城市泔水油氢化工艺单因素实验研究

了餐饮泔水油氢化反应的工艺参数单因素实验,实验结果表明:氢化反应温度在180 ℃,0.25%的催化剂添加量,搅拌速度采用900 r/min,实验压力控制在1.2 MPa时氢化反应效果比较理想.     

城市泔水油氢化工艺正交实验研究

对餐饮泔水油的氢化反应工艺参数进行了正交实验,实验结果表明:氢化反应温度在180 ℃,0.25%的催化剂添加量,搅拌速度采用900 r/min,实验压力控制在1.2 MPa时氢化反应效果比较理想.     

餐饮潲水油水解生产混合酸工艺

探讨了潲水油水解生产混合酸工艺。直接用水作催化剂,适应成分复杂的餐饮潲水油,污水处理简单。从酸析、水洗、压力、温度、水解等几方面进行研究,得出最佳水解工艺条件,具有推广意义。     

NaOH强化催化湿式氧化处理制药污泥

采用NaOH强化催化湿式氧化的方法处理制药污泥,考察了各工艺条件对污泥VSS去除率和COD去除率的影响。实验结果表明,在NaOH加入量10 g/L、反应温度260 ℃、初始氧气压力1.0 MPa、反应时间60 min的最佳工艺条件下,污泥VSS去除率和 COD去除率分别达到95%和60%,VSS去除率较高,污泥减量化效果显著。NaOH强化催化湿式氧化反应处理制药污泥的机理是氢氧根在高温条件下促进了微生物细胞的水解,促使污泥固体组分分解转移到液相中,最终有机物被降解为小分子有机物、CO₂和水。     

湿法腈纶废水的生化处理

采用水解酸化—固定化微生物流化床—氧化混凝联合工艺处理湿法腈纶废水.该工艺采用的高效菌微生物固定化技术及新型氧化混凝技术均对湿法腈纶废水有较好的处理效果.实验结果表明:在水解酸化温度为42℃、水解酸化运行周期为20 h的条件下,接种活性污泥和高效菌的SBR的COD去除率为26.0％;在新型氯铁型氧化混凝剂加入量为15 mL/L的条件下,混凝出水COD可降至66 mg/L.水解酸化—固定化微生物流化床—氧化混凝联合工艺的总COD去除率可达89.4％.     

用甲基硫酸钠废渣制备二甲基硫醚

根据酯在碱性条件下水解反应生成醚的原理，研究了以甲基硫酸钠废渣为原料制备二甲基硫醚（DMS）的方法。在反应温度100℃、加水量100mL、搅拌时间30min、合成反应时间50min的最佳工艺条件下，制得的DMS产品纯度为99％，收率为83．59％。该法工艺简单，技术可行，操作稳定，既消除了环境污染，又能制备化工产品，具有明显的环境效益和经济效益。     

植物秸秆的综合利用及防治造纸污染方法

该发明提供的是一种植物秸秆的综合利用及防治造纸污染方法：将植物秸秆粉碎后，加水进行高温水煮处理，再用热水洗涤；高温水煮后的固形物，加入H2SO4进行连续水解处理，水解结束后过滤，水解处理后的液体用作制造木糖的原料，水解处理后的固形物加入NaOH溶液进行高温碱蒸煮处理，     

高掺量粉煤灰烧结砖的制备

研究了高掺量粉煤灰烧结砖的制备工艺条件。结果表明：采用半干压成型，在成型压力19．6MPa、煅烧温度1000—1050℃、保温时间8h的条件下，可制得粉煤灰掺量高达80％的烧结砖，其物理力学性能及耐久性能都超过MU15普通粘土砖。     

