lesson 14_ sedimentation and flotation

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7/11/2014 Lesson 14: Sedimentation and Flotation http://w ater.me.v ccs.edu/courses/ENV110/Lesson14 print.htm 1/14 Lesson 14: Sedimentation and Flotation Objective In this lesson we will learn the following: How does sedimentation fit into the water treatment process? What zones are present in a sedimentation basin? How is sedimentation sludge disposed of? Reading Assignment Along with the online lesson, read Chapter 5: Sedimentation and Flotation in your textbook Operation of Wastewater Treatment Plants Volume I . Lecture Pr imar y Sedimentation Purpose Sedimentation is a treatment process in which the velocity of the water is lowered below the suspension v elocity and the suspended p articles settle out of th e water due to gravity . The pro cess is also known as settling or clarification  .

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Lesson 14:

Sedimentation and Flotation

Objective

In this lesson we will learn the following:

How does sedimentation fit into the water treatment process?What zones are present in a sedimentation basin?How is sedimentation sludge disposed of?

Reading Assignment

Along with the online lesson, read Chapter 5: Sedimentation and Flotation in your textbook Operation of Wastewater Treatment Plants Volume I .

Lecture

Primary Sedimentation

Purpose

Sedimentation is a treatment process in which the velocity of the water is lowered below thesuspension velocity and the suspended particles settle out of the water due to gravity. The processis also known as settling or clarification .

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Settled solids are removed as sludge, and floating solids are removed as scum. Wastewater leavesthe sedimentation tank over an effluent weir to the next step of treatment. The efficiency or

performance of the process is controlled by: detention time, temperature, tank design, and conditionof the equipment.

Most water treatment plants include sedimentation in their treatment processes. However,sedimentation may not be necessary in low turbidity water of less than 10 NTU. In this case,coagulation and flocculation are used to produce pinpoint (very small) floc which is removed fromthe water in the filters.

Location in the Treatment Process

The most common form of sedimentation follows coagulation and flocculation and precedesfiltration. This type of sedimentation requires chemical addition (in the coagulation/flocculation step)and removes the resulting floc from the water. Sedimentation at this stage in the treatment processshould remove 90% of the suspended particles from the water, including bacteria. The purpose of sedimentation here is to decrease the concentration of suspended particles in the water, reducingthe load on the filters.

Sedimentation can also occur as part of the pretreatment process, where it is known aspresedimentation . Presedimentation can also be called plain sedimentation because the

process depends merely on gravity and includes no coagulation and flocculation. Withoutcoagulation/flocculation, plain sedimentation can remove only coarse suspended matter (such asgrit) which will settle rapidly out of the water without the addition of chemicals. This type of sedimentation typically takes place in a reservoir, grit basin, debris dam, or sand trap at the

beginning of the treatment process.

While sedimentation following coagulation/flocculation is meant to remove most of the suspended particles in the water before the water reaches the filters, presedimentation removes most of the

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sediment in the water during the pretreatment stage. So presedimentation will reduce the load onthe coagulation/flocculation basin and on the sedimentation chamber, as well as reducing the volumeof coagulant chemicals required to treat the water. In addition, presedimentation basins are useful

because raw water entering the plant from a reservoir is usually more uniform in quality than water entering the plant without such a holding basin.

The rest of this lesson will be concerned with sedimentation following coagulation and flocculation.

We will consider types of sedimentation basins and parts of a typical sedimentation basin, as well asthe disposal of sludge.

Types of Basins

Three common types of sedimentation basins are shown below:

Rectangular basins are the simplest design, allowing water toflow horizontally through a long tank. This type of basin isusually found in large-scale water treatment plants. Rectangular

basins have a variety of advantages - predictability, cost-effectiveness, and low maintenance. In addition, rectangular

basins are the least likely to short-circuit, especially if the lengthis at least twice the width. A disadvantage of rectangular

basins is the large amount of land area required.

Double-deck rectangular basins are essentially two rectangular sedimentation basins stacked one atop the other. This type of

basin conserves land area, but has higher operation andmaintenance costs than a one-level rectangular basin.

Square or circular sedimentation basins with horizontal flow areoften known as clarifiers . This type of basin is likely to have

short-circuiting problems.

