Title: Troubleshooting LPP Systems
1Troubleshooting LPP Systems
- Taking a closer look
- OM 110 Fall 2005
2Troubleshooting Steps
- Identify the problem
- Observe conditions
- Draw conclusions
- Test conclusions
- Fix the problem
- Check to make sure the fix works
3Observations
- If youve been there before,
- look for things that are different from your last
visit. - If the system is new to you,
- look for things that dont match the
documentation, or - look for things that just dont make sense.
4Bad Conclusions
- Whatever you do, dont jump
5Seeing ? Understanding
6The wrong approach!
- Scenario conventional line with seepage at end.
- Repair add 50 of line.
- Puts the effluent back under ground where it
belongs for a while - What did you fix? A symptom? (surfacing effluent)
or a disease? (infiltration into tank, leaking
toilet, settled distribution box, etc.)
7Disease/symptom Cause/effect
- A single cause can have several effects
- A particular effect can result from several
different causes. - The operator inspection is a physical exam for
the LPP system.
8Anatomy 101
turnups
down hill
manifolds
laterals
valves
tanks
supply line
9Pressurizing
turnups
down hill
manifolds
laterals
valves
tanks
10Pressurized (Full Volume)
turnups
down hill
manifolds
laterals
valves
tanks
supply line
11Depressurized (Draining)
turnups
down hill
manifolds
laterals
valves
tanks
12Volumes to know
- Lateral volume how much water is actually in
the lateral pipes when theyre full. - Supply line manifold volume how much water is
actually in the supply line manifold when
theyre fully pressurized - Draining volume (drainback) How much of the
supply line manifold volumes drain when the
pump shuts off .(where does it go?)
13Pump Delivery Rate
- The rate at which water is pumped from the pump
tank to the lateral field in gallons per minute.
- Controlled by two things
- Number and size of holes in laterals
- Distal pressure head
- If either of these changes, the PDR changes.
14Pressure Head
- Design pressure head specified by the system
designer - Distal pressure head adjusted to the design
pressure head in the field - Separate valve if multiple zones
15Distal Pressure Head
- Sloping Site The operating pressure in the
lateral at the highest elevation in a field or
sub-field. -
- Flat site The operating pressure in the
lateral that is farthest away from the pump. - It is represented by the height at which water
stands in the standpipe on the lateral when
the pump is running. - Set or adjust with field valve
16Distal Pressure Head sloping site
Distal Pressure head
Slope
17Distal lateral on a flat site
End-fed Manifolds
Distal lateral Subfield 1
Distal lateral Subfield 2
manifolds
Valves
tanks
supply line
18Distal lateral on a flat site
Center-fed Manifold
Distal lateral
Distal lateral
Manifold
tanks
Supply line
19Lateral head
Like distal pressure head, head in each lateral
is represented by the height of water in the
standpipe when the pump is running. Its a
combination of the head in the top lateral and
elevation difference.
Lateral head 3.2
Lateral head 2.8
Lateral head 2.0
Ground surface
Distal head 2.0
2.0
2.0
Elevation of top lateral
Elev. Diff. 0.8
Elevation of second lateral
Elev. Diff. 1.2
Elevation of third lateral
20Remember Time to pressurize
- When the pump comes on,
- how long it takes for all the pipes to fill and,
- for the holes to start dosing at the designed
rate - Minimum run time for drawdown
- 3 to 5 minutes
21INSPECTION
- Preparation ahead of time
- Check weather forecast
- Notify owner to turn off pump
- Assemble documentation
- Prepare field sheet data from last inspection
to-do list
22INSPECTION - performance
- Measurement recording
- Solids levels
- Pressure heads
- Drawdown
- Dosing rate
- Meter readings
23Solids levels - what are you checking?
- Habits of occupants - FOG, a-b soaps, etc.
- In septic tank, effectiveness of primary
treatment (settling/flotation) - In pump tank, effectiveness of ST effluent screen
or other pretreatment
24Distal pressure head what are you checking?
- Difference between observed and design
- Integrity of pipe network - is effluent being
delivered correctly to each part of the field? - Anything within the network that alters the
pattern blockage, breaks affects the distal
pressure head. Where and how much the head
changes points to where the problem is.
