AP Physics 1 · Topic 8.4

Topic 8.4: Fluids and Conservation Laws

Unit 8: Fluids10-15% of the multiple-choice section

Topic 8.4 runs two conservation laws through a moving fluid. Continuity, area times speed at one point equals area times speed at another, is conservation of mass. Bernoulli's equation is conservation of mechanical energy written per unit volume, which is why every term in it is a pressure.

AP Physics: Unit 8 (topics 8.4 Fluids and Conservation Laws). AP Physics 1 Unit 8, Topic 8.4. Two learning objectives: 8.4.A, describe the flow of an incompressible fluid through a cross-sectional area by using mass conservation, supported by 8.4.A.1 (a difference in pressure between two locations causes a fluid to flow), 8.4.A.1.i (the rate matter enters a fluid-filled tube open at both ends equals the rate it exits), 8.4.A.1.ii (the rate matter flows into a location is proportional to the cross-sectional area and the speed, derived equation V/T = Av) and 8.4.A.2 (the continuity equation describes conservation of mass flow rate in incompressible fluids, relevant equation A_1 v_1 = A_2 v_2); and 8.4.B, describe the flow of a fluid as a result of a difference in energy between two locations in a fluid within the fluid-Earth system, supported by 8.4.B.1, 8.4.B.2 (Bernoulli's equation describes conservation of mechanical energy in fluid flow) and 8.4.B.3 (Torricelli's theorem, derived equation v = sqrt(2 g delta y)). The topic's boundary statement reads: all fluids will be assumed to be ideal, and all pipes are assumed to be completely filled by the fluid, unless otherwise stated. The CED's suggested skills here are 1.B, 2.A, 2.C, 3.A, and 3.B. Unit 8 carries 10 to 15 percent of the multiple-choice section and a suggested 12 to 17 class periods.

What Topic 8.4 requires

Topic 8.4 carries two learning objectives, and the CED names the conservation law in each of them. That naming is the framing to steal, because most other explanations present continuity and Bernoulli as two formulas about pipes.

  • 8.4.A asks you to describe the flow of an incompressible fluid through a cross-sectional area by using mass conservation. Under it, 8.4.A.1 states that a difference in pressure between two locations causes a fluid to flow, with two sub-statements: 8.4.A.1.i, the rate at which matter enters a fluid-filled tube open at both ends must equal the rate at which matter exits it, and 8.4.A.1.ii, the rate at which matter flows into a location is proportional to the cross-sectional area of the flow and the speed at which the fluid flows, with the derived equation V/T=AvV/T = Av. Then 8.4.A.2 states that the continuity equation for fluid flow describes conservation of mass flow rate in incompressible fluids, with the relevant equation A1v1=A2v2A_1 v_1 = A_2 v_2.
  • 8.4.B asks you to describe the flow of a fluid as a result of a difference in energy between two locations in a fluid within the fluid-Earth system. 8.4.B.1 states that a difference in gravitational potential energies between two locations in a fluid will result in a difference in kinetic energy and pressure between those two locations, described by conservation laws. 8.4.B.2 states that Bernoulli's equation describes the conservation of mechanical energy in fluid flow, and prints it. 8.4.B.3 states that Torricelli's theorem relates the speed of a fluid exiting an opening to the difference in height between the opening and the top surface of the fluid, and can be derived from conservation of energy principles, with the derived equation v=2gΔyv = \sqrt{2 g \Delta y}.

Note the CED's own labels. A1v1=A2v2A_1 v_1 = A_2 v_2 and Bernoulli's equation are marked relevant equations; V/T=AvV/T = Av and v=2gΔyv = \sqrt{2g\Delta y} are marked derived equations. The CED explains the difference: derived equations are printed in the framework for reference or to show the result of a derivation students are expected to be able to perform, and they are not on the equation sheet handed out with the exam. Check that against the AP Physics 1 equation sheet and it holds. The sheet prints seven fluid relations in total: ρ=m/V\rho = m/V, P=F/AP = F_{\perp}/A, P=P0+ρghP = P_0 + \rho g h, Pgauge=ρghP_{\text{gauge}} = \rho g h, Fb=ρVgF_b = \rho V g, A1v1=A2v2A_1 v_1 = A_2 v_2, and Bernoulli's equation. Torricelli's theorem is not among them, and neither is V/T=AvV/T = Av.

