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Cube Equilibrium in Liquid: Heat Transfer & Gas Thermodynamics, Exams of Physics

Solutions to various physics problems. The first problem deals with a cube in equilibrium in a liquid, where the length tr is to be found in terms of the densities and volume. The second problem involves a liquid entering a tank at a volume flow rate and finding the height to which the water level will rise. The third problem is about heat transfer, where the latent heat of vaporization is measured using a calorimeter and the final temperature is to be found. The fourth problem is related to an ideal gas with specific heat ratio and finding the efficiency of the heat engine.

Typology: Exams

Pre 2010

Uploaded on 10/12/2009

koofers-user-idk
koofers-user-idk 🇺🇸

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Download Cube Equilibrium in Liquid: Heat Transfer & Gas Thermodynamics and more Exams Physics in PDF only on Docsity! \ ' l/' I | ,i,-- t " t. f i . ' lJ.y'" i"t t- l. t I t^ . Sf tD+; t' t\ fd PHY 206 EXAM I ID: 1- .l l. ',. .l /_. 3. 1, p + pgg * ;pu" : const. dQ : n'LCdT dQ -- ncdTL L,L-: aLgLT LV : pVa'LT ,# - *lO,.-, ' dt -' l' .' P :-oAeTa .py : nRT dQ : dU + dW" . dW : pd,V "pV1 :'cons!. ^y - cp/cv,) l. ^'\ T)- 17.D J (110) <td- 1. This problem consists of two i,ndependent problems. a) A hollow, massless cube with side tr is par- . tially fitled with a volumdV ota liquid with density p and the remainder with a gas of negligible density. The cube is in equilib- rium with its midpoint at the interface be- tween two liquids'of density p1 and pz t pr as shown. Find the length tr in terms of the . densities and V. b) An tank has a small hole of cross-sectional area o at the bottom. Liquid of density p enters the initially empty tank at a volume flow rate ft (i.e. in m3/s). Find the height' gr to which the water level will rise.. ?-, fl= Lt<B- L'fl- Solution:' a) In"equilibrium means'the weight of the liquid in the cube must be bal- anced by the sum of buoyant forces from each of the displaced liquids: pvg:)orr'o +)orL's + L: (-ryL)"'. \Pt + P2,1 b) The water level will risi: until the flow rate exiting the hole equals ft. The flow rate out the hole is ou, where u is the speed of effiux which we compute in the usual way using Bernouilli's'equation. Taking a point at the water level, height y .frorn the bottom, and the second poidt at the output of the hole, Bernouilli reads: PolPgA:Po*lO"4u-frW So now,we have: R : ou : or1Zfu. Squaring both sides and solving for y gives the desired result:. l, a: +(.u)' /i\ t-Q.v,'; ."."2 I f- { I I I I irt - I : t :-" I Mar.."5, 2008 PHY 206'EXAM II NAME: SIGNATURE: I. ) a a'J. ID: ! rl 1,. , . Some relations you may need: "*t '1 L -t P + PgA -t ;Pu' - corlSt.z Er' l - LL:."aL'oLT LV : pVoLT dQ : rncdT dQ : ncdT -' #::f,"' i ,-R Na W . lQoutl '7: e;,:'r - ad DV -D "'f (110) I t' 1. In the following three 'independent problems irll gases are ideal and vibrational degrees of freedorh are to be ignored. Yoir are to use: ly'a : 6 x'1023 rholecules/mol, R: 8 J/mol.K, | ' ''" and the table beiow as needbd n- ' a)''Suppose Cl2 and N2 gases are in equilibrium in* a contd,inef at temperature ?. What is the ratio of their rms speeds, uffi"lrY,A"? b),A d,i,atomi',c gas from the table below is measured to have a con- stant-volum"e specific heat per, mass, C : (5000/8)J/kg.K. Use' ' the equipartition of energy principle to find'the molar mass and identify the gas. c) The specifib heat of a mixture of gases is the weighted sum of the respective "specific heats of the gases: "_n(rLnzci t , I 1-* 71,2 . *hete fi,1 and. n2 are the number of moles of each gas. A student has a cohtairier with 57g.of dr,atom'ic Fl2 gas in it. She wants to add monatomic helium gas to create a mixture with constant" uolume molar specific'heat (2L110)8. How many mols of helium' must she add? R f, Molecule M (e/mol H2 2 N2 28 o2 32 FI, 38 CI, 70 mole: M- a, 5n r / 1 r.:6JlmOI .nzl (5000/8) l lkg-K (5000/8)J lke.K *y \PV= A simple dimensional analysis tells you that the specific heat per mol divided by the'spiecific heat per mass is the mass per =Fr A $r/ =1. /P ffi in 32 1 | r ,: ,O*Ug/mol :32glmol + 02 ,i I ,t l!1- {, I a lr' It- ,I LI c) First we determine that 57g of Fl2 corresponds to nz : 57 g/(3S S/mol) -'",/ * mol. Then the specific heht equation reads:..2 ']n:tiff i 2r., 3. 3 15 i_(n1 +_):_rt1 +_. 10.--. 2, 2.'4 1 ' 21(2nt + 3) : 30nr + 75 jr .'.(42 - 30)n1 :75 - 63 + nr - 1'. tt- ti i I.r r I '. j" I''t -l' t''".i 1',t'-'l Irf I PHY 206 EXAM III ; Apf. 9, 2008 C . NAME: . . SIGNATURE: I I ID: .t. I I 1. 