25One lateral head too low
- Water thats supposed to be in the standpipe is
going some place else. Where? - a break in the lateral - acts like larger
hole or extra holes - partial blockage in lateral some of the
water can get past - (but this will create an increase somewhere else)
Lateral head 3.2
Lateral head 1.8
Lateral head 2.0
Ground surface
Design head 2.0
2.0
Elev. Diff. 0.8
Elevation of top lateral
Elev. Diff. 1.2
Elevation of second lateral
Elevation of third lateral
26One lateral head too high
- Water cant leave lateral through the holes, so
it shows up in the standpipe. Why? - Some of the holes are blocked
Lateral head 3.2
Lateral head 3.6
Lateral head 2.0
Ground surface
Design head 2.0
2.0
Elevation of top lateral
Elev. Diff. 0.8
Elevation of second lateral
Elev. Diff. 1.2
Elevation of third lateral
27 Drawdown what are you checking?
- Drawdown x gallons/inch Dose Volume
-
- Slipping of floats changes dose volume
28PDR what are you checking?
- Another view of the integrity of the pipe network
- You cant change PDR directly- it changes in
response to other changes. This is why you should
measure it before you make changes.
29Meters what are you checking?
- Water meter how much water has been supplied to
the house for a given period of time. - If there is no outside use (irrigation, car
washing, etc.), roughly the same amount of water
goes to the septic tank.
30Event counter what are you checking?
- Counts electrical events how many times has the
pump come on? - Gives no information about length of events
- Must know dose volume to learn how much water has
been delivered. - IF all the events are the same length and IF the
dose volume hasnt changed, you can estimate how
much water has been delivered. -
31Elapsed time meter what are you checking?
- Gives running total of how long the pump has run.
- Must know PDR to tell how much water has been
pumped. - IF the PDR has stayed the same, you can estimate
how much water has been pumped. - Measure the PDR before you make adjustments, or
this reading isnt much use.
32LPP troubleshooting chart
- A centerfold for operators
33Fixing the problems
- Repair things that are broken
- Adjust things that can be adjusted
- What are you trying to change?
- What ELSE will happen?
34OPERATIONTHE ART OF MAKING ADJUSTMENTS
- Identify changes
- Compare measurements to previous data
- Compare measurements to design specs
- Evaluate changes
- Heads too high or too low
- PDR too high or too low
- Evaluate options what can you change, and what
will happen when you change it?
35Changes
- If no changes have occurred within the system
since the last time you checked it, then the
heads and the PDR should be exactly as you left
them. - This is why you take baseline measurements before
you make adjustments - to see whats changed.
36PDR Too High
- GPM too high, but heads are okay.
- Expected amount of water is going out of lateral
holes, and also to stand pipes but the extra is
going somewhere. Where? - Leak in supply line or manifold
- same thing a different way
- GPM okay, but heads are too low.
37PDR Too Low
- GPM too low, but heads are okay.
- Water is getting to standpipes, but not enough
is leaving lateral holes. Why? - Blockage of lateral holes - some, many, all?
- Blocked by accumulated solids
- Blocked by roots
- Blocked by water i.e., saturation in the
trench - the same thing another way
- GPM okay, but heads are too high
38PDR and head BOTH too high (or too low)
- If both parameters are off in the same direction,
the system may just be out of adjustment. - Use gate valve to adjust head, and then check
dosing rate. - If you get head adjusted correctly but dosing
rate doesnt match, then consider possible
causes.
39Monitoring data checking only one lateral
Zone 1
Zone 2
40Monitoring data Checking all laterals
Scenario 1
41Monitoring data Checking all laterals
Scenario 2
42Options
- What can you change?
- Operating head (distal pressure head) adjust
valve(s) - Dose volume adjust drawdown with floats
- Can you change dosing rate?
- What will these changes do?
43Increase distal pressure head
- Distal pressure heads in laterals will increase
- Flow per hole will increase
- PDR will increase
- Pump run time will decrease
- Time to pressurize will decrease
- Dose volume will not change
- Distribution pattern (top to bottom) will change
44Decrease distal pressure head
- Flow per hole and PDR will decrease
- Pump run time and time to pressurize will
increase - Distribution pattern will change
45Increase drawdown
- Distal pressure head and PDR will not change
- Dose volume will increase (mind your maximum!)
- Pump run time will increase
- Time to pressurize will not change
- Doses will occur less frequently
- Distribution pattern will change, and
overloading at bottom of system is more likely.
46Decrease drawdown
- Heads will not change
- Dose volume and pump run time will decrease
- Doses will occur more often
- Time to pressurize will not change
- Distribution pattern will be less effective
because length of time at operating pressure
decreases
47Summary of changes
48Analyzing Meter Data
49Using ETM readings to analyze flow
- Residence of John Smith
- 4 Bedroom home
- Demand-dosed system
- LPP distribution
50Measuring flow ETM
51Measuring flow ETM
52Measuring flow ETM
53Measuring flow ETM
54Measuring flow ETM
55Measuring flow ETM
56Measuring flow ETM
57Incoming flow Water Meter
- Know how to read the water meter
58Comparing figures to analyze flow
59Analyzing flow
60- How much is being used relative to design?
