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  • Welcome to lesson 25 on Flow Control Valves of the course on Industrial Automation. Flow

  • control valves are very important, so after learning the lesson, the student should be

  • able to describe the importance of flow control valves, they are found everywhere in process

  • industries. Learn the structure of major types of flow control valves, learn about the their

  • flow characteristics, because that is very important in designing the applications. And

  • finally, the how to actuate these valves and how to affect their characteristics to achieve

  • a certain characteristic of the process control loop, so these are the topics, that the student

  • is expected to learn from this lesson.

  • So, the first of all, let us have a look at, the importance of flow control, flow control

  • is probably the most important control in a process control application, and as we shall

  • see, during our process control module, that flow control loops, form a part of most type

  • of control loops. For example, they are parts of flow loops, where directly flow has to

  • be controlled, flow is a final objective of control, they are parts of temperature loops,

  • because temperature is generally controlled by controlling, flow of either a coolant or

  • and let us say steam, for heating, this is not stream, this is steam.

  • Of course, for level loops, because by integrating flow only you have level, so all level control

  • is essentially flow control. Similarly, pressure loops, because again pressure control is achieved

  • by using flow control, and composition loop, because compositions of products, are typically

  • dependent on the compositions of the components in a let say a reactor. So, if you want to

  • control the composition of a particular product, flow control is often a very important part

  • of that, control applications. So, we see that, for most types of control

  • applications, flow control is a part, and the element that finally, achieves the control

  • is the flow control part. So, it is importance, cannot be overstated and as we shall, as we

  • need to mention again slight spelling mistake. So, this is a valve flow is actually a function

  • of valve, the pressure drop across the valve and this, and the stem position, as we shall

  • as we perhaps know that by Bernoulli's equation. The flow of a, flow through a, through an

  • orifice, of flow control valve is essential in orifice and it is the dimensions of the

  • orifice, which are varied is proportional to, proportional to a root over of delta P.

  • Delta P is the pressure difference across the valve, and K is proportionality constant,

  • which contains among other things, a what we, what we call as discharge coefficient

  • or C v, so the flow the inflow control valves, it is this K or this discharge coefficient

  • of the valve which is changed, by changing the orifice dimensions, so that is the way,

  • we achieves flow control.

  • Now, so first of all we see, the various kinds of valves and the first kind of valve that

  • we see are globe valves. Globe valves are so before we must understand the various parts,

  • so I am going to hatch it, so this is the, these are the ports, this particular flow

  • control valve, this is inlet port, this is outlet port, this is another component of

  • the body, not this one, not I am sorry, not this one, not this one, this part, this part,

  • this is the body, the fluid in fact, there are, this is a top and bottom guided.

  • Top and bottom guided means the basic valve assembly movement is guided at in the top

  • and at the bottom. And, it is a double seated globe valve, so there are two seats, one seat

  • is here, another seat is here. So actually the fluid enters through this and will go

  • through this, when this valve will rise, when this valve will rise, it will go through this

  • and will flow out, similarly, it will go through this, it will go through this path and go

  • out. So, since there are two seats, it is a double

  • seated globe valve, one of the advantages of double seating, is that the force as you

  • can see, that the fluid when it flows through the valve, it actually exerts a pressure on,

  • this valve mechanism, this is called the stem and these are called the plugs, these are

  • the plugs. So, the plugs actually come and this is the seat, and the plug actually comes

  • and sits over the seat, and seals the, seals the orifice and when the valve opens, this

  • plug goes up, so the fluid flows through the orifice.

  • And, this plug movement is actually realized, by moving the stem, to which the plug is connected,

  • so obviously, there is the fluid, exerts force on the plug and plug sometimes has to work

  • against this force. So, to reduce for double seated valves, although they are not so popular

  • now a days, but double seated valves, one of the biggest advantages of double seated

  • valves is that, since the force, when the liquid is flowing in this direction and the

  • force that the liquid exerts in this direction are opposing each other, so the net force

  • on the stem is actually small. So, therefore, it requires a smaller capacity

  • of the actuator, to make a movement, but still nevertheless these valves are not so popular,

  • because of mainly two reasons. Firstly, that single seated valves are can be realized with

  • a much smaller size number 1, Number 2 is that, because of you know slight mechanical

  • problems, it is very difficult to ensure that, both the plugs actually seal the, seal the

  • orifice at the same time, and therefore, often you have problems of leaking through the valve,

  • that the shut off of the valve is not so tight.

  • So it is for this reason that people, nowadays prefer single seated valves, so this is a

  • single seated valve, you know you this is the plug, this is the plug you can see that.

