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折流板反应器中硫化物生成型挥发性脂肪酸的降解

Sulfidogenic volatile fatty acid degradation in a baffled reactor.

作者信息

Vallero M V G, Lens P N L, Bakker C, Lettinga G

机构信息

Sub-department of Environmental Technology, Wageningen University and Research Centre, Bomenweg 2, P.O. Box 8129, 6700 EV Wageningen, The Netherlands.

出版信息

Water Sci Technol. 2003;48(3):81-8.

Abstract

The effect of staging the sludge bed on volatile fatty acid degradation by sulfidogenic reactors was evaluated in a baffled reactor. In a 5.4 l baffled reactor, containing three equal compartments, a volatile fatty acid (VFA) mixture (acetate:propionate:butyrate ratio 1:2:2 on COD basis; pH 8) was treated under mesophilic (30 degrees C) and sulfidogenic (COD:SO4(2-) ratio: 0.5) conditions for 38 days. At a specific sludge loading rate of 0.50 g COD.gVSS(-1) x d(-1), a COD and sulfate removal of 85% and 30%, respectively, was obtained. In the baffled reactor, staging of the sulfidogenic VFA degradation occurred. Propionate and butyrate were mainly degraded in the first compartment. Their degradation was incomplete, resulting in elevated acetate concentrations in compartment I. In the second and third compartment of the baffled reactor, a net degradation of acetate took place. Acetate was the sole substrate present in compartment III and residual acetate concentrations of about 200 mg/l were present in the effluent at a specific sludge loading of 0.50 g COD x gVSS(-1) x d(-1). Sludges with different maximum specific VFA and acetate degrading activities developed in the first and second compartment. These maximal specific activities were almost equal for sludge present in compartment II and III.

摘要

在一个折流板反应器中评估了污泥床分段对产硫化物反应器中挥发性脂肪酸降解的影响。在一个5.4升的折流板反应器中,该反应器包含三个相等的隔室,在中温(30℃)和产硫化物(COD:SO4(2-) 比例为0.5)条件下,对一种挥发性脂肪酸(VFA)混合物(基于COD,乙酸盐:丙酸盐:丁酸盐比例为1:2:2;pH值为8)进行了38天的处理。在特定污泥负荷率为0.50 g COD·gVSS(-1)×d(-1)时,COD和硫酸盐的去除率分别为85%和30%。在折流板反应器中,产硫化物的VFA降解发生了分段。丙酸盐和丁酸盐主要在第一个隔室中降解。它们的降解不完全,导致隔室I中乙酸盐浓度升高。在折流板反应器的第二个和第三个隔室中,乙酸盐发生了净降解。乙酸盐是隔室III中存在的唯一底物,在特定污泥负荷为0.50 g COD·gVSS(-1)×d(-1)时,流出物中残留的乙酸盐浓度约为200 mg/l。在第一个和第二个隔室中形成了具有不同最大比VFA和乙酸盐降解活性的污泥。隔室II和III中存在的污泥的这些最大比活性几乎相等。

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