Biological Systems Engineering Department, Virginia Tech, Blacksburg, Virginia, United States of America.
PLoS One. 2007 May 23;2(5):e456. doi: 10.1371/journal.pone.0000456.
The future hydrogen economy offers a compelling energy vision, but there are four main obstacles: hydrogen production, storage, and distribution, as well as fuel cells. Hydrogen production from inexpensive abundant renewable biomass can produce cheaper hydrogen, decrease reliance on fossil fuels, and achieve zero net greenhouse gas emissions, but current chemical and biological means suffer from low hydrogen yields and/or severe reaction conditions.
METHODOLOGY/PRINCIPAL FINDINGS: Here we demonstrate a synthetic enzymatic pathway consisting of 13 enzymes for producing hydrogen from starch and water. The stoichiometric reaction is C(6)H(10)O(5) (l)+7 H(2)O (l)-->12 H(2) (g)+6 CO(2) (g). The overall process is spontaneous and unidirectional because of a negative Gibbs free energy and separation of the gaseous products with the aqueous reactants.
Enzymatic hydrogen production from starch and water mediated by 13 enzymes occurred at 30 degrees C as expected, and the hydrogen yields were much higher than the theoretical limit (4 H(2)/glucose) of anaerobic fermentations.
The unique features, such as mild reaction conditions (30 degrees C and atmospheric pressure), high hydrogen yields, likely low production costs ($ approximately 2/kg H(2)), and a high energy-density carrier starch (14.8 H(2)-based mass%), provide great potential for mobile applications. With technology improvements and integration with fuel cells, this technology also solves the challenges associated with hydrogen storage, distribution, and infrastructure in the hydrogen economy.
未来的氢能经济提供了一个引人注目的能源愿景,但存在四个主要障碍:氢气的生产、储存和分配,以及燃料电池。从廉价丰富的可再生生物质中生产氢气可以生产更便宜的氢气,减少对化石燃料的依赖,并实现零净温室气体排放,但目前的化学和生物学方法存在氢气产量低和/或反应条件苛刻的问题。
方法/主要发现:在这里,我们展示了一种由 13 种酶组成的合成酶途径,用于从淀粉和水中生产氢气。计量反应为 C(6)H(10)O(5)(l)+7 H(2)O(l)-->12 H(2)(g)+6 CO(2)(g)。由于 Gibbs 自由能为负和气态产物与水相反应物的分离,整个过程是自发的和单向的。
通过 13 种酶从淀粉和水中进行的酶法产氢在 30°C 下如预期那样发生,并且氢气产率远高于厌氧发酵的理论极限(4 H(2)/glucose)。
温和的反应条件(30°C 和大气压)、高氢气产率、可能的低成本(约 2 美元/千克 H(2))和高能量密度载体淀粉(基于 14.8 H(2)的质量%)等独特特点,为移动应用提供了巨大的潜力。随着技术的改进和与燃料电池的集成,该技术还解决了氢能经济中与氢气储存、分配和基础设施相关的挑战。