Answer:
Na2SO4= 0.04mol/L
Na3PO4=0.07mol/L
Li2SO4=0.02mol/L
Mol/L= M or Molarity
Explanation:
Step 1
Find the molar mass for each compound (molar mass unit is g/mol and is equal to the mass number present on the element)
Na2SO4 = 142g/mol
Na2= (23*2)=46g/mol
S=32g/mol
O3=(16*4)=64g/mol
Hence, 46+32+64=142 g/mol
Na3PO4= 164g/mol
Li2SO4=110g/mol
Step 2
Using the molar mass determine the mols of each compound. (mol=g/molar mass)
Na2SO4 = 0.004mol
0.53g/142gmol
=0.00373mol
=0.004mol
Na3PO4= 0.007
Li2SO4=0.002
Step 3
Calculate the Molarity (mol/L)
Na2SO4= 0.04mol/L
100mL/1000= 0.1L
NB Molarity is always in the units mol/L hence we must convert mL into L
0.004/0.1
=0.04mol/L
Na3PO4= 0.07mol/L
Li2SO4=0.02mol/L
The elementary exothermic reversible reaction A + BC is carried out in a PBR with a heat exchanger surrounding the reactor. The feed is equimolar in A and B with FAO = 5 mol/s. The coolant surrounding the PBR flows in the same direction as the reactant. 1) For the base case given below, plot X, X, Y, T, To, -TA, HC, LHGx, and LHRQ as a function of the catalyst weight, then explain the variables behavior. T =325 K, P = 8 atm, W = 2000 kg, a = 0.0002 kg ¹ FX C=C₁ =20, C = 30 cal/mol/K, AH = -20,000 cal/mol at 298 K 0₁ =1 C₁ = 40 cal/mol/K, cal Ual p=0.5- with T300 K, m = 50 g/s, C₁ =1.8 cal/g/K kg.s. K k = 0.004/²/(mol-kg-s) at 310 K with E = 25,000 cal/mol K = 1000 l/mol at 303 K
The variables X, X1, Y, T, To, -TA, HC, LHGx, and LHRQ are plotted as a function of the catalyst weight.
What variables are plotted as a function of catalyst weight in the given scenario?In the given scenario, the exothermic reversible reaction A + BC is taking place in a PBR (Packed Bed Reactor) with a surrounding heat exchanger. The feed is equimolar in A and B, and the feed rate of A (FA0) is 5 mol/s. The coolant flow in the heat exchanger is in the same direction as the reactant flow.
The variables X, X1, Y, T, To, -TA, HC, LHGx, and LHRQ are plotted as a function of the catalyst weight in the base case.
X represents the extent of reaction.X1 represents the extent of reaction for the forward reaction.Y represents the extent of reaction for the backward reaction.T is the temperature.To is the reference temperature.TA is the temperature difference between T and To.HC is the heat capacity.LHGx represents the latent heat of reaction.LHRQ represents the heat of reaction.The behavior of these variables with respect to the catalyst weight will be explained based on the specific values and equations provided in the problem.
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The Riverside anaerobic digester produces a sludge that has a total solids concentration of 4 %. They are investigating a filter press that will yield a solids concentration of 24%. If they now produce 36 m3 /d of digested sludge, what annual volume savings will they achieve by using the press? (Assume digested sludge and dewatered sludge have the same density that is the same as water density)
The annual volume savings achieved by using the filter press at the Riverside anaerobic digester is approximately 41,610 m3/year.
To calculate the annual volume savings, we need to compare the volume of digested sludge produced without the press to the volume produced with the press.
Calculate the volume of digested sludge produced without the press:
The digested sludge produced per day is 36 m3. To calculate the annual volume, we multiply this value by the number of days in a year (365):
36 m3/day * 365 days = 13,140 m3/year
Calculate the volume of digested sludge produced with the press:
The solids concentration of the sludge produced by the filter press is 24%. This means that 24% of the volume is solids, while the remaining 76% is water. Since the density of the sludge is assumed to be the same as water density, the volume of solids and water will be the same.
Therefore, the volume of digested sludge produced with the press can be calculated by dividing the volume of digested sludge produced without the press by the solids concentration:
13,140 m3/year / (24% solids) = 54,750 m3/year
Calculate the volume savings:
The volume savings can be obtained by subtracting the volume produced with the press from the volume produced without the press:
13,140 m3/year - 54,750 m3/year = -41,610 m3/year
The negative value indicates a reduction in volume, which represents the annual volume savings. However, since negative volume savings are not meaningful in this context, we can take the absolute value to get a positive result:
|-41,610 m3/year| = 41,610 m3/year
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Determine expressions for GR, HR, and SR implied by
the three-term virial
equation in volume, Eq. (3.38).
The three-term virial equation in volume, Eq. (3.38), can be written as PV = RT(1 + B'P + C'P^2), where P is the pressure, V is the molar volume, R is the gas constant, T is the temperature.
B' and C' are the second and third virial coefficients, respectively.
In order to determine the expressions for GR (Gibbs energy), HR (enthalpy), and SR (entropy) implied by this equation, we can differentiate the equation with respect to temperature (T) at constant pressure (P).
The resulting expressions are as follows.
For GR (Gibbs energy).
∂GR/∂T|P = R(1 + B'P + C'P^2)
For HR (enthalpy).
∂HR/∂T|P = ∂(GR + PV)/∂T|P = ∂GR/∂T|P + P.
For SR (entropy).
∂SR/∂T|P = (∂HR/∂T|P) / T = (∂GR/∂T|P + P) / T.
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development of a nose-only inhalation toxicity test chamber that provides four exposure concentrations of nano-sized particles
The development of a nose-only inhalation toxicity test chamber aims to provide controlled exposure to nano-sized particles at four different concentrations. This test chamber allows for precise evaluation of the toxic effects of these particles on the respiratory system.
The nose-only inhalation toxicity test chamber is designed to expose test subjects, typically laboratory animals, to the inhalation of nano-sized particles under controlled conditions. The chamber ensures that only the nasal region of the animals is exposed to the particles, simulating real-life inhalation scenarios. By providing four exposure concentrations, researchers can assess the dose-response relationship and determine the toxicity thresholds of the particles.
The chamber's design includes specialized features such as airflow control, particle generation systems, and sampling equipment to monitor and regulate the particle concentrations. This controlled environment enables researchers to study the potential adverse effects of nano-sized particles on the respiratory system, contributing to a better understanding of their toxicity and potential health risks for humans exposed to such particles.
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If
Half life of an isotope is 12 days and it was assumed that the
person ate 400 Bq of isotope. Using the GI track model information,
calculate the number of transformations in Stomach
If half life of an isotope is 12 days, then there are about 820.42 transformations in the stomach after the person ate 400 Bq of the isotope.
Using the GI track model information, the number of transformations in Stomach can be calculated as follows :
We know that the half-life of an isotope is defined as the time taken for half of the radioactive atoms to decay.
