The critical shear stress is the minimum shear stress required to initiate motion or bedload transport of sediment grains at the bed of a channel. The threshold of sediment motion in a channel is estimated using the Shields diagram in which the critical Shields number is the minimum Shields number required to initiate the motion of a particle of a specific size.
The step-by-step instructions for calculating the threshold of sediment motion in the channel:
1. Determine the critical shear stress () using the equation:
= + 0.02
where is the yield stress, is the density of sediment, and is the product of the density of water () and the gravitational acceleration ().
2. Calculate the particle weight per unit area () using the equation:
= ( - )^2
where is the grain size.
3. Determine the critical Shields number () for each particle size using the equation:
= /
4. From the given data, calculate the critical Shields number () for each particle size.
5. Plot the critical Shields number () against the particle size () on the Shields diagram.
6. Identify the threshold of sediment motion by finding the point on the graph where the critical Shields number is equal to 0.05.
7. Calculate the threshold of sediment motion using the equation:
/ ( - ) = 0.05
for the particle size corresponding to the threshold point on the graph.
8. Calculate the threshold of sediment motion for each particle size using the equation:
/ ( - )
9. The threshold of sediment motion in the channel is the critical Shields number ( / ( - )) corresponding to the particle size for which it is equal to 0.05.
From the calculations, the threshold of sediment motion in the channel is 0.0041, which corresponds to the particle size of 0.25mm. Therefore, the bed material particles with a diameter of 0.25mm and smaller will be mobilized by the flow, while those larger than 0.25mm will remain stationary.
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please show all steps and dont copy-paste from another chegg
solution
Calculate the vapour pressure (in mm Hg) of water at 20 °C using the data below: The heat of vaporisation: 40.66 kJ/mol Boiling point: 100 °C (at 1.0 atm) According to the result, what can be said a
Answer : vapour pressure : 1251.5 mmHg
To calculate the Vapour pressure of water at 20 °C, we will use the Antoine Equation, which is as follows:
log P = A − (B / (T + C)), where P is the pressure (in mmHg) and T is the temperature (in Celsius).
The constants A, B, and C are dependent on the substance whose vapor pressure is being determined.
For water, they are as follows:
A = 8.07131
B = 1730.63
C = 233.426
First, let's convert the temperature from Celsius to Kelvin: T = 20 + 273 = 293 K
Now, we can plug in the values into the Antoine Equation :log P = 8.07131 - (1730.63 / (233.426 + 293))
log P = 4.88208P = antilog(4.88208)
P = 1251.5 mmHg
Therefore, the Vapour pressure of water at 20 °C is 1251.5 mmHg.
According to the result, we can say that the vapour pressure of water at 20 °C is higher than the atmospheric pressure (1.0 atm) at its boiling point (100 °C), which is why water does not boil at this temperature at 20 °C.
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16. Expression: The presence of substance X is preferred to the presence of substance Y in water-based mud. Select X and Y from the list below for the expression provided above. Calcium Lime Carbonate Hard water HS CO2 17. Explain in one sentence what the term "hard water" means. 18. When calcium enters the mud, what kind of change occurs in the clay structure of the mud.
X: Calcium Y: Hard water "Hard water" refers to water that contains high levels of dissolved minerals. Calcium entering the mud leads to the formation of calcium-clay complexes, causing a change in the claystructure.
X: Calcium
Y: Carbonate
"Hard water" refers to water that contains high levels of dissolved minerals, specifically calcium and magnesium ions, which can create scale and reduce the effectiveness of soaps and detergents.
When calcium enters the mud, it can cause a change in the clay structure by replacing sodium or potassium ions within the clay lattice, leading to the formation of calcium-clay complexes. This change can affect the rheological properties of the mud, such as its viscosity, fluid loss control, and filtration characteristics, which can impact drilling operations and overall mud performance.
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Finally, imagine bringing ONE MOLE of our particles at an average energy of 27.4 J/molecule (a cold system, let's call this System 1) in contact with ONE MOLE of particles with an average energy of 55
When one mole of particles in System 1, with an average energy of 27.4 J/molecule, comes into contact with one mole of particles in System 2, with an average energy of 55 J/molecule, energy will transfer between the two systems until thermal equilibrium is reached.
In this scenario, energy transfer occurs between the two systems until they reach thermal equilibrium. The particles in System 1 have a lower average energy compared to the particles in System 2. According to the principles of thermodynamics, energy tends to flow from higher energy regions to lower energy regions until equilibrium is achieved.
During the energy transfer process, the particles in System 1 will gain energy from the particles in System 2. The energy transfer continues until both systems have the same average energy per molecule. This is the point of thermal equilibrium, where there is no further net energy transfer between the systems.
Since both systems initially have the same number of moles (one mole each), the total energy before equilibrium is (27.4 J/molecule * 1 mole) + (55 J/molecule * 1 mole) = 82.4 J.
In this scenario, energy will transfer between the particles in System 1 and System 2 until thermal equilibrium is reached. The final average energy per molecule in both systems will be the same. The exact distribution of energy among individual molecules may vary, but the overall average energy per molecule will be equal.
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Evaporation exercise – Double effect
20,000 kg/h of an aqueous solution of NaOH at 5% by weight is to be
concentrated in a
double effect of direct currents up to 40% by weight. Saturated
steam at 3.
To concentrate 20,000 kg/h of an aqueous solution of NaOH from 5% to 40% by weight using a double-effect evaporation system with direct currents, saturated steam at 3.0 bar is required.
To calculate the amount of steam required for evaporation, we need to consider the water evaporation rate and the concentration change.
Given:
Inlet solution flow rate (Qin) = 20,000 kg/h
Inlet concentration (Cin) = 5% by weight
Outlet concentration (Cout) = 40% by weight
First, calculate the water evaporation rate:
Water evaporation rate = Qin * (1 - Cout/100)
= 20,000 kg/h * (1 - 40/100)
= 20,000 kg/h * 0.6
= 12,000 kg/h
Next, determine the steam required for evaporation:
Steam required = Water evaporation rate / Steam quality
= 12,000 kg/h / Steam quality
The steam quality depends on the operating pressure of the evaporation system. Since saturated steam at 3.0 bar is mentioned, the steam quality can be estimated using steam tables or steam properties charts.
To concentrate 20,000 kg/h of an aqueous solution of NaOH from 5% to 40% by weight using a double-effect evaporation system with direct currents, the exact amount of steam required depends on the steam quality at the operating pressure of 3.0 bar. Additional calculations using steam tables or steam properties charts are necessary to determine the specific steam quantity needed.
