Analog Computers

Reference / Paper · 1962

Engineering Applications of Analog Computers

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ANL-6319 Rev. is an Argonne National Laboratory report presenting seven worked engineering experiments solved on analog computers, covering reactor control rod deceleration, pressure flow through packed beds, reactor kinetics with thermal feedback, vibrating systems, temperature distribution in fins and slabs, and iodine-xenon buildup in a reactor. Each experiment follows a structured format covering problem description, mathematical statement with constants and initial conditions, machine equation derivation with scale factors, circuit diagrams with potentiometer and static check sheets, and graphical results. The document demonstrates direct analog solution of nonlinear differential equations from nuclear reactor engineering and heat transfer without linearizing simplifications.

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Argonne National Laboratory
Author
Lawrence T. Bryant, Marion J. Janicke, Louis C. Just, Alan L. Winiecki
Year
1962
Type
Reference / Paper
Language
English
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specific applications
Pages
58
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Public Domain, Google-digitized via HathiTrust Digital Library.
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Engineering Applications of Analog Computers

Y3. ANL-6319 Rev AN L -6 319 ReviEPORis Do JAN 14 1963 argonne Bational Xaboratorg ENGINEERING APPLICATIONS OF ANALOG COMPUTERS by Lawrence T. Bryant, Marion J. Janicke, Generated on 2015-10-14 01:33 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google Louis C. Just and Alan L. Winiecki LEGAL This work. person A. NOTICE report was prepared as an account of Government sponsored Neither the United States, nor the Commission, nor any acting on behalf of the Commission: expressed or implied, any warranty or representation, or respect to the accuracy, completeness, usefulness of the information contained in this report, or that the use of any information, apparatus, method, or process disclosed in this report may not infringe privately owned rights; or Makes with B. with respect to the use any damages of any information, or process disclosed in this report. method, Generated on 2015-10-14 01:33 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google liabilities Assumes resulting from the use of, or for apparatus, As used in the above, "person acting on behalf of the Commission" includes any employee or contractor of the Commission, or employee of such contractor, to the extent that such employee or contractor of the Commission, or employee of such contractor prepares, dis seminates, or provides access to, any information pursuant to his or contract with the Commission, or his employment with employment such contractor. Price $1.25 . Available from the Office of Technical of Commerce, Washington 25, D. C. Department Services, ANL-6319 Rev. Mathematics and Computers (TID-4500, 18th Ed.) AEC Research and Development Report ARGONNE NATIONAL LABORATORY 9700 South Cass Avenue Argonne, Illinois ENGINEERING APPLICATIONS OF ANALOG COMPUTERS by Lawrence T. Bryant,* Marion J. Janicke,** Louis C. Just,* and Alan L. Winiecki* Generated on 2015-10-14 01:34 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google *Applied Mathematics Division **Reactor Engineering Division Revised October 1962 (Originally published February 1961) Operated by The University of Chicago under Contract W- 3 1 - 109-eng- 38 with the U. S. Atomic Energy Commission Generated on 2015-10-14 01:34 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google TABLE OF CONTENTS Page INTRODUCTION I DECELERATION OF A REACTOR CONTROL ROD II PRESSURE VARIATIONS THROUGH A PACKED BED 13 III REACTOR KINETICS OVER MANY DECADES WITH THERMAL FEEDBACK (SIMULATION OF A TREAT TRANSIENT) 18 IV 6 A VIBRATING SYSTEM WITH TWO DEGREES OF FREEDOM 27 V TEMPERATURE DISTRIBUTION IN A RADIATING FIN 32 VI TEMPERATURE DISTRIBUTION IN AN INFINITE SLAB CONSIDERING VARIABLE THERMAL PROPERTIES 37 IODINE-XENON BUILDUP IN A REACTOR 49 VII Generated on 2015-10-14 01:34 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google 5 Generated on 2015-10-14 01:34 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google LIST OF FIGURES Title No. 1. Circuit Diagram for Solution Buffer Motion of Elias' Page Equation of 8 2. Velocity Versus Distance for Various Viscosities 11 3. Velocity Versus Distance for Various Initial Velocities 11 4. Distance 5. Velocity Versus Time for Various Viscosities 12 6. Circuit Diagram for the Solution of MacFarlane's Equation ... 