Isothermal reduction kinetics of Panzhihua ilmenite concentrate under 30vol% CO-70vol% N2 atmosphere

The reduction of ilmenite concentrate in 30vol% CO-70vol% N₂ atmosphere was characterized by thermogravimetric and differential thermogravimetric (TG-DTG) analysis methods at temperatures from 1073 to 1223 K. The isothermal reduction results show that the reduction process comprised two stages; the corresponding apparent activation energy was obtained by the iso-conversional and model-fitting methods. For the first stage, the effect of temperature on the conversion degree was not obvious, the phase boundary chemical reaction was the controlling step, with an apparent activation energy of 15.55-40.71 kJ·mol-1. For the second stage, when the temperatures was greater than 1123 K, the reaction rate and the conversion degree increased sharply with increasing temperature, and random nucleation and subsequent growth were the controlling steps, with an apparent activation energy ranging from 182.33 to 195.95 kJ·mol-1. For the whole reduction process, the average activation energy and pre-exponential factor were 98.94-118.33 kJ·mol-1 and 1.820-1.816 min-1, respectively.     

Isothermal reduction kinetics and mineral phase of chromium-bearing vanadium-titanium sinter reduced with CO gas at 873-1273 K

Reduction of chromium-bearing vanadium-titanium sinter (CVTS) was studied under simulated conditions of a blast furnace, and thermodynamics and kinetics were theoretically analyzed. Reduction kinetics of CVTS at different temperatures was evaluated using a shrinking unreacted core model. The microstructure, mineral phase, and variation of the sinter during reduction were observed by X-ray diffraction, scanning electron microscopy, and metallographic microscopy. Results indicate that porosity of CVTS increased with temperature. Meanwhile, the reduction degree of the sinter improved with the reduction rate. Reduction of the sinter was controlled by a chemical reaction at the initial stage and inner diffusion at the final stage. Activation energies measured 29.22-99.69 kJ/mol. Phase transformations in CVTS reduction are as follows:Fe₂O₃→Fe₃O₄→FeO→Fe; Fe₂TiO₅→Fe₂TiO₄→FeTiO₃; FeO·V₂O₃→V₂O₃; FeO·Cr₂O₃→Cr₂O₃.     

In situ reaction mechanism of MgAlON in Al–Al_2O_3–MgO composites at 1700°C under flowing N_2

The Al–Al_2O_3–MgO composites with added aluminum contents of approximately 0wt%, 5wt%, and 10wt%, named as M_1, M_2, and M_3, respectively, were prepared at 1700°C for 5 h under a flowing N_2 atmosphere using the reaction sintering method. After sintering, the Al–Al_2O_3–MgO composites were characterized and analyzed by X-ray diffraction, scanning electron microscopy, and energy-dispersive X-ray spectroscopy. The results show that specimen M_1 was composed of MgO and MgAl_2O_4. Compared with specimen M_1, specimens M_2 and M_3 possessed MgAlON, and its production increased with increasing aluminum addition. Under an N_2 atmosphere, MgO, Al_2O_3, and Al in the matrix of specimens M_2 and M_3 reacted to form MgAlON and AlN-polytypoids, which combined the particles and the matrix together and imparted the Al–Al_2O_3–MgO composites with a dense structure. The mechanism of MgAlON synthesis is described as follows. Under an N_2 atmosphere, the partial pressure of oxygen is quite low; thus, when the Al–Al_2O_3–MgO composites were soaked at 580°C for an extended period, aluminum metal was transformed into AlN. With increasing temperature, Al_2O_3 diffused into AlN crystal lattices and formed AlN-polytypoids; however, MgO reacted with Al_2O_3 to form MgAl_2O_4. When the temperature was greater than(1640 ± 10)°C, AlN diffused into Al_2O_3 and formed spinel-structured AlON. In situ MgAlON was acquired through a solid-solution reaction between AlON and Mg Al_2O_4 at high temperatures because of their similar spinel structures.     