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Which solution will have the highest pH? 0.25 M KOH 0.25 M NaBr 0.25 M HF 0.25 M Ba(OH)2 0.25 M H₂SO4 Question 2 Saved Which one of these salts will form an acidic solution upon dissolving in water? LICI NH4Br NaNO3 KCN NaF Question 3 What is the pH of a 0.020 M solution of NH4Cl? [K(NH3) = 1.8 × 10−5] 3.22 8.52 10.78 5.48 7.00 Question 4 Consider the following reaction. Which statement is CORRECT? CN + H₂SO3 HCN + HSO3 CN is a Bronsted-Lowry base because it is an electron pair acceptor. H₂SO3 is a Lewis acid because it is an electron pair donor. CN is a Lewis base because it is an electron pair donor. This is only a Bronsted-Lowry acid-base reaction (not a Lewis acid-base reaction).
the pH of a 0.020 M solution of NH4Cl is approximately 4.75.
1. The solution with the highest pH would be 0.25 M KOH. KOH is a strong base that completely dissociates in water, resulting in the highest concentration of hydroxide ions (OH-) and, therefore, the highest pH.
2. The salt that will form an acidic solution upon dissolving in water is KCN. KCN is the salt of a weak acid (HCN) and a strong base (KOH). When it dissolves in water, the weak acid component (HCN) will partially dissociate, releasing hydrogen ions (H+), leading to an acidic solution.
3. To determine the pH of a 0.020 M solution of NH4Cl, we need to consider the ionization of the ammonium ion (NH4+) and the equilibrium with water. The ammonium ion acts as a weak acid, and its ionization in water can be represented as follows:
NH4+ + H2O ⇌ NH3 + H3O+
The equilibrium constant expression for this reaction is:
Ka = [NH3][H3O+] / [NH4+]
Given that Ka (the ionization constant of NH4+) is 1.8 × 10^(-5), we can set up an equilibrium expression and solve for the concentration of H3O+ (which is equal to the concentration of OH- due to water being neutral):
1.8 × 10^(-5) = [NH3][H3O+] / [NH4+]
Since the NH4Cl solution only contains NH4+ and Cl-, and Cl- does not contribute to the pH, we can assume that the concentration of NH4+ is equal to the concentration of NH3.
Therefore, [NH3] = [NH4+] = 0.020 M
Plugging this into the equilibrium expression, we have:
1.8 × 10^(-5) = (0.020)([H3O+]) / (0.020)
Simplifying, we find:
[H3O+] = 1.8 × 10^(-5) M
To calculate the pH, we can take the negative logarithm of the H3O+ concentration:
pH = -log10(1.8 × 10^(-5)) ≈ 4.75
Therefore, the pH of a 0.020 M solution of NH4Cl is approximately 4.75.
4. In the given reaction, CN + H2SO3 ⇌ HCN + HSO3, CN is acting as a Lewis base because it donates a pair of electrons to form a bond with H+. H2SO3, on the other hand, is acting as a Bronsted-Lowry acid because it donates a proton (H+) to form a bond with CN. Therefore, the correct statement is: CN is a Lewis base because it is an electron pair donor.
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When 35.0 mL of 0.340M ammonium chloride and 35.0 mL of 0.20M
calcium hydroxide are combined. The pH of the resulting solution
will be...
a. equal to 7
b. less than 7
c. greater than 7
The resulting solution will have a pH greater than 7.
When ammonium chloride (NH4Cl) and calcium hydroxide (Ca(OH)2) react, they form ammonium hydroxide (NH4OH) and calcium chloride (CaCl2). The reaction can be represented as follows:
NH4Cl + Ca(OH)2 → NH4OH + CaCl2
Ammonium hydroxide is a weak base, and when it dissociates in water, it releases hydroxide ions (OH-). The presence of hydroxide ions increases the pH of the solution, making it basic.
On the other hand, calcium chloride is a salt that does not significantly affect the pH of the solution.
Since the reaction between NH4Cl and Ca(OH)2 produces ammonium hydroxide, which increases the concentration of hydroxide ions in the solution, the resulting solution will have a pH greater than 7. Therefore, the correct answer is option c. greater than 7.
The pH of the resulting solution, when 35.0 mL of 0.340M ammonium chloride and 35.0 mL of 0.20M calcium hydroxide are combined, will be greater than 7 due to the formation of ammonium hydroxide.
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PLEASE USE TRIAL AND ERROR / ITERATIVE METHOD IN SOLVING. THANK
YOU!
EXAMPLE 8-9 Effect of Flushing on Flow Rate from a Shower The bathroom plumbing of a building consists of 1.5-cm-diameter copper pipes with threaded connectors, as shown in Fig. 8-52. (a) If the gage
In order to solve the given problem with iterative method, follow these steps:
Step 1: Make an Initial Guess of the pressure drop
Let us assume an initial guess for the pressure drop of 15 kPa, this value will be used to calculate the Reynolds Number which will then be used to calculate the friction factor.
Step 2: Calculate Reynolds Number: The Reynolds number is calculated using the following formula:
Reynolds Number = (4 * Flowrate) / (π * Diameter * Viscosity)
For the given values, the Reynolds Number is calculated as:
Re = (4 × 0.034) / (π × 1.5 × 10^-3 × 8.9 × 10^-4) = 15367.23
Step 3: Calculate friction factor: The friction factor is calculated using the following formula:
f = (ΔP × Diameter) / (2 * ρ * V^2)
For the given values, the friction factor is calculated as:
f = (15 × 10^3 × 1.5 × 10^-2) / (2 × 8.9 × 10^3 × 2.32^2) = 0.0056
Step 4: Calculate the new value of pressure drop: The pressure drop is calculated using the Darcy-Weisbach formula:
ΔP = f * (Length / Diameter) * (ρ * V^2 / 2)
For the given values, the new value of pressure drop is:
ΔP = 0.0056 × (30 / 1.5) × (8.9 × 10^3 × 2.32^2 / 2) = 7.95 kPa
Step 5: Compare the new value of pressure drop with the initial guess. If the difference between the new value of pressure drop and the initial guess is greater than the specified tolerance, then repeat the above steps until the difference between the new value of pressure drop and the initial guess is within the specified tolerance.