15 7. Pressure Versus Distance 17 8. Circuit Diagram for Duplication of TREAT Transient 23 9- Kex and 10. Versus Time for Various Initial Velocities r\ 11 - In nj Versus Time 26 Illustration of a Vibrating System with Two Degrees of Freedom 11. 27 Circuit Diagram for the Solution of the Equations Describing Generated on 2015-10-14 01:34 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google a Vibrating System with Two Degrees 12. Distance of Freedom 29 Versus Time for a System with Two Degrees of Freedom 31 13. Geometry of Radiator Fin and Coolant Tubes 32 14. Circuit Diagram for Solution of Second-order, Fourth-degree 15. Differential Equation 34 Temperature Versus Length and dT/dx Versus Length for a 0.25-ft Fin (K = 25.0) 36 16. Model of the Infinite Slab Showing Regions Used for Analysis 17. Circuit Diagram for an Infinite Slab with Thermal Conductivity 18. K = Constant Relay Circuit for the Heat Pulse Used in Experiment VI . . 37 40 40 Title No. 19- 20. Circuit Diagram for an Infinite Slab with Thermal Conductivity K = F(Taverage) Generated on 2015-10-14 01:34 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google 41 Circuit Diagram for an Infinite Slab with Thermal Conductivity K. = F(Temperature of Region Described by the Heat Balance) 21. Page 42 Circuit Diagram for an Infinite Slab with Thermal Conductivity K - F(Average Temperature Across an Interface) 42 22. Temperature Distribution for an Infinite Slab - Case I 47 23. Temperature Distribution for an Infinite Slab - Case II 47 24. Temperature Distribution for an Infinite Slab - Case III 48 25. Temperature Distribution for an Infinite Slab - Case IV 48 ENGINEERING APPLICATIONS OF ANALOG COMPUTERS by Lawrence T. Bryant, Marion J. Janicke, Louis C. Just, and Alan L. Winiecki INTRODUCTION This publication is an extension of Bryant, L. T., Just, L. C., and Pawlicki, G. S., Introduction to Electronic Analog Computing, ANL-6187 (July I960). engineering, Six experiments are presented from the fields of reactor heat transfer, and dynamics. Generated on 2015-10-14 01:35 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google The mathematical representation for most of these experiments is in the form of nonlinear differential equations. In usual practice sim plifying assumptions are introduced to linearize the equations. This linearization may alter the mathematical model sufficiently to cast doubt upon its applicability. If an analog computer is available, the nonlinear equation may be solved directly. The presentation of these experiments has been designed to pro vide insight into physical phenomena and their mathematical representa tion. The steps required for producing the analog solution will be shown, as well as complete information for duplicating the solution. Graphical results are provided. The format of each experiment 1. 2. will be: Description of the problem Mathematical statement of the problem including: a. b. Constants Initial Conditions 3. Preparation of machine equations Machine Variables a. Scale Factors b. 4. Analog a. b. c. circuit diagram Flow Sheet Potentiometer setting sheet Static Check sheet 5. Graphical representation of the solution. 6. Bibliography I. 1 . DECELERATION OF A REACTOR CONTROL ROD Problem Description When a control rod is suddenly inserted or rejected from the core of a reactor, the rapid motion is quickly dampened by a dashpot or buffer mechanism, usually consisting of a hydraulic system which prevents sudden shock of the control drive mechanisms. Constant deceleration-type dashpots give the most favorable charac Essentially, a piston moves through oil, and the oil is squeezed into small clearances; this process in turn develops large amounts of frictional resistance. This friction, which is proportional to the speed of the moving piston, instigates the retarding force which slowly stops the motion of the control drive. teristics for protection against shock loads. This hydraulic drag and the ensuing kinetic energy dissipation are frequently described by differential equations. Elias1 equation of buffer motionU"!)