The cardiovascular counter-current heat exchanger has an overall heat transfer coefficient of \(100 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Arterial blood enters at \(37^{\circ} \mathrm{C}\) and exits at \(27^{\circ} \mathrm{C}\). Venous blood enters at \(25^{\circ} \mathrm{C}\) and exits at \(34^{\circ} \mathrm{C}\). Determine the mass flow rates of the arterial blood and venous blood in \(\mathrm{g} / \mathrm{s}\) if the specific heat of both arterial and venous blood is constant and equal to \(3475 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\), and the surface area of the heat transfer to occur is \(0.15 \mathrm{~cm}^{2}\).

Short Answer

Expert verified
Answer: The mass flow rate of the arterial blood is approximately \(4.03 \frac{g}{s}\), and the mass flow rate of the venous blood is approximately \(4.47 \frac{g}{s}\).

Step by step solution

01

(Step 1: Calculate the logarithmic mean temperature difference)

We first need to calculate the logarithmic mean temperature difference between the arterial and venous blood, which we will use in the heat transfer equation. The formula is: \(\Delta T_{LM} = \frac{(\Delta T_1 - \Delta T_2)}{\ln(\frac{\Delta T_1}{\Delta T_2})}\) where \(\Delta T_1 = T_{Ain} - T_{Vin}\) and \(\Delta T_2 = T_{Aout} - T_{Vout}\). The given temperature values are: \(T_{Ain} = 37^\circ C\) \(T_{Aout} = 27^\circ C\) \(T_{Vin} = 25^\circ C\) \(T_{Vout} = 34^\circ C\) Plugging in these values, we have: \(\Delta T_1 = 37^\circ C - 25^\circ C = 12^\circ C\) \(\Delta T_2 = 27^\circ C - 34^\circ C = -7^\circ C\) Now, we can find the \(\Delta T_{LM}\): \(\Delta T_{LM} = \frac{(12 - (-7))}{\ln(\frac{12}{-7})} = 9.378^\circ C\)
02

(Step 2: Calculate the rate of heat transfer)

Now that we have the \(\Delta T_{LM}\), we can plug it into the heat transfer equation along with the given overall heat transfer coefficient \(U = 100 \frac{W}{m^2 K}\) and the surface area \(A = 0.15 cm^2 = 1.5 \times 10^{-5} m^2\) to find the rate of heat transfer \(Q\): \(Q = U \cdot A \cdot \Delta T_{LM} = 100 \frac{W}{m^2 K} \cdot 1.5 \times 10^{-5} m^2 \cdot 9.378 K = 0.014 W\)
03

(Step 3: Relate mass flow rates to the rate of heat transfer and specific heat)

The heat transfer between arterial and venous blood can be related to the mass flow rates of each blood type and the specific heat using the equation, \(Q = m_a \cdot c_p \cdot (T_{Ain} - T_{Aout}) = m_v \cdot c_p \cdot (T_{Vin} - T_{Vout})\) Where \(m_a\) is the mass flow rate of arterial blood, and \(m_v\) is the mass flow rate of venous blood. The specific heat for both arterial and venous blood is \(c_p = 3475\frac{J}{kgK}\). Since we know the specific heat and temperature differences for both blood types, we can divide the equation by \(c_p\) and plug in the temperature values: \(\frac{Q}{c_p} = m_a (37-27) = m_v (25-34)\)
04

(Step 4: Calculate mass flow rates)

Now we can substitute the value of \(Q\) calculated in step 2 and solve for the mass flow rates: \(\frac{0.014W}{3475\frac{J}{kgK}} = m_a (10K) = m_v (-9K)\) Solving for \(m_a\) and \(m_v\), we get: \(m_a = \frac{0.014W}{3475\frac{J}{kgK} \cdot 10K} = 4.03 \times 10^{-6} kg/s\) \(m_v = -\frac{0.014W}{3475\frac{J}{kgK} \cdot 9K} = 4.47 \times 10^{-6} kg/s\) Finally, we convert these values to grams per second: \(m_a = 4.03 \times 10^{-6} kg/s \cdot \frac{1000g}{1kg} = 4.03 \frac{g}{s}\) \(m_v = 4.47 \times 10^{-6} kg/s \cdot \frac{1000g}{1kg} = 4.47 \frac{g}{s}\) #Conclusion# The mass flow rate of the arterial blood is approximately \(4.03 \frac{g}{s}\), and the mass flow rate of the venous blood is approximately \(4.47 \frac{g}{s}\).