  • This is the seat on which the plug sits, this is the seat, this is the stem, this is the,

  • these are the bodies, this is the body. So, the fluid actually flows like this, like this,

  • like this, so this is the fluid path, when the valve opens, this is the inlet port, inlet

  • and this is the outlet port. So, this is a top entry, top entry because

  • the valve stem enters from the top, top guided here there is only one guidance, one guiding

  • piece, that is top guided not, not top and bottom guided, single seated, because there

  • is only one seat globe valve. So, these valves are one of the most common types of valves

  • used in the process industry.

  • Next are ball valves, these valves have, the in the previous case, the stem actually moves

  • in a linear fashion up and down, and for these valves the stem actually rotates, so it is

  • a so it requires a rotary actuator, it can be directly coupled to a motor. So, you see

  • that, actually you have a ball, a ball like structure, through which there is a hole,

  • so you can see, the hole, this is the ball, these are ball valves and this is the hole

  • through the, this is the hole through the ball.

  • So, now suppose, so this is the hole suppose, so when the ball is in this position, then

  • you can understand, that this is the inlet port and this is the outlet port. So, when

  • the suppose the fluid is coming like, this is the inlet port and this is the outlet port,

  • so when the hole is aligned with the inlet port and outlet port holes, then the fluid

  • can flow from inlet to outlet. On the other hand if the ball rotates, then the flow is

  • blocked, so it is by rotating the ball, that various amounts of flows can be realized,

  • so this is the basic principle of a ball valve.

  • For example this is a multi-port ball valves, so you can see the ball, this is a cross section,

  • so the ball is you know like this, semi cylindrical ellipsoidal, and these are the holes. So,

  • the in this case, this has this can take care of three ports, so you can see that, in various

  • positions of the ball, if the ball is aligned like this, then liquid can flow from here

  • to here, if it is aligned this way, it can flow from this to this or this to this. So,

  • under the various positions of the ball valve, you can have various kinds of, various ports

  • can be connected to various others. This is a T ported ball valve we can have an angle

  • ported valve, ball valve and things like that, so this is the basic principle of balls valve.

  • This is this picture shows how when a ball valve rotates, then how the flow throttling

  • takes place, so you see, that as it is rotating. So this, the effective area of flow, they

  • gets reduced, so as it rotates slowly the effective area of flow, will get reduced and

  • therefore, the flow will get reduced, so the flow gets throttled.

  • This is another, kinds of ball valve, where the ball is of a certain shape, so it is called

  • a characterized ball valve. So, here you can see that, as again as it rotates this surface,

  • slowly comes and closes the flow, and therefore the flow the flow can be throttled or it can

  • be completely shut off, so these are this is another kind of ball valve called the characterized

  • ball vale.

  • The third kind of valve, actually there are various kinds of valves, we are going to only

  • talk about some major ones, but there are at least ten, fifteen different types of valve,

  • which are, which are used in various kinds of applications in the industry diaphragm

  • valve, pinch valve a sliding gate valve, etcetera, etcetera. So, this is another kind of valve,

  • which is called a butterfly valve, so basic idea is that, this is butterfly valves are

  • used in large pipes, they are also used for the apart from you know, applications in let

  • us say, a liquid applications like water, water flow control etcetera.

  • They are also used in gas applications, like they are used in a, heating ventilation, air

  • conditioning applications of large buildings, where the airflow needs to be controlled.

  • so in such applications butterfly valves are also used. So, basic idea is that, in all

  • valves there has to be an variable obstruction right, so it is this disc, which is the, which

  • creates the obstruction, and there is a shaft or a pin about which, so you can understand,

  • that you can understand that this is a butterfly valve and there is basically a shaft runs

  • across it and this shaft is driven. So, this is valve is actually, stuck to this

  • and if you rotate this actuator, then this valve can be either in this position or in

  • this position. So, if you have pipe here, if you have a pipe here, then if you connect

  • in this position then it is open, if you connect at this, if you put it in this positive then

  • it is closed. So, exactly that is the position, so the these two positions are shown, so this

  • is the open position of the disc, open position and this is the closed position of the disc,

  • both positions are shown closed position. And this is the shaft or pin, which is driven

  • to move the disc, various shapes of discs are used to you know again, to reduce the

  • torque requirement on the shaft or to reduce noise, of these such big discs, when you have

  • a fast flowing fluid can sometimes vibrate and create noise.

