PPT-Production of Acrolein from the Catalytic Oxidation of Propylene in a Fixed Bed Reactor

Team 1 Michael Glasspool Sarah Wilson Nicole Cosgrove Production Goals Produce 30000 Metric Tonnes year Operate for 350 days year Produce acrolein at 00177 kmol s Allowable Process Conditions. 1. Ref: . Seider. et al, Product and process design principles, 3. rd. ed., Wiley, 2010.. . Temperature Control. Temperature control is an important consideration in reactor design.. . Adiabatic operation is always considered first because it provides the simplest and least-expensive reactor.. Processing(TKK-2136). 14/15 Fall semester. Instructor: Rama Oktavian. Email: rama.oktavian86@gmail.com. Office Hr.: . M.13-15, Tu. 13-15, W. 13-15, Th. 13-15, F. 09-11. Outlines. . 1. . Catalytic reforming. nanocrystals toward glucose oxidation. Wang, J.; Gong, j.; . Xiong. , Y.; Yang, J.; . Gao. , Y.; Liu, Y.; Lu, X.; . Zhiyong. Tang, Z. . Chem. . Commun. ., 2011, . 47, 6894–6896. . P.RAMANA MURTHY. Kazem.R.Abdollah. Synthetic Organic Chemicals. 1. Introduction. Synthetic organic chemicals are produced by the transformation of carbonaceous . feedstocks. into functionalized molecules through one or more chemical reactions. Such transformations are accomplished at vast industrial scales and the resulting products permeate every aspect of modern society.. Petrochemicals. Islamic University in . Madinah. Department of Chemistry. Prepared By. Dr. Khalid Ahmad Shadid. Chemistry department – Islamic university in . madinah. . 1. Petrochemicals: Chemical compound or Elements derived partially or entirely from petroleum or natural gas and are intended for Chemical markets. . 15. TH. FEB 2012. PRESENTED BY. HARIDASAN V A. CAPACITY AND TECHNOLOGY. Plant capacity : 290,000 MT of Cumene per year. On stream factor : 8,000 Hours. Hourly production rate : 36.25 MT/hr of Cumene . and . poisons. Rates of Reaction. Catalytic Converters. Exhaust fumes contain. CO – . due . to incomplete combustion of hydrocarbons. NO & NO. 2. – . N. 2. . in air is oxidised at high temperatures. Chemical Basis for Catalytic Activity. Enzymes promote . transition state. (. TS. ).. Transition state favored by tight binding. .. Figure depicts anti-CCR-5 “protease”.. Strategy. : Raise against TS analogs.. Real CSTRs. R. elatively high reactant . conc. at entrance. Relatively low . conc. in stagnant regions, called dead zones (corners & behind baffles) . Dead . Zone. Dead . Zone. Short . Circuiting. . Nuclear Energy Fundamentals . Module 4: Nuclear Reactor Design . Module Objectives . After the completion of this module, the student will be able to: . • . Explain the fuel assembly geometry, specifications and material. . 2. . Materials in . pwr. In this Chapter. Major component and degradation mechanisms. Design and Materials of PWR Components . Corrosion-Related Issues in PWR . Major Components . Reactor . pressure vessel . measurement of Daya Bay Experiment Haoqi Lu Institute of High Energy physics, China On behalf of the Daya Bay collaboration EPS - HEP 2019, July 10 - 17, Ghent, Belgium 1 2 Daya Bay Daya Bay Exp Department of Petroleum Studies. AMU Aligarh- 202002, UP, India. Email: sm_kamil@rediffmail.com. PK 605: Reactor Analysis and Design (3L-1T, 4 Cr.) . . Research Institute of Nuclear Reactors, State Scientific Centre, Joint-Stock Company . (. RIAR JSC. ). A.L. . Izhutov. , A.L. . Petelin. , . Yu.M. . . Krasheninnikov. , . I.Yu. . . Zhemkov. , V.B. . Kharlov.