Design of Topas photonic bandgap fiber with high birefringence and low confinement loss

A highly birefringent hollow-core photonic bandgap fiber based on Topas cyclic olefin copolymer is designed. The rhombic hollow-core with rounded corners is formed by omitting four central air holes of the cladding structure. The guided modes, birefringence and confinement loss of the fiber are investigated by using the full-vector finite element method. A high phase birefringence of the order of 10(-3), a group birefringence of the order of 10(-2) and confinement loss less than 0.1 dB/km are obtained at the central wavelength (1.55 mu m) range of the bandgap for fiber with seven rings of air holes in the cladding region. (C) 2010 Elsevier B.V. All rights reserved.

肉牛B超活体取卵效果的研究

对肉牛(莫累灰×婆罗门) 利用B 超活体取卵,研究不同年龄和促卵泡素(FSH) 对平均卵泡数、平均卵母细 胞数、平均可利用卵母细胞(COC) 数、卵母细胞回收率、COC 回收率、囊胚率和平均囊胚数的影响。结果表明:肉牛 B 超活体所取卵的数量和质量受年龄的影响,青年牛好于经产牛,经产牛好于老年牛;适量注射FSH 可以提高经产 牛和老年牛的囊胚率和(或) 平均囊胚数。

年龄和FSH在肉牛活体取卵过程中对卵泡和卵母细胞发育的影响

青年牛(12月龄)和经产牛(7-8岁)平均卵泡数(≥2mm)及>10mm卵泡数明显高于老年牛(≥14岁)(P<0.01)。青年牛和经产牛平均卵母细胞数及平均COC数高于老年牛(P<0.05)。1和2级卵母细胞比例青年牛高于或等于经产牛高于老年牛,3和4级卵母细胞比例老年牛高于经产牛高于或等于青年牛(P<0.05)。青年牛和经产牛2级卵母细胞占优势,而老年牛3级卵母细胞居多。不同剂量外源性FSH诱导后,经产牛和老年牛平均卵泡数在各剂量组之间没有显著差异(P>0.05);但≥6mm卵泡数及2级卵母细胞比例明显增加,而2-5mm卵泡数相应减少及裸卵和老化卵比例降低(P<0.05)。在10次取卵过程中,青年牛和经产牛发情当天平均卵母细胞数均较以后各次的数量低(P<0.05)。

非茂过渡金属烯烃聚合催化剂的研究

本论文合成、表征了一系列以镍、钦为中心离子的非茂过渡金属配合物，研究了这些配合物催化烯烃聚合的反应行为。主要工作和结论如下：1．合成、表征了一系列水杨醛亚胺中性镍配合物。在改性甲基铝氧烷（MMAO）的活化下，这些中性镍配合物可高效催化降冰片烯伽BE）的加成聚合，在优化条件下，催化活性高达7.1×107 gPNBE／molNi.h，聚降冰片烯的分子量高达1.5×106g／mol。2．合成、表征了三种新型p一二酮单亚胺中性镍配合物。X-射线分析表明，这些中性镍配合物的空间构型为扭曲的平面四边形。在Ni（CO）2的活化下，这些中性镍配合物可催化乙烯聚合生成以甲基支化为主的支化聚乙烯。在MMAO的活化下，这些中性镍配合物是降冰片烯加成聚合的高效催化剂，在优化条件下，催化活性高达4.5×107gPNBE／molNi.h，聚降冰片烯的分子量高达1.1×106g／mol。另外，这些中性镍配合物在MMAO的活化下，可催化甲基丙烯酸甲酷（MMA）聚合，生成富间规的聚甲基丙烯酸甲酷（rr一70％）。令人惊讶的是，这些中性镍配合物／MMAO体系还能催化乙烯和MMA的共聚合反应，生成乙烯与MMA的无规共聚物，极性单体的插入率可达16.7 mol％。3．合成、表征了一系列新型β-二酮单亚胺钦配合物。X-射线分析表明，这些钦配合物的立体构型为含有一个CZ轴的变形八面体。常温下，这些钦配合物在MMAO的活化下，可以高效催化乙烯活性聚合，催化活性可达1.3×l06g PE/molTi-h，生成无支链的线性聚乙烯。常温下，这些钦配合物瓜IMAO体系还能高效催化乙烯和降冰片烯的活性共聚合反应，催化活性高达3.2×106gpolymer／molTi'h，所得聚合物为乙烯与降冰片烯的交替共聚物（COC）。利用该催化体系的活性聚合性质，制备了包含半晶和无定形两种结构片段的新型A-B二嵌段共聚物（PE-b1ock-COC）。4．合成、表征了一系列新型β-二亚胺钦配合物。在MMAO的活化下，这些钦配合物可以常温催化乙烯聚合，在优化条件下，催化活性可达4.6×105 gPe／molTi-h，生成双峰分布的聚乙烯，重均分子量高达6.6×105g／mol。

