Process for recovering useful products and energy from siliceous plant matter
View Patent ↗In the process disclosed herein, siliceous plant matter is steeped in water, soaked in an aqueous solution containing a solute which solubilizes inorganic oxides, soaked in an aqueous solution containing an oxidizing solute, rinsed, dried and thermally pyrolyzed to produce amorphous silica with of low carbon content, low water content, low inorganic impurity content and is of high porosity. Practice of the invention yields usable energy, does not produce carbonization of the atmosphere and is of lower nitrogen oxide and sulphur emission than currently used processes. Lignin, hemicellulose and cellulose derived sugars may be recovered from the steep or soak water. By varying steps of the process herein disclosed, the carbon content, inorganic impurities and porosity of the resulting amorphous silica may be selectively controlled.
1. A process for production of amorphous silica from siliceous plant matter containing water insoluble metallic compounds comprising the steps of:
soaking said siliceous plant matter in an aqueous solution comprising citric acid wherein said citric acid is present in an amount which solubilizes at least some of said water insoluble metallic compounds;
after said step of soaking said siliceous plant matter, separating the aqueous solution from said siliceous plant matter; and,
after said step of separating the aqueous solution from the siliceous plant matter, thermally pyrolyzing said siliceous plant matter in the presence of oxygen at a temperature wherein the resulting silica is comprised of silica of amorphous form.
2. The process of claim 1 further comprising the step of soaking the siliceous plant matter in an aqueous solution containing an oxidizing solute prior to the step of thermally pyrolyzing the siliceous plant matter in the presence of oxygen.
3. The process of claim 2 wherein the oxidizing solute is selected from the group consisting of peroxides, chlorates, perchlorates, nitrates and permanganates.
4. The process of claim 3 wherein the oxidizing solute is comprised of peracetic acid.
5. The process of claim 4 wherein the siliceous plant matter is pyrolyzed at a temperature in the range between 500° C. to 800° C.
6. The process of claim 2 wherein the siliceous plant matter is pyrolyzed at a temperature less than 950° C.
7. The process of claim 2 wherein the siliceous plant matter is pyrolyzed at a temperature less than 1000° C.
8. The process of claim 2 wherein the siliceous plant matter is pyrolyzed at a temperature less than 1600° C.
9. The process of claim 3 wherein the siliceous plant matter is pyrolyzed at a temperature in the range between 500° C. to 800° C.
10. The process of claim 3 wherein the siliceous plant matter is pyrolyzed at a temperature less than 950° C.
11. The process of claim 3 wherein the siliceous plant matter is pyrolyzed at a temperature less than 1000° C.
12. The process of claim 3 wherein the siliceous plant matter is pyrolyzed at a temperature less than 1600° C.
13. The process of claim 1 wherein the siliceous plant matter is pyrolyzed at a temperature in the range between 500° C. to 800° C.
14. The process of claim 1 wherein the siliceous plant matter is pyrolyzed at a temperature less than 950° C.
15. The process of claim 1 wherein the siliceous plant matter is pyrolyzed at a temperature less than 1000° C.
16. The process of claim 1 wherein the siliceous plant matter is pyrolyzed at a temperature less than 1600° C.
17. The process of claim 4 wherein the siliceous plant matter is pyrolyzed at a temperature in the range between 500° C. to 800° C.
18. The process of claim 4 wherein the siliceous plant matter is pyrolyzed at a temperature less than 950° C.
19. The process of claim 4 wherein the siliceous plant matter is pyrolyzed at a temperature less than 1000° C.
20. The process of claim 4 wherein the siliceous plant matter is pyrolyzed at a temperature less than 1600° C.