Process for increasing production of light olefins from hydrocarbon feedstock in catalytic cracking
View Patent ↗Disclosed is a process for increasing production of light olefinic hydrocarbons from hydrocarbon feedstock by catalytic cracking. In the process, an effective separation process structure and recycle method of light olefins are used not only to increase the productivity and efficiency of an overall process, thus effectively increasing the production of light olefins, but also to simplify the overall process.
1. A process for increasing production of light olefinic hydrocarbons from hydrocarbon feedstock by catalytic cracking, the process comprising the steps of:
(a) feeding paraffinic naphtha or kerosene and steam into a catalytic cracking furnace where the naphtha or kerosene is subjected to a catalytic cracking reaction in the presence of a catalyst;
(b) regenerating the catalyst used in the catalytic cracking reaction by a continuous or periodic regeneration procedure and recycling the regenerated catalyst into the catalytic cracking furnace;
(c) quenching, compressing and separating the product of the catalytic cracking reaction, to separate and recover each of hydrogen, methane and C2-C3 olefinic hydrocarbons, and to separate a stream containing C2-C3 paraffinic hydrocarbons and a stream containing C4+ hydrocarbons;
(d) feeding the stream containing C2-C3 paraffinic hydrocarbons into a recycling furnace where it is converted to C2-C3 olefinic hydrocarbons by a thermal cracking reaction, and recycling the converted C2-C3 olefinic hydrocarbons to the quenching step (c); and
(e) recycling C4-C5 hydrocarbons of the stream containing C4+ hydrocarbon to the catalytic cracking furnace wherein the recycled C4-C5 hydrocarbons are subjected to a catalytic cracking reaction in the presence of a catalyst; and
(f) optionally recycling C6+ hydrocarbons of the stream containing C4+ hydrocarbon to the catalytic cracking furnace wherein the recycled C6+ hydrocarbons are subjected to a catalytic cracking reaction in the presence of a catalyst,
wherein a yield of ethylene and propylene produced by the catalytic cracking reaction of the recycled C4-C5 hydrocarbons together with the thermal cracking reaction of the recycled C2-C3 paraffinic hydrocarbons is higher than the yield of ethylene and propylene produced by the catalytic cracking reaction of the naphtha and kerosene.
2. The process of claim 1 , wherein the catalyst is a zeolite compound.
3. The process of claim 2 , wherein the zeolite compound is ZSM-5 zeolite.
4. The process of claim 1 , wherein the catalytic cracking reaction is carried out at a temperature of 500-750° C. and a naphtha or kerosene to steam weight ratio of 0.01-10.
5. The process of claim 1 , wherein the catalytic cracking reaction is carried out in a fixed-bed reactor or a fluidized-bed reactor.
6. The process of claim 5 , wherein, if the catalytic cracking reaction is carried out in the fixed-bed reactor, the catalytic cracking reaction is carried out at a naphtha or kerosene residence time of 0.1-600 seconds.
7. The process of claim 5 , wherein, if the catalytic cracking reaction is carried out in the fluidized-bed reactor, the catalytic cracking reaction is carried out at a naphtha or kerosene residence time of 0.1-600 seconds and a catalyst to naphtha or kerosene weight ratio of 1-100.
8. A process for increasing production of light olefinic hydrocarbons from hydrocarbon feedstock by catalytic cracking, the process comprising the steps of:
(a) feeding parrafinic naphtha or kerosene and steam into a catalytic cracking furnace where naphtha or kerosene is subjected to a catalytic cracking reaction in the presence of a catalyst;
(b) regenerating the catalyst used in the catalytic cracking reaction by a continuous or periodic regeneration procedure and recycling the regenerated catalyst into the catalytic cracking furnace;
(c) quenching, compressing and separating the product of the catalytic cracking reaction, to separate and recover each of hydrogen, methane and C2-C3 olefinic hydrocarbons, and to separate a stream containing C2-C3 paraffinic hydrocarbons and a stream containing C4+ hydrocarbons;
(d) feeding the stream containing C2-C3 paraffinic hydrocarbons into a recycling furnace where it is converted to C2-C3 olefinic hydrocarbons by a thermal cracking reaction, and recycling the converted C2-C3 olefinic hydrocarbons to the quenching step (c); and
(e) recycling the whole amount of C4-C5 hydrocarbons of the stream containing C4+ hydrocarbon to the catalytic cracking furnace wherein the recycled C4-C5 hydrocarbons are subjected to a catalytic cracking reaction in the presence of a catalyst; and
(f) optionally recycling C6+ hydrocarbons of the stream containing C4+ hydrocarbon to the catalytic cracking furnace wherein the recycled C6+ hydrocarbons are subjected to a catalytic cracking reaction in the presence of a catalyst,
wherein a yield of ethylene and propylene produced by the catalytic cracking reaction of the recycled C4-C5 hydrocarbons together with the thermal cracking reaction of the recycled C2-C3 paraffinic hydrocarbons is higher than the yield of ethylene and propylene produced by the catalytic cracking reaction of the naphtha and kerosene.
9. The process of claim 1 , wherein a portion of a stream containing C6+ of the stream containing C4+ hydrocarbons is recycled to the catalytic cracking reaction step, and the remaining portion can be separated into a stream containing C6-C8 hydrocarbons and a stream containing C9+ hydrocarbons.
10. The process of claim 1 , wherein the paraffinic naphtha or kerosene is free of olefins.
11. The process of claim 8 , wherein the paraffinic naphtha or kerosene is free of olefins.