Process for cryogenic fluid odorisation
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.
1. A process for odorizing a cryogenic fluid in a liquid state, comprising at least the following steps:
a) 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,
b) feeding said odorizing agent in liquid or gaseous form from step a) into a buffer zone in which the odorizing agent is brought to a temperature of about the temperature of the cryogenic fluid, and
c) feeding said odorizing agent cooled in step b) into the contact zone at a temperature lower than the crystallization temperature of said odorizing agent causing said odorizing agent to solidify, wherein said odorizing agent in a solid form then comes into contact with said cryogenic fluid to be odorized.
2. The process 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.
3. The process as claimed in claim 1 , wherein the odorizing agent is brought, in step b), to a temperature less than 30° C. above the temperature of the cryogenic fluid to be odorized.
4. The process 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).
5. The process as claimed in claim 1 , wherein the odorizing agent is chosen from terpenes, alcohols, phenols, aldehydes, ethers, esters, fatty acids, ketones, lactones and nitriles, pyrazine compounds, mercaptans, cyclic sulfides, dialkyl sulfides, dialkyl disulfides, or else from selenium derivatives, alone or in mixtures of two or more, in any proportions.
6. The process as claimed in claim 1 , wherein the odorizing agent is chosen 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.
7. The process as claimed in claim 1 , wherein the odorizing agent is used pure, mixed or diluted with other compounds compatible with the cryogenic fluid.
8. The process as claimed in claim 1 , wherein the odorizing agent also comprises one or more additives chosen from heat stabilizers, dyes and antioxidants.
9. The process as claimed in claim 1 , wherein the cryogenic fluid is Liquefied Natural Gas.
10. The process as claimed in claim 1 , wherein the odorizing agent is injected in the form of a spray in step a).
11. The process as claimed in claim 1 , wherein the arrival in the buffer zone b) of the odorizing agent is carried out by means of at least one or more elements chosen from a cannula, a nozzle, an injector or any other means for drip or spray feeding; it being possible for said abovementioned elements to be used alone or in a combination of one or more of them.