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《Process Safety and Environmental Protection》2014,92(6):532-544
This paper presents a generic mathematical model for retrofitting the steam power plants in an industrial site. The industrial sector under review consists of one steel mill, one oil refinery, and several petrochemical plants, where only small-scale steam integration has been implemented before this study. The relevant unit models in a typical steam power plant are established, and the steam plant retrofit problem is formulated as a mixed-integer nonlinear program (MINLP). Feasible retrofit alternatives suggested by experienced field engineers are investigated in sequence to examine the revenue of those possible modifications. The first scenario examines operational optimization of existent plants; the second option allows installation of one new turbine and replacement of several boilers and turbines with lower efficiency; the third scenario considers using a steam ejector to upgrade the disqualified import steam in the oil refinery. The significant merits from these three retrofit alternatives show that the proposed MINLP formulation has been a great help to enhance the inter-plant steam integration in an industrial sector. 相似文献
3.
After a short update of the current more accepted definition of BLEVE, the special features of water BLEVEs are analyzed. The stronger overpressure wave generated in the case of water as compared to that of other substances is justified in terms of volume change. Through a comparison with liquefied pressurized propane, three possibilities are analyzed: the simultaneous contribution of both the liquid and the preexisting vapor, the contribution of the liquid flash vaporization, and the contribution of the pre-existing vapor. Also a historical survey on a set of 202 BLEVE accidents –the largest sample of BLEVE accidents surveyed until now– is presented. LPG was the most common substances in this set of accidents. However, water and LNG (11% of water and 4% of LNG in the studied cases) have also been involved. Impact failure (44.8%) and human factor (30.3%) were the most common causes of BLEVEs. Transport, storage, process plants, and transfer were the activities in which more accidents occurred. 相似文献
4.
采用蒸发法处理城市生活垃圾焚烧厂垃圾沥滤液,着重考察了不同沥滤液初始pH值对蒸发去除COD和氨氮效果的影响,并采用GC-MS对蒸发冷凝液中有机物成分进行了分析鉴定.结果表明,生活垃圾沥滤液的初始pH对冷凝液中COD、氨氮含量及有机污染物分布产生了决定性的影响.沥滤液在酸性条件下(pH≤6)蒸发,随着pH的增加,冷凝液中COD的含量线性降低,而氨氮的含量线性增加.当沥滤液的初始pH值从6增加到11,冷凝液中COD的含量呈对数函数降低,而氨氮的含量表现出显著增加趋势.从冷凝液中鉴定出38种有机污染物,多为沸点较低的醇、酸、酚和酯类.在酸性条件下(pH=3),冷凝液中挥发性有机酸和低碳醇的相对丰度接近90%.在近中性条件下(pH=6.2),冷凝液中的有机污染物以酚、酸和杂环类化合物为主.在碱性条件下(pH =11),冷凝液中酚和杂环类化合物占比较高,而酸的含量极少. 相似文献
5.
In this communication, a new design of solar-energy-based water distillation cum drying unit with parabolic reflector has been designed, fabricated, and tested. Bitter gourd and potato slices are chosen as a drying commodity. Thermal performance of the developed system has been evaluated based on the experimental results and using linear regression analysis. Heat transfer coefficients (convective, evaporative, and radiative) for solar distillation system have been observed to be 2.48–4.09, 13.25–52.38, and 8.75–9.66 W/m2°C, respectively. Overall thermal efficiency and exergy efficiency for the distillation system has been found to be 18.77% and 1.2%, respectively. The convective heat transfer coefficient for potato slices are observed higher for initial hours and decreases as the day progresses. The average convective heat transfer coefficients for bitter gourd and potato slices have been observed as 2.18 and 5.04 W/m2°C, respectively. Experimental error in terms of percent uncertainty for bitter gourd and potato slices are found to be 42.93% and 37.06%, respectively. The present design of solar distillation and drying in a single unit could be beneficial for the development of remote, arid, and rural areas. 相似文献
6.