* is given by 2 (J.TT DpLd dX X W(LdC - CX)2 Various plots of the buffer characteristics are shown on Figs. 2, 3, 4, and 5. Many parameters may be investigated before the design conditions for a particular problem are satisfied. (1-2,1-3) Generated on 2015-10-14 01:35 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google 2. Mathematical Statement of the Problem a. Equations: X (1) W(LdC - CX)2 b. Constants and Variables Description Symbol VP DP C velocity into the dashpot diameter of the dashpot dashpot clearance Value Units Variable f t/ s e c 2 inches 0.03 inch 6 inches Variable lb/(ft)(sec) Ld dashpot length M viscosity of the dashpot fluid w weight of the control rod 290 Ib X distance into the dashpot 6 inches *References in each section are given at the end of each section. Initial Conditions c. At t X = 0: = 0 = 70 ft/sec ' dt Analysis of Equations d. Since dVp dX the dVp/dt dX/dt _" _~ d2x/dt2 ' dX/dt ( ' original equation may be restated as dx dt 3. Preparation of Machine Equations Machine Variables and Scale Factors Generated on 2015-10-14 01:35 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google a. X' = bX ; a = 1 03 t' = at ; b = 10 b. (4) Scaled Equations d2X' b /2/"TDpLdx' WdX' dt'2 a2 I WC2 A b/Vdt' a ' i y ~^&—)r d^ALdb-x') c. • (5) Machine Equation When the values of constants and scale factors are introduced into Eq. (5), the machine equation results: = - (5.07 M) X' [^-lU-iy.) . (6) The initial conditions (in terms of voltages) are: X' dX' dt' = bX(0) = 0 b dX a dt = 7.0 volts d2X' dt 12 4. Analog a. dt2 a2 Circuit Diagram Flow Sheet Generated on 2015-10-14 01:35 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google -100 V Fig. 1. Circuit Diagram for Solution of Elias' Equation of Buffer Motion argonne national laboratorg APPLIED MATHEMATICS DIVISION ANALOG COMPUTER b. POTENTIOMETER SETTINGS REACTOR CONTROL ROD DECELERATION POTENTIOMETER NO. MATHEMATICAL VALUE DRAWING MACHINE VALUE CORREC TION SETTING PROBLEM DRAWING NO. NO. . DATE PARAMETERS SET 1 V'p (volts) v '"l 7.00 0700 a = 103 2 X' (volts) -50.00 5000 b = 102 3 0.2 0.2000 2000 4 I^(5-07M) For Figs. 2 & 5 Vp(0) = 70 ft/sec Mi = 0.0494 0.0125 0125 Dp = 2 in. M? = 0.0795 0.0202 0202 C M3 = 0.102 0.0258 0258 = 0.03 in. L , = 6 in. W = 290 Ib X Generated on 2015-10-14 01:35 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google 1 2 Vp(0) (volts) Yj = 70 ft/sec 7.00 0700 V2 = 50 ft/sec 5.00 0500 V3 = 20 ft/sec 2.00 0200 X* (volts) -50.00 5000 0.2 0.2000 2000 I £. C\~? ti \ {-K<)7 ^2) 0.0202 0202 3 4 AMI-2C 18-57) 5 100 For Fiaq 3 & 4 = 6 in. 10 argonne National Caboratorg APPLIED MATHEMATICS DIVISION ANALOG COMPUTER c. STATIC CHECK PROBLEM DRAWING REACTOR CONTROL ROD DECELERATION UNIT NUMBER UNIT OUTPUT (VOLTS) DRAWING MACHINE 1 POT Generated on 2015-10-14 01:35 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google AMP MULT AM).7ft (8-57) REMARKS M2 = 0.0795 7.00 1 + 2 -50.00 5 -10.00 3 - 1.40 4 + 0.02 1 - 7.00 2 + 10.00 3 +40.00 4 +16.00 5 - 8.75 6 - 0.02 1 -16.00 2 + 8.75 3 + 0.88 FOR STATIC CHECK INTE GRATOR NO. NO.. DATE INITIAL CONDI TION SET PARAMETERS 11 Graphical Results 5. 70 o z o 60 w 50 » 40 iUJ iij ". >-\- o ° UJ > V\ /«! 30 \' Fig. 2 w =.0494 POUND FORCE PER FOOT SECOND II " " " » A =.0795 Velocity Versus Distance for Various Viscosities /".= .102 20 10 01 0.2 03 0.4 05 DISTANCE, FEET Fig. 3 Generated on 2015-10-14 01:35 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google Velocity Versus Distance for Various Initial Velocities. Viscosity is 0.0795 Pound Force per Foot-Second 02 03 DISTANCE, FEET Fig. z 4 Distance Versus Time for 02 Various Initial Velocities 3 4 5 6 TIME, SECONDS X 10-' 12 70 60 Fig. 30 5 Velocity Versus Time for Various Viscosities >i, =0494 POUND FORCE PER FOOT SECOND yU, ■.0795 ><, =.102 20 10 2 6. 3 7 Bibliography 1-1. Freund, G. A. et al., Design Summary Report on the Transient Reactor Test Facility (TREAT), ANL-6034 (June I960). 1-2. Koch, Li. J. et al., Hazard Summary Report Experimental Breeder Reactor II (EBR^II), ANL.-5719 (May 1957) p. 30. 1-3. Bishop, A. A., and Berringer, R. T., Hydraulic Shock Absorbers for Reactor Control Rods, YAEC-111 (March 1959). the Yankee Generated on 2015-10-14 01:35 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google 4 5 6 TIME, SECONDS X 10-' 13 II. PRESSURE VARIATIONS THROUGH A PACKED BED 1 . Problem Description The future applications of nuclear power sources will depend on whether reactor technology can match the demand for higher power densities and higher operating temperatures. A popular concept for advanced appli cation is the packed bed reactor. I""* / Ul-^j Equations of fluid flow and heat transfer for this concept are dependent upon the particular packed-bed system, particle shape, and the fluid for which they are developed. The solutions to problems for this type of reactor design are usually ' obtained through use of empirical corrections.