The CED lists five suggested skills for Topic 8.4, the same count it gives Topic 8.1 and one more than it gives Topics 8.2 and 8.3: 1.B, create quantitative graphs with appropriate scales and units, including plotting data; 2.A, derive a symbolic expression from known quantities by selecting and following a logical mathematical pathway; 2.C, compare physical quantities between two or more scenarios or at different times and locations in a single scenario; 3.A, create experimental procedures that are appropriate for a given scientific question; and 3.B, apply an appropriate law, definition, theoretical relationship, or model to make a claim. Unit 8 is weighted at 10 to 15 percent of the multiple-choice section, with a suggested 12 to 17 class periods.

Continuity is conservation of mass

Say it in those words, because that is what 8.4.A.2 says and it is what a justification question wants to hear. The continuity equation is not a fact about pipes. It is bookkeeping on matter: fluid cannot be created inside a full tube, and it cannot pile up, so whatever flows in per second must flow out per second.

Build it from the volume side. In a time TT, fluid moving at speed vv through a cross-section of area AA sweeps out a volume V=AvTV = Av T, so the volume flow rate is

VT=Av\frac{V}{T} = Av

which is 8.4.A.1.ii. That quantity has units of m3^3/s. For an incompressible fluid the density is fixed, so a constant volume per second is also a constant mass per second, and setting the rate at one location equal to the rate at another gives

A1v1=A2v2A_1 v_1 = A_2 v_2

The practical form is a ratio: v2=v1(A1/A2)v_2 = v_1 (A_1/A_2). Speed and area are inversely proportional, which is why the exam almost never wants you to compute an area in square meters.

Watch how area scales for a circular pipe, because this is where the arithmetic goes wrong. A=πr2A = \pi r^2, so doubling the radius multiplies the area by 4 and divides the speed by 4. The CED's own sample multiple-choice question for learning objective 8.4.A does exactly this: a fluid moves from a section of radius RR into a section of radius 2R2R, and the ratio of the speed in the wide section to the speed in the narrow section is 1/41/4. That question is aligned to skill 2.C, comparing quantities at different locations in a single scenario, and it needs no calculator at all.

Change to the pipeChange to the areaChange to the speed
Radius doublestimes 4times 1/4
Radius halvestimes 1/4times 4
Diameter times 3times 9times 1/9

The volume flow rate itself is the thing that does not change, and quoting it is often the fastest way to answer a question about how long a tank takes to fill.

What makes a fluid flow in the first place

Essential knowledge 8.4.A.1 states the cause plainly: a difference in pressure between two locations causes a fluid to flow. That sentence is the hinge between this topic and Topic 8.3, where learning objective 8.3.A asks about the conditions under which a fluid's velocity changes and the answer is a net force.

The two descriptions are the same physics at two altitudes. A parcel of fluid with higher pressure behind it than in front of it has a net force on it, so it accelerates: that is Newton's second law, Topic 8.3. Track the same parcel down the pipe and add up the work done on it, and you get Bernoulli's equation: that is conservation of energy, Topic 8.4.

This also fixes the order of work inside a problem. Continuity first, because it needs only geometry and gives you the speeds. Bernoulli second, because it needs the speeds and gives you the pressures.

