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    • 95. 发明申请
    • AMMOXIMATION REACTOR FOR CYCLOHEXANONE OXIME PRODUCTION
    • 环己酮氧化酶生产的抗氧化反应剂
    • WO2012152600A1
    • 2012-11-15
    • PCT/EP2012/057746
    • 2012-04-27
    • VERSALIS S.P.A.DEL SEPPIA, AlessandroGHIRARDO, Elena
    • DEL SEPPIA, AlessandroGHIRARDO, Elena
    • B01J8/00B01J8/22C07C249/04
    • B01J8/10B01J8/006B01J8/226B01J2208/00141B01J2208/0015B01J2208/00212B01J2208/00902B01J2219/00247C07C249/04C07C2601/14C07C251/44
    • Ammoximation reactor for cyclohexanone oxime production comprising: (a) a reactor vessel provided with a stirrer; (b) an internal filtering system; (c) an internal liquid ammonia evaporation coil; (d) an internal gaseous ammonia toroidal distributor; (e) an external cyclohexanone toroidal distributor; (f) an internal hydrogen peroxide toroidal distributor; (g) an internal cylindrical draft tube; (h) an external cooling jacket. Said ammoximation reactor allows to obtain a better mixing of the components of the ammoximation reaction and to maximize both the heat-transfer coefficients and the mass-transfer coefficients. Moreover, said ammoximation reactor allows to increase the packing time of the catalyst used in the ammoximation reaction on the filtering system (i.e. the plugging phenomena) so as to avoid the necessity of carrying out the backwashings with nitrogen. Moreover, said ammoximation reactor does not require external downstream separation units to separate the catalyst from the reaction mixture obtained from the ammoximation reaction.
    • 用于环己酮肟生产的肟化反应器包括:(a)设置有搅拌器的反应器容器; (b)内部过滤系统; (c)内部液氨蒸发线圈; (d)内部气态氨环形分配器; (e)外部环己酮环形分配器; (f)内部过氧化氢环形分配器; (g)内部圆柱形引流管; (h)外部冷却套。 所述氨肟化反应器允许获得氨肟化反应组分的更好混合,并使传热系数和质量传递系数最大化。 此外,所述氨肟化反应器允许增加过滤系统中氨肟化反应中使用的催化剂的填充时间(即堵塞现象),以避免用氮气进行回洗的必要性。 此外,所述氨肟化反应器不需要外部下游分离单元,以将催化剂与从氨肟化反应获得的反应混合物分离。
    • 96. 发明申请
    • INTEGRATED PROCESS FOR THE PRODUCTION OF POLYHYDROXYALKANOATES AND BIOETHANOL FROM LIGNOCELLULOSE HYDROLYZATE
    • WO2023079455A1
    • 2023-05-11
    • PCT/IB2022/060557
    • 2022-11-02
    • VERSALIS S.P.A.
    • RODIGHIERO, ValentinaERCOLE, AlessiaRIVA, DanieleDEL SEPPIA, AlessandroPRANDO, TommasoFRATTINI, Alessandra
    • C12P7/625C12P7/10C12P7/14C12R1/05C12R1/07C12R1/38C12R1/85
    • Integrated process for the production of polyhydroxyalkanoates (PHAs) and bioethanol from lignocellulosic hydrolyzate comprising the following steps: (a) feeding at least a part of said lignocellulosic hydrolyzate to a first fermentation device in the presence of at least one microorganism capable of using sugars with six carbon atoms (C6) and organic acids, obtaining a first fermentation broth; (b) subjecting the first fermentation broth obtained in said step (a) to separation obtaining an aqueous suspension of cellular biomass comprising at least one polyhydroxyalkanoate (PHA) and an aqueous phase comprising sugars with five carbon atoms (C5) in a quantity greater than or equal to 10 g/L, preferably between 12 g/L and 100 g/L; (c) optionally, feeding at least a part of the aqueous phase obtained in said step (b), to a second fermentation device in the presence of at least one microorganism capable of using both sugars with five carbon atoms (C5) and sugars with six carbon atoms (C6), obtaining a second fermentation broth (inoculum); (d) feeding at least a part of the aqueous phase obtained in said step (b) and, optionally, the second fermentation broth (inoculum) obtained in said step (c) and/or at least a part of said lignocellulosic hydrolyzate, to a third fermentation device in the presence of at least one microorganism capable of using both sugars with five carbon atoms (C5) and sugars with six carbon atoms (C6), obtaining a third fermentation broth; (e) subjecting said third fermentation broth to separation obtaining bioethanol. The aforementioned polyhydroxyalkanoates (PHAs) can be advantageously used in various applications, in particular in the medical, pharmacological, agricultural, engineering and food fields. The aforementioned bioethanol can be advantageously used as it is, or mixed with fossil fuels, for automotive purposes, or, suitably purified, in the production of biochemicals (for example, disinfectants).