^ An equation derived by MacFarlane^"') from the basic Bernoulli equation illustrates a fundamen tal method for calculating the performance of packed bed arrangements. This relationship dP (K + Hx)P E + Dx - P2 dx expresses in differential form the variation of pressure and distance of a packed bed one square foot in cross section. MacFarlane also indicates four other general methods used for calculating laminar fluid flow in packed beds and describes their derivation. Generated on 2015-10-14 01:35 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google 2. Mathematical Statement of the Problem a. Equations dP and Constants (K + Hx)P E + Dx - P2 dx QP0G -- D = G = H = E = G2P0/gcP0 K = D + G - , k 1'73x = . lb2 3. 439x10* -r^r ft5 f°po - 2gcDpPo - lbz = = 3.44 x 108 10 ' 14 = Volumetric heat generation rate = 5 G = Mass flow rate of helium coolant = 0.378 lb/(sec)(ft2) gc = Gravitational constant = 32.17 p = Initial density = 0.083 lb/ft3 T0 = Initial temperature = 200°F P0 = Initial pressure = 10 C = Specific heat at constant pressure = 1.25 BTU/(lb)(°F) D = Diameter of the particle = 200 microns f = friction factor, a + jS (x/L,) = 285 +230 (x/L) b. Initial Conditions ft/secz atmospheres 2.12 x 104 lb/ft2 P0 = x0 = 0 L =0.2 ft. Preparation of the Machine Equations Machine Variables and Scale Factors a. x = t t1 = at " P'= bP P' = t'(final) = bP0 X(final) t(final) dt1 = adt a = 102 dP1 = bdP b = = 102(0.2) 10-3 (2) =21. 2 volts, (10-3)(2.12 x 104) at(final) = = 20.0 volts The Scaled Equation equations dt1 = _ [K f dP1 _!_ Substituting obtained: a E + b. I Generated on 2015-10-14 01:42 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google Mw/ft3 (2) into equation (l), the scaled equation is (H/a) t'] P' (Dt'/a) - (P'2/b2) + 3. Q (3) 15 c. The Machine Equation When equation (4) dP' dt' 4. (3.44 + 0.522 t')P' 0.0002 t1 - P'2 (4) Analog Circuit Diagram a. Generated on 2015-10-14 01:42 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google numerical values are placed into equation (3), the machine results: Flow Sheet ORIGINALPOSITIONOF RELAY TO HOLDRELAY +60V Fig. 6. Circuit Diagram for the Solution of MacFarlane's Equation 16 Slrgonnt Bational laboratorg APPLIED MATHEMATICS DIVISION ANALOG b. COMPUTER SETTINGS POTENTIOMETER PROBLEM DRAWING PRESSURE NO. POTENTIOMETER DATE REDUCTION THROUGH A PACKED BED MATHEMATICAL VALUE DRAWING MACHINE CORREC TION VALUE 1 O.0la volt -1.00 0100 2 P0b volt +21.2 2120 3 b2D/a 0.0002 0002 4 b2H/a2 0.5220 5220 5 b2K/a 3.44 0344 6 VTo 3.162 3162 7 aL -20.00 2000 PARAMETERS SET SETTING NO. NO. . ( 1C ) 2lrgonne national laboratory APPLIED MATHEMATICS DIVISION ANALOG COMPUTER c. STATIC CHECK PROBLEM DRAWING NO. NO.. DATE PRESSURE REDUCTION Generated on 2015-10-14 01:42 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google UNIT NUMBER UNIT DRAWING MACHINE AMP POT MULT OUTPUT (VOLTS) 1 + 1.00 2 0.0 3 -3.96 4 -21.2 5 +66.9 6 44.7 7 -0.188 8 0.0 3 0.0 4 0.52 6 -6.69 1 -0.84 2 -44.7 3 +1.88 THROUGH A PACKED BED REMARKS INTE GRATOR INITIAL CONDITION SET PARAMETERS 17 5. Graphical Results 25 O 20 "- 15 IE m L±J S 0.1 DISTANCE, FEET 0.2 Fig. 7. Pressure Versus Distance 6. Bibliography II- 1. Leroy, M. M., and Newgard, J. J., Pebble Bed Nuclear Reactor for Space Vehicle Propulsion, Aero/Space Engineering, 19.(4), 54-58 (April I960). T., and Bevenati, R. F., A High Temperature Gas Cycle Pebble Bed for Central Station Use, TID-7564 (1958). II-2. Robinson, S. R. B., Leyberg, E. A., and Morris, J. F., Heat-transfer Coefficients for a Full-scale Pebble-Bed Heater, Ind. Eng. Chem. Generated on 2015-10-14 01:42 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google II- 3 . Lancashire, 52, 433 (I960). II-4. Rodin, M. B., Study of the Packed-Bed Fuel Element Concept, ANL-6193 (August I960). 