Anaerobic column reactor for biodegradation of wastes and the process thereof

Patent metadata

Field	Value
Publication number	US-10457613-B2
Application number	US-201615240851-A
Country	US
Kind code	B2
Filing date	Aug 18, 2016
Priority date	Aug 19, 2015
Publication date	Oct 29, 2019
Grant date	Oct 29, 2019

Abstract

The present invention relates to an anaerobic column reactor for biodegradation of wastes. Particularly the present invention relates to a process for conversion of biodegradable wastes to biogas and compost. More particularly, the present invention relates to an anaerobic reactor with unique arrangement of expanded and constricted portions alternatively placed vertically over each other which enhances the mixing pattern and thereby the mass transfer rates while controlling the biomass washout by regulating the upflow liquid velocity.

First claim

We claim:

1. An anaerobic column reactor for conversion of biodegradable organic matter present in wastewaters and solid wastes into biogas and compost; said reactor consisting essentially of a column of at least four expanded portions (EP), connected to each other by constricted portions (CP), waste feeding and chemicals feeding facility, biogas collection sampling and measurement assembly, slurry/digestate recirculation assembly, with backwash facility;
wherein, the waste feeding and chemicals feeding either through inlet pipe ( 5 ) with a pump ( 4 ) and regulating valve ( 6 ) or directly through a funnel with a valve ( 16 ); the biogas collection sampling and measurement assembly connected through a pipe ( 17 ) with a valve ( 18 ); the slurry/digestate recirculation through a pipe with a pump ( 13 ) and a valve ( 14 ) into the constricted portion; and the bottom opening of the reactor with a valve ( 15 ) to impart backwash facility.

2. An anaerobic column reactor ( 100 ) for conversion of biodegradable organic matter present in wastewaters and solid wastes into biogas and compost, said reactor having a feed tank ( 1 ) equipped with waste feeding funnel ( 2 ), mixing arrangement ( 3 ), feed pump ( 4 ), inlet pipe ( 5 ), regulating valves ( 6 ), said reactor ( 100 ) having a constricted portion ( 7 ) and expanded portion ( 8 ), recirculation pipe ( 9 ), outlet ( 10 ), valves ( 11 ) and ( 12 ), slurry recirculation facility ( 13 ) ( 14 ) ( 15 ), chemicals feeding facility ( 16 ), biogas collection facility ( 17 ) ( 18 ), sampling and a measurement assembly ( 19 ) ( 20 ), outlet pipe ( 10 ) of reactor connected to a settling tank ( 21 ), a biogas collection assembly ( 22 ) connected with outlet ( 23 ), sludge disposal outlet ( 24 ), and slurry/digestate recirculation arrangement ( 25 ) connected with valves ( 26 ) ( 27 ) and a stand ( 28 ) to support the column reactor; wherein the chemicals feeding facility directly through a funnel with a valve ( 16 ); the slurry recirculation facility through a pipe with a pump ( 13 ) and a valve ( 14 ) into the constricted portion and a valve ( 15 ) to impart backwash facility.

3. The anaerobic column reactor according to claim 2 , wherein said reactor ( 100 ) consisting a column of at least four alternate expanded portions ( 8 ) connected to each other by constricted portions ( 7 ).

4. The anaerobic column reactor according to claim 2 , wherein alternate expanded portions ( 8 ) and constricted portions ( 7 ) are connected in series that the reactor has a single outlet ( 23 ) and single biogas collection point.

5. The anaerobic column reactor according to claim 2 , wherein said reactor ( 100 ) is operated in a batch mode, semi-continuous or continuous mode with automated or manual operation possible.

6. The anaerobic column reactor according to claim 2 , wherein alternate expanded portions ( 8 ) are interconnected through a recirculation pipe ( 9 ) is facilitate recirculation of digested from a particular expanded portion ( 8 ) with the help of the inlet ( 5 ) connected with controlling valves ( 6 ).

7. The anaerobic column reactor according to claim 2 , wherein biogas collection assembly ( 17 , 18 , 22 ) sampling and measurement assembly ( 19 , 20 ) is provided to facilitate biogas collection from the reactor ( 100 ) and settling tank ( 21 ).

8. The anaerobic column reactor according to claim 2 , wherein the funnel ( 2 , 16 ) with valve ( 6 ) is being used for waste feeding and chemicals feeding facility respectively.

9. The anaerobic column reactor according to claim 2 , wherein settling tank ( 21 ) is provided with effluent outlet ( 23 ) for removal of clarified effluent and sludge disposal outlet ( 24 ) at the bottom of the settling tank ( 21 ) for the discharge of the settled sludge.

10. The anaerobic column reactor according to claim 1 , wherein mixed culture of consortia anaerobic microorganisms is being used to digest organic biodegradable waste to biogas and compost.

11. The anaerobic column reactor according to claim 1 , wherein the biodegradable wastes is selected from biodegradable solid wastes, waste water and aqueous slurry of biomass, fruits, vegetables, agro-processing waste, animal compost, poultry wastes, aquatic plants, fraction of municipal solid wastes, energy crops and combinations thereof.

12. The anaerobic column reactor according to claim 2 , wherein mixed culture of consortia anaerobic microorganisms is being used to digest organic biodegradable waste to biogas and compost.

13. The anaerobic column reactor according to claim 2 , wherein the biodegradable wastes is selected from biodegradable solid wastes, waste water and aqueous slurry of biomass, fruits, vegetables, agro-processing waste, animal compost, poultry wastes, aquatic plants, fraction of municipal solid wastes, energy crops and combinations thereof.

14. A process for the conversion of biodegradable wastes into biogas and compost by using the reactor according to claim 2 , wherein the process steps comprises:
a. pumping the wastes and passing from inlet ( 5 ) at the bottom to outlet ( 23 ) at the top through constricted portion ( 7 ) and expanded portion ( 8 );
b. degrading wastes by mixing wastes with the culture of consortia anaerobic microorganism the reactor to obtain slurry;
c. recirculating the slurry obtained in step (b) in the reactor through recirculation pump ( 9 ) to produce biogas;
d. collecting the biogas generated in step (c) from settling tank ( 21 ) and biogas collection sampling assembly ( 17 , 18 ) and measurement assembly ( 19 , 20 );
collecting sludge from the setting tank ( 21 ) through sludge disposal outlet obtained in step (c) and sent for its disposal.

Assignees

• Council Scient Ind Res

Inventors

• Bodkhe Sandeep Y
• Vaidya Atul N

Classifications

• C12M23/02 Primary

  Form or structure of the vessel (large containers B65D88/00) · CPC title

• C05F17/964

  Constructional parts, e.g. floors, covers or doors · CPC title

• C05F17/95 Primary

  Devices in which the material is conveyed essentially vertically between inlet and discharge means · CPC title

• C05F17/50

  Treatments combining two or more different biological or biochemical treatments, e.g. anaerobic and aerobic treatment or vermicomposting and aerobic treatment · CPC title

• C05F17/40

  Treatment of liquids or slurries · CPC title