Como pensou
We need answer in Portuguese, show development item by item. Need solve question. Let's parse.
Question: A system, composed of one mole ideal gas, initial state P1,V1,T1. undergoes state change in four steps:
- Etapa I - compressão lenta e isotérmica a P2,V2.
- Etapa II - compressão muito rápida a P3,V3,T3.
- Etapa III - expansão lenta e isotérmica a P4,V4.
- Etapa IV - expansão muito rápida de volta ao estado inicial a P1,V1,T1.
Second and fourth stages so rapid no heat exchange between system and environment (adiabatic).
a) sketch P x V graph, identifying steps.
b) considering W1,W2,W3,W4 works in each step, show total work in described process reduces to Wtot = W1 + W3.
Need answer. Need maybe derive.
Let's understand process.
Initial state 1: (P1,V1,T1). Step I isothermal compression slowly to (P2,V2) at T1 (since isothermal). So T2 = T1. P1 V1 = P2 V2? ideal gas n=1: PV=RT, so P1V1=RT1 = P2V2. Since compression V2<V1, P2>P1.
Step II rapid compression to P3,V3,T3. No heat exchange Q2=0, adiabatic. Since compression, work done on gas, internal energy increases, T3 > T2 = T1? likely T3 > T1. State 3.
Step III slow isothermal expansion to P4,V4. T4 = T3 (isothermal at T3). P3 V3 = P4 V4 = R T3. Since expansion V4>V3, P4<P3.
Step IV rapid expansion back to initial P1,V1,T1. Adiabatic (Q4=0). Expansion, work done by gas, internal energy decreases, T returns to T1. So state 4 to 1 adiabatic.
Need graph P x V: Four points? Steps I and III are isotherms (curves PV=const), II and IV are adiabats (curves PV^γ=const? For ideal gas adiabatic reversible? "muito rápida" no heat exchange but maybe irreversible? However for ideal gas adiabatic process with no heat exchange, if rapid maybe not quasi-static? But likely treat as reversible adiabatic? In thermodynamics, "muito rápida" means adiabatic (Q=0), not necessarily reversible. But for work calculation, if irreversible adiabatic, work equals -ΔU = n Cv (T_initial - T_final)? Need examine. The problem asks show Wtot = W1 + W3, maybe because W2 + W4 = 0? Wait adiabatic work W2 + W4 maybe cancel? Let's see.
For ideal gas, internal energy depends only T. Over cycle, ΔU_total = 0 = Q_total + W_total (with sign convention? Need careful: First law ΔU = Q - W? In Portuguese, work W usually realizado pelo gás? They define W1,W2,W3,W4 as trabalhos em cada etapa. Total work? Need sign. Let's infer.
In many Brazilian thermodynamics: ΔU = Q - W, where W is work done by gas (expansão positive? Actually sometimes W = work done by gas, so ΔU = Q - W; if gas receives work, W negative). They ask show Wtot = W1 + W3. If W2 + W4 cancel? Let's compute.
For adiabatic steps: Q=0, ΔU = -W (if W by gas). For one mole ideal gas, ΔU = Cv ΔT (assuming Cv constant). Thus W = -ΔU = -Cv ΔT? Wait if ΔU = Q - W, then 0 = ΔU + W => W = -ΔU = -Cv ΔT. For compression (T increases), ΔT>0, W<0 (work done on gas). For expansion, ΔT<0, W>0. For step II: W2 = -Cv (T3 - T1) = Cv(T1 - T3). Step IV: W4 = -Cv (T1 - T3) = Cv(T3 - T1) = -W2. So W2 + W4 =0. Then Wtot = W1+W3. This is simple. Even if irreversible, internal energy state function, Q=0, so W = -ΔU = -Cv ΔT for each adiabatic step, regardless of reversibility. So W2+W4=0. Good.
But need graph. Need describe shape. Since steps I and III are isotherms, II and IV adiabats. But note order: I isothermal compression from state 1 to state 2 (lower volume, higher pressure) at T1. II adiabatic compression from state 2 to state 3 (further lower volume? Actually "compressão muito rápida a P3,V3,T3": compression means V3<V2, P3>P2, T3>T1). III isothermal expansion at T3 from state 3 to state 4 (V4>V3, P4<P3). IV adiabatic expansion from state 4 back to state1 (V1>V4? Wait final volume V1; since from state 4 to 1 expansion: V1 > V4? But state 1 initial volume V1; state 4 likely has V4 < V1? Let's think. Overall cycle: compression I, compression II, expansion III, expansion IV. Net work? The cycle likely is a refrigeration? Need graph.