18 III. REACTOR KINETICS OVER MANY DECADES WITH THERMAL FEEDBACK (SIMULATION OF A TREAT TRANSIENT) 1. Problem Description The TREAT reactor was designed to generate a very large, transient, thermal flux field of short duration. (HI-1) The maximum in tegrated flux is greater than 1015 neutrons/cm2. The core is a dispersion of highly enriched uranium (as the oxide or carbide) in a graphite matrix. The graphite serves as a moderator, a heat sink, and a generator of a sizeable negative temperature coefficient. The latter effect is due to the fact that the energy of the thermal neutrons increases with graphite temperature thus causing an increase in the leak age probability. The purpose of this experiment is to simulate a TREAT transient initiated by control rod withdrawal and terminated by the negative tempera ture coefficient. Since a large excursion is expected, the reactor kinetics equations will be transformed by a substitution. (III-2) ri =£n n(t)/n(0) The equations describing the neutron kinetics (with will be solved on the analog computer. delayed groups) They will be forced by changes in Kex- Generated on 2015-10-14 01:42 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google 2. Mathematical Statement of the Problem Equations: a. =1 where T\ = .gn n(t)/n(0) 6 19 Constants b. p = 0.00755 3, = 8.6 x 10-4 Generated on 2015-10-14 01:43 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google M Pi 1 0.01246 0.00025 2 0.0315 0.00166 3 0.1535 0.00213 4 0.456 0.00241 5 1.612 0.00085 6 14.3 0.00025 c. Initial Conditions 7](0) = 0 ^i = 0 Kiex= 3. i 0 Preparation of Machine Equations Machine Variables a. t1 = at T)' = bT) Kiex - c Kiex Scale Factors b. a = b = 2 c = 25 = d2 10 . = d = 2 20 c. Scaled Equations 3 ex dt' dt1 d. The Generation of K The expression for Kex is made up of two parts: the contribution of the control rod and the contribution of the negative temperature coeffi cient, that is, Kex = K(t) - K(n,t) where K(t) _ fo.04t for 0<t£0.5 sec for t>0.5 sec I 0.02 and Generated on 2015-10-14 01:43 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google K(n.t) = ICT10/ n dt Since _c_ IB then = J K(t) - j K(n,t) or, more simply, = Kj(t) - Ki(n,t) 0.04-| - for 0<t'<0.5a sec 0.02 —for t'>0.5a sec ') can be generated by means of an integrator and a relay. 21 The generation of Ki(n,t) is more complicated: a function generator is needed. If the machine variables and scale factors are sub stituted into K(n,t) the = / ndt 10"10 result is Kj(n,t) ~ 10"10 /ndt' . But n = ni n(0) ; therefore / Bldt Kf(n,t) = filler10 pa The analog computer variable) and since e^n ni Generated on 2015-10-14 01:43 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google Kf(n,t) = £^i£l 10-io = . will supply 7) = in n^ (due to a change in n^ J er?dt, After the terms are collected, Ki(n,t) = c / eadt' where a = t) +£n n(0) - Zn 1010 - £n ap For the values given the constants, a= i) - 15.836. and for n(0) - 102, Then 25 ea will be generated with a diode-function generator (DFG).'111"3) In order to decrease the slope of the function, the DFG will be driven by 107] - 100. 22 In the actual experiment, the input to integrator means of a relay) until 25 ea = 0.01 volt. (by DFG DATA e. dr Generated on 2015-10-14 01:43 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google dt' 7] ion - 0.0 a 25 ea -100 -15.836 - 8.012 - 19.88 - 7.821 00.01 9.938 - 0.62 - 6.438 00.04 10.42 + 4.2 - 5.416 00.11 12.0 + 20.0 - 3.836 00.54 13.0 + 30.0 - 2.836 1.47 14.0 + 40.0 - 1.836 3.96 15.0 + 50.0 - 0.836 10.59 16.0 + 60.0 + 0.164 29.45 17.0 + 70 + 1.164 80.75 100 Machine Equations = 0.0697 K^ex +0.3512 (0.0331^/{ + 0.2821^ + 0.3192^4 + 0.1126^^ dt' + 0.2199^1 + 0.0331^) 3 is removed 23 = 0.0001 - 1.43^ = -0.5 KJ(t) - Kj(n,t) fl3.25t' volts for 0<t'<5 sec , Ki(n,t) = 25 exp 4. Analog - 15.836) Circuit Diagram Flow Sheet a. -100 3-K'iex EXPERIMENT Fig. 8. - ? EXPERIMENT 3 Generated on 2015-10-14 01:43 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google (7] " ' ' 1 66.23 volts for t'>5 sec = iU -n, Circuit Diagram for Duplication of TREAT Transient 24 argonnt national taooidtorji APPLIED MATHEMATICS DIVISION ANALOG COMPUTER b. POTENTIOMETER SETTINGS PROBLEM DRAWING DATE THE TREAT REACTOR POTENTIOMETER NO. MATHEMATICAL VALUE DRAWING MACHINE 0697 S, = 8.6x10- 2 0/a2 0.8779 8779 /3 = 0.00755 3 b/VdiJ3 0.0331 0331 4 b/Vd^ 0.2199 2199 X, = 0.0315 5 b/Vdj/3 0.2821 2821 X3 = 0.1535 6 bA,/d4/3 0.3192 3192 X4 = 0.456 b/Bj/dsjS 0.1126 1126 X5 b/36/d6,3 0.0331 0331 \ = 1.612 V'a 0.0012 0012 0j = 0.00025 Va Va Va Va Va 0.0032 0032 /3Z = 0.00166 0.0154 0154 |33 = 0.00213 0.0456 0456 /34 = 0.00241 0.1612 1612 /35 = 0.00085 1.43 1430 /36 PARAMETERS 7 SET 8 SETTING 0.0697 = 0.00025 15 d5X5|3/ac 0.0001 0001 a = 10 16 d6X6(3/ac 0.0009 0009 17 FOR TO STATIC 24 CHECK 25 - 5.0 volts 0500 26 1.0 volts 0100 27 28 AtO-2C (8-571 + -0.04c//3a volt -19.88 volts = 25 = n(0) 1325 1988 2 b = c 1( -- 14.3 dt 14 ( 13 ) 12 0 11 0.01246 0 10 \- 0 1 Generated on 2015-10-14 01:43 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google CORREC TION 9 6b(l - 0)/a^c VALUE NO. NO. . ..