蒙古国巴嘎诺尔(Baganuur)褐煤水蒸气气化制富氢合成气及其固有矿物质的催化作用

利用固定床气化-色谱联用装置,考察了蒙古国巴嘎诺尔(Baganuur)褐煤的水蒸气气化反应性能,研究对比了巴嘎诺尔褐煤原煤BN-R、盐酸洗煤BN-HCl、氨水洗煤BN-NH₄OH、先酸洗后碱处理煤BN-HCl-NaOH及原煤和盐酸洗煤热解预处理煤样BN-R-Char与BN-HCl-Char在水蒸气气化过程中气态产物H₂、CO和CO₂的生成规律.研究结果表明,上述煤样的水蒸气气化过程中H₂、CO和CO₂的生成速率存在明显差异,与盐酸洗煤样相比,BN-R、BN-HCl-NaOH及BN-R-Char比对应矿物质脱除煤样的水蒸气气化速率高,充分说明巴嘎诺尔褐煤中某些固有矿物质对其水蒸气气化反应具有显著的催化作用,显著提高了其气化反应速率,使起始气化温度和气化反应主体温度均降低100 ℃以上,在提高H₂和CO₂生成量同时,还降低了CO生成量,制得了高H₂/CO(物质的量比)的合成气.用盐酸脱除矿物质所得BN-HCl同BN-HCl-Char的水蒸气气化性能相似.与BN-R相比,BN-HCl与BN-HCl-Char水蒸气气化反应性明显下降,说明对巴嘎诺尔褐煤水蒸气气化起催化作用的矿物质成分在盐酸洗脱的矿物质中.经过分析,发现矿物质对巴嘎诺尔褐煤水蒸气气化反应的催化作用,主要是通过提高水煤气变换反应速率实现的.最后,结合文献报道,提出了巴嘎诺尔褐煤水蒸气气化反应过程中矿物质的原位催化机理.     

纳米负载型V2O5-WO3/TiO2催化剂碱中毒及再生研究

实验制备了陶瓷颗粒为骨架的纳米级V₂O₅-WO₃/TiO₂(C)催化剂。采用浸渍法模拟碱金属中毒,研究了中毒及再生对催化剂脱硝活性的影响,运用XRD、FT-IR、H₂-TPR、XPS技术表征分析了碱金属对催化剂的失活作用。实验表明,碱金属能使催化剂活性降低,钾的毒性大于钠。FT-IR结果显示,催化剂以Lewis酸作为活性酸位。H₂-TPR、XPS结果表明,钾的加入降低了催化剂的氧化能力,主要影响了催化剂表面的吸附氧。采用单纯的水洗方法并不能提高催化剂活性,而酸洗再生后催化剂在较高反应温度下活性得到较好的恢复。     

污水污泥空气气化特性的研究

利用外热式下吸固定床气化实验装置,以空气为气化剂对五种不同性质污泥的气化特性进行了研究。结果表明,升高气化温度有利于提高气化气的品质,气化气中CO、CH₄和H₂的含量和气化气热值随气化剂流量的减小而增加。污泥厌氧消化过程使气化气品质降低;污水处理工艺对污泥气化气组成和热值亦产生影响,其中连续SBR工艺的未消化污泥气化气中CO、CO₂的含量最高,而H₂、CH₄和C_mH_n的含量最低;活性污泥法的未消化污泥气化气中H₂和C_mH_n含量最高;A²/O工艺的未消化污泥气化气中CO、CO₂的含量最低,而CH₄的含量最高,且三个污水工艺污泥的气化气热值依次升高。     

