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Implications of using “Torch Oil”

“Torch oil” is a term which is usually applied to a gas oil that is burned in FCC regenerators, to supply necessary heat requirements during startup, shutdown, or feed-outage conditions, when coke is not being produced in the reactor. It is injected usually through special nozzles which discharge into the dense catalyst bed of a regenerator.Implications of FCCU torch oil in the regenerator

Requirements for Torch Oil Lightoff

Almost any gas oil can be utilized as torch oil to an FCC unit. However, it is essential to ensure that the oil lights off properly when injected. Torch oil that does not ignite at the injection points in the dense bed will pass into the upper zones of the vessel, i.e. dilute phase, cyclones, and overhead system, where it can ignite, possibly even explode, with obvious undesirable consequences.

It should be recognized that different gas oils have different ignition characteristics. Generally, the lighter the oil, the higher is its ignition temperature.

Nozzles used for torch oil should be properly designed for the service. This usually involves a reasonably high pressure drop, possibly with steam injection, to achieve adequate atomization.

The catalyst dense bed temperature should be safely above the ignition temperature of the gas oil before it is injected. For virgin VGO, this is usually specified as a minimum temperature of 700 to 750°F (370 – 400°C). In addition, there should be an adequate depth of catalyst above the T.O. nozzles, to ensure proper ignition of the oil, and efficient dispersion of the heat into the catalyst bed. Some refiners specify a minimum bed coverage of about 5 ft. (1.5 m) above the nozzles.

When Should Torch Oil Be Used

Obviously, it is necessary to use torch oil during a unit startup, when heat is required to heat the unit catalyst in preparation for introduction of feed, and often during a unit shutdown, to control the rate of unit cooldown.

Torch oil is also used when it is necessary to remove feed during normal operation, possibly due to an emergency condition. Often, the catalyst can be kept circulating between regenerator and reactor during the feed outage, with appropriate temperatures being maintained by torch oil injection to the regenerator dense bed. This holding condition can be maintained indefinitely.

However, there is a downside to continuous torch oil use for long periods of time; that is, deactivation of the unit catalyst inventory. Localized high temperatures at the torch oil nozzles are believed to be the cause of that deactivation. Generally, maintaining this condition for more than about two days is found to be uneconomic. There is a balance between maintaining the catalyst inventory hot in the unit, and accepting the resulting catalyst deactivation, versus taking the time to withdraw the catalyst and re-load it later when the unit is again ready to resume operations. CatCracking / FCCU logo

One factor which can minimize the degree of catalyst deactivation with torch oil usage is to employ multiple torch oil nozzles in the regenerator. This lessens the concentration of high temperature heat released in a single localized zone of the bed.

2 responses to “Implications of using “Torch Oil””

  1. mikee751 says:

    There are many ways to increase regen temperature, and during S/U, S/D, emergencies the use of torch oil is quite suitable. But in normal operation, it kills catalyst more than the other options. Reduce excess O2 to regen if full combustion, increase air if partial combustion, increase feed preheat (esp. if you have preheat furnace), decrease lift / feed steam, reduce stripper steam, in that order for less impact on conversion and cat deactivation than using torch oil. If long term problem, change to higher coke (generally higher RE) catalyst. Torch oil is worst option of the above, for non emergency cases (which include S/U, S/D).

  2. dasila.prabha@gmail.com says:

    If there is no option to increase Feed preheat temp, and not using Excess O2 for full combustion . What else other options can be to increase the Regen bed temp to reduce the torch oil consumption.

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Posted by: Paul R Orlowski

Paul Orlowski is General Manager for the Refining Community which includes Coking.com, CatCracking.com, SulfurUnit.com, Resid Hydrocracking and SDA. They consult at refineries around the world. They've hosted 36 technical conferences around the globe, trained 1,000's and completed very beneficial consulting and troubleshooting projects. Paul co-founded Coking.com Inc in 1998 with Gary Pitman. Evan Hyde later joined the team. Besides being an educator and software applications engineer, he worked 18 years at ARCO and BP refineries near Seattle, WA USA. Previously he worked for Science Applications International Corporation and Dealer Information Systems. In 2019 look for #RefComm Galveston Coking | CatCracking | Resid Hydrocracking and RefComm® Rotterdam Coking | CatCracking. In 2020 Galveston; Gdansk, Poland and Rio de Janeiro, Brazil and Singapore.

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