US2017166930A1PendingUtilityA1
Syngas biomethanation process and anaerobic digestion system
Est. expiryJan 23, 2032(~5.5 yrs left)· nominal 20-yr term from priority
C02F 3/28C05F 11/00Y10T137/85978C02F 11/10C02F 11/04C10K 1/04C10B 53/02C02F 2203/00Y02P20/145C02F 11/121C12P 5/023C10B 53/00C02F 3/12Y02W10/40C05D 9/00C02F 3/2893C02F 11/13Y02W30/40Y02E50/10Y02E50/30
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Claims
Abstract
An anaerobic digester is fed a feedstock, for example sludge from a municipal wastewater treatment plant, and produces a digestate. The digestate is dewatered into a cake. The cake may be dried further, for example in a thermal drier. The cake is treated in a pyrolysis system to produce a synthesis gas and biochar. The gas is sent to the same or another digester to increase its methane production. The char may be used as a soil enhancer.
Claims
exact text as granted — not AI-modifiedWe claim:
1 . A process comprising steps of,
a) producing a synthesis gas from pyrolysis of a feedstock; and, b) adding the synthesis gas to an anaerobic digester.
2 . The process of claim 1 wherein the feedstock comprises one or more of a raw biomass, wood, municipal yard waste, municipal solids waste, primary sludge from a wastewater treatment plant, waste activated sludge from a wastewater treatment plant or an agricultural waste or residue.
3 . The process of claim 1 wherein the feedstock comprises digestate.
4 . The process of claim 3 wherein the digestate is produced by the anaerobic digester.
5 . The process of claim 1 wherein the anaerobic digester is coupled with or part of a municipal wastewater treatment plant, or an agricultural or industrial digester.
6 . The process of claim 1 wherein the synthesis gas is cooled before it is fed to the digester.
7 . The process of claim 1 wherein condensable organic compounds are removed from the synthesis gas and returned as feedstock to step a).
8 . An apparatus for transferring syngas to digestate comprising,
a) a pipe between a source of digestate and a digester; b) a pump to create a flow of digestate in the pipe; c) an ejector, microbubble pump or gas transfer membrane in communication with pipe having an inlet connected to a source of the syngas.
9 . The apparatus of claim 8 wherein the source of digestate is the digester.
10 . The apparatus of claim 8 wherein the pipe is connected to multiple outlets in the digester.
11 . The apparatus of claim 8 wherein the inlet is further connected to the headspace of the digester.
12 . The apparatus of claim 8 further comprising a heat exchanger between the ejector and the source of the syngas.
13 . The apparatus of claim 12 wherein the heat exchange provides heat to a digestate cake drier.
14 . A process and apparatus for treating wastewater comprising,
a) treating the wastewater to generate a sludge; b) feeding the sludge to an anaerobic digester to produce biogas and digestate; c) dewatering the digestate to produce a cake; d) thermally drying the cake to produce a dried cake; e) pyrolysing the dried cake to produce char and syngas; f) feeding the syngas to the anaerobic digester.
15 . The process of claim 14 further comprising extracting heat from the syngas and using the extracted heat in step d).
16 . The process of claim 14 comprising using the char as a soil enhancer.
17 . The process of claim 14 comprising steps of extracting a condensable gas from the syngas, pyrolysing the condensable gas to produce additional syngas, and feeding the additional syngas to the digester.
18 . The process of claim 14 wherein step e) is conducted at a temperature of 250 degrees C. or more.
19 . The process of claim 14 wherein the syngas includes one or more vapors and step f) comprises condensing the one or more vapors on contact with a digestate from the anaerobic digester.Join the waitlist — get patent alerts
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