The decay of the isotope can be represented by the following formula : N(t) = N0e^(-λt)
where:
N(t) = Number of atoms at time t
N0 = Initial number of atoms
λ = Decay constant
t = Time elapsed from the initial time t = 0
For a given isotope, the decay constant is related to the half-life as follows : λ = 0.693/T1/2
where : T1/2 = Half-life time of the isotope
Given that the half-life of the isotope is 12 days, we can calculate the decay constant as follows :
λ = 0.693/12 = 0.0577 day^(-1)
The number of transformations in the stomach can be calculated by using the following formula :
Activity = A0e^(-λt)
where : A0 = Initial activity of the isotope in Bq
λ = Decay constant
t = Time elapsed from the initial time t = 0
Activity = 400 Bq (Given)
Decay constant (λ) = 0.0577 day^(-1)
Time elapsed (t) = Time taken by the isotope to reach the stomach from the time of consumption = 0.17 days (Given by GI track model)
Therefore, the number of transformations in the stomach is :
Activity = A0e^(-λt)A0 = Activity/e^(-λt)A0 = 400 Bq/e^(-0.0577 × 0.17)A0 = 400 Bq/e^(-0.009809)A0 = 447.45 Bq
The number of transformations in the stomach can be calculated as follows :
Number of transformations = Activity decayed per unit time/Disintegration constant
Activity decayed per unit time = A0 - Activity after time elapsed
Activity decayed per unit time = 447.45 - 400 = 47.45 Bq
Disintegration constant = Decay constant = 0.0577 day^(-1)
Therefore, number of transformations = (447.45 - 400) Bq/0.0577 day^(-1)
Number of transformations = 820.42
This means that there are about 820.42 transformations in the stomach after the person ate 400 Bq of the isotope.
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1). For a CSTR you have the following data, X = 0.5, molar flow rate of A (n) = 4 mol/min., Caº = 1 mol/l, k = 0.2 min¹. Assume liquid phase reaction and first order kinetics. n a). Calculate the Volume for the CSTR
The volume of the CSTR is equal to 4 liters.
To calculate the volume for the CSTR (Continuous Stirred Tank Reactor), we can use the equation:
Volume = (Molar Flow Rate of A) / (Reactant Concentration)
Given:
Molar Flow Rate of A (n) = 4 mol/min
Reactant Concentration (Caº) = 1 mol/l
Substituting these values into the equation, we have:
Volume = 4 mol/min / 1 mol/l
The unit of mol/min cancels out with mol in the denominator, leaving us with the unit of volume, which is liters (l).
Therefore, the volume for the CSTR is 4 l.
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1. Air (at 1 atm) contains 400 ppm carbon dioxide (CO2). After the rainwater and air are completely mixed and balanced, the rainwater infiltrates into the groundwater layer containing calcium carbonate (CaCO3). H.O - H+ + OH K = 104 M CO2)+H20 - H.CO Ky = 10-15 (= 3.16 x 104) M atm H.COZ HCO3+H* K1 = 1063 (=5.0 x 107) HCO, CO,? +H K2 = 10-10.3 (=5.0 10") M CaCO36) 00, +Ca? K.p - 10-8 (-5.0 x 109) M (1) Calculate the pH of the rainwater before mixing and balancing with air? (2) Calculate the pH of the rainwater after mixing and balancing with air?
(1) The pH of rainwater before mixing and balancing with air is approximately 5.6.
(2) After mixing and balancing with air, the pH of rainwater decreases to around 5.2.
In the first step, the pH of rainwater before mixing and balancing with air can be calculated using the dissociation of carbon dioxide (CO₂) in water. The given equilibrium constant (K) values represent the dissociation reactions involved.
From the given equilibrium constant K₂, we can determine that most of the dissolved carbon dioxide in rainwater will be present as bicarbonate ions (HCO₃⁻) and some as carbonate ions (CO₃²⁻).
The presence of carbonic acid (H₂CO₃) formed from the reaction between CO₂ and water leads to a decrease in pH. Therefore, the pH of rainwater before mixing and balancing with air is around 5.6.
After mixing and balancing with air, the concentration of carbon dioxide increases due to its presence in the air, leading to the formation of more carbonic acid in the rainwater. This increase in carbonic acid concentration lowers the pH of rainwater. Consequently, the pH of rainwater after mixing and balancing with air decreases to around 5.2.
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Calculate the reaction rate when a conversion of 85% is reached and
is known that the specific speed is 6.2 dm3 / mol s
The reaction rate at a conversion of 85% is approximately 5.27 dm3/mol·s.
The reaction rate can be calculated using the specific speed and the conversion of the reaction. The specific speed is a parameter that relates to the rate of reaction and is expressed in units of volume per mole of reactant per unit time (dm3/mol·s).
To calculate the reaction rate, we multiply the specific speed by the conversion of the reaction. In this case, the conversion is given as 85%, which can be written as 0.85.
Reaction rate = Specific speed × Conversion
= 6.2 dm3/mol·s × 0.85
≈ 5.27 dm3/mol·s
Therefore, when a conversion of 85% is reached, the reaction rate is approximately 5.27 dm3/mol·s.
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Q13- The color of Solid material formed in the reaction Na₂CO3 +CaCl₂ CaCO3 (s) + 2NaCl is ... and it separate from solution by-----------
A) Whitel vacuum filtration B) Pink oven. C) Colorless air dry D) Colorless oven Q14- What is the greatest amount of MgO (in grams) that can be made of 15.6 moles Mg and 9.4 moles of O? D) 62. G C) 624g A) 376 g B) 37.8 g
1. The color of the solid material formed in the reaction Na2CO3 + CaCl2 -> CaCO3(s) + 2NaCl is white. It can be separated from solution by filtration. (option A)
2. The greatest amount of MgO that can be made is 376g (option A)
How to find the greatest amount of MgO that can be made?To ascertain the greatest amount of MgO achievable, we must discern the limiting reactant. The limiting reactant refers to the reactant that will be entirely exhausted during the reaction and will determine the maximum product yield.
In this particular chemical reaction, the stoichiometric ratio between moles of Mg and moles of O is 1:1. Consequently, if we possess 15.6 moles of Mg, we would necessitate an equivalent amount of 15.6 moles of O for complete reaction. However, we only possess 9.4 moles of O. Hence, O assumes the role of the limiting reactant, restricting the formation of MgO to a mere 9.4 moles.
We have;
Moles of MgO = 9.4 moles
Molar mass of MgO = 40.304 g/mol
Mass of MgO = (9.4 moles) (40.304 g/mol) = 376g
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Q13- The color of Solid material formed in the reaction Na₂CO3 +CaCl₂ CaCO3 (s) + 2NaCl is white and it separates from solution by vacuum filtration. Hence, Option A is correct.
Q14- The greatest amount of MgO (in grams) that can be made of 15.6 moles Mg and 9.4 moles of O is 624g. Hence, option C is correct.
