共查询到19条相似文献,搜索用时 218 毫秒
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为明确大豆地上和地下部分对干旱胁迫的响应及对产量的影响,以用于大豆抗旱改良,利用耐旱型品种
辽豆14与干旱敏感型品种辽豆21进行相互嫁接,采用盆栽试验,在结荚期进行水分胁迫处理(土壤含水量保持在
田间持水量的50%)13 d后,测定大豆叶片相关生理指标和各器官生物量。结果表明,水分胁迫使辽豆21自身嫁接
植株叶片的叶色值、叶面积、PSII 系统光化学量子产量Y(II),调节性能量热耗散Y(NPQ)、最大电子传递速率
ETRmax、半饱和光强下最小饱和光强Ik显著降低,非调节性能量热耗散Y(NO)显著提高。无论以哪个品种为砧木,
与辽豆21相比,辽豆14作为接穗始终具有较高的叶色值、叶面积、Y(II),Y(NPQ)、ETRmax和Ik,从而获得较高的植
株生物量。另外,干旱条件下,辽豆14作为砧木具有较高的根系活力,能使辽豆21接穗的叶面积、Y(II),Y(NPQ)、
ETRmax和Ik显著提高,最终获得荚重的增加。由此说明,大豆PSII性能和物质生产能力主要由地上部叶片特性决
定,但干旱下大豆的生长也会受到根系生理活性的影响。 相似文献
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转基因抗草甘膦大豆的光合及荧光特性 总被引:1,自引:0,他引:1
本文比较了转基因抗草甘膦大豆40-3-2与常规栽培大豆荷豆13在光合、叶绿素荧光以及繁殖适合度参数上的差异,以评价在我国农田生境中转基因大豆相对于本土栽培种是否具备更强的入侵性或杂草化特征。结果表明,40-3-2花期叶片净光合速率低于同期的荷豆13,但水分利用策略优良,即蒸腾速率低、水分利用效率高,环境适应能力强。叶绿素荧光测定显示40-3-2全天只有轻微的光抑制现象,其光系统Ⅱ能够在高温和强光照条件下维持较高的光化学效率,而荷豆13叶片在正午时有强烈的光抑制。尽管如此,在没有除草剂选择压条件下,在生长和繁殖适合度上40-3-2相对于荷豆13无竞争优势,入侵性风险较低。 相似文献
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高水分蒸煮挤压小麦混合粉的研究 总被引:2,自引:0,他引:2
食品蒸煮挤压技术是多学科交叉所产生的一门高新技术,蒸煮挤压作为一种高温短时的加工方法,能够将输送、压缩、混合、蒸煮、杀菌、成型等多种操作单元同时完成。本实验优化了双螺杆机的加工工艺参数,DS56-Ⅲ型双螺杆挤压膨化机挤压腔内限流区的温度在125℃.含水率为40%、螺杆转速为215rpm,该条件下得到的最好产品膨化度为2.51,经过蒸煮挤压后的食品含水率为35%~37%。 相似文献
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本文对绿茶提取物的消除无氧性运动疲劳作用进行分析,对绿茶提取物功效进行调查,发现绿茶提取物能够提高运动员身体的运动强度,进一步增强运动员身体体质,缓解疲劳,提高抗压能力。通过摄入绿茶提取物可以促进运动员血清的活性的提高,能够缓解肌肉拉伤和修复无氧运动,避免身体骨骼的损伤和细胞膜的受损,同时能够减速身体蛋白质的分化,增强人体抗氧化酶的活动,从而促进身体的新陈代谢,提高运动员的氧自由基,从而增强运动员无氧运动的能力。 相似文献
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为明确渍前和渍后施用外源物对长江中下游地区渍水小麦生长和产量减损效应的差异,以当地主栽品种扬辐麦4号为供试材料,对渍前和渍后喷施外源调节物质(DDTC、GA、肥料元素和复配外源物)后花期渍水胁迫下小麦光合与叶绿素荧光特性、干物质积累与转运及籽粒产量进行了比较分析。结果表明,花期渍水胁迫后小麦光合性能减弱,光能利用和电子传递受阻,花后光合同化物积累减少,籽粒灌浆速率降低,粒重和产量下降。渍前和渍后喷施外源调节物质均可提高花期渍水小麦的叶片光合性能,增强叶片光能利用和电子传递能力,促进籽粒中花后光合同化物积累,提升籽粒灌浆速率以及粒重,从而增加籽粒产量。与渍后喷施相比,渍前喷施外源物能够有效提高花期渍水小麦的叶片光合速率、光化学效率和叶绿素含量以及降低热耗散;渍前喷施外源物能够有效促进花期渍水小麦的花后光合同化物积累,降低花前营养器官贮藏物转运;渍前喷施外源物能够有效提升花期渍水小麦的籽粒灌浆速率,促进粒重和籽粒产量增加。综上所述,与渍后喷施相比,渍前喷施外源调节物质能够有效提升花期渍水小麦光合性能,促进干物质积累与转运以及降低籽粒产量损失,从而减少渍水胁迫对小麦生长和产量的不利影响,其中... 相似文献
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Ph. Evon V. Vandenbossche P.Y. Pontalier L. Rigal 《Industrial Crops and Products》2009,29(2-3):455-465
The objective of this study was to evaluate the feasibility of an aqueous process to extract the residual oil from sunflower press cakes using a co-rotating twin-screw extruder. Two different configurations were tested: the expression from whole seeds followed by the aqueous extraction, in two successive apparatus or in the same one. For the aqueous extraction stage, the oil yield depended on the operating conditions including screw rotation speed, screw profile, and inlet flow rates of press cakes and water. Liquid/solid separation required the addition of a lignocellulosic residue (wheat straw), upstream from the filtration zone. However, even with maximum fiber inlet flow (around 20% of the inlet flow rate of the solid matters for the highest amount of wheat straw), drying of the cake meal did not improve. The lixiviation of the material was also incomplete. Oil yield was better when the expression and the aqueous extraction were conducted in the same extruder. For all the trials carried out using such a configuration, the corresponding cake meal contained less than 10% residual oil, and the total oil yield was 78% in the best operating conditions. Nevertheless, the contribution of the aqueous extraction stage was extremely limited, less than 5% in the best trial, partly due to a ratio of the water to the press cake too low. For the aqueous extraction stage, the oil was extracted in the form of an oil-in-water emulsion whose stability was minimized because of its low proteins content due to their thermo-mechanical denaturation during the expression stage. 相似文献