Impact of technology advances on China’s CO2 emission reduction

Global warming tends to be the major characteristics of the dramatic global climate change. To deal with these changes, the impact of reducing greenhouse gas (GHG) emission on Chinese future economic and social development has to be assessed. In this paper, a Regional Integrated model of Climate and the Economy (RICE), which is well known and accepted widely, has been used for Chinese economic assessment of climate change after introduction, assimilation and verification. Based on a sensitivity analysis of technical parameters in the RICE model and constrained targets proposed for energy saving and emissions reduction technological advance programs of China from 2000 to 2050, the economic impact of the programs is examined. The results indicate that when technology advances, Chinese CO₂ emission, climate loss, and the growth rate of atmospheric CO₂ concentration and temperature will all decrease. It is assumed that in 2010, the CO₂ emission is 20% lower than in 2005, CO₂emission in 2050 would only double the level in 2000, the accumulative CO₂ emission would be decreased by 12.4 GtC, and the atmospheric CO2 concentration and temperature in 2050 would reduce by 35 GtC and 0.04°C respectively from 2000 to 2050. The accumulative climate loss from 2000 to 2050 will drop down by 4.6 billion dollar, which only accounts for 6% of the global total benefits. However, the economic benefit the developed countries will obtain is 10 times that for China under such a technological advance scenario. The decrease of the CO₂ emission control rate is 1% in cooperation policy while 4.6% in non-cooperation policy, which would relieve China’s burden in the control of CO₂ total emission and thereby benefit China in participation of the international cooperation for CO₂ emission reduction.     

Static opaque chamber-based technique for determination of net exchange of CO2 between terrestrial ecosystem and atmosphere

Carbondioxide(CO2),akeygreenhousegas,con-tributesgreatlytoglobalwarming.TheatmosphericCO2concentrationhasincreasedby31%since1750[1].Theincreaseratewas3.2±0.1Pga-1(1Pg=1015g)inthe1990sandthecurrentincreaserateisunprecedentedoverthepast20000years[1].TheatmosphericCO2contentismostlydependentonthenetexchangeofCO2withincarbonpoolsinvolvedinthecarboncycleprocesses.InvestigationoftheprocessesandmechanismsofCO2exchangebetweenterrestrialecosystemandtheatmos-pherehasbeenbecomingoneofthehotspotswit…     

Reduction mechanism of high-chromium vanadium–titanium magnetite pellets by H_2–CO–CO_2 gas mixtures

The reduction of high-chromium vanadium–titanium magnetite as a typical titanomagnetite containing 0.95wt% V2O5 and 0.61wt% Cr2O3 by H2–CO–CO2 gas mixtures was investigated from 1223 to 1373 K. Both the reduction degree and reduction rate increase with increasing temperature and increasing hydrogen content. At a temperature of 1373 K, an H2/CO ratio of 5/2 by volume, and a reduction time of 40 min, the degree of reduction reaches 95%. The phase transformation during reduction is hypothesized to proceed as follows: Fe2O3 → Fe3O4 → FeO → Fe; Fe9 TiO 15 + Fe2Ti3O9 → Fe2.75Ti0.25O4 → FeT iO 3 → TiO 2;(Cr0.15V0.85)2O3 → Fe2VO4; and Cr1.3Fe0.7O3 → FeC r2O4. The reduction is controlled by the mixed internal diffusion and interfacial reaction at the initial stage; however, the interfacial reaction is dominant. As the reduction proceeds, the internal diffusion becomes the controlling step.     

Responses of rice growth to copper stress under free-air CO2 enrichment （FACE）

The responses of rice to the second degree contamination of copper were studied by pot experiments under free-air CO2 enrichment （FACE） with 570 μmol ·mol^-1 of CO2. The results showed that the content of copper in rice leaves was reduced with the CO2 concentration reaching 570 μmol· mol^-1 and this happened more significantly under the second degree contamination of copper. Under FACE, activities of superoxide dismutase （SOD） enzyme in rice leaves treated by copper contamination were induced, whereas the contents of glutathione （GSH） and glutathione disulfide （GSSG） had no significant difference from the control. In the presence of ambient CO2, activities of SOD enzyme treated by copper pollution were suppressed during the whole rice growth, however, the contents of GSH and GSSG were induced at tillering and jointing stages, and then restored to the control levels in later growth under the second degree contamination of copper. With the rice growing, the content of malondialdehyde （MDA） rises continuously, but there had been no significant difference between the treatments at the same growth stage. Further studies are needed on the response mechanism of rice to Cu stress under elevated CO2.     

