Mechanically enhanced separation of reaction products in biodiesel production
Abstract
Apparatus and related methods for reacting a natural oil with a short chain alcohol in the presence of an alkaline catalyst and mesh to produce biodiesel, significantly decreasing the amount of time for the glycerol byproduct to settle out of the reaction mixture. The process for the production of biodiesel includes providing animal or vegetable oil to create a first component, combining a short chain alcohol with a strong base to create a second component, and combining the first and second components together in the presence of a mesh, such that the mesh is in contact with the combined components. The combined compositions represent a reaction mixture that undergo a transesterification reaction and produce fatty acid methyl ester biodiesel and also a glycerol byproduct. The mesh material that is present during the transesterification reaction decreases the amount of time required for the glycerol byproduct to settle out of the reaction mixture.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1 . A process for the production of biodiesel, comprising the steps of:
creating a first component using animal or vegetable oil; combining a short chain alcohol with a strong base to create a second component; and combining said first and second components together in the presence of a moveable mesh, such that the mesh is in contact with the combined first and second components.
2 . The process of claim 1 , wherein the short chain alcohol is methanol or ethanol.
3 . The process of claim 1 , wherein the strong base is sodium hydroxide or potassium hydroxide.
4 . The process of claim 1 , wherein the mesh comprises a metal.
5 . The process of claim 1 , wherein the mesh comprises nickel.
6 . The process of claim 1 , wherein the mesh comprises a polymer or a plastic.
7 . The process of claim 1 , wherein the mesh comprises both a metal and a plastic.
8 . The process of claim 1 , wherein the first and second components are each heated to a range of about 50° C. to about 55° C. before being combined.
9 . The process of claim 1 , wherein the first and second components are each heated to a range of about 45° C. to about 60° C. before being combined.
10 . The process of claim 1 , wherein the first and second components are each heated to a range of about 40° C. to about 65° C. before being combined.
11 . The process of claim 1 , wherein after the first and second components are combined, said combination is heated to a range of about 50° C. to about 60° C., and the temperature is maintained in said range for a duration of about 30 minutes to about 90 minutes.
12 . The process of claim 1 , wherein after the first and second components are combined, said combination is heated to a range of about 30° C. to about 70° C., and the temperature is maintained in said range for a duration of about 30 minutes to about 120 minutes.Cited by (0)
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