標(biāo)題: Titlebook: Chemical Reactor Design and Technology; Overview of the New Hugo I. Lasa Book 1986 Martinus Nijhoff Publishers, Dordrecht 1986 dynamics.en [打印本頁] 作者: ODE 時(shí)間: 2025-3-21 19:08
書目名稱Chemical Reactor Design and Technology影響因子(影響力)
書目名稱Chemical Reactor Design and Technology影響因子(影響力)學(xué)科排名
書目名稱Chemical Reactor Design and Technology網(wǎng)絡(luò)公開度
書目名稱Chemical Reactor Design and Technology網(wǎng)絡(luò)公開度學(xué)科排名
書目名稱Chemical Reactor Design and Technology被引頻次
書目名稱Chemical Reactor Design and Technology被引頻次學(xué)科排名
書目名稱Chemical Reactor Design and Technology年度引用
書目名稱Chemical Reactor Design and Technology年度引用學(xué)科排名
書目名稱Chemical Reactor Design and Technology讀者反饋
書目名稱Chemical Reactor Design and Technology讀者反饋學(xué)科排名
作者: 消音器 時(shí)間: 2025-3-21 20:47
Understanding the product lifecycle,icles are normally carried into and out of the unit by the liquid stream. In three-phase fluidized beds the solids are not transported out of the unit by the liquid stream, they are fed and withdrawn independently of the liquid stream [3]. Epstein [3] introduced an interesting classification for thr作者: Tracheotomy 時(shí)間: 2025-3-22 00:26 作者: 毛細(xì)血管 時(shí)間: 2025-3-22 06:27
Product lifecycle management systems,an fluids. Beasly and Clark [8] found that spatial variations in void fraction significantly influenced on the dynamic response of both fluid and solid temperature in the simulation of a packed bed for thermal energy storage. Snaddon and Dietz [9] took the structure of the bed into account when they作者: endoscopy 時(shí)間: 2025-3-22 08:45
Modelling and Simulation of Two-Phase Fluidized Bed Reactors,idized beds. Models for gas-solid reactions are treated separately. A brief survey is given of some advanced models which do not fall neatly within the usual range of assumptions or conditions. Emphasis throughout is not only on what is known, but also on challenges and new developments, including t作者: Alopecia-Areata 時(shí)間: 2025-3-22 13:06 作者: Alopecia-Areata 時(shí)間: 2025-3-22 20:34 作者: 無節(jié)奏 時(shí)間: 2025-3-22 21:22 作者: 的’ 時(shí)間: 2025-3-23 04:10
0168-132X processes to pave the way to a less vulnerable society, Because Chemical Reactor Design and Technology activities are at the heart of these required new techno978-94-010-8457-4978-94-009-4400-8Series ISSN 0168-132X 作者: 槍支 時(shí)間: 2025-3-23 06:36
Book 1986earchers that with or without immediate crisis, acting both in industry and academia, will face the challenge of developing technologies and processes to pave the way to a less vulnerable society, Because Chemical Reactor Design and Technology activities are at the heart of these required new techno作者: 可以任性 時(shí)間: 2025-3-23 11:39
Converting Methanol into Gasoline in a Novel Pseudoadiabatic Catalytic Fixed Bed Reactor,作者: Mingle 時(shí)間: 2025-3-23 17:24 作者: 符合國(guó)情 時(shí)間: 2025-3-23 22:02
Tracer Methods in Chemical Reactors. Techniques and Applications,echanisms of chemical and catalytic reactions, measurement of diffusion rates, etc. All these methods rely on perturbing the system under investigation and monitoring the system’s response to such perturbations. This response is then interpreted. Some conclusions can be obtained on a model-free basis, others are model dependent.作者: 西瓜 時(shí)間: 2025-3-24 00:50 作者: 無孔 時(shí)間: 2025-3-24 05:21
Kinetic Data Analysis and Parameter Estimation,e at reliable parameter estimates dependent on the operating variables of the reactor, like pressure, temperature, flow conditions etc. These parameters then will be used in a reactor model, i.e., a set of equations that describe the behavior of a reactor with sufficient accuracy.作者: BROOK 時(shí)間: 2025-3-24 07:44
Hydrodynamics of Trickle-Beds. The Percolation Theory, the description of the fluid flow pattern is very difficult because of the high number of intricate mechanisms that can control this pattern. The situation is so complex that, in many cases, we do not even know the essential hydrodynamic parameters that may affect the performance of the reactor.作者: 一小塊 時(shí)間: 2025-3-24 12:49
0168-132X on high energy consumption, accustomed to the use of cheap non-renewable energy and to the acceptance of eXisting imbalances between the resources and demands of countries. Despite all these stressing factors, our world is still hesitatins about the urgency of undertaking new and decisive research t作者: 敏捷 時(shí)間: 2025-3-24 17:44 作者: GRATE 時(shí)間: 2025-3-24 19:46 作者: faultfinder 時(shí)間: 2025-3-25 02:20