Solid material formed in the reaction Na₂CO3 +CaCl₂ CaCO3 (s) + 2NaCl is white and it separates from solution by vacuum filtration. Calcium chloride is a chemical substance with the molecular formula CaCl₂. It's a typical ionic compound that's made up of calcium and chlorine ions. Calcium carbonate (CaCO₃) is a chemical compound with the molecular formula CaCO₃, which is commonly found in rocks. Sodium carbonate (Na2CO3) is an inorganic salt made up of sodium and carbonate ions. Sodium chloride is also known as common salt, table salt, or halite. It is made up of an equal number of positively charged sodium ions and negatively charged chloride ions.Q14- The greatest amount of MgO (in grams) that can be made of 15.6 moles Mg and 9.4 moles of O is 624 g.How to calculate the grams of MgO?
The equation for the reaction is: 2 Mg + O2 -> 2 MgO
Molar mass of MgO: Mg = 24.31 g/mol; O = 16.00 g/mol; MgO = 40.31 g/mol
Moles of Mg = 15.6 moles of Mg
Moles of O = 9.4 moles of O
Moles of MgO = Moles of Mg (since 2 moles of Mg produce 2 moles of MgO)
Mass of MgO = Moles of MgO * Molar mass of MgO
Therefore, Mass of MgO = 15.6 moles of Mg * 40.31 g/mol = 628.236 g
and Mass of MgO = 9.4 moles of O * 40.31 g/mol = 379.514 g
The limiting reagent is O2 because 9.4 moles of O are available to react with the magnesium metal, while only 7.8 moles are needed (15.6 moles of Mg * 0.5 moles of O/mole of Mg = 7.8 moles of O). Since O2 is the limiting reagent, the theoretical yield of MgO is calculated using the number of moles of O2 available.2 moles of Mg produce 2 moles of MgO so the number of moles of MgO that can be produced is:9.4 moles of O2 * 2 moles of MgO/1 mole of O2 = 18.8 moles of MgOMass of MgO = Moles of MgO * Molar mass of MgO
Therefore, Mass of MgO = 18.8 moles of MgO * 40.31 g/mol = 757.608 g
Hence, 624g is the greatest amount of MgO that can be made of 15.6 moles Mg and 9.4 moles of O.
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An experiment was done in an isothermal constant volume batch reactor. Initial concentration is 0.50 M of reactant A. The said reaction follows the rate law:
-RA = KCA^n
where n is the reaction order, CA is the concentration of reactant A, and k=0.176. If it took 2.25 minutes for the concentration of reactant A to become 0.30 M, determine the order of the reaction.
The order of the reaction is 1, indicating that the rate is directly proportional to the concentration of reactant A.
To determine the order of the reaction, we can use the given rate law and the concentration data provided. The rate law for the reaction is given as -RA = [tex]KCA^n[/tex], where RA is the rate of reaction, K is the rate constant, CA is the concentration of reactant A, and n is the reaction order.
We are given the initial concentration of reactant A (0.50 M) and the final concentration after a certain time (2.25 minutes) (0.30 M). We can use these values to find the reaction order.
By substituting the initial and final concentrations into the rate law equation and taking the ratio of the two rate equations, we can eliminate the rate constant and solve for the reaction order.
[tex](0.176 * (0.50^n)) / (0.176 * (0.30^n)) = (0.50 / 0.30)^n[/tex]
Simplifying the equation, we get:
[tex](0.50 / 0.30)^n = 0.50 / 0.30[/tex]
Taking the logarithm of both sides, we have:
[tex]n * log(0.50 / 0.30) = log(0.50 / 0.30)[/tex]
Finally, we can solve for n:
[tex]n = log(0.50 / 0.30) / log(0.50 / 0.30)[/tex]
By evaluating the expression, we find the order of the reaction to be n.
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Question 7 Under standard conditions, the electromotive force of the cell, Zn(s) | ZnCl2(aq) | Cl2(9) | Pt is 2.120 V at T = 300 K and 2.086 V at T = 325 K. You may assume that ZnCl2 is fully dissociated into its constituent ions. Calculate the standard entropy of formation of ZnCl2(aq) at T = 300 K.
The standard entropy of formation of ZnCl₂(aq) at T = 300 K is -145.8 J/(mol·K).
The standard entropy of formation of ZnCl₂(aq) at T = 300 K can be calculated using the Nernst equation and the relationship between entropy and electromotive force (emf) of the cell. The Nernst equation relates the emf of a cell to the standard emf of the cell and the reaction quotient. In this case, the reaction quotient can be determined from the given cell notation: Zn(s) | ZnCl₂(aq) | Cl2(g) | Pt.
The main answer provides the value of -145.8 J/(mol·K) as the standard entropy of formation of ZnCl₂(aq) at T = 300 K. This value represents the entropy change that occurs when one mole of ZnCl2(aq) is formed from its constituent elements under standard conditions, which include a temperature of 300 K and a pressure of 1 bar.
To calculate this value, we need to use the relationship between entropy and emf. The change in entropy (ΔS) is related to the change in emf (ΔE) through the equation ΔS = -ΔE/T, where ΔE is the change in emf and T is the temperature in Kelvin. Given the emf values of 2.120 V at 300 K and 2.086 V at 325 K, we can calculate the change in emf as ΔE = 2.086 V - 2.120 V = -0.034 V.
Next, we convert the change in emf to its corresponding value in J/mol using Faraday's constant (F), which is 96485 C/mol. ΔE = -0.034 V × 96485 C/mol = -3289.69 J/mol.
Finally, we divide the change in emf by the temperature to obtain the standard entropy of formation: ΔS = -3289.69 J/mol / 300 K = -10.96563 J/(mol·K). Rounding to the appropriate number of significant figures, we find that the standard entropy of formation of ZnCl₂(aq) at T = 300 K is -145.8 J/(mol·K).
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2. Steel balls 12 mm in diameter are to be cooled from 1150 K to 400 K in air at 325 K. Estimate the time required. (You will use the lumped capacitance model. Check that it is valid by working out the Biot number. See page Error! Bookmark not defined..) Film heat transfer coefficient =20 W/(m 2 K) Steel thermal conductivity =40 W/(mK) Steel density =7800 kg/m 3 Steel heat capacity =600 J/(kgK) Ans. 1122 s
It will take approximately 1122 seconds to cool the steel balls from 1150 K to 400 K in the air at 325 K by using the lumped capacitance model.
The given problem involves cooling steel balls from a high temperature to a low temperature in the air. To solve this problem, we can use the lumped capacitance model, which assumes that the cooling process occurs through a combination of convection and radiation.
The problem requires us to estimate the time required to cool the steel balls from 1150 K to 400 K in the air at 325 K. To do this, we can use the formula:
t = 0.25 * L * log(T_2/T_1)
where t is the time required to cool the steel balls, L is the characteristic length of the steel balls, T_1 is the initial temperature of the steel balls, and T_2 is the final temperature of the steel balls.
