Floating methanation system

• US 10,189,734 B2
• Filed: 12/12/2015
• Issued: 01/29/2019
• Est. Priority Date: 12/16/2014
• Status: Active Grant

• Current Assignee: Gilles Nadon
• Original Assignee: Gilles Nadon
• Inventors: Nadon, Gilles
• Primary Examiner(s): Bhat, Nina
• Application Number:
  US14/967,277
• Publication Number:
  US 20160168000A1
• Time in Patent Office: 1,144 Days
• Field of Search: 4352891, 4352908, 4352973, 210605, 210613
• CPC Class Codes: C02F 11/04 Anaerobic treatment; Production of methane by such processes
• CPC Class Codes: C02F 2203/006 details of construction, e.g. specially adapted seals, modules, connections
• CPC Class Codes: C02F 3/2866 Particular arrangements for anaerobic reactors
• CPC Class Codes: C05F 7/00 Fertilisers from waste water, sewage sludge, sea slime, ooze or similar masses
• CPC Class Codes: E03C 1/2665 Disintegrating apparatus specially adapted for installation in waste pipes or outlets disintegrating apparatus per se B02C
• CPC Class Codes: F17D 1/005 for a two-phase gas-liquid flow
• CPC Class Codes: F17D 3/00 Arrangements for supervising or controlling working operations
• CPC Class Codes: F28D 1/0213 for heating or cooling a liquid in a tank
• CPC Class Codes: F28D 1/022 for immersion in a natural body of water, e.g. marine radiators
• CPC Class Codes: F28D 1/06 with the heat-exchange conduits forming part of, or being attached to, the tank containing the body of fluid
• CPC Class Codes: F28D 21/0012 the heat being recuperated from waste water or from condensates
• CPC Class Codes: F28F 19/008 by using scrapers
• CPC Class Codes: Y02A 20/30 Relating to industrial water supply, e.g. used for cooling
• CPC Class Codes: Y02A 40/20 Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
• CPC Class Codes: Y02E 50/30 Fuel from waste, e.g. synthetic alcohol or diesel
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage
• CPC Class Codes: Y02W 10/20 Sludge processing
• CPC Class Codes: Y02W 30/40 Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse

Abstract

An apparatus for the treatment and transformation of municipal wastewater sludge or any other organic putrescible matter into biogas and liquid fertilizer by methanation. Several consecutive floating cylindrical bioreactors almost totally immersed in water, are bathing longitudinally in a thermally insulated basin to maintain set temperatures, mixing their contents by revolving on themselves by the action of air ejected from a conduit underneath them, engaging all elements in a collective momentum, from a multiplied force, because of the constant free power of each air bubble lodged in exterior buckets and grouped as a lifting force. The gas produced by methanation of the organic waste furnishes a source of heat and its pressure is used for the functioning of the whole apparatus, including several types of pumps, valves, and a new model of steam engine. A network of hoses is provided to bring the fertilizer to the farmlands.

Claims

1. An apparatus for treatment and transformation of municipal wastewater sludge or other organic putrescible matter into biogas and liquid fertilizer by anaerobic digestion, said apparatus comprising a plurality of floating bioreactors consecutively arranged in series;

wherein a first bioreactor initially processes wastewater sludge or other organic putrescible matter also wherein to remove sand, gravel or crushed glass;

a series of middle bioreactors which process and digest the wastewater sludge or putrescible matter and a final bioreactor wherein the sludge or matter is further digested;

wherein the final bioreactor includes means for measuring and monitoring the end of biogas production;

said apparatus further comprising a heat exchanger for heating the sludge or matter for the destruction of harmful bacteria and pathogens;

wherein each bioreactor comprising a longitudinal body to digest and provide methanation reaction of said sludge or matter within the bioreactor;

each of said bioreactors further comprising a longitudinal inlet end, an inlet spout, located at a middle point of said longitudinal inlet end, connected to an inlet conduit by an inlet elbow, for purpose of receiving the matter into the bioreactor;

said bioreactors further comprising a longitudinal outlet end, an outlet spout located at a middle point of said longitudinal outlet end, connected to an outlet conduit by an exhaust elbow for the purpose of exiting the matter from one bioreactor to the next bioreactor and from the last bioreactor at the end of the process, wherein pressure is created by retaining the biogas produced and wherein said floating bioreactors are almost totally immersed in warm water in a thermally insulated basin to maintain predetermined temperature for digestion and methanation conditions;

wherein said bioreactors revolve on themselves by air ejected from a conduit disposed underneath said bioreactors, wherein said air is pumped into said conduits by air diaphragm pumps activated by the pressurized biogas;

said air lodging in rotation buckets aligned as circular saw teeth outside the longitudinal body of the bioreactor, said air provoking a rotating action, mixing the contents;

each of said bioreactors include mixing buckets aligned inside the body of the bioreactor;

each of said bioreactors further comprise flotation rings located at the inlet and outlet of the bioreactor for counterbalancing the weight of the bioreactors and to provide buoyancy to the bioreactors so that the bioreactors remain horizontally disposed while floating;

said apparatus further comprising a primary inlet pump, which is a dual hydraulic command diaphragm pump having a dual purpose, first to initiate and supply initial matter to be processed, and secondly, to drive said matter through the heat exchanger and squeeze the pressure created by heat against a first swivelling valve exhaust pump, said first swivelling valve exhaust pump working in combination with a last swivelling valve exhaust pump, both being two-diaphragm pumps having two functions;

