ES2656790T3 - Microorganismos para la producción de ácido adípico y otros compuestos - Google Patents
Microorganismos para la producción de ácido adípico y otros compuestos Download PDFInfo
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- C12Y101/01—Oxidoreductases acting on the CH-OH group of donors (1.1) with NAD+ or NADP+ as acceptor (1.1.1)
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Abstract
Un organismo microbiano de origen sintético, que comprende un organismo microbiano que tiene una ruta para convertir adipil-CoA en ácido 6-aminocaproico (ruta de ácido 6-aminocaproico) y al menos una ruta para producir adipil-CoA (ruta adipil-CoA), comprendiendo dicha ruta de ácido 6-aminocaproico dos ácidos nucleicos exógenos que codifican cada uno una enzima de la ruta de ácido 6-aminocaproico expresada en una cantidad suficiente para producir ácido 6-aminocaproico, comprendiendo dicha ruta de ácido 6-aminocaproico aldehído deshidrogenasa dependiente de CoA, y transaminasa o 6-aminocaproato deshidrogenasa, en el que dicha al menos una ruta de adipil-CoA comprende al menos una de una ruta para convertir adipato en adipil CoA y una ruta para convertir succinil-CoA más acetil-CoA en adipil-CoA, en el que dicha ruta para convertir adipato en adipil CoA comprende adipil-CoA sintetasa o fosfotransadipilasa/adipato cinasa; y en el que dicha ruta para convertir succinil-CoA más acetil-CoA en adipil-CoA comprende succinil-CoA:acetil-CoA acil transferasa, 3-oxoadipil-CoA transferasa, 3-oxoadipato reductasa, 3-hidroxiadipato deshidratasa, 2-enoato reductasa, y adipil-CoA sintetasa, fosfotransadipilasa/adipato cinasa, adipil-CoA:acetil-CoA transferasa o adipil-CoA hidrolasa.
Description
han descrito previamente y se conocen bien en la técnica. Las condiciones aerobias y anaerobias ejemplares se describen, por ejemplo, en la Solicitud de Patente de Estados Unidos N.º de serie 11/891.602, presentada el 10 de agosto de 2007. Las fermentaciones pueden realizarse de forma discontinua, en lote alimentado o de forma continua, como se divulga en el presente documento.
5 Si se desea, el pH del medio se puede mantener a un pH deseado, en particular pH neutro, como un pH de aproximadamente 7 mediante la adición de una base, tal como NaOH u otras bases, o ácido, según sea necesario para mantener el medio de cultivo a un pH deseable. La velocidad de crecimiento puede determinarse midiendo la densidad óptica usando un espectrofotómetro (600 nm), y la tasa de captación de glucosa controlando el
10 agotamiento de la fuente de carbono a lo largo del tiempo.
El medio de crecimiento puede ser, por ejemplo, cualquier fuente de carbohidratos que pueda suministrar una fuente de carbono al microorganismo de origen sintético. Dichas fuentes incluyen, por ejemplo, azúcares tales como glucosa, xilosa, arabinosa, galactosa, manosa, fructosa y almidón. Otras fuentes de carbohidratos incluyen, por 15 ejemplo, materias primas renovables y biomasa. Los tipos ejemplares de biomasas que se pueden usar como materias primas en los métodos de la invención incluyen biomasa celulósica, biomasa hemicelulósica y materias primas de lignina o porciones de materias primas. Dichas materias primas de biomasa contienen, por ejemplo, sustratos de carbohidratos útiles como fuentes de carbono tales como glucosa, xilosa, arabinosa, galactosa, manosa, fructosa y almidón. Dadas las enseñanzas y la orientación proporcionadas en el presente documento, los
20 expertos en la técnica entenderán que las materias primas renovables y la biomasa distintas de las ilustradas anteriormente también pueden usarse para cultivar los organismos microbianos de la invención para la producción de adipato, ácido 6-aminocaproico o caprolactama.
Además de materias primas renovables tales como las ilustradas anteriormente, los organismos microbianos de
25 adipato, ácido 6-aminocaproico o caprolactama de la invención también pueden modificarse para su crecimiento en singás como su fuente de carbono. En esta realización específica, una o más proteínas o enzimas se expresan en los organismos productores de adipato, ácido 6-aminocaproico o caprolactama para proporcionar una ruta metabólica para la utilización de singás u otra fuente de carbono gaseoso.
