MDEA-TETA混合液捕集电厂烟气中CO2的实验研究

分别以MDEA溶液和MDEA-TETA混合液为吸收剂对电厂烟气中的CO_2进行捕集.在相同的实验条件下,研究了吸收时间、吸收液浓度配比和反应温度对CO_2吸收率的影响,并对两种吸收剂的吸收效果进行对比分析.结果表明:吸收效率随着温度的升高而下降,温度低于45℃时,混胺吸收剂MDEA-TETA的吸收效率受温度的影响显著,温度高于45℃时,单一吸收剂MDEA的活化性能大幅度增强.MDEA-TETA混合液中两种胺的配比为6∶1,反应温度在25~65℃内,反应时间在5~20 min内时CO_2的吸收效果较佳,吸收率达90%以上,不同配比的混胺吸收剂的吸收效果均优于MDEA的吸收效果.     

膜法氨水吸收脱除烟气中CO2的研究

以氨水为吸收剂,对聚丙烯中空纤维膜分离烟气中CO2进行了实验研究.结果表明:随着气体流量和入口CO2浓度的增加,CO2去除率下降而传质速率增加;随着氨水浓度和氨水流量的增加,CO2去除率和传质速率均显著增加,但当氨水浓度大于2.5 mol·L-1,吸收液流量大于80m L·min-1后,膜接触器对CO2去除率和传质速率基本保持不变;膜接触器连续运行15 d后其吸收性能显著下降,CO2去除率、传质速率、总传质系数均下降约40%~50%.接触角测量、SEM及XPS表征结果表明:随着操作的进行,聚丙烯膜在吸收液环境中接触角逐渐降低,疏水性减弱,造成膜孔润湿;同时碳酸盐在膜孔形成结晶,堵塞膜孔,使得传质阻力进一步增加,从而造成膜接触器吸收性能的下降.     

基于碳捕集的富氧燃煤烟气联合脱硫脱硝试验研究

富氧燃煤烟气压缩液化CO2的高压低温工况为NO氧化为易溶于水的NO2提供了十分有利的条件.基于小型高压吸收试验装置,采用配制的富氧燃煤模拟烟气,在高压常温下进行了NO、SO2、O2与H2O的吸收反应试验.根据反应前后的气液产物分析,测定了不同组分比例与不同压力下混合气体中NO与SO2的转化率.NO氧化与吸收试验表明,NO转化为HNO3的比率随压力升高而增加,在0.5 ～2 MPa之间增加很快,在2 ～3 MPa之间增速趋丁平缓,压力达3 MPa以上时,90％以上的NO均转化为稀硝酸,且初始NO浓度越高,NO的转化率越大.混合气体中同时存在5O2与NO的联合吸收试验发现,只有少量的NO转化成了NO3-,SO2向H2SO4的转化率随压力升高而增加,初始SO2浓度越大,转化率越高.分析表明,SO2与NO同时存在时SO2先行转化为SO3,NO充当了催化剂,但SO2转化为SO3的一次转化率小于35％,反应酸液产物的多次循环能使SO2的转化率达到90％以上.建议的工艺流程中需采用两座吸收反应塔顺序脱除SO2与NO并回收稀酸溶液,有望在富氧燃煤发电捕集CO2系统中降低脱硫脱硝成本,部分地弥补富氧燃烧机组发电成本的增加.     

Influence of SO2 in incineration flue gas on the sequestration of CO2 by municipal solid waste incinerator fly ash

The influence of CO2 content and presence of SO2 on the sequestration of CO2 by municipal solid waste incinerator(MSWI) fly ash was studied by investigating the carbonation reaction of MSWI fly ash with different combinations of simulated flue gas.The reaction between fly ash and 100% CO2 was relatively fast;the uptake of CO2 reached 87g CO2/kg ash,and the sequestered CO2 could be entirely released at high temperatures.When CO2 content was reduced to 12%,the reaction rate decreased;the uptake fell to 41g CO2/kg ash,and 70.7% of the sequestered CO2 could be released.With 12% CO2 in the presence of SO2,the reaction rate significantly decreased;the uptake was just 17g CO2/kg ash,and only 52.9% of the sequestered CO2 could be released.SO2 in the simulated gas restricted the ability of fly ash to sequester CO2 because it blocked the pores of the ash.     