Bernoulli is conservation of energy per unit volume

Essential knowledge 8.4.B.2 says Bernoulli's equation describes the conservation of mechanical energy in fluid flow. Here is the printed form:

P1+ρgy1+12ρv12=P2+ρgy2+12ρv22P_1 + \rho g y_1 + \tfrac{1}{2}\rho v_1^2 = P_2 + \rho g y_2 + \tfrac{1}{2}\rho v_2^2

Every term is an energy divided by a volume, which is why they can all be measured in pascals. Take the conservation of energy statement you already know and divide it by VV:

Mechanical energy termDivide by volumeBernoulli term
Kinetic energy 12mv2\tfrac{1}{2}mv^2m/V=ρm/V = \rho12ρv2\tfrac{1}{2}\rho v^2
Gravitational potential energy mgymgym/V=ρm/V = \rhoρgy\rho g y
Work done by the surrounding fluidforce times distance over volumePP

The check that convinces people: a pascal is a newton per square meter, and multiplying top and bottom by a meter turns that into a newton meter per cubic meter, which is a joule per cubic meter. Pressure is an energy density. Once you see that, the equation reads as a sentence rather than a formula: the total mechanical energy per cubic meter of fluid is the same at location 1 and location 2.

Two consequences carry most of the multiple-choice questions.

  • Along a horizontal flow, y1=y2y_1 = y_2, the height terms cancel, and pressure and speed trade off directly. Faster fluid means lower pressure. This is not because moving fluid "has less pressure" by nature; it is because the energy that went into 12ρv2\tfrac{1}{2}\rho v^2 had to come out of PP.
  • In a fluid at rest, all the vv terms are zero and Bernoulli collapses to P1+ρgy1=P2+ρgy2P_1 + \rho g y_1 = P_2 + \rho g y_2, which rearranges into P=P0+ρghP = P_0 + \rho g h from Topic 8.2. The static pressure relation is the special case of Bernoulli with nothing moving, which is worth knowing if only because it means one fewer equation to trust.

One bookkeeping rule: pick a reference height for yy, and a pressure convention, gauge or absolute, before you substitute, then use the same choice on both sides. Only differences in yy appear, so the zero can go anywhere, but it cannot move partway through a problem.

Torricelli's theorem, and what a derived equation means

Essential knowledge 8.4.B.3 gives Torricelli's theorem, v=2gΔyv = \sqrt{2g\Delta y}, for the speed of fluid leaving an opening a height Δy\Delta y below the top surface, and states that it can be derived from conservation of energy principles. Since it is a derived equation rather than a relevant one, it is not printed on the equation sheet, so the derivation is the thing to own.

Put point 1 at the top surface and point 2 at the opening. Both are open to the atmosphere, so P1=P2P_1 = P_2 and the pressure terms cancel. If the tank is wide compared with the hole, continuity makes the surface's speed negligible next to the jet's, so v10v_1 \approx 0. What is left is

ρgy1=ρgy2+12ρv22\rho g y_1 = \rho g y_2 + \tfrac{1}{2}\rho v_2^2

The density cancels from every term, leaving v2=2g(y1y2)=2gΔyv_2 = \sqrt{2g(y_1 - y_2)} = \sqrt{2g\Delta y}.

That result is worth a second look: it is the same speed an object would reach after falling freely through the same height, and it does not depend on the fluid's density at all. Mercury and water leave a hole at the same depth at the same speed. Students expect the heavier fluid to shoot out faster, and the cancellation on line 3 is the answer to why it does not.

Two cautions. The approximation v10v_1 \approx 0 is an approximation, and it is only good while the hole is small compared with the tank. And Δy\Delta y is measured from the fluid surface down to the hole, not from the floor, not from the top of the container.

The boundary statement, and the exception it carries

Topic 8.4 is the only topic in Unit 8 with a boundary statement, and it is one sentence: all fluids will be assumed to be ideal, and all pipes are assumed to be completely filled by the fluid, unless otherwise stated.

The last three words are part of the rule. "Unless otherwise stated" means a question is free to hand you a fluid that is not ideal, and if it does, the assumptions below stop applying. Do not read the boundary statement as a promise that non-ideal fluids never appear; read it as the default when a question is silent.

