共查询到20条相似文献,搜索用时 78 毫秒
1.
2.
污泥是污水处理厂的必然产物,目前污泥处理处置的矛盾日益突出,而污泥焚烧是处理速度最快,减量化程度最高的方法。本文对比了浓缩污泥和深度脱水污泥的热值,提出污泥焚烧处理的合理路线。并利用工业分析法和元素分析法计算污泥热值,提出了污泥热值的参考计算方法,方便污泥处理企业使用。 相似文献
3.
通过讨论污泥化学性质对污泥脱水性影响,介绍了胞外聚合物对污泥脱水性影响的几种不同学说,同时介绍了金属离子对污泥脱水性的影响;对污泥深度脱水技术进行了介绍,对传统污泥脱水技术、基于污泥高压过滤脱水的调理技术以及电渗透污泥脱水技术的优劣进行了比较;阐述了污泥深度脱水工艺的工艺适配性和应用现状,并对污泥深度脱水技术的未来进行了展望。 相似文献
4.
5.
6.
7.
8.
9.
10.
为解决污泥与煤掺混制浆时存在配入量少、污泥水煤浆浓度过低、添加剂用量大、成本高等问题,在实验室开发了污泥复合改性剂与高效改性机相结合的新型污泥改性制备高浓度污泥水煤浆的工艺,并进行了中试制浆试验。结果表明,采用复合改性剂与高效改性机对污泥进行改性,得到的改性污泥黏度比单纯用改性剂得到的改性污泥黏度降低30%以上,这种改性方法完全可以替代流体激波工艺处理污泥。污泥添加量为15%时,污泥水煤浆浓度比不添加改性污泥的普通水煤浆低3%左右,而采用同样污泥改性工艺和优化粒度级配,污泥水煤浆的浓度与普通水煤浆浓度相当,说明采用污泥改性和优化粒度级配可以解决污泥水煤浆浓度低的问题。中试生产线制浆试验结果验证了小试结果和中试装置的可靠性。 相似文献
11.
内循环式厌氧反应器常温下启动过程试验研究 总被引:1,自引:1,他引:0
为在常温启动运行条件下,探索简便、实用,可靠的内循环式厌氧反应器(IC)颗粒污泥的培养途径,缩短IC反应器启动时间,以葡萄糖模拟废水作为IC进水,逐渐增大进水有机物含量和流量,研究了启动过程的运行参数、影响因素及颗粒污泥的形成效果.结果表明,IC在70d内完成启动,在30d的时间内可实现了污泥的颗粒化.启动试验结束时颗粒污泥直径多在1~3mm,部分粒径能够迭到4~5mm.因此,通过调整运行条件可以实现IC在较短时问内完成启动和实现污泥的颗粒化,并且IC对污水中有机物有明显的去除效果. 相似文献
12.
二次流场促进高浓度颗粒污泥体系的传质效率 总被引:1,自引:0,他引:1
将提供特定流体动力条件(二次流)的SSBR反应器和普通向上流SBR反应器进行对比,试验分析氧传质性能、降解性能和颗粒污泥形态,研究高浓度颗粒污泥体系中,优化的流体动力条件-二次流对氧传质效率的影响以及由此引起的种群分布变化.结果表明,SSBR反应器的氧传质速度更快,稳定运行的SSBR反应器能维持更高的溶解氧,有利于提高颗粒污泥内部的溶解氧渗透能力,对颗粒污泥中心区域的营养供给充分,颗粒污泥内部微生物不易老化,有利于颗粒污泥体系的稳定和强化有机物的降解效率. 相似文献
13.
14.
15.
通过系统地分析国内外近期相关研究成果,深入地讨论了城市污泥与煤炭及其他燃料混烧处理技术的环境相容性、混烧热工特性和混烧工艺可行性,研究了城市污泥混烧处理工艺的技术特点和存在问题,认为污泥混烧处理技术具有明显的技术合理性和良好的发展前景,但在污泥预处理与混烧技术的结合方面还需要进一步完善和发展。 相似文献
16.
随着经济的发展和国民生活水平的提高,污水污泥的排放量逐年增加,环境问题愈发严重,污泥的处理处置成为焦点问题,污泥脱水是制约污泥处置处理进一步发展的关键。本文针对目前污泥深度脱水技术开展,首先简述了不同来源污泥的分类及其基本特性,然后重点阐述了不同污泥预处理技术,分析了各污泥深度脱水技术作用机理,并对各自脱水效果及优缺点进行比较分析。结果表明,物理法中水热预处理对污泥的可脱水程度提升最大。较低声强、短时间的超声波处理对污泥脱水性能有着明显的改善。化学法在污泥过滤性能以及脱水速率方面有很大优势,酸碱处理后污泥zeta电位上升,污泥过滤性能及脱水速率得到改善。高级氧化法处理后污泥脱水效果高于酸碱处理,微生物细胞被溶解释放出有机物,可脱水程度改善。生物法处理污泥除改善污泥脱水性能外,还有对环境污染小等特点,但耗时较长。最后对污泥的后续脱水工艺进行综述,介绍了现存的主流脱水工艺,包括机械脱水、热干化技术、水热脱水工艺等;并针对不同的污泥后续利用方法,选取合适的预处理技术,提出相应优化的污泥处理工艺流程。 相似文献
17.
