A gas chromatographic method for separating hydrogen isotopes

Abstract: The six isotopic species of hydrogen, H₂, D₂, T₂, HT, HD and DT, are separated from isotopic mixtures thereof with improved efficiency by low temperature gas column chromatography using a molecular sieve as the packing material, initially at a temperature of from -185°C to -160°C, but gradually increasing the column temperature at a rate of up to 10° per hour.

Description: The present invention relates to a method for separating the isotopic species of hydrogen on a moderately large scale using low temperature gas chromatography. The invention is addressed principally to those applications where a sufficient amount of material is not available to warrant a separation by cryogenic distillation. The invention may be used to separate and store all six dimeric isotope species of hydrogen, i.e. H₂, HD, HT, D₂, DT, T₂. The capacity or throughput possible by use of the present method is much greater than that previously available without sacrificing the high separation efficiency obtainable by gas chromatography. While cryogenic distiliation has been known and used for the purpose of separating isotopic mixtures of hydrogen, this technique is only suitable for use on a large scale. Distillation suffers from the disadvatages of providing a low separation efficiency as well as requiring the retention of a fairly large inventory of material in the distillation system. On the other hand, gas chromatography provides a high separation efficiency and leaves no inventory of desired material in the system, but generally, gas chromatography of hydrogen isotope mixtures has been utilized previously as an analytical tool. One approach for the development of a large scale gas chromatographic process for separating hydrogen isotopes has been taken by a group at Max Planck Institute in Germany, and is described in US-A-4469496 dated 4 September 1984. Essentially, the approach described in this patent involves increasing the diameter and length of the chromatography column and using up to 5% by volume of an inert fibrous filler material in the column packing. The patent states that separation efficiency is affected by factors such as column cross section, column length, carrier gas velocity, and column packing. However, according to the patent teachings, these various factors can be balanced or adjusted to give wholly satisfactory separations of hydrogen isotope mixtures of up to about 500 ml using a column having an internal diameter of 50 mm and length of 3 m. The Max Planck columns are packed with a pre-treated alumina powder. Separation times of 80 to 120 min were reported by them in Nuclear Tech/Fusion, 4, 687, 1983 for this system giving a throughput of 250 to 375 ml/h which may be written as 50 to 75 ml/h/1 cm column. In contrast with the foregoing, the present invention provides a method for chromatographically separating all six hydrogen isotope species at column throughputs of about 380 ml/h/1 cm column, or more than 5 times that of the Max Planck system. This is achieved by injecting a sample of the mixture to be separated at a first end of a column which is packed with a molecular sieve material, said column having an initial temperature of about -185°C to about -160°C; causing the injected sample to flow through the column by means of a pressurized stream of an invert gas while increasing the temparature of the column at a rate of up to about 10°C per hour up to a maximum column temperature of about -145°C, so that the various isotopic species contained in the sample are chromatographically separated from one another; and eluting the separated isotopic species from a second end of the column. The process of the present invention is described with reference to the accompanying drawings, in which: Figure 1 is a schematic diagram of a gas chromatographic system for use in accordance with the invention; Figure 2 is a schematic diagram of an experimental gas chromatographic system used to develop the data set out in the Examples; Figures 3a, b and c are schematic diagrams of the six-way valves used in the systems shown in Figures 1 and 2, showing the particular valving arrangements for various stages of the process; and Figure 4 is a more detailed schematic diagram of the column temperature control system used in carrying out the invention. Gas chromatographic separation of hydrogen isotopes has been reported in the literature dating from the late 1950's. Basically, three approaches have been employed to effect separations on an analytical scale, and these approaches may be distinguished on the basis of the column packing material used. It should be noted at the outset that the term "column" as used herein and as it is understood by those skilled in this art, means a tubular structure usually made of metal such as copper or stainless steel which is packed with a material for effecting a separation of gaseous components which are caused to flow therethrough by means of a carrier gas. Columns commonly used for gas chromatography are of a sufficient length that it is often inconvenient to deploy them in a linear fashion. Therefore, gas chromatography columns are frequently formed into spiral coils so that they may be conveniently stored and used, however, linear columns are within the scope of the invention. Three different column