Resid catalytic cracker and catalyst for increased propylene yield

A cracking catalyst and catalyst technology, applied in the direction of catalytic cracking, physical/chemical process catalyst, metal/metal oxide/metal hydroxide catalyst, etc., can solve the problem of reducing the negative impact of catalyst activity and selectivity

Inactive Publication Date: 2014-06-18
UOP LLC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Other methods called metal passivation keep the metals in place but reduce their negative impact on the activity and selectivity of the catalyst

Method used

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  • Resid catalytic cracker and catalyst for increased propylene yield
  • Resid catalytic cracker and catalyst for increased propylene yield

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Embodiment Construction

[0014] In the method for increasing the yield of propylene, the light naphtha feedstock is obtained from the residual oil catalytic cracking zone. Any catalytic cracking process or apparatus may be used as the primary cracking zone, including those suitable for processing catalytic cracking feedstocks derived from atmospheric or vacuum residues. An example of this method includes figure 1 Residual Catalytic Cracking Process ("RFCC") licensed from UOP, LLC as indicated.

[0015] In some typical embodiments, the catalytic cracking zone uses a fluidized bed process. The cracking catalyst is combined with the lift gas and the catalytic cracker feed at the inlet of the first riser reactor 10 . The catalytic cracker feedstock is resid with vanadium, sodium or a combination thereof. It is also contemplated that the feedstock contains other metals, including but not limited to nickel and zinc. Vanadium is present in an amount of 20-400 ppm, preferably 20-150 ppm, more preferably a...

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Abstract

A process and catalyst for improving the yield of propylene from residual oil feedstock includes obtaining residual oil feedstock from a vacuum distillation tower. The residual oil feedstock has contaminant metals such as sodium or vanadium. The residual oil feedstock is contacted with a cracking catalyst in a catalytic cracking zone to make products. A ZSM-5 zeolite, a binder, a filler and a metal trap are components of the cracking catalyst. The metal trap has a trapping agent in an outer shell of the catalyst, a trapping agent in the ZSM-5 binder or combinations thereof. After reacting, the cracking catalyst is separated from the products in a separator zone, then regenerated by combusting coke deposited on a surface of the cracking catalyst in an oxygen-containing environment. The cracking catalyst is returned to the catalytic cracking zone. The catalyst with the metal trap is also disclosed.

Description

[0001] Priority claims from earlier national applications [0002] This application claims priority to US Application No. 13 / 300,091, filed November 18, 2011. field of invention [0003] This invention relates to increasing the yield of propylene in refining processes. More specifically, it relates to processes and catalysts for increasing the yield of propylene from high metal content feedstocks. Background of the invention [0004] In a typical refining operation, residual oil ("resid") is produced in a vacuum distillation column. As the demand for petroleum fuels and petrochemicals increases, processing often low-value feedstocks such as residual oils becomes more important. In one method of converting resid into more valuable products, the resid is fed to a resid catalytic cracking zone ("RFCC") to produce higher value naphtha and distillate fuels. Cracking of high boiling resids into lighter hydrocarbon streams such as naphtha or diesel thus yields additional benefit...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G11/18B01J29/40B01J29/46
CPCB01J21/04B01J29/90B01J29/04B01J2229/42B01J35/02B01J35/0073B01J35/0006B01J29/40B01J29/405B01J29/46C10G35/00C10G11/00B01J37/0045B01J23/10B01J38/12C10G11/05C10G11/18C10G11/182C10G2300/107C10G2300/1077C10G2400/02C10G2400/20
Inventor R·梅尔柏格E·D·加马斯-卡斯特拉诺斯C·R·霍维
Owner UOP LLC
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