The given temperature of ethanol is 28 °C, and its boiling point is 78 °C. Thus, the temperature given is less than its boiling point, which means that the ethanol is in the liquid state, not in the gaseous state. The answer is option B. 0.111atm.
This means that the vapor pressure is the saturated vapor pressure of ethanol at 28 °C. The Clausius-Clapeyron equation is used to calculate the saturated vapor pressure. The equation is given as:
log P2/P1 = ΔHvap/R × (1/T1 - 1/T2)
where ΔHvap is the heat of vaporization, R is the gas constant, T1 is the boiling point of the liquid, T2 is the temperature for which the saturated vapor pressure is to be calculated, P1 is the vapor pressure at T1, and P2 is the vapor pressure at T2.The values are given as follows:
ΔHvap = 38.6 kJ/molR
= 8.314 J/mol.
KT1 = 78 °C + 273.15
= 351.15 K (boiling point of ethanol)
T2 = 28 °C + 273.15
= 301.15 K (temperature given)
P1 = atmospheric pressure (because the boiling point of ethanol is above the atmospheric pressure)P2 = ?log P2/atm atmospheric pressure/atm = 0.111atmapproximately.So, the answer is option B. 0.111atm.
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Need answers asp please
Answer:
B, [tex]2x + 3 - \frac{4}{x}[/tex]
Step-by-step explanation:
Our given expression is [tex]\frac{6x^2 + 9x - 12}{3x}[/tex]
In order to solve this expression, you need to distribute the 3x by dividing each individual term in the trinomial by it.
That should look like this:
[tex]\frac{6x^{2}}{3x} = 2x[/tex]
[tex]\frac{9x}{3x} = 3[/tex]
[tex]\frac{-12}{3x} = \frac{-4}{x}[/tex]
Once you have divided each term by 3x, simply move the negative sign in front of the [tex]\frac{4}{x}[/tex] term and put them all together for:
B, [tex]2x + 3 - \frac{4}{x}[/tex]
Use the Laplace transform to solve the given initial value problem. y" - 4y - 60y = 0; y(0) = 12, y'(0) = 24 y(t)
Using the Laplace transform, the solution to the given initial value problem y" - 4y - 60y = 0; y(0) = 12, y'(0) = 24 y(t) is "y(t) = 6e^(8t) + 6e^(-8t)."
To use the Laplace transform to solve the given initial value problem, we need to follow these steps:
1. Apply the Laplace transform to both sides of the equation. Recall that the Laplace transform of the derivative of a function is given by sF(s) - f(0), where F(s) is the Laplace transform of f(t). Similarly, the Laplace transform of the second derivative is s^2F(s) - sf(0) - f'(0).
Taking the Laplace transform of the given equation, we have:
s^2Y(s) - sy(0) - y'(0) - 4Y(s) - 60Y(s) = 0
Substituting the initial values y(0) = 12 and y'(0) = 24, we get:
s^2Y(s) - 12s - 24 - 4Y(s) - 60Y(s) = 0
2. Combine like terms and rearrange the equation to solve for Y(s):
(s^2 - 4 - 60)Y(s) = 12s + 24
Simplifying further, we have:
(s^2 - 64)Y(s) = 12s + 24
3. Solve for Y(s) by dividing both sides of the equation by (s^2 - 64):
Y(s) = (12s + 24) / (s^2 - 64)
4. Decompose the right side of the equation into partial fractions. Factor the denominator (s^2 - 64) as (s - 8)(s + 8):
Y(s) = (12s + 24) / ((s - 8)(s + 8))
Using partial fractions decomposition, we can write Y(s) as:
Y(s) = A / (s - 8) + B / (s + 8)
where A and B are constants to be determined.
5. Solve for A and B by equating numerators:
12s + 24 = A(s + 8) + B(s - 8)
Expanding and rearranging the equation, we get:
12s + 24 = (A + B)s + (8A - 8B)
Comparing the coefficients of s on both sides, we have:
12 = A + B (equation 1)
0 = 8A - 8B (equation 2)
From equation 2, we can simplify it to:
A = B
Substituting this result into equation 1, we get:
12 = 2A
Therefore, A = 6 and B = 6.
6. Substitute the values of A and B back into the partial fractions decomposition:
Y(s) = 6 / (s - 8) + 6 / (s + 8)
7. Take the inverse Laplace transform of Y(s) to find the solution y(t):
y(t) = 6e^(8t) + 6e^(-8t)
Therefore, the solution to the given initial value problem y" - 4y - 60y = 0; y(0) = 12, y'(0) = 24 y(t) is:
y(t) = 6e^(8t) + 6e^(-8t)
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Discuss the sterilization method currently used for metal alloys.
The sterilization method currently used for metal alloys is typically heat sterilization. This method involves subjecting the metal alloys to high temperatures for a specified period of time to effectively kill or inactivate any microorganisms present on the surface of the alloys.
Here is a step-by-step explanation of the heat sterilization process for metal alloys:
1. Cleaning: Before sterilization, the metal alloys must be thoroughly cleaned to remove any dirt, grease, or contaminants that may be present on the surface. This can be done using detergents, solvents, or ultrasonic cleaning.
2. Packaging: The cleaned metal alloys are then packaged in a manner that allows for effective heat penetration during the sterilization process. This may involve using sterile pouches, wraps, or containers made of materials that can withstand high temperatures.
3. Heat sterilization: The packaged metal alloys are subjected to high temperatures using various methods, such as dry heat or moist heat sterilization.
- Dry heat sterilization: In this method, the metal alloys are exposed to hot air at temperatures ranging from 160 to 180 degrees Celsius for a period of time. This helps to denature and kill any microorganisms present on the surface of the alloys.
- Moist heat sterilization: This method involves the use of steam under pressure. The metal alloys are placed in a sterilization chamber, and steam is generated to create a high-pressure, high-temperature environment. The most commonly used moist heat sterilization method is autoclaving, which typically involves subjecting the metal alloys to temperatures of 121 degrees Celsius and pressure of around 15 psi (pounds per square inch) for a specified duration of time. The combination of heat and pressure effectively kills bacteria, fungi, and viruses present on the metal alloys.
4. Cooling and storage: After the heat sterilization process, the metal alloys are allowed to cool before they are stored or used. It is important to handle the sterilized alloys with clean, sterile gloves or instruments to prevent recontamination.
