|
Static
pressure is an indication of the operating condition of an HVAC system.
Just as a doctor or nurse measures blood pressure to begin the
examination, so
should service techs, and duct renovation specialists
measure static pressure "to begin their diagnostics
procedures." The entire duct system must be leak sealed before final checking of
duct Static Pressures. SIMPLE BTUH AIRFLOW MATH | AIR
FLOW
FORMULAS Figuring
Delivered BTUH | SIMPLE
BTUH AIRFLOW MATH | Formula
for finding CFM Airflow
AIRFLOW
DIAGNOSTICS and REPAIR PDF Excellent & thorough
Why Look at your Ducts (Leakage up-to 33% of cooling cost)
when replacing your AC System; a must viewing:
http://www.youtube.com/watch?v=IV0Rwv5gco4
Local Contractor Locater Map - Talk with These Forum Contractor PROs in
your area
Room
Air Pressure
Differentials in Pascals & IWC |Sizing Units' Tonnage
to enough
Airflow |Selecting Correct Sized
Diffusers |*Video checking static ESP|
*Video 2 checking static ESP View!Got DSL 11/2010
*Video measuring
airflow Velocity - Vane anemometer on a Return Air grille
Depending on the filter used; I'd use
between to 50% & 55% for the
free-air--area (sf) (Ak) of
a clean FILTER, & 85 to 90% factor for an open grille
area.
He programmed it in, because when I did the math using .90%
for
the grille I got 336.57863-FPM Vel *X 2.376562-SF free-air-area=
799.9-CFM, or 2-Ton of air flow.
A New Brand of Comfort and Efficiency Excellent linked articles by 'Doc'
Jan 2, 2013 1:33 PM, By Rob 'Doc' Falke
*Selecting Air Filters - Sizing the
Filtering Area - Critically
important to air flow!
CFM
& FPM Velocity Sizing MERV 8 Pleaded Filters
1”
deep M-8 filter’s rated at 175 FPM medium and 350 FPM high; A
16X20 1" MERV 8, Rated @ only 780-CFM
Comparative Tests concerning Pressure Drops of
HVAC Filters - Important Criteria!
At 300-fpm, the 4" deep
Merv 7 has the
same pressure drop at
.10 of an inch, as the 1" fiber glass filter; all
filter areas were 24X24.
*Basics
Featuring the Testo 556 -*Video of a very thorough Air
Conditioning BTUH performance test
COMFORT INSTITUTE
Consumer Protection Division
Found 04/14/12 What I've been saying for years
Do a Search for a Comfort Institute HVAC Contractor Member in your zip
code area
Home Energy Audits - Rochester, NY Area Real
Energy Cost Savings - Ted Kidd
A
lot more Videos at bottom of this page |* HEAT PUMP DIAGNOSTICS
MO
Home Energy Audits LLC
HVAC Talk
Community Ask the Experts FREE Forum - Save Money!
HVAC-TALK
GENERAL DISCUSSIONS -
OPEN FORUM
Importance of Two-Way Communications with HVAC
Customers
ENERGY
EFFICIENCY AUDITOR TALK FORUM - This is the future of the
HVAC field of work
I
found this new Video confirmation today of my mass
communication ideas, 03/05/12; VIEW ALL of this New VIDEO:
THE CONVERGENCE OF
COMMUNICATIONS & ENERGY a world changing video
about everyone's future, by Jeremy Rifkin View this Video, it opens a
future of unlimited economic opportunities...
CFM Formula Per Room You should measure
static pressure every time you service a unit?
Designing Duct Systems Solving for ASP
| Filter
Rack Sizing | Opportunity | Measuring
Static Pressure - Profits | Photos Diagrams | 50% Load -Home Air Leaks |#Evacuation Procedures Refrigerant
piping
System Evacuation
Procedures - Pulling
a Deep Vacuum pdf
- Oil Furnace Airflow Problems
Air Flow fixes
Heating Cooling
Systems must be tested to measure real time BTU Capacity. It is common to find a 3 ton, 13 SEER, Heat & Cool
System only producing 2 tons and 8 SEER. New installations are found
with these problems, & even worse conditions.
