R. Hirschmann, W. Reule, T. Oppenländer, F. Baganz, V. Hass
{"title":"将芳香化合物的全细胞生物转化转化为一种新的生物炼制概念","authors":"R. Hirschmann, W. Reule, T. Oppenländer, F. Baganz, V. Hass","doi":"10.5772/INTECHOPEN.88158","DOIUrl":null,"url":null,"abstract":"The synthesis of aroma compounds that are utilized as precursors of multiple synthesis chains in the pharmaceutical industries and as ingredients in food and fragrance industries can be carried out using chemical processes, enzyme biocatalysis and whole cell biotransformation. Whole cell biotransformation has the potential of being more environmentally benign than chemical synthesis and more cost-effective as compared to enzyme catalysis. In a recently published study by the authors, the aroma compound Ethyl(3)hydroxybutyrate was produced by whole cell biotransformation under aerobic and anaerobic conditions. The yield of the anaerobic processes was similar to that of the aerobic processes, but additionally generated CO 2 and ethanol as useful by-products. In this chapter we illustrate how the production process of Ethyl(3)hydroxybutyrate by whole cell biotransformation can be integrated into a novel biorefinery concept, based on the finding that the production of Ethyl(3)hydroxybutyrate under anaerobic conditions is efficient and environmentally friendly. CO 2 may be converted to bio-methane together with H 2 produced from excess regenerative power. A life cycle assessment confirmed that the anaerobic whole cell biotransformation process embedded into a biorefinery concept including bio-methane production has a lower environmental impact as compared to a concept based on the aerobic whole cell biotransformation. E3HB could be produced. In the anaerobic process, 14.8 g L −1 E3HB and 41.6 g L −1 ethanol were produced. The yield Y E3HB/EAA for the anaerobic process was 0.78 as compared to 0.92 for the aerobic process. These results show that the biotransformation may be conducted aerobically as well as anaerobically, although up to now it was usually conducted aerobically.","PeriodicalId":352923,"journal":{"name":"Biorefinery Concepts, Energy and Products","volume":"1 1","pages":"0"},"PeriodicalIF":0.0000,"publicationDate":"2019-08-14","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Integrating Whole Cell Biotransformation of Aroma Compounds into a Novel Biorefinery Concept\",\"authors\":\"R. Hirschmann, W. Reule, T. Oppenländer, F. Baganz, V. Hass\",\"doi\":\"10.5772/INTECHOPEN.88158\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"The synthesis of aroma compounds that are utilized as precursors of multiple synthesis chains in the pharmaceutical industries and as ingredients in food and fragrance industries can be carried out using chemical processes, enzyme biocatalysis and whole cell biotransformation. Whole cell biotransformation has the potential of being more environmentally benign than chemical synthesis and more cost-effective as compared to enzyme catalysis. In a recently published study by the authors, the aroma compound Ethyl(3)hydroxybutyrate was produced by whole cell biotransformation under aerobic and anaerobic conditions. The yield of the anaerobic processes was similar to that of the aerobic processes, but additionally generated CO 2 and ethanol as useful by-products. In this chapter we illustrate how the production process of Ethyl(3)hydroxybutyrate by whole cell biotransformation can be integrated into a novel biorefinery concept, based on the finding that the production of Ethyl(3)hydroxybutyrate under anaerobic conditions is efficient and environmentally friendly. CO 2 may be converted to bio-methane together with H 2 produced from excess regenerative power. A life cycle assessment confirmed that the anaerobic whole cell biotransformation process embedded into a biorefinery concept including bio-methane production has a lower environmental impact as compared to a concept based on the aerobic whole cell biotransformation. E3HB could be produced. In the anaerobic process, 14.8 g L −1 E3HB and 41.6 g L −1 ethanol were produced. The yield Y E3HB/EAA for the anaerobic process was 0.78 as compared to 0.92 for the aerobic process. These results show that the biotransformation may be conducted aerobically as well as anaerobically, although up to now it was usually conducted aerobically.\",\"PeriodicalId\":352923,\"journal\":{\"name\":\"Biorefinery Concepts, Energy and Products\",\"volume\":\"1 1\",\"pages\":\"0\"},\"PeriodicalIF\":0.0000,\"publicationDate\":\"2019-08-14\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Biorefinery Concepts, Energy and Products\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://doi.org/10.5772/INTECHOPEN.88158\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"\",\"JCRName\":\"\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Biorefinery Concepts, Energy and Products","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.5772/INTECHOPEN.88158","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 0
摘要
利用化学工艺、酶生物催化和全细胞生物转化,可以合成在制药工业中用作多个合成链前体的芳香化合物,以及在食品和香料工业中用作成分。与化学合成相比,全细胞生物转化具有更环保的潜力,与酶催化相比更具成本效益。在作者最近发表的一项研究中,芳香化合物乙酯(3)羟基丁酸酯在有氧和厌氧条件下通过全细胞生物转化产生。厌氧过程的产率与好氧过程相似,但额外产生co2和乙醇作为有用的副产物。在本章中,我们基于发现在厌氧条件下生产羟基丁酸乙酯是高效和环保的,说明了如何将全细胞生物转化生产羟基丁酸乙酯的过程整合到一个新的生物炼制概念中。二氧化碳和过量再生能量产生的氢可以转化为生物甲烷。一项生命周期评估证实,与基于有氧全细胞生物转化的概念相比,包含生物甲烷生产在内的生物炼制概念中的厌氧全细胞生物转化过程对环境的影响更小。可以得到E3HB。厌氧工艺产E3HB 14.8 g L−1,乙醇41.6 g L−1。厌氧工艺的E3HB/EAA产率为0.78,好氧工艺为0.92。这些结果表明,生物转化既可以进行好氧转化,也可以进行厌氧转化,尽管到目前为止通常是好氧转化。
Integrating Whole Cell Biotransformation of Aroma Compounds into a Novel Biorefinery Concept
The synthesis of aroma compounds that are utilized as precursors of multiple synthesis chains in the pharmaceutical industries and as ingredients in food and fragrance industries can be carried out using chemical processes, enzyme biocatalysis and whole cell biotransformation. Whole cell biotransformation has the potential of being more environmentally benign than chemical synthesis and more cost-effective as compared to enzyme catalysis. In a recently published study by the authors, the aroma compound Ethyl(3)hydroxybutyrate was produced by whole cell biotransformation under aerobic and anaerobic conditions. The yield of the anaerobic processes was similar to that of the aerobic processes, but additionally generated CO 2 and ethanol as useful by-products. In this chapter we illustrate how the production process of Ethyl(3)hydroxybutyrate by whole cell biotransformation can be integrated into a novel biorefinery concept, based on the finding that the production of Ethyl(3)hydroxybutyrate under anaerobic conditions is efficient and environmentally friendly. CO 2 may be converted to bio-methane together with H 2 produced from excess regenerative power. A life cycle assessment confirmed that the anaerobic whole cell biotransformation process embedded into a biorefinery concept including bio-methane production has a lower environmental impact as compared to a concept based on the aerobic whole cell biotransformation. E3HB could be produced. In the anaerobic process, 14.8 g L −1 E3HB and 41.6 g L −1 ethanol were produced. The yield Y E3HB/EAA for the anaerobic process was 0.78 as compared to 0.92 for the aerobic process. These results show that the biotransformation may be conducted aerobically as well as anaerobically, although up to now it was usually conducted aerobically.