Catalyst Technology for Reactors used to Hydrocrack Petroleum Residua,Co or Ni) is also described. The catalyst is deactivated by coke and by metals. Furthermore, the reaction rate is often controlled by the rate of diffusion of the large carbonaceous molecules in the residua. All of these factors have been considered in mathematical simulations of the phenomena occuring in the catalyst.作者: Fabric 時(shí)間: 2025-3-25 03:52 作者: observatory 時(shí)間: 2025-3-25 07:38
Preparing for the PLM strategy,equations — one for each reaction — by use of the stoichiometric coefficients..The differential equations are solved numerically for the catalyst effectiveness factor by means of the orthogonal collocation method.作者: Moderate 時(shí)間: 2025-3-25 11:45
Preparing for the PLM strategy,e at reliable parameter estimates dependent on the operating variables of the reactor, like pressure, temperature, flow conditions etc. These parameters then will be used in a reactor model, i.e., a set of equations that describe the behavior of a reactor with sufficient accuracy.作者: etidronate 時(shí)間: 2025-3-25 19:31 作者: Axon895 時(shí)間: 2025-3-25 20:55 作者: 曲解 時(shí)間: 2025-3-26 03:36
Design Aspects of Industrial Fluidized Bed Reactors. Research Needs. Selected Subjects,beds, the size and velocity of gas bubbles are thus presented. Correlations and models to characterize entrainment of solids from fluidized beds and to provide guidelines for the design of gas distributors are also reviewed.作者: 極小 時(shí)間: 2025-3-26 05:07
Book 1986ergy consumption, accustomed to the use of cheap non-renewable energy and to the acceptance of eXisting imbalances between the resources and demands of countries. Despite all these stressing factors, our world is still hesitatins about the urgency of undertaking new and decisive research that could 作者: Charitable 時(shí)間: 2025-3-26 08:54
Chemical Reactor Design and Technology978-94-009-4400-8Series ISSN 0168-132X 作者: miracle 時(shí)間: 2025-3-26 13:08 作者: right-atrium 時(shí)間: 2025-3-26 19:40
Product lifecycle management systems,the liquid, a reactive solid or catalyst may be fluidized. BCR can be single staged or multi staged, batch or continuous with regard to the liquid (or slurry) phase. Continuous BCR can be operated cocurrently or countercurrently.作者: Moderate 時(shí)間: 2025-3-26 22:22
,e-Business — electronic business and PLM,umn with a fixed bed of catalyst particles through which liquid flows in the form of films, droplets and rivulets. Gas moves cocurrently; sometimes counter-current flows are also used. Usually one reactant is introduced in the liquid phase and the other in the gas phase.作者: 尊重 時(shí)間: 2025-3-27 04:49
Antti Saaksvuori,Anselmi Immonenroductivity, lowering the process selectivity and reducing the life of the catalyst. Among these include the oxidation of ethylene, benzene, C. hydrocarbons and methanol, the ammoxidation of propylene, methanol synthesis (Lurgi), the hydrochlorination of methanol and steam reforming of natural gas and naphtha.作者: 手勢(shì) 時(shí)間: 2025-3-27 05:50
Preparing for the PLM strategy,restrictions against mass and heat transfer in the interior and in the gas film surrounding the particle, and it accepts a general type reaction rate expression such as a power law expression or a Langmuir-Hinshelwood expression. The model is reduced to a number of coupled second order differential 作者: angina-pectoris 時(shí)間: 2025-3-27 11:45 作者: 爭(zhēng)論 時(shí)間: 2025-3-27 14:30 作者: 破裂 時(shí)間: 2025-3-27 20:25 作者: 協(xié)議 時(shí)間: 2025-3-28 02:00
Preparing for the PLM strategy, for many catalytic and noncatalytic reactions involving solid particles and a gas or liquid. However, gas fluidized bed reactors present a challenge to the engineer because their patterns of gas-solid contacting and mixing are complex and difficult to characterize. Contacting and mixing are intimat作者: 得體 時(shí)間: 2025-3-28 02:34 作者: 鄙視讀作 時(shí)間: 2025-3-28 08:36 作者: Bph773 時(shí)間: 2025-3-28 11:07
Understanding the product lifecycle,[3], Baker [4] and Muroyama and Fan [5]. Epstein [3] distinguished in particular the difference between three-phase fluidized beds and slurry reactors. In slurry reactors the size of the solid particles is normally smaller than 0.1 mm while in three-phase fluidization the particle diameter is bigger作者: Feckless 時(shí)間: 2025-3-28 17:00 作者: 蘑菇 時(shí)間: 2025-3-28 21:08
Product lifecycle management systems,the liquid, a reactive solid or catalyst may be fluidized. BCR can be single staged or multi staged, batch or continuous with regard to the liquid (or slurry) phase. Continuous BCR can be operated cocurrently or countercurrently.作者: Myocyte 時(shí)間: 2025-3-29 00:35
