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    • 1. 发明授权
    • Production of isoprene from iso-butanol
    • 从异丁醇生产异戊二烯
    • US09115040B2
    • 2015-08-25
    • US13825749
    • 2011-09-06
    • Walter VermeirenJosé Castor Gonzalez
    • Walter VermeirenJosé Castor Gonzalez
    • C07C1/22C07C1/24C07C2/86
    • C07C2/867C07C1/22C07C1/24C07D301/02C07C11/09C07C11/18
    • The present invention is a process to make isoprene comprising: a) providing a reaction zone comprising an acidic aqueous solution, b) introducing, continuously or intermittently, in said reaction zone a mixture comprising (i) isobutanol and optionally (ii) t-butanol or an iso-butene precursor which is not isobutanol and not t-butanol or iso-butene or any combination of two or three of these (ii) components, an aqueous solution of formaldehyde, c) operating said reaction zone at conditions effective to dehydrate isobutanol and optionally (ii) t-butanol and optionally the iso-butene precursor to iso-butene and produce isoprene by reaction of formaldehyde and iso-butene while distilling away a mixture comprising produced isoprene, water, unreacted starting materials and other low boiling point components from this reaction zone to the outside of the reaction zone. In another embodiment isobutanol provides 10% or more of the iso-butene for the isoprene synthesis.In another embodiment isobutanol provides 20% or more of the iso-butene for the isoprene synthesis.In another embodiment isobutanol provides 30% or more of the iso-butene for the isoprene synthesis.In another embodiment isobutanol provides 40% or more of the iso-butene for the isoprene synthesis.In another embodiment isobutanol provides 50% to 100% of the iso-butene for the isoprene synthesis.
    • 本发明是一种制备异戊二烯的方法,其包括:a)提供包含酸性水溶液的反应区,b)在所述反应区中连续或间歇地引入混合物,所述混合物包含(i)异丁醇和任选的(ii) 或不是异丁醇而不是叔丁醇或异丁烯的异丁烯前体或这些(ii)组分的两种或三种的任何组合,甲醛水溶液,c)在有效脱水的条件下操作所述反应区 异丁醇和任选的(ⅱ)叔丁醇和任选的异丁烯前体加成异丁烯,并通过甲醛和异丁烯的反应产生异戊二烯,同时蒸馏出包含产生的异戊二烯,水,未反应的起始原料和其它低沸点的混合物 组分从该反应区到反应区外。 在另一个实施方案中,异丁醇为异戊二烯合成提供10%或更多的异丁烯。 在另一个实施方案中,异丁醇为异戊二烯合成提供20%或更多的异丁烯。 在另一个实施方案中,异丁醇为异戊二烯合成提供30%或更多的异丁烯。 在另一个实施方案中,异丁醇为异戊二烯合成提供40%或更多的异丁烯。 在另一个实施方案中,异丁醇为异戊二烯合成提供50%至100%的异丁烯。
    • 2. 发明申请
    • PRODUCTION OF ISOPRENE FROM ISO-BUTANOL
    • 从ISO-丁醇生产异丙苯
    • US20130217942A1
    • 2013-08-22
    • US13825749
    • 2011-09-06
    • Walter VermeirenJosé Castor Gonzalez
    • Walter VermeirenJosé Castor Gonzalez
    • C07C1/22
    • C07C2/867C07C1/22C07C1/24C07D301/02C07C11/09C07C11/18
    • The present invention is a process to make isoprene comprising: a) providing a reaction zone comprising an acidic aqueous solution, b) introducing, continuously or intermittently, in said reaction zone a mixture comprising (i) isobutanol and optionally (ii) t-butanol or an iso-butene precursor which is not isobutanol and not t-butanol or iso-butene or any combination of two or three of these (ii) components, an aqueous solution of formaldehyde, c) operating said reaction zone at conditions effective to dehydrate isobutanol and optionally (ii) t-butanol and optionally the iso-butene precursor to iso-butene and produce isoprene by reaction of formaldehyde and iso-butene while distilling away a mixture comprising produced isoprene, water, unreacted starting materials and other low boiling point components from this reaction zone to the outside of the reaction zone. In another embodiment isobutanol provides 10% or more of the iso-butene for the isoprene synthesis.In another embodiment isobutanol provides 20% or more of the iso-butene for the isoprene synthesis.In another embodiment isobutanol provides 30% or more of the iso-butene for the isoprene synthesis.In another embodiment isobutanol provides 40% or more of the iso-butene for the isoprene synthesis. In another embodiment isobutanol provides 50% to 100% of the iso-butene for the isoprene synthesis.
