Please wait a minute...

过刊目录

    2017, Vol. 26, No. 5 Online: 2017-09-15

    Special Topic: Graphene and 2D Materials for Energy Storage

    This special topic entitled graphene and 2D materials for energy storage,organized by guest editors Prof.Zhong-Shuai Wu and editor-inchief Prof.Xinhe Bao,highlight the recent advances of fundamental and applied research of cutting-edge graphene and 2D materials for advanced energy storage systems,covering the aspects of (i) preparation and characterization of graphene and 2D materials,including MXene,MoS2,phosphorene,boron nitride,metal oxides,and polymer nanosheets,(ii) assembly of 1D graphene fibers,2D nanoarchitectures, and 3D porous networks,(iii) supercapacitors,micro-supercapacitors, asymmetric supercapacitors&lithium ion capacitors,(iv) Li/Na/K ion batteries,Li-S batteries and other batteries,(v) new materials,concepts&device geometries,with a special focus on graphene and 2D materials for flexible and new-concept energy storage devices.

    全选选: 隐藏/显示图片
    Preface
    Preface to Special Issue: CO 2 capture storage and utilization
    Yanqiang Huang, Qiang Wang, Jinlong Gong
    2017, 26(5): 0-0. 
    摘要 ( 1454 )  
    Reducing the anthropogenic CO2 emissions from fossil resource combustion and human activities has become one of the major challenges we are facing today. Beyond those practical applications for the utilization of CO2, such as the synthesis of salicylic acid, methanol, urea, NaHCO3-Na2CO3 chemicals and recently developed polycarbonate synthesis, scientists are still seeking new materials and technologies for efficient capture, storage and conversion of CO2 with consideration into reducing CO2 emission at a large amount. Until now, CO2 capture and utilization is not only an academic event but a social and government guiding project all over the world. The special issue in Journal of Energy Chemistry is an update of recent research works on the topic of carbon capture storage and utilization (CCUS) which covers the material and technology innovations for CO2 capture and utilization. Five reviews, two communications and seventeen research articles are included in this special issue.   As a first step for limiting the CO2 emission, efficient capture of CO2 with a cost-effective strategy, is likely to rely on new adsorbents and the development of technologies that can reduce energy consumption, especially for the separation of low concentrated CO2 from coal-fired power plant flue gas and selective capture of CO2 from humid gases. CO2 molecules are often preferred to be adsorbed in porous materials with high surface area and abundant sorption sites. The concept of molecular basket sorbent (MBS) for CO2 capture has been proposed by Song et al. in this special issue. They use polyethylenimine (PEI) or polyethylene glycol (PEG) to reside in the mesopore structure of SBA-15, TUD-1 and fumed silica HS-5 materials to provide plenty of amine sites for CO2 adsorption. Zhong et al. synthesize a type of 2D covalent triazine-based framework material (namely, CTF-DCBT) for efficient capture of CO2. CTF-DCBT contains ultramicropore (6.5 Å) and high heteroatom contents (11.24 wt% of N and 12.61 wt% of S), which is responsible for the highly selective CO2/N2 and CO2/CH4 preferential adsorption. Porous carbon materials with well-developed heteroatom doped sites are widely examined as CO2 adsorbents. In the work of Ahn et al., nitrogen-doped carbon materials are synthesized by the carbonization of a low-cost porous covalent triazine polymer, PCTP-3. The textural properties of the porous carbon materials are additionally activated by KOH, to form a narrow micropore size distribution. A type of porous carbon sphere with highly developed ultra-microporosity and uniform pore size is prepared by Zhou and Zhuo et al. These well-designed porous carbon materials on purpose are examined as excellent adsorbents with high CO2 capture capacity and selectivity. Pfeiffer and co-workers systematically investigate the CO2 chemisorption process on a series of alkaline pentalithium aluminate (β-Li5AlO4) based solid solution. With an addition of alkaline carbonate compound or iron exchange with the aluminum position into β-Li5AlO4, the CO2 chemisorption enhances. CO2 molecules are more likely to reside on the superficial position of those (modified) alkaline solid solution adsorbents. CO2 capture by ionic liquids (ILs) has also attracted wide attention. In the contributions of Yu et al. and Sun et al., a series of ILs monomers and ILs polymers (PILS) and a type of layered hybrids material containing ILs are prepared, respectively. Both the PILs and BMIMCl/LP layered hybrids are identified as efficient adsorbents with high CO2 capture capacity. Zhang et al. select a series of [CnMIm][Tf2N] ILs as physical CO2 adsorbents and the adsorption condition is operated under a wide temperature and pressure range, which is appealing at higher temperature. Kanoh et al. examine the capacity and kinetics of CO2 capture over K2CO3 adsorbent. In this work, a detailed study on the influence of temperature with changed moisture conditions and further insight into the NaHCO3 formation mechanism has been carried out. Shi et al. employ a combination of WGS reaction and elevated-temperature pressure swing adsorption technology to deeply remove trace CO2 and CO impurities to harvest high purity H2 gas. The technology is based on potassium promoted hydrotalcite adsorbents, which can reduce the residual CO2 concentration to 3.5 ppm after 12 h of temperature swing operation at 450 °C. In the search of highly efficient CO2 adsorbents under different real working conditions, Wang et al. and Ahn et al. critically review the development of molten salts modified MgO-based adsorbents and Amine-functionalized silica composite materials, respectively. Molten salts-modified MgO-based adsorbents show their advantages in the high adsorption capacity (the highest CO2 capture capacity of 12.9 mmol g-1 as reported), low cost, wide availability and suitable for the CO2 capture at intermediate temperature range (200400 °C). Amine-functionalized silica composite materials are promising