Always
begin with a thorough Home Energy AUDIT that shows all the options for
lowering the heat-gain & heat-loss, then after reducing air
infiltration, etc., have a room by room manual J heatload calc
performed. A reduction in
equipment sizing will
usually greatly improve the duct system performance.
This
is where the greatest savings in both heating & cooling will
accrue; this will help in the down-sizing of
equipment.
"The 'proper heatload' on the evaporator coil must be established"
Check and thoroughly seal all the ductwork! For efficient operation,
always check the return air temperature at the blower & at the
Return Air Grille(s) to know whether it is drawing hot air from the
attic or garage areas.
What I stated above, that ought to be done is far more important than
SEER rating; as the above will determine the SEER achieved & the
energy
savings.
Then
do a manual J room by room heat-gain calc
with the option shown so you can do everything
possible to reduce all
sources of heat-gain & heat-loss, greatly reducing both heat
& cooling BTUH equipment sizing.
Before
you do
anything else, educate
yourself enough
to
"ensure
that you request the proper things be done in the proper order of
sequence." Checking ductwork
& Airflow Checking
Static Pressures is
Critically Important. As is knowing the operating feet per minute
(FPM) velocity, the CFM & BTUH to each room along with the Total
CFM airflow & BTUH.
-------------------------
Simple easy anyone can do ways
to check the performance of your central air conditioner so, if needed,
you can
call an Energy Efficiency HVAC Technician
If U want me to run a
ballpark analysis of how your system is performing in respect to its
'Nominal
Rated Btuh' we need at least the following numbers:
Performance Data
Collection – Best Time to collect data is Late afternoon around 4:30
pm, when
attic is HOT; also when outdoor temps are around 85 to 95-F, or above.
*All U need is a good
thermometer (digital
reading in tenths preferable) & and indoor Humidity Gauge
1) Helpful; Tonnage &
SEER of Unit & outdoor condenser model number: __________________
2) TXV or, orifice
metering device? _______. Only if U know…
3) Outdoor condenser’s
discharge-air-temperature ______-F
Subtract Outdoor air
temperature: _______ F
Outdoor Condenser
Air-Temp-Split _______F
4) Need the ‘Indoor’
percent of relative humidity - away from Supply-Air outlets ______
5) Indoor
Return-Air
Temperature ______ F
Subtract Indoor Supply-Air
Temperature ______ -F
Indoor temperature-split
_______-F
Need the above
information for troubleshooting & performance analysis.
Example below:
A Goodman 2-Ton 13-SEER
condenser, 800-cfm indoor airflow; 80-F indoor dry bulb & 50%
relative humidity;
Indoor temp-split 18 to 19-F.
@ 85-F outdoors; 103.9-F
- 85-F outdoors or around an 18.9-F temp-split;
@ Indoor 75-F & 50%
RH condenser temp-split is only around 14.9-F.
In summer
an all electric farm home TWO Half-Ton Window A/Cs & basement large
dehumidifier:
June
30, 2012; Darrell’s electric meter; 62610 – 62140= used 470-KWh *
.0985= $46.29
================================
In
a recent survey conducted at the National Balancing
Institute, less than 6% of the
companies surveyed said they measured
static pressures on a regular basis. In fact, many
companies
make
the mistake of measuring
static pressure only as a last resort when they're in trouble and have
exhausted all other traditional testing.
Establishing
a proper
airflow
should always be the first diagnosis that a tech does, because
nothing
will work properly nor can the system be charged properly, until an
adequate airflow and heatload passes through clean evaporator coils and
fins for absorption of heat into the evaporating refrigerant.
First,
the piping should be checked for proper oil return
to the
compressor, if not adequate, do that before proceeding. Also, too
many do not properly purge & evacuate contaminated central air
conditioning systems.|
Download these Energy Saving PDF Graphics
It will provide ways to cut your monthly Energy Bills, hopefully in
HALF. Thanks TEDKIDD
==========================
===============
A Major Oil Furnace Airflow Problem Fix
Regal & Hallmark
& nearly all Oil Furnaces - Installation manuals
http://www.boyertownfurnace.com/ProductDocuments/index.aspx
Download the installation & service manuals from ABOVE LINK BELOW
LINK MAY NOT WORK!
http://www.boyertownfurnace.com/ProductDocuments/HallmarkONLYManual042909.pdf
To find the
information below; Use within the pdf search: at least 6” above
Or use down arrow to
P-8 & scroll down a-ways...
