壳聚糖衍生物的合成及其絮凝性能的研究

对从虾蟹壳中制备的壳聚糖进行改性，分别制得壳聚糖衍生物——壳聚糖季铵盐和羧甲基壳聚糖，用于味精废水的絮凝实验。实验结果表明，壳聚糖、壳聚糖季铵盐和羧甲基壳聚糖作为絮凝剂处理味精废水均有较好的效果，以壳聚糖季铵盐的效果最好，其pH值适用范围宽、絮体沉降快，是一种具有良好反应活性的高分子絮凝剂。     

壳聚糖季铵盐处理玉米酒精清糟液的研究

介绍了新型高效无毒天然高分子混凝剂壳聚糖季铵盐（GTCC）的制备，将GTCC和壳聚糖对玉米酒精发酵清糟液分别进行絮凝处理，结果表明，GTCC的絮凝效果明显优于壳聚糖，以黑龙江肇东华润金玉酒精厂清糟作为研究对明，当GTCC投加量为3mg/L（用量仅为壳聚糖的二十分之一左右）时，CODCr的去除率率达到25％，浊度去除率达78％，初步分析表明，壳聚糖季胺盐强的电中和能力是具有好的絮凝能力的主要原因。     

改性壳聚糖-凹凸棒石复合絮凝剂絮凝采收小球藻

用3-氯-2-羟丙基氯化铵(CTA)季铵化改性壳聚糖(CTS),制备了季铵化改性壳聚糖(CTS-CTA);将壳聚糖(CTS)、阳离子淀粉(CS)、二甲基二烯丙基氯化铵(DMDAAC)进行三元接枝共聚,制备了三元接枝改性壳聚糖(CTS-DMDAAC-CS)。并且比较了壳聚糖(CTS)、季铵化改性壳聚糖(CTS-CTA)、三元接枝改性壳聚糖(CTS-DMDAAC-CS)对小球藻的絮凝效果,选择三元接枝改性壳聚糖与凹凸棒石进行复配,确定了最佳絮凝条件为:p H=8,絮凝剂与凹凸棒石的比例为1∶14,沉降时间为20 min,絮凝剂投加量为0.4 g。在该条件下进行了重复实验,得出小球藻的絮凝率为98.8%,并且絮体紧密、沉降速度快,不需要再次分离,具有很好的应用前景。     

壳聚糖改性粘土对高藻水中藻类的絮凝去除

对壳聚糖改性粘土用于天然高藻水中藻类的絮凝去除进行了研究。实验表明,经壳聚糖改性后的粘土对高藻水中藻细胞有较好的去除效果。粘土的种类对除藻效果有一定影响,其中以高粘凹凸棒石为最佳,其最佳投加量为66mg/L(壳聚糖6 mg/L),此时的叶绿素去除率达到95.45%。相比单独投加壳聚糖,粘土的加入增加了絮体密实度,减少了絮体体积,并使絮体分布更均匀。粘土的粒径对絮凝效果基本没有影响,粒径范围在25～74μm时,改性粘土对藻细胞的凝聚效果是一致的。经壳聚糖改性的粘土在酸性条件下絮凝效果较好,当pH值大于7时,其絮凝能力迅速下降。     

活化粉煤灰改性壳聚糖絮凝除藻的研究

将活化后的粉煤灰滤液对壳聚糖进行改性,研究其絮凝除藻性能.实验表明,改性后的壳聚糖除藻性能优良,较少的用量(0.5 mL)可去除接近90%的藻.而分泌可溶性的胞外有机物(EOM)会优先争夺絮凝剂--壳聚糖,导致其投加量增加.适当增加改性壳聚糖投加量可以使藻絮体密实,增强抗水流冲击能力,由此展开改性壳聚糖投加量与絮凝除藻的动力学研究.最后,测定了絮凝上清液的藻光合活性,发现投加改性壳聚糖后有效降低了藻光合活性,防止水华二次爆发.     

壳聚糖-纳米金属絮凝剂絮凝沉降水华蓝藻研究

研究了壳聚糖与纳米钛、纳米铁或妫水湖沉积物絮凝剂絮凝沉降水华蓝藻的效果。结果表明:在壳聚糖浓度为3 mg/L情况下,与妫水湖沉积物和纳米钛相比,纳米铁絮凝沉降蓝藻细胞的效果最好,在10 min内可以絮凝沉降79.5%以上的水华蓝藻细胞。进一步研究显示,在pH值为5~9的范围内,随着pH值的降低,絮凝沉降藻细胞的效率逐渐提高,pH值为5时10 min内可以絮凝去除89.6%以上的水华蓝藻细胞,具有重要的研究价值与应用价值。     