candidates for post-combustion CO2 capture from low CO2 concentrated flue gases. They show the advantages of excellent CO2 uptake, selectivity, less sensitive to moisture and facile for the regeneration. Besides CO2 capture, considerations about the recycling and utilization of CO2 when using CO2 as the abundant carbon resource are in progress to accomplish the challenging task of carbon neutral process. Direct catalytic conversion of CO2 to value added chemicals or fuels has aroused great attention in both academic and commercial fields. Hydrogenation of CO2 to formic acid and CO and other carbonaceous products in the lower carbon chemical valence state has been widely studied. Jin et al. investigate the auto-catalytic role of Zn/ZnO interface, which is formed in-situ during the reaction, in the transformation of CO2 to formic acid in the water medium. They also provide an overview of the current advances in research of highly efficient reduction of CO2 or NaHCO3 into formic acid/formate by in-situ hydrogen from water dissociation with a metal/metal oxide redox cycle under mild hydrothermal condition. In the review made by Huang et al., the catalytic performance of CO2-to-CO conversion and recent updates in designing of heterogeneous catalysts with high CO product selectivity and high temperature robustness are specifically elaborated. In the contribution of Chen et al., Ca(OH)2 and 10% Ni/ZrO2 are introduced in the biomass conversion processes of cellulose. Ca(OH)2 greatly enhances the H2 production rate with a yield of 36.4%, while the in-situ reforming of light gases and carbon capture processes significantly suppress the CO2 formation. Ma et al. delicately design a dual active center containing Salen-Cu(II)@MIL-101(Cr) via the “ship in a bottle” approach, which is developed as the active catalyst for the synthesis of propylene carbonate from CO2 and propylene oxide. The sorption enhanced methane reforming process of CO2 has been studied by Pfeiffer et al. and Courson et al., by using CaO-NiO mixed oxide and CaO-Ca12Al14O33, respectively. The studied catalyst systems show excellent chemical stability in obtaining syngas (H2 + CO) with high CH4 conversion and H2 yield. Smart conversion processes such as chemical looping and mineral carbonation of CO2 are capable of utilizing CO2 at large quantities. Haider et al. describe the use of copper(II) oxides in combination with limestone in the form of a mechanical pelletizer as the oxygen carriers in the chemical looping processes. The oxygen carriers exhibit an enhanced crushing strength with high CO yield. Li et al. report the mineral carbonation processes of blast furnace slag with intention to reduce substantial CO2 emission at large quantities. As a recyclable extractant, (NH4)2SO4, is used to extract calcium and magnesium from blast furnace slag by using low-temperature roasting to fix CO2 through aqueous carbonation. Alternatively, electrochemical reduction of CO2 provides another promising way in reducing CO2 emission, which can be delivered in the form of renewable energy. Co-electrolysis of CO2 and H2O using high-temperature solid oxide electrolysis cells (SOECs) into valuable chemicals is the topic of contribution made by Wang and Bao et al. The review discusses the so far cathode material development, the alternative cathode materials preparation strategies and the possible cathode reaction mechanism for CO2/H2O electrolysis. Different reaction modes of the CO2/H2O co-electrolysis in SOECs are summarized to offer new strategies to enhance the CO2 conversion. Kang et al. report a nitrogen doped tin oxide material with enhanced Faradaic efficiency (90%) for CO2 electro-reduction to formate, which also shows sulfur tolerance. The combined catalyst structure of partially reduced metallic tin and N-doped tin oxide (Sn/N-SnO2) is identified as the key for CO2 to formate electro-reduction. In summary, all these high quality works provided by the outstanding contributions in this highly attentive research area of CCUS will render this special issue to contribute a broad vision for the future research activities. Finally, we would like to express our sincere thanks to the reviewers and the editors for giving your time and expertise to review the papers and facilitate the publication of this issue.  
    COMMUNICATIONS
    Salen-Cu(II)@MIL-101(Cr) as an efficient heterogeneous catalyst for cycloaddition of CO2 to epoxides under mild conditions
    Caijuan Liu, Xiao-Huan Liu, Bo Li, Lei Zhang, Jian-Gong Ma, Peng Cheng
    2017, 26(5): 821-824.  DOI: 10.1016/j.jechem.2017.07.022
    摘要 ( 1823 )  
    A double active center system, namely Salen-Cu(Ⅱ)@MIL-101(Cr), was successfully synthesized via the "ship in a bottle" approach, which acted as a bifunctional material for both capture and conversion of CO2 in a single process. For the first time, Salen-Cu(Ⅱ)@MIL-101(Cr) catalyst was developed for the synthesis of propylene carbonate from CO2 and propylene oxide under room temperature and ambient pressure with a yield of 87.8% over 60 h. Furthermore, the reaction mechanism was also discussed.
    Preface
    Nitrogen doped tin oxide nanostructured catalysts for selective electrochemical reduction of carbon dioxide to formate
    Qiankun Li, Zhuo Wang, Miao Zhang, Pengfei Hou, Peng Kang
    2017, 26(5): 825-829.  DOI: 10.1016/j.jechem.2017.08.010
    摘要 ( 2156 )  
    Tin/tin oxide materials are key electrocatalysts for selective conversion of CO2 to formate/formic acid. Herein we report a tin oxide material with nitrogen doping by using ammonia treatment at elevated temperature. The N doped material demonstrated enhanced electrocatalytic CO2 reduction activity, showing high Faradaic efficiency (90%) for formate at -0.65 V vs. RHE with partial current density of 4 mA/cm2. The catalysis was contributed to increased electron negativity of N atom compared to O atom. Additionally, the N-doped catalyst demonstrates sulfur tolerance with retained formate selectivity. The analysis after electrolysis shows that the catalyst structure partially converts to metallic Sn, and thus the combined Sn/N-SnO2 is the key for the active CO2 catalysis.
