IP Library Granted Patent US 7,828,939
Granted Patent B2
US 7,828,939 · App. 12/293,361 · Granted Nov 9, 2010

Method for concentrating heavy nitrogen isotope

Assignee: Taiyo Nippon Sanso Corporation
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Quick Facts
Patent No.
US 7,828,939
App. No.
12/293,361
Granted
Nov 9, 2010
Kind
B2
Abstract

A method for concentrating effectively the heavy nitrogen isotope 15 N to 50 atom % or more in which 14 N 15 N and/or 15 N 2 , which are molecules containing a heavy nitrogen isotope of 15 N, are concentrated by distilling successively nitrogen N 2 using plural distillation columns T 1 to T 4 each of which includes at least one condenser C 1 to C 4 and at least one reboiler R 1 to R 4 and is arranged in series, and a part of nitrogen in the distillation is drawn out to be subjected to isotope scrambling in an isotope scrambler S 1 , and nitrogen after the isotope scrambling is returned to the distillation to produce nitrogen N 2 with a 15 N concentration of 50 atom % or more.

Claims (15)

1. A method for concentrating a heavy nitrogen isotope 15 N in which 14 N 15 N and/or 15 N 2 , which are molecules containing a heavy nitrogen isotope of 15 N, are concentrated, wherein the method comprises:

distilling successively raw material nitrogen N 2 using plural distillation columns each of which comprises a condenser and a reboiler and is arranged in series, and a part of nitrogen in the distillation is drawn out to be subjected to isotope scrambling, and nitrogen after the isotope scrambling is returned to the distillation to produce nitrogen N 2 with a 15 N concentration of 50 atom % or more,

wherein supplying N 2 from a certain distillation column other than a final distillation column to another distillation column which is the next stage is performed using a pressure difference between the two distillation columns as driving force, and N 2 is present from a distillation column other than a first column to another distillation column of a former stage using a liquid head pressure of nitrogen as a driving force, and

wherein a cooling fluid used in the condenser is nitrogen N 2 which is other than nitrogen N 2 to be distilled in the distillation step to control the pressure at the top of the distillation column provided with the condenser, and a pressure difference which is a driving force to supply N 2 to the distillation column is obtained.

2. A method for concentrating a heavy nitrogen isotope according to claim 1 , wherein argon and/or oxygen are present in the raw material nitrogen in the plural distillation columns in an amount of 10 ppm or less.

3. A method for concentrating a heavy nitrogen isotope according to claim 1 , wherein a gas or liquid containing nitrogen having a concentration of 3 mol % or less and concentrated argon and/or oxygen is discharged from the bottom portion of the final column, and a product containing concentrated 15 N is obtained from the portion 2 to 10 m above the bottom of the final distillation column.

4. A method for concentrating a heavy nitrogen isotope according to claim 3 , wherein the flow rate of a gas or liquid discharged from a bottom portion of the final distillation column is adjusted to 80% to 100% relative to 100% of a total amount of the argon and oxygen contained in the raw material nitrogen.

5. A method for concentrating a heavy nitrogen isotope 15 N in which 14 N 15 N and/or 15 N 2 , which are molecules containing a heavy nitrogen isotope of 15 N, are concentrated, wherein the method comprises:

distilling successively raw material nitrogen N 2 using plural distillation columns each of which comprises a condenser and a reboiler and is arranged in series, and a part of nitrogen in the distillation is drawn out to be subjected to isotope scrambling, and nitrogen after the isotope scrambling is returned to the distillation to produce nitrogen N 2 with a 15 N concentration of 50 atom % or more,

wherein supplying N 2 from a certain distillation column other than a final distillation column to another distillation column which is the next stage is performed using a pressure difference between the two distillation columns as driving force, and N 2 is present from a distillation column other than a first column to another distillation column of a former stage using a liquid head pressure of nitrogen as a driving force, and

wherein a pipe for resending nitrogen N 2 from a distillation column to the former distillation column is cooled with liquid nitrogen which is other than the nitrogen in the distillation.

6. A method for concentrating a heavy nitrogen isotope according to claim 5 , wherein a cooling fluid used in a condenser is used to cool the pipe.

7. A method for concentrating a heavy nitrogen isotope according to claim 5 , wherein argon and/or oxygen are present in the raw material nitrogen in the plural distillation columns in an amount of 10 ppm or less.

8. A method for concentrating a heavy nitrogen isotope according to claim 5 , wherein a gas or liquid containing nitrogen having the concentration of 3 mol % or less and concentrated argon and/or oxygen is discharged from the bottom portion of the final distillation column, and a product containing concentrated 15 N is obtained from the portion 2 to 10 m above the bottom of the final distillation column.

9. A method for concentrating a heavy nitrogen isotope according to claim 8 , wherein the flow rate of the gas or liquid discharged from the bottom portion of the final distillation column is adjusted to 80% to 100% relative to 100% of a total amount of the argon and oxygen contained in the raw material nitrogen.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 17, 2008
From: KIHARA, HITOSHI; KAMBE, TAKASHI; HAYASHIDA, SHIGERU
To: TAIYO NIPPON SANSO CORPORATION
Reel/Frame 021544/0167 →
Priority Claims (1)
JP P2006-080345 · Mar 23, 2006 · national
Continuity (1)
Related Publication 20090071814A1 · Mar 19, 2009