~(179)Au的1/2[660](πi_(13/2))转动带

利用能量为 16 4— 180MeV的 3 5Cl束流 ,通过重离子核反应 14 9Sm(3 5Cl ,5n)研究了 179Au的高自旋态能级结构 .实验进行了γ射线的激发函数、X γ和γ γ t符合测量 .基于对实验测量结果的分析 ,首次建立了 179Au的 1 2 [6 6 0 ](πi13 2 )转动带 .结合已有的实验数据 ,着重讨论了奇AAu核中1 2 [6 6 0 ](πi13 2 )转动带的带头激发能随中子数的变化

~(12)C~(6+)重离子束照射治疗复发性软组织肉瘤临床疗效探讨

目的: 应用我国自主研发的重离子加速器产生的12C6+重离子束治疗复发性软组织肉瘤,评价其高线性能量传递 (LET)及低 LET在临床应用中的优劣. 方法: 3例经病理证实为软组织肉瘤自愿接受重离子束照射的患者,其中 2例病变位于腹部,1例在背部. 所有患者均为手术复发 2次以上,最多达 6次,并经手术行常规放疗失败. 应用 80～100mev/u重离子束对 3例患者分别给予总剂量 72～120 GyE/6212 f照射,生物效应剂量 (RBE) =3. 结果:2例患者 3mo后病变完全消失,达临床治愈;1例缩小 75%,达临床部分缓解,总有效率为100%.治疗中及治疗后照射野皮肤无破溃等放射性损伤.结论:12C6+重离子束具有治疗精度高,疗程短,对肿瘤周围正常组织损伤小等特点. 特别在射线抗拒的难治性肿瘤中可达到常规放疗难以实现的疗效,具有很好的临床应用前景.

A 2-kW COIL with a square pipe-array JSOG and nitrogen buffer gas

A 2-kW-class chemical oxygen-iodine laser (COIL) using nitrogen buffer gas has been developed and tested since industrial applications of COIL devices will require the use of nitrogen as the buffer gas. The laser, with a gain length of 11.7 cm, is energized by a square pipe-array jet-type singlet oxygen generator (SPJSOG) and employs a nozzle bank with a designed Mach number of 2.5. The SPJSOG has advantages over the traditional plate-type JSOG in that it has less requirements on basic hydrogen peroxide (BHP) pump, and more important, it has much better operational stability. The SPJSOG without a cold trap and a gas-liquid separator could provide reliable operations for a total gas flow rate up to 450 mmol/s and with a low liquid driving pressure of around 0.7 atm or even lower. The nozzle bank was specially designed for a COIL using nitrogen as the buffer gas. The cavity was designed for a Mach number of 2.5, in order to provide a gas speed and static temperature in the cavity similar to that for a traditional COIL with helium buffer gas and a Mach 2 nozzle. An output power of 2.6 kW was obtained for a chlorine flow rate of 140 mmol/s, corresponding to a chemical efficiency of 20.4%. When the chlorine flow rate was reduced to 115 mmol/s, a higher chemical efficiency of 22.7% was attained. Measurements showed that the SPJSOG during normal operation could provide a singlet oxygen yield Y greater than or equal to 55%, a chlorine utilization U greater than or equal to 85%, and a relative water vapor concentration w = [H2O]/([O-2] + [Cl-2]) less than or equal to 0.1.

成核剂1,3:2,4-二(亚苄基)-D山梨醇对PET/PEN共混体系结构和结晶形态影响

利用差示扫描量热仪、X射线衍射仪、正交偏光显微镜研究了成核剂 1,3 :2 ,4-二 (亚苄基 ) -D山梨醇(DBS)对聚对苯二甲酸乙二醇酯 (PET) /聚 2 ,6-萘二甲酸乙二醇酯 (PEN)共混体系的结构及结晶形态的影响。结果表明 :成核剂的加入 ,使PET/PEN共混体系熔融起始温度升高 10℃左右 ,结晶峰形变尖锐 ,说明加入成核剂后有效促进了PET/PEN共混体系的结晶。实验结果表明 :成核剂含量低于 1%时 ,PET/PEN共混体系晶体的球晶完整。成核剂含量大于 3 %时 ,PET/PEN /DBS共混体系晶体的球晶碎小。成核剂的加入 ,能够有效地减小球晶尺寸和降低球晶的完善性

