苯酚产需现状及市场分析

2000年世界苯酚总生产能力约为740万t/a,总消费量为636万t/a,主要用于生产双酚A和酚醛树脂。预计世界苯酚需求将以每年4％-5％的速度增长。美国、西欧和日本是世界上3个最主要的苯酚生产国家和地区,北美地区的总生产能力为300万t/a,占世界总产能的40.6％,而德国酚化学公司是世界最大的苯酚生产厂家,其产能为145万t/a,占世界总产能的19.6％。2000年,我国有30家苯酚生产企业,总生产能力为28.9万t/a,总产量为24.94万t/a,主要用于酚醛树脂和水杨酸的生产。在1996-2000年间,中国大陆苯酚的净进口量分别为9.79万t、6.22万t、3.72万t、7.38万t和9.69万t,从2000年9月开始,从中国台湾的苯酚进口量增长很快。为增强市场竞争力,中国大陆苯酚生产企业应提高单套装置的生产能力,采用一体化生产模式。     

Trans FA and solid fat contents of margarines marketed in Turkey

Trans FA (TFA), solid fat contents (SFC), and slip melting points of 12 different tub and stick margarines marketed in Turkey were examined in this study. No trans isomers were found in four margarines, which suggests they were formulated from interesterified or blended fats and oils. The products with no TFA generally had more short-chain saturated FA, which suggests coconut oil-based oil components. TFA content of the other 10 products varied from 7.7 to 37.8%. Compared to the products formulated in North America, Turkish margarines contain more TFA and have higher SFC.     

高纯度盐酸游离氯的控制

介绍了高纯盐酸的生产原理、游离氯超标原因，通过工艺改进、提高操作水平及加强管理将游离氯含量控制在指标范围内。     

聚酯下脚料生产对苯二甲酸型不饱和聚酯的研究

研究了利用聚酯下脚料生产对苯二甲酸型不饱和聚酯树脂的方法。分析了原料配比及工艺参数对产品性能的影响,将对苯二甲酸型不饱和聚酯的性能与邻苯二甲酸型不饱和聚酯及间苯二甲酸型聚酯的性能进行了比较。结论认为对苯二甲酸型不饱和聚酯树脂是一种性能良好的耐腐蚀树脂。     

富锰渣制备硫酸锰过程中除杂方法新探

研究了以富锰渣为原料,经硫酸浸出制备硫酸锰的工艺过程中除杂方法。分别探讨了以MnO2、H2O2、空气为氧化剂,以NH3.H2O、Ca(OH)2、富锰渣等为中和除杂剂,控制pH在5~6,中和除杂温度为50~60℃,保温时间1~1.5 h情况下,采用不同的除杂剂及除杂条件,取得了不同的除杂效果。     

林地腐殖土腐植酸对毒死蜱水解影响及吸附作用

采用平衡振荡法研究腐植酸对毒死蜱水解的影响和毒死蜱在腐植酸上的吸附特征及其影响因素.结果表明,在试验浓度范围内腐植酸可促进毒死蜱的水解,腐植酸浓度为120 mg/L时,毒死蜱的水解速率常数k明显增大,为不加腐植酸时的2.53倍,腐植酸浓度增加毒死蜱的水解速率降低.毒死蜱在腐植酸上的吸附行为均可用Linear方程和Freundlich方程来描述,拟合效果均达到显著水平;试验条件下温度为15℃时毒死蜱在腐植酸上的吸附量最大,随温度的升高吸附量呈现出先降低后增大的趋势;pH值减小,腐植酸对毒死蜱的吸附能力增大;而离子强度对毒死蜱的吸附影响不明显;腐植酸添加量越大,吸附量越大,但单位质量的腐植酸吸附量越小.     

多羧酸系高效减水剂与水泥的相容性

研究了不同高效减水剂(多羧酸系、萘系)对普通硅酸盐水泥、中热硅酸盐水泥、矿渣硅酸盐水泥及快硬硅酸盐水泥浆体的流动度及流动度经时损失情况。结果表明,多羧酸系高效减水剂比萘系高效减水剂与水泥具有更好的相容性;多羧酸系和萘系高效减水剂与不同水泥之间的相容性规律基本相同,即与矿渣水泥相容性较好,而与普通硅酸盐水泥相容性较差;多羧酸系高效减水剂适宜的使用温度为10～30℃。     

Photocatalytic degradation rate of oxalic acid on the semiconductive layer of n-TiO2 particles in the batch mode plate reactor Part I: Mass transfer limits

Organic compounds dissolved in water can be decomposed on a layer of n-TiO2 particles irradiated by u.v. light, which generates holes and electrons in the TiO2 material. Dissolved oxygen was used as electron scavenger and holes reacted with water to give OH radicals. The rate of degradation of the dissolved organic compounds by OH radicals is limited by the transfer of either oxygen or of theorganic compounds to the surface of n-TiO2 particles. The consequence of these limits is that, in the batch mode reactor with recirculation of the liquid, the dependence of the concentration of an organic compound on time has either a linear or an exponential form. Experiments with decomposition of oxalic acid in aqueous solutions using a plate reactor (60 cm × 120 cm) confirmed the analysis. Equations for evaluation of the mass transfer coefficient of the dissolved species to the surface of the plate reactor with a moving liquid fil m were developed for the case of the thickness of the Nernst diffusion layer being thinner than the thickness of the liquid. The experimentally obtained decomposition rate of oxalic acid was about 60 to 80% of the theoretical decomposition rate limited by oxygen flux through the film of a moving liquid. The present theory neglects the diffusion of oxygen into the porous layer of n-TiO2.     

Rinsing effect of alkaline electrolyzed water on nickel surfaces

The improvement in the surface cleanliness of electroplated nickel by rinsing in alkaline electrolyzed water (AEW) was determined. When the nickel plated sample was rinsed with the AEW, it was found that the amount of residual sulfate ion on the surface of a sample decreased approximately by half compared to one rinsed only with de-ionized pure water. Because nanosize hydrogen bubbles are present in the AEW, and the zeta-potential has a negative value, we then surmised that the mechanism of rinsing was as follows: The sulfate ions are selectively absorbed on the nanosize colloidal hydrogen bubbles, or substituted for anions absorbed on the hydrogen bubbles. The sulfate ions absorbed on the nickel surface then become detached. The detached sulfate ions are absorbed on the surface of the hydrogen bubbles, and negatively charge the hydrogen bubbles. It can be considered that any detached sulfate ions do not re-adhere due to the electrical repulsion force of the negatively charged nickel surface. Thus the sample is efficiently rinsed.     

Adsorption of benzoic acid by CTAB exchanged montmorillonite

This paper reports the adsorption of benzoic acid from water on cetyl trimethylammonium exchanged montmorillonite (CTAB-montmorillonite). Important factors are the adsorbent concentration, ionic strength, equilibrium time and pH. The largest adsorption is at pH 9. The adsorption kinetics data fitted the pseudo-second-order equation. The adsorption isotherms at different pH were linear indicating a partition mechanism. Up to about 61% of the dissolved benzoic acid was adsorbed by CTAB-montmorillonite. These results indicate that CTAB-montmorillonite is a potential adsorbent for benzoic acid.