What ideal means is fixed elsewhere in the unit. Essential knowledge 8.1.A.4 defines an ideal fluid as incompressible and having no viscosity, and 8.2.A.3 adds that the volume and density of a given amount of an incompressible fluid are constant regardless of the pressure exerted on it. Put together, the default gives you three things:

  • No viscosity. No internal friction, so no energy is lost to the fluid rubbing against itself or the pipe walls, which is what lets Bernoulli's equation be an equality rather than an inequality.
  • Incompressible. The density is the same at every point, which is what lets the single symbol ρ\rho appear on both sides of Bernoulli's equation and what turns a constant volume flow rate into a constant mass flow rate.
  • Pipes completely filled. No air gaps, so the cross-sectional area in A1v1=A2v2A_1 v_1 = A_2 v_2 really is the pipe's area.

Be careful about one thing this page cannot tell you: the AP Physics 1 CED does not use the word turbulence anywhere, so do not write that the course "excludes turbulent flow" as though quoting a rule. What the CED excludes by default is viscosity and compressibility, in the words above.

Graphs, experiments, and where skill 1.B lands

Two of Topic 8.4's five suggested skills point straight at the laboratory: 1.B, create quantitative graphs with appropriate scales and units, including plotting data, and 3.A, create experimental procedures appropriate for a given scientific question. Topic 8.1 is the only other topic in Unit 8 that lists either of them. Take that as a warning that this topic is a natural home for an experimental free-response question.

It is not a hypothetical warning. The sample free-response set in the CED includes an Experimental Design and Analysis question aligned to learning objectives 1.5.B, 8.2.B, and 8.4.B. Students are given a cylinder of liquid, meter sticks, and a pressure sensor but no scale, and asked to design a linear-graph method for the liquid's density; then a second cylinder of water has a small hole punched at various heights, the exit speed is measured at each, and the students are asked to plot v2v^2 against a quantity of their own choosing so the graph comes out linear, and to get a value for gg from it.

That second part is the graph to be able to build cold. Square Torricelli's theorem:

v2=2gΔyv^2 = 2g\,\Delta y

Plot v2v^2 on the vertical axis and Δy\Delta y on the horizontal axis and you get a straight line through the origin whose slope is 2g2g, so gg is half the slope. Notice what the linearization bought: the raw vv against Δy\Delta y plot is a curve, and you cannot read a physical constant off a curve by eye. Choosing which quantity to square so that a graph comes out linear is the recurring move in AP Physics 1 experimental questions, and the third worked example below runs the numbers.

The CED also suggests a Bernoulli bar-chart activity here: draw bars for PP, ρgy\rho g y, and 12ρv2\tfrac{1}{2}\rho v^2 at two or more points in a flow, then defend a claim about the pressure using the chart as evidence. Bar charts make the conservation statement visible, because the three bars must add to the same total at every point.

Traps that cost points

  • Using continuity on a compressible flow. A1v1=A2v2A_1 v_1 = A_2 v_2 is stated in 8.4.A.2 for incompressible fluids. What is conserved in general is the mass flow rate; the areas-and-speeds form is the incompressible special case.
  • Adding an area to a Bernoulli equation. Bernoulli has no AA in it. Areas enter only through continuity, which supplies the speeds you then substitute.
  • Mixing gauge and absolute pressures across the equal sign. Both are fine, but a 1.0×1051.0 \times 10^5 Pa discrepancy is the classic result of using one on each side.
  • Assuming faster always means lower pressure. That shortcut is only true when the height terms cancel. In a pipe that both narrows and climbs, the speed term and the height term can push the pressure in opposite directions, and only the arithmetic settles it.
  • **Forgetting that vv in Torricelli's theorem is the exit speed, not a final speed.** Fluid leaving a hole horizontally is a projectile from that moment on, and how far it travels is a separate projectile motion question.
  • Writing the density into a Torricelli answer. It cancels. If ρ\rho survives to your final expression for exit speed, an algebra step went wrong.

