1000 resultados para Heat denaturing


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应用改进DEAE-Toyopearl 650S阴离子交换柱层析从高等植物菠菜(Spinacia oleracea)中分离纯化了核心天线复合物CP43和CP47。并对它们的纯度和完整性色素种类和含量,以及色素分子的结合状态进行了研究并对色素分子间的能量传递机制进行了讨论。结果如下: 1、HPLC检测结果表明:纯化的CP43和CP47均只含Chla和β-Car两种色素分子,并且,平均每分子CP43多肽含19-20分子Chla和4-5分子β-Car;而平均每分CP47则含20-21分子Chla和3-4分子β-Car。 2、以436nm和480nm激发光激发样品得到的CP43和CP47的低温荧光发射光谱的最大荧光发射峰分别位于683nm和693nm。进一步发现,CP43和CP47,在相同条件下分别以436nm和480nm激发光激发样品得到的低温荧光发射光谱经归一化后几乎完全重叠,而且400-500nm波长范围内的激发光扫描得到的三维低温荧光发射光谱沿激发轴具有较好的对应关系,表明纯化的CP43和CP47都具有较高的完整性。 3、纯化的CP43和CP47的吸收光谱的红区最大吸收峰分别位于671nm和674nm。该光区的导数光谱均分辨出偏蓝区和偏红区两个子峰,CP43的这两个子峰分别位于669nm和682nm;而CP47的两个子峰则分别位于669nm和680nm。进一步用包含这两个子峰的高斯解析参数对红区最大吸收峰进行拟合,结果证明,拟合的曲线与实测曲线几乎完全吻合,这表明,CP43和CP47均至少包含两种不同状态的Chla分子。 3.1应用不同的变性温度处理CP43,发现随变性温度的不断提高,其红区最大吸收峰的峰值逐渐减小,四阶导数光谱分辨出的两个子峰同时减小,但差光谱显示:随处理温度的不断提高,这两个组分峰值的变化并不同步进行,较低温度范围内(55℃以下)682nm吸收峰下降明显,而较高温度范围内(55℃以上),669nm吸收峰下降明显。 同时,随处理温度不断提高CP43脱辅基蛋白的结构也在不断发生变化,其变化过程明显表现出两个跃变阶段。这两个跃变阶段分别出现在40~50℃范围内和55~60℃范围内,恰与吸收光谱两个组分峰变化的转变过程相一致。这证明,CP43中分别位于669nm和682nm的不同的色谱组分即代表两种不同结合态的Chla分子,分别简称为“CP43-669”和“CP43-682”。它们在色素蛋白复合物中所处的环境不同,因而对蛋白质结构的依赖性不同,前者更高地依赖于蛋白复合物的整体构象,而后者则主要依赖于蛋白质的二级结构。 3.2 经不同的变性温度处理的CP47,其红区最大吸收峰的峰位逐渐蓝移,而吸收峰值无明显的变化,只有当处理温度提高到65℃以后,蓝移后的吸收峰值(669nm)才开始明显减小;四阶导数光谱表现为680nm吸收峰的信号逐渐下降669nm的吸收信号逐渐明显;处理减对照差光谱只观察到680nm吸收值的逐渐减少,而几乎观察不到669nm吸收值的变化。同时,随变性温度的不断提高,CP47的脱辅基蛋白的结构也发生相应的变化与CP43不同,蛋白结构变化最大的温度范围为60℃~65℃之间,但同CP47的峰位蓝移、导数光谱中680nm信号的减小,以及差光谱中680nm吸收值的减小相一致。由此认为,同CP43一样,CP47的吸收光谱中分辨出的分别位于669nm和680nm处的两个不同光谱组分亦分别代表两种不同结合状态的Chla分子,分别简称为“CP47-669”和“CP47-680”,与CP43中的相应组分对应,它们处于不同的蛋白环境中,从而对蛋白质结构变化的依赖性不同。 3.3 CP43和CP47的CD光谱表现出明显的正负双峰,表明色素分子间存在较强的激子相互作用。随变性温度的不断提高,正负CD双峰的信号逐渐减弱,变化过程与脱辅基蛋白结构的变化以及CP43-682的变化相一致,表明色素分子间的激子相互作用更高依赖于CP43-682和CP47-680。并认为CP43-682和CP47-680可能以二聚体或多聚体的形式存在,并且二聚体或多聚体的形成依赖于蛋白天然构象。而CP43-669和CP47-669则以单体的形式位于蛋白结构中相对伸展的区域。并提出:在CP43-682以CP47-680分子之间,激发能主要以激子偶合机制进行而在CP43-669,CP47-669分子间及CP43-669至CP43-682间,CP47-669至CP47-680之间激发能则主要以Foster机制进行。 4、以488nm激发光得到的CP43和CP47的共振拉曼光谱都具有全反式构型类胡萝卜素分子的四个典型特征峰由此认为CP43和CP47中的β-Car分子亦具有全反式构型;与溶于丙酮抽体物中的β-Car分子相比较,CP43和CP47中的β-Car分子的共振拉曼光谱中具有较强的960cm~(-1)的拉曼峰,表明,CP43和CP47中的β-Car分子具有扭曲的构象。 应用经归一化后的吸收光谱与荧光激发光谱相比较的办法发现CP43和CP47中存在β-Car分子和Chla分子间的能量传递其能量传递效率分别为29.8~29.9%和52.3~56.9%。这表明,在正常条件下,CP47中β-Car分子和Chla分子间的能量传递效率远大于CP43。此外,当选用蛋白结构变化最明显的热变性温度处理样品后,发现,不论CP43还是CP47中β-Car与Chla分子间的能量传递效率大大降低,表明,这两种色素分子间的能量传递严格依赖于蛋白复合物的天然构象,并认为,正常条件下,CP43和CP47内β-Car与Chla分子间的空间距离较近,可能不大于10A,CP43和CP47相比较,CP47内这两种色素分子间的距离更近。并进一步提出,在CP43和CP47中,β-Car到Chla分子间的能量传递最大可能以Dexter的电子交换机制进行。

