packed+bed+reactor+design+calculations

... different design levels of conversion on the sizes of the reactor and the condenser. A 90% conversion design produces a 1.68-m 3 reactor Figure 2.25 Matlab program for autorefrigerated reactor. 2.7 ... the conversion is only 85% in the first reactor. If the 2-CSTR design has more potential control problems than the 1-CSTR design, we would expect the 3-CSTR design to be even worse. This is precisely ... each reactor is further reduced (14.4 m 3 with diameter 2.09 m), so the total reactor volume of the thr ee vessels is 43 m 3 , which is only 16% of the volume of the reactor in the 1-CSTR design. ...

Ngày tải lên: 01/04/2014, 10:24

... FIVE Introduction to Reactor Design Fundamentals for Ideal Systems 260 Introduction 260 A General Approach 262 Ideal Isothermal Reactors 264 Numerical Methods for Reactor Systems Design 279 Reversible ... Selectivity in Reactors 351 Relationship Between Conversion, Selectivity, and Yield 353 Plug Flow Reactor 362 Heterogeneous Tubular Reactor 371 Design Equation for Systems of Variable Density 372 Design ... 434 Batch Reactor 457 Plug Flow Reactor 472 Autothermal Reactors 477 Conversion in Ammonia Synthesis 478 Two-Dimensional Tubular (Plug Flow) Reactor 492 Pressure Drop (∆P) in Tubular (Plug Flow) Reactors...

Ngày tải lên: 01/04/2014, 10:25

... 1965. B. References Pertinent to the Engineering or Reactor Design Aspects of Kinetics 1. R. Aris, Introduction to the Analysis of Chemical Reactors, Prentice-Hall, Englewood Cliffs, N.J., 1965. 2. ... and J. C. R. Turner, Chemical Reactor Theory, Second Edition, Cambridge University Press, London, 1971. 6. H. S. Fogler, Tlw Elements of Chemical Kinetics and Reactor Calculations, Prentice-Hall, ... fertile environment for research and textbook writing in the area of chemical kinetics and reactor design. The text by O. A. Hougen and K. M. Watson represents a classic pioneering effort to...

Ngày tải lên: 01/04/2014, 10:25

... HCCO+O=HCO+CO CHEMICAL REACTIONS AND DESIGN OF CHEMICAL REACTORS 5 (a) Tubular reactor, plug flow (b) Tank reactor, mixed flow. The basic concepts of these reactors are shown in Figure 1.2 ... catalyst is charged into a fixed -bed reactor. The reactor structure is designed in such a way that the reaction fluid is uniformly distributed over the catalyst bed with a low and uniform pressure ... facilitate the generalized design strategy of reactors. The reactor types and applications are introduced in subsequent sections. 4.1.1 HOMOGENEOUS REACTORS Reactors which handle reacting...

Ngày tải lên: 01/04/2014, 10:29

... are either perfectly mixed tanks or packed bed and pipeline reactors with no mixing. The changes in conversion with reaction time or reactor length are described and the advantages and problems ... performance of a tubular reactor, a packed bed, or perhaps a new type of contactor for the same reaction. Fundamental kinetic parameters obtained from a small fixed -bed reactor might lead to consideration ... vented from the reactor while products accumulate in the solution. A type of continuous reactor with performance similar to a batch reactor is the plug-flow reactor, a tubular or pipeline reactor with...

Ngày tải lên: 01/04/2014, 10:31

... Three-Phase Reactors 412 11.2.1 Trickle -Bed Reactors 412 11.2.2 Gas-Fed Slurry Reactors 413 11.3 Moving Solids Reactors 413 11.3.1 Bubbling Fluidization 416 11.3.2 Fast Fluidization 417 11.3.3 Spouted Beds ... a constant-pressure reactor) , V(t) Variable cross section, A c (z) Fed batch reactors, Q in 6¼ 0 Transpired wall reactors Nonideal batch reactors may have spatial variations in concentration Nonideal tubular reactors ... result. If local stoichiometry is preserved, no more than M reactor design equations need to be solved to determine all 68 CHEMICAL REACTOR DESIGN, OPTIMIZATION, AND SCALEUP follow first-order kinetics...

Ngày tải lên: 01/04/2014, 10:31

Ngày tải lên: 01/04/2014, 10:33

... kinetics and reactor design / J.B. Butt. ± 2nd ed., rev. and expanded. p. cm. ± (Chemical industries ; v. 79) Includes index. ISBN 0±8247±7722±0 (alk. paper) 1. Chemical kinetics. 2. Chemical reactors. ... pro- blems that arise during the development and implementation of procedures for chemical reactor and process design on a large scale. If we must give names to these two extremes, we might call the ... related topics of interest are given by Froment and Bischo (G.F. Froment and K.B. Bischo, Chemical Reactor Design and Analysis, John Wiley, New York, 1979) and in a review by Ray [W.H. Ray, J. Macromolec....

Ngày tải lên: 01/04/2014, 10:37

Ngày tải lên: 29/06/2014, 00:20

Ngày tải lên: 10/08/2014, 20:20

Ngày tải lên: 10/08/2014, 20:20

Ngày tải lên: 10/08/2014, 20:20

Ngày tải lên: 10/08/2014, 20:20

Ngày tải lên: 10/08/2014, 20:20

Ngày tải lên: 10/08/2014, 20:20

Ngày tải lên: 10/08/2014, 20:20

Ngày tải lên: 05/09/2013, 16:11

Ngày tải lên: 18/12/2013, 09:19

... NG NGUY NGHIÊN CU NG DNG CÔNG NGH MBBR (MOVING BED BIOFILM REACTOR)  X C THI SN XUT BIA Chuyên ngành : Công ngh ng MSHV : ... system encountered many difficulties. This research was studied on application of Moving Bed Biofilm Reactor for brewing wastewater treatment, given more options for upgrading existing wastewater ... nh tính cn thit khi la ch  tài: “Nghiên cư ́ u ứng dụng công nghệ MBBR(Moving Bed Biofilm Reactor) để xử lý nước thải sản xuất bia”. 2. Tng quan 31 s c các vi sinh...

Ngày tải lên: 26/02/2014, 13:08

... biofilm khác, vì vy nó tu kin thun li cho quá trình x Hình 2.8b. Anoxic reactor Hình 2.8a. Aerobic reactor 2. Tng quan 29 Hình 2.9. Các loại giá thể K1, K2, K3, Biofilm ... NG NGUY NGHIÊN CU NG DNG CÔNG NGH MBBR (MOVING BED BIOFILM REACTOR)  X C THI SN XUT BIA Chuyên ngành : Công ngh ng MSHV : ... Chuyên ngành : Công ngh Môi trng 1- TÊN  TÀI: Nghiên cu ng dng công ngh MBBR (Moving Bed Biofilm  x lc thi sn xut bia. 2- NHIM V LUN VN:  Lp mô hình nghiên...

Ngày tải lên: 20/03/2014, 03:21