How Topic 8.4 is tested, and where it leads

The recurring question shapes, mapped to the CED's suggested skills for this topic:

  1. Given a change in a pipe's radius or area, give the factor by which the speed changes, with no numbers (skill 2.C).
  2. Run continuity and then Bernoulli through a pipe that changes both width and height, and find a pressure (skills 2.A and 2.C).
  3. Derive Torricelli's theorem from Bernoulli's equation, stating which terms you cancelled and why (skill 2.A).
  4. Choose axes that linearize fluid data, plot them, take a slope, and turn it into a physical quantity (skill 1.B).
  5. Design a procedure to measure a fluid property with the equipment listed, then say what you would graph (skill 3.A).
  6. Justify a claim about pressure at two points in a flow, using conservation of mass and conservation of energy by name (skill 3.B).

The sixth is the one that separates answers. "The pressure is lower because the fluid is faster" earns less than "the flow speeds up because the cross-sectional area decreased and mass is conserved, and the pressure must drop because the total mechanical energy per unit volume is conserved."

Topic 8.4 closes both Unit 8 and the course, and the CED calls Unit 8 the culminating unit, tying together threads woven through the whole year. Every piece here is borrowed: conservation of energy from Unit 3, and projectile kinematics from Unit 1 whenever a jet leaves a hole. The fluids guide has the standard routines, Topic 8.3 has the force side of the same physics, and the Unit 8 page shows how the four topics fit together.

A pipe that narrows and climbs: continuity first, then Bernoulli

Water (ρ=1000\rho = 1000 kg/m3^3) flows through a pipe of radius 6.0 cm at 1.5 m/s, where the absolute pressure is 2.0×1052.0 \times 10^5 Pa. Further along, the pipe has narrowed to a radius of 3.0 cm and risen 2.0 m. Find the volume flow rate, the speed in the narrow section, and the absolute pressure there.

  1. Areas: A1=π(0.060)2=1.13×102A_1 = \pi (0.060)^2 = 1.13 \times 10^{-2} m2^2 and A2=π(0.030)2=2.83×103A_2 = \pi (0.030)^2 = 2.83 \times 10^{-3} m2^2. The radius halved, so the area is one quarter of what it was.

  2. Volume flow rate: V/T=A1v1=(1.13×102)(1.5)=1.70×102V/T = A_1 v_1 = (1.13 \times 10^{-2})(1.5) = 1.70 \times 10^{-2} m3^3/s, about 17 litres per second. This is the quantity that stays the same everywhere in the pipe.

  3. Continuity for the speed: v2=v1(A1/A2)=(1.5)(4)=6.0v_2 = v_1 (A_1/A_2) = (1.5)(4) = 6.0 m/s. Check it against the flow rate: A2v2=(2.83×103)(6.0)=1.70×102A_2 v_2 = (2.83 \times 10^{-3})(6.0) = 1.70 \times 10^{-2} m3^3/s, which matches.

  4. Set up Bernoulli with the low section as point 1 and y1=0y_1 = 0, so y2=+2.0y_2 = +2.0 m: P2=P1+12ρ(v12v22)+ρg(y1y2)P_2 = P_1 + \tfrac{1}{2}\rho(v_1^2 - v_2^2) + \rho g (y_1 - y_2).

  5. Evaluate the terms separately. 12ρv12=(0.5)(1000)(1.5)2=1125\tfrac{1}{2}\rho v_1^2 = (0.5)(1000)(1.5)^2 = 1125 Pa. 12ρv22=(0.5)(1000)(6.0)2=1.80×104\tfrac{1}{2}\rho v_2^2 = (0.5)(1000)(6.0)^2 = 1.80 \times 10^4 Pa. ρgΔy=(1000)(9.8)(2.0)=1.96×104\rho g \Delta y = (1000)(9.8)(2.0) = 1.96 \times 10^4 Pa.

