会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 1. 发明申请
    • PROCESS FOR POLYMER MIXTURE HYDROCONVERSION
    • WO2020129020A1
    • 2020-06-25
    • PCT/IB2019/061213
    • 2019-12-20
    • ENI S.P.A.VERSALIS S.P.A.
    • BALDUCCI, DanieleGUIDETTI, StefaniaSCAVELLO, FrancescoVECCHINI, NicolaMARIANI, Paolo
    • C10G1/00C10G1/08C10G1/10C10G47/02C10G47/26
    • The present invention relates to a process for the hydroconversion of mixtures of polymers or plastics which comprises the pre-treatment of the mixtures through methods selected from mechanical methods, chemical methods, thermal methods, or combinations thereof forming a pre-treated charge. The pre-treated charge is mixed with a hydrocarbon vacuum residue, optionally pre-heated, to form a reactant mixture. The reactant mixture is fed to a hydroconversion section in slurry phase, together with a catalyst precursor containing Molybdenum, and a stream containing hydrogen, forming a reaction effluent. The effluent is separated into at least one high-pressure and high-temperature separator in a vapour phase and a slurry phase. The separate vapour phase is sent to a gas treatment section with the function of separating a liquid fraction from the gas containing hydrogen and hydrocarbon gases having from 1 to 4 carbon atoms; said liquid fraction comprising naphtha, atmospheric gas oil (AGO), vacuum gas oil (VGO). The slurry phase is then sent to a separation section that has the function of separating the fractions of the Vacuum Gas Oil (VGO), Heavy Vacuum Gas Oil (HVGO), Light Vacuum Gas Oil (LVGO), Atmospheric Gas Oil (AGO), from a stream of heavy organic products which contains asphaltenes, unconverted charge, catalyst and solid formed during the hydroconversion reaction. This stream of heavy organic products is partly recirculated to the hydroconversion section and partly forms a purge stream.
    • 5. 发明申请
    • PROCESS FOR THE DEHYDRATION OF OXYGENATED COMPOUNDS
    • 氧化化合物脱水方法
    • WO2016135605A1
    • 2016-09-01
    • PCT/IB2016/050926
    • 2016-02-22
    • VERSALIS S.P.A.
    • VECCHINI, NicolaGIROTTI, Gianni
    • C07C1/24C07C11/167C07C33/025C07C29/60
    • C07C1/24B01J21/12B01J23/10B01J35/023B01J37/031C07C29/60C07C2521/12C07C11/167C07C33/025C07C33/03
    • The present invention relates to a process for the dehydration of at least one oxygenated compound, preferably selected from saturated alcohols, unsaturated alcohols, diols, ethers, in the presence of at least one dehydration catalyst selected from cerium oxide (CeO 2 ), aluminium oxide (γ-Al 2 O 3 ), aluminium silicate, silica-aluminas (SiO 2 -Al 2 O 3 ), aluminas, zeolites, sulfonated resins, ion-exchange resins, metal oxides (for example, lanthanum oxide, zirconium oxide, tungsten oxide, thallium oxide, magnesium oxide, zinc oxide); of at least one basic agent selected from ammonia (NH 3 ), or from inorganic or organic compounds containing nitrogen capable of developing ammonia (NH 3 ) during said dehydration process; and, optionally, of silica (SiO 2 ), or of at least one catalyst for the dissociation of ammonia (NH 3 ) selected from catalysts comprising silica (SiO 2 ), preferably of silica (SiO 2 ).