粉煤灰用于碳捕集、利用及封存的研究进展

总结了国内外粉煤灰用于CO₂捕集、利用和封存的不同技术研究进展,同时对今后的研究和机遇进行了展望.粉煤灰自身可通过直接干式、半干式、湿式和间接方法对CO₂进行矿化捕集封存,在CO₂矿化的同时降低粉煤灰自身重金属的浸出,并且矿化后的粉煤灰因有效降低游离CaO和MgO的含量而更适合于制作混凝土添加剂.粉煤灰也可制成活性炭、沸石和多孔二氧化硅等产品,并对CO₂进行物理吸附捕集,制成产品的类型主要取决于粉煤灰自身的成分组成和理化性质.在CO₂利用方面,粉煤灰除了可拓展建材的利用途径外,还可制作CO₂多种化学工艺所需催化剂或催化剂载体,以及制作新型材料拟薄水铝石等.我国“双碳”目标的提出及燃煤电厂粉煤灰自身的理化特性为粉煤灰提供了一条新的综合利用途径.     

粉煤灰对烟气中CO2的吸收特性及矿物相演变机理研究

粉煤灰矿化CO₂是一种极具前景的减少燃煤电厂CO₂排放的技术.然而,目前还缺乏从矿物学角度对碳酸化反应机理的详细认识.本研究选取了3种粉煤灰开展碳酸化实验和矿物学研究,考察碳酸化过程中温度对碳酸化能力及粉煤灰矿物学变化的影响.结果表明,在任一温度下,BJ粉煤灰的碳酸化率均高于YA和LY粉煤灰,这是由于BJ粉煤灰中硬石膏、钙铁石和无定形相等活性矿物相含量较高,LY粉煤灰缺少高活性的钙、镁结晶相.对YA粉煤灰而言,升高温度可显著提高透辉石、尖晶石、黑钙铁矿和方镁石的转化率.在碳酸化YA粉煤灰中同时检测出碳酸钙和碳酸镁/铁,说明除含钙相其他活性元素(Mg和Fe)也参与了碳酸化过程.因此,需要对每个粉煤灰原始材料的矿物学和操作温度进行具体的个案优化,以最大限度地提高固定CO₂能力和碳酸化率.结果还表明温度对不同晶型碳酸钙的形成具有重要作用.方解石在低温(40和80℃)下形成,而文石在高温(180和220℃)下形成.     

Toward rational design of amines for CO2 capture: Substituent effect on kinetic process for the reaction of monoethanolamine with CO2

Amines have been considered as promising candidates for post-combustion CO₂ capture. A mechanistic understanding for the chemical processes involved in the capture and release of CO₂ is important for the rational design of amines. In this study, the structural effects of amines on the kinetic competition among three typical products (carbamates, carbamic acids and bicarbonate) from amines + CO₂ were investigated, in contrast to previous thermodynamic studies to tune the reaction of amines with CO₂ based on desirable reaction enthalpy and reaction stoichiometry. We used a quantum chemical method to calculate the activation energies (E_a) for the reactions of a range of substituted monoethanolamines with CO₂ covering three pathways to the three products. The results indicate that the formation of carbamates is the most favorable, among the three considered products. In addition, we found that the E_a values for all pathways linearly correlate with pK_a of amines, and more importantly, the kinetic competition between carbamate and bicarbonate absorption pathways varies with pK_a of the amines, i.e. stronger basicity results in less difference in E_a. These results highlight the importance of the consideration of kinetic competition among different reaction pathways in amine design.     

以粉煤灰为原料制备低温CO2吸附剂的工艺参数优化

利用高铝粉煤灰预脱硅液作为载体原料,通过使用胺基化合物对载体改性制备低温CO_2吸附剂.应用6 sigma中的工具,对制备工艺进行优化,得到理想的吸附剂,并对吸附剂样品进行表征.结果表明制备的CO_2吸附剂表现出良好的CO_2吸附性能.此类CO_2吸附剂具有吸附容量高(160 mg·g~(-1))、吸附速率快、对设备腐蚀低、成本低廉等特点,是一种极具工业应用潜力的CO_2吸附剂.     

Probing the potential of polyester for CO2 capture

Global warming, the major environmental issue confronted by humanity today, is caused by rising level of green house gases. Carbon capture and storage technologies offer potential for tapering CO2 emission in the atmosphere. Adsorption is believed to be a promising technology for CO2 capture. For this purpose, a polyester was synthesized by polycondensation of1,3,5-benzenetricarbonyl trichloride and cyanuric acid in pyridine and dichloromethane mixture. The polymer was then characterized using FT-IR, TGA, BET surface area and pore size analysis, FESEM and CO2 adsorption measurements. The CO2 adsorption capacities of the polyester were evaluated at a pressure of 1 bar and two different temperatures（273 and 298 K）.The performance of these materials to adsorb CO2 at atmospheric pressure was measured by optimum CO2 uptake of 0.244 mmol/g at 273 K. The synthesized polyester, therefore, has the potential to be exploited as CO2 adsorbent in pre-combustion capture process.     