,e-Business — electronic business and PLM,from catalytic hydrogenation of edible oils, coal hydrogenation, Fischer- Tropsch reactions to biological reactors (e.g. single cell proteins) and polymerization reactors. Doraiswamy and Sharma [1] identified over 50 different processes in which slurry reactors have been used and more applications a作者: FOLLY 時(shí)間: 2025-3-29 03:54
https://doi.org/10.1007/b138258thermodynamics,...) and by the contacting pattern. The importance of this contacting pattern is quite obvious in the case of multiphase reactors like trickle-bed reactors. Reactants are indeed present in both fluid phases and reactions occur at the contact of the catalytic solid phase. Unfortunately作者: 最后一個(gè) 時(shí)間: 2025-3-29 07:51
,e-Business — electronic business and PLM,umn with a fixed bed of catalyst particles through which liquid flows in the form of films, droplets and rivulets. Gas moves cocurrently; sometimes counter-current flows are also used. Usually one reactant is introduced in the liquid phase and the other in the gas phase.作者: 信徒 時(shí)間: 2025-3-29 13:36 作者: 有效 時(shí)間: 2025-3-29 18:24 作者: fringe 時(shí)間: 2025-3-29 21:44 作者: Blanch 時(shí)間: 2025-3-30 01:15
https://doi.org/10.1007/978-94-009-4400-8dynamics; energy consumption; engine; flow; fluidized bed; heat transfer; hydrodynamics; measurement; methan作者: 一起 時(shí)間: 2025-3-30 07:53
978-94-010-8457-4Martinus Nijhoff Publishers, Dordrecht 1986作者: Soliloquy 時(shí)間: 2025-3-30 10:36 作者: 組成 時(shí)間: 2025-3-30 14:21
https://doi.org/10.1007/b138157Attempts to describe mixing in chemical reactors is one of the most striking examples which show that Chemical Reaction Engineering is not a mere combination of chemistry and applied physics, but an original scientific discipline which has developed its own concepts .作者: 恃強(qiáng)凌弱的人 時(shí)間: 2025-3-30 18:10
https://doi.org/10.1007/b138258This review deals with the engineering aspects of trickle-bed reactors as it applies to general design, scale-up, pilot plant design and operation, and reactor troubleshooting. Also, research needs in trickle-bed technology are discussed.作者: extinguish 時(shí)間: 2025-3-30 23:03 作者: Brochure 時(shí)間: 2025-3-31 02:19 作者: 干旱 時(shí)間: 2025-3-31 05:39
Engineering Aspects of Trickle Bed Reactors,This review deals with the engineering aspects of trickle-bed reactors as it applies to general design, scale-up, pilot plant design and operation, and reactor troubleshooting. Also, research needs in trickle-bed technology are discussed.作者: 染色體 時(shí)間: 2025-3-31 10:51 作者: anniversary 時(shí)間: 2025-3-31 13:22 作者: ambivalence 時(shí)間: 2025-3-31 20:08 作者: 浸軟 時(shí)間: 2025-3-31 23:52 作者: itinerary 時(shí)間: 2025-4-1 05:49
Transport Restrictions in Catalyst Particles with Several Chemical Reactions,restrictions against mass and heat transfer in the interior and in the gas film surrounding the particle, and it accepts a general type reaction rate expression such as a power law expression or a Langmuir-Hinshelwood expression. The model is reduced to a number of coupled second order differential 作者: 得罪 時(shí)間: 2025-4-1 07:59 作者: ascetic 時(shí)間: 2025-4-1 11:20 作者: 公豬 時(shí)間: 2025-4-1 15:35
Tracer Methods in Chemical Reactors. Techniques and Applications,apillary permeability of the microcirculation in medicine and by flow visualization in channels and around airplane wings in mechanical and aerospace engineering. Other applications are flow and transport measurements in rivers in hydrology, transport measurements of pollutants in soils in civil eng作者: 保存 時(shí)間: 2025-4-1 19:39 作者: 罐里有戒指 時(shí)間: 2025-4-2 02:17 作者: Diluge 時(shí)間: 2025-4-2 06:44
Design Aspects of Industrial Fluidized Bed Reactors. Research Needs. Selected Subjects,s and their effect on the quality of fluidization; (2) bubble size control through small solid particle size or baffles; (3) particle recovery by means of cyclones; (4) heat transfer tubes; (5) solids circulation systems; (6) instrumentation, corrosion and erosion, mathematical models, pilot plants 作者: Medicaid 時(shí)間: 2025-4-2 07:19
Three-Phase Fluidized Bed Reactors,[3], Baker [4] and Muroyama and Fan [5]. Epstein [3] distinguished in particular the difference between three-phase fluidized beds and slurry reactors. In slurry reactors the size of the solid particles is normally smaller than 0.1 mm while in three-phase fluidization the particle diameter is bigger