It is worth noting that the exact sterilization method used for metal alloys may vary depending on the specific application and requirements. Other sterilization methods, such as chemical sterilization or radiation sterilization, may also be used in certain cases. However, heat sterilization remains one of the most commonly employed methods for ensuring the sterility of metal alloys.
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How to lay a pipeline to a new pond which would be situated near to the main highway alongside the existing ore transporter belt which would provide a much more secure access to the water needed for treatment.
A pipeline to a new pond near the main highway alongside the existing ore transporter belt, providing secure access to water for treatment.
You can follow these general steps:
Planning and Design:
Determine the location and size of the new pond, considering factors such as water availability, treatment requirements, and proximity to the main highway and existing transporter belt.
Obtain Necessary Permits and Approvals:
Identify the regulatory bodies or local authorities responsible for granting permits for pipeline construction and obtain the necessary approvals.
Ensure compliance with environmental regulations and any specific requirements related to the proximity of the highway and transporter belt.
Procurement and Logistics:
Procure the required materials, including pipes, fittings, valves, and other necessary equipment for pipeline construction.
Arrange for transportation and logistics to deliver the materials to the construction site.
Construction:
Prepare the construction site by clearing any vegetation or debris along the pipeline route.
Excavate trenches along the planned pipeline route, ensuring the depth and width are appropriate for the pipe size and soil conditions.
Connection and Integration:
Establish the necessary connections between the pipeline and the new pond, ensuring proper fittings and valves are in place.
Integrate the pipeline system with the water treatment infrastructure, including pumps, filters, and any other necessary components.
Testing and Commissioning:
Conduct thorough testing of the pipeline system to ensure its functionality, including flow tests and pressure tests.
Address any identified issues or leaks and rectify them before commissioning the pipeline.
Remember, the specific details and requirements of pipeline construction may vary depending on factors such as local regulations, terrain conditions, and project scope. It is recommended to consult with experienced professionals, engineers, or contractors specializing in pipeline construction to ensure a successful and compliant installation.
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Benzoic Acid l bu Naphthalene 1.35 g 2.65 g 3. Like dissolves like is an important term in liquid-liquid extraction. Draw the structure of 3 compounds, 2 that will likely be miscible and 1 that will be immiscible.
Liquid-liquid extraction relies on the principle of "like dissolves like," indicating that compounds with similar polarities or solubilities are miscible, while those with different polarities or solubilities are immiscible. Three compounds, benzoic acid, naphthalene, and benzoic acid, are examples of compounds with different polarities or solubilities.
In liquid-liquid extraction, the principle of "like dissolves like" is important. This means that compounds with similar polarities or solubilities are likely to be miscible (able to dissolve in each other), while compounds with different polarities or solubilities are likely to be immiscible (not able to dissolve in each other).
Now, let's draw the structures of three compounds:
1. Benzoic Acid (C6H5COOH):
- Structure:
H-C6H5COOH (benzoic acid consists of a benzene ring attached to a carboxylic acid group)
2. Naphthalene (C10H8):
- Structure:
C10H8 (naphthalene consists of two benzene rings fused together)
3. Compound likely to be miscible with benzoic acid:
- Structure:
H-C6H5COOR (R represents a group that can increase the polarity or solubility of the compound, such as an alcohol group)
4. Compound likely to be miscible with naphthalene:
- Structure: C10H8-COOH (a carboxylic acid group attached to naphthalene)
5. Compound likely to be immiscible with both benzoic acid and naphthalene:
- Structure: C6H5CH3 (a methyl group attached to a benzene ring)
I hope this helps! Let me know if you have any more questions.
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The table shows the approximate height of an object x seconds after the object was dropped. The function h(x) = –16x2 + 100 models the data in the table.
A 2-column table with 5 rows. The first column is labeled time (seconds) with entries 0, 0.5, 1, 1.5, 2. The second column is labeled height (feet) with entries 100, 96, 84, 65, 37.
For which value of x would this model make the least sense to use?
–2.75
0.25
1.75
2.25
The value for which the model makes the least sense to use is D) 2.25. Option D
To determine for which value of x the model would make the least sense to use, we need to compare the predicted heights from the model with the actual heights provided in the table.
Given the function h(x) = -[tex]16x^2 + 100[/tex], we can calculate the predicted heights for each value of x in the table and compare them with the corresponding actual heights.
Let's calculate the predicted heights using the model:
For x = 0, h(0) [tex]= -16(0)^2 + 100 = 100[/tex]
For x = 0.5, h(0.5) =[tex]-16(0.5)^2 + 100 = 96[/tex]
For x = 1, h(1) =[tex]-16(1)^2 + 100 = 84[/tex]
For x = 1.5, h(1.5) = [tex]-16(1.5)^2 + 100 = 65[/tex]
For x = 2, h(2) [tex]= -16(2)^2 + 100 = 36[/tex]
Comparing these predicted heights with the actual heights given in the table, we can see that there is a significant discrepancy for x = 2. The predicted height from the model is 36, while the actual height provided in the table is 37. This indicates that the model does not accurately represent the data for this particular value of x.
Therefore, the value for which the model makes the least sense to use is D) 2.25. This value is not present in the table, but it is closer to x = 2, where the model shows a significant deviation from the actual height.
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Lists the ordinates of - run off hydrograph shown in the table. below which were in response to a rainfall 20.9mm during the first two hours, 41.9mm in the next two hours, and 30.9mm during the last two hours of the rainfall which lasted for six hours. Catchment area is 133.1 km^2. Assume a constant 5 m^3/sec constant base flow, find - Index. Time(hr.) 0 2 4 6 8 10 12 14 16 18 Q(m³/sec) 0 171 313 522 297 133 51 5 5 5 ≈1.42 mm/hr O ≈1.76 mm/hr ≈ 2.04 mm/hr O ≈2.13 mm/hr 10 points
To calculate the ordinates of the runoff hydrograph, we need to subtract the base flow from the total flow values given in the table.
Catchment area = 133.1 km²
Base flow = 5 m³/sec
To find the runoff values, we subtract the base flow from the corresponding flow values:
Time(hr.) Q(m³/sec) Runoff (Q - Base flow)
0 0 0
2 171 166
4 313 308
6 522 517
8 297 292
10 133 128
12 51 46
14 5 0
16 5 0
18 5 0
The runoff hydrograph ordinates, obtained by subtracting the base flow from the total flow values, are as follows:
0, 166, 308, 517, 292, 128, 46, 0, 0, 0
Now, let's calculate the intensity index:
Intensity Index = Total Rainfall (mm) / Duration of Rainfall (hr)
Total Rainfall = 20.9 + 41.9 + 30.9 = 93.7 mm
Duration of Rainfall = 6 hours
Intensity Index = 93.7 mm / 6 hours
Intensity Index ≈ 15.62 mm/hr
Therefore, the intensity index for the given rainfall is approximately 15.62 mm/hr.