"If
the oil furnace is used in connection with summer air conditioning the
evaporator coil must be installed at least 6” above the oil furnace for proper
airflow. Distances less than 6” will result in decreased airflow."
Make
sure outlet supply takeoffs are NOT blocked by the coil. In all cases,
refer to the manufacturers’ data for static pressure losses to ensure
the total system static pressure does not exceed 0.5” WC.
Dons
1.5 Ton Heil AC Data Chart The Condenser is ejecting HALF the heat
of its Nominal Rating; evap-coil way under heat loaded!
============================================
Home
owners:
To ballpark efficient
performance, you must know the Cubic
Foot per Minute (CFM) airflow of your central system.
To ballpark CFM, I'd use an anemometer & measure the velocity out
of those ducts.
If using cheap MPH only anemometer, as you know - multiply by 88 to get
FPM.
Use the formula: register
face velocity in FPM *X's area in sq.ft
6" rd metal duct 6*6=36*.7854=28.2744-sq.ins./144= 0.19635-sq.ft.
7" rd duct 7*7=49*.7854=38.4846/144= 0.2672541-sq.ft.,
etc.
Add together the number of branch runs to ballpark the actual CFM
delivered to the rooms.
Air
conditioners & heat pumps need 400 to 450-CFM of airflow
per-ton of cooling.
Importance
of figuring static pressure & Amp draw changes in respect to CFM
air flow changes:
- SP2 (Static Pressure new)
= {CFM-new
/ CFM-old}2 *X old SP
SP2= 1.5-Ton {600-CFM / 475-CFM|2 = 1.26157895 or
1.595567867 * .50" old SP= .80"SP new;
too high
SP2= 4-Ton {1600-CFM / 1350-CFM=
1.85185 * 1.85185= 1.4046634 *.55" old SP= 0.80" new SP2; too high
SP2= 5-Ton A/C {2000-CFM / 1650-CFM}2 = 1.21212 * 1.21212=
1.469237833 * old SP .55" = 0.80"
new SP; too high.
It is always better to add
SA branch runs & more RA
area, plus "a lot more
RA filter area."
Oil furnaces, ALWAYS RAISE
the E-COIL,where possible, 6 to 8 or 10" above the Oil furnace!
OL 11 112 model Thermo Pride Oil furnace with E-Coil directly on top of
furnace + long duct runs; HEATING 1000-CFM.
SP2= {1000 / 700}2 Above Oil furnace: SP2 ={rpm2
1000/700rpm 1}2= 1.42857 power2 = 2.04" X SP1 .5" = SP2 is 1.02" way
too high!
Going from a quarter
HP to a half HP motor & a
300 increase in RPM still won't get the needed air flow on the blower
graph!
- Fan
amp-draw increases as to the cube of the cfm increase
- Amp2 = Amp1
(cfm2/cfm1)3 cubed *x Amp1= Amp2
Required
fan motor horsepower (hp) varies as to the cube of the rpm
speed:
- hp2 = {rpm2/rpm1}3 x hp1 = hp2
- {840-rpm/700-rpm}3 =1.2 cubed = 1.728 * .25-hp= .43hp2
or, a .5, a 1/2 hp motor at 840-rpm SP @.
- Because of A-Coil back-pressure is way high due to
being set to close to the hugh Oil Furnace HT/EX
Duct
retro-work can solve the problem,
increasing blower HP alone won't usually work well!