=d6=2 = 102 25 Slrgonnc .Rational laboratory APPLIED MATHEMATICS ANALOG c STATIC DIVISION COMPUTER CHECK NO. PROBLEM DRAWING NO.. DATE THE TREAT REACTOR UNIT NUMBER DRAWING MACHINE POT Generated on 2015-10-14 01:43 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google AMP OUTPUT (VOLTS) REMARKS INTE GRATOR CONDI TION 17 -10 1 +10 18 + 10 2 -10 19 + 10 3 -10 20 + 10 4 -10 21 + 10 5 -10 22 + 10 6 -10 23 + 10 7 -10 24 -50 23 +50 9 -7.0 10 -10 11 -10 12 +50 13 +50 14 + 50 15 +50 16 +50 17 + 50 18 +5.0 20 Negative 25 Positive ALL M ULTIPl ,IER CI JANNELS = +5 volts AMD-?A(8-57) INITIAL SET PARAMETERS 26 5. Graphical Results Fig. 9 = Kex and T) J>n n, Versus Time 345 TIME,Seconds 6. Bibliography III-l. Okrent, D., The Reactor Kinetics of the Transient Reactor Test Facility (TREAT), ANL-6174 (Sept. I960) III-2. Bryant, L. T., Just, L. C., and Pawlicki, G. S., Introduction To Generated on 2015-10-14 01:43 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google Electronic Analog Computing, ANL-6187 (July I960). III-3. Scott, W. E., Fundamental Components of~ the "PACE" Analog Computer, ANL-6075 (Nov. 1959). 27 A VIBRATING SYSTEM WITH TWO DEGREES OF FREEDOM IV. 1. Problem Description Problems of vibration must be considered in the design of power plants using fissionable fuel. Fuel elements, control rods, and structural supporting members are capable of vibrating; their characteristics must be analyzed, for vibration problems prove to be of importance to eliminate concern for the safe operation of the power plant. Good representations of the true situation usually involve systems with several degrees of freedom. A typical vibration problem which will serve as an introduction to multi-degree-of-freedom systems is shown in Fig. 10. The two masses mj and m2 are suspended vertically by springs kj and k2. The masses are constrained such that they only move vertically. The displacements xj and x2, taken positive for a downward motion, are measured using static equi librium as reference. The elongation of the upper spring is Xj and the elongation of the lower spring is (x2 - xj). The restoring force acting on mi is [-kjXj + k2(xz - xj], and on m2 the restoring force is -k2(x2 - xj), where ki and k2 are the spring constants of the respective springs. Effects due to energy dissipation in the elastic spring, wind friction, and springs that have appreciable mass have been neglected in the equations Generated on 2015-10-14 01:43 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google of motion given below. Fig. 10 Illustration of a Vibrating System with Two Degrees of Freedom m-, x axis 2. Mathematical Statement of the Problem. a. Equations + k2(x2 - (1) 28 m2 d2x2 — — dt b. -kz(X2 - XiJ = (2) Equation Constants mj: mass (ib) (i = 1, 2) A: spring constant (ib force/ft) (i = 1, 2) Initial displacement of the springs (feet) c. Initial Conditions kj: It is obvious that with the springs displaced a certain distance, A, the initial conditions will have the following values Xl(0) = = dt dX2(0) dt = 0 d2Xl(0) d2X2(0) dt2 dt2 dXl(0) Generated on 2015-10-14 01:44 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google 3. A x2(0) (3) = 0 Preparation of Machine Equations: In transforming to the machine equations, the folio-wing relationships are made. Let jq - bXi (i = 1, 2) and (4) t1 = Substitution at of equations (4) into equations (1) and (2) yields 2 ix dt a iri ~k? dt'2 a2mz a 'fc-xj) (x2-x{) (5) (6) 29 where xi(0) = bXl(0) = bA x£(0) = bx2(0) = bA and The solution to the equations will vary with m1( m2, kj, kz, and A. solution given here, we consider the following physical constants: ki = k2 = 0.2 lb force/ft mj - m2 = 1 lb mass A = 1 ft 4. Analog a. Circuit Diagram Flow Sheet Generated on 2015-10-14 01:44 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google -IOOV Fig. 11. Circuit Diagram for the Solution of the Equations Describing a Vibrating System with Two Degrees of Freedom In the 30 argonne national Xaboratorg APPLIED MATHEMATICS DIVISION ANALOG COMPUTER b. POTENTIOMETER SETTINGS A VIBRATION SYSTEM WITH TWO DEGREES OF FREEDOM POTENTIOMETER NO. MATHEMATICAL VALUE DRAWING MACHINE VALUE CORREC TION PROBLEM NO. DRAWING NO. . DATE PARAMETERS SET SETTING 1 bA -50.00 -5000 a = 1 2 bA -5000 -5000 b = 50 3 k^/a2^!j 0.2 2000 4 k2/a2mj 0.2 2000 5 k2/azm2 0.2 2000 argonne Rational laboratory APPLIED DIVISION MATHEMATICS ANALOG COMPUTER c. STATIC CHECK PROBLEM DRAWING NO. NO.. Generated on 2015-10-14 14:13 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google DATE UNIT NUMBER UNIT DRAWING MACHINE POT AMP OUTPUT (VOLTS) 3 10.00 4 0.0 5 0.0 1 0.0 2 +50.0 3 -50.0 4 0.0 5 -10.0 6 0.0 7 50.0 REMARKS INTE GRATOR INITIAL CONDI TION SET PARAMETERS 31 Graphical Results 5. 