碳酸钾-二乙烯三胺复合溶液吸收烟气中CO2实验研究

热钾碱溶液在工业脱除二氧化碳中已获得较广泛的应用,但存在吸收速率差、再生负荷高等缺点-开发新型热钾碱溶液成为目前研究热点.采用搅拌实验装置,研究碳酸钾溶液及不同配比的碳酸钾-二乙烯三胺(DETA)复合溶液对烟道气中二氧化碳的吸收和解吸性能,揭示了吸收速率、吸收容量和酸碱度与时间之间的内在联系;对CO2初始逸出温度,试液...     

小浪底水库影响下的黄河花园口站和小浪底站pCO2特征及扩散通量

于2011年11月至2012年10月在黄河小浪底站和花园口站进行连续采样分析,根据亨利定律计算出表层水体二氧化碳分压(p CO2),研究了在小浪底水库"水沙调控"的影响下黄河花园口站和小浪底站表层水体p CO2特征及水-气CO2通量.结果表明,在小浪底水库正常调度期间,小浪底站表层水体p CO2在82~195 Pa之间,花园口站表层水体p CO2在99~228 Pa之间,且花园口站表层水体p CO2均高于同期的小浪底站;在小浪底水库调水调沙期间,两个水文站均表现为水库泄水期间的表层水体p CO2明显低于水库排沙期间的表层水体p CO2.无论是在小浪底水库正常调度期间还是在调水调沙期间,两个水文站表层水体p CO2均与DIC含量呈现显著的正相关关系.8、9月Ep CO2/AOU的比值高于生物好氧呼吸作用控制水体p CO2的理论下限0.62,因此8、9月生物好氧呼吸作用对水体p CO2的贡献比较明显.从全年来看小浪底站和花园口站平均水-气CO2扩散通量分别为0.486μmol·(m2·s)-1和0.588μmol·(m2·s)-1;在水库正常调度期间花园口站水-气CO2扩散通量明显高于同期的小浪底站;在小浪底水库调水调沙期间两个水文站均表现为水库泄水期间的水-气CO2扩散通量明显低于水库排沙期间的水-气CO2扩散通量.     

固定化碳酸酐酶在立式反应器催化吸收模拟烟气中CO2的实验研究

利用海藻酸钠包埋和戊二醛交联法固定碳酸酐酶,并在立式反应器进行了固定化酶吸收CO2的特性实验.实验结果表明:固定化酶的酶活力回收率是56.3%;固定化酶显著加快模拟烟气中CO2的吸收;载酶量小时,气体流量是影响吸收CO2效果的主要因素,气体流量增大,载酶量成为主要因素;气体流量增大,载酶量对反应终止p H的影响减小;载酶量增大,气体流量对反应终止p H的影响减小;气体流量增大,CO2吸收效率下降,载酶量提高,CO2吸收效率上升;气体流量为650 m L·min-1和载酶量为1 mg时,固定化酶催化吸收CO2效果显著;固定化酶具有较高的操作稳定性;SEM显示反应后的固定化酶表面出现大量形状不规则的小孔,空隙结构变得发达.     

新安江水库二氧化碳排放的时空变化特征

新安江水库是我国华东地区最大的水库,面积580 km2,平均深度30 m,水库水体处于中贫营养状态.为了研究新安江水库中CO_2排放的时空变化特征,2014年12月至2015年12月采用静态浮箱法收集水库表面以分子扩散方式排放的CO_2,使用气相色谱仪分析CO_2浓度.结果表明,新安江水库CO_2排放通量从上游入库河流[(120.39±135.41)mg·(m~2·h)~(-1)]至库区主体[(36.65~61.94)mg·(m~2·h)~(-1)]呈下降趋势,而大坝下游河流中CO_2排放通量[(1 535.00±1 447.46)mg·(m~2·h)~(-1)]显著增加,约分别是上游入库河流和库区主体的13倍和25~42倍.但随着与大坝距离增加,大坝下游河流中CO_2排放通量显著下降,如7 km处的CO_2排放通量仅为出库水体处的20%.在库区主体中,CO_2排放通量具有明显的季节变化:CO_2排放通量在秋、冬季时为正值,最大值出现在冬季(12月或1月),说明此时库区表层水体是CO_2排放源;而CO_2排放通量在春、夏季为负值,最小值出现在春季(3、4或5月),说明此时库区表层水体是CO_2吸收汇,这可能与春、夏季时水体中藻类繁殖有关.所以,在调查水库表面CO_2排放时,应对水库的上游入库河流、库区主体和坝下河流进行全面长期的观测,才能避免低估水库中CO_2排放总量.     

