# US 7,610,692 B2 · Systems for prevention of HAP emissions and for efficient drying/dehydration processes > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 7,610,692 B2 - Document ID: US7610692B2 - Status: Granted - Kind: B2 - Application number: 11/335,153 - Filed: 2006-01-18 - Published: 2007-07-19 - Granted: 2009-11-03 - Earliest claimed: 2006-01-18 - Assignees: EarthRenew, Inc. - Applicants: Christianne Carin, legal representative - Inventors: Christianne Carin; Brian N. Gorbell; Alvin W. Fedkenheuer; John S. Jonasson; Alexander Starosud - Web page: https://patentgrep.com/patent/US7610692B2 ## CPC - F26B 23/022: {incinerating volatiles in the dryer exhaust gases, the produced hot gases being wholly, partly or not recycled into the drying enclosure} - Y02E 20/12: Heat utilisation in combustion or incineration of waste - F26B: DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM (drying devices for combines A01D41/133; racks for drying fruit or vegetables A01F25/12; drying foodstuffs A23; drying hair A45D20/00; body-drying implements A47K10/00; drying household articles A47L; drying gases or vapours B01D; chemical or physical processes for dewatering or like separating liquids from solids B01D43/00; centrifugal apparatus B04; drying ceramics C04B33/30; drying yarns or fabrics in association with some other form of treatment D06C; drying frames for laundry without heating or positive air circulation, domestic laundry-or spin-driers, wringing or hot pressing laundry D06F; furnaces, kilns, ovens F27) - Y02E: REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION ## Abstract This invention discloses systems, apparatuses and methods for drying or dehydrating high moisture content feedstock to dry or low moisture products. 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, flakes or other desired form for the final product. The systems, apparatuses and methods of this invention also provide for prevention of release of HAP, including VOC, emissions from manufacturing facilities in conjunction with or independent of the above treatment of high water content feedstock. ## Claims ### Claim 1 A method for treatment of high water content feedstock in a manufacturing facility comprising: producing first and second waste streams within the manufacturing facility, the first waste stream including a high water content feedstock and the second waste stream including HAP emissions; operating a gas turbine producing exhaust gases; directly contacting the exhaust gases with the high water content feedstock produced within the manufacturing facility for a contact time sufficient to produce a dried material having a moisture content less than the feedstock; and directing the HAP emissions produced in the manufacturing facility and ventilation air from the manufacturing facility into the combustion air intake of the gas turbine. ### Claim 2 (depends on 1) A method according to claim 1 wherein the gas turbine comprises a gas turbine generator. ### Claim 3 (depends on 1) A method according to claim 1, wherein at least one of NOx, SOx, and COx gases present in the exhaust gases of the gas turbine are absorbed directly into the high water content feedstock during drying of the high water content feedstock. ### Claim 4 (depends on 1) A method according to claim 1, wherein the exhaust gases do not pass through an intermediate heat exchanger before directly contacting the high water content feedstock. ### Claim 5 (depends on 1) A method according to claim 1, wherein the HAP emissions and the ventilation air are passed through a filter before being directed into the combustion air intake of the gas turbine. ### Claim 6 (depends on 1) A method according to claim 1, wherein the exhaust gases directly contacting the high water content feedstock have a temperature of at least 700 degrees F. ### Claim 7 (depends on 1) A method according to claim 1, wherein contact between the exhaust gases and the high water content feedstock does not cause substantial pyrolysis of the high water content feedstock. ### Claim 8 (depends on 1) A method according to claim 1, wherein contact between the exhaust gases and the high water content feedstock takes place in a rotary dryer vessel. ### Claim 9 (depends on 8) A method according to claim 8, wherein a temperature in the rotary dryer vessel is at least 700 degrees F. ### Claim 10 (depends on 9) A method according to claim 9, wherein dried feedstock and the exhaust gases exit the rotary dryer vessel through a common outlet. ### Claim 11 (depends on 10) A method according to claim 10, wherein a dryer outlet conduit conveys the dried feedstock and the exhaust gases from the common outlet of the rotary dryer vessel to a solids/gas separator, wherein a blower draws the exhaust gases from the solids/gas separator and directs the exhaust gases to atmosphere, and wherein the blower reduces backpressure in the rotary dryer vessel via the dryer outlet conduit. ### Claim 12 (depends on 6) A method according to claim 6, wherein the exhaust gases do not pass through an intermediate heat exchanger as the exhaust gases flow from the gas turbine to the high water content feedstock. ### Claim 13 (depends on 1) A method according to claim 1, wherein the dried material includes fertilizer or soil builder. ### Claim 14 (depends on 1) A method according to claim 1, further comprising using the gas turbine to generate electricity.