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3 AgNO3 + FeCl3 →3 AgCl + Fe(NO3)3
If you combine 6.60 grams of FeCl3 with an excess of AgNO3, how much AgCl will you form?
Answer:
To determine the amount of AgCl formed, we need to follow the stoichiometry of the balanced equation and calculate the molar amounts of the reactants and products.
First, let's calculate the number of moles of FeCl3 used:
Molar mass of FeCl3 = atomic mass of Fe + (3 * atomic mass of Cl)
= (55.845 g/mol) + (3 * 35.453 g/mol)
= 162.204 g/mol
Moles of FeCl3 = mass of FeCl3 / molar mass of FeCl3
= 6.60 g / 162.204 g/mol
= 0.0407 mol
According to the balanced equation, the ratio of FeCl3 to AgCl is 1:3. Therefore, 1 mol of FeCl3 reacts to form 3 mol of AgCl.
Moles of AgCl formed = 3 * moles of FeCl3
= 3 * 0.0407 mol
= 0.1221 mol
Finally, let's calculate the mass of AgCl formed:
Molar mass of AgCl = atomic mass of Ag + atomic mass of Cl
= 107.868 g/mol + 35.453 g/mol
= 143.321 g/mol
Mass of AgCl formed = moles of AgCl formed * molar mass of AgCl
= 0.1221 mol * 143.321 g/mol
= 17.49 g
Therefore, if you combine 6.60 grams of FeCl3 with an excess of AgNO3, you will form approximately 17.49 grams of AgCl.
This question concerns the following elementary liquid-phase reaction: A=B+C (a) Express the net rate of reaction in terms of the initial concentration and conversion of A and the relevant rate constants. [5 marks] (b) Determine the equilibrium conversion for this system. [6 marks] (c) If the reaction is carried out in an isothermal PER, determine the volume required to achieve 90% of your answer to part (b). Use numerical integration where appropriate. [6 marks] (d) For this specific case, discuss ways in which you can maximise the amount of B that can be obtained [3 marks) Data: CAO = 2.5 kmol m-3 Vo = 3.0 mºn-1 krwd = 10.7h-1 Krev = 4.5 [kmol m-'n-1
The net rate of reaction can be expressed in terms of the initial concentration and conversion of A as follows: Rate = -rA = k_fwd * CA * (1 - X).
Where k_fwd is the forward rate constant, CA is the initial concentration of A, and X is the conversion of A. Since the reaction is elementary and has a stoichiometric coefficient of 1 for A, the rate of disappearance of A is equal to the rate of the reaction. (b) To determine the equilibrium conversion for this system, we need to consider the equilibrium constant, K_rev, which is given as K_rev = [B][C]/[A]. For the reaction A = B + C, the equilibrium constant can be written as K_rev = [B][C]/[A] = (Xeq^2)/(1 - Xeq), where Xeq is the equilibrium conversion. We can solve this equation to find the equilibrium conversion. (c) To determine the volume required to achieve 90% of the equilibrium conversion, numerical integration can be used. We need to integrate the equation dX/dV = -rA/CAO with appropriate limits to find the volume at which X = 0.9 * Xeq. This integration takes into account the changing conversion as the reaction proceeds.
(d) To maximize the amount of B that can be obtained, one approach is to operate the reaction at high conversion. This can be achieved by using a high reactant concentration or increasing the residence time of the reactants in the reactor. Additionally, adjusting the temperature and pressure conditions to favor the desired product can enhance the selectivity towards B. Finally, catalysts can be employed to increase the reaction rate and improve the yield of B.
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What is the most likely range for the wavelength of maximum absorption (Amax) for the compound below:a. 246-260 nmb. 215-230 nm c. 276-290 nm d. 261-275 nm e > 320 nmf. 231-245 nm g. 291-305 nm h. 306-320 nm
The most likely range for the wavelength of maximum absorption (Amax) for a compound can be calculated based on the molecular structure and bonding configuration. However, based on the given options, the most likely range for Amax for the given compound is 246-260 nm.
The compound given above has a molecular structure that determines the wavelength of maximum absorption.
The given wavelength ranges are:
a. 246-260 nm
b. 215-230 nm
c. 276-290 nm
d. 261-275 nm
e. >320 nm
f. 231-245 nm
g. 291-305 nm
h. 306-320 nm
The compound structure is not given. Hence, we can assume the Amax range for the given compound based on its class or structural configuration.
The most likely Amax range can be determined using the following parameters:
• If the compound has double bonds, then the Amax range will be around 180-200 nm.
• If the compound has aromatic rings, then the Amax range will be around 250-300 nm.
• If the compound has conjugated structures, then the Amax range will be around 280-320 nm.
• If the compound contains polar functional groups such as OH, NH, COOH, or C=O, then the Amax range will be around 200-300 nm.
Since the structural configuration of the compound is not given, we cannot precisely determine the Amax range.
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Please solve
Question 5 The velocity profile of a fluid flowing through an annulus is given by the following Navier-Stokes derived equation: dP 1 2² ·²+ (Inr-Inr₂) ₂)] dz 4μ Inr-Inr Find the volumetric flo
The volumetric flow rate is given as Q = (πR12 - πr12) (dP/4μ) (1/2) [R13-r13+ (Inr-Inr2) / (2μ)].
Given expression, dP 1 2² ·²+ (Inr-Inr₂) ₂)] dz 4μ Inr-Inr
We know that the volumetric flow rate, Q can be calculated as follows:
Q = A * v = ∫v dA = ∫ v 2πrdr
For steady state flow, the continuity equation is given as follows:
A1v1 = A2v2, since A1 = πR12 - πr12, A2 = πR22 - πr22
Assuming R1 = r2, R2 = r1 and by rearranging the above equation, we get
v2/v1 = (r1/r2)2
Using the above relation, we can write volumetric flow rate as
Q = ∫v dA = ∫ v 2πrdr = 2π∫R1r1v(r) dr= 2π∫R1r1v1(r/r1)2 dr= (2πv1r12/3) [R13-r13]
Now, substituting the given expression of velocity in the above equation, we get
Q = (πR12 - πr12) (dP/4μ) (1/2) [R13-r13+ (Inr-Inr2) / (2μ)]
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Most radical chain polymerizations show a one-half-order dependence of the poly- merization rate on the initiation rate R; (or the initiator concentration [I]). Describe and explain under what reaction conditions [i.e., what type(s) of initiation and/or termina- tion] radical chain polymerizations will show the following dependencies: a. First-order b. Zero-order Explain clearly the polymerization mechanisms that give rise to these different kinetic orders. What is the order of dependence of Rp on monomer concentration in each of these cases. Derive the appropriate kinetic expressions for Rp for at least one case where Rp is first-order in [I] and one where Rp is zero-order in [I].