Shear-thinning behavior of the CaO–SiO_2–CaF_2–Si_3N_4 system mold flux and its practical application

Satisfying the mold-flux performance requirements for high-speed continuous casting necessitates the development of a new non-Newtonian-fluid mold flux with shear-thinning behavior, i.e., a mold flux whose viscosity is relatively high under lower shear rates and relatively low under higher shear rates. In this work, a mold flux that exhibits shear-thinning behavior was developed by adding different amounts of Si_3N_4 to the CaO–SiO_2–CaF_2 mold flux. The shear-thinning behavior was investigated using a rotational viscometer. In addition, the microstructure of the newly prepared slags was studied by high-temperature Raman spectroscopy and X-ray photoelectron spectroscopy. The results showed that the mechanism of shear-thinning was attributable to a temporary viscosity loss caused by the one-way shear stress, whereas the corresponding magnitude of shear-thinning was closely related to the degree of polymerization(DP). Finally, the non-Newtonian fluid mold flux was used for laboratory casting tests, which revealed that the mold flux could reduce slag entrapment and positively affect the continuous casting optimization.     

高浓度CO2对70%正庚烷+30%甲苯着火延迟的影响

为了研究柴油在O2/CO2环境下的着火延迟时间,建立了以70%正庚烷+30%甲苯作为柴油表征燃料的着火延迟时间模型,该模型考虑了高浓度CO2对着火的阻燃作用,得到了着火延迟时间与温度、环境密度以及O2、CO2气体浓度等之间的函数关系。利用正庚烷/甲苯机理的仿真计算和定容燃烧弹可视化试验,对不同CO2体积分数下的着火延迟时间和影响着火发生的重要基元反应进行深入研究。结果表明：该模型能够预测柴油在O2/CO2环境下的着火延迟时间,且在50%CO2环境下计算和实验的平均误差值为5.71%;CO2的热效应对着火延迟时间的影响起主导作用,同时当CO2体积分数大于60%时,CO2的第三体碰撞效应对着火发生的促进作用显著增强。     

E-E energy transfer rate for the reaction of N_2(a~1Π_g)+CO(X~1∑)→CO(A~1Π)+N_2(X~1∑_g)

The metastable N_2(a~1 Π_g, v~′) is not only one of the most important energy carriers in the discharge of nitrogen, but also one of the most prominent ultraviolet molecular emission source in the ionosphere. Knowledge of its energy transfer processes is important for chemical lasers, atmosphere chemistry and remote sensing applications. In 1972, Golde and     

Comparative study on the corrosion behavior of X52, 3Cr,and 13Cr steel in an O2–H2O–CO2 system: products,reaction kinetics,and pitting sensitivity

The corrosionbehaviors of X52, 3Cr low-alloy steel, and 13Cr stainless steel were investigated inanO2–H2O–CO2 environment at varioustemperaturesand O2–CO2partial-pressure ratios. The results showed thatthe corrosion rates of X52, 3Cr, and 13Cr steels in-creased with increasing temperature. The corrosion ratesslowly increased at temperaturesless than100℃ and increased sharply when the temperature exceeded100℃. In the absence of O2, X52, 3Cr, and 13Cr exhibited uniform corrosion morphology and FeCO3 was the main corrosion product. When O2 was introduced into the system, various forms of Fe2O3 appeared on the surface of the samples. The Cr content strongly influenced the corrosion resistance. The 3Cr steel with a low Cr content was more sensitive to pitting than the X52 or 13Cr steel. Thus, pitting occurred on the surface of 3Cr when 1.25 MPa of O2 was added; this phenomenon is related to the non-uniform distribution of Cr in 3Cr.     

Evolution of ferronickel particles during the reduction of low-grade saprolitic laterite nickel ore by coal in the temperature range of 900–1250℃ with the addition of CaO–CaF_2–H_3BO_3

The method of producing ferronickel at low temperature(1250–1400℃) has been applied since the 1950s at Nippon Yakin Kogyo,Oheyama Works, Japan.Limestone was used as an additive to adjust the slag composition for lowering the slag melting point.The ferronickel product was recovered by means of a magnetic separator from semi-molten slag and metal after water quenching.To increase the efficiency of magnetic separation, a large particle size of ferronickel is desired.Therefore, in this study, the influences of CaO, CaF_2, and H_3BO_3 additives on the evolution of ferronickel particle at ≤1250℃ were investigated.The experiments were conducted at 900–1250℃ with the addition of CaO,CaF_2, and H_3BO_3.The reduction processes were carried out in a horizontal tube furnace for 2 h under argon atmosphere.At 1250℃, with the CaO addition of 10 wt% of the ore weight, ferronickel particles with size of 20 μm were obtained.The ferronickel particle size increased to 165μm by adding 10 wt% CaO and 10 wt% CaF_2.The addition of boric acid further increased the ferronickel particle size to 376 μm, as shown by the experiments with the addition of 10 wt% CaO, 10 wt% CaF_2, and 10 wt% H_3BO_3.     

