多点成形--金属板材柔性成形的新技术

多点成形是一种板材三维曲面柔性成形的新技术.简述了多点成形的基本原理与系统构成并介绍了几种成形方式.在多点成形中,厚板曲面件可直接成形,薄板曲面件则采用柔性压边技术进行成形.利用多点成形技术的柔性特点还能实现分段成形、反复成形、多道成形以及闭环成形等新的板材成形工艺.     

BT20钛合金筒形件的UOE热成形

阐述了用UOE热成形BT20钛合金筒形件的特点。通过对BT20筒形件UOE热成形的实验研究,确定了BT20钛合金筒形件UOE热成形工艺过程,得到了一系列成形工艺参数及在成形过程中控制产品质量的措施。     

工程铲车斗齿套的锻造成形工艺分析

此文对工程铲车斗齿套的锻造成形方案进行了定性分析,详细地讨论了锻造成形楔形孔薄壁件的方法,并确定了合理的成形工艺、设备选择和工艺流程。此文作者的研究和实践对解决楔形孔薄壁件的锻造成形问题具有普遍的指导意义。     

汽车门槛内板零件冲压数值模拟及参数优化

针对汽车覆盖件冲压变形复杂,成形工艺参数难以确定等特点,基于DYNAFORM软件对汽车门槛内板零件的拉延成形过程,及不同工艺参数对成形结果的影响进行了研究。用优化的工艺参数进行模拟验证,从而为工艺设计和试模提供理论指导。     

排油烟机上盖成形工艺与模具设计

此文介绍了排油烟机上盖的成形工艺、模具设计及制造特点,指出了原设计中存在的问题并提出了改进意见。经长期生产实践证明,该零件冲压成形方案可行,工艺合理、安全、可靠,能确保产品的质量。     

径向叶片等温挤压成形试验研究

本文选用超硬铝Lc9,对径向叶片的等温挤压成形工艺进行试验研究。文中给出了材料预处理和等温挤压成形的温度和速度等工艺条件;分析了径问叶片等温挤压的成形过程及该工艺对成形件强度的影响;论述了控制流动性和充填性的材料、加工及模具等主要因素。试验研究结果表明,等温挤压成形工艺对于超硬铝材料复杂形状零件的塑性成形具有实际意义。     

合金钢旋压塑流变形稳定性试验研究

中碳合金钢退火状态可旋性良好,累计变薄率为80%,未见裂纹出现。强力旋压属局部连续塑性成形工艺,很适宜大直径筒形件塑性成形。变薄旋压中碳合金钢筒形件,与卷焊成形相比,可强化组织性能,降低筒体重量,提高使用效果。试验旨在探讨中碳合金钢筒形件旋压成形的稳定性,通过变形区三向接触面积塑流试验研究,筒体变形体积与力能的分析,以及优化工艺参数和确定合理工艺过程,旋出了高精度筒形件,同时进行了批量旋压生产。     

异形件冲压成形工艺及模具设计

介绍了一异形件的冲压成形工艺,并针对该异形件的初步设计方案进行了改进,对冲压成形工序进行了合理的组合,设计并加工了生产该异形件的3套模具,对类似零件的冲压工艺分析和模具设计将会有一定的参考和借鉴价值。     

阶梯异形件拉深成形工艺研究

通过对制动室外壳成形工艺进行理论分析与实验验证,得出了阶梯异形件整体一次成形的工艺方法,并介绍了提高该类零件质量的措施。     

塑性成形的模拟材料

在塑性成形理论的研究中,需要以实验作为基础,通过实验模拟某种条件和状态,以进行塑性变形规律的研究。而在塑性成形工艺的研究中,模拟实验应用得更多,这是因为某些塑性加工的条件相当严酷,例如高温、高压,重载,有的塑性成形件达到数百吨重,加工周期长,耗资大,难以在实物上进行加工工艺和变形规律的研究。无疑,模拟实验研究是十分重要的。     

论炼油厂液氨质量及出路

炼油厂生产液氨，作为综合利用产品给社会带来益处，但液氨质量不好无法出厂，放火矩烧不仅浪费资源，同时造成大气污染。为解决炼油厂液氨出路，首先通过技术攻关解决液氨质量问题，并试用气氨作为燃料获得成功，达到既可生产液氨，又可作为锅炉燃料，彻底解决了炼油厂液氨出路。     

利用废渣废碱液年产3000t粒状五水偏硅酸钠工艺初步设计

介绍以铝矾土提取硫酸铝废渣和氧氯化锆副产废碱液为原料生产泡花碱 ,然后利用一次造粒法生产五水偏硅酸钠新工艺确定影响产品质量指标工艺因素。小试试验产品质量指标达到HG/T2 5 6 8- 94要求 ,工艺成本低 ,避免废碱液及废渣排放对环境的污染。     

基于DHGF算法的水资源定价模型研究

通过将DHGF算法与水资源价格上限理论相结合,构建了基于DHGF算法的水资源定价模型,并对模型工作步骤进行了设计。最后以西安市水资源为例,对该模型进行实例检验。结果表明该模型具有可行性和实际应用价值。     

基于能值分析理论的生态足迹模型及应用——以江苏省为例

在对传统生态足迹模型进行简要分析的基础上,提出基于能值分析理论的生态足迹计算模型。该改进生态足迹模型通过将生态经济系统中的各种能量流换算成对应的生物生产性土地面积,并比较计算得到的生态足迹和生态承载力,从而衡量研究区域的环境可持续发展状况。论文以江苏省为例,应用改进生态足迹模型分析其2003年生态经济系统的环境状况,得到人均生态承载力为0.2997hm₂/人,人均生态足迹为4.7228hm₂/人,生态足迹超过生态承载力,与传统生态足迹模型的计算结果相一致。但与传统生态足迹模型相比,改进生态足迹模型的计算结果能更真实地反映生态经济系统的环境状况。     

