyesters Q2 which have: (a) a mol.wt. (Mn) of 6000 - 60000 g/mol; (b) a viscosity no. of 30-350 g/ml (measured in o-dichlorobenzene/phenol (wt. ratio 50/50) at 25 degrees C and a Q2 concn. of 0.5 wt.%); and (c) a m.pt. of 50-170 degrees C. Q2 are obtained by reaction of a mixt. comprising: (d1) 95-99.9 wt.% of polyester P1 and/or PWD; and (d2) 0.1-50 wt.% of a diisocyanate C1; and (d3) 0-5 mol.% (based on the amt. of component (a1) used in prodn. of P1 and/or PWD) of a cpd. D. (E) biodegradable polymers T1 which have: (a) a mol.wt. (Mn) of 10000 - 100000 g/mol; (b) a viscosity no. of 30-450 g/ml (measured in o-dichlorobenzene/phenol (wt. ratio 50/50) at 25 degrees C and a T1 concn. of 0.5 wt.%); and (c) a m.pt. of 50-235 degrees C. T1 are obtd. by reaction of polyester Q1 with (e1) 0.1-5 wt.% (based on the amt. of Q1) of diisocyanate C1 and (e2) 0-5 mol.% (based on the amt. of component (a1) used in prodn. of Q1 via the polyester P1 and/or PWD) of a cpd. D. (F) biodegradable polymers T2 which have: (a) a mol.wt. (Mn) of 10000 - 100000 g/mol/. (b) a viscosity no. of 30-450 g/ml (measured in o-dichlorobenzene/phenol (wt. ratio 50/50) at 25 degrees C and a T2 concn. of 0.5 wt.%); and (c) a m.pt. of 50-235 degrees C. T2 are obtained by reaction of polyester Q2 with (f1) 0.01-50 wt.% (based on the amt. of Q2) of hydroxycarboxylic acid B1 and (f2) 0-5 mol.% (based on the amt. of component (a1) used in prodn. of Q2 via the polyester P1 and/or PWD) of a cpd
机译:要求保护以下内容:(A)可通过混合物反应制备的可生物降解的聚酯P1。包括:(a1)混合料。包含:(a11)35-95mol。%的己二酸和/或一种或多种成酯衍生物。其中,(a12)5-65摩尔%的对苯二甲酸和/或一种或多种成酯衍生物。 (a13)0-5 mol。%的cpd。续磺酸盐gps。,(a11)-(a13)中的总摩尔%为100摩尔%; (a2)二羟基cpd。选自2-6C烷烃二醇和5-10C环烷烃二醇。 (a1)与(a2)的摩尔比为0.4-1.5∶1。另外,cpd为0.01-5mol。%(基于组分(a1)的摩尔含量)。 D,包括至少三个gps。能够形成酯gps的产品也用于生产。聚酯P1。聚酯P1具有(a)摩尔%。 (Mn)为5000-50000 g / mol; (b)粘度号30-350 g / ml(以邻二氯苯/苯酚(重量比50/50)在25摄氏度和0.5重量%的P1浓度下测量);和(c)点50-170℃。(B)可生物降解的聚酯P2,可通过混合物反应制备。包括:(b1)混合。包含:(b11)20-95mol。%的己二酸和/或一种或多种成酯衍生物。其中,(b12)5-80mol。%的对苯二甲酸和/或一种或多种成酯衍生物。 (b13)cpd的0-5摩尔%。续磺酸盐gps。,(b11)-(b13)中的总摩尔%为100摩尔%; (b2)二羟基cpd。如上文(a2)所述; (b3)0.01-100重量%(基于式(Ia)或(Ib)的羟基羧酸B1的组分(b1)的含量;和(b4)0-5 mol。%(基于(b1)与(b2)的摩尔比为0.4-1.25:1;聚酯P2的(a)摩尔重量(Mn)为5000- 80000 g / mol;(b)粘度为30-450 g / ml(在25°C和0.5 wt%的P2浓度下以邻二氯苯/苯酚(重量比50/50)测量) ;和(c)m-pt。在50-235摄氏度之间。p =从1-1500开始的整数; r =从1-4开始的整数; G =亚苯基,(CH2)k,C( R = H和C(R)HCH 2; k = 1-5; R = Me或Et。(C)可生物降解的聚酯Q1,其具有:(a)5000-100000g / mol的摩尔重量(Mn);和(b)30-450 g / ml的粘度(在邻二氯苯/苯酚(重量比50/50)中,在25摄氏度和Q1浓度为0.5重量%下测量);和(c)熔点为50-235摄氏度的Q1是通过以下混合物的反应获得的:(c1)聚酯P1和/或聚酯PWD;(c2)0.01-50 wt。%(基于(c1) )的羟基羧酸酸B1; (c3)0-5mol。%(基于P1和/或PWD的产品中使用的组分(a1)的含量)。 D.聚酯PWD可通过使组分(a1)和(a2)以(a1)与(a2)的摩尔比为0.4-1.5:1反应而获得。聚酯PWD具有:(a)摩尔%。 (Mn)5000-50000 g / mol; (b)粘度号30-350 g / ml(以邻二氯苯/苯酚(重量比为50/50)在25℃和PWD浓度为0.5 wt%的条件下测量);和(c)点50-170℃。(D)可生物降解的聚酯Q2,其具有:(a)摩尔%。 (Mn)为6000-60000 g / mol; (b)粘度号30-350 g / ml(以邻二氯苯/苯酚(重量比为50/50)在25℃和Q2浓度为0.5 wt%的条件下测量);和(c)点温度为50-170℃。通过混合物反应获得Q2。包含:(d1)95-99.9 wt。%的聚酯P1和/或PWD; (d2)0.1〜50重量%的二异氰酸酯C1; (d3)0-5mol。%(基于P1和/或PWD的产品中使用的组分(a1)的含量)。 D.可生物降解的聚合物T1,其具有:(a)摩尔%。 (Mn)10000-100000 g / mol; (b)粘度号30-450 g / ml(以邻二氯苯/苯酚(重量比50/50)在25℃和T1浓度为0.5 wt%的条件下测量);和(c)点温度为50-235摄氏度。通过使聚酯Q1与(e1)0.1-5 wt。%(基于Q1的含量)的二异氰酸酯C1和(e2)0-5 mol。%(基于组分(a1)的含量)反应通过cpd的聚酯P1和/或PWD获得Q1的产品。 D.可生物降解的聚合物T2,其具有:(a)摩尔%。 (Mn)为10000-100000 g / mol /。 (b)粘度号30-450 g / ml(以邻二氯苯/苯酚(重量比为50/50)在25摄氏度和T2浓度为0.5重量%的条件下测量);和(c)点通过使聚酯Q2与(f1)0.01-50wt。%(基于Q2的含量)和羟基羧酸B1与(f2)0-5mol。%(基于Q2的含量)反应,获得T2为50-235℃。在cpd的Q2产品中通过聚酯P1和/或PWD使用的组分(a1)的修饰

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