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At 25 °C, what is the hydroxide ion concentration. [OH^], in an aqueous solution with a hydrogen ion concentration of [H"]=4.0 x 10-6 M2 [OH-] =
The hydroxide ion concentration in the aqueous solution is 2.5 x 10^-9 M. This can be determined using the ion product constant of water (Kw = 1.0 x 10^-14) at 25°C, where [H+][OH-] = Kw. Given [H+] =4.0 x 10^-6 M, we can calculate [OH-] as [OH-] = Kw / [H+] = (1.0 x 10^-14) / (4.0 x 10^-6) = 2.5 x 10^-9 M.
Explanation:
To find the hydroxide ion concentration in the given solution, we utilize the relationship between the hydrogen ion concentration, [H+], and the hydroxide ion concentration, [OH-]. This relationship is defined by the ion product of water, Kw, which is the product of [H+] and [OH-]. At 25 °C, the value of Kw is 1.0 x 10^-14. By substituting the given hydrogen ion concentration into the equation, we can solve for [OH-]. Dividing both sides of the equation by the hydrogen ion concentration allows us to isolate [OH-] and determine its value. The resulting hydroxide ion concentration is 2.5 x 10^-9 M.
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1136 liters per minute of water circulate through a pipe at 20
°C with a friction head loss of 14 m. What power is needed to
maintain this flow? (a) 0.16 kW; (b) 1.88 kW; (c) 2.54 kW; (d) 3.41
kW; (e
In the given options, the closest choice is (c) 2.54 kW.
To calculate the power needed to maintain the given flow rate and overcome the friction head loss, we can use the formula:
Power (P) = (Flow Rate * Head Loss * Density * Gravity) / 1000
Flow Rate = 1136 liters per minute = 18.9333 liters per second (since 1 liter per second is equal to 60 liters per minute)
Head Loss = 14 m
Density of water at 20°C ≈ 998 kg/m³ (assuming standard density)
Gravity (g) = 9.81 m/s²
Substituting the values into the formula, we can calculate the power:
P = (18.9333 l/s * 14 m * 998 kg/m³ * 9.81 m/s²) / 1000
P ≈ 2.6462 kW
Therefore, the power needed to maintain this flow is approximately 2.6462 kW.
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Solve the following inequality by first factoring the polynomial then making a graph or a table. ( 2x ^3−x ^2−5x−2>0
Therefore, the inequality is satisfied in the intervals (–∞, –1.089) and (0.756, +∞), orx ∈ (–∞, –1.089) U (0.756, +∞).
Given: The inequality is 2x³ - x² - 5x - 2 > 0.
The polynomial is 2x³ - x² - 5x - 2.
It's required to solve the inequality using first factoring the polynomial then making a graph or a table.
Step-by-step explanation:
First, let's factor the polynomial:
2x³ - x² - 5x - 2
= 0 ⇒ x²(2x - 1) - (5x + 2)
= 0
Since it is not easy to calculate the roots of a cubic equation in general, we can do the following:
Lets analyze the function f(x) = 2x³ - x² - 5x - 2.
We need to find the critical points of the function f(x) in order to determine its sign chart and find where f(x) is greater than zero (or less than zero).For this, we need to find the values of x that make f'(x) = 0:
f'(x) = 6x² - 2x - 5
= 0 ⇒ x
= (-(-2) ± √((-2)² - 4(6)(-5))) / (2·6) ≈ -1.089 or x ≈ 0.756.
Both critical points divide the x-axis into three intervals: (–∞, –1.089), (–1.089, 0.756), and (0.756, +∞).
Then, we need to calculate the sign of f'(x) and the sign of f(x) for each interval:
The table below summarizes the results:
f'(x)f(x)(–∞, –1.089)–––––(–1.089, 0.756)+––+(0.756, +∞)–+–+
Therefore, the inequality is satisfied in the intervals (–∞, –1.089) and (0.756, +∞), orx ∈ (–∞, –1.089) U (0.756, +∞).
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Question 8 In a road section, when the traffic flow is 1400 vehicles/h, the average speed is 20 km/h and when the flow is 1300 vehicles/h, the average speed increases to 35 km/h. If the relationship between u-k is linear, a) estimate the traffic density for both flow conditions b) estimate the maximum flow that the road section can bear c) estimate the average speed of the vehicle when the maximum flow is reached
The required estimates are:
k1 = 70 vehicles/km and
k2 = 37.14 vehicles/km
The maximum flow that the road section can bear is 1200 vehicles/h.
The average speed of the vehicle when the maximum flow is reached is 19.2 km/h.
Given data: Traffic flow when u=1400 vehicles/h
Average speed when u=20 km/h
Traffic flow when u=1300 vehicles/h
Average speed when u=35 km/h
The relationship between u and k is linear.
a) Traffic density (k) for both flow conditions: Formula to calculate traffic density is k = u/v
where, k = traffic density
u = traffic flow
v = speed of the vehicle
Case 1: Traffic flow when u=1400 vehicles/h and average speed is 20 km/h
Average speed, v1 = 20 km/h
k1 = u/v1
= 1400/20
= 70 vehicles/km
Case 2: Traffic flow when u=1300 vehicles/h and average speed is 35 km/h
Average speed, v2 = 35 km/h
k2 = u/v2
= 1300/35
= 37.14 vehicles/km
Therefore, the traffic density for both flow conditions are:
k1 = 70 vehicles/km
and k2 = 37.14 vehicles/km
b) Maximum flow that the road section can bear: The maximum flow is obtained from the graph of u and k.
Maximum flow that the road section can bear is the point of intersection of two straight lines
u = 1400 and
u = 1300.
The maximum flow is 1200 vehicles/h. The corresponding traffic density k at maximum flow is:
k = (1400+1300)/((20+35)/2)
= 62.5 vehicles/km
c) Average speed of the vehicle when the maximum flow is reached:
The average speed of the vehicle can be obtained using the formula,
v = u/k
where, v = speed of the vehicle
u = traffic flow
k = traffic density
Therefore, the average speed of the vehicle when the maximum flow is reached is
v = 1200/62.5
= 19.2 km/h
Hence, the required estimates are:
k1 = 70 vehicles/km and
k2 = 37.14 vehicles/km
The maximum flow that the road section can bear is 1200 vehicles/h.
