초록 ▼

A novel cyclone is disclosed that is effective for separating, from a contaminated gas stream, solid particulates having diameters as low as 4 to 5 microns. When multiple cyclones of the present invention are affixed between upper and lower tube sheets in a separator device, fine particle removal is

A novel cyclone is disclosed that is effective for separating, from a contaminated gas stream, solid particulates having diameters as low as 4 to 5 microns. When multiple cyclones of the present invention are affixed between upper and lower tube sheets in a separator device, fine particle removal is possible to the extent required 1) by stringent regulations governing particulate emissions into the atmosphere, or 2) to prevent damage to turbine blades in downstream power recovery equipment. The cyclones are especially relevant to the problem of removing catalyst fines from refinery effluents, most notably fluid catalytic cracking (FCC) regenerator flue gas. The cyclone separation efficiency is enhanced through the use of 1) a uni-directional flow of gas from the contaminated gas inlet to the clean gas outlet and 2) discharge openings on the surface of the cyclone body that allow ejection of solid particulates.

대표청구항 ▼

1. A fluidized catalytic cracking process for cracking a heavy hydrocarbon feed, the process comprising:a) contacting the heavy hydrocarbon feed with a cracking catalyst to produce a light hydrocarbon product and a spent catalyst having coke deposited thereon;b) regenerating the spent catalyst in a

1. A fluidized catalytic cracking process for cracking a heavy hydrocarbon feed, the process comprising:a) contacting the heavy hydrocarbon feed with a cracking catalyst to produce a light hydrocarbon product and a spent catalyst having coke deposited thereon;b) regenerating the spent catalyst in a catalyst regenerator by contacting the spent catalyst with air to burn the coke and provide a regenerated catalyst and a flue gas;c) separating the regenerated catalyst from the flue gas using a first stage and a second stage separator located within the catalyst regenerator to yield a catalyst fines-contaminated flue gas stream;d) recycling the regenerated catalyst to the cracking reactor for further production of the light hydrocarbon product; ande) purifying the catalyst fines-contaminated flue gas stream in a third stage separator apparatus having an upper and a lower tube sheet contained therein and a plurality of cyclones between the upper and lower tube sheets, each cyclone comprising:i) a substantially vertical cyclone body having a closed bottom end and a top end fixed with respect to the upper tube sheet, the cyclone body defining a gas inlet at its top end for receiving a portion of the catalyst fines-contaminated flue gas stream from above the upper tube sheet and a sidewall of the cyclone body defining a plurality of discharge openings between the upper and the lower tube sheets for tangentially discharging particles and a minor amount of an underflow gas stream;ii) one or more swirl vanes located proximate the gas inlet to induce centripetal acceleration of the catalyst fines-contaminated flue gas stream; andiii) a gas outlet tube located centrally within the cyclone body, extending through the closed bottom, and further extending through the lower tube sheet, the gas outlet tube defining a clean gas inlet for receiving a purified gas stream from within the cyclone body and further defining a clean gas outlet located below the lower tube sheet for discharging the purified gas stream. 2. The process of claim 1 where the purified gas stream has a concentration of particles of 5 microns or greater that is less than about 50% of the concentration of particles of 5 microns or greater in the catalyst fines-contaminated flue gas stream. 3. The process of claim 1 where the minor amount of the underflow gas stream is less than about 10% of the catalyst-fines contaminated flue gas stream.