    REVIEW
    Molten salts-modified MgO-based adsorbents for intermediate-temperature CO2 capture:A review
    Wanlin Gao, Tuantuan Zhou, Yanshan Gao, Benoît Louis, Dermot O'Hare, Qiang Wang
    2017, 26(5): 830-838.  DOI: 10.1016/j.jechem.2017.06.005
    摘要 ( 2354 )  
    Carbon dioxide (CO2) capture using magnesium oxide (MgO)-based adsorbents at intermediate temperatures has been regarded as a very prospective technology for their relatively high adsorption capacity, low cost, and wide availability. During the past few years, great effort has been devoted to the fabrication of molten salts-modified MgO-based adsorbents. The extraordinary progress achieved by coating with molten salts greatly promotes the CO2 capture capacity of MgO-based adsorbents. Therefore, we feel it necessary to deliver a timely review on this type of CO2 capturing materials, which will benefit the researchers working in both academic and industrial areas. In this work, we classified the molten saltsmodified MgO adsorbents into four categories:(1) homogenous molten salt-modified MgO adsorbents, (2) molten salt-modified double salts-based MgO adsorbents, (3) mixed molten salts-modified MgO adsorbents, and (4) molten salts-modified MgO-based mixed oxides adsorbents. This contribution critically reviews the recent developments in the synthetic method, adsorption capacity, reaction kinetics, promotion mechanism, operational conditions and regenerability of the molten salts-modified MgO CO2 adsorbents. The challenges and prospects in this promising field of molten salts-modified MgO CO2 adsorbents in real applications are also briefly mentioned.
    Co-electrolysis of CO2 and H2O in high-temperature solid oxide electrolysis cells:Recent advance in cathodes
    Xiaomin Zhang, Yuefeng Song, Guoxiong Wang, Xinhe Bao
    2017, 26(5): 839-853.  DOI: 10.1016/j.jechem.2017.07.003
    摘要 ( 2751 )  
    Co-electrolysis of CO2 and H2O using high-temperature solid oxide electrolysis cells (SOECs) into valuable chemicals has attracted great attentions recently due to the high conversion and energy efficiency, which provides opportunities of reducing CO2 emission, mitigating global warming and storing intermittent renewable energies. A single SOEC typically consists of an ion conducting electrolyte, an anode and a cathode where the co-electrolysis reaction takes place. The high operating temperature and difficult activated carbon-oxygen double-bond of CO2 put forward strict requirements for SOEC cathode. Great efforts are being devoted to develop suitable cathode materials with high catalytic activity and excellent long-term stability for CO2/H2O electro-reduction. The so far cathode material development is the key point of this review and alternative strategies of high-performance cathode material preparation is proposed. Understanding the mechanism of CO2/H2O electro-reduction is beneficial to highly active cathode design and optimization. Thus the possible reaction mechanism is also discussed. Especially, a method in combination with electrochemical impedance spectroscopy (EIS) measurement, distribution functions of relaxation times (DRT) calculation, complex nonlinear least square (CNLS) fitting and operando ambient pressure X-ray photoelectron spectroscopy (APXPS) characterization is introduced to correctly disclose the reaction mechanism of CO2/H2O co-electrolysis. Finally, different reaction modes of the CO2/H2O coelectrolysis in SOECs are summarized to offer new strategies to enhance the CO2 conversion. Otherwise, developing SOECs operating at 300-600℃ can integrate the electrochemical reduction and the Fischer-Tropsch reaction to convert the CO2/H2O into more valuable chemicals, which will be a new research direction in the future.
    Designing of highly selective and high-temperature endurable RWGS heterogeneous catalysts:recent advances and the future directions
    Xiong Su, Xiaoli Yang, Bo Zhao, Yanqiang Huang
    2017, 26(5): 854-867.  DOI: 10.1016/j.jechem.2017.07.006
    摘要 ( 2528 )  
    Reverse water gas shift (RWGS) reaction can be served as a pivotal stage of transitioning the abundant CO2 resource into chemicals or hydrocarbon fuels, which is attractive for the CO2 utilization and of eventually significance in enabling a rebuilt ecological system for unconventional fuels. This concept is appealing when the process is considered as a solution for the storage of renewable energy, which may also find a variety of potential end uses for the outer space exploration. However, a big challenge to this issue is the rational design of high temperature endurable RWGS catalysts with desirable CO product selectivity. In this work, we present a comprehensive overview of recent publications on this research topic, mainly focusing on the catalytic performance of RWGS reaction over three major kinds of heterogeneous catalysts, including supported metal catalysts, mixed oxide catalysts and transition metal carbides. The reaction thermodynamic analysis, kinetics and mechanisms are also described in detail. The present review attempts to provide a general guideline about the construction of well-performed heterogeneous catalysts for the RWGS reaction, as well as discussing the challenges and further prospects of this process.
    Amine-silica composites for CO2 capture:A short review
    Chao Chen, Siqian Zhang, Kyung Ho Row, Wha-Seung Ahn
    2017, 26(5): 868-880.  DOI: 10.1016/j.jechem.2017.07.001
    摘要 ( 2154 )  
    Amine-silica composite materials for post-combustion CO2 capture have attracted considerable attention because of their high CO2 uptake at low CO2 concentrations, excellent CO2 capture selectivity in the presence of moisture, and lower energy requirements for sorbent regeneration. This review discusses the recent advances in amine-silica composites for CO2 capture, including adsorbent preparation and characterization, CO2 capture under dry and moisture conditions at different CO2 partial pressures, sorbent regeneration, and stability after many cyclic sorption-desorption runs.
