公开(公告)号：US4597856A

公开(公告)日：1986-07-01

申请号：US661750

申请日：1984-10-17

申请人： Susumu Yoshioka ,  Nobuo Matsuo ,  Nobuyasu Meguri ,  Tadashi Murakami ,  Yasushi Ishibashi ,  Kenichi Matsuda ,  Teruo Suzuka ,  Satoshi Fukase ,  Hidetaka Ohse

发明人： Susumu Yoshioka ,  Nobuo Matsuo ,  Nobuyasu Meguri ,  Tadashi Murakami ,  Yasushi Ishibashi ,  Kenichi Matsuda ,  Teruo Suzuka ,  Satoshi Fukase ,  Hidetaka Ohse

IPC分类号： C10G11/20 ,  C01B3/10 ,  C01B3/30 ,  C01B3/40 ,  C01B3/44 ,  C10G47/02

CPC分类号： C01B3/44 ,  C01B3/40 ,  Y02E60/36 ,  Y02P20/52

摘要： A process for fluidized catalytic cracking of heavy oils and production of hydrogen is described, comprising contacting steam and heavy oils with fluidized catalyst particles containing reduced iron at high temperatures, wherein a fluidized bed is formed such that the catalyst particles are fed from the bottom and withdrawn from the top of the fluidized bed and the fluidized bed is provided with a means for retarding the mixing rate of the catalyst particles in the vertical direction, to thereby generate a temperature difference between zones of the fluidized bed above and below said means, and use the upper zone for cracking of heavy oils and the lower zone for production of hydrogen. Catalyst particles withdrawn from the fluidized bed may be regenerated and recycled. Thus, light oils and hydrogen can be produced in high yields.

摘要翻译： 描述了重油的流化催化裂化和氢气生产的方法，包括使蒸汽和重油与高温下含有还原铁的流化催化剂颗粒接触，其中形成流化床，使得催化剂颗粒从底部进料， 从流化床顶部排出并且流化床设置有用于延迟催化剂颗粒在垂直方向上的混合速率的装置，从而在所述装置上方和下方产生流化床的区域之间的温差，以及 使用上部区域用于重油的裂化和用于生产氢的下部区域。 从流化床排出的催化剂颗粒可以被再生和再循环。 因此，可以高产率生产轻油和氢。