4-羟基偶氮苯与6-氯-5,12-萘并萘醌反应产物的NMR分析

无水碳酸钾存在下6-氯-5,12-萘并萘醌与4-羟基偶氮苯在干燥DMF中反应的主要产物在某些反应条件下不是6[4-(苯基偶氮基)苯氧基]-5,12-萘并萘醌(1)。该未知反应产物2经核磁共振方法研究证实是6-(N,N-二甲氨基)-5,12-萘并萘醌。本文对化合物2的~1H-和~(13)C化学位移、偶合信息和结构作了详细归属,并推测其反应进程,实验结果表明,化合物2是由化合物1与溶剂DMF反应生成。

ARYLIDENE COPOLYETHER SULFONES .2. SYNTHESIS END CHARACTERIZATION OF SOME NEW COPOLYETHER SULFONES CONTAINING DIBENZYLIDENE CYCLOHEXANONE MOIETIES

New copolyether sulfones containing 2,6-bis(p-oxo-benzylidene)cyclohexanone and 2,6-bis(o,p-dioxo-benzylidene)cyclohexanone moieties were prepared in the conventional literature manner by condensing the dipotassium salts of 2,6-bis(p-hydroxybenzylidene)cyclohexanone (III), 2,6-bis(o,p-dihydroxybenzylidene)-cyclohexanone (V), and 2,2-bis(p-hydroxyphenyl)propane (Bisphenol A, VII) with 4,4'-dichlorodiphenyl sulfone (VI), or by condensing the dipotassium salts of III and VII with a new benzylidene cyclohexanone sulfone macromer (X). Finally, the polycondensation reaction of sulfonyl bis(p-benzaldehydeoxo-p-phenylene) (IX) with cyclohexanone leads to an unsaturated copolymer (XVI). The resulting copolyether sulfones were confirmed by IR, H-1-NMR, viscometry, elemental analysis, thermooptical (TOA), x-ray, and thermogravimetric (TGA) measurements.

（C_（12）H_8）~（2＋）离子中电荷定位的理论研究

本文用半经验量子化学方法ＭＮＤＯ研究了由联苯衍生物产生的［Ｃ１２Ｈ８］２＋双电荷离子的结构，讨论了其中的电荷定位和影响离子稳定性的因素，双电荷离子的两个电荷分别定位于两个苯环上，表明该离子是由联苯衍生物经两步反应产生。

粉状巯基棉富集——水中痕量CH_3Hg~+及Hg~(2+)的冷原子荧光测定

本文提出了一种新的高巯基粉状巯基棉的合成方法,按此法合成的流基棉含量在2.2%～2.5%之间.在盐酸介质中,用溴水在室温下快速分解甲基汞,冷原子荧光测定的新方法.将粉状巯基棉与稀释剂按一定比例混合装柱,用于富集水体中溶解态痕量Hg~(2+)和CH_3Hg~+,富集流速100ml/min.检出限CH_3Hg~+为4.2×10~(-5)μg/l,Hg~(2+)为6.6×10~(-5)μg/l.

Comparative effects of GLP-1 and GIP on cAMP production, insulin secretion, and in vivo antidiabetic actions following substitution of Ala8/Ala2 with 2-aminobutyric acid

The two major incretin hormones, glucagon-like peptide-1 (GLP-1), and glucose-dependent insulinotropic polypeptide (GIP), are currently being considered as prospective drug candidates for treatment of type 2 diabetes. Interest in these gut hormones was initially spurred by their potent insulinotropic activities, but a number of other antihyperglycaemic actions are now established. One of the foremost barriers in progressing GLP-1 and GIP to the clinic concerns their rapid degradation and inactivation by the ubiquitous enzyme, dipeptidyl peptidase IV (DPP IV). Here, we compare the DPP IV resistance and biological properties of Abu(8)/ Abu(2) (2-aminobutyric acid) substituted analogues of GLP-1 and GIP engineered to impart DPP IV resistance. Whereas (Abu(8))GLP-1 was completely stable to human plasma (half-life > 12h), GLP-1, GIP, and (Abu(2))GIP were rapidly degraded (half-lives: 6.2, 6.0, and 7.1 h, respectively). Native GIP, GLP-1, and particularly (Abu(8))GLP-1 elicited significant adenylate cyclase and insulinotropic activity, while (Abu(2))GIP was less effective. Similarly, in obese diabetic (ob/ob) mice, GIP, GLP-1, and (Abu(8))GLP-1 displayed substantial glucose-lowering and insulin -releasing activities, whereas (Abu(2))GIP was only weakly active. These studies illustrate divergent effects of penultimate amino acid Ala(8)/Ala(2) substitution with Abu on the biological properties of GLP-1 and GIP, suggesting that (Abu(8))GLP-1 represents a potential candidate for future therapeutic development. (C) 2004 Elsevier Inc. All rights reserved.

