1.1What you will learn1.21.1 Why we measure1.31.2 Definition of measurement1.41.3 The three elements of any measurement1.51.4 Physical quantities1.62.1 Fundamental physical quantities1.72.2 Derived physical quantities1.82.3 Physics and mathematics1.92.4 Systems of units1.102.5 The International System of Units (SI)1.112.6 Scientists who benefited humanity1.123.1 From the body to the instrument1.133.2 Examples of instruments, old and modern1.143.3 The vernier caliper — measuring length precisely1.15Lesson 4: Standard Units (Length, Mass, Time)1.164.1 The standard of length — the metre1.174.2 The standard of mass — the kilogram1.184.3 The standard of time — the second1.195.1 The idea1.205.2 Getting the unit from the dimensional formula1.215.4 Table of dimensional formulas1.225.5 Rules to remember ("Pay attention")1.236.1 Dimensional homogeneity1.246.3 Limits of the method (important!)1.25Lesson 7: Multiples and Submultiples of Units; Scientific Notation1.268.1 No measurement is perfect1.278.2 Sources of error1.288.3 Precautions when using a metre ruler1.298.4 Direct and indirect measurement1.30Extra worked problems1.31Summary2.1What you will learn2.21.1 Why study motion?2.31.2 Definition of motion2.41.3 Types of motion2.52.1 Why we need velocity2.62.2 Speed and velocity2.72.3 Converting units2.83.1 Uniform and non-uniform (variable) velocity2.93.2 Instantaneous and average velocity2.104.1 How to draw it2.114.2 Reading the displacement–time graph2.125.1 Definition2.135.2 A motion diagram: the car that gains 5 m/s every second2.145.3 Types of acceleration2.156.1 Reading the graph2.166.2 Analysing a multi-stage graph2.176.3 Extension — displacement from the v–t graph2.186.4 Motion (dot) diagrams2.19Short answers to typical discussion questions2.20Summary2.21Key Scientific Tables & Anatomical Diagrams Extracted from Official Curricula3.1What you will learn3.2Introduction3.31.1 What is force?3.41.2 Resultant force3.52.1 Observation and the old belief3.62.2 Statement of the law3.72.3 Consequences of the first law3.82.4 Inertia3.9Lesson 3: Momentum3.104.1 Statement3.114.2 Another statement of the law3.124.3 Definition of the newton3.134.4 Thinking exercise3.144.6 Life applications of the second law (force, time and change of momentum)3.154.7 The first law as a special case of the second3.165.1 Observations3.175.2 Statement3.185.3 Properties of action and reaction3.195.4 Applications3.20Short answers to typical discussion questions3.21Summary4.1What you will learn4.21.1 What is a fluid?4.31.2 Density (ρ)4.41.3 Relative density4.51.5 Applications of density4.6Lesson 2: Types of Liquid Flow4.72.1 Laminar (streamline) flow4.82.2 Turbulent flow4.92.3 Steady flow4.103.1 Volume flow rate and mass flow rate4.113.2 The continuity equation4.123.3 Everyday examples4.133.5 Enrichment: Bernoulli's principle4.144.1 Experiments showing viscosity4.154.2 Explanation: layers of a liquid4.164.3 The coefficient of viscosity (η)4.174.5 Applications of viscosity4.184.6 Think about it4.19Summary5.1What you will learn5.2Overview5.31.1 Definition5.41.2 Enrichment: heel against elephant5.52.1 Observations5.62.2 Deriving P = Pa + ρgh5.72.3 Consequences5.82.5 Balance of two immiscible liquids in a U-tube5.93.1 Atmospheric pressure5.103.2 The mercury barometer (Torricelli)5.113.3 Units of pressure5.123.4 Factors that do not affect the barometer height5.133.6 Enrichment: the ear at heights5.144.1 The manometer5.154.3 Applications of pressure5.165.1 Pascal's principle5.175.2 The hydraulic press5.185.3 Applications5.19Short answers to typical discussion questions5.20Summary6.1What you will learn6.21.1 Molecules in the three states of matter6.31.2 Brownian motion6.41.3 Intermolecular spaces6.5Lesson 2: The Variables of a Gas6.63.1 The experiment6.73.2 Boyle's law6.84.1 Do all gases expand equally?6.94.2 Charles's apparatus6.104.3 Charles's law6.115.1 The experiment6.125.2 Jolly's apparatus6.135.3 The pressure law6.146.1 Absolute zero from Charles's law and from the pressure