GB1273463A - Deuterium-hydrogen exchange using diamines - Google Patents
Deuterium-hydrogen exchange using diaminesInfo
- Publication number
- GB1273463A GB1273463A GB1392870A GB1392870A GB1273463A GB 1273463 A GB1273463 A GB 1273463A GB 1392870 A GB1392870 A GB 1392870A GB 1392870 A GB1392870 A GB 1392870A GB 1273463 A GB1273463 A GB 1273463A
- Authority
- GB
- United Kingdom
- Prior art keywords
- stream
- exchange
- tower
- exchange liquid
- deuterium
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B4/00—Hydrogen isotopes; Inorganic compounds thereof prepared by isotope exchange, e.g. NH3 + D2 → NH2D + HD
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Inorganic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
1,273,463. Deuteration of amines. ATOMIC ENERGY OF CANADA Ltd. 23 March, 1970 [8 April, 1969], No. 13928/70. Heading C2C. [Also in Division Cl] A mono- or bi-thermal process of concentrating deuterium in a gaseous, hydrogen containing stream, e.g. ammonia synthesis gas, comprises passing the stream through an exchange liquid comprising a diamine having up to five carbon atoms per molecule, e.g. 1,2-diaminoethane, 1,2- diaminopropane or 1,3-diaminopropane, or a mixture of the diamine with a liquid selected from the group consisting of another similar diamine, a monoamine and ammonia. The exchange liquid may contain a catalyst e.g. an alkyl amide of lithium, sodium, potassium, rubidium or cesium. In the bi-thermal process shown in Fig. 1 a stream 1 of nitrogen and hydrogen and a stream 2 of exchange liquid countercurrently engage in upper cold tower Cu where deuterium passes to the exchange liquid. A portion 1a of the emergent gaseous stream passes to an ammonia synthesis plant, whereas a portion 1b is fed upwardly through hot tower H and lower cold tower C L before joining the feed stream 1. In the lower cold tower C L deuterium passes from the gaseous stream 1c to the exchange liquid 2a whereas in the hot tower H deuterium passes from the exchange liquid 2b to the gaseous stream 1b Streams 1d and 2d of gas and exchange liquid respectively are taken off from points of highest deuterium concentration. In the monothermal process shown in Fig. 2, ammonia synthesis gas stream 12 passes from exchange tower T to synthesis plant S. A portion of the ammonia product 13 is taken off in stream 14 which then passes upwardly through exchange tower E. The emergent ammonia stream 14a is then cracked at stage C and returned to the exchange tower T. A stream 16a of exchange liquid cycles between the two exchange towers. Deuterium transfers from the synthesis gas to the exchange liquid in the tower T, and from the exchange liquid to the ammonia gas stream 14 in the exchange tower E. Portions 14b and 16b of the gas and exchange liquid are withdrawn.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA48002 | 1969-04-08 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1273463A true GB1273463A (en) | 1972-05-10 |
Family
ID=4085113
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1392870A Expired GB1273463A (en) | 1969-04-08 | 1970-03-23 | Deuterium-hydrogen exchange using diamines |
Country Status (6)
Country | Link |
---|---|
JP (1) | JPS4918554B1 (en) |
AU (1) | AU1326570A (en) |
CA (1) | CA901266A (en) |
DE (1) | DE2016770A1 (en) |
FR (1) | FR2042984A5 (en) |
GB (1) | GB1273463A (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA1014333A (en) | 1973-07-31 | 1977-07-26 | William J. Holtslander | Catalyst for hydrogen-amine d exchange |
CA1040218A (en) * | 1975-11-14 | 1978-10-10 | Raymond U. Lemieux | Precipitation prevention in amine-hydrogen d-h exchange |
DE3202776A1 (en) * | 1982-01-28 | 1983-08-04 | Kernforschungszentrum Karlsruhe Gmbh, 7500 Karlsruhe | METHOD FOR ENRICHING AND SEPARATING HEAVY HYDROGEN ISOTOPES FROM THESE FLUIDS CONTAINING THROUGH ISOTOPE EXCHANGE |
-
1969
- 1969-04-08 CA CA901266D patent/CA901266A/en not_active Expired
-
1970
- 1970-03-23 GB GB1392870A patent/GB1273463A/en not_active Expired
- 1970-04-01 AU AU13265/70A patent/AU1326570A/en not_active Expired
- 1970-04-06 FR FR7012376A patent/FR2042984A5/fr not_active Expired
- 1970-04-07 JP JP2910770A patent/JPS4918554B1/ja active Pending
- 1970-04-08 DE DE19702016770 patent/DE2016770A1/en active Pending
Also Published As
Publication number | Publication date |
---|---|
JPS4918554B1 (en) | 1974-05-10 |
FR2042984A5 (en) | 1971-02-12 |
AU1326570A (en) | 1971-10-07 |
CA901266A (en) | 1972-05-30 |
DE2016770A1 (en) | 1970-10-15 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
PLNP | Patent lapsed through nonpayment of renewal fees |