Method for recycling waste material with reduced odor emission
US-2015299950-A1 · Oct 22, 2015 · US
US9353476B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9353476-B2 |
| Application number | US-201414256652-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 18, 2014 |
| Priority date | Apr 18, 2014 |
| Publication date | May 31, 2016 |
| Grant date | May 31, 2016 |
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A method for recycling waste material including waste paper comprises the steps of introducing the waste material into a pressure vessel, re-pulping the waste paper in the pressure vessel at an elevated processing temperature and pressure to form a treated waste material including substantially re-pulped waste paper, thereafter introducing cooling water into the pressure vessel so as to cool the treated waste material in the pressure vessel to a discharge temperature below the elevated processing temperature and reduce odor emitted by the treated waste material, and thereafter discharging the treated waste material from the pressure vessel. The recovered paper pulp fraction is suitable as a feedstock in the manufacture of a variety of paper products including paper tissue and paper towel products.
Opening claim text (preview).
We claim: 1. A method for treating waste material including waste paper comprising the steps of: introducing the waste material and dilution water into a pressure vessel; treating the waste material in the pressure vessel at an elevated processing temperature of at least about 212° F. and an elevated processing pressure greater than atmospheric pressure to form a treated waste material including substantially re-pulped waste paper; thereafter introducing cooling water into the pressure vessel so as to cool the treated waste material in the pressure vessel to a discharge temperature less than about 140° F. and reduce odor emitted by the treated waste material; and thereafter discharging the treated waste material from the pressure vessel, wherein the dilution water is introduced into the pressure vessel in an amount up to about 3 parts by weight of a total amount of water in the pressure vessel to about 1 part by weight waste material and the cooling water is introduced into the pressure vessel in an amount such that the total amount of water present in the pressure vessel after the cooling step is at least about 3.5 parts by weight to about 1 part by weight treated waste material. 2. The method of claim 1 wherein the treated waste material includes odorous compounds which are diluted by the cooling water. 3. The method of claim 1 wherein the waste material comprises organic material that includes odorous compounds or, when subjected to the treating step, forms odorous compounds which are diluted by the cooling water. 4. The method of claim 3 wherein the organic material comprises waste food, waste beverage, or both. 5. The method of claim 1 wherein the waste material includes polymeric waste material and the method further comprises the step of separating the substantially re-pulped waste paper from the polymeric waste material after the step of introducing the cooling water. 6. The method of claim 1 further comprising adding dilution water to the pressure vessel in addition to or along with the waste material for use during the treating step. 7. The method of claim 6 wherein the pressure vessel is mounted to rotate about an inclined axis equipped with suitable agitating means to thoroughly mix said waste material and dilution water. 8. The method of claim 1 wherein the dilution water is introduced into the pressure vessel in an amount up to about 3 parts by weight of a total amount of water to about 1 part by weight waste material and the cooling water is introduced into the pressure vessel in an amount such that the total amount of water present in the pressure vessel after the cooling step but before the discharge step is at least about 3.8 parts by weight to about 1 part by weight treated waste material. 9. The method of claim 1 wherein the elevated processing pressure is at least about 5 psig. 10. The method of claim 1 wherein the cooling water has a temperature less than about 115° F. 11. The method of claim 1 wherein the step of treating includes agitating the waste material in the pressure vessel. 12. The method of claim 11 wherein the agitating step is conducted at the elevated processing temperature and pressure for a sufficient time to substantially re-pulp the waste paper, such that components of the treated waste material can be separated by density and size. 13. The method of claim 1 wherein the step of treating includes introducing thermal energy into the pressure vessel to reach the elevated processing temperature and pressure within the pressure vessel. 14. The method of claim 1 wherein the step of treating includes introducing steam into the pressure vessel to reach the elevated processing temperature and pressure within the pressure vessel. 15. The method of claim 14 wherein the one or more chemical aides include at least one chemical selected from the group consisting of alkaline agents, buffers, bleaching agents, detergents, surfactants, solvents, dispersants, chelating agents, sequestrants, and mixtures thereof. 16. The method of claim 1 wherein the treating step includes introducing one or more chemical aides into the pressure vessel to facilitate re-pulping of the waste paper. 17. The method of claim 1 wherein the pressure vessel includes a rotatable drum for containing the waste material and the step of agitating comprises rotating the drum. 18. The method of claim 1 wherein the treating step is conducted for a time from about 30 minutes to about 90 minutes. 19. The method of claim 1 wherein said pressure vessel is an elongated vessel of generally cylindrical configuration mounted to be driven in rotation about its longitudinal axis. 20. The method of claim 1 further comprising the step of reducing the elevated processing pressure in the pressure vessel after the treating step and before the cooling water introduction step by use of a vent or eductor or both.
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