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A purified commercial double-walled carbon nanotube (DWCNT) sample was investigated by transmission electron microscopy (TEM), thermogravimetry (TG), and Raman spectroscopy. Moreover, the heat capacity of the DWCNT sample was determined by temperature-modulated differential scanning calorimetry in the range of temperature between -50 and 290 °C. The main thermo-oxidation characterized by TG occurred at 474 °C with the loss of 90 wt% of the sample. Thermo-oxidation of the sample was also investigated by high-resolution TG, which indicated that a fraction rich in carbon nanotube represents more than 80 wt% of the material. Other carbonaceous fractions rich in amorphous coating and graphitic particles were identified by the deconvolution procedure applied to the derivative of TG curve. Complementary structural data were provided by TEM and Raman studies. The information obtained allows the optimization of composites based on this nanomaterial with reliable characteristics.

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Experiments were undertaken to study drying kinetics of moist cylindrical shaped food particulates during fluidised bed drying. Cylindrical particles were prepared from Green beans with three different length:diameter ratios, 3:1, 2:1 and 1:1. A batch fluidised bed dryer connected to a heat pump system was used for the experimentation. A Heat pump and fluid bed combination was used to increase overall energy efficiency and achieve higher drying rates. Drying kinetics, were evaluated with non-dimensional moisture at three different drying temperatures of 30, 40 and 50o C. Numerous mathematical models can be used to calculate drying kinetics ranging from analytical models with simplified assumptions to empirical models built by regression using experimental data. Empirical models are commonly used for various food materials due to their simpler approach. However problems in accuracy, limits the applications of empirical models. Some limitations of empirical models could be reduced by using semi-empirical models based on heat and mass transfer of the drying operation. One such method is the quasi-stationary approach. In this study, a modified quasi-stationary approach was used to model drying kinetics of the cylindrical food particles at three drying temperatures.

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The climatic conditions of tropical and subtropical regions within Australia present, at times, extreme risk of physical activity induced heat illness. Many administrators and teachers in school settings are aware of the general risks of heat related illness. In the absence of reliable information applied at the local level, there is a risk that inappropriate decisions may be made concerning school events that incorporate opportunities to be physically active. Such events may be prematurely cancelled resulting in the loss of necessary time for physical activity. Under high or extremely high risk conditions however, the absence of appropriate modifications or continuation could place the health of students, staff and other parties at risk. School staff and other key stakeholders should understand the mechanisms of escalating risk and be supported to undertake action to reduce the level of risk through appropriate policies, procedures, resources and action plans.

