초록 ▼

A mixture of gases containing hydrogen and at least one further component, for example nitrogen and argon, is enriched in hydrogen in a separation stage by adsorption, or cooling and partial condensation and/or rectification and/or scrubbing. Upstream of this separation stage, at least part of the h

A mixture of gases containing hydrogen and at least one further component, for example nitrogen and argon, is enriched in hydrogen in a separation stage by adsorption, or cooling and partial condensation and/or rectification and/or scrubbing. Upstream of this separation stage, at least part of the hydrogen is separated by membrane diffusion, thereby resulting in a highly improved process as compared to using either the separation stage or membrane diffusion alone, especially in connection with gaseous mixtures having components which are to be used at high pressures, e.g., a purge gas from an ammonia synthesis gas process.

대표청구항 ▼

1. A process for the separation of hydrogen from a mixture of gases containing about 50 to 70% by volume of hydrogen, said process comprising separating more than 60% of the hydrogen up to 95% from the gaseous mixture by diffusion through a semipermeable membrane, thereby forming a residual mixture

1. A process for the separation of hydrogen from a mixture of gases containing about 50 to 70% by volume of hydrogen, said process comprising separating more than 60% of the hydrogen up to 95% from the gaseous mixture by diffusion through a semipermeable membrane, thereby forming a residual mixture of gases depleted in hydrogen, expanding the residual gaseous mixture and passing resultant cooled residual gaseous mixture into indirect heat exchange with liquefied gas, the latter being obtained as bottoms from a rectification stage wherein at least a fraction of said residual gaseous mixture is subjected to rectification downstream of said indirect heat exchange, with the proviso that the process does not comprise a shift reaction. 2. A process according to claim 1, wherein said residual gas is directly cooled and is subjected to a first rectification, and bottoms from said rectification stage is withdrawn and evaporated under subatmospheric pressure. 3. A process according to claim 2, wherein the evaporation is conducted with heat of compression supplied by fluid in a cooling circuit, and resultant cooled fluid is further used as a cooling medium in at least one rectification stage. 4. A process according to claim 3, wherein the fluid circulated in the cooling circuit is a component of the residual mixture of gases. 5. A process according to claim 3, wherein the fluid circulated in the cooling circuit is introduced as reflux to the top of a second rectification stage and to the head condenser of said first rectification stage. 6. A process according to claim 2, wherein the components of the gaseous mixture to be separated have boiling points of not more than approximately 120° K. 7. A process according to claim 2, wherein the subatmospheric pressure is generated by passing a gaseous component of partially liquefied residual mixture of gases through an ejector, as the driving jet. 8. A process according to claim 1, wherein the components of the gaseous mixture to be separated have boiling points of not more than approximately 120° K. 9. A process for the separation of hydrogen from a mixture of gases comprising separating at least part of the hydrogen from the gaseous mixture by diffusion through a semipermeable membrane, thereby forming a residual mixture of gases depleted in hydrogen, and further comprising work expanding the residual gaseous mixture and passing resultant cooled residual gaseous mixture into indirect heat exchange with liquified gas, the latter being obtained as bottoms from a rectification stage wherein at least a fraction of said residual gaseous mixture is subjected to rectification downstream of said indirect heat exchange. 10. A process according to claim 9, wherein the components of the gaseous mixture to be separated have boiling points of not more than approximately 120° K. 11. A process according to claim 9, wherein not more than 60% of the hydrogen is separated from the gaseous by membrane diffusion. 12. A process according to claim 9, wherein more than 60% up to 95% of the hydrogen is separated from the gases by membrane diffusion. 13. A process for the separation of hydrogen from a mixture of gases comprising separating at least part of the hydrogen from the gaseous mixture by diffusion through a semipermeable membrane, thereby forming a residual mixture of gases depleted in hydrogen, directly cooling said residual mixture, subjecting resultant cooled gaseous mixture to a first stage rectification, and withdrawing bottoms from said rectification stage and evaporating said bottoms under subatmospheric pressure. 14. A process according to claim 13, wherein the evaporation is conducted with heat of compression supplied by fluid in a cooling circuit, and resultant cooled fluid is further used as a cooling medium in at least one rectification stage. 15. A process according to claim 14, wherein the fluid circulated in the cooling circuit is a component of the residual mixture of gases. 16. A process according to claim 14, wherein the fluid circulated in the cooling circuit is introduced as reflux to the top of a second rectification stage and to the head condenser of said first rectification stage. 17. A process according to claim 13, wherein the subatmospheric pressure is generated by passing a gaseous component of partially liquefied residual mixture of gases through an ejector, as the driving jet. 18. A process according to claim 13, wherein the components of the gaseous mixture to be separated have boiling points of not more than approximately 120° K.