A few calculations plus retro-work and presto, a matched airflow with
your systems'
heat absorbing coil capacities, delivering near its BTUH, EER, and SEER
ratings at normal room temperature settings! (Most don't)
Figuring
BTUH Performance
Get a low cost Testo Tester & ballpark
figure actual BTUH & EER - the information on it:
http://www.amazon.com/Testo-605-H2-H.../dp/B000774B6A
Everyone,
very low cost anemometer to get airflow FPM Velocities, get it:
http://www.amazon.com/Crosse-Technol.../dp/B0002WZRKE
This should be
helpful: (Edited 4/5/10)
Duct system CFM X* 4.5
@sea-level, or use X* 4.25 if 1000' above sea-level, X* change in enthalpy = BTUH
(Ballpark)
Operating Performance.
"U
Must
Right Click Link,open in New Tab," look-up wet bulb enthalpy
figures on chart," & figure enthalpy change.
Wet Bulb
Enthalpy Chart
Rules
of
Thumb for Duct Systems - Hart&Cooley
Google search Hart & Cooley, also this
pdf might help you
select the right diffuser for the particular application, & list
(Ak) free sq.ft., area of the diffusers:
http://www.rileysales.com/hottips/resizingreganddiffuser.pdf
History
tells us that our industry measured static
pressure many decades ago. When and why did we lose the habit of
testing
this basic factor that affects the total efficient operation of the
heat and air
system? How and why
did we lose touch with the air side of HVAC systems?
Find
the best way to save
energy in your home, use your zip code. Profitabiity of Energy
efficiency Upgrades | Hidden cost of Home
energy Use
DESIGN AND INSTALLATION OF RESIDENTIAL
FLEXIBLE DUCTWORK SYSTEMS
http://www.dca.state.ga.us/development/constructioncodes/publications/1ONE.pdf
Look
at the ducting, if it is not to code; make hard copies of this code
& give it to whoever does the ducting work
Make sure they get redo it right!
Never
have flex duct interiors commercially cleaned, I just viewed Home
Inspection photos showing the interior damaged & insulation
plugging the duct.
Home Inspectors warn people because the duct
cleaner's tell them it won't damage the ducts. Some HI's
look into the boot areas for clues of problems...
=============================================================
Identifying
your registers/diffusers & their (Ak) sq.ft. area, so you can
multiply the FPM Velocity times the Ak (open air) to get the (CFM)
Cubic Feet per
Minute airflow from that register.
Have
or do a manual J heat-gain calc for each room. If a room calls for
3,000-BTUH; first divide 12,000-BTUH by the CFM PER TON you want to
use.
I.E., Wet coil,
12,000/400=30-BTUH per each CFM; Wet coil
12,000/425=28.235294; 3000/28.235-= 106.25-CFM; Dry coil,
12,000/450=
26.6666-BTUH; 3500 / 26.6666= 131.25-CFM
If register/diffuser has the same (Ak)
free-airflow-area, as the duct run!
Room calls for 3,500-BTUH, using
450-cfm per/ton dry coil or 26.6666-BTUH per CFM= 131.25-CFM.
I.E., 6" rd duct
.6*6=36*.7854=28.2744sq.ins/144=0.19635-sq.ft.; 131.25-cfm /
0.19635-sq.ft= or 668.4-fpm velocity.
http://www.americanmetalproducts.com/lima/product_catalogs.html
Click on
the categories to see the diffusers & Return-Air Grilles then find
them on your downloaded pdf's engineering data.
Hart & Cooley: http://www.hartandcooley.com/grd/HC-100/residential/baseboard_registers/462.htm
Do a lot of Hart & Cooley engineering data searches, look at the
registers & the Ak sq.ft. data to figure register's delivered CFM.
=============================================================
Customers - A Simple FREE A/C Check you can
do!
--------------------------
Affordable Test
Instruments Techs Must Own & Use!
All I had was
the
Sling Psychrometer & spinning it was a bit time consuming, but I
used it religiously, it is information you need.
The Testo 605-H2 Humidity
Stick
(wet
bulb), displays relative humidity,
air temperature and wet bulb temperature.
It is very affordable &
because of its potential to help deliver
tons of other data everyone should have one !
For more information
on it:
http://www.amazon.com/Testo-605-H2-H.../dp/B000774B6A
The other test data you need is the system's CFM airflow
through the
evaporator coil, then with software I have you can peg the BTUH the
operating unit is delivering under those conditions.