packing materials have been reported for the gas chromatographic separation of hydrogen isotopes. These are molecular sieves used for size exclusion chromatography, alumina used for gas/solid adsorption chromatography, and palladium such as palladium dispersed on alumina used for catalytic adsorption chromatography. Chromatographic separation of hydrogen isotopes on palladium has been reported for a mixture of H₂ and D₂ (C.O. Thomas and H.A. Smith, J. Phys. Chem., 63, p 427, 1959) using argon as the carrier gas. The separation was carried out in the temperature range 150 to 190°C, and the separation efficiency was reported to be poor. The efficient separation of hydrogen isotopes on alumina has been reported by a number of groups (e.g. J. King Jr. and S.W. Benson, J. Chem. Phys, 44, No 3, pp 1007-1014, 1966; H. Weichselgartner et al, Nuclear Tech/Fusion, 4, p 687, 1983; Frischmuth et al, US Patent No 4469496), and a pilot industrial scale system has been developed. Alumina used for chromatography is a synthetic polymeric material having a highly active surface. The activity of the alumina may be reduced by moisture and by the incorporation of trace amounts of iron or other metals into the alumina crystal structure. Highly activated alumina can completely adsorb hydrogen at sub-ambient temperatures. In the systems reported by the Max Planck group, helium was used as the carrier gas and the alumina packed column was maintained at -196°C with liquid nitrogen. The desirability of operating the column at any temperature other than -196°C is not suggested by the Max Planck group in their published reports. The separation efficiency was adjusted according to those reports by altering the activity of the alumina used and increasing or decreasing the length of the column. In contrast to the adsorption type of chromatography inherent in the use of alumina or palladium, chromatography on molecular sieves proceeds on the basis of molecular size. Molecular sieves are synthetic material usually prepared from sodium or calcium aluminum silicates and are commercially available in beads having pore sizes in the range of 3 to 10 angstroms. The pores in each bead form a network of interconnecting tunnels so that small molecules entering the pores may pass through the network more readily than larger molecules. Thus, a separation of molecular species is accomplished by a sieving effect whereby smaller molecules pass through the sieve faster than larger molecules. Elution is usaually in order of increaseing molecular size. Molecular sieves are used commonly in chromatographic applications to separate gases such as helium, hydrogen, argon, oxygen, nitrogen, methane and carbon monoxide. Water, carbon dioxide and hydrocarbons are highly retained by molecular sieves. Oxygen and nitrogen are completely retained by molecular sieves at -50°C and hydrogen is retained below -180°C. The separation of hydrogen isotopes on molecular sieves has been reported (S. Akthar and H.A. Smith, "Separation and Analysis of Various Forms of Hydrogen by Adsorption and Gas Chromatography", Chem. Rev., 64, pp 261-276, 1964; M.L. Conti and M. Lesimple, J. Chromatog., 19, pp 32-43, 1967). While there is no information on the relative capacities of alumina and molecular sieves for chromatographic separations, molecular sieves may be expected to have a greater capacity since the activity thereof is proportional to the volume of the chromatographic bed, whereas the activity of alumina is proportional to the surface area. The carrier gas for conducting the gas chromatographic separation of hydrogen isotope species on molecular sieves must not interact strongly with the column packing so as to adversely modify the retention of the analytes. This rules out argon which absorbs very strongly on molecular sieves at temperatures below -20°C, however helium or neon do not interact strongly with molecular sieves at temperatures as low as -180°C and therefore, may be used. A suitable carrier gas must also have a sufficiently high diffusion rate through the column packing so that the pressure drop across the column is low. This feature reduces the likelihood of leaks forming. Separation of the carrier gas from the separated components must be readily achievable, and the carrier gas must be compatible with the detector means used to monitor the effluent from the column. From a consideration of the foregoing criteria, helium is the preferred carrier gas for use in the invention. The chromatographic systems described in the literature use narrow bore analytical columns (2 mm ID) which provide optimum efficiency but minimum capacity (<1 mL. chromatographed). The ability of a column to separate components of a mixture is a measure of column efficiency. To be efficient, the gas components must have different affinities for the packing material and sufficient surface area of the packing material must be available to ensure that the gaseous components equilibrate with the surface all the way down the column. As the amount of gas injected onto the column is increased, equilibrium conditions eventually are not satisfied and the column loses efficiency. The point at which a significant loss in efficiency is detected is defined as the column capacity. The loss in column efficiency is manifested in band broadening, decreasing retention times, and changing peak shape. Column