The average speed of the vehicle when the maximum flow is reached is 19.2 km/h.
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help me pleaseeee huryyy!!!
Answer: 235.5 ft³
Step-by-step explanation:
We are given the formula to use for this equation. We will substitute the given values and solve. However, first we must find the base.
Area of a circle:
A = πr²
Substitute given values (r, the radius, is equal to half the diameter)
A = (3.14)(2.5)²
Compute:
A = 19.625 ft²
Given formula for volume:
V = Bh
Substitute known values:
V = (19.625 ft²)(12 ft)
V = 235.5 ft³
Plsss help
A team of researchers is testing the hypothesis that taking a break every hour to do 1 minute of
physical activity can reduce stress. They randomized 100 full-time employees between a
treatment group and a control group. The treatment group was instructed to take a 1-minute
break every hour at work to do some sort of physical activity. At the beginning and end of the
study, each participant took the Psychological Strain Questionnaire (PSQ), which measures
stress at work. The higher the PSQ score, the less stress the employee feels.
Researchers found that the change in PSQ scores for the treatment group was 10 points higher
than the change in PSQ scores for the control group. To test whether the results could be
explained by random chance, the researchers performed a simulation analysis. The summary of
2000 re-randomizations of their data is recorded below.
Mean Standard Deviation
0
5.204
What is a good estimate for the expected margin of error for the simulation results?
05.2
A) 5.2
B) 7.8
C)10.4
D)13.0
My answer is 5.2.30am I am not Paris Paris I'm thankful to 6.30am I am not
The maximum number of grams of fat (F) that should be in a diet varies directly as a person's weight (W). A person weighing 114lb should have no more than 76 g of fat per day. What is the maximum daily fat intake for a person weighing 102lb ? The maximum daily fat intake is 2.
The maximum daily fat intake for a person weighing 102lb is 68 g of fat.
Given the following data:
The maximum number of grams of fat (F) that should be in a diet varies directly as a person's weight (W).A person weighing 114lb should have no more than 76 g of fat per day.
To find: The maximum daily fat intake for a person weighing 102lb.
Let "F" be the maximum number of grams of fat that a person can consume daily.
Let "W" be the weight of the person in pounds. Then we have:F ∝ W (The maximum number of grams of fat (F) that should be in a diet varies directly as a person's weight (W)).
So we can write:F = kW ------------ (1),
Where "k" is a constant of proportionality.To find the value of "k" we can use the given data.A person weighing 114lb should have no more than 76 g of fat per day.So when W = 114, F = 76.
Using equation (1), we get:76 = k(114)k = 76/114k = 2/3.Now we have:k = 2/3 (constant of proportionality).
We can use equation (1) to find the maximum daily fat intake for a person weighing 102lb.F = kW = (2/3)(102) = 68.
So the maximum daily fat intake for a person weighing 102lb is 68 g of fat.
For a person weighing 102lb, the maximum daily fat intake is 68 g of fat.
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How do we define a strong acid/base and a weak acid/base? What does this tell us about the x is small approximation?
Strong acids and bases
Strong acids are those that dissociate completely in water, and as a result, the H+ ion concentration is very high. In the same way, strong bases can absorb protons easily and produce a high concentration of hydroxide ions when dissolved in water.
Weak acids and bases
Weak acids, on the other hand, only partially dissociate in water, indicating that their H+ ion concentration is lower than that of a strong acid. Weak bases, on the other hand, do not fully absorb protons in the same way that strong bases do, resulting in lower OH- ion concentrations.
The approximation is used when the concentration of an ion is very low and can be neglected in comparison to other elements. This approximation is used in weak acid and base chemistry since, if the concentration of H+ or OH- ions is small, the ion product can be ignored, allowing for easier calculations. When the dissociation constant (Ka or Kb) is very low, the approximation is used as well.
The approximation is used in weak acid and base chemistry since, if the concentration of H+ or OH- ions is small, the ion product can be ignored, allowing for easier calculations. When the dissociation constant (Ka or Kb) is very low, the approximation is used as well.
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Water (cp= 4182 JKK) at a flow rate of 4000 Kg/hr is heated from 1 5°C to 40°C in an oil cooler by engine oil (cp= 2072 JKK) with an inlet temperature of 80°C and a flow rate of 6000 Kg/hr. Take the overall heat transfer coefficient to be 3500 W/m²K. What are the areas required for: a. Parallel Flow. b. Counter Flow.
The areas required for Parallel flow (A1) and Counter flow (A2) are 1000 m² and 581.4 m² (approx) respectively.
Given data: Mass flow rate of water = 4000 Kg/hr, cp of water (cw) = 4182 J/kg-K
Initial temperature of water (tw1) = 15 °C
Final temperature of water (tw2) = 40 °C
Mass flow rate of engine oil = 6000 Kg/hr, cp of engine oil (ce) = 2072 J/kg-K
Inlet temperature of engine oil (te1) = 80 °C
Overall heat transfer coefficient (U) = 3500 W/m²-K
We are required to find the areas required for Parallel flow (A1) and Counter flow (A2).
The rate of heat transfer can be given as:
q = m1×cp1×(t1-t2)
q = m2×cp2×(t2-t1)
where, m1 = Mass flow rate of water, cp1 = Specific heat of water, t1 = Initial temperature of water, t2 = Final temperature of water.
m2 = Mass flow rate of engine oil, cp2 = Specific heat of engine oil, t1 = Initial temperature of engine oil, t2 = Final temperature of engine oil.
Substituting the values of the given data, we get q = 4000×4182×(40-15)
q = 251280000 Joules/hour and
q = 6000×2072×(15-80)
q = -186240000 Joules/hour
Total rate of heat transfer can be calculated as:
q = m1×cp1×(t1-t2) = - m2×cp2×(t2-t1)
q = 251280000 + 186240000
q = 437520000 Joules/hour
Let's find the areas required for both Parallel flow and Counter flow.
For Parallel flow, Total heat transfer area can be calculated as:
A1 = q/(U×(t2-te1))
Substituting the given data in the above equation, we get
A1 = 437520000/(3500×(40-80))
A1 = 1000 m²2.
