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Pumping Stations Unit - II

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Page 1: Pumping Stations - WordPress.com · Pumping Stations Location of pumping stations •Proper location of pumping station requires a comprehensive study of the area to be served to

Pumping Stations

Unit-II

Page 2: Pumping Stations - WordPress.com · Pumping Stations Location of pumping stations •Proper location of pumping station requires a comprehensive study of the area to be served to

Introduction

The necessity of lifting wastewater or sewage arises under thefollowing circumstances

• When the area of a town is so low lying that it cannot be drainedby gravity to discharge into a sub-main or main unless the entiresewerage system in the other parts is installed correspondingly at lowlevel. In such circumstances, it is more economical to pump thesewage from the low lying area into the upper branch mains

• Pumping is restorted to, at intervals for a sewage system in a flatCountry, since laying of sewers at the designed grade continuouslyall along will mean expensive excavation.

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Necessity of lifting wastewater

• Pumping is resorted to when outfall sewer is at lower level than thebody of water into which it is to be discharged, or when the outfall islower than the entrance to the treatment plant.

• When a sewer has to go across a high ridge, it will moreeconomical to pump it into sewer laid across the slope of the ridgeat reasonable depth, rather than driving a tunnel.

• Pumping is required to take out sewage from the cellars or sub-basements of buildings, when the level of caller is much lower thanthe invert level of sewer to which drainage connection is to be made.

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Introduction

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Problems in Sewage Pumping

• The pumping of sewage is not as simple as pumping of water, sincethe following special problems are to be faced in sewage pumping.

• (i) Sewage has foul characteristics

• (ii) Sewage Contains a lot of suspended and floating materialsthese may make the running of pumps difficult and may causefrequent clogging of the pumps.

• Sewage contains organic and inorganic wastes which may causecorrosion and erosion of parts of the pumps and reduce the lifts ofthe pumps.

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Problems in Sewage Pumping

• The rate of flow of sewage varies continuously and hencepumping operation are to be adjusted accordingly.

• The size of sump is limited since large sized sumps willresult in the settlement of silts and organic matter at itsbottom

• The pumps should be of high order reliability since failureof pumps will lead to flooding which may cause unbearablenuisance.

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Problems in Sewage Pumping

Page 8: Pumping Stations - WordPress.com · Pumping Stations Location of pumping stations •Proper location of pumping station requires a comprehensive study of the area to be served to

Problems in Sewage Pumping

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Pumping Stations

Location of pumping stations

• Proper location of pumping station requires a comprehensivestudy of the area to be served to ensure that the entire area can beadequately drained.

• If a very large quantity of sewage is to be pumped, the site shouldbe nearer a stream, or a nallah or a storm water drain, into whichthe sewage could be discharged during emergencies such a break-down of the pumping plant, failure of power etc.

• If this precautions is not taken the station should be located andconstructed in such a manner that it will not be flooded at anytime. The storm water pumping station capacity. The station be solocated that if it is easily accessible under all weather conditions.

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Pumping Stations

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Elements of Pumping Stations

• Apart from the structure of the pump house, a sewage pumping stationconsists of the following elements:

• (i) Grit Channel or detritus pit

• (ii) Coarse and fine Screens

• (iii) Sump or Wet Well

• (iv) Pump room or dry well

• (v) Pumps

• ( vi) Miscellaneous accessories such as pipes, valves, float-switcharrangements, float-switching arrangements, flow recorders,emergency overflows, ventilation arrangements such as extraction fansetc.

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Elements of Pumping Stations

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Pumping station

• Dry well :- For housing the pumps

• Wet well: - For incoming sewage.

• Rising main:- To led the pumped sewage to high leveled gravity sewer.

• Pumps used:- Centrifugal, Reciprocating, Propeller of axial flow, Air pressure pumps or ejectors

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Elements of Pumping Stations

Pump House Structure

• The pump house structure should be designed to withstandfloatation forces to which it may be subjected. The substructure ofthe pumping station may be of mass concrete or R.C.C while thesuperstructure may be constructed of any material. The internal walls& floors should be structurally designed to take the weight of machinealong with the live load of 5 kN/ m2. The building should beplanned and designed keeping in view the requirements ad thereshould be enough scope for future expansion.