Let's assign volumes: Start V1. Step I isothermal compression: V2 < V1. Step II adiabatic compression: V3 < V2. Step III isothermal expansion: V4 > V3. Step IV adiabatic expansion back to V1: V1 > V4? Since expansion, yes V1 > V4. But can V4 be less than V2? Let's analyze. The cycle consists of two isotherms and two adiabats, but isotherms at T1 and T3; adiabats between them. This is like Carnot cycle? Wait standard Carnot cycle has two isotherms and two adiabats. Here order: isothermal compression at T_low? Actually T1 maybe lower than T3? Since adiabatic compression raises T from T1 to T3, so T3 > T1. Then isothermal expansion at T_high T3, then adiabatic expansion back to T1. This is a Carnot cycle? Standard Carnot: isothermal expansion at T_high, adiabatic expansion to T_low, isothermal compression at T_low, adiabatic compression back to T_high. Here order: isothermal compression at T1 (low), adiabatic compression to T3 (high), isothermal expansion at T3 (high), adiabatic expansion to T1 (low). So it's reversed Carnot? Actually if T1<T3, then isothermal compression at low T, adiabatic compression to high T, isothermal expansion at high T, adiabatic expansion to low T. This is a Carnot cycle but direction? Standard heat engine: high T isothermal expansion, adiabatic expansion to low T, low T isothermal compression, adiabatic compression to high T. Here first isothermal compression at low T, then adiabatic compression to high T, then isothermal expansion at high T, then adiabatic expansion to low T. That's a refrigerator/heat pump? Let's see: Work input? For heat engine, net work positive (area clockwise). Here sequence: compression at low T (work input), compression adiabatic (work input), expansion at high T (work output), expansion adiabatic (work output). Net maybe positive? Let's calculate area: From 1 to 2: compression at T1, work negative (gas receives). 2 to 3: adiabatic compression, work negative. 3 to 4: isothermal expansion at T3, work positive. 4 to 1: adiabatic expansion, work positive. Net area may be positive if high T expansion > low T compression? Since high T isotherm area larger? Actually if V4 and V1? Let's determine. For Carnot, if T3>T1, isothermal expansion at T3 from V3 to V4, isothermal compression at T1 from V1 to V2, and adiabatic relations: T1 V1^{γ-1} = T3 V4^{γ-1}? Wait for adiabatic from 4 to 1: T3 V4^{γ-1} = T1 V1^{γ-1}. For adiabatic from 2 to 3: T1 V2^{γ-1} = T3 V3^{γ-1}. Then V1/V4 = (T3/T1)^{1/(γ-1)}, V2/V3 = (T3/T1)^{1/(γ-1)}? Let's derive: T1 V2^{γ-1}=T3 V3^{γ-1} => V2/V3 = (T3/T1)^{1/(γ-1)} >1, so V2 > V3. Also T3 V4^{γ-1}=T1 V1^{γ-1} => V1/V4 = (T3/T1)^{1/(γ-1)} >1, so V1 > V4. Thus V1 > V4 and V2 > V3. Also V2 < V1 (compression I), V3 < V2 (compression II), V4 > V3 (expansion III). So order of volumes: V3 < V2 < V1? And V3 < V4 < V1? Need compare V4 vs V2. From V2/V3 = V1/V4 = r >1 => V2 = r V3, V1 = r V4. Also V2 < V1 => r V3 < r V4 => V3 < V4. So order: V3 < V4 < V2 < V1? Check V2 vs V4: V2 = r V3, V4 = V1/r. Not necessarily. Example T3/T1=2, γ=1.4, r=2^{2.5}=5.657. If V3=1, V2=5.657; V4 = V1/r. Need V1? V1 maybe > V2? Since V2 < V1, so V1 >5.657. Then V4 = V1/5.657 >1. Could be less or greater than V2? If V1=10, V4=1.77 <5.657. So V4 < V2. So order V3 < V4 < V2 < V1 likely. But graph can be schematic.
Need draw P-V diagram: x-axis V, y-axis P. Four points: 1 (V1,P1) lower pressure? State 1 initial maybe lower pressure than P2? Step I compression: from 1 to 2 along isotherm T1: as V decreases, P increases. So curve 1->2 downward? Actually P increases as V decreases, so from right (V1) to left (V2), curve up. State 2 higher P, lower V. Step II adiabatic compression from 2 to 3: V decreases further, P increases further, T increases. Adiabat steeper than isotherm? In P-V, adiabat has slope -γ P/V, steeper than isotherm slope -P/V. Since γ>1, adiabat steeper. So from 2 to 3, curve continues up-left with steeper slope. State 3 highest P? Probably P3 > P2. Step III isothermal expansion at T3 from 3 to 4: V increases, P decreases along isotherm T3 (higher T). It will cross? State 4 maybe lower P than P3 but higher T; likely P4 could be lower than P1? Let's see. Step IV adiabatic expansion from 4 to 1: V increases to V1, P decreases to P1, T decreases to T1. Adiabat steeper than isotherm? From 4 to 1, expansion, P drops. The curve 4->1 should be adiabat at lower T? Actually between T3 and T1.
