ClO_2对活性艳红K—2G和分散蓝2BLN染料的脱色研究

本论文主要利用自制高纯二氧化氯对两种常用且结构具有代表性的活性艳红K— 2G和分散蓝 2BLN料染 ,进行氧化脱色研究 ,作了温度 ,pH值 ,二氧化氯用量等条件试验 ,并用实际印染废水进行了实验 ,取得了良好的效果。在室温时 ,t =5min～ 7min ,pH值偏碱性条件下 ,单一染料溶液及混合染料溶液的脱色率均达到 90 %以上 ,实际印染废水的脱色也在 90 %左右。pH值、温度和ClO2 用量等多种因素对脱色率均有一定的影响 :pH值越高 ,染料脱色率越高。ClO2 用量存在一最佳值 ,与活性艳红K— 2G及分散蓝 2BLN染料的最佳摩尔比分别为 4 0及 2 0左右。ClO2 耗量随染料起始浓度的增大而增加 (脱色率相同时 )     

固定化真菌漆酶对分散兰-2BLN的脱色和降解

采用改良壳聚糖固定化的真菌漆酶对染料分散兰-2BLN进行脱色和降解条件的研究,探索了固定化漆酶活力、处理时间、染料浓度、温度和pH对其降解效果的影响。结果表明,固定化漆酶脱色降解分散兰-2BLN的适宜条件为：固定化漆酶活力18.2U／mL,染料浓度100mg／L,温度40℃,pH4.6,在上述条件下降解1.5h,分散兰-2BLN脱色率能达到87.68％。重复分批使用固定化漆酶处理2BLN兰,在使用6批次后,脱色率仍能保持在55％以上,其催化效率得到了较大提高。     

蒽醌染料活性艳蓝KN-R的化学氧化脱色和矿化

研究了使用NaClO化学氧化处理活性艳蓝KN-R模拟染料废水。分别以592nm、380nm、255nm波长处的吸光值为主要指标,跟踪染料的脱色降解。考察了NaClO投加量、染料浓度、温度和13H值等主要因素对模拟废水脱色的影响。结果表明：用NaClO化学氧化处理0．1mmolL^-1的活性艳蓝KN-R模拟染料废水,当NaClO与染料的摩尔比为18,T=30℃,13H值为7时,反应30分钟,脱色率可达到100％。pH值对脱色和TOC的去除有很大影响,酸性或中性条件下,染料快速脱色,30分钟后吸光值基本恒定,反应6个小时TOC的去除仍不明显;碱性条件下,染料缓慢脱色,但反应6个小时TOC的去除率可以达到40％左右。     

青霉菌X5对活性艳蓝KN-R脱色研究

采用梯度平板筛选法，从染布厂废水池污泥中分离到一株对蒽醌染料KN－R有较强脱色能力的青霉菌X5（Penicillium sp.)，并考察该菌在不同温度，pH，培养时间，染料浓度，菌量及不同碳源氮源条件下对活性艳蓝KN－R的脱色情况，结果表明,在20－40℃温度范围内该菌对活性艳蓝KN－R的脱色率均在95％以上，其最佳脱色温度为25℃，pH为4．0，培养时间为48h，染料浓度，菌量对染料脱色有一定影响，该菌对碳源、氮源具有较宽适应范围，在最佳条件下，该菌对染料的脱色率达99．3％。     

TiO2光催化降解有机颜料艳红RGS母液研究

以TiO2为催化剂,对有机颜料艳红RGS母液进行了一系列光催化降解试验.考察了催化剂用量、溶液pH值、初始浓度、不同光源和照射时间对脱色率的影响.结果表明,溶液相对初始浓度为0.2、pH<8、催化剂用量为1g/L时,以紫外灯(254nm)为光源,反应120 min,脱色率可达93%以上.     