law6.156.2 Remarks6.166.3 Relation between Celsius and Kelvin6.177.1 Combining the three laws6.187.2 Enrichment: the ideal gas equation6.197.3 Standard temperature and pressure (STP)6.20Summary and relations1.1What you will learn1.2Lesson 1: The Concept of Physical Measurement1.3Lesson 2: Fundamental and Derived Quantities, and Systems of Units1.4Lesson 3: Measuring Instruments1.5Lesson 4: Standard Units (Length, Mass, Time)1.6Lesson 5: Dimensional Formula1.7Lesson 6: Using Dimensions to Test Equations1.8Lesson 7: Multiples and Submultiples of Units; Scientific Notation1.9Lesson 8: Measurement Error1.10Extra worked problems1.11Summary4.1What you will learn4.2Lesson 1: Fluids and Density4.3Lesson 2: Types of Liquid Flow4.4Lesson 3: Flow Rate and the Continuity Equation4.54.1 Experiments showing viscosity4.64.2 Explanation: layers of a liquid4.74.3 The coefficient of viscosity (η)4.84.4 Worked examples4.94.5 Applications of viscosity4.104.6 Think about it4.11Summary5.1What you will learn5.2Overview5.3Lesson 1: Pressure5.42.1 Observations5.52.2 Deriving P = Pa + ρgh5.62.3 Consequences5.72.4 Worked examples5.82.5 Balance of two immiscible liquids in a U-tube5.9Lesson 3: Atmospheric Pressure and the Barometer5.10Lesson 4: The Manometer and Applications of Pressure5.11Lesson 5: Pascal's Principle and the Hydraulic Press5.12Short answers to typical discussion questions5.13Summary| Property | Liquids | Gases |
|---|---|---|
| Compressibility | resist compression almost completely (incompressible) | easily compressed |
| Volume | definite volume | occupy any space available to them |
| Shape | take the shape of the container | take the shape and volume of the container |
| Comparison aspect | Main idea | Keywords |
|---|---|---|
| SI unit |
| 1000 |
| Dimensional formula | ML−3 | |
| • | Why does density differ from one material to another? | doesdensitydiffermaterial |
| Comparison aspect | Main idea | Keywords |
|---|---|---|
| • | It is a ratio of two quantities of the same kind → it has no unit (and no dimensions) | ratioquantitiessamekind |
| • | Its numerical value equals the density in g/cm3 | numericalvalueequalsdensity |
| Example 1. |
| liquidvolumemassrelative |
| Example 2. |
| Findmasslitresmercury |
| Example 3. |
| ironblockdimensionsmass |
| Example 4. |
| relativedensitycertain1000 |
| Comparison aspect | Main idea | Example | Keywords |
|---|---|---|---|
| Charge state of a car battery. |
| — | electrolytedilutesulphuricacid |
| Medicine. |
| — | Blooddensitynormallylies |
| Gold jewellery (critical thinking). |
|
| PurecaratdensityAlloys |
| Laminar flow | Turbulent flow |
|---|---|
| layers slide smoothly | eddies and irregular motion |
| streamlines do not intersect | no regular streamlines |
| quiet; can be steady | noisy; arises at high speed |
In a time Δt the liquid at that section advances a distance Δx = vΔt, so the volume crossing the section is ΔVol = AΔx = A v Δt.
| Comparison aspect | Main idea | Keywords |
|---|---|---|
| Example 2 (hose and nozzle). | Water leaves a hose of inner diameter 1.8 cm at 2 m/s through a nozzle of diameter 0.6 cm. Speed at the nozzle: (1.8/0.6)2 × 2 = 9 × 2 = 18 m/s | Waterleavesinnerdiameter |
| Example 3 (blood). |
| aortaradiusflowsbranches |
| Example 4 (time to fill). | A tap delivers water through a pipe of cross-section 1.5 cm2 at a speed of 4 m/s. Qv = 1.5 × 10−4 × 4 = 6 × 10−4 m3/s = 0.6 L/s. A 60 L tank fills in 60/0.6 = 100 s. | deliverswaterthroughpipe |
| Comparison aspect | Main idea | Keywords |
|---|---|---|
| Funnels. | Pour equal volumes of alcohol and glycerin into two identical funnels. Alcohol flows out faster — alcohol flows more easily than glycerin | Pourequalvolumesalcohol |
| Stirring. |
| waterhoneyglassmoves |
| Falling ball. |
| Dropidenticalsteelballs |
directly proportional to the velocity v of the moving plate,
directly proportional to the area A of the moving plate (in contact with the liquid), and
inversely proportional to the distance d between the plates.