Need identify steps on graph: I (1→2) isothermal compression; II (2→3) adiabatic compression; III (3→4) isothermal expansion; IV (4→1) adiabatic expansion.
Need maybe note that steps II and IV are adiabatic (Q=0), so no heat exchange. Could also show arrows.
For b) We need "considerando que W1, W2, W3 e W4 são os trabalhos em cada etapa, mostre que o trabalho total no processo descrito se reduz a Wtot = W1 + W3." Need define sign convention. We can assume W is work done by gas? But they ask show. Let's develop.
Let's use first law for closed system: ΔU = Q - W, where W is work done by the gas. In cycle, ΔU_total = 0, Q_total = Q1+Q2+Q3+Q4. For adiabatic steps Q2=Q4=0. But to show Wtot = W1+W3, need W2+W4=0. For ideal gas, internal energy U depends only on T. For each adiabatic step, Q=0, so ΔU = -W. Thus W = -ΔU = -n Cv ΔT. For one mole, W2 = -Cv (T3 - T1) = Cv(T1 - T3). W4 = -Cv (T1 - T3) = Cv(T3 - T1). Therefore W2 + W4 = 0. Hence Wtot = W1 + W2 + W3 + W4 = W1 + W3. Alternatively use first law for entire cycle: ΔU=0 => Wtot = Q_total = Q1+Q3 (since Q2=Q4=0). But that doesn't show W2+W4=0. Need show. We can also note work in adiabatic processes depends only on temperatures, and T2=T1, T4=T3, so ΔU2 = Cv(T3-T1), ΔU4 = Cv(T1-T3) = -ΔU2, hence W2 = -W4. Need maybe if W sign convention opposite, still W2+W4=0.
Need be careful: In step II, compression rapid: Q=0, work done on gas. If W defined as work done by gas, W2 negative. Step IV expansion, W4 positive. Magnitudes equal because ΔT magnitudes equal? Actually T3-T1 for II; T1-T3 for IV (magnitude same). Yes.
Could also derive using adiabatic relations: For ideal gas, W_adiabatic = (P_f V_f - P_i V_i)/(γ-1)? Wait formula for reversible adiabatic: W = (P1V1 - P2V2)/(γ-1) = nR(T1 - T2)/(γ-1). For step II: W2 = (P2V2 - P3V3)/(γ-1) = R(T1 - T3)/(γ-1) (since P V = RT, n=1). Step IV: W4 = (P4V4 - P1V1)/(γ-1) = R(T3 - T1)/(γ-1). Sum zero. But this assumes reversible adiabatic? Actually formula W = (P_i V_i - P_f V_f)/(γ-1) for reversible adiabatic. But if irreversible adiabatic, the formula may not hold, but internal energy argument holds generally. However in many exams, they may treat "muito rápida" as adiabatic but irreversible? Let's examine.
The problem statement: "A segunda e a quarta etapas são tão rápidas que não há troca de calor entre o sistema e o ambiente." That defines adiabatic (Q=0), not necessarily reversible. But to calculate work in irreversible adiabatic, we cannot use PV^γ=const, but we can use ΔU=Q-W = -W, so W=-ΔU = -Cv ΔT. This is general for any adiabatic process of ideal gas, regardless of reversibility, provided initial and final temperatures known. So W2 = -Cv(T3-T1), W4 = -Cv(T1-T3) = Cv(T3-T1), sum zero. So robust.
Need maybe in b) "mostre que o trabalho total ... se reduz a Wtot = W1 + W3." We can present.
Need maybe mention for cycle ΔU=0, so Wtot = Q_total = Q1+Q3? But not enough. Use adiabatic steps.
Let's craft final answer in Portuguese. Need include graph description maybe textual since no drawing? They ask "esboce o gráfico P x V". As text, we can describe. But maybe need include a sketch? Since it's a text answer, we can describe axes, curves, points, arrows. Could also include ASCII? Probably sufficient to describe. But maybe we should provide a simple diagram? We can't draw, but can describe.
