摘要:
The invention relates to a condenser, having a process gas side and a heat transfer medium side said condenser being configured for feeding a hot process gas containing a condensable component to an inlet of the condensing side, and being further configured for withdrawing a cooled process gas from an outlet of the condensing side, and being even further configured for withdrawing a condensate in a position proximate to one end of the condenser, and said condenser having the process gas side divided in a process gas cooling zone configured for having a cool heat transfer medium inlet and a heated heat transfer medium outlet, and a process gas re-heating zone downstream the process gas cooling section, configured for re-heating of the process gas, as well as a processes for condensation and production of sulphuric acid employing such a condenser.
摘要:
A converter having an exterior shell with a central axis, at least one gas inlet and at least one gas outlet. The exterior shell includes a base and an interior support structure. A number of vertically stacked catalytic chambers within the exterior shell are each in communication with one or more gas inlets and gas outlets. Each chamber is defined by an inner wall of the external shell, a permeable catalytic bed support platform, a lower division plate spaced below the platform defining a gas retention plenum and an upper division plate above the platform. At least one of: the platform; the upper division plate; and the lower division plate have a toroid surface symmetric about the central axis with an outer periphery supported by the inner wall of the exterior shell and an inner periphery supported by the interior support structure.
摘要:
Die vorliegende Erfindung betrifft ein Verfahren zur kontinuierlichen katalytischen kompletten oder teilweisen Oxidation eines Ausgangsgases enthaltend von 0,1 bis 66 Vol. % Schwefeldioxid zzgl. Sauerstoff, wobei der Katalysator mit einer quasi-isothermen Prozessführung unter Energie Zu- oder -Abfuhr aktiv gehalten wird. Außerdem betrifft die vorliegende Erfindung eine Vorrichtung zur kontinuierlichen katalytischen kompletten oder teilweisen Oxidation eines Ausgangsgases enthaltend Schwefeldioxid und Sauerstoff, gekennzeichnet durch mindestens einen Röhrenkontaktapparat, der ein stehender Wärmetauscher aus mindestens einem Doppelmantelrohr ist, dessen mit Katalysator eingefülltes Innenrohr ein Reaktionsrohr bildet, wobei Wärme um das Reaktionsrohr im Gleichstrom übertragen wird und dem Röhrenkontaktapparat ein Absorber zur Abtrennung von SO 3 nachgeschaltet wird.
摘要:
A process for the condensation of sulfur trioxide from hot starting gases comprising the following steps: a) cooling the starting gas to a temperature of 40 to 45O0C in at least one heat exchanger (3) (4), in which a gas is used as cooling medium, b) introducing the cooled starting gas into a condensation device (5), c) condensing the sulfur trioxide in the condensation device (5), in which a liquid chemically inert to sulfur trioxide is used as cooling medium, and d) withdrawing the condensed, liquid sulfur trioxide from the condensation device (5). A plant for carrying out the process comprising: a first and a second heat exchanger (3) (4) comprising supply and discharge conduits for coolant and starting gas, and a condensation device (5), in which a liquid chemically inert to sulfur trioxide is provided as cooling medium.
摘要:
A method of suppressing corrosion of stainless steels or carbon steels exposed to environments of sulfuric acid or sulfuric acid-containing solution, wherein the stainless steel or carbon steel, and a metal selected from the group consisting of platinum, gold, silver and palladium, or an alloy thereof are brought into contact.
摘要:
A process for production of sulphuric acid comprising condensing sulphuric acid vapour from a gas mixture containing 0.01 to 10 vol.% of H 2 SO 4 vapour calculated at complete hydration of SO 3 in the gas to H 2 SO 4 and 0 to 50 vol.% of water vapour by cooling of the gas in a sulphuric acid tower, wherein a stream containing NH 3 is added upstream of the tower in an amount corresponding to 0.01-100 ppm NH 3 by vol. in the gas stream at the entry of the tower.