  • So, this is the picture which shows that, so look from a side, when the disc is, in

  • this position then the damper or then the damper is perpendicular to flow and the valve

  • is closed. When it is moving in and throttling or controlling the flow and when it is in

  • this position, then when damper is parallel flow, then is completely open.

  • So, there are various kinds of disc, which are used as I said to take care of various

  • factors like torque and noise.

  • Now, we so we have seen three different types of valves, characterized in terms of construction.

  • Now, we shall characterize valves in another way, depending on their flow characteristics,

  • so depending on their flow characteristics, valve can be generally characterized, in into

  • three different classes. One is butterfly valves are typically of equal percentage type,

  • that is why and butterfly was written, so one is this equal percentage,. so another

  • is linear and the third one is quick opening. So, this equal percentage valve is you can

  • see, equal percentage means, that if you have a this is percent lift, percent lift means,

  • the stem if it is lifted by a certain percentage, this the stem is moving, so percent lift or

  • percent stem position it, this it may not be, though it is called lift, it may not be

  • always a lift you know, sometimes it may be a rotation also. Basically means, that percent

  • of the total stem movement, so it says that, if you increase the stem movement by x percent,

  • then y percent of the current flow will it, so the flow will increase by y percent of

  • the current flow. So, if you make x percent change, if you make

  • a delta x, x percent of full scale, so if you make a 20 percent change here, then may

  • be 5 percent of the current flow, which is here will take place. On the other hand, if

  • you make a 20 percent change here, then 5 percent of the current flow, which is here

  • will take place, if you make twenty percent change here, then 5 percent of the current

  • flow which is here will take place. So, you see that for the same 20 percent change, at

  • 20 percent, 40 percent, 60 percent, 80 percent the change in flow is going to gradually increase,

  • giving rise to this characteristics. So, an equal percentage of the current flow

  • will take place, if you make a certain, a certain fixed percentage of lift change, that

  • is the reason, why these valves are called equal percentage. So, you can easily analyze,

  • you can easily understand, that this sort of characteristic exponential kind of characteristic

  • arises, so on the other hand, we have linear, which is obvious, that is for a certain percent

  • of lift change, a certain fixed percentage of the total full scale change, not current

  • flow will take place, so it is a linear it is added by constant.

  • Actually, the linear and the equal percentage are mostly used in process applications, quick

  • opening valves are you know like our bathroom taps are typically quick openings. So, you

  • must have seen that, if you the almost full flow is realized by, a may be, even one turn

  • or one and a half turns of the tap, while if you move it more and more, then not much

  • flow increase takes place. So, these walls there is a quick, increase of flow and then

  • for the rest of the movement there is very little flow.

  • So, it is a kind of opposite of the equal percentage and they are typically used more

  • in you know, on off kind of applications or some certain special kinds of process control

  • applications, but most of the control applications, they use linear and equal percentage parts.

  • Remember one thing, that these characteristics have assumed, that this characteristic are

  • called inherent characteristic and are provided by the manufacturer, inherent characteristics

  • of the valve and are provided by the manufacturer, under conditions that the pressure across

  • the valve is constant. So, they actually maintain the pressure across the valve and then they

  • characterize this curves, so this is important to understand.

  • And, now how are these characteristics realized, they are realized by various profiles of the

  • plug, so in the case of the globe valve here, say we have there are three kinds of, these

  • are three plugs, which realize equal percentage, linear or quick opening characteristics.

  • Now, it turns out one must realize, that if you actually put the valve, into an application

  • and connected up, with you know other components pumps systems pipes etcetera, then the inherent

  • characteristic will not be realized. So, the pressure flow characteristic of the actually

  • the rather the stem lift versus flow characteristic of the valve, which is provided by the manufacturer,

  • which is the inherent characteristic will not be realized, because of the fact, that

  • delta P will not remain constant. So, how does that happen, so you see that,

  • when you are connecting, so this goes to the system wherever, you want to send this flow

  • and we are just you know, arbitrarily assuming that the head of the, that the system takes

  • a particular kind of static head. So, what happens is that during flow there are actually

  • pressure drops, so there is some pressure drop at the inlet of the pump, then the pump

  • rises, the pressure, that is the job of the pump, it creates a pressure head.

  • Then this flows through the pipe, so again there is some friction loss and there is some

  • pressure head. Then there is a drop across the valves, because all, because all valves

  • will have a, you know if it has flow through an orifice, there has to be a delta P, then

  • again there is a drop at along the pipe and then the available pressure at the system

  • is there, so this is the way the pressure drops and actually as we shall see now.

