Methods and apparatus for controlling moisture in plant oils and liquid biofuels
View Patent ↗The moisture absorption capacity of biofuels can be more or less 10 times that of fossil diesel oil, causing biofuels to form acids that induce metal corrosion and form deposits in the fuel tank and pipe lines. Methods for removing moisture from stored biofuels and plant oils are described wherein glycerol is used as a solvent to extract the moisture from the bioliquid or oil, comprising the steps of placing the biofuel or oil in fluid contact with glycerol, incubating for a time, and then removing the glycerol. A cellulous ester dialysis or other semi-permeable membrane may be used to prevent the glycerol from contaminating the biofuel while allowing moisture to pass. Crude glycerol produced as a byproduct of biodiesel production may be used in the method of the disclosed invention with good result. Preferred embodiments of apparatus that employ the method of the subject invention are described.
1. A method for removing moisture from a plant oil or bioliquid, the method comprising the steps of:
placing the oil or bioliquid in fluid contact with glycerol through a semi-permeable membrane, said membrane permitting moisture to traverse from the oil or bioliquid into the glycerol, but preventing the bioliquid or oil and the glycerol from mixing; and
incubating the fluids for some period of time;
whereby the glycerol functions as a solvent to extract moisture from the plant oil or bioliquid.
2. The method according to claim 1 , wherein said semi-permeable membrane has a molecular weight cut-off smaller than the molecular weight of glycerol.
3. The method according to claim 1 , wherein the semi-permeable membrane is a cellulose ester dialysis membrane.
4. The method according to claim 3 , further comprising:
measuring the methanol content of the bioliquid or oil and the glycerol prior to contacting the one with the other; and
selecting bioliquid or oil and glycerol having a methanol content below that which causes damage to the cellulose ester dialysis membrane.
5. The method according to claim 1 , wherein the glycerol is a crude glycerol byproduct from biofuel production.
6. The method according to claim 1 , wherein the glycerol is acid-treated glycerol.
7. The method according to claim 1 , wherein the glycerol is pure glycerol.
8. The method according to claim 1 , wherein the percent proportion by weight of glycerol to bioliquid or oil ranges from 2% to 12% (w/w).
9. The method according to claim 1 , wherein the incubation period ranges from 3 hours to 24 hours.
10. The method according to claim 1 , further comprising the step of agitating the bioliquid or oil and/or the glycerol during the period of incubation.
11. A method for removing moisture from a bioliquid or oil, the method comprising:
providing a first container;
providing a smaller second container made from semi-permeable membrane, said membrane permitting moisture to traverse from the oil or bioliquid into the glycerol, but preventing the bioliquid or oil and the glycerol from mixing;
wherein said first container is filled with bioliquid or oil containing moisture and said second container is filled with glycerol;
introducing said second container into said first container for a period of incubation sufficient to permit moisture to cross the membrane to the glycerol; and
removing said second container from said first container.
12. The method according to claim 11 , wherein said second glycerol filled container is enclosed by a protective case.
13. The method according to claim 11 , further comprising agitating the first container is during the period of incubation.
14. The method according to claim 11 , wherein the semi-permeable membrane has a molecular weight cut-off smaller than the molecular weight of glycerol.
15. A method for removing moisture from a bioliquid or oil, the method comprising:
providing a first storage tank filled with bioliquid or oil;
providing a second storage tank filled with glycerol;
providing a membrane separator module having a first side and a second side, wherein said first side and said second side are separated by a semi-permeable membrane;
circulating the contents of the first storage tank through the first side of the membrane module;
placing the contents of the second storage tank in fluid contact with the second side of the membrane module and the semi-permeable membrane; and
circulating the contents of the first storage tank through the first side of the membrane separator, wherein said semi-permeable membrane permits moisture to traverse from the oil or bioliquid into the glycerol but prevents the bioliquid or oil and the glycerol from mixing, thereby reducing the moisture content of the bioliquid or oil.
16. The method of claim 15 , wherein the first storage tank comprises an inlet conduit, said conduit configured to transfer fluid from the first storage tank to an inlet of the first side of the membrane separator, and an outlet conduit, said conduit configured to transfer fluid from an outlet of the first side of the membrane separator back to the first storage tank, and a circulation pump integrated with either the inlet conduit or the outlet conduit.
17. The method of claim 16 , wherein the semi-permeable membrane has a molecular weight cut-off smaller than the molecular weight of glycerol.
18. The method of claim 1 , further comprising removing glycerol with the extracted moisture.