A fourth type of sedimentation basin is more complex. Solids-contact clarifiers , also known asupflow solids-contact clarifiers or upflow sludge-blanket clarifiers combine coagulation,flocculation, and sedimentation within a single basin. Solids-contact clarifiers are often found in

packaged plants and in cold climates where sedimentation must occur indoors. This type of clarifier is also often used in softening operations.

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Zones

Introduction

All sedimentation basins have four zones - the inlet zone, the settling zone, the sludge zone, and theoutlet zone. Each zone should provide a smooth transition between the zone before and the zoneafter. In addition, each zone has its own unique purpose.

Zones can be seen most easily in a rectangular sedimentation basin, such as the one shown below:

In a clarifier, water typically enters the basin from the center rather than from one end and flows outto outlets located around the edges of the basin. But the four zones can still be found within the

clarifier:

Inlet Zone

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The two primary purposes of the inlet zone of a sedimentation basin are to distribute the water andto control the water's velocity as it enters the basin. In addition, inlet devices act to preventturbulence of the water.

The incoming flow in a sedimentation basin must be evenly distributed across the width of the basinto prevent short-circuiting. Short-circuiting is a problematic circumstance in which water

bypasses the normal flow path through the basin and reaches the outlet in less than the normal

detention time. We will discuss short-circuiting in the next lesson.

In addition to preventing short-circuiting, inlets control the velocity of the incoming flow. If thewater velocity is greater than 0.5 ft/sec, then floc in the water will break up due to agitation of thewater. Breakup of floc in the sedimentation basin will make settling much less efficient.

Two types of inlets are shown below. The stilling wall , also known as a perforated baffle wall ,spans the entire basin from top to bottom and from side to side. Water leaves the inlet and entersthe settling zone of the sedimentation basin by flowing through the holes evenly spaced across thestilling wall.

From: Water Works Operator's Manual

The second type of inlet allows water to enter the basin by first flowing through the holes evenlyspaced across the bottom of the channel and then by flowing under the baffle in front of thechannel. The combination of channel and baffle serves to evenly distribute the incoming water.

Settling Zone

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After passing through the inlet zone, water enters the settling zone where water velocity is greatlyreduced. This is where the bulk of floc settling occurs and this zone will make up the largest volumeof the sedimentation basin. For optimal performance, the settling zone requires a slow, even flow of water.

The settling zone may be simply a large expanse of open water. But in some cases, tube settlersand lamella plates, such as those shown below, are included in the settling zone.

Tube settlers and lamella plates -Water flows up through slanted tubes or along slanted plates.

Floc settles out in the tubes or plates and drifts back down into th elower portions of the sed imentat ion basin. Clarified water passes

through the tubes or between the plates and th en flows out of the bas in.

Tube settlers and lamella plates increase the settling efficiency and speed in sedimentation basins.Each tube or plate functions as a miniature sedimentation basin, greatly increasing the settling area.Tube settlers and lamella plates are very useful in plants where site area is limited, in packaged

plants, or to increase the capacity of shallow basins.

Outlet Zone

The outlet zone controls the water flowing out of the sedimentation basin - both the amount of

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water leaving the basin and the location in the basin from which the outflowing water is drawn. Likethe inlet zone, the outlet zone is designed to prevent short-circuiting of water in the basin. Inaddition, a good outlet will ensure that only well-settled water leaves the basin and enters the filter.The outlet can also be used to control the water level in the basin.

Outlets are designed to ensure that the water flowing out of the sedimentation basin has theminimum amount of floc suspended in it. The best quality water is usually found at the very top of

the sedimentation basin, so outlets are usually designed to skim this water off the sedimentation basin.

A typical outlet zone begins with a baffle in front of the effluent. This baffle prevents floatingmaterial from escaping the sedimentation basin and clogging the filters. After the baffle comes theeffluent structure, which usually consists of a launder, weirs, and effluent piping. A typical effluentstructure is shown below:

The primary component of the effluent structure is the effluent launder , a trough which collectsthe water flowing out of the sedimentation basin and directs it to the effluent piping. The sides of alaunder typically have weirs attached. Weirs are walls preventing water from flowing uncontrolledinto the launder. The weirs serve to skim the water evenly off the tank.

