The molar solubility of the salt that produces [X²⁺](aq) and [Y³⁻] (aq) ions is 7.39 x 10⁻⁹ M.
To calculate the molar solubility of the salt, we must find the volume of the solution first.
Volume of solution, V = 100mL (or) 100cm³
We know that for the sparingly soluble salt, X3Y2, the equilibrium is given by the following equation:
⟶ X3Y2(s) ⇋ 3X²⁺(aq) + 2Y³⁻(aq)
At equilibrium, Let the solubility of X3Y2 be ‘S’ moles per liter. Then, The equilibrium concentration of X²⁺ is 3S moles per liter.
The equilibrium concentration of Y³⁻ is 2S moles per liter. The solubility product constant (Ksp) of X3Y2 is given by:
Ksp = [X²⁺]³ [Y³⁻]²
But we know that [X²⁺] = 3S and [Y³⁻] = 2S
Thus, Ksp = (3S)³(2S)²
Ksp = 54S⁵or
S = (Ksp/54)⁰⁽.⁵⁾
S = (1.50 x 10⁻²¹/54)⁰⁽.⁵⁾
= 7.39 x 10⁻⁹ mol/L (or) 7.39 x 10⁻⁶ g/L
Therefore, the molar solubility of the given salt is 7.39 x 10⁻⁹ M.
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a) In your own words with help of diagrams describe the movement of solid particles in liquid and what forces are typically operating
[5 marks]
Due to the combined effect of the forces acting on solid particles in liquids, solid particles in a liquid exhibit a continuous and random motion known as Brownian motion.
What is the movement of solid particles in liquids?When solid particles are suspended in a liquid, they can exhibit various types of movement due to the forces acting upon them.
The movement of solid particles in a liquid is known as Brownian motion. This motion is caused by the random collision of liquid molecules with solid particles.
The forces operating in the movement of solid particles in a liquid include:
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The movement of solid particles in a liquid can be explained by diffusion and sedimentation.
In addition, Brownian motion, a random motion of particles suspended in a liquid, also plays a role. The particles' motion is influenced by gravitational, viscous, and interparticle forces. The solid particles in a liquid have a random motion that causes them to collide with one another. The rate of collision is influenced by factors such as particle concentration, viscosity, and temperature. The movement of solid particles in a liquid is governed by the following principles:
Diffusion is the process by which particles spread out in a fluid. The rate of diffusion is influenced by temperature, particle size, and the concentration gradient. A concentration gradient exists when there is a difference in concentration across a distance. In other words, the rate of diffusion is proportional to the concentration gradient. Diffusion is essential in biological processes such as respiration and excretion.Sedimentation is the process by which heavier particles settle to the bottom of a container under the influence of gravity. The rate of sedimentation is influenced by the size and shape of the particle, the viscosity of the liquid, and the strength of the gravitational field. Sedimentation is important in the separation of liquids and solids.
Brownian motion is the random motion of particles suspended in a fluid due to the impact of individual fluid molecules. The rate of Brownian motion is influenced by the size of the particles, the temperature, and the viscosity of the fluid. Brownian motion is important in the movement of particles in biological systems. The forces operating on solid particles in a liquid are gravitational force, viscous force and interparticle force. The gravitational force pulls particles down towards the bottom of the liquid container, while the viscous force acts to slow down the movement of particles. The interparticle force is the force that particles exert on each other, causing them to either attract or repel. These forces play a crucial role in determining the motion of particles in a liquid.
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A monatomic ideal gas, kept at the constant pressure 1.804E+5 Pa during a temperature change of 26.5 °C. If the volume of the gas changes by 0.00476 m3 during this process, how many mol of gas where present?
Approximately 0.033482 moles of gas were present during the process of the temperature change.
To find the number of moles of gas present during the process, we can use the ideal gas law:
PV = nRT
where: P is the pressure (1.804E+5 Pa),
V is the volume (0.00476 m³),
n is the number of moles,
R is the ideal gas constant (8.314 J/(mol·K)),
T is the temperature change in Kelvin.
First, we need to convert the temperature change from Celsius to Kelvin:
ΔT = 26.5 °C = 26.5 K
Rearranging the ideal gas law equation to solve for the number of moles:
n = PV / (RT)
Substituting the given values into the equation:
n = (1.804E+5 Pa × 0.00476 m³) / (8.314 J/(mol·K) × 26.5 K)
Simplifying the equation and performing the calculations:
n ≈ 0.0335 mol
Therefore, approximately 0.0335 moles of gas were present during the process.