    Highly-efficient and autocatalytic reduction of NaHCO3 into formate by in situ hydrogen from water splitting with metal/metal oxide redox cycle
    Guodong Yao, Jia Duo, Binbin Jin, Heng Zhong, Lingyun Lyu, Zhuang Ma, Fangming Jin
    2017, 26(5): 881-890.  DOI: 10.1016/j.jechem.2017.08.011
    摘要 ( 2282 )  
    The Earth's sustainable development is threatened by the increasing atmospheric CO2 level which can be attributed to the imbalance of CO2 due to the rapid consumption of fossil fuels caused by human activities and the slow absorption and conversion of CO2 by nature. One of the efficient methods for reconstructing the balance of CO2 should involve the rapid conversion of CO2 into fuels and chemicals. The hydrogenation of CO2 with gaseous hydrogen is currently considered to be the most commercially feasible synthetic route, however, the supply of safe and economical hydrogen sources poses a significant challenge to up-scaling application. Direct utilization of hydrogen from dissociation of water, the most abundant, cheap and clean hydrogen resource, for the reduction of CO2 would be one of the most promising approaches for CO2 utilization. This paper provides an overview of the current advances in research on highly efficient reduction of CO2 or NaHCO3, a representative compound of CO2, into formic acid/formate by in situ hydrogen from water dissociation with a metal/metal oxide redox cycle under mild hydrothermal conditions.
    ARTICLES
    Copper-based oxygen carriers supported with alumina/lime for the chemical looping conversion of gaseous fuels
    Syed K Haider, María Erans, Felix Donat, Lunbo Duan, Stuart A Scott, Vasilije Manovic, Edward J Anthony
    2017, 26(5): 891-901.  DOI: 10.1016/j.jechem.2017.07.014
    摘要 ( 1611 )  
    Copper (Ⅱ) oxide in varying ratios was combined with either an alumina-based cement (Al300), or CaO derived from limestone as support material in a mechanical pelletiser. This production method was used to investigate its influence on possible mechanical and chemical improvements for oxygen carriers in chemical looping processes. These materials were tested in a lab-scale fluidised bed with CO or CH4 as a reducing gas at 950℃. As expected, the oxygen carriers containing a greater ratio of support material exhibited an enhanced crushing strength. Oxygen carriers comprised of a 1:3 ratio of support material to active CuO exhibited increased crushing strength by a minimum of 280% compared to pure CuO pellets. All oxygen carriers exhibited a high CO conversion yield and were fully reducible from CuO to Cu. For the initial redox cycle, Al300-supported oxygen carriers showed the highest fuel and oxygen carrier conversion. The general trend observed was a decline in conversion with an increasing number of redox cycles. In the case of CaO-supported oxygen carriers, all but one of the oxygen carriers suffered agglomeration. The agglomeration was more severe in carriers with higher ratios of CuO. Oxygen carrier Cu25Al75 (75 wt% aluminate cement and 25 wt% CuO), which did not suffer from agglomeration, showed the highest attrition with a loss of approximately 8% of its initial mass over 25 redox cycles. The reducibility of the oxygen carriers was limited with CH4 in comparison to CO. CH4 conversion were 15%-25% and 50% for Cu25Ca75 (25 wt% CuO and 75 wt% CaO) and Cu25Al75, respectively. Cu25Ca75 demonstrated improved conversion, whereas Cu25Al75 exhibited a trending decrease in conversion with increasing redox cycles.
    A thiophene-containing covalent triazine-based framework with ultramicropore for CO2 capture
    Keke Wang, Yuanzhe Tang, Qin Jiang, Youshi Lan, Hongliang Huang, Dahuan Liu, Chongli Zhong
    2017, 26(5): 902-908.  DOI: 10.1016/j.jechem.2017.07.007
    摘要 ( 1886 )  
    In this work, a 2D covalent triazine-based framework was prepared by using 1,3-dicyanobenzo[c]thiophene (DCBT) as monomer to effectively capture CO2. The resulting CTF-DCBT was characterized by FT-IR, XPS, PXRD, elemental analysis, SEM, TEM, and N2 adsorption-desorption. The results indicate that CTF-DCBT is partially crystalline and has ultramicropore (6.5 Å) as well as high heteroatom contents (11.24 wt% and 12.61 wt% for N and S, respectively). In addition, the BET surface area and total pore volume of CTF-DCBT are 500 m2/g and 0.26 cm3/g, respectively. CTF-DCBT possesses excellent thermal stability (450℃) and chemical stability towards boiling water, 4 M HCl, and 1 M NaOH. The CO2 adsorption capacity of CTF-DCBT is 37.8 cm3/g at 1 bar and 25℃. After six adsorption-desorption cycles, there is no obvious loss of CO2 uptake observed. Due to the ultramicropore and high heteroatom contents, CTF-DCBT has high isosteric heats of adsorption for CO2 and high selectivities of CO2 over N2 and CH4. At 25℃, the CO2/N2 and CO2/CH4 selectivities are 112.5 and 10.3, respectively, which are higher than those of most POFs. Breakthrough curves indicate that CTF-DCBT could effectively separate CO2/N2 and CO2/CH4 mixtures.
