PTA生产废水处理装置的开工及问题探讨

阐述了乌石化ＰＴＡ废水两段好氧处理系统的原理和启动运行过程，并对运行中发现的问题提出了解决方案     

精对苯二甲酸残渣的处理现状及综合利用

综述了国内外精对苯二甲酸（PTA）生产企业的残渣处理概况和残渣中有价物质的回收方法：提出了PTA残渣的控制和综合利用思路，分析了PTA残渣综合利用的经济效益。     

微生物燃料电池改性阳极处理PTA废水

探讨了不同改性阳极对微生物燃料电池(microbial fuel cell,MFC)产电性能及其对MFC处理难降解废水能力的影响.以单室空气阴极为基础,利用0.1 g电气石、质量分数75%二氧化锰/埃洛石纳米管(manganese bioxide/halloysite nanotube,MnO_2/HNT)和多壁碳纳米管-羧基(multi-walled carbon nanotube-carboxyl,MWCNT-COOH)对MFC阳极进行修饰.结果表明,不同改性阳极的MFC对含精对苯二甲酸(purified terephthalic acid,PTA)废水的去除率均高于70%,且化学需氧量(chemical oxygen demand,COD)去除率在79%以上.相较于其他几种改性阳极,以MWCNT-COOH改性材料作阳极的MFC产生的最大输出电压最高,获得的最大功率密度最高,分别为529 mV和252.73 mW·m~(-2).     

回收PTA废料生产增塑剂

介绍了扬子石化公司ＰＴＡ生产过程中所排各种废料的分离提纯及回收利用，对难以回收的氧化残渣的分离回收和利用作了重点论述。提供了用所回收的ＴＡ和混合苯二甲本乡生产剂的工艺流程和工艺参数。     

气提预处理后PTA聚酯废水的处理技术

经气提预处理后PTA聚酯废水的BOD/COD值为＜0.2,可生化性差,采用中温厌氧+接触氧化的方法,控制厌氧温度在38℃左右,提高厌氧去除率的同时改善废水可生化性,降低接触氧化的负荷,出水可稳定达标.     

PTA废液回收利用技术

介绍了从精对苯二甲酸（PTA）废液中回收醋酸,邻、对苯二甲酸,醋酸钴锰盐的回收工艺。醋酸得率为90％,邻、对苯二甲酸得率为70％,醋酸钴锰盐得率为95％。该技术成熟、合理,具有较好的经济效益和环境效益。     

对苯二甲酸对鱼类毒性的研究

通过实验室内短期毒实验，评价了对苯二甲酸对鱼草的毒性，给出了对苯二甲酸对草鱼仔鱼及幼鱼的９６ｈＬＣ５０值及其安全浓度。     

洛阳化纤PTA装置污水排放的综合治理

根据洛阳化纤工程PTA装置污水排放情况及与之配套的化纤污水处理场的处理情况，采取一系列有效措施，治理源头，达到PTA高浓度有机污水达标排放的目的。     

Implications of network particle tracking (NPT) for ecological model interpretation

Network particle tracking (NPT), building on the foundation of network environ analysis (NEA), is a new development in the definition of coherence relations within and between connected systems. This paper evaluates three ecosystem models in a comparison of throughflow- and storage-based NEA and NPT. Compartments in models with high indirect effects and Finn cycling showed low correlation of NEA storage and throughflow with particle repeat visits and numbers of particles in compartments at steady state. Conversely, the correlation between NEA and NPT results was high with two models having lower indirect effects and Finn cycling. Analysis of ecological orientors associated with NEA showed NPT to fully support conventional NEA results when the common conditions of donor control and steady state are satisfied. Particle trajectories are recorded in the new concept of a particle “passport”. Ability to track and record particle in-system histories enables views of multiple scales and opens the possibility of making pathway-dependent modeling decisions. NPT may also enable modeling of time, allowing integration of Newtonian, organismal and stochastic modeling perspectives in a single comprehensive analysis.     

Anaerobic-aerobic treatment of purified terephthalic acid (PTA) effluent; a techno-economic alternative to two-stage aerobic process

This paper addresses the treatment of purified terephthalic acid (PTA) effluent using anaerobic and aerobic processes. Laboratory studies were carried out on flow proportionate composite wastewater generated from the manufacturing of PTA. An activated sludge process (ASP-two stage and single stage) and an upflow anaerobic fixed film fixed bed reactor (AFFFBR) were used, individually and in combination. The performance of a full-scale ETP under existing operating conditions was also studied. Full scale ETP studies revealed that the treatment of PTA effluent using a two-stage ASP alone does not meet treated effluent quality within the prescribed Indian Standards. The biomass produced in the two stage ASP was very viscous and fluffy and the sludge volume index (SVI) was very high (200-450 ml/g). However, pretreatment of PTA effluent using an upflow AFFFBR ensured substantial reduction in BOD (63%) and COD (62%) with recovery of biogas at 1.8-1.96 l/l effluent treated at a volumetric loading rate (VLR) 4-5 kg COD/m(3) d. The methane content in the biogas varied between 55% and 60%. The pretreated effluent from the upflow AFFFBR was then treated through a single stage ASP. The biomass produced in the ASP after anaerobic treatment had very good settlability (SVI: 75-90 ml/g) as compared to the two stage ASP and the treated effluent quality with respect to BOD, COD and SS was within the prescribed Indian Standards. The alternative treatment process comprising an upflow AFFFBR and a single stage ASP ensured net power saving of 257 kW and in addition generated 442 kW of power through the AFFFBR.