30 El gas de síntesis, también conocido como singás o gas productor, es el producto principal de la gasificación de carbón y de materiales carbonosos tales como materiales de biomasa, incluyendo cultivos agrícolas y residuos. El singás es una mezcla principalmente de H2 y CO y puede obtenerse a partir de la gasificación de cualquier materia prima orgánica, incluyendo, pero sin limitación, carbón, aceite de carbón, gas natural, biomasa y materia orgánica residual. La gasificación generalmente se realiza bajo una alta relación de combustible con respecto a oxígeno.
35 Aunque principalmente contiene H2 y CO, el singás también puede incluir CO2 y otros gases en cantidades inferiores. Por lo tanto, el gas de síntesis proporciona una fuente rentable de carbono gaseoso tal como CO y, adicionalmente, CO2.
La ruta de Wood-Ljungdahl cataliza la conversión de CO y H2 en acetil-CoA y otros productos, tal como acetato. Los
40 organismos capaces de utilizar CO y singás también tienen generalmente la capacidad de utilizar CO2 y mezclas de CO2/H2 a través del mismo conjunto básico de enzimas y transformaciones incluidas por la ruta de Wood-Ljungdahl. La conversión dependiente de H2 de CO2 en acetato por microorganismos se reconoció mucho antes de que se revelara que el CO también podría ser utilizado por los mismos organismos y que estaban implicadas las mismas rutas. Se ha demostrado que muchos acetógenos crecen en presencia de CO2 y producen compuestos tales como
45 el acetato, siempre que haya hidrógeno presente para suministrar los equivalentes reductores necesarios (véase, por ejemplo, Drake, Acetogenesis, págs. 3-60 Chapman y Hall, Nueva York, (1994)). Esto se puede resumir por la siguiente ecuación:
2 CO2 + 4 H2 + n ADP + n Pi → CH3COOH + 2 H2O + n ATP
50 Por lo tanto, los microorganismos de origen sintético que poseen la ruta de Wood-Ljungdahl pueden utilizar mezclas de CO2 y H2, también para la producción de acetil-CoA y otros productos deseados.
La ruta de Wood-Ljungdahl se conocen bien en la técnica y consiste en 12 reacciones que pueden separarse en dos
55 ramificaciones: (1) ramificación de metilo y (2) ramificación de carbonilo. La ramificación de metilo convierte el singás en metil-tetrahidrofolato (metil-THF), mientras que la ramificación de carbonilo convierte el metil-THF en acetil-CoA. Las reacciones en la ramificación de metilo son catalizadas en orden por las siguientes enzimas: ferredoxina oxidorreductasa, formato deshidrogenasa, formiltetrahidrofolato sintetasa, meteniltetrahidrofolato ciclodeshidratasa, metilentetrahidrofolato deshidrogenasa y metilentetrahidrofolato reductasa. Las reacciones en la ramificación de
15
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Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US4005908P | 2008-03-27 | 2008-03-27 | |
| US40059P | 2008-03-27 | ||
| PCT/US2009/038663 WO2009151728A2 (en) | 2008-03-27 | 2009-03-27 | Microorganisms for the production of adipic acid and other compounds |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| ES2656790T3 true ES2656790T3 (es) | 2018-02-28 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ES09763021.4T Active ES2656790T3 (es) | 2008-03-27 | 2009-03-27 | Microorganismos para la producción de ácido adípico y otros compuestos |
Country Status (14)
| Country | Link |
|---|---|
| US (11) | US7799545B2 (es) |
| EP (2) | EP3351619A1 (es) |
| JP (6) | JP5951990B2 (es) |
| CN (4) | CN106119112B (es) |
| BR (1) | BRPI0910928A2 (es) |
| CA (3) | CA3175935A1 (es) |
| DK (1) | DK2265709T3 (es) |
| ES (1) | ES2656790T3 (es) |
| HU (1) | HUE035611T2 (es) |
| LT (1) | LT2265709T (es) |
| NO (1) | NO2265709T3 (es) |
| PL (1) | PL2265709T3 (es) |
| SI (1) | SI2265709T1 (es) |
| WO (1) | WO2009151728A2 (es) |
Families Citing this family (142)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2008091627A2 (en) | 2007-01-22 | 2008-07-31 | Genomatica, Inc. | Methods and organisms for growth-coupled production of 3-hydroxypropionic acid |