    Synthesis of polymeric ionic liquids material and application in CO2 adsorption
    Haiying Ran, Jiexin Wang, Ahmed A. Abdeltawab, Xiaochun Chen, Guangren Yu, Yinghao Yu
    2017, 26(5): 909-918.  DOI: 10.1016/j.jechem.2017.06.001
    摘要 ( 1898 )  
    We synthesized one quaternary ammonium polymeric ionic liquids (PILs)P[VBTHEA]Cl and three imidazolium PILs of P[VEIm]Br, P[VEIm]BF4, P[VEIm]PF6 by free-radical polymerization in solution. These PILs were characterized by FT-IR, 1H-NMR, 13C-NMR, TGA, XRD and SEM. Their CO2 adsorption capacities were measured under different pressures and temperatures by constant-volume technique. It was observed that quaternary ammonium PILs of P[VBTHEA]Cl have higher adsorption capacity for CO2 than those imidazolium PILs, following P[VBTHEA]Cl > P[VEIm]PF6 > P[VEIm]BF4 > P[VEIm]Br, which may be ascribed to higher positive charge density on ammonium cation than that on imidazolium cation and thus stronger interaction with CO2, consistent with the results from dual-mode adsorption model that ammonium PILs have much higher CO2 bulk absorption than imidazolium PILs. CO2 adsorption capacity of P[VBTHEA]Cl is 9.02 mg/g under 295 K and 1 bar, which is comparable to that of some other PILs, and is much higher than that of the corresponding ILs monomer. These PILs have good adsorption selectivity for CO2 over N2 and regeneration efficiency.
    Thermokinetic and conductivity analyzes of the high CO2 chemisorption on Li5AlO4 and alkaline carbonate impregnated Li5AlO4 samples:Effects produced by the use of CO2 partial pressures and oxygen addition
    Pedro Sánchez-Camacho, J. Francisco Gómez-García, Heriberto Pfeiffer
    2017, 26(5): 919-926.  DOI: 10.1016/j.jechem.2017.05.008
    摘要 ( 1970 )  
    The effect of CO2 partial pressure was evaluated during the CO2 chemisorption in penta lithium aluminate (Li5AlO4), using different CO2 and O2 partial pressures in the presence or absence of alkaline carbonates. Results showed that using low PO2 (0.1) did not affect the kinetic and final CO2 chemisorption process. Moreover, small additions of oxygen (PO2=0.05) into the mixture flue gas, seemed to increase the CO2 chemisorption. Additionally, the presence of alkaline carbonates modified the CO2 capture temperature range. CO2 chemisorption kinetic parameters were determined assuming a double exponential model where direct CO2 chemisorption and CO2 chemisorption controlled by diffusion processes are considered. Finally, ionic diffusion was analyzed by ionic conduction analysis, where all the gravimetric and ionic measurements were in good agreement showing different diffusion processes depending on temperature. Finally, the oxygen and alkaline carbonate additions have positive effects during the CO2 chemisorption process in Li5AlO4, and a possible reaction mechanism is presented.
    Indirect mineral carbonation of blast furnace slag with (NH4)2SO4 as a recyclable extractant
    Jinpeng Hu, Weizao Liu, Lin Wang, Qiang Liu, Fang Chen, Hairong Yue, Bin Liang, Li Lü, Ye Wang, Guoquan Zhang, Chun Li
    2017, 26(5): 927-935.  DOI: 10.1016/j.jechem.2017.06.009
    摘要 ( 1944 )  
    Large quantities of CO2 and blast furnace slag are discharged in the iron and steel industry. Mineral carbonation of blast furnace slag can offer substantial CO2 emission reduction and comprehensive utilisation of the solid waste. In this study, a recyclable extractant, (NH4)2SO4, was used to extract calcium and magnesium from blast furnace slag (main phases of gehlenite and akermanite) by using low-temperature roasting to fix CO2 through aqueous carbonation. The process parameters and efficiency of the roasting extraction, mineralisation, and Al recovery were investigated in detail. The results showed that the extractions of Ca, Mg, and Al can reach almost 100% at an (NH4)2SO4-to-slag mass ratio of 3:1 and at 370℃ in 1 h. Adjusting the pH value of the leaching solution of the roasted slag to 5.5 with the NH3 released during the roasting resulted in 99% Al precipitation, while co-precipitation of Mg was lower than 2%. The Mg-rich leachate after the depletion of Al and the leaching residue (main phases of CaSO4 and SiO2) were carbonated using (NH4)2CO3 and NH4HCO3 solutions, respectively, under mild conditions. Approximately 99% of Ca and 89% of Mg in the blast furnace slag were converted into CaCO3 and (NH4)2Mg(CO3)2·4H2O, respectively. The latter can be selectively decomposed to magnesium carbonate at 100-200℃ to recover the NH3 for reuse. In the present route, the total CO2 sequestration capacity per tonne of blast furnace slag reached up to 316 kg, and 313 kg of Al-rich precipitate, 1000 kg of carbonated product containing CaCO3 and SiO2, and 304 kg of carbonated product containing calcium carbonate and magnesium carbonate were recovered simultaneously. These products can be used, respectively, as raw materials for the production of electrolytic aluminium, cement, and light magnesium carbonate to replace natural resources.
