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cooling by evaporation相关的网络例句

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与 cooling by evaporation 相关的网络例句 [注:此内容来源于网络,仅供参考]

The evaporation of some oils and their emulsifies was modeled with pan evaporation method, and the characteristics of the evaporation in different states was inspected. The equations of evaporation rate and the factors of inhibitory action of emulsification on evaporation have been obtained. The dynamics mechanism of emulsification has been discussed based on the observation and analysis of the characteristics of oil and water motion. The processes of spilt oils weathering have been integrated by the composition and states of oils in this prediction model.

本文主要是从目前研究的薄弱环节作为研究突破口,用浅盘蒸发法对原油及其乳化物的蒸发进行模拟,考察不同原油在不同阶段和乳化状态下的蒸发特征,得出蒸发速率方程及乳化对蒸发抑制作用因子;观测和分析油水运动规律,分析乳化动力学过程;以组成和状态是决定风化特征的主要因素和联系各风化过程的纽带这一思想为基础建立溢油风化预测模型。

In some conventional fan revolution speed control methods, variable control of the number of revolutions of a cooling fan is performed by a process comprising steps of detecting an actual temperature of cooling target fluid, ie fluid to be cooled by the cooling fan, such as hydraulic oil and circulating radiator cooling water for cooling an engine (such cooling water is hereinafter referred to as coolant), determining a target fan revolution speed by a system of a proportional integral control unit based on the difference between the actual temperature detected and a target temperature, and changing the fan revolution speed based on the target fan revolution speed so as to bring the actual temperature of the cooling target fluid down to the target temperature.

在一些传统风扇转速控制方法,控制变量的数目革命的一个冷却风扇,是由一个过程组成的步骤检测到一个实际温度冷却目标流体,即流体被冷却,由冷却风扇,如液压石油和散热器循环冷却水用于冷却发动机(如冷却水是以下简称为制冷剂),确定一个目标风扇转速由一个系统的比例积分控制单元基础上的差异,实际温度检测和目标温度,并改变风扇转速的基础上,针对风扇转速,使实际温度的冷却液指标下降到目标温度。

This paper hereby introduces the cooling process of the common 160,000 m^3-in-capacity atmospheric LNG storage tank in China, the preconditions and matters to which attention is paid upon the cooling of tank. It also discusses some commissioning techniques needed in the cooling process, including pressure control, cooling medium supply and its flow control, process monitoring and cooling rate control, etc. The paper points out that the displacement of pipelines is easily to be overlarge and flange leakage takes place frequently in the cooling process and it gives corresponding solutions.

为此,详细介绍了国内LNG接收站常用16×10^4 立方分尺常压LNG储罐的冷却过程,分析了LNG储罐冷却前应具备的条件及注意事项,讨论了LNG储罐冷却过程中的压力控制、冷却介质供应及流量控制、冷却过程的监控及冷却速率控制等调试技术,指出了冷却过程容易出现管线位移过大、法兰泄漏等问题,并给出了相应解决方法。

The influence of those main design parameterssuch as evaporation saturation temperature t_s、heat dissipated power Q and charge ofworking fluid L on the temperature distribution of evaporation"s bottom and boiling heat transfer inside the evaporation has been calculated and analyzed concretely. The method that uses channels to enhance boiling heat transfer of evaporation"s bottom has also been analyzed and calculated preliminarily.

具体计算和分析了蒸发饱和温度t_s、散热功率Q和充液量L等主要设计参数对蒸发段底面温度分布和蒸发段内部沸腾传热特性的影响,对用槽道强化蒸发段底面沸腾换热也做了初步的数值计算和分析。

Microbiotic crusts had a high capacity of evaporation than the shifting sand dunes. During the evaporation process of one week after rainfall, the total evaporation in artificial vegetation regions constructed in 1956, 1964, and 1981 were 6.05, 4.99 and 4.23 times respectively as the total evaporation in shifting sand dunes.

微生物结皮有着比流沙区更高的蒸发能力,在雨后一周的蒸发过程中,1956、1964和1981年人工植被区的总蒸发量分别是流沙区总蒸发量的6.05、4.99和4.23倍。

The result showed that the conventional and optimum design model of complex multi-evaporation had good universality. The new algorithm could be used to solve model more stably and more effectivly. The energy-saving effect was notable when all kinds of energy-saving measure were adopted and T0, Tk, tpj,Δti were optimized. In these conditions, the annual cost of optimum design decreased by 36.44% and 40.76% respectively than conventional design for the complex cross-feed and parallel-feed quadruple-effect evaporation system with solid separation. An optimum design software for multi-evaporation was developed, which had strong function, amity interface and easy maneuverability. This software may be applied to conventional and optimum design of multi-evaporation system under different conditions.

