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The author analysis the inherent link between the circular economy and the adjustment of the industrial structure, then adjust the industrial structure through transforming the value chain at the micro-enterprise level and building eco-industrial park at the meso-level based on the micro, meso and macro levels of the circular economy. All the transformation is to promote the development of circular economy and to change China's economic development model. Doing this, we want to change the traditional products economic

本文从系统的角度,分析发展循环经济与产业结构调整之间的内在联系,以循环经济发展的微观、中观、宏观三个层次为基础,通过微观企业层面上改造价值链和中观层面上构建生态工业园来调整产业结构,推进循环经济发展,改变我国的经济发展模式,使我国从传统的产品经济模式,向资源经济模式转换,进而实现循环经济在整个社会层面上的大循环,从而找到在全社会建立一种以循环经济发展模式为核心的可持续发展的社会-经济系统的具体实践。

ABSTRACT Global carbon cycle is a very important issue in the study of global climate change. Forest ecosystem carbon cycle is one of the important part of global carbon cycle, but at the present time there are considerable uncertainties in the research of global carbon cycle, which also exist in forest ecosystems carbon cycle research, especially in the estimation of carbon storage of region forest ecosystems and CO〓 fluxes exchanging with other systems.

全球碳循环是全球气候变化研究的核心问题之一,森林生态系统碳循环是全球碳循环的重要组成部分,目前在全球碳循环的研究中还存在很大的不确定性,这种不确定性同样存在于森林生态系统碳循环的研究中,尤其表现在对区域森林生态系统碳库大小及其与大气CO〓交换通量的估计上。

The experimental results show that the impeller with high ratio of circulation to shear is suit to be used in circulation control process, the impeller with low ratio of circulation to shear is suit to be used in shear control process, and the impeller with medium ratio of circulation and shear is suit to be used in circulation and shear co-control process.

实验结果表明,循环与剪切配比高的桨叶适用于循环控制的混合过程,循环与剪切配比低的桨叶适用于剪切控制的混合过程,而循环与剪切配比适中的桨叶适用于循环与剪切共同控制的混合过程。

Your code should never have multiple nested loops (a loop inside a loop inside a loop).

你的代码永远都不要有多个嵌套循环循环之内的循环循环内还有循环)。

The plastic deformation induced due to cyclic rotation of principal stress axes alone can be in the same magnitude as that due to shear with fixed principal stress axes. 2 The volumetric strain due to shearing of cyclic rotation of principal stress axes is found to be composed of a reversible dilatancy component and an irreversible dilatancy component. The former is characterized by its reversibility and is independent of past shear history, the latter by its irreversibility increases with the increase of cycle number yet its increase rate decreases with its accumulation. 3 The obvious non-coaxiality between directions of the principal stresses and principal strain increments is found and its degree depends largely on the change of shear stress component. 4 The intermediate principal stress has considerable effects on the deformation behavior of sands in the condition of cyclic rotation of principal stress axes. The accumulation rate of the irreversible dilatancy component increases with the increase of the intermediate principal stress parameter.

具有初始各向异性的砂土在纯应力主轴循环旋转排水条件下的主要变形规律为:①纯应力主轴循环旋转可产生与应力主轴固定单调剪切处于同一数量级的塑性变形;②纯应力主轴循环旋转引起的剪切体变包含可逆性剪切体变分量和不可逆性剪切体变分量两部分,其中可逆性剪切体变分量在一周内可完全恢复,基本与应力历史无关;不可逆性剪切体变分量随循环周数的增加呈单调增加,且增加速率随其自身累积值的增大呈减小趋势;③应变增量主轴与应力主轴之间的非共轴现象显著,且在一周内具有分段性;④中主应力对应力主轴循环旋转条件下砂土的变形特性有重要影响,不可逆性剪切体变分量的累积速率随中主应力系数的增加而增加。

The Kalina cycle which uses ammonia-water mixture as the working-medium, has the characteristics of lower vaporization temperature and non-isothermal heat absorption. Therefore, the Kalina cycle is used in low temperature waste heat recovery based on introduction of operating principle. The primary parameters of Kalina and Rankine cycle are optimized by mean of genetic algorithm respectively, and the net output power of the two cycles is compared on the same condition.

