Co-pyrolysis of oil sludge with hydrogen-rich plastics in a vertical stirring reactor: Kinetic analysis,emissions, and products

● Collaborative treatment of plastics and OS was established to improve oil quality. ● PE addition successfully improved OS pyrolysis process by deploying H/C_eff ratio. ● Higher H/C_eff ratio promoted cracking to obtain more gas and light oil fractions. ● The degradation of PE and OS was promoted each other under their temperature range. Pyrolysis is an effective method to treat oily sludge (OS) due to its balance between oil recovery and nonhazardous disposal. However, tank bottom OS contains a high content of heavy fractions, which creates obstacles for pyrolysis due to the high activation energy. The incomplete cracking of macromolecules and secondary polymerization decreases the oil quality and causes coking during the operation process. This study introduced polyethylene (PE) into OS to deploy the H/C_eff ratio of feedstocks for pyrolysis. A strong interaction between OS and PE during copyrolysis could be observed from the TG/DTG curves. PE tightly participated in OS degradation, while OS also promoted PE degradation at high temperature. Apparent pits were generated in solid residues from copyrolysis, which was attributed to the uniform and violent gas release. In addition to HCN, other nitrogenous and sulphurous pollutants were inhibited. Accordingly, more gas products were attained after PE addition with more value-added compositions of alkanes and alkenes. Although the oil yield decreased after PE addition, the oil products from copyrolysis possessed higher heating values and higher contents of light fractions with short chains as well as paraffins. Consequently, copyrolysis of OS and PE significantly improved the pyrolysis process and resulted in high oil quality.     

Techno-economic characteristics of wastewater treatment plants retrofitted from the conventional activated sludge process to the membrane bioreactor process

• Retrofitting from CAS to MBR increased effluent quality and environmental benefits. • Retrofitting from CAS to MBR increased energy consumption but not operating cost. • Retrofitting from CAS to MBR increased the net profit and cost efficiency. • The advantage of MBR is related to the adopted effluent standard. • The techno-economy of MBR improves with stricter effluent standards. While a growing number of wastewater treatment plants (WWTPs) are being retrofitted from the conventional activated sludge (CAS) process to the membrane bioreactor (MBR) process, the debate on the techno-economy of MBR vs. CAS has continued and calls for a thorough assessment based on techno-economic valuation. In this study, we analyzed the operating data of 20 large-scale WWTPs (capacity≥10000 m³/d) and compared their techno-economy before and after the retrofitting from CAS to MBR. Through cost-benefit analysis, we evaluated the net profit by subtracting the operating cost from the environmental benefit (estimated by the shadow price of pollutant removal and water reclamation). After the retrofitting, the removal rate of pollutants increased (e.g., from 89.0% to 93.3% on average for NH₃-N), the average energy consumption increased from 0.40 to 0.57 kWh/m³, but the operating cost did not increase significantly. The average marginal environmental benefit increased remarkably (from 0.47 to 0.66 CNY/g for NH₃-N removal), leading to an increase in the average net profit from 19.4 to 24.4 CNY/m³. We further scored the technical efficiencies via data envelopment analysis based on non-radial directional distance functions. After the retrofitting, the relative cost efficiency increased from 0.70 to 0.73 (the theoretical maximum is 1), while the relative energy efficiency did not change significantly. The techno-economy is closely related to the effluent standard adopted, particularly when truncating the extra benefit of pollutant removal beyond the standard in economic modeling. The modeling results suggested that MBR is more profitable than CAS given stricter effluent standards.     

New insights into different surfactants’ impacts on sludge fermentation: Focusing on the particular metabolic processes and microbial genetic traits

• The promoting effects for VFA generation follow the order of APG>SDBS>HTAB. • Surfactants improve the WAS solubilization/hydrolysis and acidification processes. • The VFA promotion is associated with surfactants’ distinctive characteristics. • Surfactants induce the enrichment of functional bacteria for VFA biosynthesis. • The vital genes for substrates delivery, metabolism, and VFA yields are upregulated. Surfactants were expected to exhibit positive effects on the waste activated sludge (WAS) disposal. However, the systematic comparison of different categories of surfactants on the WAS fermentation and the functional mechanisms, especially microbial metabolic traits, have not yet been precisely explored. This study revealed the positive effects of different surfactants on the volatile fatty acid (VFA) production, which followed the order of alkyl polysaccharides (APG)>sodium dodecylbenzene sulfonate (SDBS)>hexadecyl trimethyl ammonium bromide (HTAB). Mechanistic exploration found that the presence of different surfactants improved solubilization and hydrolysis steps, and then contributed to the subsequent acidification with different efficiencies. The functional microorganisms associated with VFA generation were enriched in surfactant-conditioned reactors. Metagenomic analysis further indicated that the key genes involved in the particular process of VFA generation were over-expressed. The simultaneous bioavailable substrate improvement, functional bacterial enrichment, and metabolic activity upregulation induced by different surfactants jointly contributed to VFA promotion during WAS fermentation. This study could provide a comprehensive realization of surfactants’ impacts on the WAS fermentation process, and more importantly, it reminded the public to discern the distinct interplaying effects induced by different chemicals in regulating the WAS disposal and resource recovery.     