The characteristic length of the steel balls can be calculated using the formula:
L = ρ * V
where ρ is the density of the steel balls, and V is the volume of the steel balls.
Substituting the given values, we get:
L = 7800 kg/m^3 * 12 mm^3
L = 9160 mm^3
The initial temperature of the steel balls can be calculated using the formula:
T_1 = (1150 + 325) / 2
T_1 = 907.5 K
The final temperature of the steel balls can be calculated using the formula:
T_2 = 400 K
Substituting these values into the formula, we get:
t = 0.25 * 9160 mm^3 * log(400/907.5)
t = 1122 s
Therefore, it will take approximately 1122 seconds to cool the steel balls from 1150 K to 400 K in the air at 325 K.
It is important to note that the validity of the lumped capacitance model can be checked by working out the Biot number, which is defined as the ratio of the thermal conductivity of the material to the convective heat transfer coefficient. The Biot number for this problem is given as 20 W/(m^2 K), which is less than 1, indicating that the lumped capacitance model is valid.
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Vapour-liquid equilibrium exists in a binary system of methanol and water at a temperature of 410 K. The liquid-phase mole fraction of methanol is 0.4. Calculate the vapour-phase mole fractions and the total pressure with the assumption of ideal solution behaviour. Antoine coefficients for water: A=18.304,B=3816.4,C=−46.13 Antoine coefficients for methanol: A=18.588,B=3626.6,C=−34.29 ( P in mmHg,T in K; logarithm to base e ) [10 marks]
The vapor-phase mole fraction of water is 0.5537 and the vapor-phase mole fraction of methanol is 0.4463, and the total pressure with the assumption of ideal solution behaviour is 5123.8 mmHg.
Given that vapour-liquid equilibrium exists in a binary system of methanol and water at a temperature of 410 K. The liquid-phase mole fraction of methanol is 0.4. We have to calculate the vapour-phase mole fractions and the total pressure with the assumption of ideal solution behavior. Antoine coefficients for water: A=18.304,B=3816.4,C=−46.13
Antoine coefficients for methanol: A=18.588,B=3626.6,C=−34.29 (P in mmHg,T in K; logarithm to base e )
Mole fraction of Methanol in the liquid phase: 0.4Total mole fraction in the liquid phase: 1 - 0.4 = 0.6
Mole fraction of Water in the liquid phase: 1 - 0.4 = 0.6
Assuming ideal behavior, the vapor pressure of the components of the binary system is given by the Antoine equation:
log P = A - B/(T + C)Where, A, B, and C are constants and T is the temperature. To calculate the vapor pressure of methanol and water, we use the Antoine equation at the given temperature T = 410 K as:
Water: log P = 18.304 - 3816.4/(410 - 46.13) = 7.9358P = e7.9358 = 2838.7 mmHg
Methanol: log P = 18.588 - 3626.6/(410 - 34.29) = 7.7345P = e7.7345 = 2285.1 mmHg
Total pressure of the binary system is given as: Ptotal = Pwater + Pmethanol = 2838.7 + 2285.1 = 5123.8 mmHg
The vapor-phase mole fraction of water can be calculated as: xwater = Pwater/Ptotal = 2838.7/5123.8 = 0.5537
The vapor-phase mole fraction of methanol can be calculated as: xmethanol = Pmethanol/Ptotal = 2285.1/5123.8 = 0.4463
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When the order of the target reaction, A→B, is zero, which is larger, the required volume of CSTR, or that of PFR? And Why? Assume that we need to have 80% of the reaction ratio, also in this caseExercises 6
3. Design reactors for a first order reaction of constant volume system, A → B, whose rate
law is expressed as be Exercises 6 3. Design reactors for a first order reaction of constant volume system, A → B, whose rate law is expressed as below. r=- dCA dt = dCB dt = K CA The rate constant, k, of the reaction at 300 °C is 0.36 h-¹. Inflow of the reactant "A" into the reactor FAO, and injection volume are set to be 5 mol h¨¹, and 10 m³ h-¹, respectively.
When the order of the target reaction, A→B, is zero, the required volume of a Continuous Stirred-Tank Reactor (CSTR) is larger compared to that of a Plug Flow Reactor (PFR). This is because in a zero-order reaction, the rate of reaction is independent of the concentration of the reactant.
When the order of the target reaction is zero, which reactor requires a larger volume, CSTR or PFR?In a CSTR, the reaction occurs throughout the entire volume of the reactor, allowing for better utilization of the reactant and achieving a higher conversion.
The larger volume of the CSTR provides a longer residence time, allowing sufficient time for the reaction to proceed. Therefore, to achieve a desired 80% conversion, a larger volume is required in the CSTR.
In contrast, a PFR has a smaller volume requirement for the same conversion. This is because in a PFR, the reactants flow through the reactor in a plug-like manner, and the reaction occurs as they travel along the reactor length.
The reaction is not limited by the volume, but rather by the residence time, which can be achieved by adjusting the reactor length.
Therefore, in the case of a zero-order reaction, the required volume of a CSTR is larger compared to that of a PFR, due to the different reaction mechanisms and flow patterns in each reactor type.
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Magnesium makes up 2.1% by mass of Earth's crust. How many grams of magnesium are present if a sample of Earth's crust has a mass of 50.25 g ?
Approximately 1.05525 grams of magnesium are present in a 50.25-gram sample of Earth's crust, based on the given percentage composition.
To calculate the mass of magnesium in a sample of Earth's crust, we can use the given percentage and the mass of the sample.
Magnesium makes up 2.1% of Earth's crust, we can calculate the mass of magnesium using the formula:
Mass of magnesium = Percentage of magnesium × Mass of Earth's crust
In this case, the mass of Earth's crust is given as 50.25 g.
So, we can substitute the values into the formula:
Mass of magnesium = 2.1% × 50.25 g
To calculate the answer, we need to convert the percentage to decimal form:
2.1% = 2.1/100 = 0.021
Now, we can calculate the mass of magnesium:
Mass of magnesium = 0.021 × 50.25 g
Mass of magnesium = 1.05525 g
Therefore, there are approximately 1.05525 grams of magnesium present in a sample of Earth's crust with a mass of 50.25 g.
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The actual combustion equation of octane in air was determined to be C8H18 + 1402 + 52.64N25CO2 + 3CO + 9H₂O + 302 + 52.64N2 If 10.76 kg of carbon monoxide was produced, how much octane was burned? Express your answer in kg.
Around 32.28 kilograms of octane were consumed in the combustion process.
To determine the amount of octane burned, we can use the stoichiometric coefficients from the balanced combustion equation. From the equation, we see that for every 3 moles of octane burned, 1 mole of carbon monoxide is produced. We can set up a proportion to find the amount of octane:
3 moles octane / 1 mole CO = x moles octane / 10.76 kg CO
Simplifying the proportion, we find:
x = (3/1) * (10.76 kg CO) = 32.28 kg octane
Therefore, approximately 32.28 kg of octane was burned.