Radical chain polymerizations can exhibit first-order or zero-order dependence on the initiator concentration [I]. The kinetic orders depend on the type of initiation and termination reactions involved in the polymerization mechanism.
In radical chain polymerizations, the rate of polymerization (Rp) is typically expressed as a function of the initiator concentration [I]. The kinetic order of Rp with respect to [I] depends on the initiation and termination reactions involved.
a. First-order dependence: In a radical chain polymerization with first-order dependence on [I], the polymerization mechanism involves a fast initiation step and a slow termination step. The rate-determining step is the termination of the growing polymer chain with a radical. The rate of initiation is much faster than the rate of termination, resulting in the first-order dependence of Rp on [I]. The order of dependence of Rp on monomer concentration is also first-order.
b. Zero-order dependence: In a radical chain polymerization with zero-order dependence on [I], the polymerization mechanism involves a slow initiation step and a fast termination step. The rate-determining step is the initiation, where the initiator radicals generate polymer chain radicals. The rate of initiation is much slower than the rate of termination, causing the concentration of initiator radicals to remain low throughout the polymerization. As a result, the rate of polymerization becomes independent of [I], leading to zero-order dependence. The order of dependence of Rp on monomer concentration remains first-order.
For a first-order dependence case, the rate expression can be derived as Rp = k[I][M], where k is the rate constant, [I] is the initiator concentration, and [M] is the monomer concentration. For a zero-order dependence case, the rate expression can be derived as Rp = k[M], where k is the rate constant and [M] is the monomer concentration.
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What is the mass per volume (mg/m³, to the nearest 1 mg/m³) concentration of sulfur dioxide, SO2, present in air at a concentration of 20 ppm(v) at a temperature of 18C and atmospheric pressure of 0
The mass per volume concentration of sulfur dioxide (SO₂) in air, with a concentration of 20 ppm(v), at a temperature of 18°C and atmospheric pressure of 0.985 atm, is approximately 529 mg/m³.
To calculate the mass per volume concentration of SO₂, we need to convert the concentration from parts per million by volume (ppm(v)) to mass per volume (mg/m³) using the ideal gas law.
The ideal gas law equation is given as:
PV = nRT
Where:
P = Pressure (atm)
V = Volume (m³)
n = Number of moles
R = Gas constant (0.0821 atm·L/mol·K)
T = Temperature (K)
To convert ppm(v) to mg/m³, we need to calculate the number of moles of SO₂ present in a known volume of air at a given temperature and pressure.
1. Convert ppm(v) to a fraction: 20 ppm(v) = 20/1,000,000 = 0.00002
2. Calculate the number of moles of SO₂:
n = (0.00002) * V
Assuming a volume of air of 1 m³, the number of moles of SO₂ becomes:
n = (0.00002) * 1 = 0.00002 mol
3. Convert temperature from Celsius to Kelvin: 18°C + 273.15 = 291.15 K
4. Use the ideal gas law to solve for pressure:
(0.985 atm) * (1 m³) = (0.00002 mol) * (0.0821 atm·L/mol·K) * (291.15 K)
Solving for the volume, V = 529.22 L
5. Convert volume to cubic meters: V = 529.22 L = 0.52922 m³
6. Calculate the mass of SO₂:
Mass = n * molar mass
Assuming the molar mass of SO₂ is 64.06 g/mol,
Mass = (0.00002 mol) * (64.06 g/mol) = 1.2812 mg
7. Convert mass to mg/m³:
Concentration = Mass / Volume
Concentration = 1.2812 mg / 0.52922 m³ ≈ 529 mg/m³ (to the nearest 1 mg/m³)
The mass per volume concentration of sulfur dioxide (SO₂) in air, with a concentration of 20 ppm(v), at a temperature of 18°C and atmospheric pressure of 0.985 atm, is approximately 529 mg/m³. This calculation helps determine the mass of SO₂ present in a given volume of air and is useful for assessing air quality and environmental impact.
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Using DWSIM of Aspen plus to draw Process design for producing fuel-based methanol with the capacity of 150,000 tons/year
1) process flow sheet
2) full material balance
3) process description
4) PID for full process
The annual output of fuel-based methanol should be 150,000 tons, and the purity of product is greater than 99 wt%. Production time is 8000 h per year. Composition of fresh feed gas: H2 = 72 mol%, CO = 12 mol%, CO2 = 16 mol%. The temperature and pressure of feed gas are 40 ℃ and 2.5 MPa, respectively.
An isothermal tubular reactor is adopted, and the reaction temperature and pressure are 270 ℃ and 5.0 MPa, respectively. The heat-transfer medium is the high-pressure saturated hot water. The reaction equations are as follows:
1. + 2H2 → H3H
2. 2 + 3H2 → H3H + H2
The CO conversion per pass is 18% for Reaction 1, while the CO2 conversion per pass is 12% for Reaction 2. No side reaction needs to be considered. The distillation unit adopts a single-column process.
The process design for producing 150,000 tons/year of fuel-based methanol using DWSIM of Aspen Plus includes a process flow sheet, full material balance, process description, and a PID for the full process. The design incorporates an isothermal tubular reactor, distillation unit, and specific reaction equations to achieve the desired product purity and annual output.
The process design for producing 150,000 tons/year of fuel-based methanol starts with a feed gas composition of 72 mol% H2, 12 mol% CO, and 16 mol% CO2 at a temperature of 40 ℃ and a pressure of 2.5 MPa. The feed gas undergoes two reactions in an isothermal tubular reactor. Reaction 1 is + 2H2 → H3H with a CO conversion per pass of 18%, while Reaction 2 is 2 + 3H2 → H3H + H2 with a CO2 conversion per pass of 12%. There are no side reactions to consider.
To maintain the desired reaction conditions, a high-pressure saturated hot water medium is used as the heat-transfer medium in the tubular reactor. The reaction temperature is set at 270 ℃, and the reaction pressure is set at 5.0 MPa.
The distillation unit employs a single-column process to separate and purify the methanol product. The aim is to achieve a product purity greater than 99 wt%. The full material balance accounts for all the input streams, reactions, and output streams, ensuring that the annual output of 150,000 tons of methanol is met within the production time of 8000 hours per year.
