珠江口水体中铜与悬浮颗粒物相互作用的研究

使用无机离子交换法研究珠江口水体中铜与悬浮颗粒物的相互作用，测出钢与悬浮颗粒物相互作用的ｐＨ曲线呈Ｓ形，其分级离子交换等温线是一种新的“台阶”型；从分级离子交换理论求得分级平衡常数Ｋ１为５．０，Ｋ２为７８．１，珠江口水体中铜的表观络合容量为０．９２μｍ及其条件稳定常数为３．５×１０７。     

渝东南地区下寒武统牛蹄塘组页岩孔径分布测试方法研究

低温氮气吸附法已普遍用于评价页岩的孔隙结构,但是文献中报道的脱气温度和脱气时间等测试条件不尽相同,此外测试结果中经常出现滞后环不闭合的情况,严重影响了孔径分布等结构参数测试的准确性。为了评价和探索有效的页岩孔径分布测试方法,本文选取渝科1井下寒武统牛蹄塘组黑色页岩,重点研究应用低温氮气吸附法分析其孔径分布的测试条件,系统探讨了样品质量、脱气温度、升温速率和脱气时间对测试结果的影响,通过进一步优化参数建立了可靠的孔径分布测试方法,并成功用于测定其他页岩样品。结果表明:吸附-脱附等温线呈反C型,属于Brunauer等提出的BDDT等温吸附曲线分类中的V型,滞后环完全闭合,属于IUPAC分类中的H4型,对应狭窄的狭缝型孔隙,说明此类页岩中除了含有峰值孔径主要集中在3.5~4.5 nm的中孔和一定数量的大孔外,还存在大量微孔。研究认为脱气温度是影响测试结果的主要因素。该研究是页岩孔径分布测试方法的一项补充,为我国页岩气的深入研究提供了关键参数支持。     

Mechanisms and factors affecting the adsorption of sodium alginate onto modified clays

Algal organic materials (AOMs) are one critical factor affecting the efficiency of modified clays used for the mitigation of harmful algal blooms (HABs). This study was conducted to develop a deeper understanding of the mechanisms and factors affecting the adsorption of AOMs onto modified clays. Sodium alginate (polysaccharide) and kaolinite modified with polyaluminium chloride (PACl) were used as AOMs and modified clay model substances, respectively, and the effects of modifier dosage, contact time, solution pH and ionic strength were investigated through batch adsorption experiments. Kinetics revealed that the alginate adsorption rate was described well by a pseudo-second order model. PACl effectively enhanced the adsorption capacity of kaolinite and increased the adsorption rate, and the optimum additive amount of PACl was 5%. The experimental data fitted both the Freundlich and Langmuir adsorption equations well. The adsorption thermodynamics for alginate onto modified clays suggests that alginate adsorption is a spontaneous process. The adsorption of alginate onto modified clays was highly dependent on pH, with a decrease in adsorption observed with increased pH to 9.48, but the opposite was true above pH 9.48. Finally, adsorption increased with increasing ionic strength.     

Partitioning of Fluoroquinolones on Wastewater Sludge

Laboratory‐scale batch experiments were conducted to investigate the adsorption behavior of eight fluoroquinolones (FQs) on aerobic, anoxic, and anaerobic sludge, under different adsorpiton time, pH, and temperature conditions. Results indicated that adsorption of FQs onto all sludge was a physical sorption process. The relationship of the partitioning coefficient (K_d) and the octanol/water partition coefficient (K_ow) for each FQ was established. The adsorbed fraction of FQs on sludge could then be predicted with the K_d. It was calculated that about 50–72% of the FQs were adsorbed on the sludge. Therefore, the adsorption effect must be considered when studying the fate and occurrence of FQs in wastewater treatment systems.     

Rice Husk Ash as a Low Cost Adsorbent for the Removal of Methylene Blue and Congo Red in Aqueous Phases

Adsorption is of significant importance for effluent treatment, especially for the treatment of colored effluent generated from the dyeing and bleaching industries. Low cost adsorbents have gained attention over the decades as a means of achieving very high removal efficiencies to meet effluent discharge standards. The present article reports on batch investigations for color removal from aqueous solutions of Methylene Blue (MB) and Congo Red (CR) using Rice Husk Ash (RHA) as an alternative low cost adsorbent. The performance analysis was carried out as a function of various operating parameters, such as initial concentration of dye, adsorbent dose, contact time, shaker speed, interruption of shaking and ionic concentration. Performance studies revealed that a very high percentage removal of color was achievable for both dyes. The maximum percentage removal of MB was 99.939%, while 98.835% removal was observed for CR. These percentage removals were better than existing systems. Detailed data analysis indicated that adsorption of MB followed the Temkin isotherm, while CR followed the Freundlich isotherm. These isotherms were feasible within the framework of experimentation. Batch kinetic data, on the other hand, indicated that pseudo second order kinetics governed adsorption in both cases. Sensitivity analysis further indicated that the effects of initial dye concentration, shaker speed, pH and ionic strength had no noticeable effect on the percentage dye removal at equilibrium. Batch desorption studies revealed that 50% acetone solution was optimum for CR, while desorption of MB varied directly with acetone concentration.     

Supercritical gas sorption on moist coals

The effect of moisture on the CO₂ and CH₄ sorption capacity of three bituminous coals from Australia and China was investigated at 55 °C and at pressures up to 20 MPa. A gravimetric apparatus was used to measure the gas adsorption isotherms of coal with moisture contents ranging from 0 to about 8%. A modified Dubinin–Radushkevich (DR) adsorption model was found to fit the experimental data under all conditions. Moisture adsorption isotherms of these coals were measured at 21 °C. The Guggenheim–Anderson–de Boer (GAB) model was capable of accurately representing the moisture isotherms over the full range of relative pressures.Moist coal had a significantly lower maximum sorption capacity for both CO₂ and CH₄ than dry coal. However, the extent to which the capacity was reduced was dependent upon the rank of the coal. Higher rank coals were less affected by the presence of moisture than low rank coals. All coals exhibited a certain moisture content beyond which further moisture did not affect the sorption capacity. This limiting moisture content was dependent on the rank of the coal and the sorbate gas and, for these coals, corresponded approximately to the equilibrium moisture content that would be attained by exposing the coal to about 40–80% relative humidity. The experimental results indicate that the loss of sorption capacity by the coal in the presence of water can be simply explained by volumetric displacement of the CO₂ and CH₄ by the water. Below the limiting moisture content, the CO₂ sorption capacity reduced by about 7.3 kg t^− 1 for each 1% increase in moisture. For CH₄, sorption capacity was reduced by about 1.8 kg t^− 1 for each 1% increase in moisture.The heat of sorption calculated from the DR model decreased slightly on addition of moisture. One explanation is that water is preferentially attracted to high energy adsorption sites (that have high energy by virtue of their electrostatic nature), expelling CO₂ and CH₄ molecules.     

注入CO2提高煤层气产能的可行性研究

根据煤储层吸附一解吸机理,首次采用“解吸一注气一解吸”的实验方法,分别进行CH4,CO2的吸附一解吸和CO2注入置换煤层CH4实验,模拟了煤层气井“排采一注气一排采”的增产途径和效果。结果表明：在CH4和CO2二元体系的竞争吸附中,CO2组分的吸附速率是先快后慢,而CH4组分的吸附速率先慢后快,解吸时则相反,反映出CO2在竞争吸附中占据优势;注入CO2气体的数量越大和相对浓度越高,单位压降CH4解吸率和CO2吸附率就越高。实验结论对工业规模的煤层气开发试验具有指导意义。