  • That now, as now as we know, that these pressure various pressure drops, vary with flow itself,

  • so for example, the pipe friction pressure loss, will also rise with flow. Similarly,

  • if the pump head, because there are pressure losses inside the pumps, so the pump head

  • available, the pump head that will be generated, will also be lower. Similarly, here we have

  • assumed a static head pressure, it may be constant or in some cases, even this for example,

  • if the fluid is a you know, kind of heat exchanger, then again the heat exchanger is actually

  • nothing but, a intertwined length of pipe. So, basically the pressure head across the

  • system will also increase with flow, so eventually what happens, is that see the pump is the

  • prime mover right. So, the total pump head available is this one, and that must be equal

  • to the sum of the drop in pipes, drop in the valves, plus drop in the system. So, as the

  • drop in the pipe and the drop in the system rises, there is less and less delta P available,

  • across the valve and, so the flow actually reduces.

  • So, the operating point that are established, will always have delta P falling, so the valve

  • differential pressure available, actually falls quite sharply with the flow, so it is

  • not constant.

  • In effect what happens is that, for example, this is the case of an equal percentage valve,

  • at some delta P, so you see that the inherent characteristic is almost like an equal percentage

  • nearly. On the other hand, if you put the valve, that valve into along with a pipe and

  • a pump and a system, then initially, there is a lot of fresh delta P available, because

  • there is hardly any drop, in the flow is low, so there is hardly any drop in the system.

  • So, the pump, so the valve flow with change in lift, because delta P available across

  • the valve is now quite high at this stage, so there is a, for a sudden change in lift,

  • there is a good change in the flow, so the rate remains high. On the other hand here,

  • you see that in this part, for the inherent characteristic the rate of flow change is

  • high, but that much rate of flow change is not achieved in the installed characteristics,

  • because of the fact, that now the delta P has come down.

  • So, if the delta P has come down, then for a then for a given change in the lift, now

  • so much change, which was available see previously when delta P was held constant, a lot of change

  • could be possible, by changing a certain part of the lift. But now, since a delta P is going

  • to fall, so therefore, so much change is not possible, and we get a different characteristic,

  • that characteristic is called the installed characteristics, and this must be remembered,

  • because it is the installed characteristic finally, which is going to decide the characteristic

  • in the process control. So, therefore, we must understand that the

  • inherent characteristic gets changed, because of pressure drops and the resulting characteristic

  • is called the installed characteristic. So, the same thing happens for, linear valves

  • again there is a high higher than, inherent you can we are assuming that the inherent

  • characteristic delta P will be will be maintained, you know somewhere in the middle of the delta

  • P range. So, initially you have higher, you have a higher delta P, so therefore, the rate

  • of rise is high, later on the, rate of rise is lower, than the inherent characteristic,

  • this is what happens?

  • This is the characteristic for an inherent characteristic for a seeing, and they are

  • not so much use, so the installed characteristic is actually not drawn.

  • Now, these characteristic sometimes you know, especially when you are trying to design process

  • control application, the valve gain, the valve gain also comes along with the process gain.

  • So, if so when we want to decide the controller gain, then sometimes it is it is desirable,

  • that we change the, that we change the valve characteristic to actually suit the, requirements

  • of the process, for example as we shall see that we can we may like, to have, that the

  • valve process combination gain, remains more or less flat over the operating region, this

  • may be requirement for designing a good, good controller.

  • So, what I am trying to say is that, from the, you know there is an electronic controller,

  • from which output is actually going to the valve actuator, the valve stem is being moved

  • by some mechanism called actuator as we shall see, so this is going to the actuator. Now,

  • between this control and the actuator, sometimes we can put some signal processing blocks,

  • which are for example, in this case, this is a, this is called a multiplier relay.

  • So, what we are achieving here, is that, the see the signal available at the A port, is

  • a multiplication of B to C port, so suppose this is increased. So, immediately this will

  • increase, then this will, also increase and therefore, this will increase sharper, so

  • what happens, is that, if you change this linearly, that is if the input is changed,

  • in a linear fashion over time, then the output will change, in this fashion, so what happens,

  • is that effectively actually, so if you put this really now, then what will happen, is

  • that a linear valve, will start behaving like an equal percentage part.

  • So, what we, what is the massage is that, by putting such signal processing blocks,

  • we can change the valve characteristic, I mean depending on the availability sometimes,

  • it may not be, it may not be easy to locate a valve of that appropriate characteristic

  • in the market. But, by signal processing after the controller, we can always change the valve

  • characteristics.