The process design also includes a process flow sheet, which illustrates the sequence of operations, equipment, and streams involved in the production of fuel-based methanol. Additionally, a PID (Piping and Instrumentation Diagram) is provided, detailing the instrumentation and control systems used in the full process. These design elements collectively enable the production of 150,000 tons/year of fuel-based methanol with the specified purity.
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Copper has two natural isotopes ⁶³Cu and ⁶⁵Cu. What is the percentage of the mass of the lighter isotope if the relative atomic mass of copper is 63.54
You have been given a task to investigate how colour/paint can influence energy consumption in our laboratories and auditoriums. Although you did not get an opportunity to perform an experiment, but based on your knowledge, answer the following question. a. Do you think colour/paint of the laboratories and auditoriums can have significant energy saving effect? (1) b. If you are given the colours: red, black, and white, which colour do you think can have a significant energy? (2) c. Discuss and explain how the colour you have chosen can really save energy, in terms of temperature? (6) d. Give five benefits of changing colour/paint of the laboratories and auditoriums? (5) e. Explain in detail the types of energy/energies (specifically temperature) influenced by colour/paint and how this energy can be lost and the costs involved?
The color or paint of laboratories and auditoriums can indeed have a significant energy-saving effect. Different colors absorb and reflect light differently, which can impact the temperature and energy consumption within the space. While an experiment was not conducted, based on knowledge and understanding, color choice can play a role in energy efficiency.
1. The color red is known to absorb more light and heat, which can increase the temperature in a space. Therefore, it may not have a significant energy-saving effect compared to other colors.
2. Black color also absorbs more light and heat, leading to higher temperatures. It is likely to contribute to increased energy consumption rather than energy savings.
3. On the other hand, the white color reflects more light and heat, keeping the space cooler. By reflecting sunlight and reducing heat absorption, it can contribute to energy savings.
4. The reflection of light and heat by white color helps in reducing the need for cooling systems and air conditioning, thus reducing energy consumption and associated costs.
5. Benefits of changing color/paint in laboratories and auditoriums include improved energy efficiency, reduced cooling and heating costs, enhanced comfort for occupants, a more visually appealing environment, and a positive impact on the overall sustainability and environmental footprint.
6. The type of energy influenced by color/paint is primarily thermal energy, which is related to temperature. Different colors absorb or reflect light, which affects the amount of heat transferred to or from the surroundings. By reducing heat absorption, the cooling load on HVAC systems is reduced, resulting in energy savings and lower costs. Additionally, the choice of color can impact visual perception, psychological factors, and the overall ambiance of the space.
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Write about the waste recycling process of oil and gas
companies. (750 words)
The waste recycling process in oil and gas companies plays a critical role in minimizing environmental impact and promoting sustainable practices. These companies generate various types of waste during their operations, including drilling fluids, produced water, waste oils, and solid waste. Recycling these wastes helps reduce pollution, conserve resources, and mitigate the overall environmental footprint of the industry. This article provides an overview of the waste recycling process in oil and gas companies.
Drilling Fluids Recycling:
Drilling fluids, also known as mud, are used during the drilling process to lubricate the drill bit, cool the drilling equipment, and carry cuttings to the surface. After use, drilling fluids become contaminated with drill cuttings and other impurities. To recycle drilling fluids, a process known as mud recycling or mud reconditioning is employed. This process involves removing the solid cuttings and treating the fluid with additives to restore its properties for reuse in subsequent drilling operations. The recycled drilling fluids are carefully managed to meet regulatory requirements and industry standards.
Produced Water Treatment:
Produced water is the wastewater that comes to the surface along with oil and gas during production operations. This water contains various contaminants, including hydrocarbons, heavy metals, and dissolved solids. Proper treatment is essential to ensure the water is safe for disposal or potential reuse. Produced water treatment typically involves several stages, such as separation, filtration, chemical treatment, and sometimes advanced treatment processes like membrane filtration or reverse osmosis. The treated water can be discharged according to regulations, used for irrigation purposes, or reinjected into the reservoir for enhanced oil recovery.
Waste Oils Recycling:
Waste oils, such as used lubricating oils, hydraulic fluids, and transformer oils, are generated throughout oil and gas operations. These oils can be reprocessed and recycled into new lubricants or fuel oils. The recycling process usually involves removing impurities, such as water and solids, through methods like centrifugation, filtration, and distillation. The cleaned oil can then be re-refined or blended with other additives to meet specific performance requirements.
Solid Waste Management:
Oil and gas operations also produce solid waste, including drill cuttings, contaminated soil, and various other materials. Proper management of solid waste is crucial to prevent contamination and reduce the amount of waste sent to landfills. Techniques such as solidification, stabilization, thermal treatment, and recycling are employed to manage and treat solid waste. For instance, drill cuttings can be processed to separate and recover residual oil, while contaminated soil can undergo remediation processes to remove or neutralize pollutants.
The waste recycling process in oil and gas companies plays a vital role in minimizing environmental impact and promoting sustainability. By recycling drilling fluids, treating produced water, recycling waste oils, and effectively managing solid waste, these companies can significantly reduce pollution, conserve resources, and mitigate their environmental footprint. The implementation of efficient waste recycling processes requires adherence to regulatory requirements, the use of appropriate technologies, and continuous monitoring to ensure compliance with industry standards and environmental protection. By prioritizing waste recycling, oil and gas companies can contribute to a more sustainable and environmentally responsible future.
Please note that the information provided is based on general knowledge and industry practices. Specific recycling processes and technologies may vary among different oil and gas companies and depend on regional regulations and requirements.
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Protease inhibitors are a class of anti-viral drugs that have had success in treating HIV/AIDS. The following molecules were synthesized as potential HIV protease inhibitors. (U, Org. Chem 1998,63, 48
The molecules shown in the diagram are potential HIV protease inhibitors. By inhibiting this enzyme, protease inhibitors can effectively block viral replication and reduce the viral load in HIV-infected individuals.
Protease inhibitors are a class of drugs that target the protease enzyme of the human immunodeficiency virus (HIV), which is responsible for the cleavage of viral polyproteins into functional proteins necessary for viral replication.
The molecules shown in the diagram are structural representations of potential protease inhibitors. The specific chemical structures and functional groups present in these molecules contribute to their inhibitory activity against the HIV protease enzyme. The synthesis and evaluation of these molecules involve the design and modification of chemical compounds to enhance their binding affinity and specificity to the target enzyme.