F ∝ A v / d → F = η A v / d
| Comparison aspect | Main idea | Keywords |
|---|---|---|
| Unit | N·s/m2 (= Pa·s) = kg/(m·s) | |
| Dimensional formula | [F][d]/([A][v]) = MLT−2 · L / (L2 · LT−1) = ML−1T−1 | |
| • |
| dependstypeliquidtemperature |
| Example 1 — finding η. | A plate of area 0.04 m2 moves at 0.1 m/s over a layer of oil 2 mm thick when a force of 0.5 N is applied. η = Fd/(Av) = 0.5 × 0.002 / (0.04 × 0.1) = 0.001/0.004 = 0.25 N·s/m2 | plateareamovesover |
| Example 2 — finding the force. |
| liquidliesbetweenplates |
| Comparison aspect | Main idea | Keywords |
|---|---|---|
| Example 3 — effect of doubling. |
| distancebetweenplatesdoubled |
| Example 4 — comparing liquids. | To move the same plate at the same velocity needs a force of 0.3 N in oil A and 1.2 N in oil B. Then ηB/ηA = 4: oil B is four times as viscous. | movesameplatevelocity |
| Comparison aspect | Main idea | Keywords |
|---|---|---|
| Lubrication. |
| Machinepartsmustoiled |
| Moving vehicles. |
| reachesmaximumspeedmost |
| Medicine — the blood sedimentation rate. |
| ballfallingliquidacted |
| Comparison aspect | Main idea | Keywords |
|---|---|---|
| Choosing engine oil |
| viscositymustsuitworking |
| Drip irrigation / pipe networks | designers use the continuity equation to choose pipe diameters so that the desired flow rate and pressure reach every outlet | designerscontinuityequationchoose |
| Comparison aspect | Main idea | Keywords |
|---|---|---|
| Fluids flow |
| liquidsgasesrelativedensity |
| Laminar flow |
| smoothlayersstreamlinesnever |
| Steady flow |
| tubefullsameamount |
| • | Qv = Av (m3/s); Qm = ρAv (kg/s); Vol = Avt = πr2vt; M = ρAvt. | πr2vtρAvt |
| Continuity equation | A₁v₁ = A₂v₂ (v inversely proportional to A) | A₁v₁A₂v₂inverselyproportional |
| Bernoulli (enrichment) | faster flow → lower pressure (lift on a wing) | fasterflowlowerpressure |
| Viscosity |
| resistancebetweenlayersunit |
| Comparison aspect | Main idea | Keywords |
|---|---|---|
| Laminar vs Turbulent Flow |
| Streamlinesmoothfluidlayer |
| Streamlines and Flow Rates | A streamline is the continuous curve tangent to velocity vectors of fluid particles. Volumetric flow rate Qv = A v (m3/s). Mass flow rate Qm = ρ A v (kg/s). | continuouscurvetangentvelocity |
| Equation of Continuity | Mathematical expression of mass conservation in steady incompressible flow: A₁ v₁ = A₂ v₂ (fluid velocity is inversely proportional to cross-sectional area) | Mathematicalexpressionmassconservation |
| Viscosity Coefficient (η) | The tangential force per unit area required to maintain unit velocity gradient between two parallel fluid layers unit distance apart: η = F d / (A v) in (N·s/m2 or Pa·s) | tangentialforceunitarea |
| Comparison aspect | Main idea | Keywords |
|---|---|---|
| Volumetric Flow Rate | Qv = A v (m3/s) | |
| Mass Flow Rate | Qm = ρ A v (kg/s) | |
| Continuity Equation | A₁ v₁ = A₂ v₂ | For circular tubes: r₁2 v₁ = r₂2 v₂ | circulartubes |
| Branching into n identical sub-pipes | A v = n (a vbranch) | vbranch |
| Viscous Shear Force | F = η (A v / d) |
| Comparison aspect | Main idea | Keywords |
|---|---|---|
| Why does a falling stream of tap water narrow as it descends? |
| Gravityacceleratesdownwardincreases |
| • |
| bloodvelocitydramaticallylower |
| Why are high-viscosity lubricants used in hot seasons? |
| Highertemperaturesthinmotor |
| Parameter | Laminar / Streamline Flow | Turbulent Flow |
|---|---|---|
| Velocity Regime | Moderate, below critical velocity limit | High, exceeding critical threshold |
| Streamline Paths | Orderly, parallel, never intersecting | Disordered swirling eddies and vortices |
| Flow Rate Stability | Constant volumetric and mass throughput | Fluctuating chaotic delivery |
| Governing Form | Governed strictly by continuity equation | Requires complex Navier-Stokes turbulence analysis |
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