For Counter flow, Total heat transfer area can be calculated as:
A2 = (q/[(t2-te2)/ln(t2-te2/t1-te1)]) / U
where, te2 = t1
Substituting the given data in the above equation, we get
A2 = (437520000/[(40-80)/ln((40-80)/(15-80))]) / 3500
A2 = 581.4 m² (approx)
Therefore, the areas required for Parallel flow (A1) and Counter flow (A2) are 1000 m² and 581.4 m² (approx) respectively.
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Fill the blanks with suitable words or phrases? 1- The time that elapses from the start of the green indication to the end of the red indication for the same phase of a signalized intersection is called - -----------, while any part of the cycle length during which signal indications do not change is called an
The time that elapses from the start of the green indication to the end of the red indication for the same phase of a signalized intersection is called the phase length, while any part of the cycle length during which signal indications do not change is called an interval.
There are four kinds of intervals that constitute a complete traffic signal cycle: phase interval, clearance interval, all-red interval, and pedestrian interval.
The duration of each signal interval is referred to as its time length.
The effective capacity of signalized intersections, according to HCM 2000, is a function of cycle length. Long cycle lengths (more than 120 seconds) result in reduced capacity.
As a result, cycle length should be kept as short as feasible in order to maximize capacity.
Short cycle lengths, on the other hand, reduce the capacity of a signalized intersection since there is less time for each phase to service traffic.
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Similar triangles. Tripp helps set up a new tent next to an old tent. The rope from the tent poles to be stakes forms similar triangles. How tall is the pole of the new tent. One side is 15, the base is 20, the long side is blank. The second triangle long side is 20, the base is a question mark and the other side is a question mark. Help
The length of the base of the second triangle is also 15.
To determine the length of the long side of the new tent pole, we can use the concept of similar triangles.
Since the triangles formed by the ropes of the old and new tents are similar, their corresponding sides are proportional.
Let's denote the length of the long side of the new tent as x. According to the given information, we have the following ratios:
15/20 = x/20
By cross-multiplication, we can solve for x:
15 x 20 = 20 [tex]\times[/tex] x
300 = 20x
x = 300/20
x = 15
Therefore, the length of the long side of the new tent pole is 15.
In the second triangle, where the long side is 20 and the base is unknown, we can use the same principle.
Let's denote the length of the base as y. The ratio of the corresponding sides is:
20/y = 15/20
By cross-multiplication, we can solve for y:
20 x 15 = 20 x y
300 = 20y
y = 300/20
y = 15
So, the length of the base of the second triangle is also 15.
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A 4ft hollow cylinder fixed at one end is subjected to a Load 1500lb at the other end perpendicular to the longitudinal axis with inner and outer diameter equal to 3.2in and 4.0in respectively. Determine the maximum shear stress (psi) in the cylinder.
The maximum shear stress in the cylinder is 22500 psi.
The maximum shear stress in the cylinder can be determined using the formula:
τ = (3 * F * r) / (2 * t^2)
Where:
- τ is the maximum shear stress in psi,
- F is the applied load in lb (1500 lb in this case),
- r is the radius of the cylinder in inches ((4.0 in - 3.2 in) / 2 = 0.4 in),
- t is the wall thickness of the cylinder in inches (0.4 in - 0.2 in = 0.2 in).
Now let's plug in the values into the formula:
τ = (3 * 1500 lb * 0.4 in) / (2 * (0.2 in)^2)
Simplifying the equation:
τ = 1800 lb * in^2 / (0.08 in^2)
τ = 22500 psi
Therefore, the maximum shear stress in the cylinder is 22500 psi.
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Create your own example of integers using bedmas
The volume of a cone is 763.02 cubic inches. The radius and height of the cone are equal. What is the radius of the cone? Use 3.14 for π.
The radius of the cone is approximately 9.1 inches.
To find the radius of the cone, we can use the formula for the volume of a cone, which is given by V = (1/3) * π * r^2 * h, where V is the volume, π is approximately 3.14, r is the radius, and h is the height.
In this case, we are given that the volume of the cone is 763.02 cubic inches and the radius and height are equal. Let's denote the radius and height as r and h, respectively.
So, we have the equation 763.02 = (1/3) * 3.14 * r^2 * h.
Since the radius and height are equal, we can simplify the equation to 763.02 = (1/3) * 3.14 * r^2 * r.
Simplifying further, we get 763.02 = (1/3) * 3.14 * r^3.
Multiplying both sides by 3, we have 2289.06 = 3.14 * r^3.
Dividing both sides by 3.14, we get approximately 728.24 = r^3.
Taking the cube root of both sides, we find that r ≈ 9.1 inches.
Therefore, the radius of the cone is approximately 9.1 inches.
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What are the constraints (conditions) of RAOULT’s law?
The Raoult's law is a principle that governs the distribution of volatile substances between liquid and vapour states in a mixture.
It describes the relationship between the vapour pressure of the mixture and the mole fractions of the components in the liquid phase. However, this law has certain constraints or conditions that are as follows: The components must have similar molecular sizes and shapes, and the intermolecular interactions between the components must be identical in both the liquid and vapour phases.
In a mixture, the components must be non-reactive and the interaction between them must be ideal. This means that they should obey the ideal gas law, and their molecules should not experience any intermolecular forces such as hydrogen bonding, dipole-dipole interaction, or van der Waals forces.
This law applies only to dilute solutions that contain a small amount of solute relative to the solvent. The temperature must be constant while the pressure is variable.
Raoult's law provides a valuable tool for determining the properties of mixtures. However, it has certain constraints that must be met to obtain accurate results. The most important condition is that the components must be non-reactive and the interaction between them must be ideal. This means that the components should obey the ideal gas law, and their molecules should not experience any intermolecular forces. If the intermolecular forces are present, then the actual vapour pressure of the mixture will be lower than predicted by Raoult's law.
The deviations from the ideal behaviour can be quantified using the activity coefficient. Another constraint is that the components must have similar molecular sizes and shapes, and the intermolecular interactions between the components must be identical in both the liquid and vapour phases. This is because Raoult's law is based on the assumption that the solute molecules behave like the solvent molecules.
If the molecular sizes and shapes are significantly different, then the solute molecules will not behave like the solvent molecules. Lastly, this law applies only to dilute solutions that contain a small amount of solute relative to the solvent. This is because the assumption of ideal behaviour becomes less accurate as the concentration of solute increases.
