垃圾渗滤液处理技术及装置

由烟台德利环保工程有限公司开发的垃圾渗滤液处理技术及装置,适用于大中小城市生活垃圾填埋场渗滤液、垃圾中转站渗滤液的处理。主要技术内容一、基本原理先通过专用絮凝剂利用物化原理将废水中重金属、悬浮物等不利于生化的有害物除去,再进行中温厌氧, 去除75%左右的CODcr。厌氧出水经好氧 兼氧,可有效脱氮并去除CODcr、BOD5等,再经物化深度处理,出水指标达到一级排放标准。垃圾渗滤液经格栅沉砂池,去除大的悬浮渣质及砂     

含油污泥固化与燃煤混烧的可行性

为利用含油污泥的潜在能量,采用脱水、降粘、固化、固化物脱水等工艺技术进行含油污泥的固化。固化废物经粉碎处理后,按一定比例与燃煤混合,在燃煤锅炉中进行燃烧。混烧后的烟道气中的SO2、NO、烟尘含量等排放指标达到GB 13271-2001《锅炉大气污染物排放标准》的要求。     

联合生物法处理炼油厂含油污泥的研究

大港石化公司采用联合生物法处理含油污泥,对使用好氧、厌氧工艺处理含油污泥的结果进行了探讨。实验结果表明:先进行好氧处理然后脱水再进行厌氧堆肥工艺处理含油污泥,除油率达到97.6%,除磷、钾的指标低于《城镇垃圾农用控制标准》(GB8172-87)的要求外,其他指标均符合该标准要求,且避免了二次污染。     

城市污水厂混合污泥好氧消化处理研究

以城市污水处理厂的初沉污泥与剩余污泥的混合污泥为对象,研究了影响污泥好氧消化处理的各项因素.通过测定氧摄取速率(OUR)和此污泥好氧速率(SOUR),对实验结果进行了探讨.     

气田污泥脱水工艺研究

在对气田废水处理中产生的污泥进行处理时,普遍存在着干化周期长、含水率高等问题,严重影响了废水处理装置的处理能力。脱水剂优化选择实验以及污泥脱水性能实验结果表明:先加入聚合氯化铝并搅拌15 s,再加入阴离子聚丙烯酰胺并搅拌混合30 s,最后加入FO4190SH搅拌,混合凝聚30 s后静止分层,其凝聚效果较好。在污泥脱水性能的各项指标中,真空脱水均好于重力脱水,特别是对于新鲜污泥滤层,真空(45 kPa)脱水速度比重力脱水速度约高8倍。     

污泥处理处置技术路线综述

在目前污泥处理处置市场中,厌氧消化+土地利用、好氧发酵+土地利用、机械热干化+焚烧、工业炉窑协同焚烧、石灰稳定+填埋、深度脱水+填埋等6种处理处置技术路线被广泛采用。对上述技术路线从稳定化、减量化、无害化、资源化等方面,结合定义与内涵、相关标准要求、实现程度等加以分析、对比,得出结论 :厌氧消化+土地利用因其具备能源化和肥料化两方面应用潜力在资源化程度上表现最优;干化焚烧类技术路线在无害化、稳定化方面表现突出;采用填埋作为最终处置方案的技术路线在四个方面均表现不佳;好氧发酵在四个方面表现最均衡。最后,给出污泥处理处置技术路线的选择可参考的三条原则。     

基于两级DTRO膜系统处理垃圾渗滤液的工程应用

针对安岳县垃圾填埋场渗滤液处理工艺存在的问题,采用两级DTRO系统作为渗滤液处理的主工艺,从工艺设计、运行参数、处理效果、工程投资及运行成本等方面对该工程进行了全面分析。在线监测结果表明,出水COD_(Cr)浓度低于17mg/L,NH_3-N浓度低于6mg/L,特征出水水质指标稳定且满足《生活垃圾填埋场污染控制标准》(GB16889-2008)中表3对渗滤液排放标准的要求,且工程总投资(694.12万元)和运行成本(41.82元/t)较低,经济性好。该工程可为类似垃圾填埋场渗滤液处理工艺的优化和提升提供借鉴和指导。     

油气田废水污泥脱水处理工艺流程优化研究

油气田开发产生的污泥来源于油气田生产废水产生过程,具有干化周期长、含水率高、体积大、堆放、运输困难等特点。因此有必要对污泥脱水的工艺流程优化进行研究,提高污泥脱水效率,缩短污泥干化周期,为后续运输和处理创造必要的条件。本文选取实例,通过对污泥特性、污泥脱水剂优化选择试验和污泥脱水性能试验,提出了油气田废水污泥脱水处理工艺流程优化方案。     

含油污泥热解工艺技术方案研究

文章以辽河油田欢三联合站稠油污水处理系统压滤脱水污泥及沉降罐清罐污泥为处理对象,根据含油污泥热解处理的技术原理,通过对物料输送系统、热解反应系统、剩余固体排出系统和馏分冷凝分离系统等主要工艺单元的技术比选,提出了"柱塞泵管道密闭输送、多燃烧器回转炉热解、高温馏分管式换热器冷凝、不凝气罗茨风机引送和湿式排渣"的含油污泥热解处理工艺技术方案。同时,文章还对污泥热解处理运行的能耗与费用做了简要理论分析。     