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Most popular questions from this chapter

In a chemical plant, a certain chemical is heated by hot water supplied by a natural gas furnace. The hot water \(\left(c_{p}=\right.\) \(4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K})\) is then discharged at \(60^{\circ} \mathrm{C}\) at a rate of \(8 \mathrm{~kg} / \mathrm{min}\). The plant operates \(8 \mathrm{~h}\) a day, 5 days a week, 52 weeks a year. The furnace has an efficiency of 78 percent, and the cost of the natural gas is \(\$ 1.00\) per therm ( 1 therm \(=105,500 \mathrm{~kJ})\). The average temperature of the cold water entering the furnace throughout the year is \(14^{\circ} \mathrm{C}\). In order to save energy, it is proposed to install a water-to-water heat exchanger to preheat the incoming cold water by the drained hot water. Assuming that the heat exchanger will recover 72 percent of the available heat in the hot water, determine the heat transfer rating of the heat exchanger that needs to be purchased and suggest a suitable type. Also, determine the amount of money this heat exchanger will save the company per year from natural gas savings.

Ethanol is vaporized at \(78^{\circ} \mathrm{C}\left(h_{f g}=846 \mathrm{~kJ} / \mathrm{kg}\right)\) in a double-pipe parallel-flow heat exchanger at a rate of \(0.03 \mathrm{~kg} / \mathrm{s}\) by hot oil \(\left(c_{p}=2200 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) that enters at \(120^{\circ} \mathrm{C}\). If the heat transfer surface area and the overall heat transfer coefficients are \(6.2 \mathrm{~m}^{2}\) and \(320 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), respectively, determine the outlet temperature and the mass flow rate of oil using \((a)\) the LMTD method and \((b)\) the \(\varepsilon-\mathrm{NTU}\) method.

Can the temperature of the hot fluid drop below the inlet temperature of the cold fluid at any location in a heat exchanger? Explain.

Saturated water vapor at \(40^{\circ} \mathrm{C}\) is to be condensed as it flows through the tubes of an air-cooled condenser at a rate of \(0.2 \mathrm{~kg} / \mathrm{s}\). The condensate leaves the tubes as a saturated liquid at \(40^{\circ} \mathrm{C}\). The rate of heat transfer to air is (a) \(34 \mathrm{~kJ} / \mathrm{s}\) (b) \(268 \mathrm{~kJ} / \mathrm{s}\) (c) \(453 \mathrm{~kJ} / \mathrm{s}\) (d) \(481 \mathrm{~kJ} / \mathrm{s}\) (e) \(515 \mathrm{~kJ} / \mathrm{s}\)

A 2-shell passes and 4-tube passes heat exchanger is used for heating a hydrocarbon stream \(\left(c_{p}=2.0 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\) steadily from \(20^{\circ} \mathrm{C}\) to \(50^{\circ} \mathrm{C}\). A water stream enters the shellside at \(80^{\circ} \mathrm{C}\) and leaves at \(40^{\circ} \mathrm{C}\). There are 160 thin-walled tubes, each with a diameter of \(2.0 \mathrm{~cm}\) and length of \(1.5 \mathrm{~m}\). The tube-side and shell-side heat transfer coefficients are \(1.6\) and \(2.5 \mathrm{~kW} / \mathrm{m}^{2} \cdot \mathrm{K}\), respectively. (a) Calculate the rate of heat transfer and the mass rates of water and hydrocarbon streams. (b) With usage, the outlet hydrocarbon-stream temperature was found to decrease by \(5^{\circ} \mathrm{C}\) due to the deposition of solids on the tube surface. Estimate the magnitude of fouling factor.

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