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Pump House Structure

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Pump House Structure

• The building should contain wide passages, without any abrupt changesin levels. The building should possess enough ventilation so that foul gases,moisture etc. are easily carried out of the building.

• The ventilation equipment should have a minimum capacity of six airchanges per hour.

• The component of the building should be safe against vibrations causeddue to pumping machinery. In designing the substructure due to allowancesshould be made for earth pressure, water pressure, and uplift pressure.

• Natural or artificial illumination of the interior of the building shouldbe adequate. Dust proof, vapor Proof, fire proof and expansion proof,fixtures and luminaries should be provided. It is advisable to providestairs instead of ladders between different floors of the buildings Theuse of spiral stairs should be avoided as far as possible

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Pump House Structure• Grit Chamber or Detritus Pit

• The sewage entering into a pumping station contains a lot of Indestructible solidmatter such as grit, rags, sticks, faeces. Etc. all of which is in suspension as long as thesewage is flowing It is therefore essential to remove as much of this matter as possiblebefore pumping so as to minimize the wear and tear of the pump impeller and the risingmain.

• The grit is separated from the sewage by the provision of grit or detritus pit beforeor after the screens. A grit channel is a long basin with enlarged cross- section. Thisresults in the reduction of velocity of flow to 0.15 to 0.3 m/sec.

• The bottom of the pit is kept below the invert line of the sewer to allow thedeposition of the grit that will not interfere with a sewage flow through the pit. Thechannel or pit should have a minimum capacity of 1 % of daily dry weather flow. Thechannel or pit is designed to have a detention period of about 30 sec and the grit storagecapacity of 0.013 to 0.028 ,m3 per million ltres. There should be two such unit each ofwhich can be used, allowing the other to be cleaned. The grit collected is removedmanually once in a week in small installations, while in large installation, theremoval is continuous daily process by means of a series of perforated bucketsmounted or endless chain which is power driven

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Grit Chamber or Detritus Pit

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Screens

Screens

• After the removal of grit from the sewage, it is made to pass throughthe screens to trap the floating matter such as rags, sticks, paper, etc.

• It is necessary to remove these, otherwise they choke and damage thepumps. Screens are of two types: Coarse and fine. In large Installations, itis usual to provide both the coarse screen being the first to intercept theflow. Coarse screen is made up of wrought iron bars kept parallel toeach other and having a clear spacing of 50 to 100 mm in between them.

• The material trapped by coarse screen can be removed by hand raking.Fine screens should not trap any organic matter as far as possible.

• The screenings trapped by fine screens are removed by mechanicalrakes.

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Screens

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Sump Well

Sump Well

• Pumping Station are provided with two separate wells: Wet Wellfor receiving the incoming sewage and dry well for housing thepumps.

• The function performed by a sump or wet well are to act as asuction pit from which pumps draw sewage and as equalizingbasin to minimize the load fluctuations on the pumps. The sump (orwet well ) is provided either below the floor of a pump house or byside of dry wells,

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Sump Well

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Sump Well

• The sump is so designed that the sewage can collect in it for a time therise in the level operates a float switch which s suction linetarts thepumping unit and the sewage is operated at very frequent intervals dueto smaller capacity of sump. Usually a detention period of 30 min ofsewage flow is adopted in design. The shape of wet well and thedetention time provided for sewage stations shall be such thatdepositions of solids is avoided and sewage does not turn septic.

• The capacity of wet well is reckoned between the levels at which airaffects the suction line of the pump of minimum duty installed in thepump house and the designed sewer level in the incoming sewer, i.e. theportion of the well below the upper most starting point and the lower moststarting point. It is governed by the pump set installed to deal withvarying flow.

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Sump Well

In the dry well pumps are installed. The pump is locate end of thesuction pipe of pump is located near the bottom of wet well.

The motor room is situated above the pump rooms dry well.Apart from electric motors, it also accommodates otherappurtenances such as automatic starter flow recorder etc.

The flow recorders installed to know the quantity of sewagewhich is pumped per unit time, may be in the form ofrectangular weir, standing wave flume, triangular weir or venturemeter. The flow can also be recorded by suitable electrical device.

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Rising Main Valves & fittings

• Rising Main valves & fittings

• The pumped sewage is led to high levelled gravity sewer through risingmains.