A weir usually has notches, holes, or slits along its length. These holes allow water to flow into theweir. The most common type of hole is the V-shaped notch shown on the picture above whichallows only the top inch or so of water to flow out of the sedimentation basin. Conversely, the weir may have slits cut vertically along its length, an arrangement which allows for more variation of operational water level in the sedimentation basin.

Water flows over or through the holes in the weirs and into the launder. Then the launder channelsthe water to the outlet , or effluent pipe . This pipe carries water away from the sedimentation

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basin and to the next step in the treatment process.

The effluent structure may be located at the end of a rectangular sedimentation basin or around theedges of a circular clarifier. Alternatively, the effluent may consist of finger weirs , an arrangementof launders which extend out into the settling basin as shown below.

Sludge Zone

The sludge zone is found across the bottom of the sedimentation basin where the sludge collectstemporarily. Velocity in this zone should be very slow to prevent resuspension of sludge.

A drain at the bottom of the basin allows the sludge to be easily removed from the tank. The tank bottom should slope toward the drains to further facilitate sludge removal.

In some plants, sludge removal is achieved continuously using automated equipment. In other plants, sludge must be removed manually. If removed manually, the basin should be cleaned atleast twice per year, or more often if excessive sludge buildup occurs. It is best to clean thesedimentation basin when water demand is low, usually in April and October. Many plants have atleast two sedimentation basins so that water can continue to be treated while one basin is beingcleaned, maintained, and inspected.

If sludge is not removed from the sedimentation basin often enough, the effective (useable) volumeof the tank will decrease, reducing the efficiency of sedimentation. In addition, the sludge built up

on the bottom of the tank may become septic , meaning that it has begun to decay anaerobically.Septic sludge may result in taste and odor problems or may float to the top of the water and become scum. Sludge may also become resuspended in the water and be carried over to thefilters.

Sludge Disposal

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Sludge Composition

The sludge which is found in the bottom of a sedimentation tank is primarily composed of water.The solids in the sludge are mainly excess coagulant, such as alum. Alum sludge has a solidsconcentration of only about 1% when automatically removed from the basin, or about 2% if manually removed. (The greater solids concentration of manually removed sludge is due to a small

amount of gravity thickening.)

Many options exist for disposal of sedimentation sludge. Here we will discuss disposal in streams,sanitary sewers, lagoons, and landfills.

Disposal in Streams and Sewers

In the past, sludge and backwash water was typically released into streams and other bodies of water. However, this practice is becoming much less common and is now well regulated.Backwash water and sludge can only be released into streams if a discharge permit has beengranted by the NPDES. The NPDES further requires extensive daily monitoring of the water quality when the sludge is being discharged.

Alternatively, sludge may be piped directly to the sanitary sewer. However, this disposal optionalso has its disadvantages. Sludge can cause sewer blockages. In addition, fees charged by thewastewater treatment plant can be expensive. Releasing sludge into the sewage lines in large

batches makes treatment of the wastewater problematic, so sludge is typically released slowly over a long time period, which requires a large holding tank at the water treatment plant.

Thickening Sludge

Most of the other alternatives require transporting sludge away from the treatment plant. Sludge istypically dried before it is trucked away since the greater volume of wet sludge makes it much moreexpensive to transport. This drying process is known as dewatering or thickening . Alum sludgeis difficult to thicken, but a variety of devices have been developed to thicken the sludge, some of which are explained below.

In many cases, the sludge is treated by the addition of polymers to aid in the dewatering process.Alternatively, the sludge can be heated or frozen and thawed to increase the solids concentration.Treating the sludge to aid in thickening is known as conditioning the sludge.

Once the sludge has been conditioned, it may be thickened in a lagoon, drying bed, or one of

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several other devices.

Lagoons , which are small-volume storage ponds, arethe simplest device used to thicken sludge. Theselagoons are filled with sludge and the solids are allowedto settled due to gravity to the bottom of the lagoonwhile the clear water is pumped off the top.

After a few months, gravity and evaporation will have reduced the sludge to a 30-50% solidstate. The sludge can then be covered with soil and left on site, or may be trucked to a landfill off-site.

Drying beds are often used to thicken sludgedestined for a landfill more quickly than thesludge would be thickened in a lagoon.

