Control of hot spots in plug flow reactors deepdyve. Reactor performance and operating conditions here ci molm 3 represents the concentration of component i in bubbles and emulsion. Ideal plug flow reactor characteristics of ideal plug flow perfect mixing in the radial dimension uniform cross section concentration no mixing in the axial direction, or no axial dispersion segregated flow tracer pulse input at t 0 translated to equal pulse output at t lv l pfr length, v average velocity. Hot spots in adiabatic reactor student cheresources. In addition to excellent mixing, continuous reactors require plug flow conditions which means that all the material processed through the reactor has the same residence time. Diethyl sulfate hot spot heat transfer fluid reactor reactor inlet. However, a reactor deliberately designed to incorporate a hot spot can possess attributes that make it very suitable for use in a selfcontained hydrogen generator, small enough to be portable. A nonlinear control law is derived which guarantees that the hot spot temperature remains below a prespecified bound for all times after an initial transient, under relatively mild assumptions on the inlet conditions. Plug flow behavior and short mixing times could be confirmed for all investigated flow reactors. Do the hot spots always occur in adiabatic reactor. Kinetic and scaleup investigations of a michael addition. Transversal hot zones formation in catalytic packedbed reactors. Determine the output concentration of a as a function of time and plot reactor output response curves for reactant a. N2 this paper addresses the problem of suppressing the magnitude of hot spots in plug flow reactors by manipulating the jacket coolant temperature.
Control of hot spots in plug flow reactors sciencedirect. Most reactors used in industry approximate the ideal batch reactor, pfr, or cstr. Pdf chapter 9 nonisothermal reactors caltech authors. Increased reaction temperature optimised reaction temperature profile elimination of hot spots reactant addition on passagebypassage basis, with rapid mixing multiple sequential reactant additions and reactions. Water is run through the reactor at a flow rate q m 3sec and t0 the reactant a is added to the input stream on a continuous basis. Is there any way of calculating and even reducing the hot spots temperature. Plug flow reactor pfr nonideal reactors definition. Hlavacek20,21 observed both periodic and aperiodic traveling hot spots in a catalytic packedbed reactor during co oxidation.
In addition to excellent radial mixing, continuous reactors require plug flow conditions. In such reactors, the reaction rate expression must be known determined. Reactor theory and practice plug flow reactor pfr the third general type of reactor is the plug flow reactor pfr. For example a fully laminar regime would provide a very wide normal distribution curve significant backmixing spreads the tracer, whereas a true plug flow system would see the same tracer spike that was injected at the start. We observe hot spots in the trickle bed reactor with a local. The batch reactor, the continuous stirredtank reactor, and the plug ow reactor. In a plug flow reactor, nutrients and sometimes organisms are introduced to the reactor continuously and move through the reactor as a plug.
Control of hot spots in plug flow reactors control of hot spots in plug flow reactors karafyllis, iasson. Plug flow reactorthe plug flow reactor pfr, sometimes called continuoustubular reactor, ctr, or piston flow reactors is a modelused to describe chemical reactions in continuous, flowingsystems of cylindrical geometry. Fixedbed catalytic reactors fbcrs key engineering problems 1. Two commonly used reactors are the cstr continuous stirred tank reactor and the pfr plug flow reactor. The integral to calculate the pfr volume can be evaluated using a method such as simpsons onethird rule pg 925. This paper addresses the problem of suppressing the magnitude of hot spots in plug flow reactors by manipulating the jacket coolant temperature. An important class of carboncarbonbond coupling reactions is the dielsalderreactions. Furthermore, interactions of reaction kinetics and the formation of hot spots in the reactor channel were investigated. Would having a shorter shallow catalyst bed help with the temperature distribution. The plug flow reactor model pfr, sometimes called continuous tubular reactor, ctr, or piston flow reactors is a model used to describe chemical reactions in continuous, flowing systems of cylindrical geometry. Plug flow operation very narrow residence time distribution. Pdf normal operation and hot spots formation in a trickle bed reactor.
Given r a as a function of conversion, one can size any type of reactor. Vertical plug flow shellandtube reactors are used for the system. Plug flow reactor pfr molar balance equation reactor engineering class 9 duration. Hot spots in chemical reactors are phenomena that the reactor designer would. Bilge alpaslan kocamemi if the series is composed of one reactor complete mix regime prevails if the series consists of an infinite number plug low regime prevails. Size reactors either alone or in series once given the molar flow rate of a, and the rate of reaction, r a, as a function of conversion, x. Industrial finechemical and pharmaceutical production. A hot spot is formed due to a very small change in wall temperature. Avoidance of hot spots the pioneering work of bilous and amundsen aiche j. Case study on tubular reactor hotspot temperature control. Tubular reactor, plug flow reactor, saponification, integral method, differential method. The plug flow pfr reactor, shown in figure 1, is modeled by means of a first principles. Hot spots in chemical reactors are phenomena that the reactor designer would normally try to avoid.
