The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Apr. 07, 2020

Filed:

Jun. 18, 2019
Applicant:

Aries Gasification, Llc, Nashville, TN (US);

Inventors:

Douglas R. Bull, Vancouver, CA;

Ross M. Patten, Palm Coast, FL (US);

Paul Cairney, Deltona, FL (US);

Gerald M. Cox, Cocoa, FL (US);

William P. Jepson, Orlando, FL (US);

Assignee:

Aries Gasification, LLC, Nashville, TN (US);

Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
C01B 7/00 (2006.01); C10J 3/46 (2006.01); B01J 8/18 (2006.01); C10J 3/48 (2006.01); C10K 1/02 (2006.01); C02F 11/10 (2006.01); C10J 3/84 (2006.01); C02F 11/12 (2019.01); C02F 11/121 (2019.01);
U.S. Cl.
CPC ...
C10J 3/466 (2013.01); B01J 8/1809 (2013.01); B01J 8/1827 (2013.01); C02F 11/10 (2013.01); C10J 3/482 (2013.01); C10J 3/84 (2013.01); C10K 1/026 (2013.01); B01J 2208/00893 (2013.01); B01J 2208/00902 (2013.01); C02F 11/12 (2013.01); C02F 11/121 (2013.01); C10J 2300/0909 (2013.01); C10J 2300/0916 (2013.01); C10J 2300/0923 (2013.01); C10J 2300/0956 (2013.01); C10J 2300/1643 (2013.01); C10J 2300/1807 (2013.01); Y02P 20/129 (2015.11); Y02W 10/40 (2015.05); Y10T 29/49 (2015.01);
Abstract

A fluidized bed biogasifier is provided for gasifying biosolids. The biogasifier includes a reactor vessel and a feeder for feeding biosolids into the reactor vessel at a desired feed rate during steady-state operation of the biogasifier. A fluidized bed in the base of the reactor vessel has a cross-sectional area that is proportional to at least the fuel feed rate such that the superficial velocity of gas is in the range of 0.1 m/s (0.33 ft/s) to 3 m/s (9.84 ft/s). In a method for gasifying biosolids, biosolids are fed into a fluidized bed reactor. Oxidant gases are applied to the fluidized bed reactor to produce a superficial velocity of producer gas in the range of 0.1 m/s (0.33 ft/s) to 3 m/s (9.84 ft/s). The biosolids are heated inside the fluidized bed reactor to a temperature range between 900° F. (482.2° C.) and 1700° F. (926.7° C.) in an oxygen-starved environment having a sub-stoichiometric oxygen level, whereby the biosolids are gasified.


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