Optimization of CO2 adsorption capacity and cyclical adsorption/desorption on tetraethylenepentamine-supported surface-modified hydrotalcite

The objective of this research was to investigate CO_2adsorption capacity of tetraethylenepentamine-functionalized basic-modified calcined hydrotalcite(TEPA/b-c HT)sorbents at atmospheric pressure formed under varying TEPA loading levels,temperatures,sorbent weight to total gaseous flow rate(W/F)ratios and CO_2concentrations in the influent gas.The TEPA/b-c HT sorbents were characterized by means of X-ray diffraction(XRD),Fourier transform infrared spectrometry(FT–IR),thermal gravimetric analysis(TGA),Brunauer–Emmet–Teller(BET)analysis of nitrogen(N_2)adsorption/desorption and carbon–hydrogen–nitrogen(CHN)elemental analysis.Moreover,a full 2~4factorial design with three central points at a 95%confidence interval was used to screen important factor(s)on the CO_2adsorption capacity.It revealed that85.0%variation in the capacity came from the influence of four main factors and the15.0%one was from their interactions.A face-centered central composite design response surface method(FCCCD–RSM)was then employed to optimize the condition,the maximal capacity of 5.5–6.1 mmol/g was achieved when operating with a TEPA loading level of 39%–49%(W/W),temperature of 76–90°C,W/F ratio of 1.7–2.60(g·sec)/cm~3and CO_2concentration of 27%–41%(V/V).The model fitted sufficiently the experimental data with an error range of±1.5%.From cyclical adsorption/desorption and selectivity at the optimal condition,the 40%TEPA/b-c HT still expressed its effective performance after eight cycles.     

Development of a hybrid photo-bioreactor and nanoparticle adsorbent system for the removal of CO2 , and selected organic and metal co-pollutants

Fossil fuel combustion and many industrial processes generate gaseous emissions that contain a number of toxic organic pollutants and carbon dioxide (CO₂) which contribute to climate change and atmospheric pollution. There is a need for green and sustainable solutions to remove air pollutants, as opposed to conventional techniques which can be expensive, consume additional energy and generate further waste. We developed a novel integrated bioreactor combined with recyclable iron oxide nano/micro-particle adsorption interfaces, to remove CO_2, and undesired organic air pollutants using natural particles, while generating oxygen. This semi-continuous bench-scale photo-bioreactor was shown to successfully clean up simulated emission streams of up to 45% CO₂ with a conversion rate of approximately 4% CO₂ per hour, generating a steady supply of oxygen (6 mmol/hr), while nanoparticles effectively remove several undesired organic by-products. We also showed algal waste of the bioreactor can be used for mercury remediation. We estimated the potential CO₂ emissions that could be captured from our new method for three industrial cases in which, coal, oil and natural gas were used. With a 30% carbon capture system, the reduction of CO₂ was estimated to decrease by about 420,000, 320,000 and 240,000 metric tonnes, respectively for a typical 500 MW power plant. The cost analysis we conducted showed potential to scale-up, and the entire system is recyclable and sustainable. We further discuss the implications of usage of this complete system, or as individual units, that could provide a hybrid option to existing industrial setups.     

杭州地区大气CO2体积分数变化特征及影响因素

选取2015年8月至2016年9月杭州城区、远郊地区在线观测CO_2体积分数,分析杭州地区CO_2体积分数的城郊差异,并结合风向、CO_2体积分数周末效应、二十国集团(G20)峰会期间CO_2体积分数变化过程分析,探讨杭州城市对CO_2体积分数的影响程度.结果表明,杭州城区、远郊地区CO_2体积分数的日变化分布以单峰型形态为主,植物光合作用/呼吸作用和大气输送条件的日变化是主要的影响因素;城郊CO_2体积分数差值表现为双峰形态,人为排放对城郊CO_2体积分数差值的日变化分布存在重要影响.CO_2体积分数日变化幅度在春夏季节远郊地区大于城区,秋季则反之.杭州城区、远郊地区CO_2体积分数的季节变化趋势基本一致,均表现为冬、春季高,夏季低;城郊CO_2体积分数差值冬季最高,夏季最低.杭州地区CO_2体积分数高值的输送方向与周边城市区域的分布方向一致.杭州城区、远郊地区CO_2体积分数均呈现周末效应,尤其在城区,机动车排放对工作日-周末CO_2体积分数的日变化分布存在影响.杭州城区CO_2平均体积分数比远郊地区高9.3×10-6,G20峰会期间人为源排放的减少有效地降低了大气CO_2体积分数,尤其对市区的削减效果更为明显.     