Seasonal and diurnal variations in ultraviolet-B and ultraviolet-A irradiances at and below the sea surface at Helgoland (North Sea) over a 6-year period

Ultraviolet(UV) radiation at four wavelengths (305, 320, 340 and 380 nm) and photosynthetically active radiation (PAR) were measured from May 1994 to October 1999 using Biospherical UV radiometers. A surface reference sensor located on the roof of the Marine Station at Helgoland recorded values every 5 min, and an equivalent profiling underwater sensor was used for measurements in the sea at approximately monthly intervals. The ratio of 305-nm radiation to PAR varied seasonally, with a 14-fold increase from winter to summer. A much weaker seasonal trend (ca. 1.5-fold) was apparent in the ratio of 320-nm radiation to PAR, but there was no seasonal trend in the ratios of 340- or 380-nm radiation to PAR. The year-to-year variations in 305-nm radiation were also much greater relative to PAR than for the other UV wavelengths, but there was no evidence of a change in the 305 nm:PAR ratio over the study period. The ratios of both 305- and 320-nm radiation to PAR increased from dawn to midday, but those of 340- and 380-nm radiation were almost constant through the day, except shortly before sunrise and after sunset when the proportions of 340- and 380-nm radiation increased. Underwater measurements of PAR and UV suggest that the 1% depth for 305-nm radiation was little more than 1 m, but this estimate is valid only for summer and autumn because, in other seasons, few reliable readings for 305-nm radiation could be obtained underwater, and no attenuation coefficient could be calculated. The 1% depths recorded for the other UV wavelengths in the middle 6 months of the year were 2.0 m for 320 nm, 2.6 m for 340 nm and 4.6 m for 380 nm, compared with 12 m for PAR, but the attenuation of all wavebands increased sharply in October and remained higher until March. An analysis of the influence of sun angle, total column ozone concentration, the proportion of skylight, and cloud cover on the ratio of UV wavelengths to PAR in surface irradiance demonstrated that solar angle has a greater influence than ozone concentration on the irradiance at 305 nm, and that the typical occurrence of ozone

SO2 Saturation of the Room Temperature Ionic Liquid [C(2)mim][NTf2] Much Reduces the Activation Energy for Diffusion

The physical effect of high concentrations of reversibly dissolved SO2 on [C(2)mim][NTf2] was examined using cyclic voltammetry, chronoamperometry, and ESR spectroscopy. Cyclic voltammetry of the oxidation of solutions of ferrocene, N,N,N',N'-tetramethyl-p-phenylenediamine (TMPD), and chloride in the room temperature ionic liquid (RTIL) 1-ethyl-3-methylimidazolium bis(trifluoromethanesufonyl)imide ([C(2)mim][NTf2]) reveals an increase in limiting current of each species corresponding to the addition of increasing concentrations of sulfur dioxide. Quantitative chronoamperometry reveals an increase in each species' diffusion coefficient with SO2 concentration. When chronoamperometric data were obtained for ferrocene in [C(2)mim][NTf2] at a range of temperatures, the translational diffusion activation energy (29.0 +/- 0.5 kJ mol(-1)) was found to be in good agreement with previous studies. Adding SO2 results in apparent near-activationless translational diffusion. A significant decrease in the activation energy of rotational diffusion with the SO2 saturation of a 2,2,6,6-tetramethyl-1-piperidinyloxyl (TEMPO) solution in [C(2)mim][NTf2] (29.9 +/- 2.0 to 7.7 +/- 5.3 kJ mol(-1)) was observed using electron spin resonance (ESR) spectroscopy. The reversible physical absorption Of SO2 by [C(2)mim][NTf2] should have no adverse effect on the ability of that ionic liquid to be employed as a solvent in an electrochemical gas sensor, and it is possible that the SO2-mediated reduction of RTIL viscosity could have intrinsic utility.

