IP Library Granted Patent US 12678759
Granted Patent B2
US 12678759 · App. 17/769,388 · Granted Jul 14, 2026

Process and system for producing pulp, energy, and bioderivatives from plant-based and recycled materials

Inventors: Sandeep Kumar (Virginia Beach, VA); Peter Majeranowski (Danville, VA); Igor Kostenyuk (Winter Haven, FL); Iulian Bobe (Danville, VA); Florin Barla (Danville, VA)
Assignee: Circ, LLC
B01J19/0053B01D11/0207C10G1/04C10G1/065C12M21/12C12M43/02C12P7/10C12P7/649D21B1/14D21C1/02D21C3/02D21C3/22D21C5/02D21C7/00D21C11/0007D21H11/02B01J2219/00051B01J2219/00162B01J2219/00353B01J2219/00891C10G2300/1014Y02E50/10Y02P30/20Y02W30/64
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Quick Facts
Patent No.
US 12678759
App. No.
17/769,388
Granted
Jul 14, 2026
Kind
B2
Abstract

The presently disclosed subject matter relates to an industrial system for processing various plant materials to produce marketable materials. Particularly, the system integrates subcritical water extraction technology and includes a pre-processing module and a two-stage extractor (processing module) with constant control of temperature, pressure, and/or residence time. In some embodiments, the final product of the disclosed system can include feedstock constituents for biofuel production (sugars and/or oil), biochar, raw materials for various industries (such as pulp for manufacturing paper or cellulose for use in various industries). The disclosed system can be modular or non-modular, stationary or mobile, and can include prefabricated elements with programmed automatic or manual operation so that it can be easily moved and/or assembled on site.

Claims (19)

1 . A system comprising:

a pre-processing portion having a mechanical processor/material handler for extraction of water soluble fermentable carbohydrates and preparation of material for further extraction;

an extractor portion comprising a reactor or a reactor assembly to which biomass and subcritical water is supplied, the reactor or the reactor assembly having a first operating condition at a first pressure and a first temperature at a constant level that is held for a first defined period of time to break down carbohydrates of a first chain strength and a second operating condition at a second pressure and a second temperature at a constant level that is held for a defined second period of time to break down remaining oligo-carbohydrates of a second chain strength and fatty acids,

wherein the system is repeatable until the recovery rate of the fermentable carbohydrates, fatty acid, or both reaches a desired yield, and

wherein the mechanical processor/material handler of the pre-processing portion comprises a mechanical press for primary extraction of soluble carbohydrates, a wet or dry mill operably coupled to a material feeding mechanism, or both.

2 . The system according to claim 1 , wherein the mechanical processor/material handler of the pre-processing portion further comprises a storage tank for mixing with water or other liquid.

3 . The system according to claim 1 , further comprising a variable speed and flow rate pump that pumps the mixed biomass and liquid downstream.

4 . The system according to claim 1 , further including:

a high pressure pump for increasing a pressure in the system, wherein a variable speed and flow rate are provided; a pressure control valve for maintaining pressure in the first operating condition;

a pump for increasing the pressure of biomass in the flow channel to the second temperature and second pressure; and

a pressure control valve for maintaining pressure in the second pressure and second temperature section.

5 . The system according to claim 1 , wherein first operating condition comprises a pressure of about 0-300 psi and temperature of up to about 180° C. and the second operating condition comprises a pressure of about 301-3000 psi and a temperature of about 180° C. to 350° C.

6 . The system according to claim 1 , wherein the pre-processing and first and second operating conditions are controlled and monitored by a centralized computer software able to maintain constant a desired pressure, temperature, and flow rate for a desired period of time;

wherein the system comprises multiple sensors that are installed and connected to centralized computer managing software comprising a network in which technical information about major parameters such as pressure, temperature, flow, content level, is collected in real time, relayed to a managing system, and analyzed;

wherein the above parameters are controlled and modified in real time.

7 . The system according to claim 1 , wherein the reactor assembly comprises an assembly of one or more reactors followed by one or more pressure control valves, heat exchangers for cooling down the outputs from the reactor, and separators to collect valuable materials from the water phase and consequently recycle the water.

8 . The system according to claim 1 , wherein the system is configured to produce as its final product feedstock constituents such as fermentable carbohydrates, fatty acids, and other compounds for biofuel production, biochar, pulp, cellulose, or raw materials for various industries, or combinations thereof from plant based materials or putrescible waste.

9 . The system according to claim 1 , wherein the system is modular and scalable, stationary or mobile;

wherein when in mobile form, the system can be mounted on one or more truck trailers, rail cars, shipping containers, other platforms used to transport from one site to another, or combinations thereof.