物化-生化组合工艺处理化纤厂浆粕综合废水

根据化纤厂浆粕综合废水的水质特点 ,选择采用中和曝气 水解酸化 生物接触氧化 絮凝沉降处理工艺。实验结果表明 :当浆粕综合废水进水CODCr浓度 310 0～ 34 6 0mg/L ,BOD5浓度 10 2 0～ 142 0mg/L范围内时 ,处理后水质可达到《污水综合排放标准》GB8978 96中化纤浆粕工业二级排放标准。     

缺氧生物筛选--好氧处理技术及其在造纸废水处理工程上的应用

阐述了缺氧生物筛选——好氧生物处理技术的基本原理、特点和设计要求。该技术用在造纸废水处理工程上作为主要的生化处理单元，可抑制丝状菌繁殖，避免污泥膨胀，而且还具有耐冲击负荷、污泥沉降性能好等特点，实际工程取得了理想的效果。     

Utilization of Bagasse Energy in Thailand

Bagasse, a biomass fuel, is the waste generated by the sugar-making process from sugar cane. Sugar making is one of the most important agricultural-produce processing industries for developing countries in Southeast Asia, Latin America and Africa. As sugar producing plants need electric power and process steam, co-generation using bagasse as an alternate fuel for petroleum has been in use for some time. Thailand recently became one of the largest sugar exporters by enlarging plant capacities and improving equipment, thus reducing its production cost. In addition, the Thai government promotes power generation using bagasse as a means to combat global warming by raising the purchase price of the surplus power. The industry is in the process of further raising the plant capacity, and improving the power-generating efficiency. This will enable a plant to generate more electric power than its in-plant need so that the surplus power can be sold to the commercial grid. It also plans to become a local power supplier during off-season of sugar making by adding a condensing turbine generator. A typical Thai sugar plant of the latest design generates steam of 4Mpa at the bagasse boiler outlet with the temperature of 400°C at 84% boiler efficiency. With the bagasse LHV of 7,540 kJ/kg and that of fuel oil 41, 840 kJ/kg, and taking 90%as oil-burning boiler efficiency, 5.95 kg of bagasse would replace 1 kg of oil. The Kyoto Mechanism defines CO₂ generation by fuel oil as 2.65 kg per liter. Using 0.85for the specific gravity of fuel oil, the amount of CO₂ generation will be 3.12 kg-CO₂/kg. Therefore, CO₂reduction per ton of bagasse in terms of fuel oil will be: 3.12/5.95 =0.524 kg-CO₂/kg-bagasse. As 1 kg of bagasse generates 2 kg of steam, the CO₂reduction of a 100t/h steam boiler will be112,660 ton/year for an annual operation of4,300 hours, as follows. 0.524 × 100/2 = 26.2 t-CO₂/h, 26.2 × 4,300 =112,660 t-CO₂/year. This revised version was published online in August 2006 with corrections to the Cover Date.     

Analysis of the hydrocyclone stock cleaning process for wasted fibre in a paper mill

The main objective of this project was to evaluate the possibility of reducing the quantity of fibre wasted at one of many hydrocyclone (centrifugal) cleaning processes in a paper mill. It was found that the application of elutriation water to both the tertiary and quaternary cleaners was essential to minimise the fibre discharged to the sewer, and the pressure of this elutriation water had a dramatic effect of reducing the fibre wastage. Accordingly, it has been shown that 150–160 kPa as the optimum pressure range to apply elutriation water to minimise the product grade fibre wasted whilst sending undesired shive fibre to the sewer. Also, monitoring of the press uhle box wastewater revealed that the paper mill has the potential to make substantial cost savings by reducing the waste stream. Further investigation is necessary to determine the types of fibre that are being wasted, and the viability of a screen to recycle the wasted fibre to the process. However, these fibres may be unsuitable to reuse in the process and alternative uses must be found.     