2. a J. I ' Som'e.relations vou mav"need: a2o-a_Lo-a, r 0r2 - u2 0t2 .t,' n.1^sin 0t : n2sin02 " +?Z - U4l,sstR (i+il: cos r cos yasiir r siny , sin2r+cos2h:I 1* H 5 (1?o) 1. The following expression is proposed as'a solution of the wave equation: t- a@, t) - A sinlk (L - r)] cos(c,.'l), ' " where A, k,, L, aind a are constants. _ . a) Show that it is a solution of the wave equation, or more precisely, find a condition involving some of the constants that ensures it is a solution. b) This expression"is to represent standing waves on a string (7 : 2rf w and ) - 2nlk'are the peiiod and wavelength). One end of, the string is at r - 0 and ihe other end is at tr : tr. Suppose the end at r - 0 is tied down so that A : 0 there forall time. What does this condition imply about the relationship between ) and Z , (this specifies the normal modes of vibration)? c) Using the axes below,'plot the two longest-wavelength ' modes of vibration at time t : T 12. H_tlt Solution: a). The wave equations is on the -A \N I l : - k A coslk(L-r)] cos(c..'t) ;' - -w A sinlk (L -r)l sin(alf) ; Now put these results in the wave equation: -k'a(*,t) : \w2y(r,t)u. which is satisfie d if u2 - (w lk)2 . >Y r ora ./ l'c:-- u2,0t2 A2o, # : -t*Asinfk(r-r)] cos(r,.'t) : -k2a@,t) 0'a ) t . 17 /r \ 1 / ;# - -r2 Asinfk(I-r)l cos(urt) :'-r2,y(r,t) o'a' A"' 0a 0r 0y a 1'' h b; 'l\' a\,t) - Asih(kp)cos(ut) :0+.sin(k,t) :0 +kL\-Lmtr, in-0,!,2,...U\ J / .i i'-- =* .\ : 2Lf m, . TrL : I:2,,'3, ... ' I 6) 'ih" t*o longest wavelength riormal modes "oir"rporrd tb rn : 1, and ni:'2. Note that y(Ltr) -- 0, so the right'hand'end rnust also be tied down (i:e. a node). To plot these two modes at t : T 12, check a point (that's not a node!) such as r-: Ll2 (for.m _- 1) and r = L/4 (for T:2):'. u ' : .nL - 1 + ,\ - 2L: y(Ll2,T12) - Asinlk(L - Ll2)]c.os@r12)n.t' f l* r.1 - .4 sin l;; I cos(zr) - .:A - L-" - ) ,. rrL:2 + ),: L; y(Ll4,f l4 - Asinlk(L -'Ll4)lcos(uT12) .,--', lzTgrl , \ , ' .r ='i, qrnl+;1cos(r) -1 ' * L- J ,I This is,enough to draw the plots shown. t. ,* I P I i I I I I I I I, j I 'i I I I I i I I I I t I "l I I l .t (1 Jt' 1 l r lI l 1 I .1 J I .J l I l' 1 l ,LI I I l , -) l PHY 206 FINAT EXAM NAME:M.y. 5, 2OO8 ' lrr -: , ( SIGNATURE: a ,ID: 1. '2. t.1 J. 4. 5. . $ome relations you may need: .1 2p + psa * ioy? - const. dQ = mCd'T dQ : :",1:T- . L,L-: aLsLT Lv -- pvoar # : "f+, P - oAeTa pV : ?RT -," dQ - d,(l+d,W .. dW - pdV p.V' : cbns,t. 'y : cp/cv f - 1 , 3- _ R ", : iR I KEporttcle ): ,*u;*r: ifu, , kB : lrla ,-!a--1- W4 ds-Q ",- Qun, t lQo"l @u T 0'a L*a : a.r,: ,"# 'Tr1sind1 - rl2Sindz "ry .-? : *#' o' "" 70) 1. A Vpnturi tube consists of a pipe having regions sectional areas, l.1 and 42, resp€ctively, through po is flowing. The air flow causes liquid (density p) to be displaced so that the level heights on either t. with diftering crosS- which air of. density in a separate u*tube side differ by h. terms cancel since we take our a) Find the aiq speed u2 (in the region witb cross-sectional area A2) in terms oj ut, Ar, and A2. b) Compute the pressure difference, pt-pz,-between the two sides of the u-tube in terms of po, ut,At, and A2 fif you couldn't solve a), use pa, 't)1, and u2] c) F ind an expression for the height h. Solutioni. , a) Continuity of the air volume'flow rate dictates, Apt - Azuz ) uz: *r, b) Appl;ling the Bernouilii equation to point, in th" airflow just above the ' sides of the u-tube yields: h*t^r^u?:Pz+!P"3zz (The gravitational potential energy points at the same height) 7 ,, ,' 1? Pr - p? - |0"(u3 - "?) - )o"u? c) The weight of the liquid of height h is balanced by forces associated.with the pressure difference. Let sectional area of the u-tube: . frr\'- l\tz / , the A 1l I difference in be the cross- PgAh:(P'r-Pr)A*h: p,b?[f*l'-1]/\ \Pr - Pz) 2pg '2. A liquid with volume exp-ansion coeffici ent p just 'fills a thin-walled, spherical container <jf volume V at temperature T. Th'e'"container has volume expansion coefficient go < 0. When the'terhperature in- cr€ases by A" the liquid is free to expand into an.open tube with c_ross-sectional area A proje,"cting from the top of .the sphere'. Assume the container and liquid are in thermal equilibrium throughout and the tube does not erpand. . nA a) Write down expressitins for the vol- .ume changes of th'e container and liquid. b) fo what height h does the liquid rise in the tube T!AT Solution: a) container : LV" - PyV LT, liquid : LU - PV LT .i b) The difference in the volume chdnges must equal the volume.of liquid that goes up the tube: '. -s tl \#v T "V' Ah + h: A(P - 0o)LT. \ p\I
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