    Mechanism study of reduction of CO2 into formic acid by in-situ hydrogen produced from water splitting with Zn:Zn/ZnO interface autocatalytic role
    Yi Le, Heng Zhong, Yang Yang, Runtian He, Guodong Yao, Fangming Jin
    2017, 26(5): 936-941.  DOI: 10.1016/j.jechem.2017.03.013
    摘要 ( 1752 )  
    We have previously developed a new process of highly efficient conversion of CO2 and water into formic acid with metallic Zn without the addition of catalyst, however, its mechanism is not clear, particularly in the catalytic role of Zn/ZnO interface. Herein, the autocatalytic role of Zn/ZnO interface formed in situ during the reduction of CO2 into formic acid with Zn in water was studied by combining high resolution transmission electron microscopy (HRTEM), X-ray diffraction (XRD) and X-ray photoelectron spectroscopy (XPS) techniques and experimental data. The electron microscope results show that possible defects or dislocations formed on Zn/ZnO interface, in which plays a key role for ZnH-formation. Further XPS analyses indicate that oxygen vacancies on Zn/ZnO interface increased at short reaction times (less than 10 min). These analyses and experimental results suggest that a highly efficient and rapid conversion of CO2 and water into formic acid should involve an autocatalytic role of the Zn/ZnO interface formed in situ, particularly at the beginning of the reaction.
    NiO-CaO materials as promising catalysts for hydrogen production through carbon dioxide capture and subsequent dry methane reforming
    Alejandra Cruz-Hernández, J. Arturo Mendoza-Nieto, Heriberto Pfeiffer
    2017, 26(5): 942-947.  DOI: 10.1016/j.jechem.2017.07.002
    摘要 ( 1697 )  
    In this work, CaO-NiO mixed oxide powders were evaluated as consecutive CO2 chemisorbents and catalytic materials for hydrogen production thought the CH4 reforming process. Between the NiOimpregnated CaO and CaO-NiO mechanical composite, the first one presented better chemical behaviors during the CO2 capture and CH4 reforming processes, obtaining syngas (H2 + CO) as final product. Results showed that syngas was produced at two different temperature ranges, between 400 and 600℃ and at T > 800℃, where the first temperature range corresponds to the CH4 reforming process but the second temperature range was attributed to a different catalytic reaction process:CH4 partial oxidation. These results were confirmed through different isothermal and cyclic experiments as well as by XRD analysis of the final catalytic products, where the nickel reduction was evidenced. Moreover, when a CO-O2 flow was used during the carbonation process a triple process was achieved:(i) CO oxidation, (ii) CO2 chemisorption and (iii) CH4 reforming. Using this gas flow the hydrogen production was always higher than that obtained with CO2.
    Synthesis and evaluation as CO2 chemisorbent of the Li5(Al1-xFex)O4 solid solution materials:Effect of oxygen addition
    Paulina Olavarría, Elizabeth Vera, Enrique J. Lima, Heriberto Pfeiffer
    2017, 26(5): 948-955.  DOI: 10.1016/j.jechem.2017.08.002
    摘要 ( 1955 )  
    Pentalithium aluminate (β-Li5AlO4) and the corresponding iron-containing solid solution (Li5(Al1-xFex)O4) were synthetized by solid-state reaction. All the samples were characterized structural and microstructurally by X-ray diffraction, solid-state nuclear magnetic resonance, scanning electron microscopy, N2 adsorption-desorption and temperature-programmed desorption of CO2. Results showed that 30 mol% of iron can be incorporated into the β-Li5AlO4 crystalline structure at aluminum positions. Moreover, iron addition induced morphological and superficial reactivity variations. Li5(Al1-xFex)O4 samples chemisorbed CO2 between 200 and 700℃, where the superficial chemisorption presented the highest enhancement, in comparison to β-Li5AlO4. Additionally, Li5(Al1-xFex)O4 samples sintered at higher temperatures than β-Li5AlO4. Isothermal CO2 chemisorption experiments of β-Li5AlO4 and Li5(Al1-xFex)O4 were fitted to a first order reaction model, corroborating that iron enhances the CO2 chemisorption, kinetically. When oxygen was added to the gas flow, CO2 chemisorption process was mainly enhanced between 400 and 600℃ for the Li5(Al0.8Fe0.2)O4 sample in comparison to β-Li5AlO4. Hence, Li5(Al1-xFex)O4 solid solution presented an enhanced CO2 chemisorption process, in the presence and absence of oxygen, in comparison to β-Li5AlO4.
    CO2 residual concentration of potassium-promoted hydrotalcite for deep CO/CO2 purification in H2-rich gas
    Xuancan Zhu, Yixiang Shi, Ningsheng Cai
    2017, 26(5): 956-964.  DOI: 10.1016/j.jechem.2017.06.006
    摘要 ( 1679 )  
    Elevated-temperature pressure swing adsorption is a promising technique for producing high purity hydrogen and controlling greenhouse gas emissions. Thermodynamic analysis indicated that the CO in H2-rich gas could be controlled to trace levels of below 10 ppm by in situ reduction of the CO2 concentration to less than 100 ppm via the aforementioned process. The CO2 adsorption capacity of potassiumpromoted hydrotalcite at elevated temperatures under different adsorption (mole fraction, working pressure) and desorption (flow rate, desorption time, steam effects) conditions was systematically investigated using a fixed bed reactor. It was found that the CO2 residual concentration before the breakthrough of CO2 mainly depended on the total amount of purge gas and the CO2 mole fraction in the inlet syngas. The residual CO2 concentration and uptake achieved for the inlet gas comprising CO2(9.7 mL/min) and He (277.6 mL/min) at a working pressure of 3 MPa after 1 h of Ar purging at 300 mL/min were 12.3 ppm and 0.341 mmol/g, respectively. Steam purge could greatly improve the cyclic adsorption working capacity, but had no obvious benefit for the recovery of the residual CO2 concentration compared to purging with an inert gas. The residual CO2 concentration obtained with the adsorbent could be reduced to 3.2 ppm after 12 h of temperature swing at 450℃. A new concept based on an adsorption/desorption process, comprising adsorption, steam rinse, depressurization, steam purge, pressurization, and high-temperature steam purge, was proposed for reducing the steam consumption during CO/CO2 purification.
