Method for operating a steam cycle process
US-9163530-B2 · Oct 20, 2015 · US
US9518729B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9518729-B2 |
| Application number | US-201213366729-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 6, 2012 |
| Priority date | Dec 13, 2011 |
| Publication date | Dec 13, 2016 |
| Grant date | Dec 13, 2016 |
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Methods are disclosed for providing recovered lignin of suitable quantity and quality to provide sufficient heating value to power the generation of supercritical or near critical water without the need for outside sources of energy. Supercritical or near critical water generator devices and systems are also disclosed.
Opening claim text (preview).
What is claimed is: 1. A system for generating supercritical or near critical water, comprising: a biomass conversion system adapted to produce lignin from a material comprising lignocellulose using supercritical or near critical water; a supercritical or near critical water generator adapted to provide supercritical or near critical water to said biomass conversion system, said supercritical or near critical water generator comprising: at least one pump adapted to provide water at a pressure of at least about 221 bar to form compressed water; and at least one fuel combustion apparatus adapted for combusting a fuel composition comprising said lignin; wherein said lignin has a heating value of at least about 3,000 BTU/lb; a fuel handling system adapted to transport said lignin from said biomass conversion system to said fuel combustion apparatus; and a water circulation system adapted to transport said compressed water in proximity of said fuel combustion apparatus adequate to heat said compressed water to a temperature of at least about 373° C. to produce said supercritical or near critical water. 2. The system of claim 1 , wherein said lignin has a heating value of at least about 5,000 BTU/lb. 3. The system of claim 1 , wherein said lignin has a heating value of at least about 7,500 BTU/lb. 4. The system of claim 1 , further comprising: at least one dryer for said fuel composition comprising lignin. 5. The system of claim 1 , wherein said lignin is in a powdered form. 6. The system of claim 5 , wherein said lignin is in a pelletized form. 7. The system of claim 5 , wherein said lignin is in a liquid form. 8. The system of claim 1 , further comprising: a preheater for said water or said compressed water in association with said water circulation system. 9. The system of claim 8 , wherein said preheater heats said water or said compressed water to a temperature of about 100° C. to about 300° C.
with a power/heat generating installation · CPC title
Detecting the properties of waste to be incinerated, e.g. heating value, density · CPC title
the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines · CPC title
Heat utilisation in combustion or incineration of waste · CPC title
drying · CPC title
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