无花果曲霉菌丝球对活性艳蓝KN-R的脱色研究

生物吸附法是染料废水处理中很有前途的一种方法。本文将培养的无花果曲霉菌丝球用于蒽醌染料活性艳蓝KN-R的脱色，研究了培养时间、温度、转速、pH值及盐浓度、不同碳源、不同氮源对菌丝球脱色的影响；比较了活菌与死菌的脱色效果；探讨了菌丝球重复利用对脱色率的影响。结果表明：培养时间为72h，温度为33℃，转速为150rpm，pH值为6．0，盐浓度为0.5％，以乳糖为碳源、硝酸钠为氮源时，菌丝球对活性艳蓝KN-R的脱色效果最好：活菌对染料的吸附性能比死菌好；菌丝球在重复利用了四次后，脱色率仍达85．7％。     

染料废水脱色的物理化学处理技术

染料废水目前主要的脱色方法有吸附、混凝、氧化还原和生化法.活性炭吸附适用于低浓度的染料废水处理.聚硅硫酸铁混凝效果与Fe/SiO4摩尔比和pH值相关.氢氧化镁可有效去除印染废水中的直接红染料.有机絮凝剂往往需要和其它药剂复配.氧化法脱色率大,但成本高昂,且受染料废水的组成、氧化性及pH值影响.还原法药剂价格低廉,但还原降解产物具有毒性,必须经过二次处理.生物法成本较低,又受制于染料的生物降解性.因此发展多种手段联合应用已是当前染料废水处理的研究方向.     

茄子秸杆活性炭对染料废水的吸附性能研究

以茄子秸秆为原料,ZnCl2为活化剂制备粉末状活性炭,主要研究了活性炭对染料废水的吸附性能;以活性红X-3B和酸性蓝RL为模型染料,考察了染料初始浓度、pH值、活性炭投加量和吸附时间等对染料脱色率的影响。结果表明,染料初始浓度和活性炭投加量对染料脱色率影响较大。初始浓度为300mg／L时,活性炭的最佳投加量分别为1g／L和1．4g／L;在最佳工艺条件下,脱色率分别在93％和98％以上,COD去除率分别为94．5％和86．4％,出水水质达到国家一级《纺织染整工业水污染物排放标准》（GB 4287—1992）。     

阳离子艳红染料的光催化降解

本文研究了以沉淀法制备的TiO2为催化剂，紫外杀菌灯为光源，对阳离子艳红染料进行光催化降解的可行性，结果表明，在实验条件下，本系统对阳离子艳红染料有明显的降解效果，浓度为10mg/L的阳离子艳红染料经过30min的处理，其降解率＞88％，此外，还探讨了溶液初始pH值，催化剂的投加量，光照距离和液层高度等因素对光降解反应的影响。     

真菌产漆酶对蒽醌类染料脱色的研究

以香菇发酵获得漆酶粗酶液,用该酶液对蒽醌类染料进行脱色研究,分别考察了反应温度、pH值、时峰、漆酶浓度和不同染料的脱色影响.结果表明,香菇产漆酶粗酶液对蒽醌类染料具有良好的脱色效果,脱色最佳条件为：温度在30℃左右、pH3-4、反应8h、酶单位在20-30U/L的脱色率达85％.     

二氧化碳回收技术进展

CO2的过量排放对全球的气候变暖有着不可推卸的责任,同时CO2又是一种重要的碳资源,对它的回收和利用将具有很大的经济效益和社会效益。CO2回收的方法主要是膜吸收法、变压吸附法、化学吸收法和低温分离法,特别是离子液体对CO2的吸收,为CO2的减排提供了良好的手段。     

