Enriched fuel making and sewage treating process

• US 4,135,888 A
• Filed: 09/20/1977
• Issued: 01/23/1979
• Est. Priority Date: 09/20/1977
• Status: Expired due to Term

• Current Assignee: Nuclear Supreme
• Original Assignee: Nuclear Supreme
• Inventors: Waltrip, Owen R.
• Primary Examiner(s): Dees, Carl
• Application Number:
  US05/835,022
• Time in Patent Office: 490 Days
• Field of Search: 44/1 R, 44/1 D, 44/1 F, 44/10 A, 44/10 C, 44/10 F, 201/21, 201/22, 201/25, 201/38, 201/41
• US Class Current: 44/552
• CPC Class Codes: C10B 53/00 Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form wet carbonising of peat C10F
• CPC Class Codes: C10L 5/46 on sewage, house, or town refuse C10L5/403, C10L5/406 take precedence
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel
• CPC Class Codes: Y02E 50/30 Fuel from waste, e.g. synthetic alcohol or diesel

Abstract

Particulate coke and raw sewage are mixed and conveyed as a slurry through series connected, pressure sealed chambers into which super-heated steam is injected to convert the mixture into a molten mass depleted of noxious gases and volatiles. The molten mass is compacted while exposed to reactive hydrogen gas to form an enriched solid fuel log.

Claims

1. In a process for producing a solid fuel from a slurry formed from raw sewage and particulate coke, the steps of:

conducting said slurry through a plurality of pressure sealed zones in series;

physically agitating the slurry during movement through said zones;

injecting super-heated steam into said zones during said movement of the slurry therethrough to release only non-noxious gases and volatiles leaving a liquid depleted residue;

compacting the residue discharged under pressure from the zones within a reaction zone;

injecting hydrogen gas into the reaction zone during compaction of the residue to form a compacted mass; and

cooling said compacted mass to form the solid fuel product.

2. The process of claim 1 wherein said non-noxious gases and volatiles are water and hydrocarbon gases and vapors.

3. The process of claim 2, wherein said slurry is conveyed through the mixing zones by forced feed flow.

4. The process of claim 1 wherein said slurry is conveyed through the mixing zones by forced feed flow.

5. A method of continuously treating raw sewage and enriching a relatively low energy content solid fuel, comprising the steps of:

grinding said solid fuel into particles;

mixing said particles with the raw sewage to form a slurry;

mixing the slurry during movement with super-heated steam until non-noxious gases and volatiles are evolved therefrom, leaving a liquid depleted mass;

exposing said mass to a reactive gas other than steam; and

compacting said mass into a solid fuel product.

6. The method of claim 5 wherein said low energy content solid fuel is coke.

7. The method of claim 6 wherein said reactive gas is hydrogen.

8. The method of claim 5 wherein said reactive gas is hydrogen.

9. A method of treating sewage which comprises mixing the sewage with particulate coke within a pressure sealed chamber;

subjecting the mix to the action of heat during movement through said chamber by mixing with superheated steam;

extracting volatile by-products from the chamber during the heating operation;

discharging a liquid-depleted residue of said mix from said chamber;

compacting said residue; and

subjecting said residue to hydrogen gas during compaction thereof.