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Pump - 3 EBook Package
ESBN: C60-592B-3b38-70C3 |
| Description:
Pump selection, installation, maintenance and repair ... from a maintenance engineer that got fed
up with pumping problems! NEW, ENHANCED "Pumps E-Book Package", a 3 volume set of E-Books from pumping basics to pump solutions.
A
must have for facility maintenance, mechanical engineering, chemical industry, marine engineers and the oil refinery.
This E-book package will help you out with that pool pump, submersible pump, chemical pump, well pump, heat pump, sump pump
and water pumps in general.
For a limited time receive 3 E-Books as a set for only US$35.00! |
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Download E-books immediately after purchase |
Price: US$125 NOW US$35.00 (Free ebook about
downtime cost with every order. For a total of 4 ebooks!) |
| Centrifugal Pump Problems & Answers |
| ESBN: C60-592B-1A38-60B0 |
| Description:
If you have a centrifugal pump problem, the odds are Mike Sondalini has included the solution in this
very detailed e-book - "Centrifugal Pump Problems & Answers".
Mike goes through the problem solving steps in detail
with his own experiences and research. Although this book primarily focuses on the centrifugal pump, many of the solutions
are applicable to well... pumps in general.
With over 50 sections, we can only list a few here. Some of the areas of
discussion are flow, mechanical seal, bearings, rotor, cavitations, liquid density, couplings, vibration isolation, fan, metal
corrosion, impeller, balancing, alignment and even the effects on electric motors.
If you have a centrifugal pump problem, Mike has the solution. Get a copy of "Centrifugal
Pump Problems & Answers" now |
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Download E-book immediately after purchase |
Price: US$35 NOW US$15.00 |
The free online e-book sample below is copyright protected. You may not modify, publish,
transmit, display, participate in the transfer or sale, create derivative works, or in any way exploit, any of the free online
ebook sample content, in whole or in part.
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ABSTRACT
When spinning equipment is out of balance. Vibration from out-of -balance rotating equipment can be frightening.
The ground shakes, machines jump about, hold down bolts come loose and parts break. An unbalanced rotating body will produce
forces on its bearings and transmit them throughout its structure and into the foundations.
Keywords: rotor, centrifugal forces, balance quality. |
CAUSES OF OUT-OF-BALANCE
Below lists some common causes for unbalance.
The drawings below provide examples of some of the problems listed in the table above.
Example only...
| Pump Types Explained |
| ESBN: C60-592B-1A38-60B2 |
| Description:
If you own, work with or are studying a water pump, sump pump, pool pump, chemical pump, industrial
pump or any other type of pump, you will find the knowledge in this book by Mike Sondalini very valuable.
Mike gives
you insight to design, uses, installation, calibration, troubleshooting and maintenance for the various pump types in his
book titled "Pump Types Explained". Mike starts out with details about the centrifugal pump with pump curves, cavitations
and how to correct the situation.
In addition to the centrifugal pump chapters, the peristaltic pump (hose pump), metering
pump (dosing pump), gear pump, helical pump and the magnetic drive pump are explained. Of special interest during the design
phase is Mike's cost / accuracy guide to pump types.
Learn how to choose the right pump for the job, get a copy of "Pump Types
Explained" now! |
|
Download E-book immediately after purchase |
Price: US$19.99 NOW US$12.50 |
The free online ebook sample below is copyright protected. You may not modify, publish,
transmit, display, participate in the transfer or sale, create derivative works, or in any way exploit, any of the free online
ebook sample content, in whole or in part.
|
ABSTRACT
Gear pump operation & maintenance. A gear pump uses two meshing, toothed cogs to force liquid from the
inlet of the pump through to the outlet. Being a positive displacement pump there deliver very precise quantities for each
revolution and this means they have good dosing characteristics regardless of their speed or the pressure into which they
discharge.
Keywords: internal, external teeth, pressure relief, viscosity. |
Figure No. 1 shows a simplified drawing of an external teeth gear pump on the left along with the alternate arrangement
of internally pointing teeth.