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Acrylonitrile-Butadiene-Styrene copolymers (ABS) reinforced with wood flour were investigated for rheological, mechanical
and thermal properties. Three grades of commercial ABS resin (high flow (HF-ABS), medium impact (MI-ABS) and super high impact
(SI-ABS) grades) were characterized using H-NMR and elemental analysis for the determination of co-monomer content. Wood flour
from Para rubber trees treated with N-2 (aminoethyl)-3-(aminopropyl) trimethoxy silane was blended with ABS in the melt blending
process using a twin-screw extruder. Wood flour contents used in this work were 0.0 %, 9.1 %, and 33.3 % wt. The composites
with higher acrylonitrile contents showed higher melt viscosity especially at the low shear rate. Carreau’s model was used
for curve-fitting. The extrudate swell ratio of the composites tended to increase at the shear rate of 10–500 s−1 and then decreased dramatically once the shear rate were further applied. Neat ABS and wood/ABS composites with higher butadiene
content illustrated a higher swelling ratio. The neat MI-ABS and composites showed the highest ultimate tensile strength and
modulus due to the butadiene content effect. As the wood flour loading was increased, the tensile modulus of all ABS composites
increased with the sacrifice of the tensile strength of composites. The elongation at break and impact strength were noticeably
the highest for wood/SI-ABS composites among all because of the effect of rubbery butadiene content. Thermal stability of
plastic in 9.1 % wood in HF-ABS composites was improved compared with the neat HF-ABS due to the low acrylonitrile content. 相似文献
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对2011~2015年连续4年开展的白背毛木耳栽培基质添加豆粕试验与示范结果进行调查,结果表明:在常规栽培料发酵结束后加入豆粕栽培白背毛木耳,会导致污染率急剧增加,添加6%豆粕的菌包废包率高达32.5%;在常规栽培料建堆时,将豆粕与麸皮、轻质碳酸钙等辅料一起加入到木屑中进行充分发酵,可以显著提高木耳产量和品质。需要特别指出的是,相对常规料栽培白背毛木耳,添加豆粕的栽培料发酵时间和翻堆次数需要适当增加,必须确保培养料发酵充分,否则容易出现培养料氨味过重,以致菌丝不吃料或吃料困难,影响栽培效果。 相似文献
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The melt-blowing technique is usually used for thermoplastic resins, not for non-thermoplastic materials. In this study, nonwoven fabric was successfully obtained by a cellulose solution through melt-blowing technique. The solution was prepared by a twin-screw extruder after mixing cellulose pulp with 1-Allyl-3-methylimidazolium Chloride ([AMIM]Cl). Nonwoven fabric exhibited typical characteristics of those from melt-blown thermoplastic resins. Some aspects of meltblowing process are discussed, such as cellulose concentration, temperature of extrusion die and hot air pressure. In experimental range, to obtain nonwoven web, cellulose concentration was below 15 wt%. Temperature of extrusion die and hot air pressure had great influence on the fabric. With the increasing of temperature of extrusion die and hot air pressure, the fiber changed thin and the fiber web became better, while the fiber diameter became thicker after increasing the cellulose concentration. Elevating the temperature of extrusion die, the degree of polymerization decreased, and the quality of the fiber webs declined. 相似文献