capacity depends on the choice of column packing material and the size of the chromatographic bed. When using the same column packing material, column capacity increases as the square of the column internal diameter. The group at the Max Planck Institute have chromatographed up to 600 mL of gas on 76.2 mm ID columns packed with alumina. Scaling up, however, results in a loss of resolution predicted in chromatography theory by the multi-path component of column efficiency. In accordance with the present invention, it has been found that the system shown in Figures 1 to 4 and described below may be used to effect a full separation of all six isotopic species of hydrogen using temperature programming on a single column. System Description A gas chromatography system includes a carrier gas supply, gas chromatography columns, a temperature controlled container for the columns, flow switching, gas detectors, and carrier gas/hydrogen isotope separation facilities. The experimental system used to generate the data presented below comprises the following components, and is generally shown in Figure 1. Carrier Gas Supply 1. Helium was the carrier gas and the system was designed for a flow rate of 0.5 to 2 L/min at a pressure of up to 800 kPa (90 psig). 2. Hydrogen isotope gas samples were injected in 2 L size from a pressurized container. The samples were injected as a pressure of 300 kPa (30 psig) up to 800 kPa (90 psig). 3. The hydrogen sample loop and associated valves were fully tritium compatible. GC Column 1 . The GC column had an internal diameter of 2 cm and a length of 7.5 m, and was in the form of a coil to minimize the space requirement. 2. The column was packed with 5A molecular sieve in the size range of 0.25 to 0.42 mm (40 to 60 mesh). Temperature Controlled Container 1. The container was sufficiently large for the column and a heating coil. 2. The container was vacuum jacketed for insulation (super insulated stainless steel dewar flask with flange top supplied by Minnesota Valley Engineering, Inc. suitable for this application). 3. The temperature of the container was maintained in the range of -140°C to -185°C by spraying liquid nitrogen into the container. The temperature was controlled to <±1°C of the set point in this temperature range. 4. The container was also heated to 300°C for 16 hours continuously for not more than once every three months. 5. A temperature controller to control the liquid nitrogen flow and the heater was used. Gas Detectors 1. A thermal conductivity detector with signal appropriate for operating relays and or motorized valves was used. 2. A flow proportional counting detector (β-detector) with signal appropriate for operating relays and or motorized valves was used. Automatic Flow Switching 1. Automatic on-off valve, two six-point valves, and one three-way valve were installed in the system. 2. Controllers to switch the automatic valves to divert the flow to appropriate downstream equipment were used. 3. Signals from the gas detectors were used to control the position of the valves. 4. The response of the valve switching to signal was less than one second. Carrier Gas/Hydrogen Isotope Separation 1. Uranium beds or cryogenic condensation units would be used to separate the carrier gas (helium) from the hydrogen isotopes. 2. Heaters installed in the uranium beds would be used to desorb the hydrogen isotopes from the bed when required. 3. The carrier gas separation system should be fully tritium compatible. System Operation The GC column was conditioned before it was used to separate hydrogen isotopes and re-conditioned every three to four months. The conditioning and normal operation of the column are discussed below. Conditioning of GC Column 1. A small flow of helium (e.g. 10 mL/min) was maintained through the column during conditioning. 2. The container was heated to 275°C gradually at a rate of 2 C/min and maintained at 275°C for 14 hours. Hydrogen Isotope Separation Operation 1. The system was purged with helium for at least ten volumes of the total system. 2. The temperature in the container was controlled to <±1°C of the desired temperature with liquid nitrogen spraying into the container. 3. The sample loop was pressurized to the desired pressure. 4. The sample was injected into the GC column by switching the six-way valve A automatically (Figure 1). 5. The flow from the downstream of the column was connected to the appropriate carrier gas/isotope separation unit by automatic valve switching according to the signal from the detectors. In the laboratory experiments conducted using this system, non-radioactive gases separated in the column were usually vented rather than captured in uranium beds or otherwise separated from the carrier gas. Of course, in a commercial system, the separated components would be recaptured as desired. Experimental A more detailed schematic diagram of the equipment used is shown in Figure 2. The system can be divided into five parts, namely, sample preparation, gas supply, column container, gas detection and data recording systems. In the sample preparation system, hydrogen isotope gas mixtures were prepared in a 1.7 L aluminum cylinder 11. The cylinder 11 was fitted with two entry ports 12 and 13 and a pressure gauge 14. One of the ports 13 was connected to a septum 15 and the other port 12 attached to either a vacuum