10 -1.0 Fig. 12 Distance Versus Time for a System with Two Degrees of Freedom 10 -i.o 0 20 40 60 80 TIME, SECONDS 6. Bibliography IV- 1. Timoshenko, S., Vibration Problems in Engineering, D. Van Nostrand Generated on 2015-10-14 14:13 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google Company, Inc., Princeton, New Jersey, (1955) 3rd. Ed. 32 TEMPERATURE DISTRIBUTION IN A RADIATING FIN V. 1. Problem Description The only economical method for rejecting heat from an outer-space power plant is by thermal radiation. (V - 1) if the working fluid of the power plant passes through tubes, the additions of extended surfaces to the tubes in the form of fins reduces the number of tubes required. This reduction decreases the probability that a meteor will puncture a vital coolantcarrying passageway. (The puncture of a fin is of lesser concern for the continued operation of the power plant.) An analysis of the temperature distribution of these extended surfaces is very important in calculating the effectiveness (and, indirectly, the safety of the plant) of various fin geometries. 2. Mathematical Statement of the Problem In the development of a differential equation for conduction, (V-2) dq = d/dx f2kWYx-|^dx j (l) A general heat balance requires this differential equation (l) to be equal to dq = 2ae (T4 - Generated on 2015-10-14 14:13 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google the heat rejected Ts) dA (2) by radiation. By assuming that the arc length (ds) on the arbitrary surface is equivalent to dx on the abscissa and assigning Yx equal to a constant thick ness for a straight fin geometry, the differential equation for temperature is d2T dx' ae Hk Tl) (3) A constant heat source will be assumed at one end of the fin and dT dx 0 x=L at the other end.v""^) This will correspond to the fin in Fig. 13. -TEMPERATURE Fig. 13 Geometry of Radiation Fin and Coolant Tubes 33 a. Constants and Variables T = Absolute temperature along the fin Ts = Absolute temperature of the sink a = Stefan-Boltzmann constant e = Emissivity W - Width of the fin in the z-direction L = Total length of the fin in the x-direction q = Heat dissipated H = Half -thickness of the fin k = Thermal conductivity of the fin material Generated on 2015-10-14 14:13 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google Typical values are: Ts = 0°R O = 0.173 x ID-8 c = 0.9 W = 1.0 ft L = 0.25 ft H = 1.250 x 10"3 ft k = 25.0 b. Initial Conditions T(0) = BTU/(hr)(ft2)(°R4) BTU/(hr)(ft)(°R) 2000°R The most efficient use of radiator material weight dictates the arrangement of the finned tubes in a straight bank. The general tempera ture distribution, of this arrangement, along the fin is given in Fig. 15. 3. Preparation of Machine Equations a. Machine Variables and Scale Factors. bT ax = x1 adx = dx' bdT = dT' a2dx2 = dx'2 bd2T = d2T' a = 102 b = 5 TT x 10"2 . . 34 Scaled Equation b. Substituting Equations aeT'4 (Note Ts a2b\H dt' (5) into Equation = (3) we get, 0. Machine Equation c. ' 0.03986 •= f T '4 dt |2 d. Initial Conditions T1 = bT = Y volts dT1 dt1 = 100 volts so that dT1 Generated on 2015-10-14 14:13 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google dt' 4. Analog a. = 0 t=aL Circuit Diagram Flow Sheet — 100v i ) i loov T' D> Fig. 14. Circuit Diagram for Solution of Secondorder, Fourth-degree Differential Equation 35 argonne Bational laboratory APPLIED MATHEMATICS DIVISION ANALOG COMPUTER b. POTENTIOMETER SETTINGS PROBLEM DRAWING NO. NO. . DATE POTENTIOMETER NO. MATHEMATICAL VALUE DRAWING MACHINE dT1 CORREC TION VALUE 1 7—r volts Ht1 * 2 106ae/a2b3kH 0.03986 * Variabl e to produce SETTING 0399 -dT — = 0 at X :-- L ax. argonne Bational Xaboratoru. APPLIED MATHEMATICS DIVISION ANALOG COMPUTER c. STATIC CHECK PROBLEM DRAWING NO. NO.. DATE UNIT NUMBER Generated on 2015-10-14 14:13 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google UNIT DRAWING MACHINE OUTPUT (VOLTS) POT 2 -3.99 MUH 1 AB -lOOv AB -100v 3 + 3.99 2 AMP REMARKS INTE GRATOR 2 INITIAL CONDI TION +100 PARAMETERS 36 5. Graphical Results 2000 1500 1000 500 0.10 0.15 FIN LENGTH,FEET Fig. 15. Temperature Versus Length and dT/dx Versus Length for a 0.25-ft Fin (K = 25.0) Generated on 2015-10-14 14:13 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google dT / *dT/dx was plotted to show when boundary condition - — is satisfied. 