Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
385 words
A process for the exchange of hydrogen isotopes using a catalyst bed assembly, comprising: a. simultaneously contacting streams of liquid water and hydrogen with one another and a catalyst packed bed assembly in the path of the contacting streams, both of said streams being at a temperature in the range 273° to 573° K., with one of the streams containing a concentration of a hydrogen isotope in excess of that which it would contain when the liquid water-gaseous hydrogen streams are in isotopic equilibrium at the operating conditions of temperature and mass flow rates of the streams and the other stream being a deficient stream and containing a concentration of that hydrogen isotope which is less than that which it would contain when the liquid water gaseous hydrogen is in equilibrium at said operating conditions, so that the deficient stream is enriched by transfer of the hydrogen isotope in a two-step hydrogen isotope exchange process from the other stream with the following simultaneous reactions being closely coupled in space ##EQU5## b. recovering the said stream enriched in the hydrogen isotope, and wherein: c. the catalyst packed bed assembly comprises: i. a catalyst structure comprising at least one carrier, catalyst crystallites of at least one catalytically active metal selected from Group VIII of the Periodic Table on the support, and a water repellent, water vapour and hydrogen gas permeable, porous, polymeric material partially enclosing the catalyst crystallites to substantially inhibit the contact of liquid water with the catalyst crystallites while allowing contact therewith of hydrogen gas and water vapour from the liquid water, and ii. a packing structure interspersed with (i) to form therewith the catalyst packed bed assembly across the whole path of the contacting streams, and having an exterior surface which is substantially hydrophilic and relatively noncatalytically active with regard to hydrogen isotope exchange between hydrogen gas and water vapour to that of the catalyst bodies, so that: d. the hydrogen isotope exchange primarily occurs simultaneously between hydrogen gas and water vapour contacting the catalyst crystallites, and between water vapour contacting the liquid water and that liquid water, and the substantially hydrophilic exterior surface of the packing structure increases the contact surface area between the water vapour and liquid water thereby increasing the rate of hydrogen isotope exchange between water vapour and liquid water.
Claim 2
Dependent Claim
385 words
A process for the exchange of hydrogen isotopes using a catalyst bed assembly, comprising: a. simultaneously contacting streams of liquid water and hydrogen with one another and a catalyst packed bed assembly in the path of the contacting streams, both of said streams being at a temperature in the range 273° to 573° K., with one of the streams containing a concentration of a hydrogen isotope in excess of that which it would contain when the liquid water-gaseous hydrogen streams are in isotopic equilibrium at the operating conditions of temperature and mass flow rates of the streams and the other stream being a deficient stream and containing a concentration of that hydrogen isotope which is less than that which it would contain when the liquid water gaseous hydrogen is in equilibrium at said operating conditions, so that the deficient stream is enriched by transfer of the hydrogen isotope in a two-step hydrogen isotope exchange process from the other stream with the following simultaneous reactions being closely coupled in space ##EQU5## b. recovering the said stream enriched in the hydrogen isotope, and wherein: c. the catalyst packed bed assembly comprises: i. a catalyst structure comprising at least one carrier, catalyst crystallites of at least one catalytically active metal selected from Group VIII of the Periodic Table on the support, and a water repellent, water vapour and hydrogen gas permeable, porous, polymeric material partially enclosing the catalyst crystallites to substantially inhibit the contact of liquid water with the catalyst crystallites while allowing contact therewith of hydrogen gas and water vapour from the liquid water, and ii. a packing structure interspersed with (i) to form therewith the catalyst packed bed assembly across the whole path of the contacting streams, and having an exterior surface which is substantially hydrophilic and relatively noncatalytically active with regard to hydrogen isotope exchange between hydrogen gas and water vapour to that of the catalyst bodies, so that: d. the hydrogen isotope exchange primarily occurs simultaneously between hydrogen gas and water vapour contacting the catalyst crystallites, and between water vapour contacting the liquid water and that liquid water, and the substantially hydrophilic exterior surface of the packing structure increases the contact surface area between the water vapour and liquid water thereby increasing the rate of hydrogen isotope exchange between water vapour and liquid water.
Claim 3
Dependent Claim
49 words
A process according to claim 1, wherein the catalyst packed bed assembly comprises corrugated sheets with fluid passage intertices between them, platinized carbon particles are deposited on some of the sheets to provide the catalyst structure and are bonded thereto with polytetrafluoroethylene, and the remaining sheets have hydrophilic surfaces.
Claim 4
Dependent Claim
54 words
A process according to claim 1, wherein the catalyst packed bed assembly comprises a mixture of corrugated and plane sheets with fluid passage interstices between them, platinized carbon particles are deposited on some of the sheets to provide the catalyst structure and are bonded thereto with polytetrafluoroethylene, and the remaining sheets have hydrophilic surfaces.
Claim 5
Dependent Claim
50 words
A process according to claim 1, wherein the catalyst packed bed assembly comprises corrugated gauze members with fluid passage interstices between them, platinized carbon particles are deposited on some of the members to provide the catalyst structure and are bonded thereto with polytetrafluoroethylene, and the remaining members have hydrophilic surfaces.
Claim 6
Dependent Claim
55 words
A process according to claim 1, wherein the catalyst packed bed assembly comprises a mixture of corrugated and plane gauze members with fluid passage interstices between them, platinized carbon particles are deposited on some of the members to provide the catalyst structure and are bonded thereto with polytetrafluoroethylene, and the remaining members have hydrophilic surfaces.
Claim 7
Dependent Claim
34 words
A process according to claim 1, wherein the catalyst structure comprises a plurality of discrete catalyst bodies and the packing structure comprises a plurality of discrete packing bodies intermingled with the discrete catalyst bodies.
Claim 8
Dependent Claim
24 words
A process according to claim 6, wherein the catalyst bodies and packing bodies are randomly dispersed together to form the packed catalyst bed assembly.
Claim 9
Dependent Claim
36 words
A process according to claim 6, wherein the catalyst packed bed assembly comprises layers of catalyst bodies alternating with layers of the packing bodies, with each layer extending across the whole width of the contacting streams.
Claim 10
Dependent Claim
41 words
A process according to claim 6, wherein the catalyst packed bed assembly contains catalyst bodies whose volume is in the range of 1% to 80% of the total volume of the catalyst and packing bodies in the catalyst packed bed assembly.
Claim 11
Dependent Claim
30 words
A process according to claim 6, wherein the catalyst bodies each comprise the carrier, platinized carbon particles deposited on the carrier, and polytetrafluoroethylene bonding the platinized carbon to the carrier.