钢厂热锯机噪声控制方案

某钢厂热锯机的工作噪声问题严重影响附近居民的日常生活，急需解决。根据其发声机理，通过采取对圆盘锯边缘开槽，安装吸隔声罩，对锯片增加阻尼材料，夹紧工件等措施取得了较好的降噪效果。     

固硫剂制备工艺探讨

探讨了循环流化床锅炉脱硫方法中固硫剂的制备工艺，对几种石灰石破碎设备及工艺进行了分析比较，通过柱磨机粉磨石灰石的工业试验，了解其产品粒度分布，从而择优确定固硫剂制备工艺流程。     

Electrochemical treatment of olive mill wastewater: Treatment extent and effluent phenolic compounds monitoring using some uncommon analytical tools

Problems related with industrials effluents can be divided in two parts: (1) their toxicity associated to their chemical content which should be removed before discharging the wastewater into the receptor media; (2) and the second part is linked to the difficulties of pollution characterisation and monitoring caused by the complexity of these matrixes. This investigation deals with these two aspects, an electrochemical treatment method of an olive mill wastewater (OMW) under platinized expanded titanium electrodes using a modified Grignard reactor for toxicity removal as well as the exploration of the use of some specific analytical tools to monitor effluent phenolic compounds elimination. The results showed that electrochemical oxidation is able to remove/mitigate the OMW pollution. Indeed, 87% of OMW color was removed and all aromatic compounds were disappeared from the solution by anodic oxidation. Moreover, 55% of the chemical oxygen demand (COD) and the total organic carbon (TOC) were reduced. On the other hand, UV- Visible spectrophotometry, Gaz chromatography/mass spectrometry, cyclic voltammetry and 13 C Nuclear Magnetic Resonance (NMR) showed that the used treatment seems efficaciously to eliminate phenolic compounds from OMW. It was concluded that electrochemical oxidation in a modified Grignard reactor is a promising process for the destruction of all phenolic compounds present in OMW. Among the monitoring analytical tools applied, cyclic voltammetry and 13 C NMR are among the techniques that are introduced for the first time to control the advancement of the OMW treatment and gave a close insight on polyphenols disappearance.     

基于资源环境承载力的全国造纸工业类型区划分研究

本文从造纸行业特征、资源消耗、污染物排放等方面入手,结合区域资源环境承载力,分析行业发展可能带来的环境污染问题.分析造纸行业发展与其所需主要资源间的空间布局关系,明确选定行业发展的资源、环境和生态制约条件.结合造纸行业特点,从环境约束、生态约束和资源约束入手,构建其环境管理类型区划分的指标体系;采用层次分析法、灰色定权聚类分析等方法对分区数据进行必要处理,采用二维判断矩阵法等方法进行环境管理类型区划分,对实施针对造纸行业分区域、分类别、差别化的环境管理提供了决策依据和方法基础.     

制浆造纸工业废水达标可行性研究

2008年6月颁布的《制浆造纸工业水污染物排放标准》(GB 3544-2008)与原标准(GB 3544-2001)相比,增加了控制排放的污染物项目,污染物排放控制要求也大幅提高,传统的废水二级生化处理工艺已不能满足新标准要求。文章通过梳理和分析调研及现场监测的资料和数据,提出目前制浆造纸企业通过有效的技术改造和升级,增加废水三级深度处理流程,在加强管理的情况下可以实现废水稳定达标排放。但不可避免会增加企业建设和运营成本,大中型制浆造纸企业尚可接受,对小型企业的冲击则相对较大。同时提出目前制浆造纸企业废水处理仍存在一些技术和管理方面的问题,尚需通过制定技术规范、强化环境监管、深入开展相关基础研究等多方面对策,优化制浆造纸行业结构调整,确保行业污染物减排。     

Dioxin formation in pulp and paper mills of India

Samples of effluents, sludge, pulp, final products (paper) and soil were collected from the identified pulp and paper mills in India. The samples were analysed for 2,3,7,8-tetrachloro-dibenzo-p-dioxin (2,3,7,8-TCDD) and other dioxin congeners and precursors. Pulp and paper mills using chlorine for the bleaching process showed the presence of 2,3,7,8-TCDD in effluent samples. In the effluent and pulp samples from mills where chlorine dioxide was used as a bleaching agent, the 2,3,7,8-TCDD congener ranged from below the detection limit 0.05 to 0.12 ngL⁻¹/ngg⁻¹. The relative standard deviation of reproducibility and the percent recovery of 2,3,7,8-TCDD were 2.07 and 82.4% in pulp and 2.8 and 92% in effluent, respectively. The 1,3,6,8-TCDD was the only other major dioxin congener found in the treated and untreated effluent and sludge samples. However, dichlorobenzene, trichlorophenyl, and hexachlorobiphenyl were detected in all samples. The formation of dioxins can be minimised by replacing chlorine with chlorine dioxide in bleaching processes in pulp and paper mills.