    • 本发明涉及在至少一种选自氧化铈(CeO 2),氧化铝(CeO 2)的脱水催化剂存在下脱水至少一种含氧化合物,优选选自饱和醇,不饱和醇,二醇,醚的方法, γ-Al2O3),硅酸铝,二氧化硅 - 氧化铝(SiO 2 -Al 2 O 3),氧化铝,沸石,磺化树脂,离子交换树脂,金属氧化物(例如氧化镧,氧化锆,氧化钨,氧化铊,氧化镁, 氧化锌); 的至少一种选自氨(NH 3)的碱性试剂,或在所述脱水过程中由含有能发展氨(NH 3)的氮的无机或有机化合物) 或二氧化硅(SiO 2)或至少一种用于解离选自包含二氧化硅(SiO 2),优选二氧化硅(SiO 2)的催化剂的氨(NH 3)的催化剂)。
    • 10. 发明申请
    • PROCESS FOR THE PRODUCTION OF 1, 3-BUTADIENE FROM 1, 4 -BUTANEDIOL VIA TETRAHYDROFURAN
    • 通过四氢呋喃从1,4-丁二醇生产1,3-丁二烯的方法
    • WO2016092517A1
    • 2016-06-16
    • PCT/IB2015/059540
    • 2015-12-11
    • VERSALIS S.P.A.
    • VECCHINI, NicolaGALEOTTI, ArmandoPISANO, Andrea
    • C07C1/247C07C11/167
    • C07C1/247C07C11/167
    • Process for the production of 1,3-butadiene comprising: feeding a mixture (a) comprising 1,4-butanediol and water to an evaporator, said water being present in an amount of greater than or equal to 5% by weight, preferably ranging from 10% by weight to 85% by weight, more preferably ranging from 15% by weight to 30% by weight, relative to the total weight of said mixture (a), to obtain: (b) a gaseous stream comprising 1,4-butanediol exiting from the top of said evaporator; and, optionally, (c) a blowdown stream exiting from the bottom of said evaporator; feeding said gaseous stream (b) to a first reactor containing at least one dehydration catalyst to obtain (d) a stream comprising tetrahydrofuran, water and, optionally, impurities and/or unreacted 1,4-butanediol, exiting from said first reactor; optionally, feeding said stream (d) to a first purification section to obtain: (e) a stream comprising tetrahydrofuran, water, and, optionally, impurities; (f) a stream comprising water and, optionally, impurities and/or unreacted 1,4- butanediol; feeding said stream (d) or said stream (e) to a second reactor containing at least one dehydration catalyst to obtain (g) a stream comprising 1,3-butadiene, water and, optionally, impurities and/or unreacted tetrahydrofuran, exiting from said second reactor; feeding said stream (g) to a second purification section to obtain: (h) a stream comprising pure 1,3-butadiene; (i) a stream comprising water and, optionally, unreacted tetrahydrofuran; and, optionally, (I) a stream comprising impurities. Said 1,3-butadiene may advantageously be used as a monomer or intermediate in the production of elastomers and (co)polymers.
    • 制备1,3-丁二烯的方法包括:将包含1,4-丁二醇和水的混合物(a)加入到蒸发器中,所述水以大于或等于5重量%的量存在,优选范围 相对于所述混合物(a)的总重量为10重量%至85重量%,更优选为15重量%至30重量%,以获得:(b)包含1,4 - 丁二醇从所述蒸发器的顶部排出; 和(c)从所述蒸发器的底部排出的排污流; 将所述气流(b)进料到含有至少一种脱水催化剂的第一反应器,以获得(d)包含从所述第一反应器排出的四氢呋喃,水和任选的杂质和/或未反应的1,4-丁二醇的物流; 任选地,将所述物流(d)加入到第一纯化部分以获得:(e)包含四氢呋喃,水和任选的杂质的物流; (f)包含水和任选的杂质和/或未反应的1,4-丁二醇的物流; 将所述物流(d)或所述物流(e)加入到含有至少一种脱水催化剂的第二反应器中,以获得(g)包含1,3-丁二烯,水和任选的杂质和/或未反应四氢呋喃的物流, 第二反应堆; 将所述物流(g)加入第二纯化部分以获得:(h)包含纯的1,3-丁二烯的物流; (i)包含水和任选的未反应四氢呋喃的流; 和(I)包含杂质的物流。 所述1,3-丁二烯可有利地用作制备弹性体和(共)聚合物的单体或中间体。