Add to that a low cost Magnehelic gauge to read static pressures to
compare with mfg'ers blower performance charts; plus a velocity meter
& you have a ballparked CFM to plug into for the BTUH.
We could easily provide a detailed psychrometric print
out what the operating system is delivering in BTUH, including
condensate
lbs/hr, & actual sensible & latent cooling BTUH & Ratio,
every data
detail imaginable. - Darrell
========================================
Air
Conditioning Performance Diagnosis using listed (CT) Condensing
Temperatures
Using Goodman 16-SEER "Expanded Performance Data"
Find the correct (CT) Condensing Temperature with the following
known mfg’ers data.
Outdoor Ambient Temp (OAT) 85-F; IDB 75-F; IWB 63-F or 50%-RH.
Listed pressure is 316-psig, or 99-F CT; that is 99-F -85-F is a 14-F
SPLIT.
The delta T or temp-split should be within a 10-psig range or, +/- 2-F
degrees; 97 or 101-F.
The mfg’ers Supply Outlet should be able to provide Contractors &
Techs with those performance data charts. Goodman has their “Expanded
Performance Data” on the Internet. BTUH = CFM X
enthalpy difference from Chart X 4.5
<-Click
==============================
Home Energy Magazine Online
September/October 1993
Raising Standards and
Savings
New Group Hunts Bad Ducts
Does
40 billion kWh sound like a lot of energy? How about 4 billion
therms? Researchers believe
that's how much electrical and gas energy this
country "could save by fixing inefficient ducts using current
techniques."
"Refining those techniques could reap savings of 90 billion kWh"
plus 9 billion
therms! Peak loads would be reduced too. To pursue these
tremendous
savings,
national, state, and utility research laboratories, the U.S. Department
of
Energy, utilities, and energy service companies are collaborating. Their
consortium is called "Residential Energy Efficient Distribution
Systems," or
REEDS.
These techniques, along with reducing air infiltration &
heatgain/heatloss calcs, ought to be taught in all our schools as
part
of the Science & math curricula. Half the
heatgain/heatloss can be due to a high Home Air
Infiltration Rates!
ASHRAE
standard 62-1989 is 0.35 ACH (Air changes per Hour) or
3-hours for a total interior, Air
INFILTRATION Change.
Home Air
Infiltration
Air
Infiltration sources DTI
Corp Catalog

--------------------------------------
Years
Ago
it was the "U-tube"
. . .
Years
ago a method of measuring air flow
and air pressure was required, and the "U-tube" was used.
This instrument is still used today. It's a 1/4-in. tube
formed into a 'U' shape. A scale is written on it in inches, and
it's filled half-full with water. I still had one when I retired
from the business.
When
pressure is collected in the duct with a static
pressure tip. The pressure travels through the hose to the manometer,
or pressure reading gauge. The distance the pressure moves the water is
Inches of Water Column or (IWC).
Modern
instruments usually use pressure sensors to
interpret the readings digitally, which makes our jobs much easier. But
the old liquid-filled gauges still do the job, if that's all you have
to
get started.
How long
does it take to read the static pressure? About
five minutes. Drill holes into the duct or equipment to insert your
positive
static pressure tip just before the evaporator, the negative just
before
the blower, set up the pressure measuring gauge and read and
record the Total Static of the system. Also, probe
to read the Return & Supply separately to determine where work
needs to be performed; just place only the positive before the
evaporator & read gauge, then only the negative ahead of the blower
& read static. That's all
there is to
it. You have to be super careful,
drill should be fixed so it just goes through the metal.
Solving the
Mysteries of ESP
- External Static Pressure & Duct System Design by
finding TEL,
ASP, & FR:
ESP
is the static
pressure "external to the
air handler," which includes the entire ductwork. This
is the
reading that manufacturers' refer to on the equipment tag of their
airhandler's performance data, usually .50"-ESP.
In other words, ESP is the sum of the static pressure drop in straight
ductwork, and the static and dynamic pressure drops in duct fittings
(i.e. elbows, tees, transition pieces, air outlets, etc.)
