Sulphur Recovery - SUPERCLAUS® / Caustic Scrubber Process
Applications: Selection of an appropriate and cost-effective Tail Gas Treatment process to follow existing Claus plants is a challenge facing refiners and natural gas plant owners around the world. New emission regulations, interest in increasing sulphur recovery and processing of higher sulphur crudes are the main drivers.
The most common approach is to install an amine-based Tail Gas Treatment Unit (TGTU), however, lower investment costs and higher reliability can be achieved by combining two well established processes, Comprimo’s SUPERCLAUS® process and caustic scrubber wet gas technology.
By combining these technologies investment costs are reduced, the process is less expensive to operate and to maintain, requires a smaller footprint, greatly simplifies overall operation and has a greater on-stream reliability when compared to an amine based TGTU.
Description: By combining the SUPERCLAUS® and caustic scrubber technologies, the overall system can achieve greater than 99.9% sulphur removal at compelling capital and operating costs. Minimum 99.0% of the H2S is captured and recovered as elemental sulphur by the SUPERCLAUS® process and the remaining sulphur is scrubbed and converted to Na2SO4 by the caustic scrubber. The residual SO2 content in the flue gas is typically less than 50 ppmv.
The SUPERCLAUS® process consists of a thermal stage followed by minimum three catalytic reaction stages with sulphur removed between stages by condensers. The first two or three reactors are filled with standard Claus catalyst while the final reactor is filled with selective oxidation catalyst. In the thermal stage, the acid gas is burned with a substoichiometric amount of controlled combustion air such that the tail gas leaving the last Claus reactor contains typically 0.8 to 1.0 vol.% of H2S. The selective oxidation catalyst in the final reactor oxidizes the H2S to sulphur at an efficiency of more than 85%. Depending on feed gas conditions and unit layout, a sulphur recovery up to 99.2% can be achieved.
The resulting SUPERCLAUS® tail gas is routed to an incinerator, in which all sulphur compounds are converted to SO2.
In the downstream caustic scrubber, scrubbing liquid is injected, counter current to the incinerator flue gas. Liquid collides with down flowing gas to create a region with extreme turbulence, with a high rate of mass transfer. Quenching of the incinerator flue gas and SO2 removal from the gas occur in this region, there with creating sulphite salts. The clean, water saturated gas is then passed on to atmosphere through mist removal devices, reducing the SO2 content to < 50 ppmv.
The liquid reverses to the vessel sump for recycle back to the inlet. In the vessel sump, oxidation air is used to convert the sulphites to sulphates, that can be routed to waste water treatment.
Applications: Refineries and gas plants around the world are challenged by new emission regulations, a stronger push to increase sulphur removal and the processing of higher sulphur crudes. The addition of a Beavon Sulfur removal - Methyldiethanolamine (BSR®-MDEA) Tail Gas Treatment Unit (TGTU) to ...
Applications: The ADIP process is a regenerative process developed to selectively reduce H2S in gas to very low concentrations in the presence of CO2. The ADIP process uses an aqueous solution of diisopropanol amine (DIPA) or the aqueous solution of methyldiethanol amine (MDEA). MDEA is used for those ...
The SUPERCLAUS® process recovers elemental sulphur from H2S-containing gases originating from gas treating and sour water stripper plants. Yields up to 99.2% overall sulphur recovery, without any further tail gas clean-up, are possible. The SUPERCLAUS® process consists of a thermal stage followed ...
Applications: The design intent is to have accurate SRU tail gas quality control in order to optimize sulphur recovery. ABC provides that. It is clearly superior over conventional SRU control and has always been Comprimo’s control system of choice for the EUROCLAUS®/SUPERCLAUS® process ...