磷酸盐对亚硝化系统的抑制及恢复

通过接种城镇污水处理厂的污泥,采用连续流反应器启动亚硝化系统并改变进水磷酸盐的浓度,研究了不同磷酸盐浓度对亚硝化系统的影响.结果表明经过14 d的运行,亚硝化系统启动成功,氨氮转化率达到92.2%,亚硝酸盐累积率为73.66%,亚硝酸盐产生速率达到14.42 g·(m~3·d)~(-1).磷酸盐浓度在10~30 mg·L~(-1)时对亚硝化系统的影响并不大;随着磷酸盐浓度持续提高,氨氮转化率在不断降低.当磷酸盐的浓度为80 mg·L~(-1)时,系统的氨氮转化率为13.6%,亚硝酸盐累积率仅18.19%,亚硝酸盐产生速率仅0.54 g·(m~3·d)~(-1),亚硝化反应受到严重抑制.将进水磷酸盐浓度降低到0,经过14 d运行,亚硝化系统获得恢复,且氨氮转化率可以达到80%以上,亚硝酸盐累积率达到86.96%,亚硝酸盐产生速率为15.63g·(m~3·d)~(-1).     

Metal distribution characteristic of MSWI bottom ash in view of metal recovery

Bottom ash is the major by-product of municipal solid waste incineration(MSWI), and is often reused as an engineering material, such as road-base aggregate. However, some metals(especially aluminum) in bottom ash can react with water and generate gas that could cause expansion and failure of products containing the ash; these metals must be removed before the ash is utilized. The size distribution and the chemical speciation of metals in the bottom ash from two Chinese MSWI plants were examined in this study, and the recovery potential of metals from the ash was evaluated. The metal concentrations in these bottom ashes were lower than that generated in other developed countries. Specifically, the contents of Al,Fe, Cu and Zn were 18.9–29.2, 25.5–32.3, 0.7–1.0 and 1.6–2.5 g/kg, respectively. Moreover,44.9–57.0 wt.% of Al and 55.6–75.4 wt.% of Fe were distributed in bottom ash particles smaller than 5 mm. Similarly, 46.6–79.7 wt.% of Cu and 42.9–74.2 wt.% of Zn were concentrated in particles smaller than 3 mm. The Fe in the bottom ash mainly existed as hematite, and its chemical speciation was considered to limit the recovery efficiency of magnetic separation.     

Assessment of the clear-sky bias issue using continuous PM10 data from two AERONET sites in Korea

A bias in clear-sky conditions that will be involved in estimating particulate matter(PM)concentration from aerosol optical depth(AOD) was examined using PM_(10) from two Aerosol Robotic Network sites in Korea. The study periods were between 2004 and 2007 at Anmyon and between 2003 and 2011 at Gosan, when both PM_(10) and AOD were available. Mean PM_(10) when AOD was available(PM AOD) was higher than that from all PM_(10)data(PM all) by 5.1 and9.9 μg/m~3 at Anmyon and Gosan, which accounted for 11% and 26% of PM all, respectively.Because of a difference between mean PM_(10) under daytime clear-sky conditions(PM clear)and PM AOD, the variations in ΔPM_(10), the difference of PM all from PM clear rather than from PM AOD, were investigated. Although monthly variations in ΔPM_(10)at the two sites were different, they were positively correlated to those in ΔT, similarly defined as ΔPM_(10)except for temperature, at both sites. ΔPM_(10)at Anmyon decreased to a negative value in January due to an influence of the Siberian continental high-pressure system while ΔPM_(10)at Gosan was high in winter due to an effect of photochemical production at higher temperatures than at Anmyon.     

Phosphorus recovery from municipal and fertilizer wastewater: China's potential and perspective

Phosphorus (P) is a limited resource, which can neither be synthesized nor substituted in its essential functions as nutrient. Currently explored and economically feasible global reserves may be depleted within generations. China is the largest phosphate fertilizer producing and consuming country in the world. China''s municipal wastewater contains up to 293,163 Mg year of phosphorus, which equals approximately 5.5% of the chemical fertilizer phosphorus consumed in China. Phosphorus in wastewater can be seen not only as a source of pollution to be reduced, but also as a limited resource to be recovered. Based upon existing phosphorus-recovery technologies and the current wastewater infrastructure in China, three options for phosphorus recovery from sewage sludge, sludge ash and the fertilizer industry were analyzed according to the specific conditions in China.     