• The rising mains are made up of steel, cast iron spun iron or asbestoscement pressure pipes, Generally, cast iron pipes with flanged joints areprovided. The flanged joint provide easiness in dismantling the repair ofpumping station equipment. The length of the discharge pipe should bekept as small as possible beause long detention of sewage in closed pipesunder pressure causes their anaerobic deterioration. As far as possiblerising main should rise steadily from the pumping stations to the point ofdischarge. The velocity of flow in the rising main should not be less than0.75 m/sec. As the same time velocities higher than 2 m/sec should beavoided.

• For economic design, the velocity of 0.85 m/sec for normal rate ofpumping is desirable.

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Rising Main Valves & fittings

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Rising Main Valves & fittings

• A reflux or non- return valve is fitted on the rising main, just nextto the pump, to prevent a backflow through the pump when the pumpis stopped.

• Check valve should be provided in the sewer line discharging thesewage, to prevent the back flow of sewage during floods in the riveror discharge area.

• Gate valves should be provided on the sewer line just before thewet well and on the suction and discharging pipe to close the flowof sewage during maintenance, inspection and repair of the pumps.

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Rising Main Valves & fittings

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Check Valve & Gate Valve

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Check Valve & Gate Valve

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Types of Pumps

• Following are the types of pumps commonly used forsewage and storm water pumping

• (i) Centrifugal pumps

• (ii) Reciprocating pumps

• (iii) Propeller or axial flow pumps

• (iv) Air Pressure pumps or ejectors

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Types of Pumps

Centrifugal Pump

• Centrifugal pumps are most widely used for pumping sewage andstorm water, as these can be easily installed in pits and sumps, andcan easily transported the suspended matter in the sewage withoutgetting clogged too often . These pumps work on the principle ofcentrifugal force, These essential consists of two main parts

• (i) The casing and

• (ii) The impeller

• The impeller rotates with high speed inside the casing

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Centrifugal Pump

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Centrifugal Pump

The centrifugal pump can be classified under

(a) Axial flow pumps: Axial flow pumps develop most of their headby propelling action of the impeller vanes on the liquid. They arecharacterized by a single inlet impeller with the flow entering axiallyand generally used for large installations with capacities greater than2000 m3/hr. and head less than 9 m. The pumps are generally ofvertical type. The axial flow pumps have relatively high specificspeed ranging from 8000 to 16000

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Axial flow pumps

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Mixed flow pump

Mixed flow pump

• The head developed by mixing flow pumps is partly bycentrifugal action and partly by the lift of the impellervanes on the liquid. The pump has a single inlet impellerwith the flow entering axially and discharging in an axial andradial direction, usually into a volume type casing. They areused for medium heads of 8 to 15 m and for medium tolarge capacities

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Mixed flow pump

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Radial flow pumps

• The head developed in these types of pumps is principally by theaction of force. Pump of this type can be obtained with eithersingle suction or double suction inlet impellers, the flow leaving theimpeller radially and normal to the shaft axis.

• These pumps are characterized by relatively low speeds, withsingle inlet impeller having specific speed less than 4200 anddouble suction units having specific speed less than 6000 singlesuction pumps are generally used for sewage and storm water pumpingas they are less susceptible to clogging

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Radial flow pumps

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Reciprocating Pumps

Reciprocating Pumps

• Reciprocating pumps are more or less obsolete in modern sewagepumping station since they are liable to be clogged by solids orfibrous material, even through sewage may have to pass throughcoarse screens. Also their initial cost is higher and efficiency is lowerthan those of a centrifugal pump. However, in cases where it isrequired to deal with difficult sludge's and where large quantity isto be pumped against low heads, reciprocating pumps may beused after passing the sewage through screen with 20 mm spacing.

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Reciprocating Pumps

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Reciprocating Pumps

• Reciprocating pumps are of two types

• (i) Ram Type

• (ii) Propeller Type

• In the ram type reciprocating pump, a piston or plunger moves throughgland displacing liquid in a vessel. The piston is not arranged to fit closelyin the cylinder .

• The diaphragm pump is an example of the ram type reciprocatingpump.

