Claims
- 1. A process for producing a compost which comprises grounding municipal waste, magnetically freeing from iron contained therein, separating said mixture into components of various sizes by fractionation and, treating said mixture in a tank in a fermentation process at a temperature of about 65.degree. C. by continuously passing air thereto and mixing a solvent with said mixture and heating said tank until the contents of the tank are dried, thereby forming a compost.
- 2. The process of claim 1 wherein the municipal waste is comprised of:
- ______________________________________ % by weight______________________________________water about 30 to about 50%organic sub-stances about 20 to about 40%phosphorous about 0.3 to about 0.9%nitrogen about 0.3 to about 0.9%potassium about 0.3 to about 0.6%magnesium about 0.3 to about 0.9%calcium about 0.6 to about 6.0%______________________________________
- 3. The process of claim 2 wherein the solvent: waste is mixed in a ratio of about 1:2 to about 4 parts by weight waste:solvent.
- 4. The process of claim 1 further comprising mixing the dry compost with synthetic resin.
- 5. The process of claim 1 wherein the solvent is selected from the group consisting of chlorinated aliphatic solvents of from one to four carbon atoms, aliphatic ketones of from one to five carbon atoms, aliphatic ethers, aromatic hydrocarbons, aliphatic alcohols of from one to six carbon atoms, aliphatic esters, styrene, hydrogen peroxide and mixtures thereof.
- 6. The process of claim 1 further comprising mixing the compost with a curing synthetic resin, castor oil, glycerol, cobalt salt solution, curing agent and accelerator.
- 7. The process of claim 6 wherein polyester resin is the synthetic resin, benzoyl peroxide is the curing agent, and dimethyl aniline is the accelerator.
- 8. A process for producing non-combustible compost useful as stone material for the building of reservoirs and port installations according to the process of claim 1 further comprising mixing together 500 parts by weight of compost, approximately 100 parts by weight quartz powder, approximately 300 parts by weight polyester resin as a plasticizer, approximately 20 parts by weight pine or spruce needle extract in a 20% alcohol solution, as a hardener, approximately 40 parts by weight benzoyl peroxide with traces of aluminum powder as an accelerator, approximately 10 parts by weight dimethyl aniline, approximately 2.5 parts by weight castor oil, approximately 1.5 parts by weight glycerine, approximately 1.6 parts by weight liquid paraffin with a boiling point of 52.degree.-56.degree. C. and approximately 2 parts by weight 10% cobalt octoate solution in styrol.
- 9. The process of claim 1 wherein before treating said mixture in a fermentation process sewage sludge or water is added and the treatment at a temperature of about 65.degree. C. is for about 24 hours.
- 10. The process of claim 1 wherein the dried compost is introduced in a second tank in which it is mixed with 2-3% by weight of chloroparaffin solution and 1-3% by weight of antimony (III) oxide while being stirred and further heated to renewed dryness.
- 11. A process for producing a compost characterized by being non-combustible fiberous materials according to the process of claim 1 wherein the solvent is a solvent for fats, waxes and oils and said solvent:waste mixture is dried to a first residue;
- forming a second mixture of solvent and said first residue;
- adding materials selected from the group consisting of aluminum powder, copper powder, silver-, gold- and brass-bronzes, amorphous forms of silicon compounds, calcium carbonate, barium compounds, organic and inorganic pigments, chlorinated hydrocarbons, or mixtures thereof; and
- drying said product to produce a second residue.
- 12. The process of claim 11 further comprising adding a 3% chloro-paraffin emulsion based on the weight of the solvent therefore, to the dried second residue.
- 13. The process of claim 11 wherein the second residue solvent mixture is comprised of 3 kg of carbon tetrachloride mixed with 0.01-0.02% by weight of aluminum powder wherein the waste:solvent is mixed in a ratio of about 1:2 to about four parts by weight waste:solvent.
- 14. The process of claim 11 wherein the second residue solvent mixture is comprised of a mixture of 3 kg of carbon tetrachloride mixed with 0.3% by weight of carbon black wherein the waste:solvent is mixed in a ratio of about 1:2 to about four parts by weight waste:solvent.
- 15. The process of claim 11 wherein the second residue solvent mixture is comprised of a mixture of 3 kg styrene mixed with 1% by weight of barium sulfate wherein the waste:solvent is mixed in a ratio of about 1:2 to about four parts by weight waste:solvent.
Priority Claims (4)
Number |
Date |
Country |
Kind |
2407383 |
Feb 1974 |
DE |
|
2432606 |
Jul 1974 |
DE |
|
2434487 |
Jul 1974 |
DE |
|
2515179 |
Apr 1975 |
DE |
|
CROSS REFERENCE TO RELATED CASES
This case is a continuation in part of: U.S. Ser. No. 550,585, filed Feb. 18, 1975 now U.S. Pat No. 4,012,231, U.S. Ser. No. 593,386, filed July 7, 1975, now abandoned, U.S. Ser. No. 597,120, filed July 18, 1975, now abandoned, and U.S. Ser. No. 674,431, filed Apr. 7, 1976, now abandoned, all of which are hereby incorporated by reference.
US Referenced Citations (23)
Foreign Referenced Citations (2)
Number |
Date |
Country |
2001583 |
Jan 1970 |
DE |
1405587 |
Sep 1975 |
GB |
Continuation in Parts (1)
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Number |
Date |
Country |
Parent |
674431 |
Apr 1976 |
|