226 resultados para 203-1243B


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In this paper, as an extension of minimum unsatisfied linear relations problem (MIN ULR), the minimum unsatisfied relations (MIN UR) problem is investigated. A triangle evolution algorithm with archiving and niche techniques is proposed for MIN UR problem. Different with algorithms in literature, it solves MIN problem directly, rather than transforming it into many sub-problems. The proposed algorithm is also applicable for the special case of MIN UR, in which it involves some mandatory relations. Numerical results show that the algorithm is effective for MIN UR problem and it outperforms Sadegh's algorithm in sense of the resulted minimum inconsistency number, even though the test problems are linear.

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针对钙质砂地基中桶形基础动态响应问题进行了实验研究.首先进行了水平静极限承载力实验,获得了水平载荷位移曲线,并为确定水平动载荷幅值的选择提供参考;然后针对主要因素,包括桶形基础尺寸、载荷幅值和频率、土体密度、压重等,进行了系列的室内小模型实验,并对结果进行了分析,获得了水平动载下桶形基础在钙质砂地基中的响应特点.结果表明:载荷幅值、频率、土体密度、桶形基础尺寸对动态响应有明显影响;动载下桶形基础周围钙质砂中孔压上升,但是较其他类砂土中的慢;在结构重量小时,桶形基础上升;有上覆较硬粘土层时,桶形基础和地基的响应减弱.

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制革行业是轻工行业中仅次于造纸业的高耗水、重污染行业,作为劳动密集型行业,在解决大量人口就业问题的同时,也对所在地区环境造成了严重污染。目前我国制革行业每年排放废水8,000~12,000万吨,废水中含铬约3,500 t,SS为1.2×105 t,COD为1.8×105 t,BOD为7×104 t,对水体污染严重。 本研究在对厌氧酸化工艺进行研究、一级好氧处理段进行工艺比选研究的基础上,获得了匀质调节—SBBR—BAF的生物处理工艺,并依托该工艺进行了生物强化处理的研究,考察了菌剂的强化运行效果及其处理水回用的可行性。 研究表明,在进水COD>3,000 mg/L,厌氧酸化具有很好的抗冲击作用,保证了好氧工艺出水COD<200 mg/L;在进水COD<3,000 mg/L,可只通过好氧处理实现出水COD<200 mg/L。厌氧酸化停留时间选择不当,会导致厌氧出水硫化物浓度升高,严重影响好氧系统,会使好氧活性污泥因中毒而解絮。 研究表明,当进水COD为2,000~2,500 mg/L,NH4+-N为130~146 mg/L时,COD、NH4+-N去除率SBBR分别为93.8%~96.6%和14.5%~55.9%,SBR分别为88.8%~94.9%和13%~50.7%,表明SBBR优于SBR。同时,研究发现SBBR污泥增长率为0.05 kgVSS/kgCOD,仅为SBR0.57 kgVSS/kgCOD的8.8%。此外,研究发现SBBR在停止运行后经3个运行周期可回复原油能力,而SBR池经9个周期培养也不能恢复,说明SBBR恢复能力明显优于SBR。 研究表明,以匀质调节—SBBR—BAF为主的制革废水处理工艺,出水水质稳定,进水COD 801~2,834 mg/L、NH4+-N 87~203 mg/L,出水COD<80 mg/L、NH4+-N<10 mg/L,基本达到中水回用标准;操作简单灵活,没有污泥回流系统,污泥产率低,污泥处理费用低;工艺基本不需要添加化学药剂,既节约成本、又避免了二次污染;两级生物膜使得该工艺具有很强的耐冲击负荷能力,特别适合制革废水水质水量波动大的特点。 研究表明,高效菌对系统的启动具有一定的促进作用,强化系统生物膜6天可以成熟,对照系统生物膜9天可以成熟。同时高效菌能加速COD降解,缩短停留时间,强化系统6~8 h可使COD<200 mg/L,对照系统8~10 h可使COD<200 mg/L。长期运行表明,强化系统的SBBR在COD和NH4+-N的去除率都优于对照系统的SBBR。最终出水COD强化系统平均为53 mg/L、对照系统为74 mg/L。在模拟循环过程中,强化系统均有更高的稳定性。可实现8次理论循环,而对照系统只能实现4次理论循环。 研究表明,通过合理的工艺设计,可以实现猪皮制革废水达到《污水综合排放标准GB8976-1996》一级标准,同时满足工厂部分用水要求。通过添加高效微生物,可提高生物处理系统处理能力,使处理水能够满足工厂的多次回用。 As a labour-intensive industry, tanning has created large amount of working opportunities as well as caused severe contamination to environment. And it is one of the highest water-consuming and polluting industry, only second to manufacturing. At present time, Chinese leather industry emits wastewater about 80,000,000~120,000,000 t annually, which contains chromium about 3,500 t, SS 1.2×105 t, COD 1.8×105 t, BOD 7×104 t and ambient riverhead has been polluted greatly. Based on the research of anaerobic acidification and comparison of SBBR and SBR, biotreatment process (Homogenization—SBBR—BAF) had been established to amend the disadvantages of traditional sewage treatment such as too much sludge, high cost of advanced treatment and NH4+-N can not reach the emission standard. Research on the bioaugmentation was also been carried out. Researches showed, when COD of influent was beyond 3,000 mg/L, anaerobic acidification could resist strong impact, thus COD of effluent was less than 200 mg/L; when COD of influent was less than 3,000 mg/L, only throughout aerobic sewage treatment could COD of effluent beless than 200 mg/L. False residence tiome of anaerobic acidification would lead to the higher effluent concentration of sulfide and disintegration of aerobic activated sludge. Researches showed SBBR worked a better than SBR: when influent between 2,000 and 2,500 mg/L, NH4+-N between 130 mg/L and 146 mg/L, COD, NH4+-N removal rate of SBBR was 93.3%~96.6%, 14.5%~55.9% respectively while COD, NH4+-N removal rate of SBR was 88.8%~94.9%, 13%~50.7% respectively. Sludge growth rate of SBBR was 8.8% of that of 0.05 kgVSS/kgCOD. Besides, SBBR could recovered after 3 operating periods while SBR worked no better after 9 operating periods.Therefore, SBBR excelled SBR. Researches showed, effluent quantity of tannery wastewater treatment process (Homogenization—SBBR—BAF) was stable. When COD of influent was between 801 and 2,834 mg/L, NH4+-N was between 87 mg/L and 203 mg/L, COD of effluent was less than 80 mg/L, NH4+-N was less than 10 mg/L, which achieved the standard of reuse. This biotreatment was featured in low cost, easy and flexible management, less sludge, no inverse sludge system. Besides, this technique required no chemical, which could lower the cost and avoid secondary pollution. Great resistant of impact due to two membranes and was suitable for tannery wastewater which was featured by fluctuation of influent quality and quantity. Researches showed effective microorganisms promotes the startup of the process.Biofilm in the bioaugmentation process matured with 6 days while biofilm in normal process matured with 9 days. Effective microorganisms could accelerate the degradation of COD and shorten the residence time. Aggrandizement system could make COD<200 mg/L with 6 to8 hours while cntrolling system could make COD<200 mg/L with 8 to 10 hours. Long-term operating shows that SBBR in the bioaugmentation system worked better than the normal system in the treatment of COD and NH4+-N. The average COC of effluent in bioaugmentation system was 53 mg/L, normal system was 74 mg/L. In the simulative circulation process,aggrandizement process, which could fulfill 8 times theoretical circulation, works more stably than controlling process which could only fulfill 4 times theoretical circulation. Researches showed that reasonable design could make the wastewater meet the first grade of discharging standard of National Integrated Wastewater Discharge Standard (GB8976-1996), and partially meet the demand of water using of the factory. Adding effective microorganisms could enhance the biotreatment and make the effluents reuse many times.