  • So, now next we come to, the various kinds of actuators, you know how to actuate the

  • valve, so we typically, we have various kinds of actuators, we have electro electromagnetic

  • actuator or solenoid actuators, we have pneumatic actuators, we have sometimes for large valve,

  • we have hydraulic actuators. So, we can also, typically we can also have mechanical actuators

  • also, manual actuators, so in this case, we will type typically look at two actuators,

  • one is a solenoid actuator and the other is an pneumatic actuator.

  • So, solenoid actuators have you know higher speeds, they are lower ratings, but higher

  • speeds, because higher speeds because, as we will see, that the force on the actuator

  • can be quickly controlled, because it is and it is controlled by current, so current can

  • be driven pretty fast. So, therefore, forces can be created very fast, varying forces can

  • be created and therefore, the valve actuation becomes fast, on the other hand for pneumatic

  • actuators, the force is created by, you know by bringing pressurized air on to work on

  • a surface or a diaphragm. So, since there is some volume involved, so

  • there is certain amount of time required for that air to come and fill the chamber and

  • then create the pressure on the diaphragm. So, pneumatic actuators are always generally

  • slower than solenoid actuators, so we have higher speed, lower size, because pneumatic

  • actuator can be, of quite high, I mean of larger size, because by just by increasing,

  • the diaphragm sometimes, we can create a lot of pressure or even higher ratings we can

  • use hydraulics. So, solenoid actuators are generally of lower

  • size and often they are used as we will see, they are often used in pilot stages of electro

  • hydraulic valves. So, you have a big control valve and you want to move the valve, so you

  • see that, that big electro hydraulic valve, actually may be controls the flow. Now, to

  • move the valve also, you need to create you need to move the valve, so you know, you have

  • a valve, this is the installed characteristic page up just a movement. So, we were talking

  • about solenoid actuators, that they can be used in, pilot stages I know why this is creating

  • a problem.

  • So, what I was saying is that the electro hydraulic valve pilot stages solenoid valves

  • are used and this is a particular construction of the solenoid valves. So, you see that this

  • is the valve, this is the plug, this is the plug, and this is the closed position shown,

  • so this is inlet and it is flowing through this, and going to this is the flow of fluid,

  • there is a spring loading, this is here the stem is actually connected to a magnetic core,

  • which is called the plunger. And, here you have a high current carrying,

  • high force creating coil, so this is the coil assembly, solenoid coil, housing, shading

  • coil is used to, you know guide the flux through the core, so that that proper force is created

  • and flux, actually the force is created by the flux, so one has to guide the flux, so

  • that an upward force is created. So, and this is the movable core, this is the tube, through

  • which the core moves, these are the connections, so what happens is that, in when the coil

  • is de-energized, then the spring will push and keep the valve closed.

  • On the other hand, when this will, you see that, if this is energized, then the flux

  • is flowing like this as shown and it is pulling the plunger up. So, when the pulling the plunger

  • up, then this spring is compressed and this opening is, opened and the fluid flows, so

  • this is the way a solenoid actuator will work.

  • This is on the other hand, this is the particular pneumatic actuator, so again same thing, again

  • you have a plug and you have these ports. So, what happens, is that here, by spring

  • force, this is a particular valve, where you can close the valve by applying air in the

  • normal position, it will stay open. There are various kinds of valves as we shall see,

  • that if you apply energy or force, they will close or if you apply energy or force they

  • will be opened, they will open. So, in the previous case, for opening the

  • valve we needed to apply current, in this case, for closing the valve, we need to apply

  • air force, so the air will enter here, this is the diaphragm, on which it will create

  • a pressure. So, the pressure multiplied by the area of the diaphragm, will give the force

  • and this force will be going to push it down and close it, so this is the operation basic

  • operation of a pneumatic valve.

  • So, as we shall see, that if you see the characteristics of this valve, then obviously, there are as

  • we said, that there are forces, acting on the plug, because when the fluid is flowing

  • out through the orifice it is actually, pushing the plug up or down, depending on the flow

  • profile. So, there is a, so there are forces acting on the plug, so what happens is that,

  • because of this the plug, the valve stem position percent, and the I mean diaphragm pressure,

  • see there are two things. Firstly, diaphragm pressure to stem position,

  • so how much diaphragm pressure is required to create, what stem position and then stem

  • position to flow stem position to flow characteristic is essentially guided by the construction

  • of the valve, and the applied delta P. On the other hand, the diaphragm pressure applied

  • to stem position, is guided is essentially affected by how much force is actually acting,

  • on the on the stem, so when you have, high plug forces then this stem position to diaphragm

  • pressure characteristic gets shifted. So, by applying and what is, what is controlled,

  • what is controlled from the controller, is actually the diaphragm pressure, you know

  • actually there is a controlled air supply pneumatic source. So, what amount of pressure

  • will be applied on the flow control valve diaphragm that is what is control so if the

  • stem position diaphragm pressure, so in open loop control, we will you know there is some

  • gain calculated. So, people will think that, now so this is the flow, so now, I know the

  • flow characteristics so therefore this much of stem position must be realized.