    • 98. 发明申请
    • PROCESS FOR THE PREPARATION OF POLYISOPRENE WITH A MAINLY ALTERNATING CIS-1,4- ALT-3,4 STRUCTURE IN THE PRESENCE OF A CATALYTIC SYSTEM COMPRISING A PYRIDYL IRON COMPLEX
    • WO2019142108A1
    • 2019-07-25
    • PCT/IB2019/050333
    • 2019-01-16
    • VERSALIS S.P.A.
    • RICCI, GiovanniSOMMAZZI, AnnaPAMPALONI, GuidoLEONE, GiuseppeMASI, Francesco
    • C08F136/08C08F4/70
    • Process for the preparation of polyisoprene with a mainly alternating cis -1,4- alt -3,4 structure comprising polymerizing isoprene in the presence of a catalytic system comprising: (a) at least one pyridyl iron complex having general formula (I): wherein: - R 1 is selected from linear or branched C 1 -C 20 , preferably C 1 -C 15 , alkyl groups, optionally substituted cycloalkyl groups, optionally substituted aryl groups; - R 2 is selected from linear or branched C 1 -C 10 , preferably C 1 -C 3 , alkyl groups; - X, mutually identical or different, represent a halogen atom such as, for example, chlorine, bromine, iodine; or they are selected from linear or branched C 1 -C 20 , preferably C 1 -C 15 , alkyl groups, -OCOR 3 groups or -OR 3 groups wherein R3 is selected from linear or branched C 1 -C 20 , preferably C 1 -C 15 , alkyl groups, - n is 2 or 3; (b) at feast one co-catalyst selected from organo-derivative compounds of aluminum, preferably from (b 1 ) aluminoxanes having general formula (II): ( R 4 ) 2 -AI-0-[-AI(R 5 )-0-} m -AI-(R 6 ) 2 ( II ) wherein R 4 , R 5 and R 6 , mutually identical or different, represent a hydrogen atom, or a halogen atom such as, for example, chlorine, bromine, iodine, fluorine; or they are selected from linear or branched C 1 -C 20 alkyl groups, cycloalkyl groups, aryl groups, said groups being optionally substituted with one or more silicon or germanium atoms; and m is an integer ranging from 0 to 1000; (b 2 ) aluminum compounds having general formula (III): AI(R 7 )(R 8 )(R 9 ) (III) wherein R 7 is a hydrogen atom, or is selected from linear or branched C 1 -C 20 alkyl groups, cycloalkyl groups, aryl groups, alkylaryl groups, arylalkyl groups, alkoxy groups; R 8 and R 9 , mutually identical or different, are selected from linear or branched C 1 -C 20 alkyl groups, cycloalkyl groups, aryl groups, alkylaryl groups, arylalkyl groups; wherein the molar ratio between the aluminum present in the co-catalyst and the iron present in the iron pyridyl complex having general formula (I) is ranging from 5 to 60, preferably from 8 to 55.