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利用实验测量和Monte Carlo模拟的方法,研究了RIBLL的传输效率。分析了影响传输效率的主要因素,发现碎片的动量分布形式对传输效率的模拟结果有重要的影响。另外通过比较,发现大部分碎片传输效率的模拟结果稍大于实验测量结果,两者最大相差约几十倍,这可以帮助估算次级束流强度,指导实验设计。

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当归新品系"DGA2000-02"是利用兰州重离子加速器研究装置(HIRFL)对"岷归1号"进行重离子束辐照选育出来的。与岷归1号相比,DGA2000-02表现出更强的抗病性,产量也有较大提高。对这两个品种的表型、品质及遗传差异进行了系统的分析。为将来进一步选育产量高、品质好及抗逆性强的新品种提供研究基础。

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对有限力程小液滴模型计算的质子数Z=101—130超重核同位素链核的基态性质进行了系统的分析,通过对这些同位素链中处于裂变稳定线上核的平均结合能、四极形变、单质子分离能、双质子分离能和α衰变能等性质的系统研究,显示了质子数Z=108,114,126和中子数N=162,180,196时壳幻数的存在,同时可以看到Z=127之后超重核的基态性质还需要进一步研究.

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用 60 Me V/u18O离子轰击天然铀靶 ,通过多核子转移反应产生重丰中子同位素 2 3 7Th。使用改进的相对快的分离钍的放射化学流程 ,从大量铀和复杂反应产物混合物中分离钍 ,用高纯锗( HPGe)探测器联同多道分析器对化学分离的钍样品做离线 γ射线谱学研究 ,通过对 2 37Th子体 2 37Pa(半衰期 8.7min)的 853.7ke Vγ射线的生长 -衰变曲线的分析 ,确定 2 37Th的半衰期为 4 .69± 0 .60min。