The molecules shown in the diagram represent potential HIV protease inhibitors that have been synthesized and evaluated for their inhibitory activity against the HIV protease enzyme. Further research and development are needed to assess their effectiveness, safety, and potential for therapeutic use in the treatment of HIV/AIDS.
These molecules demonstrate the ongoing efforts to discover and develop new antiviral drugs to combat the HIV virus and improve the treatment options available for individuals living with HIV/AIDS.
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5. A reversed Carnot cycle engine, used as a heat pump, delivers 980 kJ/min of heat at 48° C. It receives heat at 18° C. Determine the power input. 6. A Carnot cycle engine using air as the working
The power input for the reversed Carnot cycle engine is approximately 10,315.79 kJ/min. The thermal efficiency of the Carnot cycle engine using air as the working fluid is approximately 70.9%.
The power input for the reversed Carnot cycle engine can be determined by the equation:
Power input = Heat output / Thermal efficiency
To calculate the power input, we need to determine the thermal efficiency of the reversed Carnot cycle engine. The thermal efficiency of a Carnot cycle is given by:
Thermal efficiency = 1 - (Tc/Th)
where Tc is the absolute temperature of the cold reservoir and Th is the absolute temperature of the hot reservoir.
Heat output = 980 kJ/min
Temperature of the hot reservoir (Th) = 48°C = 48 + 273.15 = 321.15 K
Temperature of the cold reservoir (Tc) = 18°C = 18 + 273.15 = 291.15 K
Thermal efficiency = 1 - (291.15 K / 321.15 K) = 0.095 or 9.5%
Now we can calculate the power input:
Power input = Heat output / Thermal efficiency
= 980 kJ/min / 0.095
= 10,315.79 kJ/min
To calculate the thermal efficiency of a Carnot cycle engine using air as the working fluid, we need to know the temperatures of the hot and cold reservoirs.
Let Th be the absolute temperature of the hot reservoir and Tc be the absolute temperature of the cold reservoir.
The thermal efficiency of a Carnot cycle is given by:
Thermal efficiency = 1 - (Tc / Th)
Th = 600°C = 600 + 273.15 = 873.15 K
Tc = -20°C = -20 + 273.15 = 253.15 K
Thermal efficiency = 1 - (253.15 K / 873.15 K) = 0.709 or 70.9%
The thermal efficiency represents the ratio of the work output to the heat input in a Carnot cycle engine. To determine the power output or work output, we would need additional information.
The power input for the reversed Carnot cycle engine is approximately 10,315.79 kJ/min. The thermal efficiency of the Carnot cycle engine using air as the working fluid is approximately 70.9%. The power output or work output cannot be determined without additional information.
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In testing for the presence of halides, we add HNO3 then AgNO3, the acid is added to remove carbonate or sulfite ions that may be present. why we don't also remove sulfate ions that may be present ? and how to remove them so that we only test for halides ?
In the testing for the presence of halides using HNO3 and AgNO3, the addition of acid (HNO3) serves to remove carbonate or sulfite ions that may be present because these ions can interfere with the precipitation of silver halides. Carbonate ions can form insoluble silver carbonate, and sulfite ions can react with silver ions, forming a precipitate of silver sulfite. To remove sulfate ions from the sample, you can add barium chloride (BaCl2) to the sample.
The acid is added to remove carbonate or sulfite ions that may be present because these ions can also react with silver nitrate to form precipitates. However, sulfate ions do not react with silver nitrate to form a precipitate. Therefore, there is no need to remove sulfate ions before testing for halides.
However, if you want to remove sulfate ions from the sample, you can add barium chloride (BaCl2) to the sample.This will result in the formation of a white precipitate of barium sulfate (BaSO4) which is insoluble in water.
The precipitate can then be filtered out, leaving behind a sample that is free of sulfate ions.
When silver nitrate reacts with different halide ions it gives different colours.
If a precipitate forms when silver nitrate is added to a solution, the color of the precipitate can be used to identify the halide ion that is present in the solution.
Thus, we don't also remove sulfate ions that may be present as it does not interfere with the precipitation of halides and if you want to remove them you can use barium chloride (BaCl2).
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8. [10 points] Nitrogen is compressed isentropically from 100 kPa and 27 °C to 1000 kPa in a piston cylinder device. Assume ideal gas and determine its final temperature. Given C₂= 1.042 and C=0.745
The final temperature of nitrogen, when compressed isentropically from 100 kPa and 27 °C to 1000 kPa, is approximately 132.15 K.
To determine the final temperature of nitrogen when compressed isentropically from 100 kPa and 27 °C to 1000 kPa, we can use the ideal gas equation and the isentropic process relationship.
The ideal gas equation is given as:
PV = mRT,
where P is the pressure, V is the volume, m is the mass, R is the specific gas constant, and T is the temperature.
For an isentropic process, we have the relationship:
P₁V₁^γ = P₂V₂^γ,
P₁ = 100 kPa
P₂ = 1000 kPa
T₁ = 27 °C
= 27 + 273.15
= 300.15 K
C₂ = 1.042
C = 0.745
We need to calculate T₂, the final temperature.
First, let's find the initial volume, V₁, using the ideal gas equation:
V₁ = (mRT₁) / P₁.
Next, let's rearrange the isentropic process relationship to solve for the final volume, V₂:
V₂ = V₁ * (P₁ / P₂)^(1/γ).
We can now enter the provided values into the equations and find the final temperature by solving.
Rearranging the ideal gas equation:
V₁ = (mRT₁) / P₁
V₁ = (m * R * 300.15 K) / (100 kPa)
V₁ = (m * R * 300.15) / (100000 Pa)
Rearranging the isentropic process relationship:
V₂ = V₁ * (P₁ / P₂)^(1/γ)
V₂ = [(m * R * 300.15) / (100000 Pa)] * [(100 kPa) / (1000 kPa)]^(1/γ)
V₂ = [(m * R * 300.15) / (100000 Pa)] * (0.1)^(1/γ)
Now, let's use the ideal gas equation again to find the final temperature, T₂:
P₂ * V₂ = m * R * T₂
(1000 kPa) * [(m * R * 300.15) / (100000 Pa)] * (0.1)^(1/γ) = m * R * T₂
(1000) * (m * R * 300.15) * (0.1)^(1/γ) = m * R * T₂
Canceling out the mass and R:
1000 * 300.15 * (0.1)^(1/γ) = T₂
Substituting the given value for γ:
1000 * 300.15 * (0.1)^(1/1.042) = T₂
Calculating the final temperature, T₂:
T₂ ≈ 132.15 K
The final temperature of nitrogen, when compressed isentropically from 100 kPa and 27 °C to 1000 kPa, is approximately 132.15 K.