稀土冠醚络合物的合成及其性质的研究

近年来对稀土冠醚络合物的研究日益受到重视文献曾报导了12－冠－4，15－冠－5，18－冠－6等冠醚与稀土的固体络合物的合成性质及结构的研究，但大部分工作侧重于研究冠醚空腔与稀土离子直径的匹配程度对络合物稳定性的影响，而对于冠醚具有的取代基、空间构型及其配位阴离子等对络合物稳定性、组成结构的影响尚注意得很不够，对溶液中络合物的研究工作较少；特别是冠醚对稀土元素萃取性质的研究未见系统报导。本论文以瑞士进口的二环已基18－冠－6（DCC）混合物为原料进行异构体的分离。得到纯异构体A、B、D的~(13)C谱，不同位置的五种碳原子的谱线清析可辨，其化学位移值与计算值比较，确定了谱线的归属，利用单一异构体测定结果，对异构体A、B、D混合物进行鉴定得到满意结果。利用分离得到的纯异构体A、B及北京五所提供的异构体D合成了与轻稀土硝酸盐络合物。元素分析结果指出，除1：1络合物外，首次得到非1：1组成的络合物。La（NO_3）_3·DDC（DCC＝Ia，Id），[Ln（NO_3）_3]_3(DCC)_2 （Ln＝Ce，Pr，Nd，DCC＝Ia，Id）而异构体B得到全部3：2的络合物。选择硝酸镧与三种异构体的络合物进行了热分析，结果指出3：2与1：1络物物表现出完全不同的热分解行为。3：2络物合只有一步分解，且比1：1络物合具有更高的热分解温度1：1络合物分两步分解，首先发生向3：2络合物的转变。络合物的红外光谱研究表明，络合物中冠醚与自由冠醚的红外光谱图呈现明显区别，冠醚环上COC反对称伸展振动在生成络合物后向低频产生50～70 cm~(-1)的位移，其中3：2比1：1络合物位移量略大，络合物中硝酸根的振动吸收全部呈现配位硝酸根的特征谱带，并且3：2与1：1络合物之间呈现明显差别。另外在远红外区观察到Ln-O（NO_3~-）的振动谱带。用NMR研究冠醚与稀土在非水溶剂中的络合反应。首先测定了12－冠－4，15－冠－5与位移试剂Pr（fod）_3，Eu（fod）_3，Yb（fod）_3体系中冠醚次甲基上'H及~(13)C的化学位移值Δδ，得到了谱线随稀土与冠醚浓度比改变的变化规律。位移方向，对于Pr向高场移动，对于Eu、Yb向低场移动，位移量及谱线宽度的大小为Yb＞Pr＞Eu。且Δδ~(13)C＞Δδ~1H符合几何因素的规律，即正比于（3COS~2θ-1）/~r~3。利用二种方法计算了不同温度下络合物的稳定常数。对于不同冠醚，K值次序为冠－5＞冠－4＞冠－6，对于不同位移试剂为Pr＞Eu＞Yb。利用不同温度的K_1值，计算并讨论了平衡反应的热力学函数ΔG°，ΔH°，ΔS°。实验考察了微量水存在下络合物的结构和作用机理，在高氯酸盐与冠醚体系的研究中，观察到与位移试剂体系完全相反的规律。还发现在高氯酸稀土与冠醚的体系中快和慢两种交换过程共存，通过对单一交换体系的络合物稳定常数计算方法的改进，提出了适合混合交换体系的计算方法，并计算了18C6与Pr(clo_4)_3络合物在20℃时的稳定常数，K_1＝164升／摩乐。系统地研究了12－冠－4，15－冠－5，18－冠－6的衍生物及其二苯并24－冠－8等11种冠醚对单一稀土苦味酸盐的萃取，制备了15个稀土的苦味酸盐，考察了冠醚的空腔大小及取代基和空间构型对冠醚萃取稀土能力的影响，得到了B15C5，B18Cb，DCC萃取15个稀土元素的规律性，测定了相邻稀土元素间的分离因数，讨论了各种因素对DCC异构体萃取分离Pr Nd的影响，指出异构体A具有更大选择性。最大分离因数β_(Nd)~(Pr)=3.5，上述结果将为今后发展冠醚在稀土分离液膜萃取等方面的应用提供基础数据。

制革废水生物强化处理及中水回用试验研究

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.

Light alkenes preparation by the gas phase oxidative cracking or catalytic oxidative cracking of high hydrocarbons

The preparation of light alkenes by the gas phase oxidative cracking (GOC) or catalytic oxidative cracking (COC) of model high hydrocarbons ( hexane, cyclohexane, isooctane and decane in the GOC process and hexane in the COC process) was investigated in this paper. The selection for the feed in the GOC process was flexible. Excellent conversion of hydrocarbons ( over 85%) and high yield of light alkenes ( about 50%) were obtained in the GOC of various hydrocarbons including cyclohexane at 750 degreesC. In the GOC process, the utilization ratio of the carbon resources was high; CO dominated the produced COX (the selectivity to CO2 was always below 1%); and the total selectivity to light alkenes and CO was near or over 70%. In the COC of hexane over three typical catalysts (HZSM-5, 10% La2O3/HZSM-5 and 0.25% Li/MgO), the selectivity to COX was hard to decrease and the conversion of hexane and yield of light alkenes could not compete with those in the GOC process. With the addition of H-2 in the feed, the selectivity to COX was reduced below 5% over 0.1% Pt/HZSM-5 or 0.1% Pt/MgAl2O4 catalyst. The latter catalyst was superior to the former catalyst due to its perfect performance at high temperature, and with the latter, excellent selectivity to light alkenes ( 70%) and the conversion of hexane (92%) were achieved at 850 degreesC ( a yield of light alkenes of 64%, correspondingly).

Effect of syngas addition on lower alkene production by the oxidative cracking of hexane

The lower alkene production by the gas-phase oxidative cracking (GOC) or catalytic oxidative cracking (COC) of hexane (C6) with added syngas was investigated. The addition of syngas to the COC process could effectively enhance the selectivity to lower alkenes and decrease the selectivity to COx, because of the preferential reaction between O-2 with H-2 contained in the syngas, whereas it has little effect on the conversion of C6 and product distribution in the GOC process. The high selectivity to lower alkenes of 70% and low selectivity to CO, of 6% at C6 conversion of 66% were achieved over 0.1% Pt/MgAl2O4 catalyst. The COC process of C6 combined with the syngas in the feed could directly produce a gas mixture of lower alkenes, H-2, and CO, which usually is a suitable feedstock for the hydroformylation process.