Experimental investigation of the CO2 sealing efficiency of caprocks

Using a combination of experimental (petrophysical and mineralogical) methods, the effects of high-pressure CO₂ exposure on fluid transport properties and mineralogical composition of two pelitic caprocks, a limestone and a clay-rich marl lithotype have been studied. Single and multiphase permeability tests, gas breakthrough and diffusion experiments were conducted under in situ p/T conditions on cylindrical plugs (28.5 mm diameter, 10–20 mm thickness).The capillary CO₂ sealing efficiency of the initially water-saturated sample plugs was found to decrease in repetitive gas breakthrough experiments on the same sample from 0.74 to 0.41 MPa for the limestone and from 0.64 to 0.43 MPa for the marl. Helium breakthrough experiments before and after the CO₂ tests showed a decrease in capillary threshold (snap-off) pressure from 1.81 to 0.62 MPa for the limestone.Repetitive CO₂ diffusion experiments on the marlstone revealed an increase in the effective diffusion coefficient from 7.8 × 10^?11 to 1.2 × 10^?10 m².Single-phase (water) permeability coefficients derived from steady-state permeability tests ranged between 7 and 56 nano-Darcy and showed a consistent increase after each CO₂ test cycle. Effective gas permeabilities were generally one order of magnitude lower than water permeabilities and exhibit the same trend. XRD measurements performed before and after exposure to CO₂ did not reveal any distinct change in the mineral composition for both samples. Similarly, no significant changes were observed in specific surface areas (determined by BET) and pore-size distributions (determined by mercury injection porosimetry). High-pressure CO₂ sorption experiments on powdered samples revealed significant CO₂ sorption capacities of 0.27 and 0.14 mmol/g for the marlstone and the limestone, respectively.The changes in transport parameters in the absence of detectable mineral alterations may be explained by carbonate dissolution and further precipitation along a pH profile across the sample plug which would not be subject to quantitative mineral alteration.     

Performance of lime-BHA solidified plating sludge in the presence of Na2SiO3 and Na2CO3

This research investigated the performance of lime-BHA (black rice husk ash) solidified plating sludge with 2 wt% NaO from Na(2)SiO(3) and Na(2)CO(3) at the level of 0, 30 and 50 wt%. The sludge was evaluated for strength development, leachability, solution chemistry and microstructure. The lime-BHA solidified plating sludge with Na(2)SiO(3) and Na(2)CO(3) had higher early strength when compared to the control. The addition of Na(2)SiO(3) and Na(2)CO(3) increased the OH(-) concentration and decreased the Ca(2+) and heavy metal ions in solution after the first minute. The XRD patterns showed that the addition of Na(2)SiO(3) resulted in the formation of calcium silicate hydrates, while the addition of Na(2)CO(3) resulted in CaCO(3). The heavy metals from the plating sludge, especially Zn, were immobilized in calcium zincate and calcium zinc silicate forms for the lime-BHA with and without Na(2)SiO(3) solidified wastes, while samples with Na(2)CO(3) contained Zn that was fixed in the form of CaZnCO(3). The cumulative leaching of Fe, Cr and Zn from the lime-BHA solidified plating sludge decreased significantly when activators were added, especially Na(2)CO(3).     

Economic evaluation of the geological storage of CO2 considering the scale of economy

CO₂ capture and storage (CCS) technology is expected to play an important role in the efforts directed toward long-term CO₂ emission reduction. This paper analyzes the cost of the geological storage of CO₂ in Japan in order to consider future research, development and deployment (RD&D); these would be based on the information of the obtained cost structure. According to the analysis results, the costs, particularly those of the transportation by pipeline and of CO₂ injection, strongly depend on the scale of the facilities. Therefore, the distance of the transportation of CO₂ should be minimized in the case of small-scale storage, particularly in Japan. In addition, the potential injection rate per well is another key factor for the injection cost. Based on the analyzed cost, the injection cost of the geological storage of CO₂ in Japan for individual storage sites is estimated, and the cost–potential curve is obtained. A mixed-integer programming model has been developed to take into account these characteristics of the CCS technology and its adverse effects arising from the scale of economy with regard to the transportation and injection cost for the geological storage of CO₂. The model is designed to evaluate CCS and other CO₂ mitigation technologies in the energy systems of Japan. With all these adverse effects due to the scale of economy, the geological storage of CO₂ will be one of the important options for CO₂ emission reduction in Japan.     

