Kindly refer to the following image::
E)
The flow will move from left to right.
A fluid flows from a certain place (A) to another place (B) only when energy difference exists, energy of (A) being higher than energy of (B).
Coming to fluid mechanics, the "energy head" consists of primarily 3 sub-categories:
In the above case, A and B lie in the same height, therefore elevation head difference is ZERO (0). The magnitude of height is irrelevant when they both lie at the same height.
Initially, if the circular gate is not open, then the fluids are not moving, thus velocities are ZERO (0) and therefore, Velocity heads of both A and B are ZERO (0) then.
Now, we shall calculate Pressure head (P.H)
where
Thus,
[Note that we did not find the Pressure at A, but instead we found the pressure head at A. "Head" is an ideal way of expressing energy in Fluid Mechanics while Pressure isn't always an ideal manner..]
where
Thus,
We can see that the energy head is greater in the left side (5.9436 m) of the tank as compared to that of the right side (5.334 m) of the tank, therefore, the flow will be from left to right.
--------------------------------------------------------------------
F)
We are asked to calculate velocities at points 1 and 2.
----------------------------------------------------------
NOTE:
A certain part of the data is missing in the question. For instance, the 10 ft water tank is told to be draining out water. And if we consider the points 1 and 2 to be on the floor of the both sides of the tank, then water is going to fill up the bottom of the left side tank because water has a greater specific gravity (S = 1) as compared to the fluid in the left side of the tank (S = 0.75 ). Denser fluid falls at the bottom. This will cause the pressure head at the bottom of the tank to be different from the calculated 5.9436 m (because even water's pressure will be acting at the bottom). This will result in an increase in the velocity. But since no such information is relayed in the question, we will assume that such a phenomena doesn't occur.
-------------------------------------------------------------
Point 1:
We will assume that the water flows out into the open (atmosphere) from the left side tank.
Velocity at point 1 =
where
Point 2:
We will again assume that the water flows out into the open from the right side tank.
We will apply Bernoulli's Theorem bewteen 3 and 2.
where
-------------------------------------------------------------------------
G)
--------------------------
CONCEPT:
This is a very tricky part. What we will essentially do is that on the left hand side, of the tank, we have the space completely filled with the fluid of SG = 0.75. But on the right hand side, we do not have this homogeneity. We have water and this fluid. Now the problem is, we can find the pressure on the right hand side too by conventional means. But that will lead to a lot of confusion. Therefore, we will convert the entire right hand side liquids into one liquid (that is water). Now if we convert all the right hand side liquid to water, it will naturally result in a lower height [represented by "h"] as water is denser and thus, will take lesser volume for the same pressure force. This lower height is represented in the second image (below). So now, the first image (below) helps us calculate the force on the left hand side while the second image (below that) helps us calculate the force on the right hand side of the tank. Since these two forces act horizontally, we can then find the resultant force acting on the tank if we happen to subtract the lesser force from the greater force.
--------------------------
For this, we are not given any "width" of the tank in the question. However, we will assume that it is a square sided tank which has a width of 10 ft (perpendicular to the plane of paper).
Also, we will find the pressure acting ON ONE SIDE of the water tank.
In the above picture, we have converted all of the required data from feet to m.
The pressure acting on the left side of the tank is straight forward. We will find the hydrostatic force on the left side in the following manner.
where
Thus,
Now, for right hand side, we will convert the entire column into a water column.
Thus,
=>
= 3.048 + 0.75x (represented by "h" in the image
below - also, free surface level changes)
Now, again,
Thus,
The final force = F(right) - F(left) = 138889.587 + 68351.175x - 104167.19 - 68351.175x = 34722.397 N
This force acts on the side (which is of area 9.29 m2). Thus
---------------------------------------------------------------
This question has taken me a really long time to complete. Kindly upvote if you are satisfied with my efforts. :)
Q-1 For the two compartment flow system as shown below, the water tank (open and immersed)...
12) As shown in fig. an open-tube manometer containing water (p.-10 kg/m') and mercury (p-1.36x 10 kg/m). The height of water in the left column above the interface A is h' - 30 cm, while the height of mercury in the right column above B is h - 20 cm. The right column is open to the atmosphere Patm - 1.01 10 Pa. The pressure P in the container is: a) P-1.25x10 Pa a) P=0.56*10Pa b) P-4.29x109 Pa d) P-2.46x10*...
1. Water at 100°F is pumped from a sea-level reservoir to a tank open to the atmosphere through a new 14-in ID galvanized iron pipe as shown below. The minor loss coefficients in the suction and discharge piping are EK = 1.5 and Eduk = 7.2. Perform the following: a. derive the equation for the system curve as hy = a + b where he and a have units of feet and b has units of ft/gpm); b. plot the...
Problem Statement 1 The pump in the system shown below is used to transport water from reservoir A to and discharge it to the open atmosphere at point B. The elevation difference between the two reservoirs is Az, and the piping has a 2000 ft length of 16-in diameter. The flow is fully turbulent with kinetic energy correction factor = 1.1 and the Darcy-Weisbach friction factor f = 0.0002. The minor losses in the system are negligible and can be...
Question D.1 A2 Not sure Water flows between two tanks connected by a 100 m long pipe as shown in figure D1-1 below The tanks have a free surface height difference of 15 m and are both open to atmosphere. The first 30 m of pipe from the upper tank (section 1) has an internal diameter of 50 mm and a friction factor of 0.006, whilist the remaining 70m of pipe (section 2) has an internal diameter mm and a...