  6. Combine: P2=2.0×105+11251800019600=1.63525×105P_2 = 2.0 \times 10^5 + 1125 - 18000 - 19600 = 1.63525 \times 10^5 Pa.

  7. Read the two losses. About 16.9 kPa of pressure paid for the extra speed and another 19.6 kPa paid for the climb. Both terms grew at the pressure's expense, which is what conservation of energy per unit volume means here.

V/T=1.70×102V/T = 1.70 \times 10^{-2} m3^3/s, v2=6.0v_2 = 6.0 m/s, and P2=1.64×105P_2 = 1.64 \times 10^5 Pa to three significant figures. The pressure dropped by about 36 kPa, and the climb accounted for slightly more of that drop than the speed-up did. The same pipe with no rise would have given P2=1.83×105P_2 = 1.83 \times 10^5 Pa, so the ρgy\rho g y terms are not safe to drop unless the flow really is horizontal.

Torricelli, then projectile motion: where the jet lands

A large open tank of water has a small hole in its side, 1.8 m below the water surface. The hole is 1.0 m above the floor and the water leaves it horizontally. Find the exit speed, the volume flow rate through the hole if the hole is a circle 8.0 mm across, and how far from the tank the jet lands.

  1. The tank is open at the top and the hole opens to the air, so the pressures at both points are atmospheric and cancel in Bernoulli's equation. The tank is wide compared with the hole, so the surface speed is negligible. That leaves Torricelli's theorem, v=2gΔyv = \sqrt{2g\,\Delta y}, with Δy\Delta y measured from the surface down to the hole.

  2. Exit speed: v=2(9.8)(1.8)=35.28=5.94v = \sqrt{2(9.8)(1.8)} = \sqrt{35.28} = 5.94 m/s. The water's density never entered, so a tank of any liquid would give the same number.

  3. Hole area: A=π(0.0040)2=5.03×105A = \pi (0.0040)^2 = 5.03 \times 10^{-5} m2^2.

  4. Volume flow rate through the hole: V/T=Av=(5.03×105)(5.94)=2.99×104V/T = Av = (5.03 \times 10^{-5})(5.94) = 2.99 \times 10^{-4} m3^3/s, about 0.30 litres per second.

  5. The jet is now a projectile launched horizontally from 1.0 m up. Vertically, starting from rest in the vertical direction: 1.0=12(9.8)t21.0 = \tfrac{1}{2}(9.8)t^2, so t=2(1.0)/9.8=0.452t = \sqrt{2(1.0)/9.8} = 0.452 s.

  6. Horizontally the speed is constant: x=vt=(5.94)(0.452)=2.68x = vt = (5.94)(0.452) = 2.68 m.

The water leaves at 5.94 m/s, carrying 2.99×1042.99 \times 10^{-4} m3^3/s through the hole, and lands 2.68 m from the base of the tank. Two separate physics problems are stacked here, and the join is a single number: Bernoulli's equation supplies the launch speed, and everything after that is projectile motion with no fluid physics in it at all.

Linearizing a Torricelli experiment to measure g

Students punch a hole at five different depths in the side of a water-filled cylinder and measure the exit speed vv at each depth hh below the surface. They record: (0.10 m, 1.38 m/s), (0.20 m, 1.95 m/s), (0.30 m, 2.40 m/s), (0.40 m, 2.78 m/s), (0.50 m, 3.10 m/s). Choose axes that give a straight line, find the slope, and get an experimental value for gg.

  1. Torricelli's theorem gives v=2ghv = \sqrt{2gh}, which is a curve on a vv against hh plot. Square both sides to linearize: v2=2ghv^2 = 2gh. Plotting v2v^2 against hh should give a straight line through the origin with slope 2g2g.

  2. Square each speed: 1.382=1.901.38^2 = 1.90, 1.952=3.801.95^2 = 3.80, 2.402=5.762.40^2 = 5.76, 2.782=7.732.78^2 = 7.73, 3.102=9.613.10^2 = 9.61, all in m2^2/s2^2.

  3. Label the axes with units, m2^2/s2^2 vertically and m horizontally, and plot the five points. They fall close to a straight line through the origin, which supports the model.