大气14CO2的时空分异特征及其在化石源CO2示踪中的应用

大气CO₂中放射性碳同位素(¹⁴C)的水平可以反映化石源CO₂的影响程度,这对于评估我国目前化石源CO₂的排放状况和制定节能减排政策具有重要的指导意义。本文在概述大气¹⁴CO₂采样和分析方法的基础上,简要介绍了大气¹⁴CO₂观测的起源和主要的源汇过程,重点论述了大气¹⁴CO₂的时空分异特征及其驱动因素;阐述了化石源CO₂浓度的估算方法及¹⁴CO₂在国内外化石源CO₂示踪中的应用现状,并对大气¹⁴CO₂观测在我国化石源CO₂示踪中的应用前景进行了展望;旨在为我国正确地开展大气¹⁴CO₂的观测研究,深刻地理解特定区域大气¹⁴CO₂的时空分异特征和化石源CO₂的分布状况提供参考。     

杭州西溪湿地CH4、CO2通量及其主要影响因子

本研究采用便携式温室气体分析仪连接通量箱在线监测杭州西溪湿地CH_4、CO_2通量日变化及季节变化,同时也对包括有机碳含量、湿度、孔隙度、比重、p H、Eh在内的潜在影响因子进行了研究。结果表明,通常情况下,CH_4、CO_2通量的变化分别为-0.001 9~0.035 3mg/(m~2·h)和-109.76~442.55mg/(m~2·h);CH_4、CO_2通量的变化存在明显正相关关系。CH_4通量的季节变化表现为夏季秋季春季冬季;CO_2通量的季节变化表现为夏季春季冬季秋季。土壤湿度是影响CH_4通量变化的重要因子,通常湿度越大,CH_4通量越大;在生长季维管植物有助于CH_4的氧化;西溪湿地土质差异也使CH_4、CO_2通量排放有所差异,具体表现在土壤有机碳含量相差较大,而土壤中有机碳的含量与CH_4产生潜力呈显著正相关。     

广东省CO2排放变化的社会经济影响因素

作为我国经济最为发达的省份之一,广东省社会经济可持续发展面临CO₂排放量增长的挑战.从多角度分析广东省CO₂排放变化的社会经济影响因素,有助于其实现低碳发展.基于投入产出模型,从生产、需求和供应角度分析1987—2015年广东省CO₂排放量的变化;此外,采用结构分解分析方法,从需求和供应角度量化广东省各种社会经济因素对CO₂排放变化的相对贡献.结果表明:①与生产端相比,需求侧和供给侧的研究有助于识别不同的关键行业,如建筑业（需求侧）、金融和保险业（供给侧）.②降低碳排放强度是减少广东省CO₂排放的主要因素,而人均最终需求水平和人均初始投入增加是推动广东省CO₂排放增加的主要因素.③生产结构、最终需求结构和初始投入结构变化导致CO₂排放量略有增加,表明广东省具有较大的通过调整结构性因素减排CO₂的潜力.综上,建议除了生产端CO₂减排措施外,广东省还应采取需求侧和供给侧相关措施,如优化消费行为、产品分配行为和初始投入结构等.      

包气带水气二相流CO2运移规律

利用土柱实验装置模拟CO₂在土壤中的迁移转化规律,重点研究湿润峰处水、气二相间污染物转化实验土柱长1m,过饱和CO2溶液浓度为748mg/L.分析表明水相运移受对流、弥散、反应及水-气质量传输机制控制,气相运移受对流、扩散和水-气质量传输机制控制.对土柱中水气二相动态条件下的取样方法进行了探索,确定了CO₂在渗透湿润峰水-气二相间分配系数为0.00061,表明水相向气相有一定传输,但不显著.可进一步为低中水平放射性废物地质处置安全评价及固体废物填埋处置环境影响评价提供定量科学依据.