Method of odorizing liquid natural gas

• US 4,025,315 A
• Filed: 05/19/1971
• Issued: 05/24/1977
• Est. Priority Date: 05/19/1971
• Status: Expired due to Term

• Current Assignee: DUAL Fuel Systems Incorporated, San Diego Gas & Electric Company (Sempra Energy)
• Original Assignee: DUAL Fuel Systems Incorporated, San Diego Gas & Electric Company (Sempra Energy)
• Inventors: Mazelli, Jack R.
• Primary Examiner(s): Scovronek, Joseph
• Application Number:
  US05/144,796
• Time in Patent Office: 2,197 Days
• Field of Search: 48/195, 48/196 FM, 48/196 R, 48/196 US, 44/52, 44/59, 261/DIG. 17, 252/408
• US Class Current: 44/435
• CPC Class Codes: B01F 23/40 Mixing liquids with liquids; Emulsifying
• CPC Class Codes: B01F 23/481 using liquefied or cryogenic gases
• CPC Class Codes: C10L 3/006 detectable by the senses
• CPC Class Codes: Y10S 261/17 Odorizers

Abstract

Liquid natural gas is odorized with either ethyl or methyl mercaptan by initiallly mixing the odorant with a diluent and then introducing the resultant mixture into the liquid natural gas. It is preferred that the diluent have a freezing point below the boiling point of liquid natural gas. It is theorized that with the diluent the mercaptans either do not freeze or are dispersed sufficiently in the liquid natural gas to reduce the particle size of frozen odorant. In any event, the result is effective odorization of natural gas drawn from a liquid natural gas storage tank regardless of the amount of liquid and gaseous natural gas left in the tank.

Claims

1. A method of odorizing cryogenic liquid natural gas comprising the steps of:

(a) forming a mixture of a diluent and an odorant selected from the class of odorants consisting of ethyl mercaptan and methyl mercaptan, the diluent having a freezing point at atmospheric pressure below the boiling point of liquid natural gas at that pressure; and

(b) introducing the mixture in an odorant effective amount into the liquid natural gas.

2. The method claimed in claim 1 wherein the diluent is liquid propane.

3. The method claimed in claim 2 wherein the odorant is ethyl mercaptan and the mixture includes up to about ten percent by volume ethyl mercaptan.

4. The method claimed in claim 2 wherein the introduction step includes forcing the mixture from storage into the liquid natural gas with gaseous natural gas under pressure.

5. The method claimed in claim 4 wherein the liquid natural gas is being charged into a vessel during the introduction of the mixture.

6. The method claimed in claim 5 wherein the mixture is in a storage vessel prior to its introduction into the liquid natural gas vessel, the mixture is introduced into the liquid natural gas vessel through at least one line and the line is purged with natural gas discharged into the liquid natural gas vessel after the purge.

7. The method claimed in claim 1 wherein the diluent and odorant are mixed with sufficient diluent to prevent any substantial precipitation of odorant after the mixture is introduced into the liquid natural gas.

8. The method claimed in claim 2 wherein the introduction step includes forcing the mixture into the liquid natural gas by pressure.

9. The method claimed in claim 8 wherein the liquid natural gas is agitated during the introduction of the mixture to disperse the odorant.

10. The method claimed in claim 9 wherein the pressure forcing is by natural gas under pressure.

11. The method claimed in claim 1 wherein the diluent is methane gas and the introduction step includes forcing the mixture into the liquid natural gas by pressure.

12. The method claimed in claim 11 wherein the liquid natural gas is agitated during the introduction of the mixture to disperse the odorant.

13. The method claimed in claim 11 wherein the pressure forcing is by natural gas under pressure.

14. A method for providing cryogenic liquefied natural gas with sufficient soluble levels of a mercaptan odorant selected from the class consisting of ethyl mercaptan and methyl mercaptan, including

dissolving said odorant in a liquefied hydrocarbon gas carrier, said carrier being miscible with the cryogenic liquefied gas, said carrier having a boiling point which is higher than that of the cryogenic liquefied gas, said odorant being dissolved in said carrier at concentrations greater than could be dissolved in the cryogenic liquefied gas, and

combining said cryogenic liquefied gas and minor volumes of said carrier with dissolved odorant so that said cryogenic liquefied gas component of said mixture contains detectable concentrations of odorants.

15. A method which includes the steps of claim 14 wherein said carrier is a liquefied lower alkane hydrocarbon.