Method for making a usable hydrocarbon product from used oil
One or more computer implemented methods for continuously processing used oils are provided. The method can include a feedstock tank containing feedstock. The feedstock tank can have a sparger and a level sensor. The feedstock tank can be in fluid communication with a first pump, a first filter, a heater, a second filter, first flow meter, a primary nozzle, a secondary nozzle, a motionless inline static mixer, and a first reactor.
1. A computer implemented method for processing used oils for a usable hydrocarbon product comprising:
a. providing a feedstock stream;
b. filtering the feedstock stream;
c. heating the feedstock stream;
d. filtering the heated feedstock stream;
e. monitoring a flow rate of the feedstock stream;
f. injecting an aqueous sulfuric acid into the heated feedstock stream;
g. injecting a concentrated sulfuric acid into the heated feedstock stream;
h. blending the aqueous sulfuric acid, concentrated sulfuric acid, and the heated feedstock stream to form a mixed stream;
i. separating the mixed stream into a first interface layer, an intermediate oil product, and a water layer;
j. injecting an aromatic solvent release agent into the intermediate oil product,
k. mixing the intermediate oil product and the aromatic solvent release agent to form a blended intermediate oil product;
l. separating the blended intermediate oil product into a finished oil product, a second interface layer, and a second water layer; and
m. pumping the finished oil product to a first settling tank and allowing any remaining particulate to fall out of solution to form a finished product.
2. The method of claim 1 , further comprising using a heater to heat the feedstock stream.
3. The method of claim 2 , further comprising using steam to heat the heater.
4. The method of claim 1 , further comprising using at least a two stage filter to filter the feedstock stream, wherein each stage is at least a four hundred micron filter.
5. The method of claim 1 , wherein the heated feedstock stream is filtered using a one hundred micron filter.
6. The method of claim 1 , wherein the aqueous sulfuric acid, the concentrated sulfuric acid, or both is injected at a ratio from two gallons per one thousand gallons of feedstock to four gallons per one thousand gallons of feedstock.
7. The method of claim 1 , wherein the first interface layer includes at least fifty percent hydrocarbons.
8. The method of claim 1 , wherein the aromatic solvent release agent is injected at a ratio of from four gallons per one thousand gallons of feedstock to seven gallons per one thousand gallons of feedstock.