Figure No. 1. External and Internal Teeth Gear Pumps
GEAR PUMP DESIGN
Gear pumps use toothed gears turning inside a close tolerance housing to draw-in liquid and then squeezing it out ahead
of them. Paddle steamers used the same principle of operation. These pumps are positive displacement pumps and anything drawn
into them will be forced out. As a consequence they can generate very high discharge pressures. Materials of construction
vary from metals of various types and hardness through to plastics of various types and hardness.
Maintaining the close tolerances between the housing and the cogs is critical to efficient operation. The clearance
between the edges, of the teeth and the housing and the ends of the cogs and the back and front walls of the housing are very
small. Between the teeth and housing it is in the order of 0.1 mm (0.004”) while the clearances between the front and
back faces of the gears and the ends of the housing are only 0.025 mm (0.001”). The fine clearances reduce liquid re-circulation
back from the high-pressure discharge to the low-pressure suction side and make these pumps one of the most efficient available.
Gear pumps usually have one shaft penetration through the housing for connection to the drive. The gear shafts on
the smaller pumps can be supported in journal bearings within the ends of the housing and are lubricated by the product. On
larger pumps rolling element bearings mounted in bearing housings are used. To prevent surface to surface contact of teeth
the product provides the lubrication.
Continued in "Pump Types Explained" E-Book ...
Price: US$19.99 NOW US$12.50
The free online ebook sample below is copyright protected. You may not modify, publish,
transmit, display, participate in the transfer or sale, create derivative works, or in any way exploit, any of the free online
ebook sample content, in whole or in part.
Liquids do not all behave the same. Blood has different flow characteristics than water. Paint
flows differently to gasoline petrol. Liquids are categorized by their behaviors
when undergoing shear. Those liquids that have a constant shear rate with change
of velocity (like water) are called Newtonian ( Newton first developed the mathematical
explanation for the phenomenon). Those with shear rates that vary with changing
velocity (like paint and blood) are Non-Newtonian. The shear rate is a measure
of a fluid’s viscosity or slipperiness.
The density
of a fluid affects its viscosity. Fluids with more mass per unit volume are heavier
and require more energy to move them and shear less easily. A temperature rise
decreases the viscosity and density of liquids.
The more
viscous, or less slippery, a fluid the harder it is to get shearing between layers.
The high viscosity prevents rapid velocity changes occurring between layers.
The sub layer in viscous fluids is thicker than in low viscosity fluids.
At low speeds the whole flow across a pipe is
laminar and the fluid slides over itself. As the speed becomes faster eddies
start to form and cross the fluid layers. A transition from laminar to turbulent
flow develops. At still higher velocities the flow in the core of the pipe becomes
turbulent with swirling eddies throughout. Figure 2 shows where the various flow
regions occur at a tank nozzle.
Figure 2.
The laminar sub layer is always present against the pipe wall. But as the velocity rises the energetic swirling eddies begin to impact more deeply and the sub layer begins
to thin. At still higher velocities the sub layer thins further and the taller
roughness peaks stick into the turbulent region. Where the sub layer covers the
roughness projections the wall is considered ‘smooth’. When the wall
roughness pokes out of the sub layer the wall is considered ‘rough’. This
means the same wall can be both smooth and rough depending on the fluid’s velocity.
Experiments have proven
the pressure loss along a pipe with laminar flow is proportional to the velocity (p µ V) where as for turbulent flow
the pressure loss is proportional to the square of the velocity (p µ V2).
A slower flow permits a thicker sub layer and creates a ‘smooth’ pipe wall.
This minimizes the losses along the pipe. There is a very much greater
loss of pressure in turbulent flow.
The pipe system designer
has to strike a practical balance between increasing the pipe diameter to reduce energy loss and keeping the diameter small
to lower installation costs.
Continued in Pumping Basics E-Book ...
Price: US$19.99 NOW US$12.50
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