Let's formulate:
a) Esboço: eixos P (ordenada) e V (abscissa). Marcar estados 1,2,3,4.
- Estado 1: (V1,P1), T1.
- Etapa I: compressão isotérmica lenta de 1 até 2 (T1 constante). Curva PV=const, com V2<V1 e P2>P1; no gráfico, curva descendente da esquerda para direita? Actually from 1 to 2: V decreases, P increases. So curve from right (V1) to left (V2), upward. It's a hipérbole.
- Etapa II: compressão adiabática rápida de 2 até 3. Curva mais inclinada que a isoterma (PV^γ=const se reversível; mas em qualquer caso adiabática), com V3<V2, P3>P2, T3>T1. Seta de 2 para 3.
- Etapa III: expansão isotérmica lenta de 3 até 4 (T3 constante). Curva PV=const, com V4>V3, P4<P3. Seta de 3 para 4.
- Etapa IV: expansão adiabática rápida de 4 até 1. Curva adiabática, com V1>V4, P1<P4, T1<T3. Seta de 4 para 1.
O ciclo fica no sentido 1→2→3→4→1. As etapas II e IV são adiabáticas (Q=0); I e III são isotérmicas. As isotermas I e III estão em temperaturas T1 e T3 (T3>T1), e as adiabáticas II e IV conectam essas isotermas.
Maybe also note relative positions: V3 < V4 < V2 < V1? Let's verify with Carnot. Let's derive order maybe: From adiabatic relations: T1 V2^{γ-1}=T3 V3^{γ-1} => V2/V3=(T3/T1)^{1/(γ-1)}>1 => V2>V3. T3 V4^{γ-1}=T1 V1^{γ-1} => V1/V4=(T3/T1)^{1/(γ-1)}>1 => V1>V4. Also V2<V1 (I), V4>V3 (III). Compare V4 and V2: V4 = V1 / r, V2 = r V3? Wait r=(T3/T1)^{1/(γ-1)}. V1>V2 = r V3? Actually V2 = r V3. V4 = V1 / r. Since V1 > V2 = r V3, V4 > (r V3)/r = V3. But V4 could be less than V2 if V1 < r^2 V3? Not necessarily. Let's use known Carnot cycle: V1 (after adiabatic expansion) > V4 (before) and V2 (after isothermal compression) > V3 (after adiabatic compression). Also V4 > V3? Yes. Compare V2 and V4: V2/V4 = (r V3)/(V1/r) = r^2 V3 / V1. Since V1 = r V4 => V2/V4 = r V3 / V4? Hmm. For Carnot, the order of volumes depends on temperatures and γ. But not needed. We can just describe qualitatively.
Maybe in graph, step III is isothermal expansion at T3 from smaller volume to larger volume, but it may not cross to right of V1? It could be V4 < V1. Since step IV expands to V1. So V4 is left of V1. Step I starts at V1 and compresses to V2; V2 maybe right of V3. So V3 < V2 < V1 and V3 < V4 < V1. The relative V2 vs V4 uncertain. But can draw typical.
b) Development:
Pela Primeira Lei: ΔU = Q - W (W realizado pelo gás). Para 1 mol de gás ideal, U = Cv T (ou ΔU = Cv ΔT).
Etapa II (adiabática): Q2 = 0. Como T2 = T1 (etapa I isotérmica) e o estado final é T3:
ΔU2 = Cv(T3 - T1). Assim, W2 = Q2 - ΔU2 = -Cv(T3 - T1) = Cv(T1 - T3).
Etapa IV (adiabática): Q4 = 0. Estado inicial T4 = T3 (etapa III isotérmica) e final T1:
ΔU4 = Cv(T1 - T3). Assim, W4 = Q4 - ΔU4 = -Cv(T1 - T3) = Cv(T3 - T1).
Portanto, W2 + W4 = Cv(T1 - T3) + Cv(T3 - T1) = 0.
O trabalho total no ciclo é:
Wtot = W1 + W2 + W3 + W4 = W1 + W3 + (W2 + W4) = W1 + W3.
Como queríamos demonstrar.
Maybe if using ΔU = Q + W? In some conventions W is work done on system, then ΔU = Q + W; then W2 + W4 =? Let's be consistent. In Brazilian IME? Usually "trabalho" in thermodynamics: W = work done by gas? Let's see from statement: "considerando que W1, W2, W3 e W4 são os trabalhos em cada etapa" no sign. In many Brazilian physics, work done by gas is positive when expansion; first law ΔU = Q - W. If they use ΔU = Q + W (work received), then W2+W4=0 still? Let's check: If W received, adiabatic ΔU = W_received = Cv ΔT. For step II, ΔU = Cv(T3-T1) positive, W2_received = Cv(T3-T1). Step IV, ΔU = Cv(T1-T3) negative, W4_received = Cv(T1-T3). Sum = 0. Then total W_received = W1+W3? But W1+W3 maybe negative/positive? But same. So okay.
