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从源分离尿液中电化学回收氨用于微生物蛋白质生产。

Electrochemical Ammonia Recovery from Source-Separated Urine for Microbial Protein Production.

机构信息

Center for Microbial Ecology and Technology (CMET), Ghent University , Coupure Links 653, B-9000 Gent, Belgium.

出版信息

Environ Sci Technol. 2017 Nov 21;51(22):13143-13150. doi: 10.1021/acs.est.7b02819. Epub 2017 Nov 7.

Abstract

Conventional plant and meat protein production have low nitrogen usage efficiencies and high energy needs. Microbial protein (MP) is an alternative that offers higher nitrogen conversion efficiencies with low energy needs if nitrogen is recovered from a concentrated waste source such as source-separated urine. An electrochemical cell (EC) was optimized for ammonia recovery as NH/H gas mixtures usable for MP production. Undiluted hydrolyzed urine was fed to the caustic-generating cathode compartment for ammonia stripping with redirection to the anode compartment for additional ammonium extraction. Using synthetic urine at 48 A m the nitrogen removal efficiency reached 91.6 ± 2.1%. Tests with real urine at 20 A m, achieved 87.1 ± 6.0% and 68.4 ± 14.6% requiring 5.8 and 13.9 kWh kg N recovered, via absorption in acid or MP medium, respectively. Energy savings through accompanying electrolytic H and O production were accounted for. Subsequently, MP was grown in fed-batch on MP medium with conventional NH or urine-derived NH yielding 3.74 ± 1.79 and 4.44 ± 1.59 g CDW L, respectively. Dissolution of gaseous NH in MP medium maintained neutral pH in the MP reactor preventing caustic addition and thus salt accumulation. Urine-nitrogen could thus be valorized as MP via electrochemical ammonia recovery.

摘要

传统的植物和肉类蛋白生产的氮利用率低,能源需求高。微生物蛋白(MP)是一种替代蛋白,它可以从浓缩的废物源(如分离的尿液源)中回收氮,如果使用从浓缩的废物源(如分离的尿液源)中回收氮,它具有更高的氮转化效率和低能源需求。优化了一种电化学电池(EC)用于氨回收,以获得可用于 MP 生产的 NH/H 气体混合物。将未经稀释的水解尿液进料到产生苛性碱的阴极室,用于氨汽提,并将其 redirected 到阳极室,以进行额外的铵提取。在 48 A m 的条件下,使用合成尿液时,氮去除效率达到 91.6 ± 2.1%。在 20 A m 的条件下用实际尿液进行测试,分别达到 87.1 ± 6.0%和 68.4 ± 14.6%,通过分别在酸或 MP 介质中吸收,需要回收 5.8 和 13.9 kWh kg N。考虑了通过伴随的电解 H 和 O 生产而节省的能源。随后,在 MP 培养基中以 MP 介质进行 fed-batch 培养,使用传统的 NH 或尿液衍生的 NH 分别产生 3.74 ± 1.79 和 4.44 ± 1.59 g CDW L。气态 NH 在 MP 介质中的溶解使 MP 反应器中的 pH 保持中性,从而防止添加苛性碱和因此盐的积累。尿液中的氮可以通过电化学氨回收转化为 MP。

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