Spheroidization of silica powders by radio frequency inductively coupled plasma with Ar–H_2 and Ar–N_2 as the sheath gases at atmospheric pressure

Amorphous spherical silica powders were prepared by inductively coupled thermal plasma treatment at a radio frequency of 36.2 MHz. The effects of the added content of hydrogen and nitrogen into argon(serving as the sheath gas), as well as the carrier gas flow rate, on the spheroidization rate of silica powders, were investigated. The prepared silica powders before and after plasma treatment were examined by scanning electron microscopy, X-ray diffraction, and laser granulometric analysis. Results indicated that the average size of the silica particles increased, and the transformation of crystals into the amorphous state occurred after plasma treatment. Discharge image processing was employed to analyze the effect of the plasma temperature field on the spheroidization rate. The spheroidization rate of the silica powder increased with the increase of the hydrogen content in the sheath gas. On the other hand, the spheroidization rate of the silica power first increased and then decreased with the increase of the nitrogen content in the sheath gas. Moreover, the amorphous content increased with the increase of the spheroidization rate of the silica powder.     

Synergetic effect of multiple phases on hydrogen desorption kinetics and cycle durability in ball milled MgH2–PrF3–Al–Ni composite

A new Mg MgH₂–PrF₃–Al–Ni composite was prepared by ball milling under hydrogen atmosphere. After initial dehydrogenation and rehydrogenation, Pr₃Al₁₁, MgF₂, PrH₃ and Mg₂NiH₄ nanoparticles formed accompanying the main phase MgH₂. The hydrogen absorption-desorption properties were measured by using a Sieverts-type apparatus. The results showed that the Mg MgH₂–PrF₃–Al–Ni composi...     

Evolution of ferronickel particles during the reduction of low-grade saprolitic laterite nickel ore by coal in the temperature range of 900–1250℃with the addition of CaO–CaF2–H3BO3

The method of producing ferronickel at low temperature(1250–1400℃)has been applied since the 1950s at Nippon Yakin Kogyo,Oheyama Works,Japan.Limestone was used as an additive to adjust the slag composition for lowering the slag melting point.The ferronickel product was recovered by means of a magnetic separator from semi-molten slag and metal after water quenching.To increase the efficiency of magnetic separation,a large particle size of ferronickel is desired.Therefore,in this study,the influences of CaO,CaF₂,and H₃BO₃ additives on the evolution of ferronickel particle at≤1250℃were investigated.The experiments were conducted at 900–1250℃with the addition of CaO,CaF₂,and H₃BO₃.The reduction processes were carried out in a horizontal tube furnace for 2 h under argon atmosphere.At 1250℃,with the CaO addition of 10 wt%of the ore weight,ferronickel particles with size of 20μm were obtained.The ferronickel particle size increased to 165μm by adding 10 wt%CaO and 10 wt%CaF₂.The addition of boric acid further increased the ferronickel particle size to 376μm,as shown by the experiments with the addition of 10 wt%CaO,10 wt%CaF₂,and 10 wt%H₃BO₃.     

Comparative study on the corrosion behavior of X52, 3Cr,and 13Cr steel in an O_2–H_2O–CO_2 system: products,reaction kinetics,and pitting sensitivity

The corrosion behaviors of X52, 3Cr low-alloy steel, and 13Cr stainless steel were investigated in an O_2–H2O–CO_2 environment at various temperatures and O_2–CO_2 partial-pressure ratios. The results showed that the corrosion rates of X52, 3Cr, and 13Cr steels increased with increasing temperature. The corrosion rates slowly increased at temperatures less than 100°C and increased sharply when the temperature exceeded 100°C. In the absence of O_2, X52, 3Cr, and 13Cr exhibited uniform corrosion morphology and Fe CO3 was the main corrosion product. When O_2 was introduced into the system, various forms of Fe_2O_3 appeared on the surface of the samples. The Cr content strongly influenced the corrosion resistance. The 3Cr steel with a low Cr content was more sensitive to pitting than the X52 or 13Cr steel. Thus, pitting occurred on the surface of 3Cr when 1.25 MPa of O_2 was added; this phenomenon is related to the non-uniform distribution of Crin 3Cr.