Therefore, Raoult's law has certain constraints or conditions that must be met to obtain accurate results. These include non-reactive components, identical intermolecular interactions, similar molecular sizes and shapes, ideal behaviour, constant temperature, and dilute solutions. Deviations from the ideal behaviour can be quantified using the activity coefficient.
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8. What must be the velocity of flow of the most efficient trapezoidal canal with side slopes. of 3/4:1 and to carry a discharge of 32.4 m/s on a grade of 1 m per km. Use n=0.013
The velocity of flow of the most efficient trapezoidal canal with side slopes of 3/4:1 and to carry a discharge of 32.4 m/s on a grade of 1 m per km is 2.406 m/s approximately.
Given the following,Velocity of flow of the most efficient trapezoidal canal = ?Side slopes = 3/4 : 1Discharge = 32.4 m/sGrade = 1 m/kmCoefficient of roughness, n = 0.013.
For the most efficient trapezoidal canal, critical depth, y_c = (2/5) * Hydraulic radius(R_h)----------------(1)Where, Hydraulic radius,
R_h = (A_p) / P_w,And, A_p = Area of the cross-sectionAnd, P_w = Wetted perimeter.
The area of the cross-section of the trapezoidal canal = (b + z*y_c) * y_c----------------(2),
Where, b = Width of the bottom of the canalAnd, z = Slopes of the canal sides (3/4 : 1)Therefore, b/z = 4/3 = 1.33.
The wetted perimeter, P_w = b + 2*y_c*(1 + z^2)^1/2-----------------(3).
From the discharge formula,Q = A_p * v = (b + z*y_c) * y_c * v -----------------(4),
Where, v is the velocity of flow of the fluidWe are required to find the velocity of flow, so using equation (4)We get,
v = Q / [(b + z*y_c) * y_c] -----------------(5).
Now we will substitute equations (1), (2), (3) and (5) in the Chezy's equation.Chezy's equation states that,v = (1/n) * [R_h^2 * g * S]^1/2.
Where, g = acceleration due to gravityAnd, S = Slope of the canal = 1 / 1000.
Therefore, substituting the values in Chezy's equation, we get,(Q / [(b + z*y_c) * y_c]) = (1/0.013) * [(R_h^2 * 9.81 * 0.001)]^1/2-----------------(6).
Substituting equation (1) in equation (6), we get,
(Q / [(b + z*y_c) * y_c]) = (1/0.013) * [((2/5) * (A_p / P_w))^2 * 9.81 * 0.001]^1/2-----------------(7).
Substituting equations (2) and (3) in equation (7), we get,
(Q / [(b + z*y_c) * y_c]) = (1/0.013) * [((2/5) * ((b + z*y_c) * y_c) / [b + 2*y_c*(1 + z^2)^1/2])^2 * 9.81 * 0.001]^1/2-----------------(8).
Substituting Q = 32.4 m^3/s in equation (8), we get the value of v as v = 2.406 m/s (approximately).
The velocity of flow of the most efficient trapezoidal canal is 2.406 m/s (approximately).
The canal section should be designed so that the perimeter is as small as possible, which reduces the frictional drag on the canal.
The velocity of flow in a trapezoidal canal should be such that it is sufficient to avoid silt deposits and stagnant water in the canal.A canal is said to be most efficient when its cross-sectional area is the smallest possible and its perimeter is the least possible.
Thus, the velocity of flow of the most efficient trapezoidal canal with side slopes of 3/4:1 and to carry a discharge of 32.4 m/s on a grade of 1 m per km is 2.406 m/s approximately.
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Find a power series solution of the differential equation given below. Determine the radius of convergence of the resulting series, and use the series given below to identify the series in terms of familiar elementary functions.
2(x-1)y' = 7y
(1)The power series solution is y(x) = _________ + .... (up to order of 3)
(2) The radius of convergence of the series is _____
(3) The series solution in terms of familiar elementary functions is y(x) = _________
The power series of a differential equation with y(x) as the sum of a power series that is,
[tex]y(x) = ∑_(n=0)^∞▒〖a_n(x-c)^n 〗[/tex]
The radius of convergence of the series is infinity.
The series solution in terms of familiar elementary functions is given by,[tex]y(x) = 3 x^(7/2)/(√14)[/tex]
This equation has the initial condition y(1) = 3.
Substituting the power series into the differential equation and solving for the coefficient of each power of (x - 1) provides a recursive formula that we can use to determine each coefficient of the power series representation.
2(x - 1)y' = 7y ⇒ y' = 7y/2(x - 1)
Taking the first derivative of the power series, we get,[tex]y'(x) = ∑_(n=1)^∞▒〖na_n(x-c)^(n-1) 〗[/tex]
Using this, the above differential equation becomes[tex],∑_(n=1)^∞▒〖na_n(x-c)^(n-1) 〗 = 7/2[/tex]
[tex]∑_(n=0)^∞▒a_n(x-c)^n〖- 7/2 ∑_(n=0)^∞▒a_n(x-c)^n〗⇒ ∑_(n=1)^∞▒〖na_n(x-c)^(n-1) 〗= ∑_(n=0)^∞▒〖(7/2 a_n - 7/2 a_(n-1)) (x-c)^n〗[/tex]
Since the two power series are equal, the coefficients of each power of (x - 1) must also be equal.
Therefore,[tex]∑_(k=0)^n▒〖k a_k (x-c)^(k-1) 〗= (7/2 a_n - 7/2 a_(n-1))[/tex]
The first few terms of the series for the power series solution y(x) is given by,
[tex]y(x) = 3 + 21/4 (x - 1) + 73/32 (x - 1)^2 + 301/384 (x - 1)^3,[/tex] to the order of 3.
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Determine the diameters of the pipes in the discharge line if Q design = 500 GPM (use the Darcy-Weisbach method). Determine the dimensions of the buffer tank. Also, calculate the power of the pump (Efficiency=70%, depth 80 feet); factor a calculated factor of safety into your pump TDH calculations. The pressure at the discharge point is 5 m. The friction factor for PVC is 0.016, and for steel it is 0.022.
The power of the pump is 60.48 horsepower (approximately) after factoring a calculated factor of safety into the pump TDH calculations.