温室气体二氧化碳的分离回收与综合利用

目前许多工业生产废气中都含有高浓度二氧化碳,排到大气中既造成了环境污染又浪费了宝贵的碳资源,其带来的“温室效应”给人类造成的危害越来越受到世界各国的高度重视。文章阐述了二氧化碳回收方法的原理及工艺特点,分析了各工艺的优缺点及适应性,为回收利用二氧化碳提供了技术依据,并指出了二氧化碳的应用范围和前景。     

大气中SO2的液相氧化研究

大气中ＳＯ２液相氧化是形成酸雨的重要途径，降雨中含有各种无机离子和有机物质，它们可能催化或抑制液相氧化反应的进行。本文根据四川酸雨样品组成，进行了ＳＯ２在模拟雨水及实际雨水中的氧化实验，考查了Ｖ，Ｆｅ，Ｍｎ等离子对ＳＯ２氧化的催化作用，Ｈ２Ｏ２对ＳＯ２的氧化以及降水中有机物质甲醛对各反应的影响。实验结果为了解酸雨的成固，研究酸雨控制对策提供了科学依据。     

负载型TiO2薄膜光催化剂降解亚甲基蓝

采用溶胶-凝胶法制备了玻璃负载的TiO2薄膜光催化剂,研究了该催化剂对亚甲基蓝溶液的光催化降解,考察了反应时间、水样的初始浓度、溶液的pH等对光催化降解效果的影响。     

Natural analogue of the rise and dissolution of liquid CO2 in the ocean

The behavior of natural carbon dioxide (CO₂) droplets (8–10 mm in diameter) were observed in a seafloor hydrothermal system at the Okinawa Trough. The natural CO₂ droplet contain 95–98% of CO₂, 2–3% of H₂S, and other gas species. The ascending CO₂ droplets were tracked by a remotely operated vehicle (ROV), and depth, temperature, salinity, pH and partial pressure of CO₂ (pCO₂) in seawater near the CO₂ droplets were measured during droplet ascent by a conductivity-temperature-depth sensor (CTD) and in situ pH/pCO₂ sensor. The visual images of the rising CO₂ droplets were recorded with a high definition television camera on the ROV. A mapping survey (400 m × 400 m; 4 horizontal layers) revealed a dominant distribution of low pH area over the natural CO₂ venting site. The size and rise rate of CO₂ droplets decreased during their ascent in the water column from depths of 1424 to 679 m (a tracking interval of 745 m). The CO₂ droplets dissolved gradually to become small flakes of CO₂ hydrate while rising, and these ascending flakes were found to disappear at 679 m depth. Although a pH as low as 5 was detected just above the liquid CO₂ venting site on the seafloor, no detectable pH depression in the water column ambient to the rising CO₂ droplets was observed. The results of the pH mapping survey showed only localized pH depression over the CO₂ venting site.     

Evaluating the impact of fractures on the performance of the In Salah CO2 storage site

The In Salah Gas Joint Venture CO₂ storage project has been in operation in Algeria since 2004 and is currently the world's largest onshore CO₂ storage project. CO₂ is injected into the saline aquifer of a gas reservoir several kilometres away from the gas producers. Current focus in the project is on implementing a comprehensive monitoring strategy and modelling the injection behaviour in order to ensure and verify safe long-term storage. A key part of this effort is the understanding of the processes involved in CO₂ migration within relatively low-permeability sandstones and shales influenced by fractures and faults. We summarise our current understanding of the fault and fracture pattern at this site and show preliminary forecasts of the system performance using discrete fracture models and fluid flow simulations. Despite evidence of fractures at the reservoir/aquifer level, the thick mudstone caprock sequence is expected to provide an effective flow and mechanical seal for the storage system; however, quantification of the effects of fracture flow is essential to the site verification.     

Comparative study of the heats of absorption of post-combustion CO2 absorbents

Heats of absorption of CO₂ with different solvents were measured in this work in a commercially available reaction calorimeter CPA-122 (Chemisens AS, Sweden) as function of temperature, loading and solvent composition over the temperature range from 40 to 120 °C. Studied amines include primary amines (monoethanolamine and 2-amino-2-methyl-1-propanol), tertiary amines (N-methyldiethanolamine and N,N-diethylethanolamine), diamines (1-(2-aminoethyl)-aminoethanol and N-methyl-1,3-propanediamine), triamine (diethylenetriamine), and cyclic amine (piperazine). Combinations of these amines and also mixtures of potassium carbonate and piperazine were tested. Experimental heats of absorption of CO₂ with these systems are compared.