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Experiments were undertaken to study drying kinetics of different shaped moist food particulates during heat pump assisted fluidised bed drying. Three particular geometrical shapes of parallelepiped, cylindrical and spheres were selected from potatoes (aspect ratio = 1:1, 2:1, 3:1), cut beans (length: diameter = 1:1, 2:1, 3:1) and peas respectively. A batch fluidised bed dryer connected to a heat pump system was used for the experimentation. A Heat pump and fluid bed combination was used to increase overall energy efficiency and achieve higher drying rates. Drying kinetics, were evaluated with non-dimensional moisture at three different drying temperatures of 30, 40 and 50o C. Due to complex hydrodynamics of the fluidised beds, drying kinetics are dryer or material specific. Numerous mathematical models can be used to calculate drying kinetics ranging from analytical models with simplified assumptions to empirical models built by regression using experimental data. Empirical models are commonly used for various food materials due to their simpler approach. However problems in accuracy, limits the applications of empirical models. Some limitations of empirical models could be reduced by using semi-empirical models based on heat and mass transfer of the drying operation. One such method is the quasi-stationary approach. In this study, a modified quasi-stationary approach was used to model drying kinetics of the cylindrical food particles at three drying temperatures.

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Most studies on the characterisation of deposits on heat exchangers have been based on bulk analysis, neglecting the fine structural features and the compositional profiles of layered deposits. Attempts have been made to fully characterise a fouled stainless steel tube obtained from a quintuple Roberts evaporator of a sugar factory using X-ray diffraction and scanning electron microscopy techniques. The deposit contains three layers at the bottom of the tube and two layers on the other sections and is composed of hydroxyapatite, calcium oxalate dihydrate and an amorphous material. The proportions of these phases varied along the tube height. Energy-dispersive spectroscopy and XRD analysis on the surfaces of the outermost and innermost layers showed that hydroxyapatite was the major phase attached to the tube wall, while calcium oxalate dihydrate (with pits and voids) was the major phase on the juice side. Elemental mapping of the cross-sections of the deposit revealed the presence of a mineral, Si-Mg-Al-Fe-O, which is probably a silicate mineral. Reasons for the defects in the oxalate crystal surfaces, the differences in the crystal size distribution from bottom to the top of the tube and the composite fouling process have been postulated.

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Bovine intestine was dried in a heat pump fluid bed combination. Minimum fluidisation velocity was calculated by Ergun Equation and some relations were established.

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Background: There is no global definition of a heatwave because local acclimatisation and adaptation influence the impact of extreme heat. Even at a local level there can be multiple heatwave definitions, based on varying temperature levels or time periods. We investigated the relationship between heatwaves and health outcomes using ten different heatwave definitions in Brisbane, Australia. ---------- Methodology/Principal Findings: We used daily data on climate, air pollution, and emergency hospital admissions in Brisbane between January 1996 and December 2005; and mortality between January 1996 and November 2004. Case-crossover analyses were used to assess the relationship between each of the ten heatwave definitions and health outcomes. During heatwaves there was a statistically significant increase in emergency hospital admissions for all ten definitions, with odds ratios ranging from 1.03 to 1.18. A statistically significant increase in the odds ratios of mortality was also found for eight definitions. The size of the heat-related impact varied between definitions.---------- Conclusions/Significance Even a small change in the heatwave definition had an appreciable effect on the estimated health impact. It is important to identify an appropriate definition of heatwave locally and to understand its health effects in order to develop appropriate public health intervention strategies to prevent and mitigate the impact of heatwaves.

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Promoted ignition testing (NASA) Test 17) [1] is used to determine the relative flammability of metal rods in oxygen-enriched atmospheres. A promotor is used to ignite a metal sample rod, initiating sample burning. If a predetermined length of the sample burns, beyond the promotor, the material is considered flammable at the condition tested. Historically, this burn length has been somewhat arbitrary. Experiments were performed to better understand this test by obtaining insight into the effect a burning promotor has on the preheating of a test sample. Test samples of several metallic materials were prepared and coupled to fast-responding thermocouples along their length. Thermocouple measurements and test video were synchronized to determine temperature increase with respect to time and length along each test sample. A recommended flammability burn length, based on a sample preheat of 500 degrees fahrenheit, was determined based on the preheated zone measured from these tests. This length was determined to be 30 mm (1.18 in.). Validation of this length and its rationale are presented.