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Oktay Yilmaz Emre Kısasöz F. Seniha Guner Cagri Nart Kadir Kirkkopru 《Fibers and Polymers》2014,15(1):84-90
Several restrictions which are related to extruder machinery and nature of process material exist in the design of plastic extrusion dies. To this respect, it is very important to consider design criteria and limitations in order to operate extrusion dies at desired production rate and temperature. In the current study, flow field characteristics through a conical spiral mandrel die are analysed in detail by 3D Computational Fluid Dynamics (CFD) simulations. The effects of operating conditions such as production rate and temperature on pressure drop through the spiral mandrel die and the occurence of melt fracture are investigated. The temperature dependent viscosity versus shear rate data for grade QB79P (CarmelTech) polypropylene (PP) melt under study are measured by use of rotational and capillary rheometers. Stress terms in the momentum equations are modeled by Generalized Newtonian Fluid (GNF) Model. For this, Bird-Carreau Model is employed as the viscosity model for the polymer melt. 3D CFD analyses provide comprehensive data and understanding with regard to flow behaviour through complex extrusion dies. 相似文献
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《Journal of Cereal Science》2006,43(2):183-197
In a z-blade mixer, both shear and extensional deformations contribute to the development of dough structure. I effect of simple shearing versus z-blade mixing at similar levels of work input, on the microstructure and uniaxial extensional properties of two doughs prepared from flours of different strengths. With respect to microstructure, mixing initially increased the formation of coarse protein patches, leading to a heterogeneous dough structure with a high fracture stress (σmax) and significant strain hardening. These parameters decreased with prolonged mixing. This was accompanied by loss of glutenin macro polymer (GMP) wet weight and formation of a more homogenous microstructure. Prolonged mixing typically led to an over-mixed state. In contrast, prolonged simple shearing did not affect GMP content or strain hardening and gave enhanced shear banding. Confocal scanning laser microscopy revealed that short-term simple shearing induced structure formation in the direction of the shear flow for both flour types, followed by formation of shear-banded gluten structures both parallel and perpendicular to the direction of shear flow. Uniaxial extension of dough oriented parallel or perpendicular to the shear field did not reveal anisotropy. Apparently, the observed heterogeneity on a scale of ‘mm’ was not relevant for this type of rheology. Nevertheless, a relative weakening of dough strength (reduced fracture stress) was observed as a function of long-term shearing. This seems to be related to a local segregation effect caused by differences in visco-elasticity between the gluten phase and the starch granules. The results of this study reveal important features of the dough processing and underline the importance of not only work input, but also the type of deformation applied. 相似文献