单光子/光电子在线质谱实时分析聚氯乙烯热分解/燃烧产物

实验室研制了低能光电子磁场增强电离(MEPEI)和单光子电离(SPI)复合电离源,该电离源具有电离化合物范围宽、碎片离子少、质谱图简单等优点,结合飞行时间质谱(TOF-MS)实现了聚氯乙烯(PVC)热分解/燃烧产物的在线分析.针对不同的目标化合物,MEPEI/SPI复合电离源通过调节电离区电场强度,可以快速在SPI和SPI-MEPEI之间切换.PVC热分解/燃烧产物中电离能大于光子能量(10.60 eV)的HCl和CO2(12.74 eV、13.77 eV)利用MEPEI模式电离;而烯烃、二氯乙烯、苯系物、氯苯、苯乙烯、茚满及萘系物等可通过SPI-MEPEI复合模式电离.通过实时监测PVC主要燃烧产物的信号强度随温度的变化趋势可推断出,PVC燃烧产物主要是通过两种机制生成:①250～370℃时,PVC发生脱氯及分子内环化反应,产生大量的HCl、苯和萘;②380～510℃时,PVC发生分子间交联反应,生成烷基芳烃,如甲苯和二甲苯/乙苯等.实验结果表明,SPI/SPI-MEPEI复合离子源TOF-MS分析速度快,应用范围广,在在线分析中具有广泛的应用前景.     

目标分解法在清洁生产中的应用

间苯二甲酸装置扩产改造后排污量增加较多,翻倍的排污量严重影响到装置发展,针对装置的排污问题,利用目标分解法查找关键原因并进行技术改造,改造后装置排污量大大减少,提高了装置的竞争力。     

SRT影响MBR有机污染物去除速率研究

通过考察污泥停留时间(SRT)对膜生物反应器(MBR)和粉末活性炭膜生物反应器(PAc-MBR)降解有机物速率的影响,探讨了污泥活性与胞外聚合物(EPS)的关系.结果表明:MBR和.PAC-MBR中COD降解速率随SRT延长均呈先上升后下降的趋势,分别在39～48d和48d时达到最快,对应速率常数为2.586和3.856,PAC-MBR中COD降解速率普遍高于MBR,说明投加PAC使污泥活性提高,SRT对污泥活性影响较大;MBR和PAC-MBR中胞外聚合物质量浓度与COD降解速率常数K1变化趋势一致,且胞外聚合物质量浓度与K1呈良好正相关关系,说明系统的胞外聚合物质量浓度可以作为衡量污泥活性的指标.     

SBR法处理低C/N污水的工程应用——以某基地污水处理站改造工程为例

低C/N污水的生化处理过程中,由于碳源不足,不能满足硝化和反硝化的要求,造成出水NH3-N超标。采用SBR工艺对某基地污水处理站厌氧处理后的低C/N污水进行改造,处理后出水COD去除率达到97%以上,NH3-N去除率达到93%以上。     

海水异养硝化-好氧反硝化芽孢杆菌SLWX2的筛选及脱氮特性

从分离自刺参养殖环境的7株候选菌株中筛选出1株具有较强异养硝化和好氧反硝化能力的菌株SLWX_2,通过形态学特征、生理生化特性和16S rRNA基因测序分析鉴定其为花津滩芽孢杆菌(Bacillus hwajinpoensis).该菌株脱氮特性研究结果表明,SLWX_224 h对氨氮、亚硝酸氮和硝酸氮的去除率分别达到100%、99.5%和85.6%;当3种无机氮源同时存在时,菌株优先利用氨氮,再利用NO_2~--N和NO_3~--N,72 h 3种无机氮的质量浓度均降至0.013 mg·L~(-1)以下,表明该菌株能同时进行异养硝化和好氧反硝化完成脱氮;在氨氮负荷500 mg·L~(-1)、亚硝酸氮负荷100 mg·L·~(-1)和硝酸氮负荷200 mg·L~(-1)范围内,该菌的脱氮能力不受明显抑制,对3种形态的氮均有良好去除效果,96 h最多可去除180 mg NH_4~+-N、30 mg NO_2~--N和120 mg NO_3~--N,并且在硝化过程中没有亚硝酸氮积累.该菌株在海水养殖和高盐高氮工业废水的脱氮处理方面具有更大潜力.     

