膜基活化溶液中活化剂在回收温室气体CO2过程中的作用

将AMP和PZ作为活化剂添加于MDEA溶液中,形成活化溶液,研究了膜基活化溶液回收温室气体CO2性能,着重考察活化剂的活化作用和对膜接触器传质加强的影响,提出一个活化机理来解释活化现象,建立了阻力层方程模型,并模拟膜基活化溶液回收CO2的传质过程。结果表明,活化剂对膜接触器传质的加强起到重要作用,具有双氨基环状结构的PZ对传质的加强作用高于具有空间位阻结构的AMP;活化溶液的CO2回收率和传质通量明显高于未活化的MDEA溶液,活化性能PZ〉AMP;活化剂的活化效应与分子结构有关;流体力学的改变对传质的影响有限,活化剂的反应动力学对传质的加强起主导作用;阻力层方程模型能较好地模拟膜基活化溶液回收CO2传质过程,传质通量和总传质系数的模型值与实验值符合较好。     

污泥基活性炭吸附Cu2+的应用研究

以城市污水处理厂剩余污泥为原料,以ZnCl₂为活化剂制取污泥基活性炭。以此污泥基活性炭为吸附剂,对含Cu²⁺的废水进行了吸附实验研究。考察了溶液pH值、Cu²⁺的起始浓度对Cu²⁺离子吸附量的影响;利用等温吸附实验作出吸附等温线,并考察了污泥基活性炭吸附剂吸附Cu²⁺的动力学方程。实验结果表明,污泥基活性炭对Cu²⁺具有良好的吸附性能。吸附的最佳pH值为5;吸附符合Langmuir和Freundlich吸附等温方程,吸附为优惠吸附,吸附量随着吸附质溶液浓度的增加而增大;吸附平衡时间为4 h,吸附动力学符合二级动力学方程。     

碳酸根对磷酸钙沉淀反应回收磷的影响简

以模拟的厌氧消化液为处理对象,通过小试实验,考察不同初始磷浓度C_P、Ca/P物质的量比、pH和温度下,碳酸根（CO₃^2-）对磷酸钙沉淀反应回收磷的影响;利用扫描电镜（SEM）、X射线衍射仪（XRD）和傅里叶变换红外光谱（FTIR）对沉淀产物进行表征。结果表明,高浓度的CO₃^2-对以磷酸钙沉淀反应去除和回收磷的效率影响较大;C_P相同时,CO₃^2-浓度（C_CO3^2-）越大,P的去除率越低,低C_P（20 mg/L）时尤为显著;当C_CO3^2-相同时,随着C_P的增大,反应速率加快,P的去除率逐渐升高,但升高幅度越来越小;增大Ca/P比和pH能提高P的去除率,降低CO₃^2-对磷酸钙沉淀反应的抑制作用,综合考虑实际效果,应选择Ca/P比为3.33,pH为9.0作为适宜的反应条件;升高温度对降低CO₃^2-对磷酸钙沉淀反应的抑制作用贡献不大。在C_P为60 mg/L,Ca/P比为1.67,pH为9.0,温度为20℃的条件下,当C _CO3^2-为0时,得到的沉淀产物主要为羟基磷灰石HAP;当C _CO3^2-为30 mmol/L时,得到的沉淀产物为磷酸钙和碳酸合磷灰石的混合物。     

超临界CO2回收线路板工艺研究

采用正交试验设计进行了超临界CO₂回收废弃印刷线路板的实验。以温度、压强、时间和夹带剂为实验因素,通过对实验前后样本在重量、厚度、弯曲强度和断裂强度四方面变化的分析考察了各实验因素对实验效果的影响。实验结果表明,影响超临界CO₂法回收印刷线路板的最主要因素为温度、时间和夹带剂,超临界CO₂法回收废弃印刷线路板的最佳工艺条件：温度270℃,压强大于7.38 MPa,时间3 h,夹带剂(水)160 mL。实验进一步验证了压强对实验结果的非显著性影响。     

钙化物在废弃物基活性炭制备过程中的影响

研究了以城市垃圾中3种典型的固体有机废弃物——锯木屑、纸张和塑料的热解产物(分别简称木炭、纸炭和塑料热解物)为原料,水蒸气为活化剂制备废弃物基活性炭时钙化物含量对活化过程、活性炭吸附性能(以碘值表征)及其孔结构的影响。结果表明,钙化物可加快活化反应的速度,且钙化物含量在1.5％时活化反应速度即已不再随钙化物含量的增加而增加;活性炭的吸附性能则随钙化物含量的增加而减少,同时钙化物对活性炭的孔径分布基本无影响,但降低了活性炭的比表面积、微孔孔容及中孔孔容;钙化物的2种前驱体（即CaO和Ca(OH)₂）对活化过程具有相同的催化作用。     