A drying bed is similar in design to a sand filter, with a layer of sand underlain by a layer of gravel. The sludge is applied to the top of the sand and the water percolates down through thesand and gravel and is drained away. When the sludge is sufficiently dry, it is carefully removedfrom the top of the sand and is trucked to a landfill. When sludge is preconditioned withchemicals, dewatering in a drying bed may take only a few days or weeks.

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Other processes used to thicken sludge include filter presses, belt filter presses, centrifuges, andvacuum filters. These processes result in sludge with a solids content ranging from 30 to 50%.

Process Control Calculations

As with many other wastewater treatment plant unit processes, process control calculations aid indetermining the performance of the sedimentation process. Process control calculations are used inthe sedimentation process to determine:

percent removalhydraulic detention timesurface loading rateweir overflow ratesludge pumping

percent total solids

Surface Loading Rate

The surface loading rate is the number of gallons of wastewater passing over 1 square foot of tank per day. This can be used to compare actual conditions with design. (Plant designs generally use a

surface loading rate of 300 to 1,200 gallons/day/ft 2.) To view more examples, read on page 136 inyour text.

The flow into a clarifier is 4.0 MGD in a tank 90 feet long and 35 feet wide. What is the surfaceloading rate?

You will have to convert 4.0 MGD to gal/day, which is 4,000,000 gpd. Then plug in the numbers:

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Weir Overflow Rate

The weir overflow rate is the amount of water leaving the settling tank per linear foot of weir. Theresults of this calculation can be compared with design. Normally weir overflow rates of 10,000 to

20,000 gal/day/ft are used in the design of a settling tank.

To view more examples, read page 136 in your textbook.

The circular settling tank is 90 feet in diameter and has a weir along its circumference. This effluentflow is 2.55 MGD. What is the weir overflow rate in gal/day/foot?

Sludge Pumping

For the plant operator, for process control purposes, knowing the amount of sludge pumped eachday is important. This information is not only important for proper operation of the sedimentation

process, but for sludge treatment processes as well. Such information includes accurate dataregarding the quantity of solids and volatile solids removed from the sedimentation tank.

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The sludge pump operates 15 minutes per hour. The pump delivers 30 gallons/minute of sludge.Laboratory tests indicate that the sludge is 5.1% solids and 69% volatile matter. How many poundsof volatile matter are transferred from the settling tank to the digester?

Sedimentation Expected Performance

Primary sedimentation clarifiers can be expected to remove:

Settleable solids 90-95%

Total Suspended Solids 40-60%

BOD 5 25-35%

Review

Sedimentation is a process used to remove suspended particles from water using gravity.Sedimentation may take place in a presedimentation device such as a reservoir, grit basin, debris

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dam, or sand trap; or sedimentation may follow coagulation/flocculation and take place in arectangular sedimentation basin, a double-deck rectangular basin, a clarifier, or a solids-contactclarifier.

Sedimentation basins typically have four zones - the inlet zone which controls the distribution andvelocity of inflowing water, the settling zone in which the bulk of settling takes place, the outlet zonewhich controls the outflowing water, and the sludge zone in which the sludge collects. Sludge may

be disposed of a in sewer or stream or may be conditioned and then thickened in a lagoon, drying bed, filter press, belt filter press, centrifuge, or vacuum filter before being transported to a landfill.

Assignment

Read about surface loading on page 136 of your text and answer the following question(make sure to read the footnotes): (25 points)

1. The settling tank is 120 feet in diameter and the flow to the unit is 4.5 MGD. What is thesurface loading rate in gallons/day/ft 2?

Read about weir overflow rate on page 136 of your text and answer the followingquestion: (25 points)

2. The settling tank is 120 feet in diameter and has a weir along its circumference. This effluent

flow rate is 2.34 MGD. What is the weir overflow rate in gal/day/ft?

3. Work the following crossword puzzle that comes from definitions in your textbook. You mayeither print the puzzle out, complete it and mail or fax back to the instructor or you may sendan email with the correct answers numbered accordingly. (50 points)

QuizAnswer the questions in the Lesson 14 quiz . When you have gotten all the answers correct, printthe page and either mail or fax it to the instructor. You may also take the quiz online and submityour grade directly into the database for grading purposes.