  • So, for realizing this much of stem position, I have to apply this much of diaphragm pressure,

  • so that much of output will come from the controller, this is the way, the valve is

  • going to be controlled. But it so happens, that this stem position to diaphragm pressure

  • characteristic will change, depending on whether there is plug force or not, so we depending

  • on the plug force, we may or may not be able to and the plug force depends on so many things,

  • the plug force depends on the current value of pressure, in the pipe, so we need to make

  • it is necessary, to make this make valves invariant to such variations of force.

  • So, for it is for such purposes, that we use often use, what is known as a valve positioned,

  • so valve positioner is actually a itself a control system, so what it does, is the following.

  • So, you see, that in this case, this is the valve, this is the valve stem, again there

  • is a spring, and this is the, this is the diaphragm on which the, is the pressure is

  • being applied. So, the diaphragm is coming from the air is coming from here, and it is

  • through this valve, that the pressure the position of this spool, position of this spool

  • that the pressure here is being controlled. So, how it is being controlled, so we are

  • applying a 3 to 15 PSIG input signal, which is the low power of a input signal, that is

  • being that is being applied here in this chamber. So, that crates a force on this. once it creates

  • a force on this, this spool will move downward, so when it moves downward the air supply which

  • is a high pressure air, will flow through this and through this and will come here,

  • so depending on the opening there will be a kind of pressure drop and the final pressure

  • will be realized here. Now, as this pressure increases, this thing

  • now starts moving downward and the valve opens, on the other hand, because of this mechanism

  • when this comes downward, there is a force applied upward. So, you see it is a force

  • balance principle, so finally, whatever pressure is being applied here, that must be balanced

  • that will be, that will balanced by this that will be balanced by this spring force, as

  • well as this force, so therefore, since this is an applied pressure, and this spring force

  • depends on the displacement. So, therefore, the this for a for a given

  • pressure here, the valve will as long as this force is not balanced, say when this force

  • is higher, then it will start opening and this pressure will keep increasing. As it

  • is keeping increasing, this is come trying to come down and therefore, this is going

  • to go up increasing the spring pressure, so this spring pressure will actually balance

  • this force, when a particular displacement of this spring takes place, and by the mechanism,

  • this a particular displacement of this spring, implies a particular displacement of this

  • stem. So, therefore, you when you apply a particular

  • pressure here, a particular displacement of the stem is achieved, irrespective of what

  • are the forces here. So, till this displacement is achieved, this will start moving and obviously,

  • this should have enough power to you know, you know overcome this force. So, but if you

  • have created enough power, then just enough force will be create here, so that the final

  • displacement, will actually balance this pressure. So, the final displacement is always invariant,

  • irrespective of whatever is the force on this stem, so in this way, you achieve a particular

  • stem position to control input signal, it does not depend on the plug force, because

  • by close loop control. So, such a thing is called a valve positioner, there are various

  • other mechanism, there is just one mechanism, which we have shown, there are various other

  • based mechanisms etc.

  • So, now we come to, take a look at some valve characteristics for example, you know this,

  • there are certain characteristics of the stem position movement, especially a dynamic characteristics.

  • So, if you give a small value of command this, the stem position will be this much, if you

  • give a large command will be this much, but you see there is a certain restriction on

  • the rate at which, the stem can travel, so therefore, you cannot give very large and

  • at the same time very high frequency commands. If you give them, then that input command

  • will not be realized, in terms of stem position and you will get responses like this.

  • So, for example, if you give a large and then high frequency sinusoid, then the stem position

  • will not be able to follow it, but rather it will, go up like this, so there will be

  • a distortion you know. So, these things are to be kept in mind, when one is designing,

  • a process control loop with a valve, that they have, this rate limits any actuator,

  • most of the electromechanical actuators, actually have a rate limit.

  • Similarly, there may be a, there may be hysteresis in the stem position, due to various factors

  • you know. So, when you are increasing the pressure, the stem position may actually,

  • follow this curve, and when you a decreasing the pressure, it may not follow exactly the

  • same curve. Now, such dead bands, as we know from, you know standard non-linear control

  • systems, often give rise to oscillations.