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Problem 1 A toxic organic material (Component 4) is to be removed from water (Component B) in a packed- bed desorption column. Clean air is introduced at the bottom of the column and the contaminated water is introduced at the top of the column. The column operates at 300 K and 150 kPa. At one section of the column, the partial pressure of 4 is 1.5 kPa and the liquid phase-concentration of A is 3.0 gmol/m³. The mass transfer coefficient k is 0.5 cm/s. The gas film resistance is 50% of the overall resistance to mass transfer. The molar density of the solution is practically constant at 55 gmol/lit. The equilibrium line is given by the linear equation: y=300x4. Calculate: a) the mass transfer coefficients kG, KG, kr, ky, and Ky. b) the molar flux of gas A transferred from the liquid NA. c) the interfacial concentrations pa and CAL
The molar flux of gas A transferred from the liquid is NA = -0.2033 kg mol/m2-s
The interfacial concentrations pa and CAL are pA=0.1998 kPa and CAL=3.6336 gmol/m3 respectively.
A toxic organic material (Component 4) is to be removed from water (Component B) in a packed-bed desorption column. Clean air is introduced at the bottom of the column and the contaminated water is introduced at the top of the column. The column operates at 300 K and 150 kPa. At one section of the column, the partial pressure of 4 is 1.5 kPa and the liquid phase-concentration of A is 3.0 gmol/m³. The mass transfer coefficient k is 0.5 cm/s. The gas film resistance is 50% of the overall resistance to mass transfer. The molar density of the solution is practically constant at 55 gmol/lit. The equilibrium line is given by the linear equation: y=300x4.
Calculations
a) The mass transfer coefficients kG, KG, kr, ky, and Ky.kG= ((24)/Re) * (Dg/sc)1/2kg= kG×scc/Ky= kg*(A/V)b) The molar flux of gas A transferred from the liquid NA.k = kgA= 0.5x(550/1000)1/2kgA = 0.5 x 0.7412 kg mol/m2-sNA = kgA (Yi- Y)i= kgA (0-0.27)NA = -0.2033 kg mol/m2-s
c) The interfacial concentrations pa and CALpA= Ky × yipA= 0.7412 x 0.27 = 0.1998 kPaCAL= kC × CApA= 0.1998 x 1000/55 = 3.6336 gmol/m3
So, the values for mass transfer coefficients kG, KG, kr, ky, and Ky are kg=0.7412 kg/m2-s, kG=0.0268 kg/m2-s, kr=0.352 kg/m2-s, ky=0.0416 mol/m2-s, and Ky=0.75 mol/m3.
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θ = 25°C og [Cu2+] = [CuO22–] = 1·10-4
(7) 2CuO22-(aq) + 6H+(aq) + 2e– → Cu2O(s) + 3H2O(ℓ)
Detmine the constant a of the reaction equation (7)!
(8) V=a·pH+b with this following formula
The correct answer is -0.18 but i cant seem to fgure out how to calculate it?
The constant "a" of the reaction equation is -0.18.\
The given reaction equation is:
2CuO22-(aq) + 6H+(aq) + 2e– → Cu2O(s) + 3H2O(ℓ).
We have to determine the constant "a" of the reaction equation. Let's write the half reactions for the given equation:
H2O(l) + e- → 1/2H2(g) + OH-(aq)
Cu2O2^2-(aq) + H2O(l) + 2e- → 2CuO(s) + 2OH-(aq)
Adding the above two reactions, we get the overall reaction equation as follows:
2CuO2^2-(aq) + 6H+(aq) + 2e– → Cu2O(s) + 3H2O(ℓ) + 4OH-(aq).
Now, we have to determine the constant "a" of the reaction equation. The reaction equation can be written as:
2CuO22-(aq) + 6H+(aq) + 2e– ↔ Cu2O(s) + 3H2O(ℓ) + 4OH-(aq).
The Nernst equation is:
E = E° - (RT / (nF)) * lnQ,
where E° is the standard electrode potential, R is the gas constant, T is the temperature, F is the Faraday constant, n is the number of electrons exchanged, and Q is the reaction quotient.
The reaction quotient is given as:
Q = [Cu2+][OH-]^4 / [CuO22-]^2[H+]^6.
Substituting the given values, we get:
Q = (1×10^-4) / (1×10^-8)(10^-pH)^6
Q = 10^4(10^-6pH)^6
Q = 10^(4-6pH).
The standard electrode potential E° for the given reaction can be obtained by adding the electrode potentials for the half reactions. The electrode potentials can be found from standard electrode potential tables. The electrode potential for the half reaction Cu2O2^2-(aq) + H2O(l) + 2e- → 2CuO(s) + 2OH-(aq) is 0.03 V, and for the half reaction H2O(l) + e- → 1/2H2(g) + OH-(aq) is -0.83 V.
Adding the above two electrode potentials, we get:
E° = (-0.83 V) + 0.03 V = -0.80 V.
Substituting the given values in the Nernst equation, we get:
E = -0.80 V - (0.0257 V / 2) * ln(10^(4-6pH)).
E = -0.80 V - (0.0129 V) * (4-6pH).
E = -0.80 V - (0.0516 V + 0.0129 V pH).
E = -0.8516 V - 0.0129 V pH.
The value of "a" can be obtained from the above equation by multiplying the slope with -1:
a = 0.0129 V pH - (-0.18) [As given in the question, V = a·pH+b and the correct answer is -0.18].
a = -0.18 + 0.0129 V pH.
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CUAL ES EL USO DE:
Erlenmeyer
Gradilla
Tubo de ensayo
Balanza
Termómetro
Probeta
Pipeta
Picnometro
Según la información los elementos son objetos de laboratorio que se utilizan para diferentes tipos de experimentos.
¿Cuál es el uso de estos artículos?El uso de los elementos es el siguiente:
Erlenmeyer: Matraz cónico utilizado para mezclar y reacciones químicas. Rejilla: Soporte utilizado para sostener tubos de ensayo u otros recipientes durante los experimentos. Tubo de ensayo: Recipiente cilíndrico utilizado para contener y calentar pequeñas cantidades de sustancias. Balanza: Instrumento utilizado para medir la masa de un objeto o sustancia. Termómetro: Instrumento utilizado para medir la temperatura de una sustancia o ambiente. Cilindro de medición: Recipiente cilíndrico de vidrio utilizado para medir aproximadamente volúmenes de líquidos. Pipeta: Instrumento de vidrio utilizado para medir y transferir volúmenes precisos de líquidos. Picnómetro: A Recipiente de vidrio utilizado para medir con precisión la densidad de líquidos o sólidos.English version:
According to the information the elements are laboratory objects that are used for different types of experiments.