pump or a high pressure gas cylinder 16. The sample cylinder 11 was evacuated to at least 10⁻² torr. Pure gas components were then introduced into the cylinder by syringes through the septum 15. After addition of appropriate amount of gas, the cylinder 11 was pressurized with either deuterium or hydrogen from the cylinder 16 up to 200 psig (1.38 MPa). After sample preparation, the cylinder 11 was connected to a six-way valve 20 to fill the sample loop 21 at the desired pressure to be injected to the gas chromatographic column. For experiments involving temperature programmed separation of all six isotopic species, the sample mixture comprised approximately 50% H₂ and 50% D₂ with 2.5 to 5.0 µCi/L T₂ with catalytic equilibration within the sample cylinder in the presence of a metal catalyst, so that all six dimeric isotope species were obtained. In addition to the hydrogen isotope gases supplied in the gas supply system, He, N₂, and P₁₀ (Ar and CH₄ mixture) gases are provided by high pressure gas cylinder. He was the carrier gas for the GC system, N₂ was used to pressurize the liquid nitrogen container 25, whereas the P₁₀ gas was used in the flow proportional counting detector 27. In the flow switching and column container system, the flow switching was carried out mainly by two six-way valves 20 and 30. A detailed flow diagram with the two valves 20 and 30 is shown in Figure 3. Each valve has only two positions allowing each of the six openings to be connected to an adjacent opening. Figure 3(a) shows the valve 20 position when the sample loop 21 was being filled with gas samples from the sample cylinder 11. In this position, the sample loop 21 was evacuated by closing the valve connected to the sample cylinder 11 and opening the valve to the vacuum pump. Then, the valve to the vacuum pump was closed and the valve connected to the sample cylinder 11 was opened to pressurize the sample loop 21 with the hydrogen isotope sample to the desired pressure. At this point in the description, it is to be acknowledged that the apparatus illustrated in Figures 1 to 4 was designed as a multipurpose apparatus, and not specifically for the purposes of the present invention. In particular, it was designed to evaluate a method of separating one or more isotopes of hydrogen from a mixture of such isotopes involving "peak-cutting" all enriched isotope-containing fraction from a first column for further concentration in a second column, that method being described in detail in EP-A-0245936 and from which the present application is divided. In that "peak-cutting" method, two separate chromatography columns are provided, both mounted in the container 40, and connected in series by the six-way valve 30. For the purposes of the present invention, however, only a single column was used, and the output from that column was passed directly to the isotope detector/collection systems by the valve 30, and not via a second column. Thus the positions of the valve 30 shown in Figure 3c does not apply to the present process, whilst in Figures 3a and 3b the outlet port from valve 30 was connected direct to the detectors rather than to a second column. After conditioning, the column was placed in a vacuum insulated container 40 as shown in Figure 4. The container was cooled by spraying liquid nitrogen into the container and the temperature was controlled by a temperature controller 42 which regulated the flow of liquid nitrogen via a solenoid valve 43. Liquid nitrogen was sprayed into the container near a small fan 44 located at the centre of the container 40. The fan 44 was surrounded by a stainless steel screen (not shown) to avoid direct contact of liquid nitrogen with the columns to ensure even temperature distribution in the columns. A vacuum of 10⁻³ torr was maintained between the inner and outer container during the experiment. The top of the container was insulated with a 3.8 cm layer of styrofoam insulation. Two detectors, namely a thermal conductivity detector 50 and a flow proportional counting detector 27, were used to detect the hydrogen isotope species. The thermal conductivity detector 50 detected H₂, HD and D₂ only, whereas the flow proportional counting detector 27 detected HT, DT and T₂ for all the experiments because of the very low concentration of the tritiated species. Signals from the two detectors were recorded by a dual pen recorder and integrated by two integrators. Experimental Procedure The experimental procedure was as follows. Cooling of the Column Container Liquid nitrogen was supplied by a 55 L container 25 connected to the solenoid valve 43 and the column container 40. The temperature controller 42 was then set to the desired temperature. It usually took 1.5 to 2 hours to cool the column container 40 from room temperature to -140°C to -180°C. Sample Loop Filling To fill the sample loop 21 with the hydrogen isotope mixture, the position of the six-way valve 20 was as shown in Figure 3(a). The sample loop was evacuated by opening the valve leading to the vacuum pump. After the sample loop 21 was evacuated, the valve to the vacuum pump was closed and the loop was filled with the gas sample to the desired pressure by opening the valve on the sample cylinder 11 connected to the six-way valve 20. Sample Injection to the Column To inject the sample in the sample loop, the six-way valve 20 was switched