  • So, these you know, this process control loops, flow loops the if you give an, if you give

  • an alternating command, then the process control loop may actually oscillate, so these are

  • called limit cycles in the closed loop.

  • Similarly, these are sometimes you know, there is, there is a very important quantity for

  • a valve called range ability. So, range ability means, that what is the maximum to minimum

  • flow ratio, so the maximum flow to the minimum controllable flow is it to say, so valves

  • can have, you know some sometimes valve manufactures claims, that they have you know, 10 is to

  • 1, 15 is to 1, 13 is to 1, 30 is to 1, kind of you know range abilities.

  • So, sometimes in some applications it may happen, that you need a very high range ability

  • that is you can sometimes need, very, very small flows, sometimes you need very, very

  • high flows. So, in such applications, you sometimes have to you know, have valve sequencing,

  • that is you actually have more than one valve, and in one part of the operating region, you

  • operate one valve, and in another part of the operating region, you operate another

  • valve. But, you have to ensure, you know certain

  • things like you know transitions, such that suddenly the when you move from one valve

  • to another valve the process control loop characteristic do not change. So, one of these

  • is by, you know split range control, which we have also seen, in the case of our process

  • control modules, so you have two valves, and they are fed through an amplifier and a bias,

  • so these biases are made different and in certain parts of the region, the actually,

  • the control signal comes to this valve. So, this valve will operate, then after sometime,

  • when this valve input will actually saturate, then this valve will operate no longer and,

  • then this valve will start operating. So, this the overall range of operation is split,

  • using this gain and bias mechanisms and in different parts of the operating region, different

  • valves are employed, Similarly sometimes, you can have there may be another scheme.

  • This is another valve sequencing scheme, where you have a pressure sensor, you know so this

  • pressure, this is actually the controller output, which is going to the valve actuator.

  • So, when the controller output, so the here, this the switching, which is by this three

  • way valves is actually done, based on how much controller output is being exerted to

  • this valves, and depending on them, one of the valves will be operating, either this

  • will be operating or this will be shut off or this will be vented and this will be operating.

  • So, and it turns out, that for such sequencing you know, when you will for example typically,

  • the gain of large valves, will be actually larger, than the gain of small valves. So,

  • one has to ensure, that the when you are switching from the small valve to the large valve, the

  • gain is not, the gains are the gains do not suddenly change, because that is going to

  • change the overall gain of the process control loop, and may bring in you know things like

  • instability problems, instability or saturation problems.

  • So, for doing that, that is why, it is for such kind of sequencings, equal percentage

  • valves are actually better suited, because as we know from the equal percentage characteristics,

  • the equal percentage characteristics is like this, stem position to flow. So, you see that,

  • for the small valves, when you are just before closing the small valves, the actually small

  • valve, actually has a very high gain, so when you are switching on, from this gain to the

  • gain of the large valve, so the large valve actually has a high value of gain, but it

  • is operating in it is low gain region.

  • So, we are transforming from the high gain region of the small valve characteristic,

  • to the low gain region of the large valve characteristic. So, therefore, the gain switching,

  • the suddenly when you switch from the small valve to the large valve, the overall process

  • loop gain, does not suddenly change. So, this is one reason, why you know equal percentage

  • valves are better suited for valve sequencing, rather than linear valves.

  • Often, as we have seen that, as we know I mean this is, this shows that often you know

  • valves are actually put in the closed loop. So, it is actually a part of the flow control

  • loop, generally and if you have a, that is rather than, suppose you have a temperature

  • loop, so in the temperature loop output, controller output rather than giving directly to the

  • valve, which has nonlinearities, which has dead bands, which has hysteresis as we have

  • seen it, is better to set up a flow control loop, which is a slave loop, in the sense

  • that the temperature control loop is actually the master control loop.

  • So, the temperature controller output will give a flow set point, as we have seen, in

  • the case of cascade, so what will happen is that, so. So, this is the this is the one

  • coming from the master say temperature control loop, then if you set up this is the flow

  • controller, this is the flow transmitter. So, if you set up then even if the valve is

  • non-linear, the characteristic of this loop, that is between this point and this point,

  • are much more linear, let us say, it may not be absolutely linear in the mathematical sense.

  • But, there will be much more linear and that makes it, much easier to accurate design,

  • the designer ensure that the characteristic of the temperature control loop, remains uniformly

  • good over the, over the whole region of operation, so sometimes, many times, we set up this kind

  • of loops.

  • Sometimes, you know valve characteristics can be very cleverly used, to you know match

  • the system characteristic, so for example, take the case of a liquid to liquid heat exchanger.

