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Systems and methods for cyclic operations in a fuel synthesis process

a fuel synthesis and cyclic operation technology, applied in the field of solar-driven systems, methods and apparatus for refining biomass and other materials, can solve the problems of limited conversion and still lower yield, and achieve the effect of increasing the output of a train, and rapid and efficient reactor cycling

Inactive Publication Date: 2010-09-30
SUNDROP FUELS
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0006]In some embodiments, a fuel synthesis system including a multiple methanol reactor train, operated in parallel from a common input of 1) synthesis gas from a solar driven chemical reactor and 2) synthesis gas from a storage tank. Some embodiments may include a controller to control operation of the multiple methanol trains by potentially idling one or more of the methanol reactor trains or reducing output of the trains based on a lower amount of synthesis gas being generated by the solar driven chemical reactor, or switching an idle train to an operational state or increasing output of a train when the amount of syngas gas is higher, both of which are subject to marked variations in volume of synthesis gas output based on a seasonal, diurnal and weather effects. Additionally, in some embodiments the multiple methanol reactor trains are idled as needed based on a variable amount of synthesis gas fed into the process.
[0007]In some embodiments, a fuel synthesis system can include control algorithms on reactor operation. The control algorithms may specifically allow rapid and efficient reactor cycling. This can be by using synthesis gas from a solar driven chemical reactor. Additionally, synthesis gas from a storage tank may provide for rapid and efficient reactor cycling, e.g., by maintaining reactor temperature. Recycling synthesis gas and methanol product gas from the outlet of the reactor trains can also be used to keep at least one of the trains operating at some percent of its maximum throughput.

Problems solved by technology

Between 30% and 40% of the biomass must be consumed to drive the process, and at the temperatures which the process is generally limited to (for efficiency reasons), conversion is typically limited, giving still lower yields.

Method used

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Embodiment Construction

[0016]In the following description, numerous specific details are set forth, such as examples of specific data signals, named components, connections, number of reactor tubes, etc., in order to provide a thorough understanding of the present invention. It will be apparent, however, to one of ordinary skill in the art that the present invention may be practiced without these specific details. In other instances, well known components or methods have not been described in detail but rather in a block diagram in order to avoid unnecessarily obscuring the present invention. Further, specific numeric references such as first reactor tube, may be made. However, the specific numeric reference should not be interpreted as a literal sequential order but rather interpreted that the first reactor tube is different from a second reactor tube. Thus, the specific details set forth are merely exemplary. The specific details may be varied from and still be contemplated to be within the spirit and s...

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Abstract

A method, apparatus, and system for a fuel synthesis system including a multiple methanol reactor train, operated in parallel from a common input of 1) synthesis gas from a solar driven chemical reactor and 2) synthesis gas from a storage tank. In some embodiments, the multiple methanol reactor trains are idled as needed based on a variable amount of synthesis gas fed into the process. Additionally, some embodiments may include a controller to control operation of the multiple methanol trains by potentially idling one or more of the methanol reactor trains, switching to an operational state, or altering the output from the reactor trains, based on the amount of synthesis gas being generated by the solar driven chemical reactor, which is subject to marked variations in volume of synthesis gas output based on a seasonal, diurnal and weather effects.

Description

RELATED APPLICATIONS[0001]This application claims the benefit of both U.S. Provisional Patent Application Ser. No. 61 / 248,282, filed Oct. 2, 2009 and entitled “VARIOUS METHODS AND APPARATUSES FOR SUN DRIVEN PROCESSES,” and U.S. Provisional Patent Application Ser. No 61 / 185,492, entitled “VARIOUS METHODS AND APPARATUSES FOR SOLAR-THERMAL GASIFICATION OF BIOMASS TO PRODUCE SYNTHESIS GAS” filed Jun. 9, 2009.NOTICE OF COPYRIGHT[0002]A portion of the disclosure of this patent document contains material that is subject to copyright protection. The copyright owner has no objection to the facsimile reproduction by anyone of the software engine and its modules, as it appears in the Patent and Trademark Office Patent file or records, but otherwise reserves all copyright rights whatsoever.FIELD OF THE INVENTION[0003]Embodiments of the invention generally relate to systems, methods, and apparatus for refining biomass and other materials. More particularly, an aspect of an embodiment of the inve...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): B01J19/00C07C1/04F24S20/20F24S20/30
CPCC01B3/22C10J3/56C01B2203/0216C01B2203/061C01B2203/84C07C29/15C10G2/30C10J3/00C10J3/482C10J3/485C10J3/723C10J2200/09C10J2300/0906C10J2300/0909C10J2300/0916C10J2300/0973C10J2300/0989C10J2300/1284C10J2300/1292C10J2300/1621C10J2300/1659C10J2300/1665C10J2300/1693F24J2/07Y02E10/41Y02E50/18Y02E50/32C01B3/34C10J3/54Y02B40/18C10G2300/1014C10G2300/1025C10G2300/807C07C31/04C07C29/1518C10G2/32C10G3/00C10L1/04C10L2200/0492C10L2290/02C10L2290/04C10L2290/06C10L2290/08C10L2290/28C10L2290/42C10L2290/50C10L2290/52C10L2290/547F24S20/20Y02E10/40Y02E50/10Y02E50/30Y02P20/129Y02P20/133Y02P20/145Y02P20/50Y02P30/20Y02T50/678B01J19/0013B01J19/0033B01J19/2445B01J19/245B01J2219/00117B01J2219/00186C01B3/384C01B2203/0233C01B2203/0811C01B2203/1241C01B2203/1685C10J3/466C10J3/506C10J3/58C10J3/60C10J3/62C10J3/721C10J3/82C10J3/84C10J2200/15C10J2200/158C10J2300/094C10J2300/0976C10J2300/0993C10J2300/1223C10J2300/123C10J2300/1853C10J2300/1861C10K1/024
Inventor HILTON, COURTLAND
Owner SUNDROP FUELS
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