    Facile synthesis of microporous carbonaceous materials derived from a covalent triazine polymer for CO2 capture
    Pillaiyar Puthiaraj, Wha-Seung Ahn
    2017, 26(5): 965-971.  DOI: 10.1016/j.jechem.2017.07.012
    摘要 ( 2032 )  
    Highly porous nitrogen-doped carbon materials were synthesized by the carbonization of a low-cost porous covalent triazine polymer, PCTP-3, which had been synthesized by the AlCl3 catalyzed FriedelCrafts reaction of readily available monomers. The nature of the bond and structure of the resulting materials were confirmed using various spectroscopic methods, and the effects of KOH activation on the textural properties of the porous carbon materials were also examined. The KOH-activated porous carbon (aPCTP-3c) materials possessed a high surface area of 2271 m2 g-1 and large micro/total pore volumes of 0.87/0.95 cm3 g-1, respectively, with narrower micropore size distributions than the porous carbon prepared without activation (PCTP-3c). The aPCTP-3c exhibited the best CO2 uptakes of 284.5 and 162.3 mg g-1 and CH4 uptakes of 39.6 and 25.9 mg g-1 at 273 and 298 K/1 bar, respectively, which are comparable to the performance of some benchmark carbon materials under the same conditions. The prepared materials exhibited high CO2/N2 selectivity and could be regenerated easily.
    Fundamentals in CO2 capture of Na2CO3 under a moist condition
    Hongchao Luo, Hirofumi Kanoh
    2017, 26(5): 972-983.  DOI: 10.1016/j.jechem.2017.08.005
    摘要 ( 1690 )  
    Capacity and kinetics of CO2 capture of Na2CO3 were studied to determine the mechanism for CO2 sequestration under ambient conditions. Bicarbonate formation of Na2CO3 was examined by a thermogravimetric analysis (TGA) under various CO2 and water vapor concentrations and the accompanying structural changes of Na2CO3 were demonstrated by X-ray diffraction (XRD). Morphological variations were observed during the reaction of CO2 capture through scanning electron microscope (SEM). Structural changes and morphological variations, which occurred during the course of the reaction, were then connected to the kinetic and exothermic properties of the CO2 capture process from the XRD and SEM measurements. The results showed that the bicarbonate formation of Na2CO3 has two different pathways. For higher CO2 and H2O concentrations, the bicarbonate formation proceeded effectively. However, for lower CO2 and H2O concentrations, the reactions were more complicated. The formation of Na2CO3·H2O from Na2CO3 as the first step, followed by the subsequent formation of Na5H3(CO3)4, and then the bicarbonate formation proceeds. To understand such fundamental properties in CO2 capture of Na2CO3 is very important for utilization of Na2CO3 as a sorbent for CO2 capture.
    Investigation of the role of Ca(OH)2 in the catalytic Alkaline Thermal Treatment of cellulose to produce H2 with integrated carbon capture
    Maxim R. Stonor, Nicholas Ouassil, Jingguang G. Chen, Ah-Hyung Alissa Park
    2017, 26(5): 984-1000.  DOI: 10.1016/j.jechem.2017.07.013
    摘要 ( 1772 )  
    The Alkaline Thermal Treatment (ATT) of biomass is one of the few biomass conversion processes that has a potential for BECCS (bio-energy with carbon capture and storage). Combining in-situ carbon capture with H2 production creates a carbon-neutral process that has the potential to be carbon-negative. This study has shown that the conversion of cellulose to H2 with suppressed CO2 formation can be achieved through the reforming of gaseous intermediates in a fixed bed of Ca(OH)2 and 10% Ni/ZrO2. Reforming occurs at low temperatures ≤ 773 K, which could allow for improved sustainability.
    CO2 absorption with ionic liquids at elevated temperatures
    Lu Bai, Dawei Shang, Mengdie Li, Zhongde Dai, Liyuan Deng, Xiangping Zhang
    2017, 26(5): 1001-1006.  DOI: 10.1016/j.jechem.2017.07.009
    摘要 ( 2097 )  
    CO2 capture with ionic liquids (ILs) has attracted many attentions, and most works focused on absorption ability at ambient temperatures, while seldom research was concerned at elevated temperatures. This not only limits the CO2 absorption application at elevated temperature, but also the determination of the operation condition of the CO2 desorption generally occurring at higher temperature. This work mainly reported CO2 solubilities in ILs at elevated temperatures and related properties were also provided. 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ([CnMIm] [Tf2N]) ILs were selected as physical absorbents for CO2 capture in this work due to their relative higher CO2 absorption capacities and good thermal stabilities. The long-term stability tests showed that[CnMIm] [Tf2N] is thermally stable at 393.15 K for long time. CO2 solubilities in[CnMIm] [Tf2N] were systematically determined at temperatures from 353.15 K to 393.15 K. It demonstrated that CO2 solubility obviously increases with the increase of pressure while slightly decreases with increase of temperature. As the length of alkyl chain on the cation increases, CO2 solubility in ILs increases. Additionally, the thermodynamic properties including the Gibbs free energy, enthalpy, and entropy of CO2 were also calculated.
