沸石吸附剂脱除炼油废水中低浓度氨氮试验研究

沸石(FYH)吸附剂是抚顺石油化工研究院环保所研制开发的一种交换容量大、可再生的吸附剂,用于处理炼油废水中的氨氮时,去除率可以达到90%以上。吸附剂的穿透时间与空速有着直接关系,空速越大,穿透时间越短。吸附剂的交换容量也与空速有关。本试验中,在空速1.2h-1的条件下,吸附剂达到最大交换容量。将氯化钠和氢氧化钠以一定配比配制的再生液可以对FYH吸附剂进行快速而有效的再生。汽提含铵再生液效果很好,脱铵后的再生液中氨氮的浓度为未检出,回收的氨水浓度0.47%～0.68%。经过小试证明该工艺是可行的。     

制氢弛放气中CO2胺法捕集工艺模拟及优化

为降低PSA制氢装置弛放气中CO2捕集系统蒸汽消耗量,利用Aspen Hysys软件建立了CO2捕集工艺模型并对捕集工艺进行模拟研究。考察了胺液循环量、解吸系统贫胺液CO2负载量、富胺液进解吸塔温度和解吸压力对蒸汽消耗量的影响。模拟结果表明,随着胺液循环量和解吸系统贫胺液CO2负载量的增大,CO2解吸单耗先降低后升高,最低约为2.04t水蒸气/tCO2。提高富胺液进解吸塔温度或提高解吸压力均有利于降低CO2解吸单耗。     

碳酸丙烯酯脱除沼气中CO2工艺分析

沼气是清洁的可再生能源,但含碳量较高,不满足管输要求。通过HYSYS软件应用SRK方程对碳酸丙烯酯脱碳流程进行模拟分析,考察吸收气液比、吸收压力、气提气液比、碳酸丙烯酯贫液进料温度、预处理沼气的进料温度、吸收塔板数对脱碳效果的影响:净化气中CO2的含量随着吸收气液比的增大逐渐增大,脱碳率随之减小,但吸收气液比在10~30时,净化气中的CO2含量变化不大;随着吸收塔板数的增加,净化气中的CO2摩尔含量逐渐减小,脱碳率逐渐上升,当塔板数小于10时,脱碳效果明显,当塔板数超过10时,对脱碳效果影响较小。     

含硫污水处理负压气提技术优化

元坝气田污水脱硫主要采用"气提+化学除硫+混凝沉降+过滤"的密闭处理工艺去除地层采出水中高达1 800 mg/L的硫化物。为此,文章选用负压气提脱硫技术,并对工艺运行条件进行优化,得到脱硫效率最佳、效果最稳定的条件为:气提气源采用燃料气与空气气提对脱硫效率影响不大,脱硫最佳的进水pH值为5左右;脱硫工艺最佳气液比为6∶1～8∶1。现场实验表明,脱硫率高达96%,且效果稳定,达到了高含硫气田水经济高效处理的目的。     

高效氧化吸收液治理炼油企业恶臭的研究

采用动态配气法配置硫化氢恶臭气体,筛选出一种价廉易得、吸收氧化效果好的吸收液,考察了影响处理效果的因素:漂白粉投加量、进气浓度、进气流量、温度、吸收时间对去除效果的影响,并对实验结果进行了分析。结果表明:在室温25℃、0～5391mg/m3硫化氢浓度范围、3h吸收时间的条件下,漂白粉对硫化氢去除率在92%以上。此法能在较长时间、较大浓度范围内保持较好的去除效果,适于工业化放大。     

超声波强化酶法提取污泥蛋白研究

以城市污水处理厂剩余污泥为试验对象,对超声波预处理强化中性蛋白酶提取污泥蛋白质的效果和工艺条件进行了研究。结果表明,经超声波预处理后,污泥酶解蛋白提取率可提高40%左右,污泥脱水性能也提高了80%以上。响应面分析表明,超声强化酶解污泥提取蛋白的优化工艺条件为:p H=7.4、酶加量4 500U/g、酶解时间4h、酶解温度48℃,此时最佳蛋白提取率可达35.9%。     

利用垃圾渗滤液中的氨进行烟气脱硝研究分析

应用脱氨塔蒸汽汽提将渗滤液中的游离氨回收并用于烟气脱硝,不仅解决了渗滤液中氨氮浓度高的问题,而且为烟气脱硝提供了还原剂.文章通过分析垃圾焚烧量1000t/d、渗滤液产生量500t/d、氨氮含量约4000mg/L的垃圾焚烧发电厂运用此工艺的效果,为垃圾渗滤液处理行业提供了参考.     

