催化裂化烟气转硫脱氮和助燃三功能催化剂FP-DSN的工业应用

烟气转硫、脱氮和助燃三功能新型催化剂FP DSN在中国石油天然气股份有限公司锦西石化分公司 1.4Mt/a重油催化裂化装置的工业应用表明 ,此种以La ,Ce ,Sr和Co等元素的氧化物或复合物为活性组分的催化剂 ,在其用量为催化裂化催化剂总藏量的 1%～ 2 %的情况下 ,有较强的脱除烟气中SOx 和NOx 的能力 ,大大减轻了烟气对反应器壁的腐蚀 ,减少了污染气体的排放 ,同时有CO助燃效果 ,装置可不使用其他专门的助燃剂。应用试验时 ,再生器烟气中SOx 的平均脱除率达 72 .85 %,NOx 的平均脱除率达 85 .90 %。该催化剂的使用对催化裂化产品的分布和质量无明显影响。该剂的应用为装置带来了可观的经济效益。     

修正步冷温度曲线试验研究

按修正步冷温度曲线对经步冷脆化的 2 .2 5Cr 1Mo和在加氢反应器内运行 5a的 2 2 5Cr 1Mo试块进行了修正步冷试验 ,评定了材料的回火脆性。结果表明 ,按修正步冷曲线进行修正步冷试验能使已经脆化的材料进一步脆化 ,为加氢反应器材料损伤的研究提供了一条途径。     

采用轴径向技术有效解决固定床反应器阻力降的快速升高

讨论了固定床反应器阻力降快速升高的原因，介绍了用轴径向技术解决这一问题的原理及优点，及其在铁铬系变换催化剂和钴钼系耐硫变换催化剂反应器中的实际应用。     

西安脉冲堆计算值和实测结果分析

介绍了西安脉冲堆堆芯布置、计算模型和程序以及计算值与实验测量结果分析。西安脉冲堆在满功率（2MW）下连续运行了72小时，证明西安脉冲堆整个系统和设备是良好的、安全可靠的。根据西安脉冲堆计算值与测量值的比较，证明计算程序可靠，具有较高精度。西安脉冲堆理论计算值与实验测量值符合较好，完全满足工程设计要求，实验测量结果达到了设计指标的要求。     

Design and characterisation of a close-concentric annular reactor for kinetic studies at high temperatures

A novel annular reactor for kinetic studies at high temperature and flow conditions has been designed to keep eccentricity tolerances below 10%. In a previous work, we have shown that it is very important to keep such low eccentricity values in order to collect reliable kinetic data from this type of reactors. As proposed in this study, a modified reactor with the use of a spacer could guarantee an annular duct with low levels of eccentricity. Manufacturing tolerances or deformation effects giving rise to eccentricity can be significantly minimised when using this apparatus. The reactor has been both experimentally and theoretically characterised. Carbon monoxide oxidation was used as a model reaction under mass-transfer limited conditions revealing an eccentricity of ∼5%. With such small eccentricity levels, a concentric annular form can be assumed in the reactor analysis. Simple 1D or 2D models can therefore be inexpensively used in the evaluation of the kinetic data. Also, prior to the design of the annular reactor, a numerical investigation was carried out to clarify the effects of eccentricity, physical properties of the carrier gas and the annular aspect ratio on mass-transfer limitations. Contrary to expectations, a considerable increase in the fuel mass-diffusivity by carrier gas substitution did not change the mass-transfer rates for cases when eccentricity and aspect ratios were high.     

新型可控电抗器大幅度限制操作过电压功能的研究

通过数值计算和模拟研究,本文叙述了新型可控电抗器的广泛的无功调节功能,揭示了它所具有的大幅度限压的能力,并在理想数学模型的基础上分析了电抗器的限压机理。     

含腐蚀凹坑尿素合成塔的安全评定与分析

对尿素合成塔上封头腐蚀凹坑采用中国SAPV-95和美国API579规范分别进行安全评定，给出安全裕度，简略分析安全评定的结果。     

Reactor modelling for electrochemical processes

This paper presents a relatively straightforward approach to the modelling of electrochemical reactors operated in batch or continuous modes. The models are based on ideal flow assumptions of either well-mixed or plug flow and incorporate reaction rate models based on electrochemical kinetics and mass transport at one electrode. General characteristics of the reactor models are described, particularly with regard to the need for good mass transport in metal recovery applications. An example is given on the use of the model in the recovery of a heavy metal (Cd²⁺) from an acidified solution containing Cd(II) and Fe(III) ions. The reaction rate model is based on experimental data.     

Effect of H2O2 addition mode on enzymatic removal of phenol from wastewater in the presence of polyethylene glycol

The effect of batch and semi-batch additions of the stoichiometric amount of H₂O₂ on enzymatic removal of phenol has been studied over the phenol concentration range of 1-10 mmol/L. It is found that the ratio between the maximum H₂O₂ concentration during the reaction and the initial horseradish peroxidase concentration ((H₂O₂)_max/(HRP)_o) controls the rate of phenol removal by horseradish peroxidase in the presence of the additive, polyethylene glycol. An optimum range of this ratio is determined to be between 10 and 25 μmol/U. Empirical models are proposed to predict the values of (H₂O₂)_max/(HRP)_o required to treat given phenol concentrations under different modes for adding H₂O₂.     

乳液聚合螺旋半园管夹套反应釜

本文将螺旋半园管夹套反应釜与传统的夹套反应釜进行了对比 ,并介绍了螺旋半园管夹套釜在乳液聚合中的应用