Experimental research of LNG accidental underwater release and combustion behavior

Evaluating potential hazards caused by accidental LNG release from underwater pipelines or vessels is a significant consideration in marine transportation safety. The aim of this study was to capture the dynamic behavior of LNG jet released under water and to analyze its vapor dispersion characteristics and combustion characteristics on the water surface during different release scenarios. Controlled experiments were conducted where LNG was jet released from a cryogenic storage tank. The dynamic process of LNG being jet released from orifices of different sizes and shapes, as well as the rising plume structure, were captured by a high-speed camera. The leakage flow rate and pipeline pressure were recorded by a flow meter and pressure gauge, respectively. The concentration distribution that emanated from the water surface was measured utilizing methane sensors in different positions with various wind speeds. The flame combustion characteristics of LNG vapor clouds, which immediately ignited upon the enclosed water tank, were also recorded. Additionally, the mass burning rate of the flame on the water surface was evaluated, and a new correlation between the ratio of flame length and width was established. The results indicated a large dimensionless heat release rate (Q*) and a continuous release flow rate in a limited burning area. This study could provide greater understanding of the mechanisms of LNG release and combustion behavior under water.     

Thermal decomposition mechanism of 65% lysine sulfate powder and its thermal stability based on thermal analysis

Lysine is widely used in the fields of food, medicine and feed, which generally appears in the form of lysine sulfate or lysine hydrochloride dust because of the high instability of the free L-lysine. The L-lysine Sulfate is in high risk of decomposition, spontaneous ignition and even the dust explosion, because the control temperature in its production process is high up to 90 °C. Thus, the thermal behaviors and its thermal stability of 65% lysine sulfate are experimentally explored in Air and Nitrogen using the simultaneous TG-DSC measurements. Results show: (1) the decomposition of 65% lysine sulfate can be divided into three stages both in the atmospheres of air and nitrogen, and most of the weight loss occurred in the first two stages, which are related with the decarboxylation and deamination process. (2) The effects of atmosphere on the decomposition of 65% lysine sulfate mainly occur at the third stage. In this stage, the weight loss in nitrogen is only 14.2%, which is much lower than that in air (34.3%), which is related to the oxidative degradation at high temperature. Besides, the active energy is slightly increased in nitrogen compared to that in air. (3) The initial temperatures of the decomposition of the 65% lysine sulfate are 145 °C and 155 °C, for the air and nitrogen atmosphere, respectively, which are much lower than that (260 °C) of the pure lysine.     

复合沸石滤床修复北方景观水体的实验研究

以天然矿物质沸石、细砂及煤渣取代传统滤料构建复合基质生态床,表面种植景观植物,采用下向流-上向流运行方式修复北方景观水体。分别进行静态实验及不同循环速率下的动态实验,考察对水体污染物去除过程。结果表明,2种运行方式下对水体NH⁺₄-N去除率都在85%以上,其中以1 h为循环周期的运行方式去除率达97%,较静态提高12.8%;TN去除率最高为84%;TP去除不稳定,过程缓慢。煤渣层对NH⁺₄-N的去除效果差,硝化作用不彻底与反硝化作用的加强使下层出水NH⁺₄-N 、NO^-₂-N及NO^-₃-N浓度均高于上层。提高循环速率有利于对氮的去除。     

反渗透处理稀土氨氮废水试验研究

根据稀土冶炼厂排放的碳铵沉淀洗涤废水的水质情况,采用NH4Cl和 NaCl模拟废水进行了反渗透可行性对比实验。模拟实验发现,在相同条件下反渗透对NaCl 较NH₄Cl 有着更高的去除率,而NH₄Cl 相对NaCl则有着更高的产水速率。实际废水试验结果表明,在恒定操作压力范围内回收率为65%的条件下,NH₄Cl浓度为2.85 g/L的碳铵沉淀洗涤废水经反渗透处理其NH₄Cl去除率为77.3%,可作为氨氮废水的预处理。对该废水处理成本进行了分析,得出其约为2.7元/m³,比相近浓度氨氮废水的氨吹脱处理成本节省约26%。     

高锰酸钾降解地下水中PCE的研究

以氯代有机污染物中常见的PCE为目标污染物,以自制高锰酸钾溶液为氧化剂,采用批实验方法,探讨了高锰酸钾降解PCE的反应动力学、影响因素以及反应机理。反应结果表明,高锰酸钾降解PCE的反应符合一级动力学方程,反应活化能E为57.119 kJ/mol,在30℃条件下,反应速率常数为0.0076 min^-1,半衰期为91.20 min。在pH在3～10,离子强度在0～0.1030 mol/L之间变化时,反应速率不受明显影响。