炼厂“三泥”装置工艺优化探讨

文章以某炼厂“三泥”装置为研究对象,提出“三泥”装置工艺优化技术方案,通过改造活性污泥滤 液和浮渣滤液沉降分离流程,实现两股滤液分别沉降,延长沉降时间,提高了活性污泥、浮渣离心脱水率,减少了干化污泥的产生量,间接提高了污水处理质量。改造后运行效果良好,数据表明：活性污泥含水率下降18.0％～26.4％,浮渣含水率下降19.9％～26.8％;与改造前水质污染物检测浓度相比,COD去除率平均达到80.0％,悬浮物去除率平均达到95.6％。     

真菌产漆酶对蒽醌类染料脱色的研究

以香菇发酵获得漆酶粗酶液,用该酶液对蒽醌类染料进行脱色研究,分别考察了反应温度、pH值、时峰、漆酶浓度和不同染料的脱色影响.结果表明,香菇产漆酶粗酶液对蒽醌类染料具有良好的脱色效果,脱色最佳条件为：温度在30℃左右、pH3-4、反应8h、酶单位在20-30U/L的脱色率达85％.     

石油污染物生物降解试验研究

在用人工方法改变微生物所处的环境条件下进行了生物降解试验研究,以三种不同水平的碳氮比、含油量及投菌量进行了三因素、三水平正交实验。实验结果表明,在相同温度下,温度小于或等于30 ℃时,固体菌的降解效果优于液体菌;在不同温度下,30 ℃时,固体菌的降解效果最好。最终确定出石油污染物生物降解的最佳工艺条件:温度小于或等于30 ℃,接种量为10:1,碳氧比为100:10。     

低温试验系统中露点温度控制的节能技术

本文通过对低温系统露点温度控制技术的分析,指出该控制模式存在的不足,提出采用露点模式和时间程序模式相结合的露点节能控制模式对空气的干燥度和使用工况进行监控,从而实现对低湿度干燥空气的露点温度的智能监控.同时对两种控制模式耗能进行比较,指出露点节能控制模式明显优于单纯的时间程序控制模式,为低温系统露点控制提供了新的测控手段.     

生活垃圾焚烧烟气酸露点的计算方法和分析

对影响生活垃圾焚烧烟气酸露点的主要因素进行了分析,推荐了3种实用的酸露点计算方法,并采用实例验证了3种计算方法的可靠性。     

ESTIMATION OF ENERGY REQUIREMENTS OF MORNING DEW EVAPORATION FROM LEAF SURFACES1

ABSTRACT: Evapotranspiration from vegetation is generally computed without consideration for early morning energy loss involved in drying wet leaf surfaces. In humid areas where dew formation is frequent, estimation of energy requirements for evaporating dew should be of interest. In this study, sensible heat flux (H) was computed from wind and temperature profile measurements over the study site. A leaf wetness sensor was used to measure the duration of evaporation from an exposed leaf surface, and net radiation was measured with a radiometer. The energy flux during the period of wet leaf surface evaporation was integrated over time. A cattail lysimeter situated at the site indicated the time when evapotranspiration started after wet leaves were dry. The energy requirements to dry an exposed wet leaf surface was estimated using energy balance methods. The mean value based on 44 days of observations from mid February to early May of 1993 indicates that the energy required to evaporate dew from openly exposed wet leaves was 5 percent of the total daily evapotranspiration of cattails with a coefficient of variation of 0.72. The mean time required to evaporate dew from exposed leaf surfaces from the onset of positive net radiation was 78 minutes. The mean dew evaporation in a morning from an exposed leaf surface was 0.16 mm with a maximum value of 0.41 mm. The energy required to dry wet leaves is a factor that should be considered when modeling evapotranspiration at hourly or shorter time intervals. Also, physical evapotranspiration models need to account for energy requirements for drying dew and rainfall wetted leaves.     

一种经济有效的含油地下水预处理方法——吹脱法

吹脱法应用于低浓度废水处理,可有效去除水中的溶解性气体和挥发性油类,同时还可增加水中的溶解氧,为进一步的生物处理创造有利条件。利用现场动态实验对影响除油的因素进行了试验研究,确定最佳处理条件为：气水比５∶１、淋水密度５．０ｍ３／（ｍ２·ｈ）,实验表明在最佳运行状态下,吹脱法对地下水中油类物质的去除率能够达到５０％,还能去除水中的铁、氨氮等污染物质,是一种非常有效的预处理方法。为了弄清目前炼油厂废水的处理水平,通过对三个典型炼油废水处理厂的调查,分别对其处理流程、处理效果、采用的主要处理药剂及处理工艺进行了介绍,分析了每套处理设施的长处以及与先进设施对比存在的不足。     

改性活性炭脱除硫化氢工艺参数研究

针对改性活性炭脱除硫化氢过程,研究了空速、温度、原料气浓度、颗粒分布孔径4个主要工艺参数对脱硫效率的影响。结果表明:空速在1 500～4 200h-1时穿透硫容随着空速的降低而增加,当空速继续降低为1 200h-1时穿透硫容基本不变;当0～40℃时,随着温度的升高,穿透时间增加,脱硫效率提高,当温度超过40℃时,随着温度继续升高脱硫效率降低;相同空速下原料气硫化氢浓度变化只改变穿透时间;改性活性炭脱硫剂发挥脱硫作用的微孔结构范围是1～5nm。     

