Field test of methane fermentation system for treating swine wastes

Field test of methane fermentation system for treating swine wastes
复制标题

DOI:
10.2166/wst.2002.0415
复制
发表时间:
2002-01-01
影响因子:
2.7
通讯作者:
Honda, K
Honda, K
中科院分区:
环境科学与生态学4区
文献类型:
--
作者:
Kataoka, N;Suzuki, T;Honda, K

文献摘要

被引文献

相似文献

开发了一种用于处理猪粪的甲烷发酵系统,并成功地在现场试验工厂进行了演示(0.5 m(3)/d)。该系统由螺旋压脱水机、沼气沼气池、污泥分离器、氧化沟(OD)和堆肥设备组成。采用螺旋压脱水机进行物理预处理,对预处理后的污泥进行甲烷发酵,对消化出水进行OD、总固体(TS)和化学需氧量(CODCr)的去除率分别为38%和22%。筛分的性能为:含水率57%,着火损失93%,比重0.33。经预处理的强浆料在中温条件下进行消化。消化气(沼气)产率为26 m(3)/m(3)-浆(NTP),沼气的甲烷含量为67%。在35℃的温度下,对污泥进行甲烷发酵处理,CODCr去除率为65%。当NH4+-N浓度在3000 mg/l以下时,该体系对甲烷发酵反应无抑制作用。目前中试规模研究的质量平衡表明,1 m(3)的猪粪便和尿液混合物(TS 90 kg/m(3))被生物转化为25 m(3)/m(3)的沼气浆(NTP)(甲烷含量67%),100 kg堆肥(含水量40%)。燃烧损失75%),处理水0.80 m(3) (SS 30-70 mg/l)。
A methane fermentation system for treating swine wastes was developed and successfully demonstrated in a field test plant (0.5 m(3)/d). The system was composed of a screw-press dehydrator, a methanogenic digester, a sludge separator, an oxidation ditch (OD) and composting equipment. A performance evaluation was carried out regarding physical pre-treatment using the screw-press dehydrator, methane fermentation for pre-treated slurry, and post-treatment for digested effluent by OD, Total solids (TS) and chemical oxygen demand (CODCr) removal by the screw-press pre-treatment were 38% and 22%, respectively. Properties of the screenings were as follows: water content 57%, ignition loss 93%, specific gravity 0.33. The pretreated strong slurry was digested under mesophilic conditions. Digestion gas (biogas) production rate was 26 m(3)/m(3)-slurry (NTP) and methane content of the biogas was 67%. CODCr removal of 65% with methane fermentation treatment of the slurry operating at 35degreesC was observed. No inhibition of methane fermentation reaction occurred at the NH4+-N concentration of 3,000 mg/l or less during methane fermentation by the system. Mass balance from the present pilot-scale study showed that 1 m(3) of mixture of excrement and urine of swine waste (TS 90 kg/m(3)) was biologically converted to 25 m(3)/m(3)-slurry (NTP) of biogas (methane content 67%), 100 kg of compost (water content 40%. ignition loss 75%), and 0.80 m(3) of treated water (SS 30-70 mg/l).