公开(公告)号：US20070084752A1

公开(公告)日：2007-04-19

申请号：US11498261

申请日：2006-08-03

申请人： Eduardo Sousa Aguiar ,  Claudio De Araujo Mota ,  Jose Fontes Monteiro ,  Debora Batista Peixoto ,  Adriano Do Couto Fraga ,  Ana Belizario Dos Santos ,  Antonio Fonseca Bidart ,  Fernando De Oliveira ,  Henrique Cerqueira ,  Isabela Dos Santos ,  Marcos De Frietas Sugaya

发明人： Eduardo Sousa Aguiar ,  Claudio De Araujo Mota ,  Jose Fontes Monteiro ,  Debora Batista Peixoto ,  Adriano Do Couto Fraga ,  Ana Belizario Dos Santos ,  Antonio Fonseca Bidart ,  Fernando De Oliveira ,  Henrique Cerqueira ,  Isabela Dos Santos ,  Marcos De Frietas Sugaya

IPC分类号： C10G47/24

CPC分类号： C10G11/05 ,  C10G2400/20

摘要： A selective catalytic cracking process of natural gas liquid fraction to light olefins and other products is described, the process includes placing in contact (within a reaction zone) said liquid fraction of natural gas, rich in C5+ paraffins, with an MFI type zeolitic catalyst in acid form, having a pore size of at least 4 Angstroms, a silica/alumina ratio of between 10 and 2000, and where the processing conditions involve a temperature of between 350° C. and 650° C., space velocity of between 2 and 100 h−1 and atmospheric pressure, and afterwards carrying out the catalytic cracking to separate products, to recover a product enriched with light olefins, LPG fractions, and aromatics, and where the production of olefins is favored in conditions of higher space velocities, while the production of LPG fractions and aromatics are favored in conditions of lowered space velocities.

摘要翻译： 描述了天然气液体馏分对轻质烯烃和其它产物的选择性催化裂解过程，该方法包括将富含C 5 H 6的天然气的所述液体部分置于接触（在反应区内） 具有酸形式的MFI型沸石催化剂，具有至少4埃的孔径，二氧化硅/氧化铝比率在10和2000之间，并且其中加工条件包括在 350℃和650℃，空速在2小时至100小时-1和大气压之间，然后进行催化裂化以分离产物，以回收富含轻质烯烃的产物 ，LPG馏分和芳族化合物，并且其中烯烃的生产在较高空间速度的条件下是有利的，而LPG馏分和芳族化合物的生产在降低空速的条件下是有利的。