so that the carrier gas passed through the sample loop 21 and flushed the sample through the column. The column was cooled to as low as -186°C and the 2 L sample mixture was injected. The He carrier gas was maintained at a flow rate of 4 L/min at a pressure of about 300 kPa measured just upstream of the column. The column temperature was increased at a rate varying up to 10°C every 60 min to a final temperature near -150°C. Selected results for experiments giving similar isotope separations are summarized in Table 1 compared with the results obtained at a constant temperature of -166°C. At -166°C, separation of all components was completed in about 330 min. There was overlapping of some of the components at this temperature, hence the sample would have to he partially recycled. The net throughput was estimated to be about 270 mL/h or 135 mL/h/1 cm column. When temperature programming was applied, the elution time was reduced to as low as 130 min corresponding to a net throughput of about 770 mL/h or 380 mL/h/1 cm column, which is more than five times the reported throughput of 50 to 75 mL/h/1 cm column reported by the Max Planck group. Selected Experimental Results for the 2 cm 7.5 m Column With Similar Isotope Separation for a Hydrogen Sample of 2 L Initial Temp. °C Rate of Temp. Change °C/h Final Temp. °C Elution Time of H₂ - DT (min) Estimated Net Throughput (mL/h) -166 0 -166 330 270 -170 3 -155 170 600 -172 5 -152 130 770 -184 to -186 10 -154 >180 >570 These results indicate that separation of hydrogen isotope species using the temperature programming method of the invention enables one to obtain a much greater throughput for the separation of hydrogen isotopes than was previously thought possible. The invention provides a viable alternative to processing hydrogen isotope mixtures by cryogenic distillation. Isotope Storage The standard technique for dealing with separated hydrogen isotope species involves storage in a bed of a suitable powdered metal. Powdered uranium beds are commonly used in this regard, and the hydrogen species absorbed thereon are usually stored at room temperature. The ability to absorb hydrogen onto uranium powder also provides a means for separating the isotope species from the carrier gas which is not so absorbed. While this method of separation from the carrier gas and storage is suitable for H₂, D₂ or T₂ species, it will not allow the mixed dimers to maintain their integrity due to the catalytic effect provided by the metal absorbent. Thus, HD absorbed onto uranium quickly equilibrates to form a mixture of H₂, HD and D₂. In order to avoid this equilibration of mixed dimeric species, the present invention includes the step of separating and storing such mixed dimers at low temperature free of catalyzing metals. This feature of the invention takes advantage of the fact that hydrogen and its various isotopic species condense at about 20 K, while helium does not condense until about 4 K. Therefore, fractions eluted from the GC system in accordance with the invention may be separated from the helium carrier gas and captured for storage by cooling the effluent to abut 15 K. In particular, the mixed species, i.e. HD, DT and HT, may be captured and stored in pure form free from equilibration by using this technique.

Claims: A method of separating the isotopic species of hydrogen from a mixture thereof, which comprises injecting a volume of the isotopic mixture into a low temperature gas chromatography column containing a molecular sieve as a packing material therein, flowing that mixture through the column by means of a pressurised inert gas that is not strongly absorbed by the molecular sieve under the conditions of flow through the column, and eluting the separated isotopic species from the column, characterised in that the initial injection into the column is made with the column at a temperature in the range -185°C to -170°C, and that during the course of flow through the column, the column temperature is increased at a rate of up to about 10°C per hour up to a maximum column temperature of about -145°C. A method according to claim 1, wherein the molecular sieve used as packing in the column is a sodium or calcium aluminum silicate. A method according to claim 2, wherein the molecular sieve used as packing in the column is a type 5A material having a pore size of about 5 angstroms. A method according to claim 1, 2 or 3, wherein the molecular sieve used as packing in the column is in the form of beads having diameters in the range 0.25 to 0.42 mm. A method according to any one of claims 1 to 4, wherein the carrier gas is helium. A method according to any one of claims 1 to 5, wherein the carrier gas pressure is in the range 100 to 800 kPa. A method according to any one of claims 1 to 6, wherein following elution from the column, the separated isotopic species are separated from the carrier gas, in the case of the H₂, D₂ and T₂ species by absorption onto separate uranium beds, and in the case of the HD, HT and DT species by condensation from the carrier gas at about 15 K.

Inventors: CHEH CHRISTOPHER HUK-SHI, CHEH, CHRISTOPHER HUK-SHI, HAWTHORNE, SAMUEL HUGH, KVETON, OTTO KARL, MASSEY, RONALD ELLARD, SOOD, SAVTANTAR KUMAR
Applicants: CHEH CHRISTOPHER HUK SHI, CHEH, CHRISTOPHER HUK-SHI
Application year: 1991
Main classification: B01D59
IPC codes: G01N30, B01D59