H2气氛下褐煤快速热解过程中CH4逸出规律的分析

在带有输送煤样的管式反应器上进行了霍林河褐煤加压快速氢解实验,分析了H₂对煤/半焦的化学键断裂和对CH₄生成规律的影响。在加压快速氢解条件下,CH₄产率随着热解温度升高、压力的增大而增大;在50% H₂气氛下,操作压力为1.0 MPa、温度为900 ℃时,CH₄产率为8.08%,达到最大,较N₂气氛下的提高了72.5%。H₂或H·自由基诱发了芳环的开裂、侧链、脂肪链和醚键的断裂,促进了煤热解。CH₄产率的增加主要是由于外部供H的结果;热解温度低于700 ℃时,H₂对煤结构中活性基团的作用促进了煤热解,导致了CH₄产率的增加;而热解温度高于700 ℃后,煤/半焦加氢气化促进了CH₄产率的增加。     

稻秆的烘焙预处理及其固体产物的气化反应性能

稻秆资源分散、水分含量高且密度低、热值低,烘焙预处理技术能够降低收集运输的物流成本,获得的固体产物能量密度高、可磨性好,适于气流床气化。在固定床热解装置上通N₂保护,稻秆分别经过200℃、250℃、300℃烘焙30min,得到的固体产物在热重分析仪中与CO₂进行非等温气化实验,升温速率20℃/min,终温1200℃。实验结果表明,稻秆烘焙产物以固体剩余物和不凝结气体为主,还有少量可凝结液体(水分和焦油)。气体产物中CO₂所占比例超过80%,其次为CO和微量CH₄。预处理温度越高,固体剩余物越少、气体产物越多,可凝结性液体变化不大。稻秆烘焙过程的能量产率为40%~60%,随温度升高经历了急剧下降和缓慢降低两个阶段。固体剩余物的可磨性相比原始稻秆有了很大的提高,易于制细粉用于气流床气化。烘焙温度升高,所得固体产物气化反应性提高。根据Coats-Redfern法确定烘焙稻秆焦-CO₂气化反应机理符合二维扩散模型,求得反应活化能73kJ/mol~88kJ/mol。     

煤炭解耦燃烧过程N迁移与转化Ⅲ:多组分气相化学反应实验

在理想平推流反应器中进行了模拟热解气对模拟烟气中NO、N₂O的还原实验研究,考察了反应温度、过剩空气系数,模拟热解气中CH₄、CO、H₂、NH₃入口浓度与模拟烟气中NO、N₂O入口浓度对NO、N₂O与总氮转化率的影响。结果表明,向NH₃添加可燃气体CO、H₂、CH₄可使NO还原窗口向低温方向移动150~200 K,该温度窗口为1 073~1 223 K;但NH₃-CO-H₂-CH₄-O₂体系对NO、N₂O的还原分解作用依赖于体系的O₂浓度,仅在富燃料情形(过剩空气系数λ为0.6)下可分别达60.6%、100%的NO、N₂O脱除率;在反应温度1 073~1 223 K及过剩空气系数λ为0.6条件下,较高的热解气CH₄、CO、H₂浓度可增加NO排放,但有利于还原N₂O;增加NH₃入口浓度可增加NO分解率。     

天然铁矿石为氧载体的生物质化学链气化制合成气实验研究

在一个小型鼓泡流化床反应器上以Ar气为流化介质,对以天然铁矿石为氧载体的生物质化学链气化制合成气过程进行了研究。考察了反应温度对合成气组分、气体产率、碳转化率以及气化效率的影响,反应时间对合成气组分的影响;探讨了氧载体存在对生物质气化过程的影响。结果表明,天然铁矿石可以作为生物质化学链气化制合成气反应过程的氧载体,代替富氧空气或高温水蒸气作为生物质气化的气化剂;随着温度的升高,产物气体中CO、H₂的浓度逐渐增加,CO₂、CH₄浓度缓慢降低;随着反应时间的延长,合成气中H₂、CO、CH₄的相对浓度缓慢增加,而CO₂相对浓度逐渐降低;氧载体的存在能显著提高气体产率和碳的转化率及气化效率。扫描电镜-能谱(SEM-EDS)分析表明,当超过850 ℃时,铁矿石氧载体颗粒表面烧结现象明显,但反应前后,颗粒表面的成分及含量基本保持不变。     