"Consider that on High efficiency furnace there is a Condenser & an
Evaporator that adds to the Supply Air Side Static."
The Return External Static Pressure is measured as the air enters the
return opening of the equipment, the Supply External Static Pressure is
measured just outside the supply opening. Try to find the
least-turbulent air to take the readings.
To avoid turbulence take the readings 3 to 5 duct diameter inches
downstream of turbulent areas.
---------------------------------------------------------------------
The North
Country Oil furnace A/C or heat pump scenario:
Any
good Tech should already
know what I am going to illustrate here; this is for Homeowners &
any who can use the least costly way to deal with this too common a
problem in the cold North Country.
We are moving into the cooling
season; however, any changes in
equipment should consider how every component matches with optimal
airflow efficiencies.
My lowest cost solution to the
cold climate oversized Oil furnace with
a small tonnage A/C evaporator coil which requires nearly half the
airflow as heating:
I ran a check on my late
brother’s home & the summer cooling
heatload is about 14,000-BTUH.
The original scenario, had
much less airflow than required for 1.5T
cooling; its 2-T A-Coil wouldn’t flow 1150-cfm for heating
I did a lot of other figuring;
45,000-BTUH output should heat that
small single story home.
However, with the 140,000-BTUH
input, 112,000 output Oil furnace
installed; the nozzle size can be dropped from one gal an hour (we’ll
use 139,000-BTUH input) to .75 @100-psi, the BTUH drops to 103,500
input, this furnace tested at .74% efficiency; *103,000 = 76,590-BTUH.
Using a 90F heating
temperature rise, which Thermo Pride can stand;
(90*1.06 here) 76,590 / 95.4F is 803-cfm.
Therefore, the 2-Ton A-Coil
will handle the CFM; mounted +6 inches
above the furnace, it has the flow capacity to work okay in both
heating & cooling modes.
With a third HP belt-drive
motor, you could simply adjust the RPM down
by turning the adjustable motor pulley out enough to get to 700 or
600-CFM for the 1.5-Ton A/C.
The other solution is to
install a multiple speed direct drive motor
with the fan relay energizing the cooling speed tap.
This
rather common situation in cold climates seems not to be properly
addressed my Techs, & the HO does not know why things don't work
well.
We should all work to improve
efficient use of high cost energy ... so
America & everyone wins.
Unless the
proper CFM heatload goes through the evaporator coil it is
nearly impossible to achieve an accurate & proper refrigerant
charge, and BTU/HR along with efficiency will be way below
Ratings!
Take the
static pressure measurements on both the
Return and Supply Plenums of the furnace (with filter(s) in
place.
Drill
two holes large enough to insert the static pressure
tip, one on the
supply side and one on the return. Pressure measurements are then
taken at
each location. The measurement on the return side will be
negative with a
positive reading on the supply but you disregard the positive/negative
and just
add the two numbers together. You have to be super careful, drill
should be fixed so it just goes through the metal.
When using two tubes (neg. & Pos.) on a modern gauge you will read what the
gauge indicates!
Once
the ESP has been determined, look at the fan curve for
that particular
blower and determine the CFM from that chart.
If the air
flow is
not per
manufacturers' recommendations, it is near impossible to get the
refrigerant
charge correct.
If
you leave out
the area
up to & including the A-Coil where does that leave you? The area to
the
coil & including the coil can represent major Static Pressure
problems!
Measure
Total-SP (TSP) by using
a Magnehelic gauge or manometer and
inserting the tube in the duct in two places - after the fan discharge
and at
the return before it enters the air handler blower.
Formula
for Changing pascals to IWC: The External
Static Pressure for the furnace is 125 Pascals, 125 x.004 = 0.5" IWC -
Inches Water Column.
Modern gauges have two
tubes that add the Return negative-side
to the Supply
positive-side; if yours doesn't, add the negative reading to the
positive reading. However, to
balance the Supply Air side pressures to the Return Air side you need
the separate
readings to know whether one or both are out of specification
perimeters!