卡林纳循环采用氨水混合物作为工质,具有气化温度低和非等温吸热的特点,因此,在简要介绍其工作原理的基础上将其应用于中低温余热回收,采用遗传算法对卡林纳循环和常规朗肯循环的主要参数进行了优化,在相同的余热条件下,比较了卡林纳循环和常规朗肯循环的净输出功率。

The energy balance equations and exergy balance equations of heat exchanger and power equipment in the combined power cycle were established.Taking condensation temperature of Rankine cycle, inlet and outlet pressure of turbine of Rankine cycle, inlet and outlet pressures of turbine of LNG cycle as key parameters, the influences of these parameters on the thermal efficiency and exergy efficiency of the combined power cycle were analyzed.

建立了混合动力循环中换热和动力设备的能量平衡方程和可用能平衡方程,并以朗肯循环冷凝温度、朗肯循环透平进出口压力、液化天然气循环透平进出口压力为关键参数,分析了上述关键参数对混合动力循环热效率和可用能效率的影响。

The energy balance equations and exergy balance equations of beat exchanger and power equipment in the combined power cycle were established. Taking condensation temperature of Rankine cycle, inlet and outlet pressure of turbine of Rankine cycle, inlet and outlet pressures of turbine of LNG cycle as key parameters, the influences of these parameters on the thermal efficiency and exergy efficiency of the combined power cycle were analyzed.

建立了混合动力循环中换热和动力设备的能量平衡方程和可用能平衡方程,并以朗肯循环冷凝温度、朗肯循环透平进出口压力、液化天然气循环透平进出口压力为关键参数,分析了上述关键参数对混合动力循环热效率和可用能效率的影响。

The invention relates to a processing method of preventing frostbite and restarting of hydrogen electric pile, whose characteristic lies in the treating processes includes: When the electric pile turns off, the unsaturated fuel gas or the nitrogen, through the circle boast to clean the dissociate water; drying the MEA film module to keep the water content below the stipulated temperature which does not ice up; then the recycle gas through a wet exchanger to dry and the dried gas is continue used in the dry pile step; when restarting the electric pile, the recycle gas must heats then through the pile to elevate the temperature, then heats the fuel gas and the oxidant of the gas source, through the weting of the wet exchanger enters to the calefactive pile, enhances the wet step of the film module in the pile, starts the power output of the pile.

本发明涉及一种氢电堆的防冻和重新启动时的处理方法,其特征在于处理过程包括:电堆停机时,将水蒸气不饱和的燃料气体或氮气,通过循环吹扫除去电堆的游离水;干燥其中的MEA膜组件,使膜组件含水量降低到规定低温下不结冰的程度;而后再令循环气体通过一个湿交换机将循环气体干燥,以及被干燥后的循环气体继续用来干燥电堆的步骤;在电堆重新启动时,须将循环气体加热后通过电堆,使电堆升温,然后再将气源的燃料气及氧化剂加热,通过湿交换机加湿后进入已升温的电堆,提高电堆中膜组件的湿度的步骤,开始电堆的功率输出。

Finally, the effect of the complete recycling use of distilled effluent on ethanol fermentation was examined in order to save the cost for the treatment of waste distillage and promote cleansing production. Based on the data of 13 circulations, although the average fermentation time needed to be extended to 30~40 hours, over 12.5% ethanol was achieved, at the same time, residual reducing sugar and total sugar were maintained below 0.70% and 0.90%, which indicates that the negative effect of the completely recycling use of waste distillage was limited, and the waste distillage can be completely recycled within the fermentation system.

在此基础上,从减轻废糟液处理负荷,实现清洁生产的需要出发,进行了无种子罐条件下酒精蒸馏废液直接全循环使用的自絮凝颗粒酵母酒精连续发酵实验研究,十三次全循环运行得到的实验数据,与无废液循环的实验结果相比,虽然平均发酵时间略增至30h~40h,但发酵终点酒精浓度仍达到12.5%以上,残还原糖和残总糖分别在0.70%和0.90%以下,说明循环积累物对发酵的影响有限,废糟液直接全循环使用的工艺技术路线可行。

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