Given,Q design = 500 GPM
Depth = 80 feet
Pressure at the discharge point = 5 m
Friction factor for PVC = 0.016
Friction factor for steel = 0.022
Efficiency = 70%
Let the diameters of the pipes in the discharge line be D1 and D2 respectively.The formula for pressure head is given by,
[tex]$$P=\frac{4fLQ^2}{2gD^5}$$[/tex]
Where,P = pressure
head f = friction
factor L = length
Q = flow rate
D = diameter
g = acceleration due to gravity
[tex]$$\implies D_1=\sqrt[5]{\frac{4fQL}{2gP}}$$[/tex]
[tex]$$\implies D_2=\sqrt[5]{\frac{4fQL}{2g(P-5)}}$$[/tex]
Substituting the given values in the above equations, we get;For PVC,
P = 5 m
and f = 0.016
[tex]$$\implies D_1=\sqrt[5]{\frac{4\times 0.016\times 100\times 500^2\times 3.28}{2\times 32.2\times 5}}$$[/tex]
[tex]$$\implies D_1=6.15$$[/tex]
For steel,P = 5 m
and f = 0.022
[tex]$$\implies D_2=\sqrt[5]{\frac{4\times 0.022\times 100\times 500^2\times 3.28}{2\times 32.2\times (5-5)}}$$[/tex]
[tex]$$\implies D_2=5.52$$[/tex]
Therefore, the diameters of the pipes in the discharge line for PVC and steel respectively are 6.15 and 5.52.The formula for volume of the buffer tank is given by,
[tex]$$V_{tank}=\frac{Q\times T}{1.44\times \Delta H}$$[/tex]
[tex]$$\implies V_{tank}=\frac{500\times 15}{1.44\times (80-5)}$$[/tex]
[tex]$$\implies V_{tank}=31.6 \space ft^3$$[/tex]
Therefore, the dimensions of the buffer tank are 31.6 cubic feet (assuming the height to be approximately equal to the diameter).The formula for power is given by,
[tex]$$P=\frac{Q\times H\times \gamma}{(3960\times E)}$$[/tex]
Where,P = power
Q = flow rate
H = head developed by the pump
[tex]$\gamma$[/tex] = unit weight of fluid
E = efficiency of the pump
[tex]$$\implies P=\frac{500\times 80\times 62.4}{(3960\times 0.7)}$$[/tex]
[tex]$$\implies P=60.48 \space hp$$[/tex]
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Discuss the factors accounted for by the modification factor K12 in the design of timber members.
In the design of timber members, the modification factor K12 is used to account for several factors, including the effect of shrinkage, swelling, and temperature changes on the strength of the timber member.
The modification factor K12 is used to adjust the strength of timber members for shrinkage, swelling, and temperature changes. The factors accounted for by this factor are as follows:
1. Shrinkage: Shrinkage is the decrease in the dimensions of timber that occurs as the moisture content decreases. The strength of timber members decreases with decreasing moisture content. The reduction in strength due to shrinkage can be accounted for by using the modification factor K12.
2. Swelling: Swelling is the increase in the dimensions of timber that occurs as the moisture content increases. The strength of timber members decreases with increasing moisture content. The reduction in strength due to swelling can be accounted for by using the modification factor K12.
3. Temperature Changes: The strength of timber members is affected by temperature changes. As temperature increases, the strength of timber members decreases. The reduction in strength due to temperature changes can be accounted for by using the modification factor K12.
4. Duration of Load: The duration of load affects the strength of timber members. A long-duration load reduces the strength of timber members more than a short-duration load. The reduction in strength due to the duration of load can be accounted for by using the modification factor K12.
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An electrolytic cell was run at a constant current of 2.10 A. The cell converted copper 2+ lons in solution to 4.10 g of solid copper at the cathode. The time needed to deposit the copper solid at the cathode was hr. Record your final answer to two decimal places (ie. 1.12) and do not include units in your final answer.
The time needed to deposit 4.10 g of solid copper at the cathode in an electrolytic cell running at a constant current of 2.10 A is approximately 3.14 hours.
Given:
Current, I = 2.10 A
Time, t = ?
Amount of solid copper, m = 4.10 g
Charge on 1 electron, e = 1.6 × 10⁻¹⁹ C
We know that the charge, Q = I × t
In electrolysis, Q = n × F
Where n is the number of moles of electrons.
F is the Faraday constant which has a value of 9.65 × 10⁴ C/mol
From this, we get:
t = n × F / I
Charge on 1 mole of electrons = 1 Faraday
Charge on 1 mole of electrons = 9.65 × 10⁴ C/mol
Charge on 1 electron = 1 Faraday / Nₐ
Charge on 1 electron = 9.65 × 10⁴ C / (6.022 × 10²³) ≈ 1.602 × 10⁻¹⁹ C
Number of moles of electrons, n = m / (Atomic mass of copper × 1 Faraday)
n = 4.10 g / (63.55 g/mol × 9.65 × 10⁴ C/mol)
n = 6.88 × 10⁻⁴ mol
Now, we can find the time taken to deposit copper solid as:
t = n × F / I
t = 6.88 × 10⁻⁴ mol × 9.65 × 10⁴ C/mol / 2.10 A
t ≈ 3.14 h
Therefore, the time needed to deposit 4.10 g of solid copper at the cathode was 3.14 hours.
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A pH meter gave a reading of 72.2 mV using a glass electrode and a Calomel reference electrode for a standard buffer of pH 7,000. A sample Of blood gave a reading of 45.6 mV. What was the pH of the blood sample?
we find that the pH of the blood sample is approximately 13.4.
The pH meter reading of 72.2 mV using a glass electrode and a Calomel reference electrode corresponds to a standard buffer of pH 7,000. The sample of blood gave a reading of 45.6 mV. We can use this information to calculate the pH of the blood sample.
To determine the pH of the blood sample, we can use the Nernst equation, which relates the measured potential difference (mV) to the pH:
E = E₀ - (0.05916 / n) * log([H+])
Where:
- E is the measured potential difference
- E₀ is the standard potential difference at pH 7,000 (72.2 mV in this case)
- n is the number of electrons involved in the reaction (usually 1 for pH measurements)
- [H+] is the concentration of hydrogen ions (protons)
First, let's calculate the value of [H+] using the Nernst equation. We'll substitute the given values into the equation:
45.6 mV = 72.2 mV - (0.05916 / 1) * log([H+])
Now, we can solve for [H+] by rearranging the equation:
0.05916 * log([H+]) = 72.2 mV - 45.6 mV
0.05916 * log([H+]) = 26.6 mV
Divide both sides by 0.05916:
log([H+]) = 26.6 mV / 0.05916
Now, we can calculate [H+] by taking the antilog (inverse logarithm) of both sides:
[H+] = 10^(26.6 mV / 0.05916)
Using a calculator, we find that [H+] is approximately 3.981 * 10^14 M.