改性壳聚糖复合凹凸棒土絮凝油漆废水

将壳聚糖、阳离子淀粉和二甲基二烯丙基氯化铵(DMDAAC)进行三元接枝共聚,制备了三元接枝改性壳聚糖(CTS-DMDAAC-CS),通过红外光谱和扫描电镜对其结构进行了表征。并且将三元接枝改性壳聚糖与凹凸棒土进行优化复配,对油漆废水进行了絮凝实验,得出了当pH=12,沉降时间为20 min,复合絮凝剂投加量为0.2 g,三元接枝共聚物∶凹凸棒土=1∶10时,该复合絮凝剂对油漆去除率最佳能够达到89.3%,并且絮凝效果好,是一种新型绿色环保的有机-无机复合絮凝剂。     

高效絮凝剂壳聚糖螯合剂的研制及其絮凝效果的研究

研究了用海虾，蟹壳为原料制取的壳聚糖的方法，并运用其螯合絮凝作用，对含蛋白废水，染色废水和电镀废水进行处理试验，结果表明，壳聚糖是一种用途很广且极富开发应用价值的天然高分子絮凝剂。     

高效絮凝剂壳聚糖螯合剂的研制及其絮凝效果的研究

研究了用海虾、蟹壳为原料制取壳聚糖的方法，并运用其螯合絮凝作用，对含蛋白废水、染色废水和电镀废水进行处理试验。结果表明，壳聚糖是一种用途很广且极富开发应用价值的天然高分子絮凝剂。     

丙烯酰胺改性壳聚糖絮凝剂处理焦化废水

合成了丙烯酰胺改性壳聚糖絮凝剂;用该絮凝剂处理了A/O工艺处理后的焦化废水.考察了pH值、絮凝剂用量及搅拌时间对去除污染物的影响.实验结果表明,当絮凝剂用量为50.0 mg·L-1,絮凝pH值为6.5,絮凝搅拌时间为12 min,COD、F-和色度的去除率分别达到64.7%、93.2%和75%;丙烯酰胺改性壳聚糖絮凝剂对焦化废水的深度处理效果优于聚合硫酸铁和聚合氯化铝絮凝剂.     

改进彩管行业含铬废水处理工艺

针对彩管行业含铬废水处理工艺存在的不足,分别从还原剂和混凝剂两方面进行改进。通过比较和分析,最终提出了采用FeSO4作为还原剂处理含铬废水,氧化还原反应pH调节范围扩大,运行安全系数提高;利用新型高效混凝剂配合泥回流工艺,化学药品用量大幅下降,出水COD和SS含量显著减少。     

改进彩管行业含铬废水处理工艺

针对彩管行业含铬废水处理工艺存在的不足,分别从还原剂和混凝剂两方面进行改进.通过比较和分析,最终提出了采用FeSO4作为还原剂处理含铬废水,氧化还原反应pH调节范围扩大,运行安全系数提高;利用新型高效混凝剂配合泥回流工艺,化学药品用量大幅下降,出水COD和SS含量显著减少.     

Gladius and its derivatives as potential biosorbents for marine diesel oil

The demand for low cost and effective materials to remove contaminants such as residues of oil spills has encouraged studies on new biosorbents produced from wastes. Considering the overgeneration of fishing residues and the necessity to provide an alternative purpose for such materials, this study aimed to evaluate squid gladius and its derivatives (β-chitin and chitosan) as sorbents to remove marine diesel oil (MDO) from fresh and artificial seawater. It was also executed an attempted to improve their performances through a high-intensity ultrasound treatment (UT-gladius and UT-β-chitin). All sorbents removed MDO at both salinities. Contact surface area, salinity, and water retention seemed to play a key role in the outcomes. UT-β-chitin’s performance was significantly superior to β-chitin’s and chitosan’s in MDO removal at salinity 0, as well as at salinity 30, where gladius and UT-gladius also excelled. Ultrasound treatment improved the oil removal performance of UT-β-chitin by increasing its contact surface area. This is the first report on the efficiency of gladius and UT-β-chitin for such purpose, and brought up huge possibilities and new questions that can lead to the achievement of biosorbents of great efficiency.     