自养脱氮污泥的亚硝化活性恢复策略

为考察自养脱氮污泥亚硝化活性快速恢复的策略,在3个反应器内分别采用不同的方法对经过长期冷冻保存后的污泥进行了恢复活性的研究.其中R1为MBR(膜生物反应器),采用低ρ(DO)(0.30 mg/L)连续流恢复策略;R2为SBR(序批式反应器),采用低ρ(DO)(0.30 mg/L)间歇流恢复策略;R3为SBR,采用低ρ(NH₄+-N)预培养-高曝气-低ρ(DO)运行三阶段的恢复策略.结果表明,R1的恢复时间为46 d,NH₄+-N氧化速率达到4.99 mg/(h·g)(以N计),最终ρ(MLSS)达到5.43 g/L;R2的恢复时间为39 d,NH₄+-N氧化速率达到4.61 mg/(h·g),最终ρ(MLSS)达到4.47 g/L;R3的恢复时间为48 d,NH₄+-N氧化速率达到5.64 mg/(h·g),最终ρ(MLSS)达到5.16 g/L. 3个反应器均能长期抑制亚硝酸盐氧化细菌的活性,使亚硝化稳定运行. 3个反应器中,R3恢复所需时间最长,但污泥活性最好; R1中的污泥活性较低,但是膜组件有效截留了污泥,达到了最高的ρ(MLSS).研究显示,通过厌氧预培养后转为膜生物反应器连续流运行的策略,可有助于污泥的极大保留及污泥活性的最大恢复.      

TiO2/PS/Fe3O4 光催化剂的低温制备及其光催化和磁回收性能

以聚苯乙烯(PS)包覆油酸修饰过的纳米Fe3O4为磁核,在低温(90℃)、中性(pH=7左右)条件下,制备了以PS为惰性隔离层的磁载TiO2光催化剂.用X射线衍射仪(XRD)、透射电子显微镜(TEM)、傅里叶红外分光光度计(FT-IR)、振动样品磁强计(VSM)对催化剂的物相组成、形貌、表面性质、磁学性质进行了表征.以苯酚为模拟污染物,考察了其光催化活性,以自制的磁回收装置,考察其回收特性.结果表明,低温制备的TiO2为锐钛矿结构,平均粒径为2～5 nm,催化剂TiO2/PS/Fe3O4[其中物质的量比为n(TiO2)∶n(St)∶n(Fe3O4)=60∶2.5∶1]具有结构完整的壳/壳/核结构,TiO2在PS/Fe3O4表面负载牢固;光催化降解苯酚遵循一级反应动力学方程,TiO2/PS/Fe3O4[n(TiO2)∶n(St)∶n(Fe3O4)=60∶2.5∶1]的反应速率常数K=0.025 8,与纯TiO2的活性接近(K=0.026 2);循环使用5次后,反应速率常数仅降低0.003 4.所制催化剂具有较强的磁感应强度,平均回收率可达到92%以上.该低温水解法制备的磁载TiO2光催化剂具有良好的应用前景.     

吸附法油气回收系统在成品油库中的应用

介绍了活性炭吸附法油气回收系统在成品油库汽油装车过程中的应用情况。结合油库油气回收改造的实际情况,重点介绍了了吸附法油气回收装置的工艺流程、油库油气回收系统的组成、监控系统主要功能、环保检测的相关事项,并分析了油气回收系统的经济效益,结合实际经验对油库油气回收改造提出了建议。     

酸性水汽提及硫磺回收工艺的研究及应用研究

文章主要通过对酸性水气体及硫磺回收工艺特点的介绍与比选,着重分析“无在线炉硫磺回收及尾气处理工艺”（SSR）,其中硫回收为一段高温转化,二级催化转化的克劳斯工艺,尾气处理为加氢还原一吸收工艺,并介绍原辅材料成分及处理效率。该工艺能够有效解决石化企业的酸性气及酸水排放问题,具有良好的社会、环境效益显著。     

乡镇垃圾综合利用途径分析研究

社会主义新农村建设推动了乡镇经济的发展,但乡镇的环境问题并没有随之解决,而固体废弃物的综合利用成为解决当前乡镇环境问题的有效手段之一。乡镇垃圾现状分析表明,其组分以有机易腐成分为主．不适用于城市垃圾的处理方式。乡镇垃圾经合理分类,其综合利用的主要途径有三条,包括可回收垃圾一回收一循环再利用,有机垃圾制肥-肥料-回田,餐厨垃圾、人畜粪便、秸秆等有机垃圾厌氧发酵-沼气-热能或电能。该途径可最终实现乡镇垃圾的资源化和能源化。     

含油污泥三相离心分离处理技术研究

针对原油生产过程中产生的大量含油污泥,油泥成分复杂、严重污染周边环境且造成资源浪费的情况,采用三相离心分离工艺对含油污泥进行处理。通过室内试验研究,确定了含油污泥处理的最佳条件。添加分离剂能够改善油泥分离性能,提高油泥温度能够改善油泥流动效果,摸索出油泥离心分离的最佳时间和离心速率,并对分离后的三相物质进行物性检测。该工艺处理含油污泥可以有效的回收原油,处理后固相减量75%,实现含油污泥减量化、资源化处理的目的。