    • 本发明是一种制备异戊二烯的方法,其包括:a)提供包含酸性水溶液的反应区,b)在所述反应区中连续或间歇地引入混合物,所述混合物包含(i)异丁醇和任选的(ii) 或不是异丁醇而不是叔丁醇或异丁烯的异丁烯前体或这些(ii)组分的两种或三种的任何组合,甲醛水溶液,c)在有效脱水的条件下操作所述反应区 异丁醇和任选的(ⅱ)叔丁醇和任选的异丁烯前体加成异丁烯,并通过甲醛和异丁烯的反应产生异戊二烯,同时蒸馏出包含产生的异戊二烯,水,未反应的起始原料和其它低沸点的混合物 组分从该反应区到反应区外。 在另一个实施方案中,异丁醇为异戊二烯合成提供10%或更多的异丁烯。 在另一个实施方案中,异丁醇为异戊二烯合成提供20%或更多的异丁烯。 在另一个实施方案中,异丁醇为异戊二烯合成提供30%或更多的异丁烯。 在另一个实施方案中,异丁醇为异戊二烯合成提供40%或更多的异丁烯。 在另一个实施方案中,异丁醇为异戊二烯合成提供50%至100%的异丁烯。
    • 3. 发明申请
    • UPGRADING LIGHT NAPHTAS FOR INCREASED OLEFINS PRODUCTION
    • 升级光催化剂用于增加油脂生产
    • US20120074039A1
    • 2012-03-29
    • US13262925
    • 2010-04-22
    • José Castor GonzalezJean MazurelleWalter Vermeiren
    • José Castor GonzalezJean MazurelleWalter Vermeiren
    • C10G59/02
    • C10G9/00C10G45/58C10G45/62C10G45/64C10G69/06C10G69/14C10G2300/1044C10G2300/4081C10G2300/807C10G2400/20
    • The present invention is a process to upgrade light naphthas comprising branched paraffins and their use as a feedstock in a steam cracking unit, said light naphthas consisting essentially of 90 to 100% by weight of hydrocarbons having at least 5 and up to 8 carbon atoms, said process comprising,a) optionally providing an isomerization zone recovered from the gasoline unit of an oil refinery, b) optionally providing a separation zone capable to treat an hydrocarbon stream comprising branched paraffins and normal paraffins to produce a first hydrocarbon stream having a reduced branched paraffins content and an enhanced normal paraffins content and a second hydrocarbon stream having an enhanced branched paraffins content and a reduced normal paraffins content, c) optionally providing a depentanizer, such that at least two of a), b) and c) are present, wherein, the light naphtha is sent to one of a), b) and c), streams are circulating between the various zones a), b) or c), a stream rich in normal paraffins is sent to the steam cracking unit.
    • 本发明是一种在蒸汽裂解装置中升级包含支链烷烃的轻石脑油及其作为原料的用途的方法,所述轻石脑油基本上由90至100重量%的具有至少5个和至多8个碳原子的烃, 所述方法包括:a)任选地提供从炼油厂的汽油单元回收的异构化区,b)任选地提供能够处理包含支链链烷烃和正链烷烃的烃流的分离区,以产生具有还原支化的第一烃流 链烷烃含量和增强的正链烷烃含量和具有增强的支链链烷烃含量和降低的正链烷烃含量的第二烃流,c)任选地提供脱苯胺化剂,使得存在a),b)和c)中的至少两个, 其中,轻石脑油被送到a),b)和c)中的一个,流在各个区域a),b)或c)之间循环, 在正常的石蜡中被送到蒸汽裂解装置。