Need maybe mention "desprezando variação de energia cinética/potencial" etc.
Let's ensure no other nuance: The problem says "um sistema, composto por um mol de um gás ideal, está em um estado inicial a uma pressão P1, volume V1 e temperatura T1. Tal sistema sofre mudança de estado em quatro etapas:" Then list. "A segunda e a quarta etapas são tão rápidas que não há troca de calor entre o sistema e o ambiente." So indeed adiabatic. They ask "a) esboce o gráfico P x V do processo descrito, identificando as etapas. b) considerando que W1, W2, W3 e W4 são os trabalhos em cada etapa, mostre que o trabalho total no processo descrito se reduz a Wtot = W1 + W3."
Maybe there is another possible answer: For adiabatic processes, work equals area under curve; maybe they want show W2 = -W4 by comparing areas? But internal energy easier.
Let's think if there is any trick: In step II and IV, "muito rápida" implies no heat exchange, but also maybe irreversibility? However for ideal gas, internal energy depends only on T, so regardless of path, ΔU = Cv ΔT. So yes.
Need maybe discuss sign of work: For compression, W negative if work done by gas. In step II compression, W2 <0; step IV expansion, W4 >0; sum zero. In final answer, perhaps state "adotando W como trabalho realizado pelo gás". But if not, just show.
Let's craft final response with item a and b.
Potential final:
a) No gráfico P×V, marcar:
- Eixo horizontal: V; vertical: P.
- Estado 1: (V1,P1), sobre a isoterma T1.
- I: curva 1→2, isoterma (PV=cte) de compressão; V2<V1, P2>P1.
- II: curva 2→3, adiabática de compressão; V3<V2, P3>P2, T3>T1; curva mais inclinada que a isoterma.
- III: curva 3→4, isoterma (PV=cte) de expansão; V4>V3, P4<P3, temperatura T3.
- IV: curva 4→1, adiabática de expansão; V1>V4, P1<P4, retornando a T1.
As setas indicam 1→2→3→4→1. As etapas I e III são lentas/isotérmicas; II e IV são rápidas/adiabáticas (Q=0).
b) Pela 1ª Lei da Termodinâmica para 1 mol de gás ideal:
ΔU = Q - W, com U = Cv T (Cv constante).
Etapa I: isotérmica, T2=T1.
Etapa II: adiabática, Q2=0. Logo ΔU2 = Cv(T3-T1) = -W2 ⇒ W2 = -Cv(T3-T1) = Cv(T1-T3).
Etapa III: isotérmica, T4=T3.
Etapa IV: adiabática, Q4=0. Logo ΔU4 = Cv(T1-T3) = -W4 ⇒ W4 = -Cv(T1-T3) = Cv(T3-T1).
Portanto, W2 + W4 = Cv(T1-T3) + Cv(T3-T1) = 0.
Assim:
Wtot = W1+W2+W3+W4 = W1+W3+(W2+W4) = W1+W3.
Como se queria demonstrar.
Need final line "Resposta final: a) ...; b) Wtot = W1 + W3." The user asked "Termine com uma linha neste formato: Resposta final: <o resultado de cada item, de forma curta>". So final line should include both items.
Let's ensure no extra after final. Need answer in Portuguese. Could include "a) gráfico descrito acima..." But final line short.
Let's maybe include a simple ASCII graph? Might be too much. The prompt says "esboce o gráfico" but in text answer, describing is okay. However, maybe to be safe, we can include a small schematic in words. Since it's an exam, a drawing is expected, but text description sufficient.
Let's maybe format:
a) Esboço: ...
Maybe include coordinates:
1 (V1,P1); 2 (V2,P2); 3 (V3,P3); 4 (V4,P4). Curvas:
I: 1→2, isoterma T1, côncava? Actually PV=const, convexa? In P-V, isotherm is convex? P = nRT/V, second derivative positive? dP/dV=-P/V; d²P/dV²=2P/V²>0, convex (upward). Adiabatic P = C V^{-γ}, d²P/dV² = γ(γ+1) C V^{-γ-2} >0, also convex but steeper. So both convex.
Maybe note "As curvas I e III são hipérboles equiláteras; II e IV são curvas adiabáticas, mais inclinadas que as isotermas."
Let's final.