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A process for producing chlorine comprising the step of oxidizing hydrogen chloride in a gas containing hydrogen chloride with a gas containing oxygen in a fixed bed reaction system having a reaction zone comprising a catalyst-packed layer, wherein a superficial linear velocity of the gas in a colum

A process for producing chlorine comprising the step of oxidizing hydrogen chloride in a gas containing hydrogen chloride with a gas containing oxygen in a fixed bed reaction system having a reaction zone comprising a catalyst-packed layer, wherein a superficial linear velocity of the gas in a column is from 0.70 to 10 m/sec. According to this process, the stable activity of the catalyst is maintained and chlorine can be stably obtained at a high yield since the excessive hot spot in the catalyst-packed layer is suppressed and the catalyst-packed layer can be effectively used.

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1. A process for producing chlorine comprising the step of oxidizing hydrogen chloride in a gas containing hydrogen chloride with a gas containing oxygen in a fixed bed reaction system having a reaction zone comprising a catalyst-packed layer, wherein a superficial linear velocity of all the gases s

1. A process for producing chlorine comprising the step of oxidizing hydrogen chloride in a gas containing hydrogen chloride with a gas containing oxygen in a fixed bed reaction system having a reaction zone comprising a catalyst-packed layer, wherein a superficial linear velocity of all the gases supplied in the catalyst-packed layer is from 0.70 to 10 m/sec. 2. The process according to claim 1, wherein the oxidation is carried out with a fixed bed reaction system comprising at least two reaction zones comprising a catalyst-packed layer. 3. The process according to claim 2, wherein the ratio of the first reaction zone, in which the raw materials are firstly supplied, is 70% by volume or less based on the whole volume of said at least two reaction zones. 4. The process according to claim 3, where in a temperature in the second reaction zone, to which the raw materials are supplied next to the first reaction zone, is at least 5° C. higher than that in the first reaction zone. 5. The process according to claim 3, an activity in the second reaction zone is at least 1.1 times higher than that in the first reaction zone. 6. The process according to claim 2, wherein the reaction zones are packed with substantially the catalyst only, a mixture of substantially the catalyst and an inactive material, a mixture of substantially the catalyst and a carrier, or a mixture of substantially the catalyst, the inactive material and the carrier so that the thermal conductivity becomes highest in the first reaction zone. 7. The process according to claim 2, wherein the reaction zones are packed with substantially the catalyst only, a mixture of substantially the catalyst and an inactive material, a mixture of substantially the catalyst and a carrier, or a mixture of substantially the catalyst, the inactive material and the carrier so that the thermal conductivity in the reaction zones successively decreases from the first reaction zone to the last reaction zone to which the raw materials are lastly supplied, along the direction of the gas flow. 8. The process according to claim 2, wherein the reaction zones are packed with substantially the catalyst only, a mixture of substantially the catalyst and an inactive material, a mixture of substantially the catalyst and a carrier, or a mixture of substantially the catalyst, the inactive material and the carrier so that the activities of the reaction zones successively increase from the first reaction zone to the last reaction zone along the direction of the gas flow. 9. The process according to claim 2, wherein the reaction zones are packed with substantially the catalyst only, a mixture of substantially the catalyst and an inactive material, a mixture of substantially the catalyst and a carrier, or a mixture of substantially the catalyst, the inactive material and the carrier so that the activity of the last reaction zone is higher than that of the reaction zone immediately preceding the last reaction zone, and the hot spot in the last reaction zone is made lower than that in the reaction zone immediately preceding the last reaction zone. 10. The process according to claim 2, wherein a gas temperature at the exit of the last reaction zone is in the range between 200 and 350° C. 11. The process according to claim 1, wherein the temperature of the reaction zones comprising the catalyst-packed layer is controlled with a heat exchange system. 12. The process according to claim 1, wherein the temperature of the reaction zones comprising the catalyst-packed layer is controlled with at least two independent temperature control systems. 13. The process according to claim 2, wherein the volume of the gas containing oxygen is divided and supplied in the reaction zones.