丙烯腈生产废水中聚合物的资源化利用

以丙烯腈生产废水中的丙烯腈低聚物为原料制备聚丙烯酰胺。通过正交实验考察了水解反应条件和交联反应条件对反应的影响。FTIR表征结果显示,丙烯腈低聚物中的氰基已完全水解为酰胺基,产物聚丙烯酰胺中含有酰胺基和羧基。实验结果表明,在自来水加入量100 m L、水解反应温度95℃、m(Na OH)∶m(丙烯腈低聚物)=2.0、水解反应时间3 h的最佳水解反应条件,交联反应温度60℃、质量分数37%~40%的甲醛加入量6 m L、交联反应时间2 h的最佳交联反应条件下,处理20 g丙烯腈低聚物,可得到产物聚丙烯酰胺14.50 g,聚丙烯酰胺的水解度为21.1%、相对分子质量为2.7×106。产品性能满足Q/SH 0046—2007《钻井液用聚丙烯酰胺技术要求》中部分水解聚丙烯酰胺的性能要求。     

餐饮泔水油及废动植物油下脚料深加工利用大有可为--介绍<国家级科技成果重点推广计划>高效益环保项目“利用餐饮泔水油及废动植物油生产油酸、甘油、硬脂酸”新工艺

综述了我国的餐饮泔水油及废油脂资源浪费、破坏环境现状,对比介绍了新工艺显著的经济及环保效益.     

高纯二聚酸清洁生产技术分析

以一个利用高真空三级分子蒸馏技术生产高纯二聚酸的大型新建项目为例，对其原料、产品、工艺和设备进行了分析。以从棉籽油下脚料中提取的粗二聚酸为原料，自主开发了高真空三级分子蒸馏技术并改进了设备及控制条件，使二聚酸的纯度最高可达98％，水、蒸汽及能源的消耗均比原工艺有所下降。对在高纯二聚酸生产中推行清洁生产提出了建议和措施。     

废聚苯乙烯硝化氧化制对硝基苯甲酸

研究了用聚苯乙烯废料为原料,经过硝化氧化制造具有高附加值的精细化工产品－对硝基苯甲酸。探讨了影响对硝基苯甲酸产率的因素,如硝酸的浓度和用量,压力,反应时间及催化剂用量等。结果表明,在优化条件下对硝基苯甲酸产率达５２％,产品纯度为９９％。     

Review of the kinetics of alkaline degradation of cellulose in view of its relevance for safety assessment of radioactive waste repositories

The degradation of cellulose (a substantial component of low- and intermediate-level radioactive waste) under alkaline conditions occurs via two main processes: a peeling-off reaction and a basecatalyzed cleavage of glycosidic bonds (hydrolysis). Both processes show pseudo-first-order kinetics. At ambient temperature, the peeling-off process is the dominant degradation mechanism, resulting in the formation of mainly isosaccharinic acid. The degradation depends strongly on the degree of polymerization (DP) and on the number of reducing end groups present in cellulose. Beyond pH 12.5, the OH^- concentration has only a minor effect on the degradation rate. It was estimated that under repository conditions (alkaline environment, pH 13.3-12.5) about 10% of the cellulosic materials (average DP = 1000-2000) will degrade in the first stage (up to 10⁵ years) by the peeling-off reaction and will cause an ingrowth of isosaccharinic acid in the interstitial cement pore water. In the second stage (10⁵-10⁶ years), alkaline hydrolysis will control the further degradation of the cellulose. The potential role of microorganisms in the degradation of cellulose under alkaline conditions could not be evaluated. Proper assessment of the effect of cellulose degradation on the mobilization of radionuclides basically requires knowing the concentration of isosaccharinic acid in the pore water. This concentration, however, depends on several factors such as the stability of ISA under alkaline conditions, sorption of ISA on cement, formation of sparingly soluble ISA-salts, etc. A discussion of all the relevant processes involved, however, is far beyond the scope of the presented overview.     

废弃线路板热解油合成改性酚醛树脂

以废弃线路板热解油为原料，采用碱溶—中和—萃取工艺提取其中以苯酚为主的粗酚，并合成改性酚醛树脂。合成硼酸改性酚醛树脂的优化工艺条件为n(粗酚)∶n(外加苯酚)=2∶3，n(粗酚+外加苯酚)∶n(甲醛)∶n(NaOH)∶n(硼酸)=1∶1.5∶0.15∶0.17;合成有机硅改性酚醛树脂的优化工艺条件为n(粗酚)∶n(外加苯酚)=2∶3，n(粗酚+外加苯酚)∶n(甲醛)∶n(NaOH)∶n(正硅酸乙酯)=1∶1.3∶0.1∶0.1。所合成的硼酸改性和有机硅改性酚醛树脂的主要性能指标均满足YB/T4131—2005《耐火材料用酚醛树脂》中牌号为PFn-5301的热固性液体树脂性能的要求。     

