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PETROBRAS. Canoas, RS. 70 mt/d Claus unit (from refinery) planned. Contr ..... 1997. Cubatao, SP. 2-35 mt/d Claus unit (from refinery) in the engineering ..... 1997. Paulinia, SP. 60 mt/d Claus unit (from fuel gas and LPG desulf
units goes to a Claus plant for sulfur recovery. The Claus unit was designed also by Elf (the former Elf proprietary ..... a negative impact on the operation of the downstream Claus unit . Click here to enlarge image At that time
sulfur-recovery unit. Plant 1 has a two-stage Claus followed by a Superclaus, while Plant 2 has a three-stage Claus unit . The plant’s license requires a current overall sulfur-recovery efficiency of 96.5%. The original feed to
energy produced by the downstream Claus unit as low-pressure (LP) steam ..... This uses only one third of the Claus unit 's steam production, and only one ..... specification is important for charging a Claus unit but is equally important for acid
possible alternatie to debottlenecking a Claus unit . What modifications are needed ..... the maximum operating pressure of a Claus unit , provided that the liquid seals ..... gas unit. Sloan: Operating the Claus unit at higher pressures enables the product
Basic Claus process Click here to enlarge image A typical Claus unit consists of a thermal stage followed by two or, more ..... before each catalytic stage. Fig. 1 shows a typical Claus unit . The thermal stage consists of a reaction furnace
Kazakhstan, Italy, and the Philippines in various stages of completion. Parsons is in the engineering phase of a Claus unit project for Tengizchevroil at Tengiz, Kazakhstan. The project, when completed in 2005, will process 2,400 t/d
natural gas by converting it to sulfur. A conventional hydrodesulfurization plant comprises an amine scrubbing unit, a Claus unit , and a Claus tail gas unit; the Shell-Paques process requires dilution in a caustic solution followed by treatment
South Killingholme, U.K. The process will boost sulfur recovery to 98%. Modifications to the upstream two-reactor Claus unit and installation of the Resulf-MM system will give the refinery two trains, each capable of fulfilling 100% of the
plant is a bottleneck for plant-capacity increase or feed-gas composition change. Sour-gas quality delivered to a Claus unit is such that it requires improvements; that is, an H 2 S concentration increase by introduction of CO 2 slippage in