The invention discloses a low temperature Claus
sulfur recovery process. The process mainly comprises a
thermal reaction section, a catalytic reaction section and a
tail gas
incineration section, wherThe invention discloses a low temperature Claus
sulfur recovery process. The process mainly comprises a
thermal reaction section, a catalytic reaction section and a
tail gas
incineration section, whertion temperature, contributes to performance of
chemical equilibrium towards the direction of
sulfur generation, so that conversion rate and
recovery rate of sulfur are improved. Moreover, the processtion temperature, contributes to performance of
chemical equilibrium towards the direction of sulfur generation, so that conversion rate and recovery rate of sulfur are improved. Moreover, the process has the advantages of simple process flow, relative small equipment and investment, low operation cost and more contribution to
environmental protection. The invention also discloses a device for thehas the advantages of simple process flow, relative small equipment and investment, low operation cost and more contribution to
environmental protection. The invention also discloses a device for the low temperature Claus sulfur recovery process.low temperature Claus sulfur recovery process.ein in a
combustion furnace of the
thermal reaction section, partial
hydrogen sulfide reacts with
oxygen to be converted into
sulfur dioxide, the
hydrogen sulfide and the
sulfur dioxide undergo a Clauein in a
combustion furnace of the thermal reaction section, partial
hydrogen sulfide reacts with
oxygen to be converted into
sulfur dioxide, the
hydrogen sulfide and the sulfur dioxide undergo a Claus reaction to generate sulfur, and process gas after sulfur separation enters the catalytic reaction section; in the reactor of each stage of the catalytic reaction section, the
hydrogen sulfide and ts reaction to generate sulfur, and process gas after sulfur separation enters the catalytic reaction section; in the reactor of each stage of the catalytic reaction section, the
hydrogen sulfide and the sulfur dioxide under conventional Claus reaction, catalyst reactivation, sub-dewpoint and sub-
solid point low temperature Claus reaction in sequence; after the catalyst reaction section, the
tail ghe sulfur dioxide under conventional Claus reaction, catalyst reactivation, sub-dewpoint and sub-
solid point low temperature Claus reaction in sequence; after the catalyst reaction section, the tail gas which is subjected to sulfur separation enters the tail gas
incineration section, and the tail gas is incinerated and exhausted in the tail gas incineration furnace. The process adopts a lower reacas which is subjected to sulfur separation enters the tail gas incineration section, and the tail gas is incinerated and exhausted in the tail gas incineration furnace. The process adopts a lower reac