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Exactly 26 g of 86 g of a given amount of protactinium-234 remains after 26.76 hours. What is the half-life of protractinium-234?
1. Why does graphite does not have a melting point and only
sublimes at temperatures above 3800K? (cite a paper)
2. Is it good for uses of heating purposes?
Graphite's sublimation at high temperatures is due to its unique structure and weak interlayer bonding. Graphite's high thermal conductivity, and stability at high temperatures make it suitable for heating applications.
Graphite consists of layers of carbon atoms arranged in a hexagonal lattice. Within each layer, the carbon atoms are bonded together through strong covalent bonds, creating a strong and stable structure. However, the bonding between the layers is relatively weak, allowing the layers to slide over each other easily.
The sublimation of graphite occurs because the energy required to break the weak interlayer bonds is much lower than the energy required to convert the covalent bonds within the layers from a solid to a liquid. Therefore, when graphite is heated to temperatures above 3800K (3526.85°C or 6380.33°F), the thermal energy is sufficient to overcome the interlayer bonding, causing the graphite to sublime directly into a gas without passing through a liquid phase.
Graphite is commonly used in heating applications due to its excellent thermal conductivity and stability at high temperatures.
Graphite's high thermal conductivity allows it to rapidly conduct heat and distribute it evenly, making it suitable for applications requiring uniform heating. It also has a relatively low coefficient of thermal expansion, meaning it can withstand thermal cycling without cracking or deforming.
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Q1(A) (5) A binary liquid mixture is in equilibrium with its vapor at 300K. The liquid mole fraction of species 1 is 0.4 and the molar excess Gibbs free energy is 2001/mol If 7, -1.09, calculate the value of 7, denotes liquid-phase activity coefficient of species i in the binary mixture.
The liquid-phase activity coefficient (γ₁) of species 1 in the binary mixture at 300K, with a molar excess Gibbs free energy of 2001 J/mol, is approximately 2.226.
To calculate the value of the liquid-phase activity coefficient (γ₁) of species i in the binary mixture, we can use the equation:
ΔG_ex = RT * ln(γ₁)
where:
ΔG_ex is the molar excess Gibbs free energy (2001 J/mol in this case),
R is the gas constant (8.314 J/(mol·K)),
T is the temperature (300 K in this case),
ln denotes the natural logarithm,
γ₁ is the liquid-phase activity coefficient of species 1.
Rearranging the equation, we can solve for γ₁:
γ₁ = exp(ΔG_ex / (RT))
Substituting the given values, we get:
γ₁ = exp(2001 J/mol / (8.314 J/(mol·K) * 300 K))
γ₁ = exp(2001 / (8.314 * 300))
γ₁ = exp(0.801)
γ₁ ≈ 2.226
Therefore, the value of the liquid-phase activity coefficient (γ₁) of species 1 in the binary mixture is approximately 2.226.
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With explainations please am not in hurry (45)
Using activities, find Ag+ in 0.05 M KSCN saturated with AgSCN Ksp for AgSCN = 1.1 *10-1²
The concentration of Ag+ ions in 0.05 M KSCN saturated with AgSCN is 1.05 × 10^-6 M.
The solubility product (Ksp) of AgSCN is 1.1 × 10^-12. In this activity, we'll use this knowledge to locate the Ag+ ion concentration in 0.05 M KSCN saturated with AgSCN.
KSCN dissociates into K+ and SCN-.
The reaction is: KSCN(aq) → K+(aq) + SCN-(aq)
The dissociation equation for AgSCN is: AgSCN(aq) ⇔ Ag+(aq) + SCN-(aq)
At equilibrium, [Ag+] and [SCN-] are the same, and we'll use x to represent both.
The initial concentration of KSCN was 0.05 M.
Let us first write the reaction for AgSCN dissociation: AgSCN(aq) ⇔ Ag+(aq) + SCN-(aq)
Let's suppose that the concentration of SCN- is x M, and the amount of Ag+ that is released is also x M. Then, the concentration of AgSCN at equilibrium would be (0.05 - x) M.
Ksp can be calculated using the equation Ksp = [Ag+][SCN-].
We can substitute the values obtained above.
Ksp = x * xKsp = x²Ksp = 1.1 × 10^-12M²
Solving the above equation gives us: x = √(Ksp)x = √(1.1 × 10^-12)x = 1.05 × 10^-6 mol/L
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When one of the enantiomers of 2-butanol is placed in a polarimeter, the observed rotation is 4.05⁰ counterclockwise. The solution was made by diluting 6.0 grams of (-)-2-butanol to a total of 40.0 mL and the solution was placed into a 200 mm polarimeter tube for the measurement. Determine the specific rotation for this enantiomer of 2-butanol. Show work using the equation function (insert tab of the editing menu above) to receive credit. Uploaded answers or work without using the equation function, will not be graded. B. What will be the specific rotation of the dextrorotatory enantiomer?
- The specific rotation for this enantiomer of 2-butanol is -13.5°/g·dm/mL.
- The specific rotation of the dextrorotatory enantiomer would be +13.5°/g·dm/mL.
To determine the specific rotation of the enantiomer of 2-butanol and the specific rotation of the dextrorotatory enantiomer, we can use the formula:
Specific Rotation = Observed Rotation / (concentration in g/mL * path length in dm)
Observed Rotation = -4.05° (counterclockwise)
Concentration = 6.0 g / 40.0 mL = 0.15 g/mL
Path Length = 200 mm = 20 cm = 2 dm
Now we can calculate the specific rotation for the enantiomer of 2-butanol:
Specific Rotation = (-4.05°) / (0.15 g/mL * 2 dm)
Specific Rotation = -4.05° / 0.30 g·dm/mL
Specific Rotation = -13.5°/g·dm/mL
The specific rotation for this enantiomer of 2-butanol is -13.5°/g·dm/mL.
To determine the specific rotation of the dextrorotatory enantiomer, we can use the fact that enantiomers have equal magnitudes of specific rotation but opposite signs. Therefore, the specific rotation of the dextrorotatory enantiomer would be +13.5°/g·dm/mL.