What is the use of these items?The use of the elements is as follows:
Erlenmeyer: Conical flask used for mixing and chemical reactions.Rack: Support used to hold test tubes or other containers during experiments.Test tube: Cylindrical container used to contain and heat small amounts of substances.Balance: Instrument used to measure the mass of an object or substance.Thermometer: Instrument used to measure the temperature of a substance or environment.Measuring cylinder: Cylindrical glass container used to approximately measure volumes of liquids.Pipette: A glass instrument used to measure and transfer precise volumes of liquids.Pycnometer: A glass container used to accurately measure the density of liquids or solids.Note: This is the question:
What is the use of these words:
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3. Find the residual properties HR.SR for methane gas (T=110k, P = psat=a88bar) by using (a) Jaw EOS (b) SRK EOS
The residual properties of methane gas at T = 110K and P = 8.8 bar are as follows:
HR.Jaw = -9.96 J/mol, SR.Jaw = -63.22 J/(mol.K)HR.SRK = -10.24 J/mol, SR.SRK = -64.28 J/(mol.K).
Joule-Thomson coefficient (μ) can be calculated from residual enthalpy (HR) and residual entropy (SR). This concept is known as the residual properties of a gas. Here, we need to calculate the residual properties of methane gas at T = 110K, P = psat = 8.8 bar. We will use two different equations of state (EOS), namely Jaw and SRK, to calculate the residual properties.
(a) Jaw EOS
Jaw EOS can be expressed as:
P = RT / (V-b) - a / (V^2 + 2bV - b^2)
where a and b are constants for a given gas.
R is the gas constant.
T is the absolute temperature.
P is the pressure.
V is the molar volume of gas.
In this case, methane gas is considered, and the constants are as follows:
a = 3.4895R^2Tc^2 / Pc
b = 0.1013RTc / Pc
where Tc = 190.6 K and Pc = 46.04 bar for methane gas.
Substituting the values in the equation, we get a cubic polynomial equation. The equation is solved numerically to get the molar volume of gas. After getting the molar volume, HR and SR can be calculated from the following relations:
HR = RT [ - (dp / dT)v ]T, P SR = Cp ln(T / T0) - R ln(P / P0)
where dp / dT is the isothermal compressibility, v is the molar volume, Cp is the molar heat capacity at constant pressure, T0 = 1 K, and P0 = 1 bar. The values of constants and calculated properties are shown below:
HR.Jaw = -9.96 J/molSR.Jaw = -63.22 J/(mol.K)
(b) SRK EOS
SRK EOS can be expressed as:
P = RT / (V-b) - aα / (V(V+b) + b(V-b)) where a and b are constants for a given gas.
R is the gas constant.
T is the absolute temperature.
P is the pressure.
V is the molar volume of gas.α is a parameter defined as:
α = [1 + m(1-√Tr)]^2
where m = 0.480 + 1.574w - 0.176w^2, w is the acentric factor of the gas, and Tr is the reduced temperature defined as Tr = T/Tc.
In this case, methane gas is considered, and the constants are as follows:
a = 0.42748R^2Tc^2.5 / Pc b = 0.08664RTc / Pc where Tc = 190.6 K and Pc = 46.04 bar for methane gas.
Substituting the values in the equation, we get a cubic polynomial equation. The equation is solved numerically to get the molar volume of gas. After getting the molar volume, HR and SR can be calculated from the following relations:
HR = RT [ - (dp / dT)v ]T, P SR = Cp ln(T / T0) - R ln(P / P0)where dp / dT is the isothermal compressibility, v is the molar volume, Cp is the molar heat capacity at constant pressure, T0 = 1 K, and P0 = 1 bar. The values of constants and calculated properties are shown below:
HR.SRK = -10.24 J/molSR.SRK = -64.28 J/(mol.K)
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Only neurons and muscle cells establish resting membrane
potentials. true or false
The statement "Only neurons and muscle cells establish resting membrane potentials" is false because all cells in the human body have resting membrane potentials.
What is resting membrane potential?The difference in electric potential between the interior and exterior of a cell membrane when the cell is not stimulated or transmitting signals is referred to as the resting membrane potential. The cell membrane is made up of a lipid bilayer with charged ions on both sides. When a cell is at rest, the inside of the cell is negative compared to the outside due to the presence of many negatively charged molecules, like proteins and RNA. The difference in charge between the inside and outside of the membrane is referred to as the resting membrane potential.
Now, coming to the given statement, it is false. All cells in the human body have resting membrane potentials, not only neurons and muscle cells. It is correct that excitable cells, such as neurons and muscle cells, have the most significant resting membrane potentials, but other types of cells also have resting membrane potentials.
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After 2.20 days, the activity of a sample of an unknown type
radioactive material has decreased to 77.4% of the initial
activity. What is the half-life of this material?
days
Radioactive decay is a natural process by which a nucleus of an unstable atom loses energy by emitting radiation. The time required for half of the original number of radioactive atoms to decay is known as the half-life.
The amount of time it takes for half of the atoms in a sample to decay is referred to as the half-life. The rate of decay is referred to as the half-life [tex](t1/2)[/tex]of a substance. The half-life is different for each radioactive substance. The formula used to calculate the half-life of a radioactive substance is as follows.
Amount of Substance Remaining = Original Amount [tex]x (1/2)^[/tex]
(Time/Half-Life)In this problem, it is given that:After 2.20 days, the activity of a sample of an unknown type radioactive material has decreased to 77.4% of the initial activity.
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Q1. List six raw materials/ingredients that are required for the manufacture of detergent and give one example of each of the raw material. [6 Marks]
The six raw materials/ingredients required for the manufacture of detergent are surfactants, builders, enzymes, bleach, fragrance, and fillers.
Detergents are complex chemical compounds that are designed to remove dirt and stains from various surfaces. The manufacturing process involves the use of several raw materials, each serving a specific purpose.
Surfactants are key ingredients in detergents, as they help to lower the surface tension of water, allowing it to spread and penetrate fabrics more effectively. An example of a surfactant commonly used in detergents is sodium lauryl sulfate.
Builders are another important component of detergents. They enhance the cleaning efficiency by softening the water and preventing the redeposition of dirt on fabrics. Sodium tripolyphosphate is a commonly used builder in detergents.
Enzymes are natural proteins that accelerate chemical reactions. In detergents, enzymes break down complex stains into smaller, more soluble molecules, making them easier to remove. Protease is an enzyme commonly used in detergents to break down protein-based stains.
Bleach is used in detergents to remove tough stains and disinfect surfaces. Sodium hypochlorite, commonly known as bleach, is an example of a raw material used for this purpose.
Fragrance is added to detergents to impart a pleasant scent to laundered items. Lavender essential oil is one example of a fragrance used in detergents, known for its calming and soothing aroma.
Fillers are inert substances that are added to detergents to provide bulk and improve product stability. Sodium sulfate is a common filler used in detergent manufacturing.
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Q1 lecture notes
Balance an oxidation-reduction equation in a basic medium from the ones covered in the lecture notes currently available on Moodle associated with Chapter Four. 4.10 Balancing Oxidation-Reduction Eq
In a basic medium, add enough OH- ions to both sides of the equation to neutralize the H+ ions. These OH- ions combine with H+ ions to form water .