6. = 0 Bibliography V-l. Corliss, W. R., Nuclear Power in Outer Space, Nucleonics, 18 (8), 59-63(1960). V-2. Schneider, P. J., Conduction Heat Transfer, Addison - Wesley Publish ing Company, Inc., Reading Massachusetts (1955). V-3. Lieblein, S., Analysis of Temperature Distribution and Radiant Heat Transfer Along a Rectangular Fin of Constant Thickness, NASA Technical Note D-196. National Aeronautics and Space Administra tion, Washington (November V-4. 1959). Carslaw, H. S., and Jaeger, J. C., Conduction of Heat in Solids, Second Edition, Oxford University Press, Amen House, London E. C.4, 1959. 37 VI. 1. TEMPERATURE DISTRIBUTION IN AN INFINITE SLAB CONSIDERING VARIABLE THERMAL PROPERTIES Problem Description When the thermal properties of various materials are studied, thermal conductivity, specific heat and density are usually considered as constants; they are, however, dependent upon temperature. (VI-1) In this experiment, an insulated zirconium slab is studied. Four cases are considered: 2. Diffusivity (2) «.F(i^Ti) (3) K. (4) K. ( K. ; - F (Temperature of the region described by the heat balance); - F (Average temperature across an interface). Mathematical Statement of the a. Generated on 2015-10-14 14:14 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google - k/p c) is constant; (1) Equations Fig. 16. Model of the Infinite Slab Showing Regions Used for Analysis 38 /T ' ( d dT dt -= Ax" v 4 pcAx Constants b. (1) Constant case Generated on 2015-10-14 14:14 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google k = thermal conductivity = 11 BTU/(hr)(ft)(°F) c = specific heat = 0.066 p = density = 0.397 lb/ft3 /c = k/cp = diffusivity = 0.4198 S = heat source = 18.3 € = emissivity a = Stephan-Boltzmann constant Ax = 1/60 ft (Z) As a function of temperature T, °F 100 ZOO 300 400 500 600 700 800 900 K(T) 0.4198 0.4 0.38 0.364 0.35Z 0.336 0.3ZZ 0.309 0.Z98 *Radiation heat loss will be neglected. BTU/(lb)(°F) ft2/hr BTU/(ft2)(sec) 39 Initial Conditions c. Ti 3. = T3 = T4 = T5 = 100°F Preparation of Machine Equations Machine Variables a. t1 = at T1 = bT S" = AxSb/k Scale Factors b. a = 1.0 b = 0.1 Machine Equations c. KS" dTl Generated on 2015-10-14 14:14 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google = T2 _jc , ~ z> Initial Conditions d. T' = TZ = ... TS = 10 volts S" = 10 volts [S = 18.3 BTU/(ft2)(sec)] for 50 sec 40 4. Analog a. Circuit Diagrams Flow Sheets Case I - ( K. = constant) Fig. 17. Circuit Diagram for an Infinite Slab with Thermal Conductivity Generated on 2015-10-14 14:14 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google K. - Constant R-RELAY CIRCUIT -TO INTEGRATOR Fig. 18. 5000 Relay Circuit for the Heat Pulse Used in Experiment VI Generated on 2015-10-14 14:14 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google 41 Case Fig. 19. II - [K = F(Tav)] Circuit Diagram for an Infinite Slab with Thermal Conductivity /c = F(Taverage) 42 Case III - [K - F( Temperature of the Region Described by the Heat Balance)] Circuit Diagram for an Infinite Slab with Thermal Conductivity K = F(Temperature of Region Described by the Heat Balance) Generated on 2015-10-14 14:14 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google Case IV - Fig. 21. = F(Average Temperature Across an Interface)] Circuit Diagram for an Infinite Slab with = F(Average Thermal Conductivity Temperature Across an Interface) K. 20. [/c Fig. 43 argonne Bational Caboratorg APPLIED MATHEMATICS DIVISION ANALOG b. COMPUTER POTENTIOMETER SETTINGS TEMPERATURE VARIATION IN A ONE FACE INSULATED SLAB CONSIDERING VARIABLE THERMAL PROPERTIES CASE I POTENTIOMETER NO MATHEMATICAL VALUE Generated on 2015-10-14 14:14 GMT / http://hdl.handle.net/2027/mdp.39015078510917 Public Domain, Google-digitized / http://www.hathitrust.org/access_use#pd-google DRAWING MACHINE CORREC TION VALUE SETTING SET PROBLEM DRAWING NO.. NO. - DATE. PARAMETERS I 0.01T] 0.1 1000 S = 18.3 2 O.OlTj 0.1 1000 S" = 10 3 0.0ITJ 0.1 1000 a = 1 4 0.01T4 0.1 1000 b = 0.1 5 O.0lTj 0.1 1000 6 (0.01/cS"/Ax2a) 0.042 0420 Ax 7 /c/Ax2a 0.4198 4198 Ti(0) = 100° 8 /c/Ax2a 0.4198 4198 9 /c/Ax2a 0.4198 4198 10 K/Ax2a 0.4198 4198 11 /c /A x2a 0.4198 4198 12 /c/Ax2a 0.4198 4198 13 /c/Ax2a 0.4198 4198 14 /c /A x2a 0.4198 4198 C ASE 0.4198 3600 II 1 0.0lTj 0.1 1000 2 0.01