研究结果表明,复杂多效蒸发系统常规及优化设计的数学模型具有很强的通用性,求解模型的新算法稳定且高效;同时采用各种节能措施且对T_0、T_k、t_、Δti进行优化的系统节能效果最显著,对有固相析出的复杂错流、平流四效蒸发系统在上述情况下的优化设计比没有节能措施的常规设计可分别节省年总费用36.44%和40.76%;用可视化语言Visual Basic 6.0 编制的多效蒸发设计软件,功能强大、界面友好、使用方便,可用于多种流程、不同情况组合的多效蒸发系统常规及优化设计计算。

Bellows Gate Valves However, in large differential pressure operating conditions, evaporation pressure has eased, the evaporator load requirements of the fluid volume decreased, but the actual situation the contrary, in the suction superheat unchanged, due to evaporation pressure has eased, the evaporator outlet pressure be reduced accordingly, pressure changes above and below the diaphragm, causing the main valve opening increases for increased fluid; but in a small pressure operating conditions, evaporation pressure rise, evaporator load demand for fluid volume increased, but the reality is that in the suction gas superheat unchanged, due to evaporation pressure rise, a corresponding increase in the evaporator outlet pressure, pressure difference above and below the diaphragm smaller, so that the main valve opening decreased for the reduction of liquid volume; in variable load is all about.

但在大压差工况下,蒸发压力降低,蒸发器负荷需求的液量减少,但实际情况相反,在吸气过热度不变的情况下,由于蒸发压力降低,蒸发器出口压力相应降低,膜片上下的压差变大,使主阀开度增大,供液量增加;但在小压差工况下,蒸发压力上升,蒸发器负荷需求的液量增多,但实际情况是在吸气过热度不变的情况下,由于蒸发压力上升,蒸发器出口压力相应提高,膜片上下的压差变小,使主阀开度减小,供液量减少;在变负荷下亦如此。

However, in large differential pressure operating conditions, evaporation pressure has eased, the evaporator load requirements of the fluid volume decreased, but the actual situation the contrary, in the suction superheat unchanged, due to evaporation pressure has eased, the evaporator outlet pressure be reduced accordingly, pressure changes above and below the diaphragm, causing the main valve opening increases for increased fluid; but in a small pressure operating conditions, evaporation pressure rise, evaporator load demand for fluid volume increased, but the reality is that in the suction gas superheat unchanged, due to evaporation pressure rise, a corresponding increase in the evaporator outlet pressure, pressure difference above and below the diaphragm smaller, so that the main valve opening decreased for the reduction of liquid volume; in variable load is all about.

但在大压差工况下,蒸发压力降低,蒸发器负荷需求的液量减少,但实际情况相反,在吸气过热度不变的情况下,由于蒸发压力降低,蒸发器出口压力相应降低,膜片上下的压差变大,使主阀开度增大,供液量增加;但在小压差工况下,蒸发压力上升,蒸发器负荷需求的液量增多,但实际情况是在吸气过热度不变的情况下,由于蒸发压力上升,蒸发器出口压力相应提高,膜片上下的压差变小,使主阀开度减小,供液量减少;在变负荷下亦如此。因此热力膨胀阀在变工况下供液量的调节方面需进一步改进。

Among them, the first quarter of the market value of fund holdings evaporation 453.213 billion yuan, with the end of 2007 the market value of 2.400673 trillion yuan of holding 18.88 percent compared to大亏; the second quarter, holding the market value of 225.916 billion yuan evaporation, shrinking the market value of 20.24 percent margin; third quarter of the market value of evaporation of 259.503 billion yuan shares, value shrank by 20.6 percent rate; by three at the end of the shareholding and the December 16 closing price, the fund market value of 609.437 billion yuan holdings, since the fourth quarter the market value of re-evaporation of the fund holdings 679.89 billion.

其中,该基金持有的蒸发四五三二一三○○○○○○元市值第一季度,与2007年底2400673000000持有18.88亿美元,比大亏元的市场价值,第二季度,持有的225.916亿美元的市场价值人民币蒸发,减少了百分之利润20.24市场价值;有关的2595.03亿元的股票市值蒸发第三季度,价值缩减率百分之20.6;由三个股份制年底和12月16日收盘价计算,该基金市值6094.37亿元持有,第四季度以来的转口市场价值基金持股6798.90亿蒸发。

C or less of saturated compressed air into the dryer of the pre-cooling device, in the pre-cooling device in heat exchange with the ambient air, high temperature air pre-cooling fan part of the heat is taken away, after pre-cooling the compressed air into the to the pre-evaporator refrigeration system with secondary refrigerant vapor heat exchange, allowing the temperature dropped close to the refrigerant evaporation temperature, and flows through the pre-filter to remove large amount of liquid water, oil mist and dust.

小于等于80°C的饱和压缩空气进入干燥机的预冷器,在预冷器中与环境空气进行热交换,高温压缩空气的一部分热量被预冷风机带走,预冷后的压缩空气进入到制冷系统的前置蒸发器,与冷媒蒸气进行二次热交换,使本身温度降到接近于冷媒的蒸发温度,并流经前置过滤器除去大量的液态水,油雾和尘埃。

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