为研究含油废水处理产生的剩余污泥和气浮污泥的厌氧消化性能,试验采取序批式厌氧消化两种含油污泥的方法,对含油污泥的组成变化及产气性能进行测定,并将其结果与市政剩余污泥进行对比。试验结果显示,经过35天的厌氧消化,含油剩余污泥和含油气浮污泥的可挥发固体(VS)降解率分别为4.98%和3.74%,TCOD降解率分别为10%和3.4%,产气量分别为0.97 L/gVS和0.56 L/gVS。经过和市政剩余污泥对比后表明,含油气浮污泥厌氧消化性能差,不宜进行厌氧消化处理;含油剩余污泥厌氧消化性能相对强于含油气浮污泥,但弱于市政剩余污泥。 相似文献
18.
Tolga Tunçal 《Drying Technology》2013,31(12):1344-1349
Drying of residual treatment sludge is one of prerequisites in final disposal of this hazardous material. In this study, sludge drying potential (SDP) of different sludge types (DST) and the effect of organic content and commonly used chemical additives, including polyelectrolyte and lime, on SDP were investigated in a full-scale municipal wastewater treatment plant (WWTP). Freshly collected sludge samples were used in all experiments, which were conducted in onsite laboratory of sludge treatment facility. Studied sludge types were composed of raw biological sludge (RBS), raw primary sludge (RPS), mixed sludge (MS), dewatered sludge (DS), and limed sludge (LS). Halogen radiation was used for sludge drying. Organic content of sludge was represented by total organic carbon (TOC), dissolved organic carbon (DOC), and lost on ignition (LOI) parameters. Relations and interactions among the SDR(s) of DST(s) were statistically determined using independent samples t-test. The effect of organic content and chemicals additives on SDP was also statistically analyzed using linear regression model. Results of the study imply that each surveyed sludge type had a different SDP. Furthermore, organic composition of sludge and chemical additives had a significant impact on SDP. 相似文献
19.
Maria Wlodarczyk-Makula 《Polycyclic Aromatic Compounds》2013,33(2):183-194
Abstract Sewage and sewage sludge from a municipal wastewater treatment plant were analyzed for 16 EPA-PAHs. This plant is a classic mechanical-biological treatment plant, consisting of activated sludge technology with additional chemical treatment for the removal of phosphorus compounds. The process of sewage sludge treatment is carried out in closed as well as open sludge digesters. Primary and mechanically thickened sludge are passed through the fermentation process. Digested sludge is dewatered on filter-press through addition of flocculent. The measurements were obtained to investigate the effect of different treatment stages on PAH content in wastewater and sewage sludge. The following wastewater samples were collected: crude ones and those after sand trap, primary sedimentation, biological treatment and secondary sedimentation. Sewage sludge samples were collected from: primary sludge, digested sludge and dewatered sludge. PAH load in influent, mechanically and biologically treated sewage, as well as in raw digested and dewatered sludge, were calculated. PAHs were extracted from wastewater and sludge samples, with cyclohexane, dichloromethane using an ultrasonic method. Gas chromatograph equipped with mass spectrometry was used for qualitative and quantitative determination of PAHs. Mechanical and biological treatment proved the removal of 83–85% of PAHs from the influent. Despite this its daily PAH load introduced into the environment was high and reached 27–37% of PAH load in influent. In sewage sludge it was 46–70 g/d of PAHs (carcinogenic PAHs content 4–12%). In waste sludge (filter pressed sludge and sand from detrirer) PAH total load reached 42–68 g/d with (10–17% of carcinogenic PAHs). 相似文献
20.
本研究建立了3个有效容积为4.2L的有机玻璃材料反应器,培养驯化自养、异养和混合营养3种不同营养类型的活性污泥.通过分析3种不同营养类型污泥沉降性能的差异,旨在找出造成3种污泥沉降性能差异的微观原因,为改善污泥的沉降性能提供新的途径和理论依据.研究结果表明,自养污泥沉降性能最好,混合营养污泥次之,异养污泥最差;污泥的粒径对沉降性能无明显影响;Zeta电位和相对疏水性是造成3种污泥沉降性能差异的重要表面理化性质,Zeta电位值越接近于0,相对疏水性越强,污泥沉降性能越好;污泥胞外聚合物(EPS)中腐殖酸和多糖含量对污泥表面Zeta电位、相对疏水性和污泥沉降性能无明显影响;EPS中蛋白质含量直接影响Zeta电位值,进而造成3种污泥污泥沉降性能差异;而EPS总量和3种污泥沉降性能没有明显相关性. 相似文献