first to retain, control, and release the flow and pressure by transferring power hydraulically to the primary inlet pump, while the second function in which they differ, is that the first swivelling valve exhaust pump creates a vise action from the high pressure created from heating matter in the heat exchanger situated between said primary inlet pump and said first swivelling valve exhaust pump while the last swivelling valve exhaust pump retains the working pressure of the entire apparatus and transfers said pressure to the primary inlet pump from a closed-center hydraulic circuit that increases said pressure by the action of gas hydraulic pumps from each bioreactor, said closed-center hydraulic circuit comprising a shut-off valve that commands the last swivelling valve exhaust pump to operate and let consumed matter to escape when production of biogas is over, and a shut-off valve that commands the primary inlet pump to operate when new material is needed;

said apparatus further comprising biogas pipes for the capture of biogas from the inside top portion of each bioreactor;

wherein each of said bioreactors include a pressure relief valve to control the pressure in each bioreactor;

said apparatus further including a plurality of hoses and conduits for the purpose of transporting fluids out of the bioreactor for the removal of fertilizers, juices and salts.

2. The apparatus of claim 1 wherein the first bioreactor is maintained at a thermophilic level of temperature, and wherein the middle bioreactors and last bioreactors are maintained at a mesophilic level of temperature.

3. The apparatus of claim 1, wherein each of said bioreactors further comprise a spiral channel situated inside the outlet end of said bioreactor to convey heavy matter from the bottom of the bioreactors through the outlet spouts.

4. The apparatus of claim 1 wherein the first bioreactor further comprising upright flat bars placed inside the body of said bioreactor under said mixing buckets forming a helical arrangement to move heavy unwanted matter from said bioreactor toward the outlet spout which can further include a spiral channel to improve transfer of material through the outlet.

5. The apparatus of claim 1, wherein the first bioreactor further comprises a lower port located at the exhaust elbow of the outlet conduit, said lower port in operative connection with a sinking reservoir for evacuating heavy material from said bioreactor to said sinking reservoir further comprising a valve controlling evacuation from the pressure of the bioreactor when said sinking reservoir reaches a predetermined low level.

6. The apparatus of claim 1 wherein the pressure of the biogas produced within the bioreactors is used to regulate the volume of the sludge contained in the bioreactors, pressurize the entire apparatus and provides power to activate a chain of mechanical motions for the functioning of said apparatus.

7. The apparatus of claim 1 wherein the last bioreactor includes a flow control valve in connection with a pressure valve to determine the end of biogas production and command the last swiveling valve exhaust pump to evacuate process material contained within the bioreactor and to allow new material to enter the apparatus.

8. The apparatus of claim 1, wherein the hoses and conduits connected to the last bioreactor by the last swiveling valve exhaust pump are constructed and arranged to deliver fluids from the reactors to farmlands as water and fertilizer.

9. The apparatus of claim 1 wherein the swiveling valve exhaust pumps further comprise a swiveling valve body of conic shape in order to use the working pressure as a sealing force, said swiveling valve further comprising two cross-directional tunnels matching two ports of a valve casing to drive pressure through one of the ports to fill a diaphragm to expand while drawing an opposite diaphragm to empty through a second cross-directional tunnel of said swiveling valve thereby creating a stroke action that generates hydraulic power because said stroke action transfers to an attached hydraulic piston, said swiveling valve turns, at the end of the stroke action, from a position of full opening to the ports of the valve casing, goes through a surface of total obstruction to arrive finally to a full opening of the opposite ports, driving the flow action in the reverse direction without losing any working pressure, said swiveling valve further comprising a rotation device that transfers a turning motion to balls disposed in-between conic holes of which a facing angle is perpendicular to the swiveling valve (41) taper edge, said balls serving to break the force by a shifting motion so that pressure keeps a gap closed while the valve turns without friction, and makes a back and forth half-rotation to prevent winding of unwanted material.

10. The apparatus of claim 1 further comprises rotary diaphragm pumps working by the action of a rotary valve functioning with a taper contact face ensuring a perfect sealing contact from entering pressure against a flange surrounding a body, said rotary diaphragm pumps receiving motion from the entering pressure driving through ports on one side, activating diaphragms of said rotary diaphragm pumps while releasing opposite diaphragms through ports on the opposite side, said rotary valve further comprising balls lodged in taper holes to apply a pushing force, acting against the friction of the taper contact when said rotary valve is in movement when the rotary diaphragm pump is in action, said rotary diaphragm pumps further comprising two diaphragm spiders related together by a bent shaft turning in their middle, rocking them, and activating diaphragms to pump consecutively.

11. The apparatus of claim 1 further comprises steam engines, the rotating energy of said steam engines powering generators to produce electricity, said steam engines comprising two rotary valves connected to diaphragm spiders where water is driven and pumped from smaller diaphragms of an inner circumference of said steam engines, the water sent to boil to steam, and directed through the second rotary valve, activating outer and bigger diaphragms of said steam engine.

12. The apparatus of claim 1 wherein the pressurized biogas dedicated to pressurize the whole apparatus, and activate several devices for the functioning of said apparatus, applies force as a cascade of decreasing pressure from one bioreactor to the next bioreactor to push sludge from one bioreactor to the next bioreactor, said pressurized biogas applying force to activate air diaphragm pumps, rotary diaphragm pumps and hydraulic pumps, said hydraulic pumps add hydraulic pressure to the closed-center hydraulic circuit.

13. The apparatus of claim 1 wherein the heat exchangers comprise coil scrapers inside tubes of said heat exchangers to remove any sticking matter from said tubes.