1) rapid drying process
快速受热
1.
Laplace Transfer Methods are applied to coupled differential equations for heat and moisture transfer in half space porous materials during rapid drying process.
针对多孔材料快速受热物理过程传热和传质藕合微分方程组,用拉普拉斯变换法进行求解,将温度和湿度藕合方程转化为温度度或湿度的常微分方程,给出了半无限体藕合方程温度或湿度拉氏变换的普遍解。
2) tachyphylaxis
[英][,tækifai'læksis] [美][,takəfɪ'læksɪs]
快速耐受
3) rapid heating
快速加热
1.
For a kind of low carbon micro-alloyed steel,a thermal simulation test was conducted with samples of F+B+P microstructure and the effects of its cold deformation at room temperature on the distribution,size and composition of precipitates were investigated via a technological process for rapid heating and short holding time.
实验用试样的原始组织为铁素体、珠光体加少量贝氏体,采用一种快速加热短时保温的工艺方法探讨室温变形的作用。
2.
During the rapid heating for limestone calcination,a new platinum-membrane reactor(PMR),which accurately weighs the sample and acquires temperature of particles,was used.
在加热过程中,应用一种新型的快速加热装置——铂膜反应器,及时准确地获得样品质量和颗粒温度,来研究石灰石的煅烧分解,并对石灰石加热速率高达750℃/s下的分解反应特性,及其对分解后产生的氧化钙吸收CO2和脱硫的化学反应特性进行了研究。
3.
Based on studying the phase diagram of the Ti-Al binary system, the microstructure types and continuous cooling transformations of the TiAl-based alloys, and the heat treatment practices and effects, a new rapid heating cyclic heat treatment technology with the characteristics of rapid heating, holding in single α phase region, short holding time and relatively slow cooling was proposed.
在研究Ti Al二元相图及合金元素的影响、TiAl基合金显微组织类型与连续冷却转变、热处理实践及效果的基础上 ,提出了快速加热循环热处理新工艺 ,该工艺的特点是 :加热速度快 ,单相区保温 ,保温时间短 ,冷却速度相对较慢。
4) Fast pyrolysis
快速热解
1.
Experimental research on biomass fast pyrolysis with discontinuous feed for production of bio-oil;
间歇式给料的生物质快速热解制油的实验研究
2.
A combination process of straw steam-explosion and solid-state fermentation with fast pyrolysis for producing liquid fuels;
秸秆蒸汽汽爆、固态发酵处理结合快速热解制液体燃料
3.
The configuration analysis of the adsorption isotherm of nitrogen in low temperature with the lignite char produced under fast pyrolysis;
快速热解褐煤焦的低温氮吸附等温线形态分析
5) flash pyrolysis
快速热解
1.
Effects of temperature on products of flash pyrolysis of lignite in a spouted-entrained bed;
喷动载流床中温度对霍林河褐煤快速热解产物的影响
2.
Combining with the superiority of bubbling fluid bed with shallow bed depth and the characteristics of biomass pyrolysis, the fluid bed pyrolysis reactor of biomass flash pyrolysis was designed and manufactured to implement experiment of producing biomass pyrolysis oil by biomass flash pyrolysis.
根据浅床层鼓泡流化床的特点以及生物质的热解特性,研制出生物质快速热解的流化床热解反应器,并进行生物质快速热解制取生物质油的试验研究。
3.
In this paper,the research status and progress of coal pyrolysis and utilization have been reviewed,technologies of coal flash pyrolysis,oriented catalytic conversion and producing valuable chemicals from coal pyrolysate were focused.
在对国内外煤热解研究现状分析的基础上,对煤的快速热解技术、定向催化转化技术和煤热解物制备化学品技术进行了探讨,提出了由煤热解物制备高价值化学品的新思路,并对煤热解及由煤热解物制高价值化学品的发展趋势和面临的一些问题提出了看法与建议。
6) rapid pyrolysis
快速热解
1.
Experimental research on rapid pyrolysis of xylan;
木聚糖快速热解试验研究
2.
