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Patent No: IN559127 [India] Application No: IN202311015544
Title: Dry Anaerobic Digester For Lignocellulosic Biomass with unique hydrodynamics (DADFOR LCB)
Issue Date: 30-01-2025 File Date: 07-03-2023
Inventor(s): Anupoju Gangagni Rao; Sameena Begum; Vijayalakshmi Arelli; Sudharshan Juntupally; Naveen Kumar Mamindlapelli; Parmeshwar Patil; Vivek Rathore; Jaya Rawat; Anurag Singh
IPC Classification: C02F11/04, C02F3/28, C12M1/00 C12M1/107
Abstract:
The present  invention provides a reactor for the anaerobic digestion of lignocellulosic biomass for biogas and biomanure (digestate) generation. The innovation is designed  primarily for the treatment of lignocellulosic biomass such as rice straw/rice husk with a total solids consistency in the slurry between 20 - 40 %. One of the major  obstacles in the AD of lignocellulosic biomass is the formation of scum layer on the top surface of the slurry with the fibrous material leading to choking of pipelines.  Scum layer formation occurs due to the phase separation of the material into solid and liquid, poor contact between the organic matter and the microorganisms, low heat  and mass transfer. Phase separation of solid and liquid occurs particularly in low density materials such as lignocellulosic biomass. Therefore, the reactor is designed in  a way that the maximum solids including the fibrous material is retained inside the reactor for efficient digestion. The reactor comprises of a feed hydrolysis duct  situated inside the reactor. The hydraulic residence time of the feed hydrolysis duct is delinked with that of the main reactor. Further the reactor is provided with open  and closed, perforated cones to ensure efficient movement of the slurry from the top to bottom. Pressurized biogas purging in the bottom elongated cone area of the  reactor ensures no settling of solids in the cone, while the slurry recirculation and the pressurized biogas purging inside the digester helps promote efficient mixing of  the reactor contents in the digester preventing the formation of phase separation, scum layer formation, choking etc. The feed slurry is initially allowed to flow through  the central duct towards the bottom of the reactor which then expands creating an upward flow regime from the bottom due to the presence of a truncated cone. The  perforated truncated cones ensure retainment of maximum solids in the reactor arresting any biomass washout. The reactor is also facilitated with a feed preparation  system, digestate collection tank, biogas balloon, feed inlet and digestate outlet valve mechanism for controlled feed in and digestate out.
Startup Options:
ADVANTAGES OF THE INVENTION
The design has unique hydrodynamics
Delinking of the residence time of the feed hydrolysis duct from the residence time of the main reactor for efficient digestion of the low-density material without any phase separation.
Middle perforated truncated cones fixed to the wall of the cylindrical reactor and the top and bottom truncated cones are meant to create turbulence in the reactor disturbing the flow behaviour of the slurry, ensure proper mixing of the material inside the digester without any mechanical equipment.
The arrangement of truncated cones create unique hydrodynamics inside the reactor even with materials such as lignocellulosic biomass by preventing phase separation and biomass washout.
The perforated truncated cone above the bottom truncated cone ensures the movement of slurry towards upward flow regime through the perforations (20 mm) while the solid material is retained in the bottom part of the reactor.
The bottom truncated cone elongated through the central duct is provided to ensure the retainment of solids and divert the flow from bottom to towards the middle perforated truncated cone.  
The top truncated cone is provided for the easy movement of the thinner slurry towards the perforated plate. 
The conical bottom of the reactor is a place where maximum solids are retained and the mixing of solids in the cone is ensured through pressurized biogas purging.
The perforated plate ensures further retainment of solids and allows the liquid to flow towards up which is then withdrawn as the final digestate. 
Scaling up of digester to handle a wide range of waste quantities from smaller capacity to larger capacity. 
Intermittent mixing of digester slurry by using the autogenerated biogas pressure and slurry recirculation from bottom to top. 
De-alienation of scum formation issue, elimination of choking and clogging, short-circuit of feed in the digester which are common issues in conventional digesters.
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