Effect of air supply on the performance of an active direct methanol fuel cell (DMFC) fed with neat methanol

Unlike the situation in the direct methanol fuel cell (DMFC) fed with dilute liquid methanol solution, the required water in anode for a DMFC fed with neat methanol is entirely transported from cathode. In this study, the water concentration in anode catalyst layer of such a DMFC operating with fully active mode is theoretically analyzed, followed by the experimental investigations on the effects of air flow rate and operating temperature on cell performance. The results revealed that the air flow rate has a strong impact on cell performance, especially at larger current density. Overmuch air causes rapid decline of cell performance, which results from the dehydration of membrane and lack of water in the anode reaction sites. Raising temperature induces faster reaction kinetics, while undesired stronger water dissipation from the DMFC. In practice, the stable cell resistance can be used as a criterion to help the DMFC to achieve a high and sustainable performance by finely combining the air flow rate and operating temperature.     

冷-干直接抽取法CEMS冷凝器的选型

探讨了烟气冷凝器的关键性能指标,提出烟气冷凝器脱水率、SO2组分丢失率和烟气出口露点温度等关键参数的计算公式,提出了适合不同工况条件下烟气冷凝器选型的依据和方法,为解决冷-干直接抽取法CEMS所面临的湿法脱硫后的高湿、低浓度SO2,及如何准确、客观地反映污染排放的现实问题,提供了一个合理的解决方案。     

屯绿陈茶有效成分提取及茶多酚提纯工艺研究

探讨了从陈茶中提取有效成分和茶多酚的提纯工艺。采用不同物料比、浸提温度、浸提时间的正交实验，通过热水煮提从茶叶中获取水溶性物质。结果表明，当料液比为1：20、90℃、120min时，测得的水提取物固化物量最多可达31％；茶叶水提物固化物、水配比为13：400时与乙酸乙酯萃取茶多酚的得率达23％，茶多糖从总量中提取的得率达2．5％。屯绿陈茶有效成分保留效果良好，具有较好的综合利用价值。     

Combining steam injection with hydraulic fracturing for the in situ remediation of the unsaturated zone of a fractured soil polluted by jet fuel

A steam injection pilot-scale experiment was performed on the unsaturated zone of a strongly heterogeneous fractured soil contaminated by jet fuel. Before the treatment, the soil was stimulated by creating sub-horizontal sand-filled hydraulic fractures at three depths. The steam was injected through one hydraulic fracture and gas/water/non-aqueous phase liquid (NAPL) was extracted from the remaining fractures by applying a vacuum to extraction wells. The injection strategy was designed to maximize the heat delivery over the entire cell (10 m × 10 m × 5 m). The soil temperature profile, the recovered NAPL, the extracted water, and the concentrations of volatile organic compounds (VOCs) in the gas phase were monitored during the field test. GC-MS chemical analyses of pre- and post-treatment soil samples allowed for the quantitative assessment of the remediation efficiency. The growth of the heat front followed the configuration of hydraulic fractures. The average concentration of total hydrocarbons (g/kg of soil) was reduced by ～ 43% in the upper target zone (depth = 1.5-3.9 m) and by ～ 72% over the entire zone (depth = 1.5-5.5 m). The total NAPL mass removal based on gas and liquid stream measurements and the free-NAPL product were almost 30% and 2%, respectively, of those estimated from chemical analyses of pre- and post-treatment soil samples. The dominant mechanisms of soil remediation was the vaporization of jet fuel compounds at temperatures lower than their normal boiling points (steam distillation) enhanced by the ventilation of porous matrix due to the forced convective flow of air. In addition, the significant reduction of the NAPL mass in the less-heated deeper zone may be attributed to the counter-current imbibition of condensed water from natural fractures into the porous matrix and the gravity drainage associated with seasonal fluctuations of the water table.     

迪那2气田液化气无水冷却工艺研究

迪那2气田液化气生产设计采用空冷加水冷工艺,存在能耗大和水冷器易腐蚀结垢等安全隐患。利用HYSYS软件对迪那2气田轻烃回收工艺进行分析,并增设液化气后冷器,利用脱乙烷塔气相对液化气进行冷却,通过醇烃液分离压力、后冷器及空冷器冷却能力等参数的模拟计算和优化,将醇烃液三相分离器压力由常规的2.5MPa提高至5MPa,取消醇烃液导热油加热和液化气水冷,降低了装置能耗,年节水1.44×104m3,节电1.45×105 kW.h,杜绝了水冷器腐蚀穿孔的安全隐患,最终提出了醇烃液高压分离+空冷器+后冷器的液化气无水冷却工艺。