基于碟管式反渗透处理垃圾渗滤液的应用分析

为了在达标排放的基础上降低建设规模为Ⅲ类、Ⅳ类型(中小型)垃圾填埋场处理垃圾渗滤液的人工及成本投入,提高系统稳定性,分析了泗县垃圾填埋场2018年3~12月渗滤液处理的运行状况。通过采用“预处理+两级碟管式反渗透+吹脱”的高度自动化工艺对垃圾渗滤液进行处理。结果表明:使用该系统处理后出水COD_Cr浓度低于26mg/L,NH3-N浓度低于15mg/L,各项出水指标均满足排放标准的要求,系统自动化程度高、稳定性好、且工程总投入834万元、运行期间处理每吨渗滤液花费为56.18元,成本较低适用性好。     

Bioleaching of heavy metals from sewage sludge: A review

During the treatment of sewage, a huge volume of sludge is generated, which is disposed of on land as soil fertilizer/conditioner due to the presence of nitrogen, phosphorus, potassium and other nutrients. However, the presence of toxic heavy metals and other toxic compounds in the sludge restricts its use as a fertilizer. Over the years, bioleaching has been developed as an environmentally friendly and cost-effective technology for the removal of heavy metals from the sludge. The present paper gives an overview of the various bioleaching studies carried out in different modes of operation. The various important aspects such as pathogen destruction, odor reduction and metal recovery from acidic leachate also have been discussed. Further, a detailed discussion was made on the various technical problems associated with the bioleaching process, which need to be addressed while developing the process on a larger scale.     

无污泥化生物技术在真丝染色综合废水处理中的研究及应用

本文主要对真丝染色综合废水Ａ／Ｏ处理中所产生的污泥进行无污泥化生物处理的研究,并把技术运用在日处理９００ｔ／ｄ的综合废水生化处理装置上,设施经四年连续运行表明：出水ｐＨ＝７． ３６,ＳＳ＝４８ｍｇ／１,ＣＯＤｃｒ＝９５ｍｇ／１,ＢＯＤ５＝３８ｍｇ／１,ＮＨ３－Ｎ＝１８ ．８ｍｇ／１,出水水质指标全部达到国家规定的排放标准,该技术不仅解决了污泥的难治理问题,而且利用生物技术彻底解决了污泥的二次污染问题,还节约了可观的运行费用和投资费用,并提高了Ａ／Ｏ的处理效果。     

垃圾渗滤液处理工艺及发展趋势探讨

分析了当前国内外几种渗滤液处理技术中存在的问题,以及渗滤液处理技术的发展方向。指出渗滤液处理技术应根据工程建设要求,并将渗滤液处理系统与垃圾焚烧系统结合起来确定,今后的发展方向和研究重点应放在渗滤液处理系统中的污泥处理系统、沼气净化及利用系统、膜系统浓缩液处理系统上。     

石油工业废弃物处置及其生物治理趋势

鉴于我国石油工作者对石油工业废弃物的普遍关注，现在介绍生物治理的基本概念及ＳＰＥ石油工程师协会中有关含油污泥生物处置的途径及其突出优越性。生物液／固处理工艺（ＬＳＴ）是目前含油污泥处置现场最经济可行的处置方案。这种好氧的ＬＳＴ工艺过程，能够比较充分地代谢和降解石油污泥中的油和脂并大量除去多环芳烃类（ＰＡＨ）化合物及其它有机化合物，明显地降低了石油废弃物对人、畜的毒害程度。其工艺较简单，操作也简易，凡经此工艺处理后的废弃物不留残毒和后患，因此早已被世界上先进国家的炼油业视为处理含油污泥的有效选择了。石油工业废弃物的生物防治和生物降解工艺较大程度地领先于目前我国现场正在执行的各种处理含油废弃物的处理工艺。     

生活垃圾填埋场渗滤液臭气生物处理技术研究

对新鲜渗滤液和经浓缩后渗滤液的臭气进行生物技术处理实验研究。实验结果表明,所采用的菌剂对两种渗滤液的臭气均有十分明显的去除效果。经生物技术处理后的两种渗滤液的各种污染物指标均有明显降低,其中大肠菌群去除率均达到了100%,氨氮的去除率分别为69.1%和58.2%,COD的去除率分别为84.8%和57.4%,总磷的去除率分别为97.7%和66.5%。该方法实现了从源头上防止渗滤液臭气产生的目标。     

The effect of landfill leachate composition on organics and nitrogen removal in an activated sludge system with bentonite additive

