CFB锅炉环保项目SNCR工艺优化提效研究

某炼化企业自备电厂循环流化床锅炉(简称CFB锅炉)环保项目所采用的脱硝方法为选择性非催化还原脱硝(简称SNCR),使用的还原剂为尿素,SNCR系统投用后,虽然能使NOX排放量显著下降,但尿素用量明显过度,增加了企业脱硝成本,并导致脱硫废水氨氮含量超标。为了应对这一情况,本研究主要通过现场调节锅炉运行参数,以及基于CFD建模的方法研究出高效可靠的SNCR工艺优化调整策略及方法,结果表明:在锅炉燃料煤∶焦=4∶1掺烧比例下,氧含量不宜超过3%,有利于降低NOX生成量;控制减少石灰石量有助于提升NOX的脱除效率;通过模拟计算发现下半部喷枪起到主要的脱硝作用,可适当减少上半部喷枪、提升环下半部喷枪的尿素喷入量来提高脱硝效率。为煤焦混烧CFB锅炉脱硝系统的优化提供指导和借鉴作用。     

冲裁模压力中心的简化求法

针对某些形状复杂的冲裁件，介绍了一种压力中心的简化求法。     

黑龙江省中部漫川漫岗区坡耕地的治理──垄作区田水土保持措施的应用

本文对黑龙江省中部漫川漫岗侵蚀区坡耕地利用现状和采取的水土保持耕作措施进行了总结分析，提出了在黑龙江省坡耕地治理中应用垄作区田技术标准和发展方向。     

不同含碳量天然气脱碳方案选择

分析国内外常用脱碳方法和各油气田不同含碳量天然气脱碳实例,比较各种脱碳方案的操作条件、适用范围以及优缺点,给出不同含碳量天然气的脱碳方案:当含碳量为2%～10%时可选用常规醇胺法、热碳酸钾法、物理-化学吸收法、变压吸附法;当含碳量为10%～30%时可选用活化MDEA法、热碳酸钾法、物理吸收法、物理-化学吸收法;当含碳量为30%～70%时可选用改良热碳酸钾法、物理吸收法、物理-化学吸收法、膜分离法+常规醇胺法、膜分离法+热碳酸钾法;当含碳量大于70%时可选用低温分离法、膜分离法+化学吸收法。     

Photodegradation of bisphenol A in simulated lake water containing algae, humic acid and ferric ions

The photodegradation of bisphenol A (BPA), a suspected endocrine disruptor (ED), in simulated lake water containing algae, humic acid and Fe3+ ions was investigated. Algae, humic acid and Fe3+ ions enhanced the photodegradation of BPA. Photodegradation efficiency of BPA was 36% after 4h irradiation in the presence of 6.5 x 10(9) cells L(-1) raw Chlorella vulgaris, 4 mg L(-1) humic acid and 20 micromol L(-1) Fe3+. The photodegradation efficiency of BPA was higher in the presence of algae treated with ultrasonic than that without ultrasonic. The photodegradation efficiency of BPA in the water only containing algae treated with ultrasonic was 37% after 4h irradiation. The algae treated with heating can also enhance the photodegradation of BPA. This work helps environmental scientists to understand the photochemical behavior of BPA in lake water.     

Quantitation of Hydroxyl Radicals from Photolysis of Fe(III)-Citrate Complexes in Aerobic Water (5 pp)

Background For their high photoreactivity, Fe(III)-carboxylate complexes are important sources of H2O2 for some atmospheric and surface waters. Citrate is one kind of carboxylate, which can form complexes with Fe(III). In our previous study, we have applied Fe(III)-citrate complexes to degrade and decolorize dyes in aqueous solutions both under UV light and sunlight. Results have shown that carboxylic acids can promote the photodegradation efficiency. It is indicated that the photolysis of Fe(III)-citrate complexes may cause the formation of some reactive species (e. g. H2O2 and ·OH). This work is attempted to quantify hydroxyl radicals generated in the aqueous solution containing Fe(III)-citrate complexes and to interpret the photoreactivity of Fe(III)-citrate complexes for degrading organic compounds. Methods By using benzene as the scavenger to produce phenol, the photogeneration of ·OH in the aqueous solution containing Fe (III)-citrate complexes was determined by HPLC. Results and Discussion In the aqueous solution containing 60.0/30.0 mM Fe(III)/citrate and 7.0 mM benzene at pH 3.0, 96.66 mM ·OH was produced after irradiation by a 250W metal halide light (l ≥ 313 nm) for 160 minutes. Effects of initial pH value and concentrations of Fe(III) and citrate on ·OH radical generation were all examined. The results show that the greatest photoproduction of ·OH in the aqueous solution (pH ranged from 3.0 to 7.0) was at pH 3.0. The photoproduction of ·OH increased with increasing Fe(III) or citrate concentrations. Conclusion In the aqueous solutions containing Fe(III)-citrate complexes, ·OH radicals were produced after irradiation by a 250W metal halide light. It can be concluded that Fe(III)-citrate complexes are important sources of ·OH radicals for some atmospheric and surface waters. Recommendations and Outlook It is believed that the photolysis of Fe(III)-citrate complexes in the presence of oxygen play an important role in producing ·OH both in atmospheric waters and surface water where high concentrations of ferric ions and citrate ions exist. The photoproduction of ·OH has a high oxidizing potential for the degradation of a wide variety of natural and anthropogenic organic and inorganic substances. We can use this method for toxic organic pollutants such as organic dyes and pesticides.     

