Method for separating light additive gas in separating nozzle cascades

Claim 2

Process for separating light additive gas at the end of and/or at the location of the change of stage sizes in a separating nozzle cascade operating with a mixture of gaseous or vaporous substances to be separated and a light additive gas, with the separation of the light additive gas being effected by utilizing at least one separating nozzle stage, comprising employing a double deflection separating nozzle stage as the separating nozzle stage for the separation of the light additive gas, wherein the mixture of substances to be separated in the separation of the light additive gas is taken at least at one change of stage size location in the separating nozzle cascade, is separated by the double deflection nozzle into a first partial stream deriched in the light additive gas and a second partial stream enriched in the light additive gas, and the first partial stream is fed into a product side of a section of the separating nozzle cascade at that point where the composition in the first partial stream with respect to the substances to be separated in the separating nozzle cascade and the composition in the separating nozzle cascade section substantially coincide after combination.

Claim 3

Process as defined in claim 1, wherein the separating nozzle stage for the separation of the light additive gas is a double deflection separating nozzle stage which serves as a preliminary separating stage and is combined with a low temperature separator.

Claim 4

Process as defined in claim 1, wherein a gas separating cascade comprising a plurality of series-connected double deflection separating nozzle stages is used for the separation of the light additive gas.

Claim 5

Process as defined in claim 3, wherein the gas separating cascade comprises an entrance separating nozzle stage and at least one separating nozzle stage connected downstream of the entrance separating nozzle stage, and a product stream is taken from a heavy fraction of a separating nozzle stage connected downstream of the entrance separating nozzle stage in the gas separating cascade.

Claim 6

Process as defined in claim 1, wherein the mixture of substances to be separated in the separation of the light additive gas and taken at the change of stage size location is separated with the use of a gas separating cascade comprising a plurality of series-connected double deflection separating nozzle stages including an entrance separating nozzle stage and at least one separating nozzle stage connected downstream of the entrance separating nozzle stage, and the partial stream is taken from a heavy fraction of a separating nozzle stage connected downstream of the entrance separating nozzle stage in the gas separating cascade.

Claim 7

In a process having an isotope separating cascade for separating a mixture of isotopes and employing light additive gas, and wherein the light additive gas is separated at the end of the isotope separating cascade and/or at the location of the change of stage sizes in the isotope separating cascade, the isotope separating cascade operating with a mixture of gaseous or vaporous isotope substances to be separated and a light additive gas, with the separation of the light additive gas being effected by utilizing at least one separating nozzle stage, comprising employing a double deflection separating nozzle stage as the separating nozzle stage for the separation of the light additive gas, wherein the mixture of substances to be separated in the separation of the light additive gas is taken at least at one change of stage size location in the isotope separating cascade, is separated by the double deflection apparatus into a first partial stream deriched in the light additive gas and a second partial stream enriched in the light additive gas, and the first partial stream is fed into a product side of a section of the isotope separating cascade at that point where the composition of the mixture of isotopes in the first partial stream and in the isotope separating nozzle cascade section substantially coincide after combination.

Claim 8

In a process having an isotope separating cascade for separating a mixture of isotopes and employing light additive gas, and wherein the light additive gas is separated at the end of the isotope separating cascade and/or at the location of the change of stage sizes in the isotope separating cascade, the isotope separating cascade operating with a mixture of gaseous or vaporous isotope substances to be separated and a light additive gas, with the separation of the light additive gas being effected by utilizing at least one separating nozzle stage, comprising employing a double deflection separating nozzle stage as the separating nozzle stage for the separation of the light additive gas, wherein the mixture of substances to be separated in the separation of the light additive gas is taken at least at one change of stage size location in the isotope separating cascade, is separated by the double deflection apparatus into a first partial stream deriched in the light additive gas and a second partial stream enriched in the light additive gas, and the first partial stream is fed into a product side of a section of the isotope separating cascade at that point where the composition of the mixture of isotopes in the first partial stream and in the isotope separating nozzle cascade section substantially coincide after combination.

Claim 9

Process as defined in claim 6, wherein the separating nozzle stage for the separation of the light additive gas is a double deflection separating nozzle stage which serves as a preliminary separating stage and is combined with a low temperature separator.

Claim 10

Process as defined in claim 6, wherein a gas separating cascade comprising a plurality of series-connected double deflection separating nozzle stages is used for the separation of the light additive gas.

Claim 11

Process as defined in claim 8, wherein the gas separating cascade comprises an entrance separating nozzle stage and at least one separating nozzle stage, and a product stream is taken from a heavy fraction of a separating nozzle stage connected downstream of the entrance separating nozzle stage in the gas separating cascade.

Claim 12

Process as defined in claim 6, wherein the mixture of substances to be separated in the separation of the light additive gas and taken at the change of stage size location is separated with the use of a gas separating cascade comprising a plurality of series-connected double deflection separating nozzle stages including an entrance separating nozzle stage and at least one separating nozzle stage connected downstream of the entrance separating nozzle stage, and the first partial stream is taken from a heavy fraction of a separating nozzle stage connected downstream of the entrance separating nozzle stage in the gas separating cascade.