A pre-denitrification activated sludge system (AS) without internal recycle was used in lab-scale studies of landfill leachate treatment. A bentonite supplement at a ratio of 1:4 (mineral : biomass) was used to ensure high sludge settling levels and to serve as a micro-organisms carrier. The system was operated within different parameters such as hydraulic retention time (HRT), ammonia loading rate (ALR) or external recycle ratio, which was adapted to treat varying leachate concentrations of COD and ammonia, ranging from 1020 to 2680 mgO(2)l(-1) and 400-890 mgNH(4)-Nl(-1) respectively. The nitrification was complete and ammonia oxidation reached 99%; this was obtained while the ALR did not exceed 0.09 g NH(4)(+)-Ng(-1)MLVSS d(-1) and HRT was not lower than 1 day (in the aeration reactor). The performance of denitrification was successfully improved by controlling the external recycle rate, when the BOD(5)/N ratio in the raw leachate was 4.1. Consequently, N-removal of up to 80% was achieved. A 10-fold decrease in the denitrification rate was obtained at a BOD(5)/N ratio of 0.5. The efficiency of COD removal varied significantly from 36% to 84%. The positive effect of bentonite addition was determined and is discussed based on preliminary studies. The experiments were carried out in fill-and-draw activated sludge with bentonite; the biomass ratio was 1:2. The activated sludge with bentonite was fed with a synthetic high ammonia and organic-free medium.     

污泥土地利用中重金属铜污染地下水的潜在风险研究

本研究旨在通过土柱淋溶实验来研究堆肥污泥土地利用后重金属铜的溶出性,以及对地下水的影响。结果表明:与去离子水相比,模拟酸雨(pH=4.5)会使土壤中Cu的淋溶强度增加,并更能促使其向下迁移。经长期淋溶后发现,淋出液中铜的浓度呈现有起伏的递减趋势,最高峰浓度达到0.0702mg/L,远低于地下水Ⅲ类标准(1.0mg/L),污泥土地利用后Cu对地下水的污染风险较小。     

城市垃圾填埋场渗滤液处理工艺综述

城市垃圾对环境的影响越来越严重，垃圾填埋导致垃圾渗滤液的大量产生，渗滤液中含有大量的有机物、大量的病菌、病毒、寄生虫等以及一些有毒有害的物质，若渗滤液不加以妥善处理、肆意排放，必将对地下水、地表水构成严重威胁，因此垃圾渗滤液的有效处理就成为一个亟待解决的问题。本文对城市垃圾填埋场渗滤液的处理工艺进行了分析和探讨，介绍了国内外垃圾渗滤液处理的主要技术，包括土地处理法、生物法和物化法，并对电解法处理垃圾渗滤液进行了详细的介绍。     

Microfiltration of pretreated sanitary landfill leachate

A laboratory study using a bench scale model of two units operation involving coagulation process with Moringa oleifera seeds extract as a coagulant and filtration process using hollow fibre microfiltration membrane, was adopted to treat Air Hitam Sanitary Landfill leachate in Puchong, Malaysia. The performance of the microfiltration membrane in pretreated sanitary landfill leachate treatment was investigated through a continuous process. The leachate sample was passed through conventional coagulation process before being filtered through a hollow fibre microfiltration membrane of 0.1 μm surface pores. The hollow fibre microfiltration membrane decreased the turbidity, colour, total suspended solids, total dissolved solids and volatile suspended solids in the leachate by 98.30, 90.30, 99.63, 14.71 and 20%, respectively. The results showed that microfiltration is capable of removing high percentage of solids from leachate and might be considered as a polishing stage after on-site biological treatment for sanitary landfill leachate.     

Transport of di(2-ethylhexyl)phthalate (DEHP) applied with sewage sludge to undisturbed and repacked soil columns

Municipal sewage sludge is often used on arable soils as a source of nitrogen and phosphorus, but it also contains organic contaminants that may be leached to the ground water. Di(2-ethylhexyl)phthalate (DEHP) is a priority pollutant that is present in sewage sludge in ubiquitous amounts. Column experiments were performed on undisturbed soil cores (20-cm depth x 20-cm diameter) with three different soil types: a sand, a loamy sand, and a sandy loam soil. Dewatered sewage sludge was spiked with 14C-labeled DEHP (60 mg kg(-1)) and bromide (5 g kg(-1)). Sludge was applied to the soil columns either as five aggregates, or homogeneously mixed with the surface layer. Also, two leaching experiments were performed with repacked soil columns (loamy sand and sandy loam soil). The DEHP concentrations in the effluent did not exceed 1.0 microg L(-1), and after 200 mm of outflow less than 0.5% of the applied amount was recovered in the leachate in all soils but the sandy loam soil with homogeneous sludge application (up to 3.4% of the applied amount recovered). In the absence of macropore flow, DEHP in the leachate was primarily sorbed to mobilized dissolved organic macromolecules (DOM, 30.3 to 81.3%), while 2.4 to 23.6% was sorbed to mobilized mineral particles. When macropore flow occurred, this changed to 16.5 to 37.4% (DOM) and 36.9 to 40.6% (mineral particles), respectively. The critical combination for leaching of considerable amounts of DEHP was homogeneous sludge application and a continuous macropore structure.