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    • 1. 发明申请
    • Process for the Preparation of Succinic Acid Ester
    • 琥珀酸酯的制备方法
    • US20160272568A1
    • 2016-09-22
    • US14785794
    • 2014-12-02
    • JOHNSON MATTHEY DAVY TECHNOLOGIES LIMITED
    • Martin Lucas SmidtIan CampbellGraham ReedPaul GordonChristopher Ferguson
    • C07C67/08B01D3/00
    • C07C67/08B01D3/009C07C69/40
    • A process for production of dialkyl succinate from bio-succinic acid feedstock where solid bio-succinic acid is fed to a reactor to react with alkanol by autocatalytic esterification. Products from the reactor including unreacted succinic acid, mono alkyl ester, dialkyl ester, alkanol, water and impurities are sent to a reaction distillation column for esterification of succinic acid and further esterification of mono alkyl ester with upflowing alkanol. The bottoms products from the reaction distillation column including residual succinic acid, mono alkyl ester, dialkyl ester, impurities and alkanol are sent to a bottoms stream separation zone where di-alkyl ester is separated from alkanol, succinic acid, mono alkyl ester and impurities. The tops products from the reaction distillation column including alkanol, water and organic components are sent to a top stream distillation zone where alkanol is separated from water and organic components. The organic components are recycled to the reaction zone column.
    • 从生物琥珀酸原料生产琥珀酸二烷基酯的方法,其中将固体生物琥珀酸加入反应器中通过自动催化酯化与烷醇反应。 将来自反应器的产物(包括未反应的琥珀酸,单烷基酯,二烷基酯,链烷醇,水和杂质)送入反应蒸馏塔用于酯化琥珀酸并进一步酯化单烷基酯与向上流动的链烷醇。 来自反应蒸馏塔的塔底产物包括残余的琥珀酸,单烷基酯,二烷基酯,杂质和链烷醇被送到底部料流分离区,其中二烷基酯与烷醇,琥珀酸,单烷基酯和杂质分离。 包括链烷醇,水和有机组分的反应蒸馏塔的顶部产物被送入顶部蒸馏区,其中链烷醇与水和有机组分分离。 将有机组分再循环至反应区柱。
    • 3. 发明授权
    • Process for the preparation of succinic acid ester
    • 制备琥珀酸酯的方法
    • US09527796B2
    • 2016-12-27
    • US14785113
    • 2014-12-02
    • Johnson Matthey Davy Technologies Limited
    • Martin Lucas SmidtIan CampbellGraham ReedPaul GordonChristopher Ferguson
    • C07C67/08C07C67/54B01D3/00B01D3/14B01D17/02
    • C07C67/08B01D3/009B01D3/143B01D17/0208C07C67/54C07C69/40
    • A process for the production of dialkyl succinate from a bio-succinic acid feedstock commencing by feeding bio-succinic acid to a reaction distillation column to enable esterification of the succinic acid. The feedstock is passed co-currently with upflowing alkanol such that an esterification reaction occurs. An overhead vapor stream is removed from the reaction distillation column comprising di-ester, alkanol, water of esterification and organic components. The vapor stream is sent to an alkanol separation column where alkanol is separated from the water of esterification and organic components. A side draw is removed from the alkanol separation column comprising partially immiscible organic and aqueous phases. The side draw is passed to a phase separation apparatus where the partially immiscible organic and aqueous phases are separated. The organic phase is passed to a column where the dialkyl succinate is recovered from residual water and other organic components.
    • 从生物琥珀酸原料生产琥珀酸二烷基酯的方法,其通过将生物琥珀酸加入到反应蒸馏塔中以使琥珀酸酯化。 原料与向上流动的链烷醇共同通过,发生酯化反应。 从包含二酯,链烷醇,酯化水和有机组分的反应蒸馏塔中除去塔顶蒸气流。 将蒸气流送入链烷醇分离塔,其中链烷醇与酯化和有机组分的水分离。 从包含部分不混溶的有机相和水相的链烷醇分离塔中除去侧馏分。 侧面抽取通过相分离装置,其中部分不混溶的有机相和水相分离。 将有机相通入残余水和其它有机组分中回收琥珀酸二烷基酯的柱。
    • 6. 发明申请
    • Process for the Preparation of Succinic Acid Ester
    • 琥珀酸酯的制备方法
    • US20160264508A1
    • 2016-09-15
    • US14785113
    • 2014-12-02
    • JOHNSON MATTHEY DAVY TECHNOLOGIES LIMITED
    • Martin Lucas SmidtIan CampbellGraham ReedPaul GordonChristopher Ferguson
    • C07C67/08B01D17/02B01D3/14C07C67/54B01D3/00
    • C07C67/08B01D3/009B01D3/143B01D17/0208C07C67/54C07C69/40
    • A process for the production of dialkyl succinate from a bio-succinic acid feedstock commencing by feeding bio-succinic acid to a reaction distillation column to enable esterification of the succinic acid. The feedstock is passed co-currently with upflowing alkanol such that an esterification reaction occurs. An overhead vapour stream is removed from the reaction distillation column comprising di-ester, alkanol, water of esterification and organic components. The vapour stream is sent to an alkanol separation column where alkanol is separated from the water of esterification and organic components. A side draw is removed from the alkanol separation column comprising partially immiscible organic and aqueous phases. The side draw is passed to a phase separation apparatus where the partially immiscible organic and aqueous phases are separated. The organic phase is passed to a column where the dialkyl succinate is recovered from residual water and other organic components.
    • 从生物琥珀酸原料生产琥珀酸二烷基酯的方法,其通过将生物琥珀酸加入到反应蒸馏塔中以使琥珀酸酯化。 原料与向上流动的链烷醇共同通过,发生酯化反应。 从包含二酯,链烷醇,酯化水和有机组分的反应蒸馏塔中除去塔顶蒸气流。 将蒸气流送入链烷醇分离塔,其中链烷醇与酯化和有机组分的水分离。 从包含部分不混溶的有机相和水相的链烷醇分离塔中除去侧馏分。 侧面抽取通过相分离装置,其中部分不混溶的有机相和水相分离。 将有机相通入残余水和其它有机组分中回收琥珀酸二烷基酯的柱。