  • So, what happens is that, now you know, this is the input, which is the cooling flow and

  • what is the output, the output is, the outgoing temperature of the liquid, which is being

  • heated let us say, so when there is a slow flow rate, that is when this flow rate is

  • low, then obviously, this liquid stays within the tube for a longer time.

  • And therefore, for both the gain between this point to this point, that is the temperature

  • for a given rate of flow of the heating liquid. The increase in temperature between inlet

  • and the outlet will be higher, not only that, this will be also, then the delay between

  • if you make a step here, then the then this will go up, but the delay between this step

  • and this step will also be higher, because of the fact, that the that the liquid is traveling

  • slowly. So, but on the other hand, when you are, so

  • you see that this is a situation, when you have a high gain and you have a high delay.

  • So, you need to keep, as we know, that the controller gain needs to be kept low, in this

  • region. On the other hand, if this flow is increased, this flow rate is increased, then

  • the gain will fall and the delay will also fall. So, now, is the case, when you can have

  • a, you can for better improve transient performance, you can have a higher controller gain, but

  • it is not you know, automatically easy to actually change controller.

  • So, for this application, if you use, if one uses a, an equal percentage valve, then as

  • we know, that the valve gain goes up, as the flow rate goes up. So, automatically the loop

  • gain increases, as the flow rate increases. So, the overall process, loop transient characteristic

  • is maintained uniform, simply by the valve characteristic, simply by the choice of the

  • valve right, so this is what I am saying. Similarly, at the, an opposite situation can

  • occur, if you have an orifice meter, so you know, so in an orifice meter as the flow rate

  • increases the, sensor gain also increases. So, again the loop gain increases, so in such

  • a case the, one has to have, the overall gain reducing, so one can use a linear valve for

  • this.

  • The lastly, you know valves are, one has to put and have a view towards, what will happen,

  • if the actuation fails, because you know sometimes this flows, can actually cause explosions

  • etcetera. So, valves are constructed in various configurations, which are shown here, for

  • example, fail open or air to close, so if this air supply somehow fails, then this valve

  • will fail and it will fail in an open situation, so the, if the air supply is not there then

  • the valve will remain open. Similarly, there are air to open valves, where

  • if the air supply closer fails, then the valve will close, so these, so one has to chose

  • a particular actuation configuration, to you know avert industrial accidents, under various

  • kinds of failures, so that brings us to the end of this lecture.

  • So, as a matter of review, we have typically seen globe valve, ball and butterfly valves,

  • we have seen various kinds of valve flow characteristics, both static and dynamic, and we have seen

  • how valves are actuated and controlled. There is one aspect, which is treated in books,

  • which is called valve sizing, that is for a given application determining, that the

  • size of the valve, we have, we are not talking about, that because this is essentially a

  • process design exercise, and not, does not concern auto machine control.

  • So, to end points to ponder, first is sketch the cross section of a globe valve, and indicate

  • four of it is major parts, you should be able to do that. What is the difference between

  • installed and inherent characteristics, this is extremely important and why this occurs,

  • What is the main advantage of a valve positioner, why one puts it. And finally, mention one

  • advantage of a solenoid actuator over a pneumatic actuator, and one advantage of a pneumatic

  • actuator over a solenoid actuator, so that brings us to the end of the lecture, thank you very much.

  • Welcome to today's lecture, which is lesson number 26 of the course on industrial automation

  • and control. Today, we are going to take our first look at hydraulic control systems and

  • we will review some elementary basic concepts, and then we will first look at the components,

  • which make a, hydraulic control systems. In the subsequent lectures, we shall see, some

  • special components, and we shall see as to how these components, can be used to make

  • a hydraulic control system, so we give, we begin here, before we begin we look at the

  • instructional objectives.

  • So, the instructional objectives are basically to describe the principle of operation, of

  • hydraulic systems and understand it is advantages, what is involved and why it is almost irreplaceably

  • used, in certain applications there are certain advantages. Then of course, we have to be,

  • the main purpose of the lesson is to be familiar with the basic hydraulic system components,

  • and their roles in the system, what they do. And describe the constructional and functional

  • aspects of hydraulic pumps and motors, how they function, and be familiar with directional

  • valves and control valves, they are very important components.

Welcome to lesson 25 on Flow Control Valves of the course on Industrial Automation. Flow

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B1 中級

講義 - 25 流量制御弁 (Lecture - 25 Flow Control Valves)

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    蔡育德 に公開 2021 年 01 月 14 日
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