Preparation of alginate-chitosan hybrid gel beads and adsorption of divalent metal ions

Naturally occurring polysaccharides such as alginic acid and chitosan have been recognized as one of the most effective adsorbents to eliminating low levels of heavy metal ions from waste water stream. The present study intended to use alginic acid and chitosan simultaneously, which are expected to form a rigid matrix structure of beads due to electrostatic interaction between carboxyl groups on alginic acid and amino groups on chitosan, and to prepare alginate-chitosan hybrid gel beads. This could be achieved for the first time by using water-soluble chitosan, which was obtained by deacetylating chitin to 36-39% degree. The water-soluble chitosan dissolved in water could remain in solution in the presence of sodium alginate, and the homogeneous solution of chitosan and alginate was dispensed into a CuCl2 solution to give gel bead particles. The resultant beads were then reinforced by a cross-linking reaction of aldehyde groups on glutaraldehyde with amine groups on the chitosan. The cross-linking reaction made the beads durable under acidic conditions. The adsorption of Cu(II), Co(II), and Cd(II) on the beads was significantly rapid and reached at equilibrium within 10 min at 25 degrees C. Adsorption isotherms of the metal ions on the beads exhibited Freundlich and/or Langmuir behavior, contrary to gel beads either of alginate or chitosan showing a step-wise shape of adsorption isotherm.     

负载壳聚糖膨润土的制备及其吸附性能的影响

以天然膨润土和壳聚糖为原料，制得一种新型水处理剂——负载壳聚糖膨润土，研究了制备条件对酸性大红印染废水处理效果的影响。实验表明，当壳聚糖的浓度为30 g/L、膨润土质量与壳聚糖溶液体积之比为0.7、浸泡时间80 min、微烘时间15 min时，壳聚糖改性膨润土对酸性大红印染废水的脱色率可达97%。对改性土进行比表面积测定、电镜扫描及X-射线衍射等结构特性分析，证明壳聚糖的引入改变了膨润土在水中的分散状态，增强了其对污染物的吸附和离子交换能力。     

绿色絮凝剂PAS的性能及混凝机理探讨

通过向聚硅酸中加入一种高价亲生物环保的金属离子Ti⁴⁺，制备了一种适合处理长江水的绿色絮凝剂PAS，并且通过实验确定了其处理长江水的最佳处理条件：酸性聚硅酸与Ti金属盐溶液复合，n_Ti/n_Si=0.3；投加量为10 mg/L（以Ti⁴⁺计），pH=6～8，UV254的去除率＞61.7％，浊度去除率＞99％。PAS的混凝效果明显优于聚合铝和聚硅铝，而且矾花形成迅速，絮体密实、沉降快、出水更加清澈，无残留铝。Ti也是亲生物金属，健康环保。因此，PAS是绿色环保友好型絮凝剂，可作为饮用水专用絮凝剂。观察所形成絮体的形貌以及观测红外光谱图均发现，絮凝剂对胶体颗粒污染物有较好的架桥网捕与络合反应作用。     

Effect of water treatment residuals on soil phosphorus, copper and aluminium availability and toxicity

Water treatment residuals (WTRs) are produced by the treatment of potable water with coagulating agents. Beneficial recycling in agriculture is hampered by the fact that WTRs contain potentially toxic contaminants (e.g. copper and aluminium) and they bind phosphorus strongly. These issues were investigated using a plant bioassay (Lactuca sativa), chemical extractions and an isotopic dilution technique. Two WTRs were applied to an acidic and a neutral pH soil at six rates. Reductions in plant growth in amended soils were due to WTR-induced P deficiency, rather than Al or Cu toxicity. The release of potentially toxic Al from WTRs was found to be mitigated by their alkaline nature and pH buffering capacity. However, acidification of WTRs was shown to release more soluble Al than soil naturally high in Al. Copper availability was relatively low in all treatments. However, the lability of WTR-Cu increased when the WTR was applied to the soil.     

A study on the evaluations of emission factors and uncertainty ranges for methane and nitrous oxide from combined-cycle power plant in Korea

In this research, in order to develop technology/country-specific emission factors of methane (CH₄) and nitrous oxide (N₂O), a total of 585 samples from eight gas-fired turbine combined cycle (GTCC) power plants were measured and analyzed. The research found that the emission factor for CH₄ stood at “0.82 kg/TJ”, which was an 18 % lower than the emission factor for liquefied natural gas (LNG) GTCC “1 kg/TJ” presented by Intergovernmental Panel on Climate Change (IPCC). The result was 8 % up when compared with the emission factor of Japan which stands at “0.75 kg/TJ”. The emission factor for N₂O was “0.65 kg/TJ”, which is significantly lower than “3 kg/TJ” of the emission factor for LNG GTCC presented by IPCC, but over six times higher than the default N₂O emission factor of LNG. The evaluation of uncertainty was conducted based on the estimated non-CO₂ emission factors, and the ranges of uncertainty for CH₄ and N₂O were between ?12.96 and +13.89 %, and ?11.43 and +12.86 %, respectively, which is significantly lower than uncertainties presented by IPCC. These differences proved that non-CO₂ emissions can change depending on combustion technologies; therefore, it is vital to establish country/technology-specific emission factors.