膜吸收法处理高浓度甲醛废气资源化技术研究

采用疏水性中空纤维膜接触器,以NaHSO₃为吸收液处理高浓度甲醛废气。研究了吸收液流量、吸收液温度、吸收液浓度、气体进口流量和气体进口浓度等因素对甲醛去除率和总传质系数的影响。结果表明,当吸收液流量为4.17×10^-6m³/s,吸收液温度为60℃,甲醛进气流量为3.7×10^-6m³/s,甲醛进气浓度为566 mg/m³时,甲醛出气浓度可低至2.8 mg/m³,甲醛的去除率可达99.5%,总传质系数为4.46×10^-5m/s。反应产物（ɑ-羟基磺酸钠）易分离,并可作为重要的有机合成原料或用于制备高纯甲醛而得到充分利用,NaHSO₃溶液经适当稀释后仍可作为吸收液循环使用。表明膜吸收法可基本实现高浓度甲醛废气处理的资源化。     

污水污泥裂解及其性能的研究

以碘吸附值为裂解残渣吸附性能的指标,通过单因素实验和正交实验,确定了制备裂解残渣的最佳工艺条件,并对残渣的表面元素组成、孔结构组成、晶相组成和吸附性能等性质进行了表征。结果显示：以浓度均为5 mol/L的ZnCl₂和H₂SO₄作活化剂、复配比2∶1、活化温度600℃、活化时间1 h、固液比1∶2.5,制得的裂解残渣酸洗后碘值平均值可达892.8 mg/g;用制备的裂解残渣对苯酚废水进行处理,室温下振荡5 min,苯酚去除率即可达到87.9%,且符合Langmuir吸附等温线方程和Freundlich吸附等温线方程。     

膜气体吸收技术分离VOCs/N2混合气性能的研究

以C₆H₆/N₂混合气为代表,疏水性聚丙烯中空纤维膜为气液接触膜,n-甲酰吗啉(NFM,n-formyl morpholine)水溶液为吸收剂,研究了膜气体吸收法分离VOCs/N₂混合气性能。考察了吸收剂流量、吸收剂体积分数、进口气流量、进口气浓度和膜组件结构等诸因素对分离性能的影响。结果表明,在吸收剂流量为20～100 mL/min,进口气流量为40～300 mL/min,进口气浓度为10.2 mg/L的条件下,苯的去除率为65.0 % ～ 99.6 %,总体积传质系数为0.0157～0.08412 s^-1。实验证明,采用疏水性多孔膜气体吸收法,NFM水溶液吸收分离VOCs/N₂混合气具有较高的分离效率和较快的传质速率。     

应用神经网络方法优化垃圾焚烧模拟灰渣熔点的预测

采用SiO₂、Al₂O₃、CaO、Na₂CO₃、NaCl和Fe₂O₃等物质来模拟垃圾焚烧的真实灰渣组成,通过实验测定模拟灰渣熔点,建立神经网络模型进行熔点预测,由预测结果来指导进一步实验,得到修正的模型,最终预测出的半球温度（HT）平均误差低于5%。     

几种阴阳离子对磷钨酸光催化降解甲基橙的影响

以磷钨酸为光催化剂,在紫外灯照射下,对甲基橙溶液进行光催化降解,考察了几种阴阳离子对磷钨酸光催化降解甲基橙溶液的影响。结果表明：Mg²⁺、Ca²⁺、NO^-₃、SO^2-₄和CO^2-₃均对催化活性有促进作用,其中Mg²⁺和Ca²⁺仅有微弱的促进作用;NO^-₃和SO^2-₄随着浓度的增加促进作用也有所增加;CO^2-₃则随着浓度的增加促进作用呈下降趋势;Mn²⁺、Al³⁺和Cl^-对光解反应存在较强的抑制作用,且Al³⁺和Cl^-随着其浓度的增加,抑制作用增强。     

旋转填充床吸收模拟工业废气中SO2的研究

选择3%SO2作为模拟工业废气,一乙醇胺(MEA)作为吸收剂在超重力条件下对模拟工业废气中脱硫工艺进行了实验研究,考察了旋转填充床转速、气液比、吸收剂入口温度以及吸收剂浓度对脱硫率的影响,确定了MEA作为吸收剂时适宜的操作条件.同时在旋转填充床中考察了几种不同吸收剂对3%SO2脱除率的影响.研究表明,1 mol/L哌嗪...     