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A geothermal power plant uses dry steam at a temperature of 308 °C and cooling water at a temperature of 23 °C. What is the maximum % efficiency the plant can achieve converting the geothermal heat to electricity?
The maximum efficiency the geothermal power plant can achieve in converting geothermal heat to electricity is approximately 49.09%
The maximum efficiency of a heat engine is determined by the Carnot efficiency, which depends on the temperatures of the hot and cold reservoirs. In this case, the hot reservoir is the geothermal steam at 308 °C (581 K), and the cold reservoir is the cooling water at 23 °C (296 K).
The Carnot efficiency (η_Carnot) is given by the formula:
η_Carnot = 1 - (T_cold / T_hot)
where T_cold is the temperature of the cold reservoir and T_hot is the temperature of the hot reservoir.
Substituting the given temperatures:
η_Carnot = 1 - (296 K / 581 K)
η_Carnot ≈ 0.4909 or 49.09%
Therefore, the maximum efficiency the geothermal power plant can achieve in converting geothermal heat to electricity is approximately 49.09%
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The number of moles of CO² which contain 8. 00g of oxygen is
Assume an isolated volume V that does not exchange temperature with the environment. The volume is divided, by a heat-insulating diaphragm, into two equal parts containing the same number of particles of different real gases. On one side of the diaphragm the temperature of the gas is T1, while the temperature of the gas on the other side is T2. At time t0 = 0 we remove the diaphragm. Thermal equilibrium occurs. The final temperature of the mixture will be T = (T1 + T2) / 2; explain
The final temperature of the mixture, T, will be the average of the initial temperatures of the two gases: T = (T1 + T2) / 2. This result holds true when the volume is isolated, and no heat exchange occurs with the surroundings.
When the diaphragm is removed and the two gases are allowed to mix, they will undergo a process known as thermal equilibration. In this process, the particles of the two gases will interact with each other and exchange energy until they reach a state of thermal equilibrium.
At the initial state (t = 0), the gases are at different temperatures, T1 and T2. As the diaphragm is removed, the particles from both gases will start to collide with each other. During these collisions, energy will be transferred between the particles.
In an isolated volume where no heat exchange occurs with the environment, the total energy of the system (which includes both gases) is conserved. Energy can be transferred between particles through collisions, but the total energy of the system remains constant.
As the particles collide, energy will be transferred from the higher temperature gas (T1) to the lower temperature gas (T2) and vice versa. This energy transfer will continue until both gases reach a common final temperature, denoted as T.
In the process of reaching thermal equilibrium, the energy transfer will occur until the rates of energy transfer between the gases become equal. At this point, the temperatures of the gases will no longer change, and they will have reached a common temperature, which is the final temperature of the mixture.
Mathematically, the rate of energy transfer between two gases can be proportional to the temperature difference between them. So, in the case of two equal volumes of gases with temperatures T1 and T2, the energy transfer rate will be proportional to (T1 - T2). As the gases reach equilibrium, this energy transfer rate becomes zero, indicating that (T1 - T2) = 0, or T1 = T2.
Therefore, the final temperature of the mixture, T, will be the average of the initial temperatures of the two gases: T = (T1 + T2) / 2. This result holds true when the volume is isolated, and no heat exchange occurs with the surroundings.
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7.27. An expander operates adiabatically with nitrogen entering at T, and P, with a molar flow rate n. The exhaust pressure is P2, and the expander efficiency is n. Estimate the power output of the expander and the temperature of the exhaust stream for one of the following sets of operating conditions. (a) T1 = 480°C, P, = 6 bar, n= 200 mol-s-!, P2 = 1 bar, n=0.80. (b) T1 = 400°C, P, = 5 bar, n= 150 mol-s-1.P2 = 1 bar, n=0.75.
The power output of the expander is 52.87 kW for the first set of operating conditions and 41.55 kW for the second set of operating conditions. The temperature of the exhaust stream is 123.7 K for the first set of operating conditions and 104.7 K for the second set of operating conditions.
In the given problem, a nitrogen expander is adiabatically operating with the following parameters: Inlet temperature T1Inlet pressure P1Molar flow rate n Exhaust pressure P2Expander efficiency ηThe task is to calculate the power output of the expander and the temperature of the exhaust stream. Let's calculate the power output of the expander using the following equation: Power = nRT1 η{1 - [(P2/P1) ^ ((k - 1) / k)]}where k is the ratio of specific heats. Rearranging the equation, we get: Power = nRT1 η [1 - exp (((k - 1) / k) ln (P2/P1))]Put the values in the above equation and solve it for both the cases.