Continuous flow transesterification of waste frying oil (WFO) with methanol for the biodiesel production was tested in a laboratory scale jacketed reactive distillation (RD) unit packed with clam shell based CaO as solid catalyst. The physiochemical properties of the clam shell catalysts were characterized by X-ray Diffraction (XRD), Brunauer–Emmett–Teller (BET), Scanning Electron Microscopy (SEM), and Energy Dispersive Atomic X-ray Spectrometry (EDAX). The effects of the reactant flow rate, methanol-to-oil ratio, and catalyst bed height were studied to obtain the maximum methyl ester conversion. Reboiler temperature of 65°C was maintained throughout the process for product purification and the system reached the steady state at 7 hr. The experimental results revealed that the jacketed RD system packed with clam shell based CaO showed high catalytic activity for continuous production of biodiesel and a maximum methyl ester conversion of 94.41% was obtained at a reactant flow rate of 0.2 mL/min, methanol/oil ratio of 6:1, and catalyst bed height of 180 mm. 相似文献
7.
物化-生物组合工艺处理TNT红水 总被引:1,自引:0,他引:1
采用酸析+微电解+混凝沉淀+减压蒸馏+固定化微生物滤池+活性焦吸附组合工艺处理兵器八○五厂(襄樊分部)的TNT红水,出水中的硝基化合物浓度多小于0.8 mg/L,且多次未检出;COD最高值为76 mg/L,平均值为51.6 mg/L;色度为20°;苯胺浓度全部小于1 mg/L,达到了中试方案提出的要求,出水水质指标符合《兵器工业水污染物排放标准火炸药》(GB14470.1-2002)的要求.中试期间设备没有发生堵塞、燃烧等事故,减压蒸馏装置正常稳定运行,证实了减压蒸馏法处理TNT红水的安全可靠性. 相似文献
8.
采用新型膜蒸馏技术对水中As(III)与As(Ⅴ)的去除展开了研究。实验结果表明,膜蒸馏对水中As (III)及As (Ⅴ)具有较高的去除能力:当产水中砷含量超过10 μg/L时,原水中As (III)与As (Ⅴ)的浓度可分别高达40 mg/L和2 000 mg/L。局部润湿现象的存在导致As (III)及As (Ⅴ)跨膜至产水侧,PVDF微孔膜在溶液中的负电性以及As (III)与 As (Ⅴ)在溶液中存在形式的不同导致膜蒸馏对两者去除能力的差异。360 h连续运行过程中产水通量及电导率稳定,且整个过程中As (III)均低于检测限,说明PVDF微孔膜具有良好的疏水性和稳定的除砷性能。 相似文献
9.
气提-厌氧-接触氧化-气浮工艺处理聚酯废水 总被引:1,自引:0,他引:1
介绍了气提-厌氧-接触氧化-气浮处理工艺在聚酯废水工程中的实际应用,分析并总结了工程设计及运行的经验。实践表明,运用气提塔先对高浓度聚酯废水进行预处理,可以去除废水中对生化有毒性的醛类物质,保证后续生化处理的稳定运行。经气提-厌氧-接触氧化-气浮处理工艺处理后,废水中COD总的去除效率可达到98.7%以上,能够实现稳定达标排放。并可实现部分回用至生产过程。该工艺具有运行稳定和处理效率高等优点,为企业带来了良好的经济效益和社会效益。 相似文献
10.
Motoyuki Sugano Akihiro Komatsu Masanori Yamamoto Mika Kumagai Takayuki Shimizu Katsumi Hirano Kiyoshi Mashimo 《Journal of Material Cycles and Waste Management》2009,11(1):27-31
Most landfilled plastic waste is a mixture or is in the form of composites with incombustible wastes such as glass, metals,
and ceramics. After hydrothermal treatment, including a steam-explosion process, the separation of mixed waste (MW) into organic
and inorganic substances becomes easy. However, the effect of hydrothermal pretreatment on the subsequent liquefaction of
organic substances from MW is not obvious. In this study, the effects on the liquefaction of polystyrene and high-density
polyethylene are discussed. Moreover, optimum conditions for the liquefaction of organic substances from hydrothermally treated
MW are identified. By means of this hydrothermal pretreatment, including the steam-explosion process, polystyrene and high-density
polyethylene can be significantly converted to oil by liquefaction at 300°–400°C. In comparison with liquefaction of hydrothermally
pretreated mixed waste (HMW) at 300°–400°C with a batch type reactor, the yield of oil increases significantly on liquefaction
using a semi-batch type reactor. It is considered that the radical chain and termination reactions among the radicals from
HMW were inhibited in the semi-batch type reactor. On liquefaction of HMW in a semi-batch reactor, the conversion of HMW to
oil was enhanced on increasing the liquefaction temperature to 350°C and the holding time to 60 min.
Chemical Feedstock Recycling & Other Innovative Recycling Techniques 6 相似文献