Process for cryogenic fluid odorisation
US-2022220402-A1 · Jul 14, 2022 · US
US11814596B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11814596-B2 |
| Application number | US-202217681102-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 25, 2022 |
| Priority date | Apr 25, 2017 |
| Publication date | Nov 14, 2023 |
| Grant date | Nov 14, 2023 |
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The present invention relates to a process for odorizing a cryogenic fluid, comprising a step a) of continuously feeding an odorizing agent in liquid or gaseous form into a feed zone, said feeding being carried out at a temperature above the temperature of the cryogenic fluid and above the crystallization temperature of the odorizing agent, a step b) of feeding said odorizing agent in liquid or gaseous form from step a) into a buffer zone in which the liquid or gaseous odorizing agent is brought to a temperature of about the temperature of the cryogenic fluid, and a step c) of feeding said odorizing agent cooled in step b) into the contact zone, wherein said odorizing agent comes into contact with said cryogenic fluid to be odorized. The present invention also relates to an odorizing device for implementing said odorizing process.
Opening claim text (preview).
The invention claimed is: 1. A device configured for introducing an odorizing agent in a solid form into a cryogenic fluid which is in a liquid state, the device comprising: a feed zone, where an odorizing agent in liquid or gaseous form is introduced, the feed zone containing a means for drip or spray feeding the odorizing agent to a buffer zone, the buffer zone, where the liquid or gaseous odorizing agent is brought to a temperature less than 30° C. above the temperature of the cryogenic fluid, and a contact zone at a temperature lower than the crystallization temperature of the odorizing agent, where the odorizing agent in a solid form comes into contact with the liquid cryogenic fluid to be odorized. 2. The device as claimed in claim 1 , wherein the buffer zone is equipped with mechanical assistance. 3. The device as claimed in claim 1 , wherein the odorizing agent arrives in the buffer zone from the feed zone with a carrier gas and/or with a portion of the cryogenic fluid to be odorized, or by a combination thereof. 4. The device as claimed in claim 1 , wherein the feed zone and/or the buffer zone is/are equipped with a means for maintaining the temperature of the odorizing agent above its crystallization temperature. 5. The device as claimed in claim 4 , wherein the means for maintaining the temperature is vacuum insulation, circulation of a gas where the boiling point of the gas is lower than or equal to the temperature of the cryogenic fluid, reheating the feed zone with a heat-transfer fluid, reheating by means of a heating resistor by induction or conduction, or a combination thereof. 6. The device as claimed in claim 1 , wherein the concentration of odorizing agent in the cryogenic fluid is between 0.1 mg/m 3 (n) and 500 mg/m 3 (n). 7. The device as claimed in claim 1 , wherein the odorizing agent is selected from methyl ethyl sulfide, dimethyl sulfide, diethyl sulfide, dimethyl disulfide, diethyl disulfide, methyl mercaptan, ethyl mercaptan, tert-butyl mercaptan, sec-butyl mercaptan, iso-propyl mercaptan, n-propyl mercaptan, cyclohexyl mercaptan, tetrahydrothiophene, methyl acrylate, ethyl acrylate, methyl methacrylate, ethyl methacrylate, methylethylpyrazine, dimethyl selenide and dimethyl diselenide. 8. The device as claimed in claim 1 , wherein the odorizing agent is used pure, mixed or diluted with other compounds compatible with the cryogenic fluid. 9. The device as claimed in claim 1 , wherein the odorizing agent further comprises one or more additives selected from heat stabilizers, dyes and antioxidants. 10. The device as claimed in claim 1 , wherein the cryogenic fluid is liquefied natural gas. 11. The device as claimed in claim 1 , wherein the odorizing agent is fed continuously in the feed zone. 12. The device as claimed in claim 1 , wherein the flow rate of odorizing agent in the contact zone is proportional to the flow rate of the cryogenic fluid. 13. The device as claimed in claim 1 , wherein the means for drip or spray feeding comprises one or more of a cannula, a nozzle and an injector.
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