微波辐照碳酸钾化学活化法制备菌渣活性炭

以食用菌渣为原料,以K2CO3为活化剂,利用微波辐照加热法制备活性炭。采用正交实验设计,研究了活化功率、活化时间、K2CO3与菌渣质量比、浸渍时间对活性炭碘值及得率的影响。实验结果表明,活化时间、活化功率、K2CO3与菌渣质量比对活性炭碘值影响显著,浸渍时间对活性炭碘值影响不显著;对活性炭得率,各因素影响均不显著。综合考虑碘值和得率2个指标,实验得出的最佳活性炭制备工艺条件为:活化功率560 W,活化时间20 min,K2CO3与菌渣质量比0.8,浸渍时间20 h。     

UTILIZATION OF AGRICULTURAL WASTE CORN COB FOR THE PREPARATION OF CARBON ADSORBENT

In the present study, a series of activated carbons were prepared from agricultural waste corn cob by chemical and physical activations with potassium hydroxide (KOH)/potassium carbonate (K₂CO₃) and carbon dioxide (CO₂). The effect of process variables such as impregnation ratio, impregnation time, activation temperature and soaking time of CO₂ was studied in order to relate these preparation parameters with the physical properties of final carbon products. The resulting activated carbons were characterized by nitrogen adsorption[ch-[chdesorption isotherms at 77 K. The surface areas and pore volumes of carbons were estimated by the BET equation, the Langmuir equation and the t-plot method. Under the experimental conditions investigated, the main parameters in the activation of corn cob were found to be the impregnation ratio and activation temperature. The soaking time of CO₂ is another important variable, which had a strong effect on the pore volume development. The BET surface area and total pore volume were as large as about 2000 m²/g and about 1.0 cm³/g, respectively. This study showed that the activation of agricultural waste corn cob with KOH/K₂CO₃ and CO₂ was suitable for the preparation of large-surface-area activated carbons.     

填料塔中Na_2CO_3吸收高浓度H_2S的传质特性

在填料吸收塔中考察了Na2CO3溶液吸收高浓度H2S气体的气液传质特性。通过测量填料塔进出口气体中H2S浓度计算了Na2CO3溶液吸收高浓度H2S气体的总体积传质系数(KGa),并研究了进气流速、吸收液流量、吸收温度和吸收液浓度对KGa的影响。结果表明,KGa随Na2CO3浓度、吸收液流量的增加而增加,随吸收温度、进气流速的升高而降低;在高浓度H2S吸收过程中液相传质阻力不能忽略。     

Remote sampling of a CO2 point source in an urban setting

High frequency CO₂ and wind speed measurements were used to examine the urban baseline eddy covariance CO₂ flux and analyse the CO₂ rich plume from a local power station. A reliable relationship between high frequency CO₂ maxima and the rate of CO₂ emission at the power station was established. This relationship was shown to be highly dependant on wind speed. The ensemble mean plume was found to be Gaussian in horizontal profile with a width dependant on wind speed. The relationship between peak CO₂ mixing ratio and averaging time was shown to be a simple power law with a time exponent of approximately 0.5. The large, short pulses in CO₂ mixing ratio in the power plant plume were found to have an approximately Lorentzian shape. These pulses generated negative vertical eddy flux measurements so data from the plume sector were necessarily excluded from the flux baseline results. The plume-excluded flux had a similar magnitude and variability to those reported in other urban CO₂ flux studies despite this site not being ideal due to the proximity of roughness elements to the measurement point.     

Forest floor CO2 flux estimated from soil CO2 and radon concentrations

Having a quantitative understanding of the carbon cycle in forests is of great importance for predicting global warming issues. Carbon dioxide production in soil is the largest CO₂ source in forests, and exhibits large temporal and spatial variations. Continuous observation of soil CO₂ flux at many sites over a forest is therefore necessary to obtain representative soil CO₂ fluxes for the forest. In this study, a gradient method to measure soil CO₂ flux indirectly from soil radon and CO₂ measurements was theoretically modified to conveniently measure the soil CO₂ flux from soil radon and CO₂ concentrations measured at one soil depth. To experimentally test the modified method, a field observation was conducted continuously in a forest over a 31-day period.Since changes in the soil water content near the soil surface were small throughout the observation, a constant effective diffusivity for CO₂ was assumed for the soil CO₂ flux estimation. The soil CO₂ flux was then calculated as the product of the effective diffusivity and the gradient of the soil CO₂ concentration, each calculated from soil radon and CO₂ concentrations. The estimated flux ranged from 1.9 to 5.8 μmol m^?2 s^?1, and, correlating well with the reference value, measured with a conventional ventilated-chamber method. We therefore conclude that the modified gradient method based on the measurement of soil CO₂ and radon concentration at one depth is reliable, at least under conditions where the change in the soil water content is small.     

