Continuous Regenerative (moving bed) CCR Platforming – UOP Process. In this process, three or four reactors are installed one on the top of the other. Our Garden City RF2 fans are perfect for Continuous Catalyst Regeneration in oil refineries. We set the standards for the chlorination and regeneration blowers. This course provides an overview of the CCR Platforming unit with a CycleMax or pressurized regenerator. The principles of catalyst regeneration and.

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Such a unit is referred to as a semi-regenerative catalytic reformer SRR. The table just below lists some fairly typical straight-run heavy naphtha feedstocks, available for catalytic reforming, derived from various crude oils.

If you would like to submit an enquiry please get in touch. The hot reaction products from the third reactor are partially cooled by flowing through the heat exchanger where the feed to the first reactor is preheated and then flow through a water-cooled heat exchanger before flowing through the pressure controller PC into the gas separator.

Reformate can ccrr blended directly in the gasoline pool but often it is separated in two or more streams. Our fans are designed by a team of highly experienced engineers and designers, and are manufactured by our network of qualified manufacturing partners.

In addition to a gasoline blending stock, reformate is the main source of aromatic bulk chemicals such as benzenetoluenexylene and ethylbenzene which have diverse uses, most importantly as raw materials for conversion into plastics. This means that the reformate should either be further processed in an aromatics extraction unit, or blended with appropriate hydrocarbon streams with low content of aromatics.

Catalytic reformation is profitable in that it converts long-chain hydrocarbons, for which there is limited demand despite high supply, into short-chained hydrocarbons, which, due to their uses in petrol fuel, are in much greater demand. In the years since then, many other versions of the process have been developed by some of the major oil companies and other organizations. Views Read Edit View history. Various bearing lubrication methods are available for the monoblock bearing assembly including static oil, forced lubrication, or oil mist lubrication.

Standard fan features include a custom fabricated monoblock bearing assembly, nitrogen purged Shaft Seal, and custom designed fan wheels with a focus on efficiency and reliability. Fans for this process are manufactured for lasting performance due to their purposeful design with rigid plaforming walls, and filled with high density insulation.

Continuous Catalyst Regeneration (CCR) Platforming.

A petroleum refinery includes many unit operations and unit processes. As the vaporized stream proceeds through the three reactors, the reaction rates decrease and the reactors therefore become larger. The higher the severity of the reacting conditions temperaturethe higher is the octane of the platforminf reformate but also the shorter will be the duration of the cycle between two regenerations. This contributes both to costs and the emissions of the process.


There are many chemical reactions that occur in the catalytic reforming process, all of which occur in the presence of a catalyst and a high partial pressure of hydrogen.

The manufacturing process is initiated by a testing and traceability procedure used to check the quality of the alloy rich materials used to fabricate your fans for conventional and high pressure catalyst regeneration process fans.

Main licensors of catalytic reforming processes, UOP and Axens, constantly work pplatforming improving the catalysts, but the rate of improvement seems to be reaching its physical limits.

Catalytic reforming – Wikipedia

Cyclic catalytic reformers serve to extend the period between required shutdowns. This page was last edited on 11 Decemberat At the same time, the amount of reheat required between the reactors becomes smaller. In practice, the higher the content of naphtenes in the naphtha feedstock, the better will be the quality of the reformate and the higher the production of hydrogen. The naphtha is a mixture of very many different hydrocarbon compounds. The process converts low-octane linear hydrocarbons paraffins into branched alkanes isoparaffins and cyclic naphtheneswhich are then partially dehydrogenated to produce high-octane aromatic hydrocarbons.

Top manufacturing capabilities and project management support.

The benzene extracted can be marketed as feedstock for cccr chemical industry. Garden City Fans are designed with quality and total cost of ownership in mind; and with service centers around the world, we remain committed to provide the parts and service our plxtforming need to mitigate downtime.

However, for the most part, catalytic reforming is mainly used on the straight-run heavy naphthas, such as those in the above table, derived from the distillation of crude oils. The liquid feed at the bottom left in the diagram is pumped up to the reaction pressure 5—45 atm and is joined by a stream of hydrogen-rich recycle gas.

As the leading global supplier of fans for this application, Howden has installed olatforming of fans for the catalyst regeneration process around the world.

The resulting liquid—gas mixture is preheated by flowing through a heat exchanger. When that reactor is regenerated, it replaces another reactor which, in turn, is isolated so that it can then be regenerated.

Dehydrogenation, an important component of reforming, is a strongly endothermic reaction, and as such, requires the reactor vessel to be externally heated.

Schematic diagram of a typical semi-regenerative catalytic reformer unit in a petroleum refinery. Our catalyst regeneration process AMCA test laboratory continually conducts performance tests, sound measurement, and stress analysis to meet our current needs, as well as developing future products. The catalyst regeneration process allows continuous regeneration of a controlled quantity of catalyst and is used for reforming applications by refineries. Catalytic reforming requires a whole range of other processing units at the refinery apart from the distillation tower, a naphtha hydrotreater, usually an isomerization unit to process light naphtha, an aromatics extraction unit, etc.


It should be noted that there are a great many petroleum crude oil sources worldwide and each crude oil has its own unique composition or “assay”. The activity of the catalyst can be periodically regenerated or restored by in situ high temperature oxidation of the coke followed by chlorination.

The isomerization of normal paraffins does not consume or produce hydrogen. Some installations use three separate fired heaters as shown in the schematic diagram and some installations use a single fired heater with three separate heating coils. It can be seen that they differ significantly in their content of paraffins, naphthenes and aromatics:.

The most commonly used type of catalytic reforming unit has three reactorseach with a fixed bed of catalyst, and all of the catalyst is regenerated in situ during routine catalyst regeneration shutdowns which occur approximately once each 6 to 24 months. The overhead liquid distillate is called naphtha and will become a major component of the refinery’s gasoline petrol product after it is further processed through a catalytic hydrodesulfurizer to remove sulfur -containing hydrocarbons and a catalytic reformer to reform its hydrocarbon molecules into more complex molecules with a higher octane rating value.

Quality and performance is in our DNA Howden Garden City Fans was one of the first manufacturers to develop a product for the platforming process and has been a global market leader for over 40 years.

It can also be used to improve the octane rating of short-chained hydrocarbons by aromatizing them. Every fan we manufacture for high pressure catalyst regeneration is built and tested to withstand psi kPa hydrostatic pressure.

Also, not all refineries process the same crude oils and each refinery produces its own straight-run naphthas with their own unique initial and final boiling points.

The naphthas derived from the distillation of crude oils are referred to as “straight-run” naphthas. Non-Destructive Test NDT procedures such as magnetic particle, liquid dye penetrant, radiograph, and ultrasonic testing are used to ensure the quality of the welds. Rate equations of this type explicitly account for the interaction of chemical species with catalyst and contain denominators in which terms characteristic of the adsorption of reacting species are presented.

Most catalytic reforming catalysts contain platinum or rhenium on a silica or silica-alumina support base, and some contain both platinum and rhenium.