  4. Take the slope from two widely separated points on the best-fit line, here the first and last: slope =(9.611.90)/(0.500.10)=7.71/0.40=19.3= (9.61 - 1.90)/(0.50 - 0.10) = 7.71/0.40 = 19.3 m/s2^2.

  5. The slope is 2g2g, so g=19.3/2=9.6g = 19.3/2 = 9.6 m/s2^2.

  6. Compare with the accepted 9.8 m/s2^2 on the AP table of information: the experimental value is under 2 percent low, consistent with a jet losing a little speed on the way out of a real hole, which the ideal-fluid model does not account for.

Plot v2v^2 against hh. The slope is 19.3 m/s2^2, and since Torricelli's theorem in squared form is v2=2ghv^2 = 2gh, half the slope gives g=9.6g = 9.6 m/s2^2. The transferable move is the first step: when a relation contains a square root, square the measured quantity so the graph comes out linear, then read the physics off the slope rather than off any single data point.

Frequently asked questions

What does the continuity equation mean in AP Physics 1?

It means mass is conserved in a flowing fluid. Essential knowledge 8.4.A.2 states that the continuity equation describes conservation of mass flow rate in incompressible fluids, and it is written A1 v1 = A2 v2. Because the fluid cannot pile up or disappear inside a full tube, whatever volume passes one cross-section each second passes every other cross-section each second, so where the pipe is narrower the fluid must move faster.

Which conservation law is Bernoulli's equation?

Conservation of energy. Essential knowledge 8.4.B.2 states that Bernoulli's equation describes the conservation of mechanical energy in fluid flow. Each of its three terms is an energy per unit volume: (1/2) rho v squared is kinetic energy per volume, rho g y is gravitational potential energy per volume, and the pressure term accounts for work done by the surrounding fluid. That is also why every term can be measured in pascals, since a pascal is a joule per cubic meter.

Why does pressure drop where a fluid speeds up?

Because the total mechanical energy per unit volume is conserved. Along a horizontal flow, the height terms in Bernoulli's equation are equal on both sides and cancel, so any increase in the (1/2) rho v squared term must be paid for by a decrease in the pressure term. The rule only holds when the heights match; in a pipe that both narrows and rises, the speed and height terms can pull the pressure in opposite directions.

What is an ideal fluid in AP Physics 1?

An ideal fluid is incompressible and has no viscosity, which is essential knowledge 8.1.A.4. The Topic 8.4 boundary statement then says all fluids will be assumed to be ideal, and all pipes are assumed to be completely filled by the fluid, unless otherwise stated. That last clause matters: the assumption is a default for silent questions, not a guarantee, so a question is free to state a non-ideal situation and expect you to notice.

Is Torricelli's theorem on the AP Physics 1 equation sheet?

No. The CED marks v = the square root of 2 g times delta y as a derived equation, and derived equations appear in the course framework for reference or to show the result of a derivation students are expected to perform, not on the equation sheet given out with the exam. The two Topic 8.4 relations that are printed on the sheet are the continuity equation and Bernoulli's equation, and Torricelli's theorem comes out of Bernoulli's equation in about three lines.

If a pipe's radius doubles, what happens to the fluid's speed?

It falls to one quarter of its previous value. The cross-sectional area of a circular pipe goes as the radius squared, so doubling the radius multiplies the area by 4, and continuity, A1 v1 = A2 v2, then divides the speed by 4. The CED's own sample multiple-choice question for this learning objective uses exactly this setup, with a fluid passing from a section of radius R into a section of radius 2R.

Does the density of the liquid affect how fast it shoots out of a hole?

No. Deriving Torricelli's theorem from Bernoulli's equation, the density appears in every remaining term and cancels, leaving a speed equal to the square root of 2 g times the depth of the hole below the surface. That is the same speed an object would reach falling freely through the same height. Mercury and water leave identical holes at identical depths at identical speeds, so if density survives in your final expression, an algebra step went wrong.