工业原料铁制备浆态床FT合成用的Fe-Cu-K-Si催化剂的探索

费托合成技术是公认的将煤基合成气转化为液体燃料和化工原料的重要技术途径。虽然固定床费托合成技术从五十年代起已经工业运转，但是浆态床费托合成技术由于其传热性能好，可直接使用第二代气化炉生产的富CO合成气，反应器结构简单，单台反应器生产能力大，开工率高，产品结构合理，     

Determination of mercury in soils and sediments by graphite furnace atomic absorption spectrometry with slurry sampling

A graphite furnace atomic absorption spectrometric procedure for the determination of mercury is presented, in which the samples are suspended in a solution containing hydrofluoric and nitric acids. Silver nitrate (4% m/v) and potassium permanganate (3%) are incorporated, in the order specified, and aliquots are directly introduced into the graphite furnace. A fast heating programme with no conventional pyrolysis step is used. The detection limit for mercury in a 125 mg ml⁻¹ suspension is 0.1 μg g⁻¹. Calibration is performed by using aqueous standards. The reliability of the procedure is proved by analysing certified reference materials.     

高温下淀粉的凝胶化作用

凝胶化作用是淀粉及改性产品生产过程中存在的一种现象。淀粉凝胶化作用的结果导致了在其产品中产生了只溶胀但不溶解的颗粒,从而影响了淀粉产品的整体性能。文章初步探讨了淀粉在高温成型过程中凝胶化作用的方式和起因。结果表明,淀粉浆料在高温成型过程中所产生的凝胶团粒是淀粉不完整的凝胶化作用的结果,足量的水分和高温是形成较多的凝胶化淀粉颗粒的原因。     

煤的孔结构特征对水煤浆性质的影响

本文选用１７种不同变质程度的中国煤，详细研究了煤孔结构特征对煤浆性质的影响。发现煤孔体积通过影响煤在分散体系中的吸水性，从而影响煤之成浆性。但由于不同变质程度煤表面亲水性的显著差异，煤孔体积在影响煤成浆性的能力方面差别很大，这使得煤吸水性和浆体最高煤浓度与煤孔体积并不存在直接的相关性，而是取决于煤孔体积Ｖ和以煤－水接触角（θ）的余弦值表示的煤表面亲水性因子的乘积，即煤之有效孔体积：Ｖ×ｃｏｓ（θ／     

CuCrAl和CuCrZr低温液相合成甲醇催化剂的研究

 用络合共沉淀法制备了CuCrAl和CuCrZr复合氧化物液相合成甲醇催化剂，其比表面分别达到119和116m2／g．在5．0～5．5MPa和383K条件下，分别用间歇式和流动式反应釜考察了催化剂的活性和稳定性．结果表明：CuCrAl和CuCrZr的活性均明显高于CuCr；CuCrAl的活性略高于CuCrZr，但甲酸甲酯（MF）的选择性明显低于CuCrZr；两者在12h内未见活性明显下降．甲醇钠在反应过程中部分转化为甲酸钠和NaOH．CuCrAl和CuCrZr有较高的氢解活性可抑制甲醇钠与MF生成甲酸钠，从而有较低的甲酸钠浓度．但是，Al2O3和ZrO2的酸性有利于甲醇脱水，引起甲醇钠水解生成NaOH．溶剂对CuCr基催化剂的活性和选择性有明显影响．对反应机理进行了讨论．     

不同水煤浆分散剂与煤之间的相互作用规律研究Ⅹ分散剂在煤粒表面上的吸附作用特征

研究了6种水煤浆分散剂在14种不同变质程度煤上的吸附作用特征。结果表明,多数分散剂在煤粒表面达到单层饱和吸附后,又形成多层吸附,单层饱和吸附量与煤的变质程度、比表面积以及分散剂的性质有关。在相同粒度分布下,煤的变质程度越低,表面含氧亲水官能团的比例越高,孔隙率越高,比表面积越大,这对增大吸附量有利。煤的变质程度越高,其表面疏水区面积的比例越高,分散剂通过疏水基团紧密吸附在煤表面的比例越大,这对增加高阶煤的吸附量有利。对不同煤,是变质程度还是比表面积为吸附分散剂的主控因素,主要依赖于分散剂的结构与性质。对同种煤,疏水与亲水基团呈线型分立分布的分散剂,吸附量明显高;而疏水与亲水基团呈线型间隔分布的分散剂,吸附量明显小。     

DSC study and computer modelling of the melting process in ice slurry

In order to understand the non-isothermal melting kinetics in the ice slurry, a differential scanning calorimetry (DSC) was used. Experimental results were compared to those obtained by a numerical simulation in which a general enthalpy method was applied. In this work the ice slurry studied consists of ice particles uniformly dispersed within a water-antifreeze liquid mixture. The effects of the heating rate and the initial antifreeze mass fraction are discussed. It has been found that the temperature gradients inside the sample of the solution become important if either heating rate increases or initial antifreeze mass fraction decreases.     

Mathematical modeling of a slurry reactor for DME direct synthesis from syngas

In this paper,an axial dispersion mathematical model is developed to simulate a three-phase slurry bubble column reactor for direct synthesis of dimethyl ether(DME) from syngas.This large-scale reactor is modeled using mass and energy balances,catalyst sedimentation andsingle-bubble as well as two-bubbles class flow hydrodynamics.A comparison between the two hydrodynamic models through pilot plantexperimental data from the literature shows that heterogeneous two-bubbles flow model is in better agreement with the experimental data thanhomogeneous single-bubble gas flow model.Also,by investigating the heterogeneous gas flow and axial dispersion model for small bubblesas well as the large bubbles and slurry(i.e.including paraffins and the catalyst) phase,the temperature profile along the reactor is obtained.Acomparison between isothermal and non-isothermal reactors reveals no obvious performance difference between them.The optimum values ofreactor diameter and height were obtained at 7 m and 50 m,respectively.The effects of operating variables on the axial catalyst distribution,DME productivity and CO conversion are also investigated in this research.     

刮片式制冰蓄冷性能的实验研究

对刮片式动态冰浆制取系统进行实验研究,分析系统的能效比和蒸发器进出口温度、冷凝器进出口温度以及冷凝水和盐溶液流量曲线变化。研究结果表明:对制冷量为20kW的刮片式制冰装置,盐溶液有1.5℃的过冷度,随着盐溶液浓度越高其冰点越低,系统的能效系数最高达到1.9,有利于制冰蓄冷节能。     

KNO3体系中离子液体辅助水煤浆电解脱硫

在稳流条件下,考察了KNO₃体系中离子液体辅助煤浆电解脱硫效果.研究了煤浆电解过程中离子液体结构、浓度、温度和时间对脱硫率的影响.当咪唑类离子液体有机结构相同时,不同阴离子脱硫率由高到低顺序为:Br^- >BF₄^- >Cl^-;当阴离子同为Br^-时,咪唑脱硫效果优于吡啶.随着吡啶类离子液体([BPy]Br)浓度增加,脱硫率先增加,在0.3 mol/L处达到最大值,而后下降.此外,脱硫率随温度和时间增加而增大.最后,通过X射线光电子能谱(XPS)分析技术对实验前后煤中有机硫形态进行了分析.结果表明,噻吩主要通过萃取-氧化反应脱除,而其他形式有机硫(如硫醚、亚砜)则主要通过促进氧化及水解反应脱除.