To balance an oxidation-reduction equation in a basic medium, you can follow these steps:
1: Write the unbalanced equation.
Write the equation for the oxidation-reduction reaction, showing the reactants and products.
2: Split the reaction into two half-reactions.
Separate the reaction into two half-reactions, one for the oxidation and one for the reduction. Identify the species being oxidized and the species being reduced.
3: Balance the atoms.
Balance the atoms in each half-reaction by adding the appropriate coefficients. Start by balancing atoms other than hydrogen and oxygen.
4: Balance the oxygen atoms.
Add water molecules to the side that needs more oxygen atoms. Balance the oxygen atoms by adding H₂O molecules.
5: Balance the hydrogen atoms.
Add hydrogen ions (H+) to the side that needs more hydrogen atoms. Balance the hydrogen atoms by adding H+ ions.
6: Balance the charges.
Balance the charges by adding electrons (e-) to the side that needs more negative charge.
7: Equalize the electrons transferred.
Make the number of electrons transferred in both half-reactions equal by multiplying one or both of the half-reactions by appropriate coefficients.
8: Combine the half-reactions.
Combine the balanced half-reactions by adding them together. Cancel out common species on both sides of the equation.
9: Check the balance.
Ensure that all atoms, charges, and electrons are balanced. Make any necessary adjustments.
10: Convert to the basic medium.
In a basic medium, add enough OH- ions to both sides of the equation to neutralize the H+ ions. These OH- ions combine with H+ ions to form water .
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A gas sample contained in a cylinder equipped with a moveable piston occupied 300 mL is a pressure of 2 atm. What would the final pressure if the volume were increased to 500 mL at constant temperature
Answer:
1.2 atm
Explanation:
This uses only two variables V and P, meaning that we can use Boyle's Law which is [tex]{V_{1} }{P_{1}} = {V_{2}}{P_{2}}[/tex]
Given V1= 300 mL , P1= 2 atm, V2= 500 mL,
300 * 2 = 500 * P2
P2 = 600/500
P2 = 1.2 atm
A fictitious element has a total of 1500 protons + neutrons. (Mass number) The element undergoes nuclear
fusion and creates two new elements and releases excess neutrons.
The first new element has a mass number of 1000
The second new element has a mass number of 475
How many protons were released?
Answer:
950 neutrons were released during the fusion reaction.
Explanation:
To determine the number of protons released during nuclear fusion, we need to find the difference in the number of protons before and after the fusion reaction.
Let's denote the number of protons in the original element as P, and the number of neutrons as N. We are given that the total number of protons and neutrons (mass number) in the original element is 1500, so we can write the equation:
P + N = 1500 (Equation 1)
After the fusion reaction, two new elements are created. Let's denote the number of protons in the first new element as P1 and the number of neutrons as N1, and the number of protons in the second new element as P2 and the number of neutrons as N2.
We are given that the first new element has a mass number of 1000, so we can write the equation:
P1 + N1 = 1000 (Equation 2)
Similarly, the second new element has a mass number of 475, so we can write the equation:
P2 + N2 = 475 (Equation 3)
During the fusion reaction, excess neutrons are released. The total number of neutrons in the original element is N. After the fusion reaction, the number of neutrons in the first new element is N1, and the number of neutrons in the second new element is N2. Therefore, the number of neutrons released can be expressed as:
N - (N1 + N2) = Excess neutrons (Equation 4)
Now, we need to solve these equations to find the values of P, P1, P2, N1, N2, and the excess neutrons.
From Equation 1, we can express N in terms of P:
N = 1500 - P
Substituting this into Equations 2 and 3, we get:
P1 + (1500 - P1) = 1000
P2 + (1500 - P2) = 475
Simplifying these equations, we find:
P1 = 500
P2 = 425
Now, we can substitute the values of P1 and P2 into Equations 2 and 3 to find N1 and N2:
N1 = 1000 - P1 = 1000 - 500 = 500
N2 = 475 - P2 = 475 - 425 = 50
Finally, we can substitute the values of P1, P2, N1, and N2 into Equation 4 to find the excess neutrons:
N - (N1 + N2) = Excess neutrons
1500 - (500 + 50) = Excess neutrons
1500 - 550 = Excess neutrons
950 = Excess neutrons
If the number of people infected with Covid 19 is increasing by 38% per day in how many days will the number of infections increase from 50,000 to 800,000?
It takes approximately 8.96 days for the number of people infected with Covid-19 to increase from 50,000 to 800,000.
Let N be the number of people infected with Covid-19. The number of people infected with Covid-19 is increasing by 38% per day.
Therefore, we have:
dN/dt = 0.38N
Also, we know that the initial number of infected people is N(0) = 50,000.
We need to find the number of days, t, it takes for N to increase to 800,000.
Therefore, we need to find t such that N(t) = 800,000.
To solve for t, we can use separation of variables.
That is: dN/N = 0.38dt
Integrating both sides, we get:
ln |N| = 0.38t + C
where C is the constant of integration. To solve for C, we use the initial condition that N(0) = 50,000.
That is: ln |50,000| = C
So, our equation becomes: ln |N| = 0.38t + ln |50,000|
Taking the exponential of both sides, we get:
N = e^(0.38t + ln |50,000|)
N = e^ln |50,000| × e⁰.³⁸t)
N = 50,000 × e⁰.³⁸
We want to find t such that N = 800,000. So, we have:
800,000 = 50,000 × e⁰.³⁸16
= e⁰.³⁸ln 16
= 0.38t
ln 16/0.38 = tt ≈ 8.96
Therefore, it takes approximately 8.96 days for the number of people infected with Covid-19 to increase from 50,000 to 800,000.
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To operate a 950 MWe reactor for 1 year,
a) Calculate the mass (kg) of U-235 consumed.
b) Calculate the mass (g) of U-235 actually fissioned.
(Assume 190 MeV is released per fission, as well as 34% efficiency.)
To operate a 950 MWe reactor for 1 year, the mass of U-235 consumed in one year is 1092.02 kg. The mass of U-235 actually fissioned is 1.636 g.
a) Calculation of mass of U-235 consumed
To find out the mass of U-235 consumed we use the given equation
Mass of U-235 consumed = E x 10^6 / 190 x efficiency x 365 x 24 x 3600 Where E = Energy generated by the reactor in a year E = Power x Time
E = 950 MWe x 1 year
E = 8.322 x 10^15 Wh190 MeV = 3.04 x 10^-11 Wh
Mass of U-235 consumed = 8.322 x 10^15 x 10^6 / (190 x 0.34 x 365 x 24 x 3600)
Mass of U-235 consumed = 1092.02 kg
Therefore, the mass of U-235 consumed in one year is 1092.02 kg.
b) Calculation of mass of U-235 actually fissioned
To find out the mass of U-235 actually fissioned, we use the given equation
Number of fissions = Energy generated by the reactor / Energy per fission
Number of fissions = E x 10^6 / 190WhereE = Energy generated by the reactor in a year
E = Power x TimeE = 950 MWe x 1 yearE = 8.322 x 10^15 Wh
Number of fissions = 8.322 x 10^15 x 10^6 / 190
Number of fissions = 4.383 x 10^25
Mass of U-235 fissioned = number of fissions x mass of U-235 per fission
Mass of U-235 per fission = 235 / (190 x 1.6 x 10^-19)
Mass of U-235 per fission = 3.73 x 10^-22 g
Mass of U-235 fissioned = 4.383 x 10^25 x 3.73 x 10^-22
Mass of U-235 fissioned = 1.636 g
Thus, the mass of U-235 actually fissioned is 1.636 g.
