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Co-digestion of tanning residues and sludge

机译:制革渣和污泥的共消化

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摘要

Codigestion experiments on sludge from tanneries’ industrial wastewater treatment plant (WWTP) mixed with chromium free (“green”) tanneries solid wastes were carried-out in a 15 m3 pilot plant reactor, operating at 20 days hydraulic retention time (HRT) and at mesophilic temperature (35 ºC). The goal was to evaluate the feasibility of a full-scale unit. Addition of “green” solid wastes improved biodegradability of the sludge and biogas production. The removal efficiencies of organic matter varied, according to the feedstock mixture. Averaged results are: COD and VS more than 55 %; TOC = 69 %. Hydrolysis of suspended volatile solids was initially moderate (36 %), but increased up to about 50 %, when the feedstock contained proteolytic enzymes. Fat removal was quite high (77 %). Biogas production was highly dependent from the fleshing content in the feedstock. Addition of 30 % by weight of fleshing to the sludge increased 4 times the average biogas production (from 3,85 m3/day to 14,62 m3/day). The maximum Biogas production rate was 38 liter/kg of feedstock. Fleshing biogas yield was found to be 630 l/kg Volatile Solids loaded, higher than the value recorded for the sludge (288 l/kg Volatile Solids loaded). Methane content in biogas was about 75 % CH4. The average biogas productivity of the reactor was 1.49 l/l/day. Sulphate removal carried-out by the biologic community (SO4 = ≥ 35%) increased Hydrogen sulphide concentration in the biogas up to 1800 ppm (average), a value higher than the limits allowed for use in internal combustion engines. Grinding and maceration of fleshing was hard, due to smell, repugnant look and high strength of its components. This feedstock must be pre-treated in order to avoid excess hydrogen sulphide and lime. Codigestion of “green” tannery wastes with sludge and others residues revealed technically feasible and a low cost solution for the environmental problem of these residues from small/average tanning factories. The potential biogas production for full scale plant is about 11 000 m3/day, making this solution refundable within 5 years. Codigestion allows substantial reduction in bio solids volume, pathogens, and odor, increasing landfill life. This is an important evolution on current solution and gives time to plan and implement new sustainable projects.
机译:在15 m3的中试工厂反应器中进行制革厂工业废水处理厂(WWTP)的污泥与无铬(“绿色”)制革厂固体污泥的共消化实验,在20天水力停留时间(HRT)下运行中温温度(35ºC)。目的是评估一个完整单位的可行性。添加“绿色”固体废物可改善污泥的生物降解能力和沼气生产。有机物的去除效率根据原料混合物而变化。平均结果是:COD和VS超过55%; TOC = 69%。悬浮的挥发性固体的水解最初是中等程度的(36%),但是当原料中包含蛋白水解酶时,水解率增加到大约50%。脂肪去除率很高(77%)。沼气的生产高度依赖于原料中的肉含量。在污泥中添加按重量计30%的果肉可使平均沼气产量增加4倍(从3,85立方米/天增加至14,62立方米/天)。最高沼气生产速度为38升/千克原料。发现新鲜的沼气产量为630 l / kg挥发性固体,高于记录的污泥值(288 l / kg挥发性固体)。沼气中甲烷含量约为75%CH4。反应器的平均沼气生产率为1.49 l / l / day。生物界对硫酸盐的去除(SO4 =≥35%)使沼气中的硫化氢浓度提高到1800 ppm(平均值),该值高于内燃机允许的限值。由于气味,令人讨厌的外观以及其成分的高强度,果肉的研磨和浸渍很难进行。必须对该原料进行预处理,以避免过量的硫化氢和石灰。制革厂的“绿色”废料与污泥和其他残留物的共消化表明,对于小型/普通制革厂的这些残留物的环境问题,在技术上是可行的且是低成本的解决方案。大规模工厂的潜在沼气产量约为11000立方米/天,因此该解决方案可在5年内退还。共消化可以大大减少生物固体的体积,病原体和气味,从而延长垃圾填埋场的寿命。这是对当前解决方案的重要改进,并给了计划和实施新的可持续项目的时间。

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