• Diaphragm pump is a ram type reciprocating pump. In this pump a piston orplunger is attached to the centre of a circular rubber diaphragm permits theup & down motion of the plunger

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Reciprocating Pumps

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Propeller or axial flow pumps

• Propeller or axial flow pumps

• The axial flow pump is sometimes called a propeller pump as itsimpeller resembles the propeller of a ship.

• The pump consists of a number of blades fixed like a screwthreads on a vertical shaft, and there are vanes both on the inletand outlet sides. When the propeller rotates, these wanes guide theflow axially along the shaft. The efficiency of axial flow pump isvery low, to the extent of about 25 % or so. These pumps aresuitable to pump large volumes of sewage against low head

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Propeller or axial flow pumps

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Air Pressure pump or pneumatic ejectors

Air Pressure pump or pneumatic ejectors

• Pneumatic ejectors work on the action of compressed air

• These are used for the following conditions:

• Where the small quantity of sewage is to be lifted from basementof buildings, to a high level sewer

• Where the quantity of waste water from the low lying area doesnot justify the construction of a pumping station

• Where centrifugal pumps of smaller capacity are likely to clogged.

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Air Pressure pump or pneumatic ejectors

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Advantages

• The ejector possess the following advantages

• (a) No sewer gases escape except through the vent shaft as sewageis completely enclosed

• (b) Operation is fully automatic and the ejector comes intooperation only when needed

• (c) Only a few part in contact with sewage thus necessitating littleattention or lubrication.

• (d) Ejector less susceptible to clogging

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Air Pressure pump or pneumatic ejectors

• The ejector consist of a cast iron chamber with a spindle having a bellat its upper end and a cup at its lower end. Two check valves V1 & V2are provided at entrance and exit ends respectively The Compressed airis supplied through this valve at a pressure of about 1.5 kg/ cm2

• The sewage enters through valve V1 and rises slowly in the chamber,the exit valve V2 and air inlet valve V3 being closed at this stage. As thelevel rises, the air from the chamber escapes through the exhaust. Whenthe sewage reaches the bottom of upper cup is entrapped. Further rise inlevel of sewage makes the entrapped air to exert vertical pressure on thespindle. Due to this , spindle is lifted up the lever is operated, the exhaust isclosed and air entrance valve V3 opened. The air entering under pressureforces the sewage inside the chamber to rise in the outlet pipe through theexit valve V2 which also opens at this stage while entrance valve V1 closes.The sewage in the chamber is discharged.

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Air Pressure pump or pneumatic ejectors

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Air Pressure pump or pneumatic ejectors

• When the sewage in the chamber is discharged. When thesewer level in the chamber fall below the cup, the weightof the sewage in the cup causes the spindle to be draggeddown, This cuts off the compressed air and open the ejectorto the atmosphere by opening the exhaust.

• The volume of air storage tank and the characteristics ofthe compressor should be adequate to provide at least 40% higher than that required to raise all the sewage to themaximum computed lift.

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Power for Pumps

Power for pumps

• Power for the operation of pump can be supplied by use of thefollowing

• (i) Stream engine

• (ii) Internal Combustion engine

• (iii) Electric Motors

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Power for Pumps

Steam engine

• Earlier, steam engine were used for the operation of pumps, butthey are not much in favor due to the following reasons

• They have large initial cost and are not economical unless their use ison the large scale such as in mine or forest area

• Because large number of moving parts, they have high maintenancecost.

• However steam power is more reliable.

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Internal Combustion engine

• Internal Combustion engine

• I.C engine may run either on diesel or gasoline. The initial cost ofdiesel engine is very high and they are difficult to start, and alsotheir speed is low

• Similarly the operational cost of gasoline engine is very high .

• Hence I.C engines are used only in emergency, or when electricpower is not available.

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Internal Combustion engine

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Electric Motor

• Electric motor

• Pumps are operated through electric motors, in themajority of the cases. They are very convenient and freefrom most of the objections mentioned above They arecompact, silent, automatic in action and free from nuisance ofsmoke. They occupy less building space and can beinstalled immediately above the pumps,

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Electric motor

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References

• Waste Water Engineering : Vol-II By B.C. Punamia

• Environmental Engineering : By Prof B.R.ShahProf A M Malek

• Internet Websites

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Thanks !