SOFC中干甲烷浓度对Ni-YSZ阳极上反应的影响

为探讨固体氧化物燃料电池(solid oxide fuel cell, SOFC)中干甲烷浓度对反应的影响,采用色谱在线测量阳极尾气,总结阳极尾气的变化规律。在此基础上,分析干甲烷在固体氧化物燃料电池Ni-YSZ阳极上的反应,寻找干甲烷浓度与电流对电池阳极反应影响的数学关系。结果表明,随着电流密度的增加,低浓度甲烷按顺序发生CH₄+O^2- → CO+2H₂+2e^-、CH₄+2O^2- → CO+H₂O+H₂ +4e^-、CH₄+3O^2- → CO+2H₂O + 6e^-、CH₄+4O^2- → CO₂+2H₂O+8e^-反应,高浓度甲烷只发生甲烷的第一个氧化反应,中浓度甲烷发生前两个或前三个反应。依据法拉第第一定律及反应物之间的关系,确定甲烷的低、中、高浓度的判定依据分别为:q_v(CH₄)≤I/(4F)、I/(4F)≤q_v(CH₄)≤I/(2F)、q_v(CH₄)≥I/(2F)。     

松木粉气流床气化特性实验研究

在气流床气化实验装置上进行了松木粉气化特性的研究。考察了温度、氧当量比、水蒸气配比对气体产物的成分、气化特性和固体产物的微观形态及成分的影响,结果表明,随着温度的升高,CO与H₂浓度显著升高,CO₂与CH₄浓度明显下降,碳转化率、产气率、产气热值有所提高;氧当量比从0.2上升至0.5时,CO与H₂浓度降低超过10%,CO₂浓度则上升100%以上,碳转化率提高至92.9%,产气率有所上升,而产气热值则降低超过20%;水蒸气配比从0增大至0.58时,H₂/CO体积比由0.63提高为1.40,碳转化率、产气率和产气热值均呈现先增大后减小趋势。由SEM照片可以看出,固体残渣主要由类球状或块状结构与纤维团聚结构两部分组成。温度升高使残渣颗粒由呈现不规则形状逐渐向球形转化,氧当量比的增大使残渣中类球状颗粒表面孔洞与裂缝明显增多直至破碎。     

甲烷自热重整制氢的热力学和动力学分析

对甲烷自热重整进行了系统的热力学分析,并采用预混合层流模型结合甲烷氧化、蒸汽重整、干重整机理对反应过程进行了动力学分析。结果表明,甲烷自热重整的平衡产物及其浓度主要受温度、O₂/CH₄、H₂O/CH₄的影响;压力影响不是十分明显,主要影响达到平衡的速度。在715℃~730℃、压力0.7MPa~1.0MPa,控制O₂/CH₄在0.60~0.70、H₂O/CH₄在3.15~3.25,可以得到H₂>68%、CO<10%的产物气,积炭率接近于0。动力学分析表明,自热重整过程分为两个主要阶段进行,在起始阶段主要发生甲烷氧化反应,产物主要为H₂O和CO₂;第二阶段以甲烷蒸汽重整反应为主,伴随水气变换反应（WGS）和微弱的干重整,H_2、CO和CO₂为主要产物。调节初始水浓度可以控制快速氧化阶段反应速率,避免“热点”出现,抑制CO的生成。     

A study of the solubility of yttrium,praseodymium, neodymium,and gadolinium sulfates in the presence of sodium and potassium in sulfuric-phosphoric acid solutions at 20°C

Solubility of yttrium, praseodymium, neodymium, and gadolinium sulfates in the presence of sodium and potassium ions and the composition of solid phases were studied at 20°C in relation to the concentration of acids in sulfuric acid, phosphoric acid, and sulfuric-phosphoric acid solutions containing up to 36 wt % H₂SO₄ and 33.12 g 1^?1 H₃PO₄.     