用外加热回转窑生产高纯活性氧化镁回收二氧化碳新工艺

针对当前镁制品生产过程中存在的严重资源浪费和环境污染严重的问题，提出以废弃菱镁矿渣为原料，利用新型外加热回转窑生产高纯氧化镁，并从生产废气中回收食品级液态二氧化碳的新工艺。     

Photocatalytic degradation of bisphenol A using an integrated system of a new gas-liquid-solid circulating fluidized bed reactor and micrometer Gd-doped TiO2 particles

A new gas-liquid-solid circulating fluidized bed photocatalytic reactor (GLSCFBPR) with internally placed multi-layered UV lamps was developed. Micrometer Gd-TiO₂ particles and commercial nanometer P25-TiO₂ were chosen as the photocatalysts, and the hazardous substance bisphenol A (BPA) was chosen as the model pollutant to investigate the performance of this new photocatalytic system. The results showed that the photocatalytic degradation efficiency of the micrometer Gd-TiO₂ particles was similar to that of the nanometer P-25 particles at their respective optimum dosage but the former could be easily separated out by gravity. After investigating the effects of process parameters on the photocatalytic BPA degradation, the response surface method (RSM) was further used for process optimization. The interactions among process parameters, i.e., TiO₂ concentration, superficial gas velocity and superficial liquid velocity were discovered and a related analysis was carried out to explore the underlying mechanism. A quadratic mathematic model was established and performed satisfactorily when used for prediction. The optimum conditions for this new process were as follows: TiO₂ concentration 4.5 g/L, superficial gas velocity 7.83 × 10^-3 m/sec and superficial liquid velocity 8.65 × 10^-3 m/sec.     

Nitrogen and phosphorus removal in an airlift intermittent circulation membrane bioreactor

A new airlift intermittent circulation integrated bioreactor was developed for simultaneous nitrogen and phosphorus removal of wastewater, in which, circulation of mixed liquid between mixing zone and aeration zone was realized by aeration power, alternately anaerobic/anoxic bio-environment in mixing zone was realized by intermittent circulation and simultaneous nitrogen and phosphorus removal was obtained through strengthened denitrifying phosphorus removal process. Removal performance of the reactor was investigated and pollutant removal and transfer mechanism in one operation circle was analyzed. The experiment results indicated that under the influent condition of chemical oxygen demand (COD) concentration of 642.1 mg/L, total nitrogen (TN) of 87.4 mg/L and PO₄^3?-P of 12.1 mg/L, average removal efficiencies of COD, TN and PO₄^3?-P reached 96.4%, 83.2% and 90.5%, respectively, with the hydraulic residence time of 22 hr and operation circle time of 185 min. Track studies indicated that the separation of aeration and mixing zones and intermittent circulation of mixed liquid between the two zones provided distinct biological environments spatially and temporally, which ensured the occurrence of multifunctional microbial reactions.     

Nitrogen and phosphorus removal in an airlift intermittent circulation membrane bioreactor

A new airlift intermittent circulation integrated bioreactor was developed for simultaneous nitrogen and phosphorus removal of wastewater, in which, circulation of mixed liquid between mixing zone and aeration zone was realized by aeration power, alternately anaerobic/anoxic bio-environment in mixing zone was realized by intermittent circulation and simultaneous nitrogen and phosphorus removal was obtained through strengthened denitrifying phosphorus removal process. Removal performance of the reactor was investigated and pollutant removal and transfer mechanism in one operation circle was analyzed. The experiment results indicated that under the influent condition of chemical oxygen demand (COD) concentration of 642.1 mg/L, total nitrogen (TN) of 87.4 mg/L and PO₄^3--P of 12.1 mg/L, average removal efficiencies of COD, TN and PO₄^3--P reached 96.4%, 83.2% and 90.5%, respectively, with the hydraulic residence time of 22 hr and operation circle time of 185 min. Track studies indicated that the separation of aeration and mixing zones and intermittent circulation of mixed liquid between the two zones provided distinct biological environments spatially and temporally, which ensured the occurrence of multifunctional microbial reactions.     

赣江流域生态足迹计算与分析

应用生态足迹理论及模型,根据赣江流域2007年出版的统计数据,对赣江流域2006年的生态足迹和生态承载力进行了定量计算,结果表明:2006年赣江流域的人圴生态足迹为0.9327hm2/cap,而当年实际上可以提供的人均生态承载力为0.9474hm2/cap,人均生态盈余为0.0147hm2/cap,生态需求与生态供给之比为1:1.02,表明人们对赣江流域生态经济系统的影响还未超出其生态承载力的阈值,赣江流域生态系统是安全的,流域发展表现为可持续状态;该流域中赣州、吉安2地市出现生态盈余,分别是0.3488hm2/cap,0.2108hm2/cap;而南昌、九江、宜春3地市出现生态赤字,分别是0.2397hm2/cap,0.1328hm2/cap,0.1696hm2/cap,其中南昌市生态赤字最大。     

气浮过程中的界面相互作用

首先讨论了水体颗粒物的基本性质以及气泡的形成过程，而后对气液界面上胶体颗粒的吸附进行分析。其次讨论了气浮过程中，气泡与颗粒物之间的相互作用。对气泡与颗粒物之间的碰撞进行分析。结合紊流气浮的理论与应用，在气浮过程中的界面相互作用分析的基础上。设计了一种新型集成的溶气气浮水处理工艺，即逆流共聚气浮工艺，并对其运行情况进行了研究。探讨了其中的界面相互作用对气浮效果的影响，进一步与传统工艺进行了对比。