Finally, to calculate the pH of the blood sample, we can use the equation:
pH = -log([H+])
Substituting the value of [H+]:
pH = -log(3.981 * 10^14 M)
Calculating this value, we find that the pH of the blood sample is approximately 13.4.
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Use a power series to solve 2y′′−y=0,
y(0)=4,
y′(0)=−9 Find the radius of convergence.
Answer; radius of convergence is given by the absolute value of the ratio of coefficients a2 and a0.
To solve the differential equation 2y′′−y=0 using a power series, we can assume that the solution can be represented as a power series:
y(x) = ∑(n=0 to ∞) an * x^n
where an are the coefficients of the power series and x is the variable.
Differentiating y(x) twice with respect to x, we get:
y′(x) = ∑(n=0 to ∞) n * an * x^(n-1)
y′′(x) = ∑(n=0 to ∞) n * (n-1) * an * x^(n-2)
Substituting these into the given differential equation, we have:
2 * ∑(n=0 to ∞) n * (n-1) * an * x^(n-2) - ∑(n=0 to ∞) an * x^n = 0
Let's simplify this equation:
2 * (0 * (-1) * a0 * x^(-2) + 1 * 0 * a1 * x^(-1) + ∑(n=2 to ∞) n * (n-1) * an * x^(n-2)) - ∑(n=0 to ∞) an * x^n = 0
2 * ∑(n=2 to ∞) n * (n-1) * an * x^(n-2) - ∑(n=0 to ∞) an * x^n = 0
Since the first term has n=2 as the lower limit, we can shift the index by letting k = n - 2:
2 * ∑(k=0 to ∞) (k+2) * (k+1) * a(k+2) * x^k - ∑(n=0 to ∞) an * x^n = 0
2 * ∑(k=0 to ∞) (k+2) * (k+1) * a(k+2) * x^k - ∑(n=0 to ∞) an * x^n = 0
Next, let's match the terms with the same power of x:
2 * (0 * 1 * a2 * x^0 + 1 * 0 * a3 * x^1 + 2 * 1 * a4 * x^2 + 3 * 2 * a5 * x^3 + ...) - (a0 * x^0 + a1 * x^1 + a2 * x^2 + a3 * x^3 + ...) = 0
2 * (2 * 1 * a2 * x^0 + 3 * 2 * a3 * x^1 + 4 * 3 * a4 * x^2 + 5 * 4 * a5 * x^3 + ...) - (a0 * x^0 + a1 * x^1 + a2 * x^2 + a3 * x^3 + ...) = 0
Simplifying further, we get:
2 * (2 * 1 * a2 + 3 * 2 * a3 * x + 4 * 3 * a4 * x^2 + 5 * 4 * a5 * x^3 + ...) - (a0 + a1 * x + a2 * x^2 + a3 * x^3 + ...) = 0
2 * (2 * 1 * a2 + 3 * 2 * a3 * x + 4 * 3 * a4 * x^2 + 5 * 4 * a5 * x^3 + ...) - (a0 + a1 * x + a2 * x^2 + a3 * x^3 + ...) = 0
Now, let's equate the coefficients of the powers of x to zero:
For the constant term (x^0): 2 * 1 * a2 - a0 = 0
For the linear term (x^1): 3 * 2 * a3 - a1 = 0
For the quadratic term (x^2): 4 * 3 * a4 - a2 = 0
For the cubic term (x^3): 5 * 4 * a5 - a3 = 0
and so on.
We can see a pattern here:
For the nth term, we have (n+2) * (n+1) * an - an-2 = 0
Simplifying, we get:
(n+2) * (n+1) * an = an-2
We can use this recursion relation to find the coefficients an in terms of a0.
Now, let's find the radius of convergence for the power series solution. The radius of convergence (R) can be found using the formula:
R = 1 / lim┬(n→∞)|an/an+1|
Substituting the values of an from the recursion relation:
R = 1 / lim┬(n→∞)|((n+2) * (n+1) * a0) / ((n+4) * (n+3) * a2)|
Simplifying, we get:
R = 1 / lim┬(n→∞)|(n+2) * (n+1) * a0 / (n+4) * (n+3) * a2|
Taking the limit as n approaches infinity:
R = 1 / |a2 / a0|
Therefore, the radius of convergence is given by the absolute value of the ratio of coefficients a2 and a0.
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Which molecule would you expect to be more soluble in water, CCl_4 or CH_2Cl_2?
Both CCl4 and CH2Cl2 are insoluble in water. CH2Cl2 is more soluble in water than CCl4 because it is a polar molecule with a dipole moment, making it a polar solvent that dissolves in polar solvents like water.
Both CCl4 and CH2Cl2 are insoluble in water. CCl4 is less soluble in water because it is nonpolar while CH2Cl2 is polar, making it more soluble. Both compounds are made up of the same atoms, with the only difference being that one hydrogen atom is replaced by a chlorine atom.CCl4 is a nonpolar molecule, it does not dissolve in polar solvents like water. CH2Cl2, on the other hand, is a polar molecule with a dipole moment, making it a polar solvent that dissolves in polar solvents like water. As a result, CH2Cl2 is more soluble in water than CCl4. CCl4 and CH2Cl2 are both halogenated organic compounds that are used as solvents and are also found in the environment. Both compounds are composed of the same elements, with the only difference being that CCl4 has four chlorine atoms while CH2Cl2 has two chlorine atoms. Because CCl4 is a nonpolar molecule with a tetrahedral shape, it has no permanent dipole moment. As a result, it is unable to interact with polar solvents like water and is therefore insoluble. CH2Cl2, on the other hand, is a polar molecule with a dipole moment due to the difference in electronegativity between hydrogen and chlorine atoms, resulting in partial positive and negative charges on the molecule. As a result, it is soluble in polar solvents like water. In conclusion, CH2Cl2 is more soluble in water than CCl4 due to its polar nature and dipole moment, allowing it to interact with the polar water molecule.
CCl4 is a nonpolar molecule and does not interact with the polar water molecule, while CH2Cl2 is a polar molecule with a dipole moment, allowing it to interact with the polar water molecule. As a result, CH2Cl2 is more soluble in water than CCl4.
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