(a) T1 = 480°C, P1 = 6 bar, n = 200 mol-s-1, P2 = 1 bar, η = 0.80k = 1.4 for nitrogen gas.R = 8.314 kJ/mol KPower = 200 * 8.314 * (480 + 273) * 0.80 / (1.4 - 1) * [1 - exp (((1.4 - 1) / 1.4) * ln (1/6))]Power = 52.87 kW
(b) T1 = 400°C, P1 = 5 bar, n = 150 mol-s-1, P2 = 1 bar, η = 0.75R = 8.314 kJ/mol KPower = 150 * 8.314 * (400 + 273) * 0.75 / (1.4 - 1) * [1 - exp (((1.4 - 1) / 1.4) * ln (1/5))]Power = 41.55 kW
The next step is to calculate the temperature of the exhaust stream. We can use the following equation to calculate the temperature:T2 = T1 (P2/P1)^((k-1)/k)Put the values in the above equation and solve it for both the cases.
(a) T2 = 480 * (1/6) ^ ((1.4-1)/1.4)T2 = 123.7 K
(b) T2 = 400 * (1/5) ^ ((1.4-1)/1.4)T2 = 104.7 K
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The fact that water is often the solvent in a solution demonstrates that water can ______. multiple choice question.
The fact that water is often the solvent in a solution demonstrates that water can dissolve a wide range of substances.
Water's ability to dissolve various solutes is due to its unique molecular structure and polarity.
Water is a polar molecule, meaning it has a slightly positive charge on one end (the hydrogen atoms) and a slightly negative charge on the other end (the oxygen atom). This polarity allows water molecules to form hydrogen bonds with other polar molecules or ions, facilitating the dissolution process.
Water's ability to dissolve substances is essential for many biological and chemical processes. In living organisms, water serves as the primary solvent for metabolic reactions, transporting nutrients, ions, and waste products. It allows for the dissolution of polar molecules like sugars, amino acids, and salts, enabling their efficient transport within cells and throughout the body.
Additionally, water's solvent properties are crucial in environmental processes. It contributes to the weathering of rocks, enabling the release of essential minerals into the soil. Water also plays a vital role in the formation of aqueous solutions in nature, such as the oceans and rivers, which support diverse ecosystems.
In conclusion, water's role as a solvent in many solutions highlights its remarkable ability to dissolve a wide range of substances due to its molecular structure and polarity. This characteristic is fundamental for numerous biological, chemical, and environmental processes.
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Why did the flame of a candle go out when a jar was put on top of it
These byproducts can accumulate within the closed jar, further contributing to the depletion of oxygen and ultimately causing the flame to go out.
When a jar is placed on top of a candle, it creates a closed environment within the jar. This closed environment leads to a depletion of oxygen, which is necessary for combustion to occur. As the candle burns, it consumes oxygen from the surrounding air to sustain the flame.
When the jar is placed over the candle, it limits the availability of fresh air and restricts the flow of oxygen into the jar. As the candle burns and consumes the available oxygen, it eventually uses up the oxygen trapped inside the jar. Without sufficient oxygen, the combustion process cannot continue, and the flame extinguishes.
Additionally, the combustion process produces carbon dioxide and water vapor as byproducts. These byproducts can accumulate within the closed jar, further contributing to the depletion of oxygen and ultimately causing the flame to go out.
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One method for the manufacture of "synthesis gas" (a mixture of CO and H₂) is th catalytic reforming of CH4 with steam at high temperature and atmospheric pressure CH4(g) + H₂O(g) → CO(g) + 3H₂(g) The only other reaction considered here is the water-gas-shift reaction: CO(g) + H₂O(g) → CO₂(g) + H₂(g) Reactants are supplied in the ratio 2 mol steam to 1 mol CH4, and heat is added to th reactor to bring the products to a temperature of 1300 K. The CH4 is completely con verted, and the product stream contains 17.4 mol-% CO. Assuming the reactants to b preheated to 600 K, calculate the heat requirement for the reactor
The heat demand of the reactor is:Q = 112.79 kJ + 206.0 kJQ = 318.79 kJ or 319 kJ (rounded off to the nearest integer).Therefore, the heat demand of the reactor is 319 kJ.
Synthesis gas is formed from the catalytic reforming of methane gas with steam at high temperatures and atmospheric pressure. The reaction produces a mixture of CO and H2, as follows: CH4(g) + H2O(g) → CO(g) + 3H2(g)Additionally, the water-gas shift reaction is the only other reaction considered in this process. The reaction proceeds as follows: CO(g) + H2O(g) → CO2(g) + H2(g). The reactants are supplied in the ratio of 2 mol of steam to 1 mol of CH4. Heat is added to the reactor to raise the temperature of the products to 1300 K, with the CH4 being entirely converted. The product stream contains 17.4 mol-% CO. Calculate the heat demand of the reactor, assuming that the reactants are preheated to 600 K.Methane (CH4) reacts with steam (H2O) to form carbon monoxide (CO) and hydrogen (H2).