61Using cycle counters to analyze flow
- Bargain Flea Market
- Days of operation Fri., Sat., Sun.
- Time-dosed flow equalization
- LPP Distribution
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63Measuring flow Event counter
64Measuring flow Event counter
65Measuring flow Event counter
66Measuring flow Event counter
67Measuring flow Event counter
68Measuring flow Event counter
69Analyzing Flow Water meter
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71Dose Volume
- Whats the correct dose volume for a given LPP
system? - Minimum
- 5 x lateral volume draining volume
- Maximum
- 10 x lateral volume draining volume
72Filling
turnups
down hill
manifolds
laterals
valves
tanks
73Diameters and volumes
- 1 Sch. 40 4.5 gallons per 100
- 1 ¼ 7.8
- 1 ½ 10.6
- 2 17.4
- 3 38.4
480 of 1 ¼ lateral holds how much
water? 480 x 7.8 35.1 gal. Lateral
Volume 100
74Dose volume example
- Laterals 480, 1 ¼ diameter
35.1 gallons - Manifold 35, 3 diameter
- portion that drains all of it 13.4 gallons
- Supply line 175, 2 diameter
- portion that drains none of it
- Minimum dose volume (5 x 35.1) 13.4
188.9 gal - Maximum dose volume (10 x 35.1) 13.4
364.4 gal
75Educated guessing
- Estimate appropriate dose volume based on lateral
length and draining volume. - Within that range, choose a drawdown that allows
the pump to run for at least 5 minutes per dose.
76Educated guessing
- Set up standpipes on all the laterals at once
- If the water levels are all the same, there is
probably no significant blockage or leakage.
77Educated guessing
- If you dont know what the design head is
supposed to be, set it at 2. - Most common starting point for systems in NC.
78One thing at a time
- When the system needs adjusting, there are only
two things you can change easily - Dose volume
- Distal pressure head
- Dont try changing both at once because you
probably wont know which one did the trick. - In general, changing dose volume is less likely
to cause surprises.
79Record-keeping and reports
- For each system you operate, maintain a file
that includes - Copy of permit
- Copy of contracts and correspondence
- Copy of plans/specs/drawings
- Copies of previous inspection reports
- Activity log, including dates of correspondence,
requests from owner, site visits, etc.
80- Never, ever, take the only copy of any
documentation to the jobsite. - It WILL fall into the pump tank or blow away or
get eaten by the dog. - Make a field copy of the plans , and prepare
a field sheet for each visit that has basic
system info as well as data from the last
inspection.
81LPP Plans - the physical
- What information do you need from the plans?
- Site plan showing location of tanks, supply line,
manifolds, laterals, valves, and any other
components - Piping details diameters, lengths
- Tankage details volumes, dimensions
- Pump and control specs
- Any other information that tells you whats
buried out there
82LPP Plans the functional
- Flow characteristics
- Design distal head
- Design dose volume
- Design system flow rate (Q)
- Total dynamic head
- Flow chart for lateral field
- These tell you how the system is meant to behave.
Used in sizing the pump
83Flow chart
84Flat World
85Slope
downhill
86To compensate for lateral/downslope water
movement,designers decrease number of holes in
lower laterals.
9 holes
7 holes
6 holes
5 holes
87Existing systems with no documentation
- Determine nature of system
- Document current conditions
- Document findings
- Make plan of action for OM
88No Documentation
- Operator must establish some kind of starting
point - Locate, measure, map, inspect, evaluate
- Determine
- Whats there
- Whats it doing
- What should be changed
89OPERATIONTHE ART OF MAKING ADJUSTMENTS
- Identify changes
- Compare measurements to previous data
- Compare measurements to design specs
- Evaluate changes
- Heads too high or too low
- Dosing rate too high or too low
- Evaluate options what can you change, and
what will happen?
90It will never be perfect.
- Sometimes the heads and the dosing rate wont
match simply because it rained yesterday. - This is usually a self-healing problem.
- If you adjust the system its going to be out of
whack as soon as the ground dries out. - Schedule your next inspection for dry weather.
91Just to reiterateThe 3 tasks of an operator
are
- Inspection
- Visually evaluate test measure record
sample report - Maintenance
- Repair, adjust, clean
- Operation
- Manage activities that affect the performance of
the system - Evaluate respond to changes diagnose problems
- Improve the function and operability of the
system
92