Hydrolysis of Polylactic Acid (PLA) and Polycaprolactone (PCL) in Aqueous Acetonitrile Solutions: Autocatalysis

Polylactic acid (PLA) is a hydrolytically degradable aliphatic polyester. The rate of polymer hydrolysis increases with time, and that has been attributed to the high reactivity of the terminal ester and the kinetics of autocatalysis. Hydrolysis is carried out in an acetonitrile/water solution to eliminate any solid-state contributions such as diffusion and crystallinity to the degradation process. A kinetic equation is derived to describe the autocatalytic effect of the increasing carboxylic acid end-group concentration. The results of solution hydrolysis are examined and found to fit the derived equation. Hydrolysis was also carried out with polycaprolactone (PCL) in acetonitrile, where reaction kinetics were found to differ from those of PLA. The PCL polymer required external acid catalysis by the addition of HCl, whereas hydrolysis of PLA was selfcatalyzed by the carboxylic acid end-groups.     

治理技术邻苯二甲酸二辛酯废水的处理

采用压滤-刮油-中和吸附-压滤-吸附工艺处理邻苯二甲酸二辛酯废水,对处理工艺的运行条件进行了探讨.出水COD和石油类的去除率分别达到97.7%和99.8%.该法设备简单、投资少、操作方便,对排放量较小的邻苯二甲酸二辛酯废水的处理是行之有效的方法.     

Novel fry-drying method for the treatment of sewage sludge

The purpose of this study is to introduce an efficient drying method named “fry-drying technology” for the treatment of sewage sludge. The basic principle of this method lies in the rapid escape of moisture from sludge material through its pores into the oil medium driven by the strong pressure gradient formed between sludge and oil media. This beneficial pressure distribution for moisture transfer can be established by the subtle combination of the difference of physical properties of specific heat and boiling temperature between water and oil. In order to determine the physical characteristics of this fry-drying technology, a series of experiments were performed in which important parameters, such as heating oil temperature, drying time, oil type, and sludge size, were varied. Numerical calculations using a single solid spherical particle model without any porosity were used to resolve the particle size effect associated with sludge drying.     

萃取法回收钛白水解废酸中的硫酸

提出了以三异辛胺作萃取剂、H2O作反萃取剂从钛白水解废酸中萃取回收硫酸的新工艺。考察了萃取剂浓度、相调节剂浓度、相比及温度对萃取和反萃取的影响，并进行了模拟试验。在以40％三异辛胺、25％仲辛醇和35％航空煤油(均为质量分数)为萃取有机相，相比为2，以H2O为反萃剂，相比为1．5的条件下，质量浓度为146．02g/L的废酸经8级萃取和6级反萃取，硫酸回收率达到91．81％，产品酸质量浓度达119．73g/L。     

膜法处理精对苯二甲酸精制废水

采用“沉淀—超滤—反渗透—电去离子”工艺处理精对苯二甲酸精制废水,产水作为生产工艺用水回用于生产系统,考察了各工艺单元的操作条件。实验结果表明,在沉淀时间为4 h、超滤膜截留分子量为1 000且采用错流过滤模式、反渗透运行压力为1.8~2.2 MPa且温度控制在25~30 ℃、电去离子单元出水电阻率为5 MΩ·cm的操作条件下,最终出水水质优于GB/T 50109—2014《工业用水软化除盐设计规范》中的二级除盐水指标,可回用为生产工艺用水。     

压水堆电厂硼酸脱除技术研究进展

对压水堆电厂含硼酸废水的来源和特点进行了分析,讨论了化学沉淀法、离子交换法、膜分离法等硼酸脱除技术的原理和优缺点,在对各种方法进综合比较的基础上,展望了压水堆电厂硼酸脱除技术的发展趋势.