The determination of copper in whetlerized carbon following destructive oxidation of carbon employing hot concentrated perchloric acid

The determination of copper in whetlerized gas mask carbon has been described. The sample is “ashed” by wet oxidation employing mixed HN0₃ + HCIO₄ + H₂SO₄. The reaction is catalyzed through the addition of small amounts of chromium.The copper recovered as copper sulfate following wet ashing is reduced to Cu(I) by potassium iodide in. acetic acid solution (with previous neutralization of sulfuric acid by sodium hydroxide). The liberated iodine is then titrated employing standard sodium thiosulfate solution with starch as indicator.Individual analyses require 25–30 minutes for complete analysis.     

Inter- und intramolekulare Umlagerung der Sulfogruppe in 2-Naphtol-1-sulfonsäure

The isomerisation of 2-naphthol-1-sulfonic acid (potassium salt) into 2-naphthol-6-sulfonic acid has been studied using labelled sulfuric acid (H₂³⁵SO₄). In 40 to 50% aqueous sulfric acid the reaction takes place exclusively by an intermolecular mechanism (protio-desulfonation and resulfonation). In glacial acetic acid, in the presence of an excess of sulfuric acid, the rearrangement is partly intramolecular. With an equimolar amount of sulfuric acid the rearrangement is completely intramolecular. This reaction is first order with respect to 2-naphthol-1-sulfonic acid and zeroth order with respect to excess of sulfuric acid. A mechanism for the reaction is proposed.     

Electrochemical Synthesis of Co-intercalation Compounds in the Graphite-H<Subscript>2</Subscript>SO<Subscript>4</Subscript>-H<Subscript>3</Subscript>PO<Subscript>4</Subscript>System

Anodic oxidation of highly oriented pyrolytic graphite in an electrolyte containing concentrated sulfuric and anhydrous phosphoric acids is studied for the first time. The synthesis was carried out under galvanostatic conditions at a current I = 0.5 mA and an elevated temperature (t = 80°C). Intercalation compounds of graphite (ICG) are shown to form at all concentration ratios of H₂SO₄ and H³PO⁴ acids. The intercalation compound of step I forms in solutions containing more than 80 wt % H₂SO₄, a mixture of compounds of intercalation steps I and II forms in 60% H²SO⁴, intercalation step II is realized in the sulfuric acid concentration range from 10 to 40%, and a mixture of compounds of intercalation steps III and II is formed in 5% H₂SO₄ solutions. The threshold concentration of H₂SO₄ intercalation is ∼2%. With the decrease in active intercalate (H₂SO₄) concentration, the charging curves are gradually smoothed, the intercalation step number increases, and the potentials of ICG formation also increase. As the sulfuric acid concentration in the electrolyte changes from 96 to 40 wt %, the filled-layer thickness d _i in ICG monotonously increases from 0.803 to 0.820 nm, which apparently is associated with the greater size of phosphoric acid molecules. With further increase in H₃PO₄ concentration in solution, d _i remains unchanged. According to the results of chemical analysis, both acids are simultaneously incorporated into the graphite interplanar spacing and their ratio in ICG is determined by the electrolyte composition.__________Translated from Elektrokhimiya, Vol. 41, No. 5, 2005, pp. 651–655.Original Russian Text Copyright © 2005 by Leshin, Sorokina, Avdeev.     

Effect of the acidic treatment on the adsorption and structural properties of the natural mineral sorbent M45C20

Adsorption and structural properties of the initial natural mineral sorbent M₄₅C₂₀ and the sorbent treated with 2.33 M H₂SO₄ were studied. The sorbent mainly consists of montmorillonite and clinoptilolite. Aluminum, calcium, magnesium, sodium, and potassium ions are removed from the structure under the action of the acid. The specific surface, porosity of the sorbent, and pore size increase during this process. The sorption of ammonium ions in the natural samples predominantly follows the ion-exchange mechanism (exchange to calcium, magnesium, sodium, and potassium ions). The acid treatment changes the composition of the cation-exchange complex and results in an increase in the sorption capacity to ammonium ions by a factor of ??1.3.     