我为故乡的大开发站岗

“手握一杆钢枪,身披万道霞光,我守卫在边防线上,为我们伟大祖国站岗……”我时常唱起这首激情昂扬的哨兵之歌。我是一名地震工作者,20多年如一日,常年值班在地震台站的机房,是保卫祖国建设和人民生命财产安全的防震减灾方队中的普通一兵。     

自贡地震监测设施屡遭破坏

地处四川东南部的自贡市是一个拥有近300万人口的中等工业城市,所处的地理位置又是一个中强震多发地区,无论历史上,还是今天,也无论是自贡的周边地区,还是城市的脚下,都遭受过一些中强地震的袭击。为了监测预防地震,搞好防震减灾工作,省市政府在经济并不宽裕的情况下,投人大量资金,建设了一些地震监测设施和自贡无线遥测地震台网。     

聚丙烯酰胺对聚合物驱含油污水中油珠沉降分离的影响

研究发现阴离子聚丙烯酰胺(HPAM)对聚合物驱含油污水处理有正反2方面影响.聚合物能增加污水粘度,降低油珠上浮速度,而且聚合物能增加油水界面水膜强度,延缓油珠聚并时间,这是聚合物对油珠沉降分离的不利影响;同时,聚丙烯酰胺具有絮凝性,能将水中油珠连接到一起,有利于油珠聚并.当聚丙烯酰胺相对分子质量为2.72×10⁶,浓度小于800mg/L时,絮凝作用大于粘度作用,有利于油珠的沉降分离.初始油珠粒径小是聚合物驱含油污水难处理的主要原因.横向流除油器可以加速油珠聚并,缩短沉降时间,适合处理聚合物驱含油污水.     

Recovery of Ni(II) from real electroplating wastewater using fixed-bed resin adsorption and subsequent electrodeposition

Resin adsorption and subsequent electrodeposition were used for nickel recovery. Treated wastewater can meet the Electroplating Pollutant Discharge Standard. The spent resin is completely regenerated by 3 BV of 4% HCl solution. 95.6% of nickel in concentrated eluent was recovered by electrodeposition. Effective recovery of high-value heavy metals from electroplating wastewater is of great significance, but recovering nickel ions from real electroplating wastewater as nickel sheet has not been reported. In this study, the pilot-scale fixed-bed resin adsorption was conducted to recover Ni(II) ions from real nickel plating wastewater, and then the concentrated Ni(II) ions in the regenerated solution were reduced to nickel sheet via electrodeposition. A commercial cation-exchange resin was selected and the optimal resin adsorption and regeneration conditions were investigated. The resin exhibited an adsorption capacity of 63 mg/g for Ni(II) ions, and the average amount of treated water was 84.6 bed volumes (BV) in the pilot-scale experiments. After the adsorption by two ion-exchange resin columns in series and one chelating resin column, the concentrations of Ni(II) in the treated wastewater were below 0.1 mg/L. After the regeneration of the spent resin using 3 BV of 4% (w/w) HCl solution, 1.5 BV of concentrated neutral nickel solution (>30 g/L) was obtained and used in the subsequent electrodeposition process. Using the aeration method, alkali and water required in resin activation process were greatly reduced to 2 BV and 3 BV, respectively. Under the optimal electrodeposition conditions, 95.6% of Ni(II) in desorption eluent could be recovered as the elemental nickel on the cathode. The total treatment cost for the resin adsorption and regeneration as well as the electrodeposition was calculated.