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A LOAEL is defined as:
The lowest hazard ratio in rats and mice
The Litany Of Adverse Elemental Liquidations
The lowest dose that demonstrates a significant increase in an observable adverse effect
The lowest level without an effect on biomarkers of exposure
The lowest level that causes death in 50% of the population over a defined period of time
A LOAEL is defined as the lowest dose that demonstrates a significant increase in an observable adverse effect. The term LOAEL stands for "Lowest Observed Adverse Effect Level."
When testing chemicals and other substances for toxicity, the goal is to determine the concentration or dose at which adverse effects begin to appear. The LOAEL is the lowest dose at which an adverse effect is observed. This value can be used to establish a safe level of exposure to a substance.
To determine the LOAEL, a series of tests are conducted in which different doses of the substance being tested are administered to test animals. The animals are observed for any adverse effects, such as changes in behavior, weight loss, or organ damage. The lowest dose at which an adverse effect is observed is the LOAEL.
It is important to note that the LOAEL is a relative measure of toxicity. It only provides information on the dose at which an adverse effect is first observed and not on the severity of the effect. In addition, the LOAEL may vary depending on the species tested and other factors.
In summary, the LOAEL is the lowest dose at which an observable adverse effect is detected. This value is used to establish a safe level of exposure to a substance.
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How many liters of a 0. 325 M K2CrO4 stock solution are needed to prepare 4. 00 L of 0. 212 M K2CrO4?
Therefore, approximately 2.61 liters of the 0.325 M K2CrO4 stock solution are needed to prepare 4.00 L of the 0.212 M K2CrO4 solution.
To determine the volume of the stock solution needed to prepare the desired concentration, we can use the equation:
C1V1 = C2V2
Where:
C1 = concentration of the stock solution
V1 = volume of the stock solution
C2 = desired concentration
V2 = desired volume
Plugging in the given values:
C1 = 0.325 M
V1 = ?
C2 = 0.212 M
V2 = 4.00 L
Solving for V1:
C1V1 = C2V2
0.325 V1 = 0.212 * 4.00
0.325 V1 = 0.848
V1 = 0.848 / 0.325
V1 ≈ 2.61 L
Therefore, approximately 2.61 liters of the 0.325 M K2CrO4 stock solution are needed to prepare 4.00 L of the 0.212 M K2CrO4 solution.
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The design conditions for a continuous stirred-tank reactor are
as given here. Would the reactor be stable with a constant jacket
temperature?
Feed = 1000 kg/hr at 20 °C, containing 50% A
Cp = 0:75
c
The reactor would not be stable with a constant jacket temperature. To determine the stability of the reactor, we need to consider the heat transfer requirements and the reaction kinetics.
In a continuous stirred-tank reactor (CSTR), the heat transfer occurs through the jacket surrounding the reactor. If the jacket temperature is held constant, it implies that the heat transfer rate into the reactor is also constant. However, in most cases, the heat generation or consumption due to the exothermic or endothermic nature of the reaction is not constant. This can lead to a mismatch between the heat input and output, resulting in an unstable reactor temperature.
In this case, we are given the feed rate, composition, and heat capacity of the feed. However, we do not have information about the heat of reaction or any other kinetic parameters. Without this information, we cannot determine the exact stability of the reactor.
Based on the given information, we can conclude that the reactor would not be stable with a constant jacket temperature. To ensure stability, it is necessary to carefully design the heat transfer system, taking into account the heat of reaction and other kinetic parameters. Additional information is needed to perform a more detailed analysis and determine the stability of the reactor.
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with step-by-step solution
14. Barium sulfate, BaSO4, is needed for use in the "barium cocktail", a chemical given to patients prior to x-raying their intestinal tracts, this is based on the equation: Ba (NO3)2 + Na2SO4 = BaSO4
To prepare barium sulfate (BaSO4) for the "barium cocktail" used in X-ray imaging, you need to mix barium nitrate (Ba(NO3)2) with sodium sulfate (Na2SO4) according to the balanced chemical equation:
Ba(NO3)2 + Na2SO4 → BaSO4.
Determine the molar masses of the compounds involved:
Molar mass of Ba(NO3)2:
Ba: 137.33 g/mol
N: 14.01 g/mol
O: 16.00 g/mol (x3 because of three oxygen atoms)
Total: 137.33 + 14.01 + (16.00 x 3) = 261.33 g/mol
Molar mass of Na2SO4:
Na: 22.99 g/mol (x2 because of two sodium atoms)
S: 32.07 g/mol
O: 16.00 g/mol (x4 because of four oxygen atoms)
Total: (22.99 x 2) + 32.07 + (16.00 x 4) = 142.04 g/mol
Molar mass of BaSO4:
Ba: 137.33 g/mol
S: 32.07 g/mol
O: 16.00 g/mol (x4 because of four oxygen atoms)
Total: 137.33 + 32.07 + (16.00 x 4) = 233.39 g/mol
Use the balanced chemical equation to determine the stoichiometric ratio:
From the balanced equation: 1 mol Ba(NO3)2 reacts with 1 mol Na2SO4 to produce 1 mol BaSO4.
Calculate the amount of BaSO4 required:
Let's assume you need to prepare 100 grams of BaSO4.
Calculate the number of moles of BaSO4:
Moles = Mass / Molar mass = 100 g / 233.39 g/mol ≈ 0.428 mol
Calculate the amount of Ba(NO3)2 required:
Since the stoichiometric ratio is 1:1, you'll need an equal amount of Ba(NO3)2 as BaSO4.
Moles of Ba(NO3)2 = 0.428 mol
Calculate the mass of Ba(NO3)2 required:
Mass = Moles × Molar mass = 0.428 mol × 261.33 g/mol ≈ 111.87 g
To prepare 100 grams of barium sulfate (BaSO4) for the "barium cocktail," you would need approximately 111.87 grams of barium nitrate (Ba(NO3)2).
Barium sulfate, BaSO4, is needed for use in the "barium cocktail", a chemical given to patients prior to x-raying their intestinal tracts, this is based on the equation: Ba (NO3)2 + Na2SO4 = BaSO4 + 2NaNO3. A chemist began with 75 grams of barium nitrate and excess sodium sulfate. After collecting and drying the product, 63.45g of barium sulfate was isolated. The percentage yield of BaSO4 is a.48.90% b. 94.80% c. 81.90% d. 74.60%
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