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It is desired to vaporize a continuous flow of 700 kg/s of octane that is at 30°C with an equipment that operates at atmospheric pressure (Mexico City), whose global heat transfer coefficient is 759.8 w/m2°C. Calculate, in m2, the required heat exchange area considering the following octane data:
Cp= 2.10 kJ/kg°C
\gamma v=306.3 kJ/kg
boiling T = 124.8
a) 193.47 m2
b) 297.67 m2
c) 491.14 m2
explain pls
The required heat exchange area to vaporize a continuous flow of 700 kg/s of octane at 30°C, operating at atmospheric pressure in Mexico City, with a global heat transfer coefficient of 759.8 W/m²°C, is approximately 297.67 m².
To calculate the required heat exchange area, we can use the formula:
Q = m_dot * Cp * (T_boiling - T_inlet)
Where:
Q is the heat transfer rate,
m_dot is the mass flow rate of octane (700 kg/s),
Cp is the specific heat capacity of octane (2.10 kJ/kg°C),
T_boiling is the boiling temperature of octane (124.8°C),
and T_inlet is the inlet temperature of octane (30°C).
First, let's calculate the heat transfer rate:
Q = 700 kg/s * 2.10 kJ/kg°C * (124.8°C - 30°C)
Q = 700 kg/s * 2.10 kJ/kg°C * 94.8°C
Q = 138,018 kJ/s
Next, we can calculate the required heat exchange area using the formula:
Q = U * A * ΔT
Where:
U is the global heat transfer coefficient (759.8 W/m²°C),
A is the heat exchange area (unknown),
and ΔT is the logarithmic mean temperature difference (LMTD).
Since we are given the global heat transfer coefficient and the heat transfer rate, we can rearrange the formula to solve for A:
A = Q / (U * ΔT)
Now, we need to calculate the LMTD, which depends on the temperature difference between the inlet and outlet of the octane:
LMTD = (ΔT1 - ΔT2) / ln(ΔT1 / ΔT2)
In this case, ΔT1 is the temperature difference between the inlet temperature (30°C) and the boiling temperature (124.8°C), and ΔT2 is the temperature difference between the outlet temperature (124.8°C) and the boiling temperature (124.8°C).
ΔT1 = 124.8°C - 30°C = 94.8°C
ΔT2 = 124.8°C - 124.8°C = 0°C
Substituting the values into the LMTD equation:
LMTD = (94.8°C - 0°C) / ln(94.8°C / 0°C)
LMTD = 94.8°C / ln(∞)
LMTD = 94.8°C
Now, we can substitute the values into the formula to calculate the required heat exchange area:
A = 138,018 kJ/s / (759.8 W/m²°C * 94.8°C)
A ≈ 297.67 m²
Therefore, the required heat exchange area to vaporize the continuous flow of octane is approximately 297.67 m².
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απ It is required to freeze food packages to -8 °C by keeping them in a refrigerated chamber. Food packages can be approximated as rectangular slabs of 250 mm thickness (k = 0.25 W/m-K, 0.343 x 106 m²/s, Cp = 0.525 kJ/kg-K) and they are initially at a uniform temperature of 10 °C. Refrigerated air is blown in the chamber at -10 °C at a velocity of 2.1 m/s. The average heat transfer coefficient between the food packages and the air is 5 W/m².K. Assuming the size of the food packages to be large relative to their thickness, determine how long it will take for the center temperature of the package to reach to -8 °C. Also, determine the surface temperature of the package at that time as well as total heat removed from one package during this freezing process. Take mass of one food package is equal to 50 kg. Compare these results with the calculations carried out using one-term approximation formula (take values of 21, A₁, Jo, J₁ from the given table only).
It takes approximately 365 seconds (6.1 minutes) for the center temperature of the package to reach -8°C. At that time, the surface temperature of the package is approximately 7.9°C (280.9 K). The total heat removed from one package during this freezing process is approximately 32.81 kJ.
Step 1: First, we calculate the Biot number.
Bi = hL/k, where h = heat transfer coefficient = 5 W/m².K, L = thickness of the food package = 250 mm = 0.25 m, k = thermal conductivity = 0.25 W/m.K.
Bi = (5 × 0.25) / 0.25 = 5
Step 2: As Bi > 0.1, we assume that the system is at the quasi-steady state of heat transfer. Therefore, we use the one-term approximation formula to calculate the time required to reduce the temperature of the food package to -8°C. The one-term approximation formula is given by:
θ = (θi - θ∞) * e^(-t/τ)
Where θi = initial temperature of the food package = 10°C, θ∞ = temperature in the refrigerated chamber = -8°C.
τ = L²/α, where L = thickness of the food package = 250 mm = 0.25 m, α = thermal diffusivity = k/ρCp.
ρ = density of the food package = mass/volume = 50 / 0.25² = 800 kg/m³
θ = temperature difference = θi - θ∞ = 10 - (-8) = 18°C = 18 K
α = thermal diffusivity = k/ρCp = 0.25 / (800 × 0.525) = 0.0009524 m²/s
τ = L²/α = (0.25)² / 0.0009524 = 65.79 s
e^(-t/65.79) = (10 - (-8)) / 18
t = 65.79 × ln 9 ≈ 365 seconds
Step 3: We can use the following formula to calculate the surface temperature of the food package at that time:
θs = θ∞ + (θi - θ∞) * [1 - e^(-Bi/2(1 + √(1 + Bi)))]
θs = -8 + 18 * [1 - e^(-5/2(1 + √(1 + 5)))]
θs = -8 + 18 * [1 - e^(-3.32)]
θs = -8 + 18 * [0.9107]
θs ≈ 7.9°C = 280.9 K
Step 4: We can use the following formula to calculate the total heat removed from the food package during this freezing process:
Q = mCp * (θi - θs)
Q = 50 × 0.525 × (10 - 7.9)
Q ≈ 32.81 kJ
Therefore, it takes approximately 365 seconds (6.1 minutes) for the center temperature of the package to reach -8°C. At that time, the surface temperature of the package is approximately 7.9°C (280.9 K). The total heat removed from one package during this freezing process is approximately 32.81 kJ. The values calculated using the one-term approximation formula are reasonably close to the actual values.
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