Based on the experiments stimulating the condition of blast furnace operation by plasma and Py-FTIR,the influence of combustion-supporting agent(KMnO4、Fe2O3、MnO2 and CaO) as catalyst on rapid pyrolysis of the mixer coal in pulverized coal injection on blast funace is studied.
选取KMnO4、Fe2O3、MnO2和CaO作为助燃催化剂,采用H2/Ar等离子体热解试验装置和快速升温热解红外连用试验装置来模拟煤粉在高炉喷吹条件下的快速热解过程,对混合煤粉的快速热解过程进行了研究,得到了助燃催化剂与煤的裂解程度(裂解气体收率)、裂解气体成分的关系,对助燃催化剂的催化裂解机理进行了讨论。
3.
The effect of CaO catalysts on tar cracking in a rapid pyrolysis fixed bed reactor was studied in order to cut down the yield of tar in pyrolysis or gasification process.
为降低煤在热解、气化过程中的焦油产量 ,在一快速热解固定床反应器中考察了氧化钙催化剂的加入对焦油裂解反应的影响 ,研究结果表明 :在相同反应条件下 ,所选三种氧化钙催化剂中以 Ca O- 3的焦油裂解活性为最大 ,它们的焦油裂解活性顺序为 :Ca O- 3>Ca O- 2 >Ca O- 1 。
补充资料：对流受热面换热
对流受热面换热
heat transfer at convection heating surfaces
dUll一U Sh0Urem一on hU0nre对流受热面换热(heat transfer at。onveetionheating surfaees)热量由受热面一侧的热流体以对流方式传给另一侧的冷流体的过程。锅炉对流受热面换热计算的基本方程为换热方程式和热平衡方程式。 换热方程式换热过程中对流受热面传递的热量Q与冷、热流体间的平均温差山和受热面积H成正比，换热方程式可写成:Q~KH山，kJ/h。锅炉对流受热面的换热计算.通常以每千克燃料为基准，因此换~~一、__一一、，_KH山，，，.、._热方程式又可表示为:Q~竺若竺，kJ/kg，式中药n‘~’协~~J~“’/子’伟B，’.”’吧’~’一J为锅炉计算燃料消耗量，kg/h;其余各项分别介绍如下. (1)传热系数K〔kJ/(m，·h·℃)]:表示温差为1℃、受热面积为lm2条件下每小时的传热量。对于锅炉中常见的各种光滑管受热面的传热系数均可用多层平壁的传热系数公式来表示:1.氏一十六尸十“1匆 民‘1+~护‘十— 人aZkJ/(mZ .h.℃)l一人一凡式中a，和aZ为加热介质对管壁和管壁对受热介质的换热系数;a，和入为管子外表面上灰垢层的厚度和导热系数;占，和人，为管壁的厚度和导热系数;氏和人为管子内表面上水垢层的厚度和导热系数。烟气对管壁的换热系数al可写成:a，一右(久十ar)，式中ac和a，为对流换热系数和辐射热系数;泞为利用系数，它是考虑由于烟气对受热面冲刷不完全而使吸热减少的修正系数。ac与许多因素有关:如气流的速度和温度、一定的线性尺寸、管子布置方式、受热面种类、烟气流经受热面的性质(纵向流、横向流或斜向流)以及流通介质的物理性质等。ar与烟气流的温度、黑度及受热面外壁温度、黑度有关。综上所述，传热系数是一个与过程有关的物理量，其值取决于参与换热的两种流体的物理性质、运动状态、受热面的结构形式及布里方式等。 (2)温差山(’C):参与换热的两种流体在整个受热面中的平均温差。温差大小与两种流体相互间流动方向有关。如果一种流体的温度在受热面范围内保持不变，则温差与两种流体相互间的流动方向无关。冷、热流体彼此反向平行流动的受热面连接方案，称为逆流，而彼此同向平行流动的，则称为顺流。
说明：补充资料仅用于学习参考，请勿用于其它任何用途。
参考词条