地铁隧道排烟口无量纲结构参数与局部阻力研究*

针对现有行业规范中的排烟口结构参数尚不明确的问题,依托过海瓦贵区间隧道,搭建隧道通风排烟模型实验系统。设定11种排烟口面积工况,结合实验与数值模拟,得到排烟口上、下游的静压值和风速。引入动能修正系数,推导出基于上下游能量差的排烟口局部阻力表达式,绘制出无量纲面积比与局部阻力系数曲线族。研究结果表明:排烟口长宽比值较大时,不利于排烟口下方风流流动;在同一风机组合工况下,当排烟口面积缩小时,局部阻力系数会呈现出先减后增的趋势;提出排烟口最优结构长宽比为1.06。研究结果可为相关规范制定提供参考,并为防灾救灾提供理论支持。     

过滤材料声学性能的实验研究*

为探讨纤维过滤材料的吸声效果,扩展吸声材料的选择范围,并为噪声粉尘一体化控制提供指导,通过实验分析不同等级一般通风用纤维层滤料的过滤性能和吸声性能,研究叠加方式及空腔设置等对滤料吸声性能的影响。研究结果表明:一定条件下,滤料的过滤效率越高吸声性能越好;单层滤料吸声效果较差,通过多层叠加,可显著提升吸声效果,达到吸声材料水平;不同等级滤料组合叠加,按过滤效率降序排列整体吸声性能更好。滤料作为吸声材料应用时,在其后侧设置空腔可明显增强吸声效果;兼顾过滤和降噪时,考虑粗效对中效滤料的保护作用,可在粗效加中效滤料后再附加粗效滤料,达到在不显著增加阻力的同时改善吸声性能的目标。     

五区电除尘技术试验研究及应用

五区电除尘技术是一种新型的电除尘器提效改造技术,由于其性能优良、工作可靠、稳定运行,工程投资少、施工周期短等优点而得到广泛应用。在模拟计算分析其阻力和对气流分布影响的基础上,试验研究其对不同粉尘的收尘性能,结果表明:五区电除尘技术可高效捕集微细、高比电阻粉尘,且设备阻力小,气流分布理想。     

酸化大豆蛋白废水的厌氧处理

对有机质浓度高,成分单一,蛋白质、总氮浓度较高,易酸化,且已酸化程度较高的大豆蛋白废水,确定以新型内循环厌氧反应池为主的处理工艺,在原废水ρ(COD)为11809~15040mg/L时,总出水浓度192~350mg/L,去除率达到96.2%~97.5%。新的内循环厌氧反应池具有高度小、结构简单、污染物去除率高的特征,COD运行负荷达6.0~7.5kg/(m3.d),COD去除率达88%~93%。当COD运行负荷5.0~7.0kg/(m3.d)时,该池内循环管道形成了连续的较强内回流。     

基于微波辐射研究城市污水污泥脱水特性

选用沈阳市仙女河污水处理厂和北部污水处理厂污水污泥作为微波脱水试验物料,分析物料性质、辐射强度、辐射时间以及添加剂投入量等对污泥脱水率和有机质损失率的影响. 结果表明:污泥中水分含量高的脱水效果最好,经过微波处理后的污泥有机质含量仍较高;辐射时间是最主要的影响因素,在540 W下辐射2～5 min即可达到良好效果;在合适的辐射时间下540～900 W都能达到良好的脱水效果,但在900 W时有机质的损失率较大,达到65.64%;添加剂投入量对污泥脱水基本不起作用,但可改变污泥微波干燥后的性状. 同时,运用灰色关联分析得到决定微波试验运行系统的主次因素,最后建立了影响因素对污泥脱水率和有机质损失率的经验公式.      

轻质陶粒滤料生态滤床的挂膜与启动研究

以自行设计的反应器作为生态滤床的基础,采用活性污泥作为接种污泥,采用轻质陶粒作为生态滤床的滤料,对其进行挂膜.在整个挂膜过程中,温度控制在中温条件下,进水pH值控制在7左右,水力停留时间为24 h,进水方式为连续进水,并根据需要对曝气量进行调节.在挂膜过程中对进、出水的COD、NH_3-N、TP、Cl~-和pH进行检测,并刮取少量轻质陶粒上的生物膜制成镜检切片后用多媒体显微镜对生物膜的形态进行观察.研究结果表明,在中温条件下采用活性污泥作为接种污泥,以轻质陶粒为滤料的生态滤床在15 d内挂膜成功;且随着进水污染负荷的提高,其去除率也逐渐提高,其中COD的去除率最后稳定在95%左右,NH3-N的去除率稳定在85%左右,TP的去除率在挂膜后期达到了80%以上;Cl~-作为微生物所需的微量元素在微生物生长高峰期为50%,稳定期保持在20%左右;进水pH保持在7左右,出水pH略高于进水,在8左右;从第13 d和第15 d的切片可观察到轮虫这种象征生物膜成熟的微生物的出现,此外还有大量的丝状菌和菌胶团.     

从造纸污泥中提取木质素制备缓蚀阻垢剂

以造纸污泥为原料,用碱溶酸析法提取其中的木质素,对木质素进行磺化改性后,与有机磷、锌盐等进行复配,以提高缓蚀阻垢效果。探讨了主原料配比、药剂投加量、反应温度、反应时间等对药剂性能的影响。结果表明:由该法制备的缓蚀阻垢剂性能较好,为造纸污泥的综合利用提供了一条新途径。