According to the balanced equation, one mole of CH4 reacts with two moles of H2O to produce one mole of CO and three moles of H2.To calculate the heat demand of the reactor, the reaction enthalpy must first be calculated. The enthalpy of reaction for CH4(g) + 2H2O(g) → CO(g) + 3H2(g) is ΔHrxn = 206.0 kJ/mol. The reaction enthalpy can be expressed in terms of ΔH°f as follows:ΔHrxn = ∑ΔH°f(products) - ∑ΔH°f(reactants)Reactants are preheated to 600 K.
The heat requirement for preheating the reactants must be calculated first. Q = mcΔT is the formula for heat transfer, where Q is the heat transferred, m is the mass of the substance, c is the specific heat of the substance, and ΔT is the temperature difference. The heat required to preheat the reactants can be calculated as follows:Q = (1 mol CH4 × 16.04 g/mol × 600 K + 2 mol H2O × 18.02 g/mol × 600 K) × 4.18 J/(g·K)Q = 112792.8 J or 112.79 kJThe reaction produces 1 mole of CO and 3 moles of H2.
Thus, the mol fraction of CO in the product stream is (1 mol)/(1 mol + 3 mol) = 0.25. But, according to the problem, the product stream contains 17.4 mol-% CO. This implies that the total number of moles in the product stream is 100/17.4 ≈ 5.75 moles. Thus, the mole fraction of CO in the product stream is (0.174 × 5.75) / 1 = 1.00 mol of CO. Thus, the amount of CO produced is 1 mol.According to the enthalpy calculation given above, the enthalpy of reaction is 206.0 kJ/mol. Thus, the heat produced in the reaction is 206.0 kJ/mol of CH4. But, only 1 mol of CH4 is consumed. Thus, the amount of heat produced in the reaction is 206.0 kJ/mol of CH4.The heat demand of the reactor is equal to the heat required to preheat the reactants plus the heat produced in the reaction.
Therefore, the heat demand of the reactor is:Q = 112.79 kJ + 206.0 kJQ = 318.79 kJ or 319 kJ (rounded off to the nearest integer).Therefore, the heat demand of the reactor is 319 kJ.
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The safety hierarchy is essential for every plant and engineered device. In the BPCS (basic process control system) layer for highly exothermic reaction, we better be sure that temperature T stays within allowed range. The measure we protect against an error in the temperature sensor (reading too low) causing a dangerously high temperature could be ___________________________________________________. The failure position of a control valve is selected to yield the safest condition in the process, so for the reactor with exothermic reaction we should select "fail open" valve, as shown in following figure, by considering the reason that ________________________________________________________.
In the SIS (safety interlock system to stop/start equipment), the reason why we do not use the same sensor that used in BPCS is that _____________________________________________________. In relief system, the goal is usually to achieve reasonable pressure (prevent high pressure or prevent low pressure), the capacity should be for the "worst case" scenario, the action is automatic (it does not require a person), and it is entirely self-contained (no external power required), in which the reason why it needs not electricity is that _______________________________________________.
In the BPCS (basic process control system) layer for a highly exothermic reaction, we better be sure that the temperature T stays within the allowed range. The measure we protect against an error in the temperature sensor (reading too low) causing a dangerously high temperature could be to install a second temperature sensor that can detect any erroneous reading from the first sensor. This will alert the BPCS system and result in appropriate actions. The failure position of a control valve is selected to yield the safest condition in the process, so for the reactor with exothermic reaction, we should select "fail-open" valve, which will open the valve during a failure, to prevent the reaction from building pressure. This will avoid any catastrophic situation such as a sudden explosion.
In the SIS (safety interlock system to stop/start equipment), the reason why we do not use the same sensor that is used in BPCS is that if there is an issue with the primary sensor, then the secondary sensor, which is in SIS, will not give the same reading as the primary. This will activate the SIS system and result in appropriate action to maintain the safety of the process. In relief system, the goal is usually to achieve reasonable pressure (prevent high pressure or prevent low pressure). The capacity should be for the "worst-case" scenario, the action is automatic (it does not require a person), and it is entirely self-contained (no external power required).
The reason why it needs no electricity is that in case of an emergency like a power cut, the relief valve still must function. Therefore, it has to be self-contained to operate in the absence of any external power.
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