Selection of technical reactor equipment for modular. Conversion and reactor sizing define conversion and space time. Diameter of the simulated fluidized bed reactor is 40 mm, for the geldart. The pfr model is used to predict the behavior of chemical reactors of such design, so that key reactor variables, such as the dimensions of the reactor, can be estimated. Polymerization plug flow reactors for viscous processing. Increased reaction temperature optimised reaction temperature profile elimination of hot spots reactant addition on passagebypassage basis, with rapid mixing. Flow intensi cation is made thanks to apparatuses in which ow behaves like a perfect plug ow. The experiment is carry out to acheive a few objective which are to study the effect of residence time on the conversion of the solution, to study the reaction rate constant and to determine the conductivity and the conversion of naoh. Plug flow reactor plug flow, or tubular, reactors consist of a hollow pipe or tube through which reactants flow. Dispersion deviates from ideal plug flow conditions shortcircuiting and dead spaces deviate from ideal mixing and plug flow conditions filling and drawing deviate from ideal batch conditions mass balance. A nonlinear control law is derived which guarantees that the hot spot temperature remains below a prespecified bound for all times after an initial transient. Pictured below is a plug flow reactor in the form of a tube wrapped around an acrylic mold which is encased in a tank.
There is however a measure of conflict between good mixing and plug flow since mixing generates axial as well as radial movement of the fluid. Plug flow reactors are the most common reactors currently being used in industry for ethylene oxide production, since they allow for high velocities to be used and require less volume than other types of reactors. The volume of a pfr can be represented as the shaded area in the levenspiel plot shown below. Specifically, three control configurations are quantitatively evaluated for tightness of hot spot temperature control and maximum achievable process throughput. Chemical reaction engineering course plan total 15 lectures. A nonlinear control law is derived which guarantees that the hot spot temperature. Thermal stability management of hot spots adjustment of catalytic bed properties length, activity, shape of particles, etcdesign of cooling.
Double pipe heat exchanger behaves like plug flow reactor, which are important for design, operational and control point of view, are presented. In fact, real reactors can be modeled as networks or combinations of multiple plug flow and stirredtank reactors towler and sinnott, 20. Shutt jhnson matthey technology centre hot spots in chemical reactors are phenomena that the reactor designer would normally try to avoid. The long tube and the lack of provision for stirring prevents complete mixing of. Plug flow reactors plug flow, or tubular, reactors consist of a hollow pipe or tube through which reactants flow. Robust pipid controller design for the reliable control of plug. The object of this experiment is to study the behaviour of a plugflow reactor by performing a series of experiments on the saponification of ethyl acetate. Where offsite areas will drain to the smp, calculate imperviousness of the offsite contributing drainage area based on its current condition. In the case of a plug flow, the dispersion model accounts for axial dispersion d, which is the physical parameter that quantifies axial backmixing and shortcircuiting of fluid. Examples of real reactors that approximate the flow pattern of ideal reactors. The disadvantage of the tubular reactor is that it is difficult to control temperature within the reactor, and hot spots can occur when the reaction. Estimation of steadystate mixed flow reactor residence time in a decay reaction left side and an autocatalytic reaction, here biomass growth right side. Water at a controlled temperature is circulated through the tank to maintain constant reactant temperature. Yet, their operation presents distinct challenges, such as a strong dependence of temperature and composition profiles on the inlet conditions, the possible appearance of a maximum in the temperature profile hot spot and the possibility of temperature runaway see for example the classic paper bilous.
Pdf flow maldistributions and hot spots in downflow. Within the limits of heat exchange, the reactor can operate isothennally maximum. An empty pipe is a poor continuous reactor because the material in the center of the pipe travels at. How to build a catalytic test reactor max planck society. Flow maldistributions and hot spots in down flow packed bed reactors. Pdf lab report tubular flow reactor muhamad faizzudin. In terms of trajectory through the reactor, the ideal flow condition for a continuous reactor is plug flow since this delivers uniform residence time within the reactor. Plug flow reactors pfrs are ubiquitous in the chemical process industry. Write the mole balances in terms of conversion for a batch reactor, cstr, pfr, and pbr. However, a reactor deliberately designed to incorporate a hot spot.
For the examined reaction, the simulations predicted the product yield under production conditions in good accuracy. Modelbased design, scaleup, and operational optimization of. Plug flow conditions means that all the material processed through the reactor must have the same residence time so that the chemicals exiting the reactor have witnessed the same reaction conditions of reactive species contacttime agingtemperature history. The hot spottm reactor hydrogen generation using a novel concept by j. These reactors provide enough residence time for the reaction to take place with satisfactory conversion. Response of cfstr to nonconservativereactant tracer input o q,c c. Karafyllis and daoutidis 20 applied a nonlinear controller to control the hot spot temperature in a pfr. A nonlinear control law is derived which guarantees that the hot spot temperature remains below a prespecified bound for all times after an initial transient, under relatively mild assumptions on the. Control of hot spots in plug flow reactors request pdf.
265 811 1311 1381 530 1000 577 377 830 762 1261 260 1327 853 306 7 576 914 753 809 378 981 1191 1490 108 275 1018 415 1172 1474 942 1427 913 922 569 1002 1377 356 354 1420 779 573 1392 796 243 1237