    Resorcinol-formaldehyde resin-based porous carbon spheres with high CO2 capture capacities
    Xuan Wang, Jin Zhou, Wei Xing, Boyu Liu, Jianlin Zhang, Hongtao Lin, Hongyou Cui, Shuping Zhuo
    2017, 26(5): 1007-1013.  DOI: 10.1016/j.jechem.2017.07.010
    摘要 ( 2088 )  
    Porous carbon spheres are prepared by direct carbonization of potassium salt of resorcinol-formaldehyde resin spheres, and are investigated as CO2 adsorbents. It is found that the prepared carbon materials still maintain the typical spherical shapes after the activation, and have highly developed ultra-microporosity with uniform pore size, indicating that almost the activation takes place in the interior of the polymer spheres. The narrow-distributed ultra-micropores are attributed to the "in-situ homogeneous activation" effect produced by the mono-dispersed potassium ions as a form of -OK groups in the bulk of polymer spheres. The CS-1 sample prepared under a KOH/resins weight ratio of 1 shows a very high CO2 capture capacity of 4.83 mmol/g and good CO2/N2 selectivity of ~17-45. We believe that the presence of a welldeveloped ultra-microporosity is responsible for excellent CO2 sorption performance at room temperature and ambient pressure.
    Catalytic steam methane reforming enhanced by CO2 capture on CaO based bi-functional compounds
    Francesca Micheli, Manuela Sciarra, Claire Courson, Katia Gallucci
    2017, 26(5): 1014-1025.  DOI: 10.1016/j.jechem.2017.09.001
    摘要 ( 2322 )  
    Sorption enhanced steam methane reforming (SE-SMR) was performed to maximize hydrogen production and contemporary remove CO2 from the product stream using bi-functional sorbent-catalyst compounds. Samples were tested at two different scales:micro and laboratory. The CaO amount varied in the CaO-Ca12Al14O33 sorbent system synthesized by wet mixing (CaO content of 100 wt%, 56 wt%, 30 wt%, or 0 wt% and balance of Ca12Al14O33) which were upgraded to bi-functional compounds by impregnation of 3 wt% of Ni. Nitrogen adsorption (BET/BJH), X-Ray Diffraction (XRD), Temperature-Programmed Reduction (TPR) and Scanning and Transmission Electronic Microscopy (SEM and TEM, respectively) analyses were performed to characterize structural and textural properties and reducibility of the bi-functional materials and evaluate their catalytic behavior. A fixed sorbent composition CaO-Ca12Al14O33 (56 wt% of CaO and Ca12Al14O33 balance), was chosen to study the effect of different weight hourly space times (WHST) and CH4 stream compositions in SE-SMR activity. Impregnated mayenite at both micro and laboratory scales showed stable H2 content of almost 74%, with CH4 conversion of 72% similarly to the values reported by the sample containing 30 wt% of CaO in the post-breakthrough. Sample with 30 wt% of CaO showed promisingly behavior, enhancing H2 content up to almost 94.5%. When the sorption enhanced reaction is performed roughly 89% of CH4 conversion is achieved, and after the pre-breakthrough, the catalyst worked at the thermodynamic level. During cycling sorption/regeneration experiments, even if CO2 removal efficiency slightly decreases, CH4 conversion and H2 yield remain stable.
    Coassembled ionic liquid/laponite hybrids as effective CO2 adsorbents
    Yin Xu, Yingjie Zhou, Jingjing Liu, Luyi Sun
    2017, 26(5): 1026-1029.  DOI: 10.1016/j.jechem.2017.09.005
    摘要 ( 1729 )  
    Hybrid adsorbents for CO2 capture were prepared by coassembling laponite (LP) nanosheets and 1-n-butyl-3-methylimidazolium chloride (BMIMCl). The prepared BMIMCl/LP layered hybrids were systematically characterized. The interlayer distance of the BMIMCl/LP layered hybrids expanded with an increasing concentration of BMIMCl, indicating that cumulative BMIMCl was intercalated into the LP layers. The efficiency of BMIMCl toward CO2 capture was significantly enhanced after it was immobilized within LP layers.
    CO2 capture over molecular basket sorbents:Effects of SiO2 supports and PEG additive
    Lin Zhang, Xiaoxing Wang, Mamoru Fujii, Linjun Yang, Chunshan Song
    2017, 26(5): 1030-1038.  DOI: 10.1016/j.jechem.2017.09.002
    摘要 ( 1809 )  
    The objective of this work is to study the influences of silica supports and PEG additive on the sorption performance of molecular basket sorbent (MBS) for CO2 capture consisting of polyethylenimine and one of the following supports:SBA-15 (2-D structure), TUD-1 (3-D sponge-like structure) and fumed silica HS-5 (3-D disordered structure). Effects of the supports regarding pore structures and pore properties, the PEI loading amount as well as the sorption temperature were examined. Furthermore, polyethylene glycol (PEG) was introduced as an additive into the sorbents and its effect was investigated at different PEI loadings and sorption temperatures. The results suggest that the pore properties of MBS (after PEI loading) play a more important role in the CO2 sorption capacity, rather than those of the supports alone. MBS with 3D pore structure exhibits higher CO2 sorption capacity and amine efficiency than those with 2D-structured support. Among the sorbents studied, fumed silica (HS-5) based MBS showed the highest CO2 sorption capacity in the temperature range of 30-95℃, probably due to its unique interstitial pores formed by the aggregation of polymer-loaded SiO2 particles. It was found that the temperature dependence is directly related to the PEI surface coverage layers. The more PEI surface coverage layers, the higher diffusion barrier for CO2 and the stronger temperature dependence of CO2 capacity. 3D MBS exceeds 2D MBS at the same PEI coverage layers due to lower diffusion barrier. Adding PEG can significantly enhance the CO2 sorption capacity and improve amine efficiency of all MBS, most likely by alleviating the diffusion barrier within PEI bulk layers through the inter-molecular interaction between PEI and PEG.