首页> 外国专利> HYDROCARBON FLUID CATALYTIC CRACKING PROCESS; A FIRST STAGE BURNS FUEL TO PRODUCE CARBON DIOXIDE AND NITROGEN AND A SECOND STAGE SEPARATES NON ADSORBED GAS FRACTION

HYDROCARBON FLUID CATALYTIC CRACKING PROCESS; A FIRST STAGE BURNS FUEL TO PRODUCE CARBON DIOXIDE AND NITROGEN AND A SECOND STAGE SEPARATES NON ADSORBED GAS FRACTION

机译:烃类流体催化裂解过程;第一阶段燃烧产生二氧化碳和氮的燃料,第二阶段分离出非吸附气体馏分

摘要

A hydrocarbon feedstock is cracked in reactor 2. Used catalyst is sent to a regenerator 4 in which coke deposits on the catalysed are oxidised in the presence of the gas mixture comprising oxygen and inert gas (e.g. CO2). Regenerated catalyst is returned to the reactor 2. A cracked hydrocarbon product stream flows to a fractionating column 6. An overhead stream from the fractionating column 6 is cooled so as to form a liquid-vapour mixture. Downstream of phase separation in an accumulator 10, a stream of the vapour phase ("wet gas") has methane and hydrogen separated therefrom by pressure swing adsorption in plant 8. Higher hydrocarbons than methane are adsorbed in the plant 8 and on regeneration of the adsorbent form a desorbed gas fraction which is sent to an upstream wet gas compressor 12 and from there to a downstream wet gas compressor 16. A compressed wet gas stream is sent from the downstream wet gas compressor 16 to further hydrocarbon processing units (not shown). The feed to the PSA plant 8 may be taken from upstream of the compressor 12 or from intermediate the compressors 12 and 16, or from both locations. Throughput of hydrocarbon feedstock through the cracking plant is able to increased. IMAGE
机译:烃原料在反应器2中裂化。用过的催化剂被送入再生器4,在该再生器中,在包含氧气和惰性气体(例如CO 2)的气体混合物的存在下,在催化剂上沉积的焦炭被氧化。再生的催化剂返回到反应器2。裂化的烃产物物流流到分馏塔6。冷却来自分馏塔6的塔顶物流以形成液-蒸气混合物。在蓄能器10的相分离的下游,蒸汽相(“湿气”)的流通过设备8中的变压吸附而从中分离出甲烷和氢气。在设备8中以及在再生时,比甲烷高的烃被吸附。吸附剂形成解吸的气体馏分,该解吸的气体馏分被输送到上游湿气压缩机12,并从那里被输送到下游湿气压缩机16。压缩的湿气流从下游湿气压缩机16被输送到其他烃处理单元(未显示) 。可以从压缩机12的上游或从压缩机12和16的中间或从两个位置取到PSA设备8的进料。通过裂化装置的烃原料的通量能够增加。 <图像>

著录项

  • 公开/公告号NZ272845A

    专利类型

  • 公开/公告日1997-05-26

    原文格式PDF

  • 申请/专利权人 THE BOC GROUP INC;

    申请/专利号NZ19950272845

  • 发明设计人 MENON RAGHU K;RAMACHANDRAN RAMAKRISHNAN;

    申请日1995-08-24

  • 分类号C10G11/14;B01J38/12;B01J38/36;

  • 国家 NZ

  • 入库时间 2022-08-22 03:26:03

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