Improvement of biogas productivity from distillery wastewater by partial potassium reduction pretreatment using two-step microfiltration and nanofiltration

IF 9 1区 工程技术 Q1 ENERGY & FUELS
Kessara Seneesrisakul , Kittitut Kunta , Krittiya Pornmai , Masahiko Abe , Prapan Ariyamethee , Tanakorn Boonayamanop , Sumaeth Chavadej
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Abstract

The main purpose of the current study was to employ filtration pretreatment to lower the K concentration in distillery wastewater (DW) from a very high level (8800 mg/L) close to severe inhibition (>12000 mg/L) to 4350 mg/L, which was in the moderate toxic range (2500–4500 mg/L) for methanogens. The filtration pretreatment system consisted of the two steps of microfiltration (MF) to remove large solid particles and nanofiltration (NF) to reduce K concentration in the retained DW. Both steps of MF and NF were operated in batch mode with continuous recirculation. The permeate of the MF step was fed to the NF unit in conjunction with different dilution ratios (dilution water volume-to-feed volume) to lower the K content in the retentate. The higher the cumulative dilution ratio, the lower the K concentration in the retentate of the NF step. However, it has to be traded off against the increasing total volume of permeate with the higher cumulative dilution ratio. Thus, at the optimum cumulative dilution ratio of 0.5:1, the DW from filtration pretreatment with a high COD value of 111500 mg/L and a low K content of 4350 mg/L was found to have significantly higher methanogenic productivities in terms of average production rate and yields of both biogas and methane with a higher optimum COD loading rate, as compared to those of the untreated DW. Moreover, the use of the two-step filtration in this investigation could significantly lower the dilution ratio as compared to the sole dilution method (0.5:1 against 2:1).

Abstract Image

利用两步微滤和纳滤进行部分降钾预处理,提高酒厂废水的沼气生产率
本研究的主要目的是采用过滤预处理技术,将酒厂废水(DW)中的钾浓度从接近严重抑制(12000 毫克/升)的极高水平(8800 毫克/升)降至 4350 毫克/升,该浓度处于甲烷菌的中等毒性范围(2500-4500 毫克/升)。过滤预处理系统包括微滤(MF)和纳滤(NF)两个步骤,前者用于去除大的固体颗粒,后者用于降低截留 DW 中的 K 浓度。微滤和纳滤这两个步骤都是以连续再循环的批次模式运行的。中质过滤步骤的渗透液与不同的稀释比(稀释水体积与进水体积之比)一起送入纳滤装置,以降低截留液中的钾含量。累积稀释比越高,纳滤步骤的回流水中的钾浓度就越低。然而,随着累积稀释比的提高,渗透物的总体积也会随之增大。因此,在最佳累积稀释比为 0.5:1 时,经过滤预处理的 DW(COD 值高达 111500 mg/L,K 含量低至 4350 mg/L)与未经处理的 DW 相比,在平均生产率和沼气及甲烷产量方面都有显著提高。此外,与单一稀释法(0.5:1 对 2:1)相比,本研究中使用的两步过滤法可显著降低稀释率。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
Energy
Energy 工程技术-能源与燃料
CiteScore
15.30
自引率
14.40%
发文量
0
审稿时长
14.2 weeks
期刊介绍: Energy is a multidisciplinary, international journal that publishes research and analysis in the field of energy engineering. Our aim is to become a leading peer-reviewed platform and a trusted source of information for energy-related topics. The journal covers a range of areas including mechanical engineering, thermal sciences, and energy analysis. We are particularly interested in research on energy modelling, prediction, integrated energy systems, planning, and management. Additionally, we welcome papers on energy conservation, efficiency, biomass and bioenergy, renewable energy, electricity supply and demand, energy storage, buildings, and economic and policy issues. These topics should align with our broader multidisciplinary focus.
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