PUMP SPECIFICATION COURSE

(PUMP SIZING

CURSO PRÁTICO ESPECIFICAÇÃO DE BOMBAS

Author: Engenharia e Cia: Cursos e Treinamentos
$750.00
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CURSO BOMBA CENTRÍFUGA
Aproveite e compre o curso conceitual BOMBAS CENTRÍFUGAS com 25% de desconto.
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CURSO PRÁTICO DIMENSIONAMENTO DE COMPRESSOR
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Exclusive Pump Sizing Software Included

ABOUT THE COURSE AUTHOR


Micelli Camargo is a Mechanical Engineer from UNIFEI – Federal University of Itajubá and holds a Master’s degree in Nuclear Technology from IPEN–USP (Institute for Energy and Nuclear Research at the University of São Paulo).


He is also a Specialist in Didactics and Methodology of Higher Education from Uniderp University and has an Executive MBA in Marketing from FGV – Fundação Getúlio Vargas.


He has more than 20 years of professional experience, including 16 years in the field of pumps and industrial equipment, working alongside sales and application engineers as well as serving as a technical instructor, delivering various training programs.


In 2016, he created the Engenharia & Cia channel, and since then he has been sharing technical content in engineering, from both a conceptual and a practical perspective.


In 2018, the first online course was launched, marking the beginning of Engenharia & Cia:

Courses and Training with its online programs.


In 2022, he began corporate training services, delivering dozens of sessions and training hundreds of professionals since then.


Today, he partners with companies in the pumps and mechanical seals sector such as OMEL, VALLAIR, and EMBRASEAL to provide training for their employees and clients.

MAIN CLIENTS – ENGENHARIA & CIA

PROGRAM CONTENT


In this course, we will cover the following topics:

1) Fluid Properties
1.1. What Is a Fluid?
1.2. Density
1.3. Specific Weight
1.4. Dynamic Viscosity
1.5. Kinematic Viscosity
1.6. Newtonian and Non-Newtonian Fluids
1.7. Apparent Viscosity
2) Fluid Statics
2.1. Pressure: Concept
2.2. Most Common Pressure Units
2.3. Absolute Pressure vs. Gauge (Manometric) Pressure
2.4. Static Pressure Calculation and Pressure Variation
2.5. Pressure Head: Concept
3) Fluid Kinematics
3.1. Steady-State vs. Transient Regimes
3.2. Laminar Flow, Turbulent Flow, and Reynolds Number
3.3. Large (Infinite) Reservoir Concept
3.4. Free Jet Concept
3.5. Flow Rate: Concept
3.6. Average Velocity: Concept
3.7. Continuity Equation
3.8. Mass Flow Rate and the Law of Conservation of Mass
4) Energy Equation
4.1. Fluid Mechanical Energy and Energy Head
4.2. Energy Equation and Total Dynamic Head (TDH)
4.3. Hydraulic Power, Shaft Power, and Pump Efficiency
5) Head Loss Calculation
5.1. Head Loss: Definition and Key Concepts
5.2. Distributed (Friction) Losses
5.2.1. Moody (Moody–Rouse) Diagram Method
5.2.2. Empirical-Formula Methods
5.2.3. Head-Loss per Unit Pipe Length Method
5.3. Local (Minor) Losses
5.3.1. Equivalent Length Method
5.3.2. Local Loss Coefficient (K-factor) Method
5.3.3. Differential Pressure Method
5.3.4. Nomograph (Nomogram) Method
5.4. Head Loss Due to Acceleration/Deceleration in Positive Displacement Pumps
6) Operation of a Centrifugal Pump
6.1. Typical Components
6.2. Types of Impellers
6.3. How a Centrifugal Pump Works
6.4. Typical Pumping Installation
6.5. Flooded-Suction vs. Non-Flooded (Suction Lift) Pumps
6.6. Characteristic Curves
6.7. System Curves and the Operating Point
6.8. BEP — Best Efficiency Point
6.9. Priming
6.10. Viscosity Corrections to Characteristic Curves
7) Cavitation and NPSH
7.1. What Is Cavitation?
7.2. Suction Head Calculation and NPSH Concepts— Flooded vs. Non-Flooded Pump
7.3. Operation of Centrifugal Pumps
7.4. Operating Point of Centrifugal Pumps — System Curve
7.5. Common Components in a Pumping Installation
7.6. Priming Concept
8) Step-by-Step Specification of Centrifugal Pumps
8.1. Sizing a Centrifugal Pump for a Conventional Pumping Installation
8.2. Sizing and Specification of a Centrifugal Pump for a Building Water Supply System with Storage Tanks
8.3. Sizing a Centrifugal Pump for a Sanitary Pumping System