Guest sorption and desorption in the metal-organic framework [Co(INA)(2)] (INA = isonicotinate) - evidence of intermediate phases during desorption

The metal-organic framework [Co(INA)(2)].0.5EtOH (INA = isonicotinate, NC5H4-4-CO2-), 1 was synthesised under solvothermal conditions. Its X-ray crystal structure shows channels containing ethanol guests which are hydrogen-bonded to carboxylate oxygens of the framework. The pyridyl rings of the framework alternate between `open' and `closed' positions along the channels resulting in large variation in the channel cross-sectional area from ca. 1.4 by 2.3 at the narrowest point to 4.9 by 5.3 at the widest. Despite the very small windows, the ethanol guests (of van der Waals diameter ca. 4.2-6.1 Angstrom) may be reversibly desorbed and sorbed into the structure quantitatively, as shown by in situ variable-temperture IR spectroscopy and XRPD. The single-crystal structure of the desolvated form [Co(INA)(2)]2 shows that there is no change in the overall connectivity on desolvation, but the rotational positions of the pyridine rings are altered. This suggests that pyridyl rotation may occur to allow guests to pass in and out. When the synthesis was conducted in 1-propanol solvent [Co(INA)(2)].0.5Pr(n)OH.H2O 3, was obtained, and a single-crystal X-ray structure revealed the same overall connectivity as in 1 but with pyridine rings disordered over closed and open positions. There was no evidence of included guests from X-ray crystallography, suggesting that they are also highly disordered. Variable-temperature XRPD performed on bulk samples showed peaks which were unsymmetrical and exhibited shoulders, suggesting that for each pattern obtained the material actually consisted of several closely-related phases. The movements of the peaks during desolvation showed the presence of intermediate phases before the final desolvated product was formed. The peak positions of the intermediate phases matched more closely with the calculated pattern for 3 than with 1 or 2, suggesting that they may have disordered structures similar to 3. The results also suggest that the intermediate phase represents an initial increase in volume before a larger decrease in volume occurs to give the final desolvated material.

Plasma levels of intermedin (adrenomedullin-2) in healthy human volunteers and patients with heart failure

Intermedin/adrenomedullin-2 (IMD) is a member of the adrenomedullin/CGRP peptide family. Less is known about the distribution of IMD than for other family members within the mammalian cardiovascular system, particularly in humans. The aim was to evaluate plasma IMD levels in healthy subjects and patients with chronic heart failure. IMD and its precursor fragments, preproIMD25–56 and preproIMD57–92, were measured by radioimmunoassay in 75 healthy subjects and levels of IMD were also compared to those of adrenomedullin (AM) and mid-region proadrenomedullin45–92 (MRproAM45–92) in 19 patients with systolic heart failure (LVEF < 45%). In healthy subjects, plasma levels (mean + SE) of IMD (6.3 + 0.6 pg ml−1) were lower than, but correlated with those of AM (25.8 + 1.8 pg ml−1; r = 0.49, p < 0.001). Plasma preproIMD25–56 (39.6 + 3.1 pg ml−1), preproIMD57–92 (25.9 + 3.8 pg ml−1) and MRproAM45–92 (200.2 + 6.7 pg ml−1) were greater than their respective bioactive peptides. IMD levels correlated positively with BMI but not age, and were elevated in heart failure (9.8 + 1.3 pg ml−1, p < 0.05), similarly to MRproAM45–92 (329.5 + 41.9 pg ml−1, p < 0.001) and AM (56.8 + 10.9 pg ml−1, p < 0.01). IMD levels were greater in heart failure patients with concomitant renal impairment (11.3 + 1.8 pg ml−1) than those without (6.5 + 1.0 pg ml−1; p < 0.05). IMD and AM were greater in patients receiving submaximal compared with maximal heart failure drug therapy and were decreased after 6 months of cardiac resynchronization therapy. In conclusion, IMD is present in the plasma of healthy subjects less abundantly than AM, but is similarly correlated weakly with BMI. IMD levels are elevated in heart failure, especially with concomitant renal impairment, and tend to be reduced by high intensity drug or pacing therapy.

