Process and system for drying and heat treating materials

• US 7,882,646 B2
• Filed: 10/30/2007
• Issued: 02/08/2011
• Est. Priority Date: 07/19/2004
• Status: Expired due to Fees

• Current Assignee: Earthrenew Inc.
• Original Assignee: Earthrenew Inc.
• Inventors: Fedkenheuer, Alvin W., Gorbell, Brian N., Starosud, Alexander, Jonasson, John S.
• Primary Examiner(s): Lorengo; Jerry
• Assistant Examiner(s): Smith; Jennifer A
• Application Number:
  US11/981,395
• Publication Number:
  US 20080104858A1
• Time in Patent Office: 1,197 Days
• Field of Search: 343/63, 34/90, 34/86, 343/81, 344/87, 345/07, 345/14, 344/43, 71/21, 71/9, 71/7, 71/8, 71/15, 607/80, 607/81
• US Class Current: 34/514
• CPC Class Codes: F26B 19/005 Self-contained mobile devices, e.g. for agricultural produce movable devices with radiation means F26B3/28; small self-contained devices for drying objects at rest F26B9/003
• CPC Class Codes: F26B 2200/18 Sludges, e.g. sewage, waste, industrial processes, cooling towers
• CPC Class Codes: F26B 23/001 using waste heat
• CPC Class Codes: F26B 23/02 using combustion heating F26B3/305, F26B13/186, F26B21/001, F26B23/10 take precedence
• CPC Class Codes: Y02E 20/12 Heat utilisation in combustion or incineration of waste
• 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
• CPC Class Codes: Y02P 70/10 Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

Abstract

This invention discloses systems and methods for conversion of high moisture waste materials to dry or low moisture products for recycle or reuse. The equipment systems comprise a gas turbine generator unit (preferred heat source), a dryer vessel and a processing unit, wherein the connection between the gas turbine and the dryer vessel directs substantially all the gas turbine exhaust into the dryer vessel and substantially precludes the introduction of air into the dryer vessel and wherein the processing unit forms the dried material from the dryer vessel into granules, pellets or other desired form for the final product. Optionally, the systems and methods further provide for processing ventilation air from manufacturing facilities to reduce emissions therefrom.

Claims

1. A method for reducing atmospheric release of emission gases from a manufacturing operation comprising:

generating a non-gaseous waste material feedstock at an operation that produces operation emission gases;

enclosing at least a portion of the operation that produces the operation emission gases to contain the operation emission gases;

enclosing the non-gaseous waste material feedstock at a storage location to contain vapors generated by the stored non-gaseous waste material feedstock;

directing at least a portion of the operation emission gases to a combustion air intake of a gas turbine, oil or gas burner or a reciprocating engine;

directing at least a portion of the vapors from the storage location to the combustion air intake of the gas turbine, oil or gas burner or reciprocating engine;

directing the non-gaseous waste material feedstock from the storage location to a dryer, wherein the non-gaseous waste material feedstock undergoes no digestion or minimal digestion before being directed to the dryer; and

directing combustion exhaust gases from the gas turbine, burner or engine directly to the dryer vessel for drying or treating the non-gaseous waste material feedstock, wherein the combustion exhaust gases do not pass through an intermediate heat exchanger before directly contacting the non-gaseous waste material feedstock.

2. A method according to claim 1 wherein the gas turbine comprises a gas turbine generator.

3. A method according to claim 1 wherein the manufacturing operation produces emission gases that contain greenhouse gases.

4. A method according to claim 1 wherein all the combustion air is from the enclosed portion of the operation.

5. A method according to claim 1, wherein the gas turbine, oil or gas burner or a reciprocating engine includes a fuel intake, and wherein natural gas is directed into the fuel intake.

10. A method according to claim 1, further comprising directing the non-gaseous waste feed stock from the dryer to a processing location where the non-gaseous waste material feedstock is processed by a processing step selected from the group consisting of granulating, pelletizing and prilling.

6. A method for reducing atmospheric release of emission gases comprising:

generating a non-gaseous waste material feedstock at an operation that produces operation emission gases;

enclosing at least a portion of the operation that produces the operation emission gases to contain the operation emission gases;

enclosing the non-gaseous waste material feedstock at a storage location to contain waste material emission gases generated by the stored non-gaseous waste material feedstock;

directing at least a portion of the operation emission gases to a combustion air intake of a gas turbine;

directing at least a portion of the waste material emission gases from the storage location to the combustion air intake of the gas turbine;

directing the non-gaseous waste material feedstock from the storage location to a dryer, wherein the non-gaseous waste material feedstock undergoes no digestion or minimal digestion before being directed to the dryer; and

directing combustion exhaust gases from the gas turbine directly to the dryer vessel for drying or treating the non-gaseous waste material feedstock, wherein the combustion exhaust gases do not pass through an intermediate heat exchanger before directly contacting the non-gaseous waste material feedstock.

11. A method according to claim 6, further comprising directing the non-gaseous waste feed stock from the dryer to a processing location where the non-gaseous waste material feedstock is processed by a processing step selected from the group consisting of granulating, pelletizing and willing.

7. A method for processing non-gaseous waste and gaseous emissions from a facility, the facility including a facility enclosure, the method comprising:

generating a non-gaseous waste feedstock in the facility enclosure;

storing the non-gaseous waste feedstock in an enclosed waste material holding location;

directing ventilation air from the facility enclosure to a combustion air intake of a gas turbine;

directing vapors from the enclosed waste material holding location to the combustion air intake of the gas turbine;

moving at least some of the non-gaseous waste feedstock from the enclosed waste material holding location to a dryer in fluid communication with an exhaust outlet of the gas turbine; and

heating the non-gaseous waste feedstock in the dryer by directly contacting the non-gaseous waste feedstock with combustion exhaust gas from the gas turbine, wherein the combustion exhaust gas from the gas turbine goes directly to the dryer and does not pass through an intermediate heat exchanger before contacting the non-gaseous waste feedstock.

8. A method according to claim 7, wherein the non-gaseous waste feedstock undergoes no digestion or minimal digestion prior to being heat treated.

9. A method according to claim 7, wherein the exhaust gas has a temperature of at least 700 degrees F. when the exhaust gas enters the dryer.

12. A method according to claim 7, further comprising directing the non-gaseous waste feed stock from the dryer to a processing location where the non-gaseous waste material feedstock is processed by a processing step selected from the group consisting of granulating, pelletizing and prilling.