| WO2009045637A2 (en) | 2007-08-10 | 2009-04-09 | Genomatica, Inc. | Methods for the synthesis of acrylic acid and derivatives from fumaric acid |
| CN107090424A (zh) | 2008-01-22 | 2017-08-25 | 基因组股份公司 | 利用合成气或其它气态碳源和甲醇的方法和有机体 |
| EP3450550A1 (en) | 2008-03-05 | 2019-03-06 | Genomatica, Inc. | Primary alcohol producing organisms |
| CN109468348B (zh) | 2008-03-11 | 2023-05-16 | 基因组股份公司 | 己二酸酯或硫代酯合成 |
| PL2265709T3 (pl) | 2008-03-27 | 2018-05-30 | Genomatica, Inc. | Mikroorganizmy do produkcji kwasu adypinowego i innych związków |
| WO2009135074A2 (en) * | 2008-05-01 | 2009-11-05 | Genomatica, Inc. | Microorganisms for the production of methacrylic acid |
| WO2009155382A1 (en) | 2008-06-17 | 2009-12-23 | Genomatica, Inc. | Microorganisms and methods for the biosynthesis of fumarate, malate, and acrylate |
| US20100184173A1 (en) * | 2008-11-14 | 2010-07-22 | Genomatica, Inc. | Microorganisms for the production of methyl ethyl ketone and 2-butanol |
| AU2009324422A1 (en) | 2008-12-12 | 2011-07-07 | Celexion, Llc | Biological synthesis of difunctional alkanes from alpha ketoacids |
| CA2746952A1 (en) | 2008-12-16 | 2010-06-24 | Genomatica, Inc. | Microorganisms and methods for conversion of syngas and other carbon sources to useful products |
| EP2210935A1 (en) * | 2009-01-19 | 2010-07-28 | Deinove | Methods for isolating bacteria |
| US8404465B2 (en) | 2009-03-11 | 2013-03-26 | Celexion, Llc | Biological synthesis of 6-aminocaproic acid from carbohydrate feedstocks |
| BRPI1013505A2 (pt) | 2009-04-30 | 2018-02-14 | Genomatica Inc | organismos para a produção de isopropanol, n-butanol, e isobutanol |
| EP3865569B1 (en) | 2009-04-30 | 2023-10-04 | Genomatica, Inc. | Organisms for the production of 1,3-butanediol |
| WO2010129936A1 (en) | 2009-05-07 | 2010-11-11 | Genomatica, Inc. | Microorganisms and methods for the biosynthesis of adipate, hexamethylenediamine and 6-aminocaproic acid |
| KR20120036851A (ko) * | 2009-05-15 | 2012-04-18 | 게노마티카 인코포레이티드 | 사이클로헥사논의 제조를 위한 유기체 |
| WO2010144746A2 (en) | 2009-06-10 | 2010-12-16 | Genomatica, Inc. | Microorganisms and methods for carbon-efficient biosynthesis of mek and 2-butanol |
| AU2010259937B2 (en) | 2009-06-13 | 2016-07-14 | Archer-Daniels-Midland Company | Production of adipic acid and derivatives from carbohydrate-containing materials |
| AU2010259935B2 (en) | 2009-06-13 | 2016-05-26 | Archer-Daniels-Midland Company | Production of glutaric acid and derivatives from carbohydrate-containing materials |
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| WO2009155382A1 (en) | 2008-06-17 | 2009-12-23 | Genomatica, Inc. | Microorganisms and methods for the biosynthesis of fumarate, malate, and acrylate |
| WO2010022763A1 (en) | 2008-08-25 | 2010-03-04 | Metabolic Explorer | Method for the preparation of 2-hydroxy-isobutyrate |
| US8357826B2 (en) | 2008-10-16 | 2013-01-22 | Karl Kharas | Methods and apparatus for synthesis of alcohols from syngas |
| CN102317437B (zh) | 2008-12-12 | 2013-08-21 | 麦特波力克斯公司 | 用于制备聚(5-羟基戊酸)和5碳化合物的绿色工艺和组合物 |
| CA2746952A1 (en) | 2008-12-16 | 2010-06-24 | Genomatica, Inc. | Microorganisms and methods for conversion of syngas and other carbon sources to useful products |
| TW201037078A (en) * | 2009-03-11 | 2010-10-16 | Dsm Ip Assets Bv | Preparation of alpha-ketopimelic acid |
| WO2010129936A1 (en) | 2009-05-07 | 2010-11-11 | Genomatica, Inc. | Microorganisms and methods for the biosynthesis of adipate, hexamethylenediamine and 6-aminocaproic acid |
| BRPI1010581A2 (pt) | 2009-06-04 | 2016-11-08 | Genomatica Inc | micro-organismos para a produção de 1,4-butanodiol e métodos relacionados |
| CN102753698A (zh) | 2009-12-10 | 2012-10-24 | 基因组股份公司 | 合成气或其他气态碳源和甲醇转化为1,3-丁二醇的方法和有机体 |
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