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A process of removing pollutants from exhaust gases in a circulating fluidized bed, in which solids are circulated through a fluidized bed reactor, separated in a separator and returned via a return line, to the reactor. The exhaust gas is introduced as a fluidizing gas into a fluidized bed which co

A process of removing pollutants from exhaust gases in a circulating fluidized bed, in which solids are circulated through a fluidized bed reactor, separated in a separator and returned via a return line, to the reactor. The exhaust gas is introduced as a fluidizing gas into a fluidized bed which consists of two solid fractions differing in particle size, namely, a coarse-grained fraction having a particle size d p 50 in the range of 150 to 500 microns and a fine-grained fraction having a particle size d p 50 below 10 microns.

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1. A process for removal of pollutants of the group consisting of SO x, HCl, HF and H 2 S from an exhaust gas by means of solids circulating in a circulating system formed by a fluidized bed reactor, a separator and a return line comprising introducing the polluted exhaust gas into said fluidized be

1. A process for removal of pollutants of the group consisting of SO x, HCl, HF and H 2 S from an exhaust gas by means of solids circulating in a circulating system formed by a fluidized bed reactor, a separator and a return line comprising introducing the polluted exhaust gas into said fluidized bed reactor to fluidize the bed therein, said bed consisting of two solid fractions, the first fraction having a particle size d p 50 in the range of 150 to 500 microns and the second fraction having a particle size d p 50 below 10 microns, collecting solids entrained by the gas in separate particle size fractions and returning at least the coarser solid fraction into said fluidized bed reactor. 2. A process according to claim 1, wherein CaO, CaCO 3, MgO, MgCO 3, dolomite and/or sand is used as the first fraction of solids. 3. A process according to claim 1, wherein Ca(OH) 2 is used as the second fraction of solids. 4. A process according to claim 1, wherein the fluidized bed is controlled to contain 70 to 90% by weight of the first fraction of solids and 10 to 30% by weight of second fraction of solids. 5. A process according to claim 1, wherein a fluidized state in the fluidized bed reactor, as defined by the Froude and Archimedes numbers, is adjusted according to: ##EQU## and ##EQU## 6. A process according to claim 1, wherein a gas velocity of 1 to 10 m/sec (stated as the velocity in the empty reactor) is maintained in the fluidized bed reactor. 7. A process according to claim 1, wherein a mean suspension density of 0.2 to 2 kg/m 3 is maintained in the fluidized bed reactor. 8. A process according to claim 1, wherein the quantity of solids circulated per hour is adjusted to 20 to 150 times the quantity of solids contained in the fluidized bed reactor. 9. A process according to claim 1, wherein the solids entrained by the gases are removed in an electrostatic precipitator. 10. A process according to claim 9, wherein the solids entrained by the gases are collected in a multi-field electrostatic precipitator in separate particle size fractions and at least the coarse fraction of solids collected in the first field are returned to the fluidized bed reactor. 11. A process according to claim 10, wherein the second fraction of solids collected are removed. 12. A process according to claim 1, wherein the solids in the gas discharged from the fluidized bed reactor are recirculated in a separator and a return line therefrom into said reactor.