Die Kosten der Modellabteilung Schnittkäserei am Beispiel der Herstellung von Gouda-Käse. Teil 2: Ergebnisse und Interpretation der Modellkalkulationen

In der vorliegenden Arbeit, deren erster Teil in Heft 2 dieser Zeitschrift veröffentlicht wurde, werden die Kosten der “Schnittkäserei” am Beispiel der Herstellung von Gouda-Käse modellhaft bestimmt, wobei die vor 17 Jahren durchgeführten Modellkalkulationen für Edamerkäse hinsichtlich der Funktionsinhalte der Abteilung ausgedehnt und dem neuesten Stand der Technik sowie heutigen Schnittkäsereiproduktionsstrukturen angepaßt wurden. Zudem sind die generell für alle Modellabteilungen geltenden methodischen Weiterentwicklungen in den Kalkulationen berücksichtigt worden. In den sechs Unterabteilungen Vorstapelung, Bruchbereitung und Pressen, Salzbad, Käsebehandlung und Reifungslager, Abpackung sowie Versandkühlraum und Expedition wird ein rindengereifter Gouda-Käse (12-kg-Laib) hergestellt und hinsichtlich seiner Kostenverursachung untersucht. Zur Bestimmung der Modellkosten wurden vier Modelle gebildet, deren Kapazitäten in der Kesselmilchverarbeitung zwischen 8.000 und 48.000 l/h liegen. In Abhängigkeit vom Beschäftigungsgrad, der für Werte zwischen 21 und 100% simuliert wurde, können so die Kosten für Käsemengen zwischen rd. 5.100 und 30.8001 Käse/Jahr bestimmt werden. Gemäß den vorgegebenen Kapazitäten müssen die technischen Voraussetzungen für die Ausgestaltung der einzelnen Unterabteilungen modellspezifisch festgelegt werden, wobei eine Anpassung der technischen Auslegung an eine verringerte Auslastung bei 33%iger Beschäftigung erfolgt. Die zu tätigenden Investitionen für die Grundversion betragen 10,6 Mio. DM in Modell 1 und 40,3 Mio. DM in Modell 4. Bezogen auf die jeweilige Rohstoffeinsatzmenge ergeben sich hieraus spezifische Investitionen, die mit zunehmender Modellgröße erheblich sinken: Machen sie im Modell 1 noch 215,6 Tsd. DM/1 Mio. kg jährlicher Rohstoffeinsatzmenge aus, so verringern sie sich im Modell 4 auf 135,3 Tsd. DM/1 Mio. kg. Produktspezifische Investitionen und Faktormengenverbräuche führen zu den Einzelkosten des Produktes Gouda, die je nach Modellgröße und Beschäftigungsgrad zwischen 510,8 und 538,5 Pf/kg Käse liegen. Die Gesamtkosten der “Schnittkäserei”, die sich aus den Einzelkosten des Produktes Gouda und den Einzelkosten der Abteilung zusammensetzen, betragen 530,9 bis 654,3 Pf/kg Käse. Den größten Anteil an den Gesamtkosten haben die Rohstoffkosten (73 bis 90%). Der Anteil der Anlagekosten schwankt je nach Beschäftigung zwischen 4 und 18%, während die Personal- und sonstige Betriebskosten im Vergleich zu den beiden vorgenannten Kostenartengruppen in allen Modellen nur eine geringere Bedeutung haben. Betrachtet man die Gesamtkosten (ohne Rohstoffkosten) hinsichtlich ihrer Entstehung in den Unterabteilungen, so ist festzustellen, daß die höchsten Kosten in der Unterabteilung Bruchbereitung und Pressen anfallen: Bei einer 100%igen Beschäftigung betragen sie z.B. in Modell 3 42% der Gesamtkosten (ohne Rohstoff). Die geringsten Kosten (2%) fallen dagegen in der Unterabteilung Versandkühlraum und Expedition an. Die Kostenanalyse zeigt deutlich, daß mit zunehmender Modellgröße und steigender Produktionsmenge erhebliche Stückkostendegressionen zu erzielen sind, wobei der Einfluß des Beschäftigungsgrades auf die Kostendegression deutlich höher ist als derjenige der Modellgröße.