Application of gas diffusion biocathode in microbial electrosynthesis from carbon dioxide

Microbial catalysis of carbon dioxide (CO₂) reduction to multi-carbon compounds at the cathode is a highly attractive application of microbial electrosynthesis (MES). The microbes reduce CO₂ by either taking the electrons or reducing the equivalents produced at the cathode. While using gaseous CO₂ as the carbon source, the biological reduction process depends on the dissolution and mass transfer of CO₂ in the electrolyte. In order to deal with this issue, a gas diffusion electrode (GDE) was investigated by feeding CO₂ through the GDE into the MES reactor for its reduction at the biocathode. A combination of the catalyst layer (porous activated carbon and Teflon binder) and the hydrophobic gas diffusion layer (GDL) creates a three-phase interface at the electrode. So, CO₂ and reducing equivalents will be available to the biocatalyst on the cathode surface. An enriched inoculum consisting of acetogenic bacteria, prepared from an anaerobic sludge, was used as a biocatalyst. The cathode potential was maintained at ?1.1 V vs Ag/AgCl to facilitate direct and/or hydrogen-mediated CO₂ reduction. Bioelectrochemical CO₂ reduction mainly produced acetate but also extended the products to ethanol and butyrate. Average acetate production rates of 32 and 61 mg/L/day, respectively, with 20 and 80 % CO₂ gas mixture feed were achieved with 10 cm² of GDE. The maximum acetate production rate remained 238 mg/L/day for 20 % CO₂ gas mixture. In conclusion, a gas diffusion biocathode supported bioelectrochemical CO₂ reduction with enhanced mass transfer rate at continuous supply of gaseous CO₂.

Open image in new window

Graphical abstract ?

     

Plot-scale spatiotemporal variations of CO2 concentration and flux across water–air interfaces at aquaculture shrimp ponds in a subtropical estuary

Human activities have increased anthropogenic CO₂ emissions, which are believed to play important roles in global warming. The spatiotemporal variations of CO₂ concentration and flux at fine spatial scales in aquaculture ponds remain unclear, particularly in China, the country with the largest aquaculture. In this study, the plot-scale spatiotemporal variations of water CO₂ concentration and flux, both within and among ponds, were researched in shrimp ponds in Shanyutan Wetland, Min River Estuary, Southeast China. The average water CO₂ concentration and flux across the water–air interface in the shrimp ponds over the shrimp farming period varied from 22.79?±?0.54 to 186.66?±?8.71 μmol L^?1 and from ??0.50?±?0.04 to 2.87?±?0.78 mol m^?2 day^?1, respectively. There was no remarkable difference in CO₂ concentration and flux within the ponds, but significantly spatiotemporal differences in CO₂ flux were observed between shrimp ponds. Chlorophyll a, pH, salinity, air temperature, and morphometry were the important factors driving the spatiotemporal patterns of CO₂ flux in the shrimp ponds. Our findings highlighted the importance and spatiotemporal variations of CO₂ flux in the important coastal ecosystems.

     

污泥活性炭固定床吸附甲苯

采用ZnCl2化学活化法制备的污泥活性炭用于固定床吸附甲苯实验,研究了吸附剂床层厚度、甲苯初始浓度、气体线速等操作条件对其吸附性能的影响,并建立了污泥活性炭吸附甲苯的传质模型,计算不同操作条件下的传质区长度和物质总传质系数。结果表明,当床层厚度从3 cm增加到7 cm,传质区长度基本不变,物质总传质系数增加了66.66%;当甲苯初始浓度增大3.36倍,传质区长度增加了17.19%,而物质总传质系数降低了22.05%;在实验流速范围内,气体线速变为原来的2倍,物质总传质系数增加了65.27%,说明污泥活性炭对甲苯吸附属于外扩散控制。     

Ultrasound enhanced activation of peroxydisulfate by activated carbon fiber for decolorization of azo dye

Activated carbon fiber (ACF) has become an emerging activator for peroxydisulfate (PDS) to generate sulfate radical (SO₄^??). However, the relative low activation efficiency and poor contaminant mineralization limited its widespread application. Herein, ultrasound (US) was introduced to the ACF activated PDS system, and the synergistic effect of US and ACF in PDS activation and the enhancement of contaminant mineralization were investigated. The synergistic effect of US and ACF was observed in the PDS activation to decolorize orange G (OG). The decolorization efficiency increased with increasing ACF loading and US power, and PDS/OG ratio from 1 to 40. The activation energy was determined to be 24.065 kJ/mol. The radical-induced decolorization of OG took place on the surface of ACF, and both SO₄^?? and hydroxyl radical (^?OH) contributed to OG decolorization. The azo bond and naphthalene ring on OG were destructed to other aromatic intermediates and finally mineralized to CO₂ and H₂O. The introduction of US in the ACF/PDS system significantly enhanced the mineralization of OG. The combination of US and PDS was highly efficient to activate PDS to decolorize azo dyes. Moreover, the introduction of US remarkably improved the contaminant mineralization.