Base-Catalyzed cyclization of N-propargylamides to oxazoles

The base-catalyzed cyclization of some N-propargylamides to oxazoles has been studied in the presence of sodium hydride and potassium carbonate. The α-arylsubstituted propargylamides 1c-d (Ar = p-OMeC₆H₄ ( 1c ), C₆H₅ ( 1d ), and p-O₂NC₆H₄ ( 1e )) cyclized with markedly higher rates ( 1e > 1d > 1c ) than the unsubstituted and α-methyl substituted propargylamides 1a and 1b . A ¹H nmr spectroscopic experiment demonstrated the presence of an allenic intermediate in the potassium carbonate-catalyzed ring closure of 1e . The observed rank order of reactivities correlates well with the acidities of the respective propargylic hydrogens of the amides and with the ability of the ring closed intermediates to stabilize an oxazole anion. The results demonstrate that the base-catalyzed formation of oxazoles from propargylamides may proceed via an allenic intermediate.     

Properties of aqueous salt solutions of poly(ethylene oxide)

The determination of the properties of aqueous salt solutions of poly(ethylene oxide) has been extended to cloud-point and θ-temperature measurements in sodium acetate, potassium fluoride, sodium thiosulfate, and potassium phosphate. The Hofmeister series for the decreasing effect of anion species in salting out the polymer is accordingly extended. However, the order of the effect depends on whether it is made on the basis of molar anion concentration the molar concentration of unit anion charge, or the ionic strength. Viscosity measurements on θ and non-θ solutions containing zinc sulfate, potassium fluoride, and potassium phosphate gave polymer dimensions (in addition to limiting viscosity numbers etc.), and characteristic ratios in good agreement with theoretical predictions (Abe and Mark), and enthalpy and entropy parameters χ_H and χ_s; the latter values, nominally ?0.14 and 0.63, are identical at 298 K for the three salt species.     

Accelerated chemical degradation of polyacrylamide

The chemical degradation of polyacrylamide(PAM) at low temperature in aqueous medium was initiated by peroxides. The degradation degree of the polymer rose with the reaction time. The degradation degree of PAM depended not only on peroxide characteristic but also on the concentration of polyacrylamide and potassium persulfate, degradation temperature and original molecular weight of PAM. The results showed that the order of degradation degree of PAM in three peroxides is K₂S₂O₈ > K₂S₂O₈ — Na₂S₂O₃ > H₂O₂. The degradation degree of PAM grew as reaction temperature, molecular weight of PAM, concentration of potassium persulfate and PAM increased.     

Demetallation of α,β,γ,δ-tetrakis(p-sulfophenyl) porphiniron(III) in mineral acid–alcohol–water media

Demetallation rates of α,β,γ,δ-tetrakis(p-sulfophenyl)porphiniron(III) in hydrochloric acid–ethanol–water, perchloric acid–ethanol–water, and sulfuric acid–alcohol–water media were determined. For a given acidity value H₀ the order of the rates for the three acids was HCl > H₂SO₄ > HClO₄. This is also the order for complex formation between acid anion and iron(III). Consequently ligands as well as protons are involved in the breaking of bonds between the metal and the porphyrin leading to the formation of the activated complex. The log k values for HCl and HClO₄ media were not linearly related to the Hammett acidity function as they were for sulfuric acid–ethanol–water media. The average ΔH? and ΔS?values for the HCl media were 18.4 ± 1.4 kcal/mol and ? 19 ± 3 cal K mol, respectively, in very close agreement with those for H₂SO₄ media despite the difference in H ₀ dependence. For H₂SO₄–alcohol–water media the order of the rates was butanol > propanol > ethanol with little difference between isomeric alcohols.     

Aerobic oxidative iodination of organic molecules activated by sodium nitrite

Aerobic oxidative iodination activated by sodium nitrite occurs effectively and selectively with 100% iodine atom economy with air as the oxidant. Silica-supported sulfuric acid was used for the activation of the catalyst and iodination. Thus, I₂/NaNO₂/air/silica-supported H₂SO₄ in acetonitrile iodinated aromatics, ketones and aldehydes effectively at ambient temperature.