If the
Supply Air side is too high say .8" that needs to be addressed by
checking to find where the static increases are occurring on the Supply
Air
side. Then adjustments can be made on the RA side to reduce any -
Negative restrictions, "to achieve the full airflow rating of the
blower to meet the A/C airflow requirements."
Additionally,
when the Return Air Filter(s) begin to load up the
positive side Static Pressure or ESP will begin to Decrease as the RA
Negative reading
Increases. If the Return Air Suction side of the system is restricted
or starved then the positive SA ESP will be “Reduced” as will the air
velocity & total CFM airflow. The
Return Air
portion has a huge effect on the CFM airflow of the system, and many
are too restrictive.
LOW
AIRFLOW - this will help to open your eyes!
Therefore, it is essential to
have a
proper balance of pressures
between the + SA & - RA sides of the duct system to achieve proper
airflow to all of the rooms. Excellent
diagrams pages on taking various Air Readings
Another
Example of imbalance, - there are rooms with "Inadequate Return
Areas," the static goes higher in those rooms & airflow is reduced,
& air also leaks to the exterior outdoors. The amount of leakage
will depend on the direction & velocity of the exterior wind on the
side of the building.
Now, if there is "Adequate Return Area in
several other rooms those
rooms will get excessive airflow, however, the SA ductwork will be
short changed & therefore the ESP reading before the E-Coil might
be a little higher than it would be if the Return Air System were in
proper balance with the SA in all rooms.
How
does the
system "Regain Required
Velocity"
when flow through the A-Coil will be produced largely by static
pressures. What
is the “Total
Static & Velocity Pressures” the Blower & its motor
must
overcome to achieve required airflow? Optimal efficiencies will
never be achieved until the proper Static Pressure
is achieved!
Ideally,
there would
be return air filter grilles
out in the system, and a nice, smooth transition between the coil and
the
furnace to drill into. However, real-life situations often force us to
take
pressure readings elsewhere.
For
instance, on the return side of the system there's
often a filter placed into the top or bottom of a furnace. The
resistance of the filter must be included in the total resistance that
the fan sees. The real-life solution is to drill into the side of the
blower compartment and measure the negative pressure at that point.
On the
supply side, the coil sits directly on top of, or,
below the furnace. This isn't an ideal situation for measuring static
pressure either, but in real-life fieldwork there are two main
practices for measuring positive static pressure.
The
first is to drill into the coil housing between the
coil and the furnace blower. I hope you shuddered a little when you
read that,
because we all hate the hissing sound when we drill into a coil.
But if you're careful, that doesn't happen. Here's how: drill a
pilot hole with a sheath, or stopper on the end of your drill bit
that only allows it to penetrate the coil housing only 1/4-in.
Then look and feel inside to see if the coast is clear for testing.
Some
coils have a secondary wall that you must also
penetrate to get into the airflow; this must be drilled through also,
go below it if possible.
The
second way to gain access to the supply side air stream is to remove
the high limit switch, and take a pressure reading there. Be certain
the power is off when removing the switch, or you could get shocked.
Also,
because the hole is much larger than the static pressure tip, you must
use a seal (a hole bored in a cover plate) to seal
off the air pressure.
WARNING: on units with a
Thermostatic Expansion Valve (TXV), you cannot use the suction pressure
to check the charge; many appear to be doing this; it tells you
nothing. "Only after you have verified that all the coils are clean
& the airflow is right-on," can you begin to check the system's
charge using Subcooling method with a Superheat check.
Always check the
actual airflow CFM 'before' checking the charge, - get
CFM Right First!
*
There is a TXV system that has very low airflow, actually less than
200-cfm per-ton of cooling, they're only checking the suction
pressure & saying the charge & everything is okay! *
That system has a TXV & shows; 98-F condenser saturation temp &
97-F liquid line temp near E-Coil, a mere 1-F Subcooling, it's
undercharged even with a mere 200-cfm per-ton cooling load!
Unbelievable, but it's happening out there.
Use my Superheat
Subcooling Charging page!
The
Proper Steps
Let's
measure static pressure step-by-step. First, read
the nameplate data on the air
handler or furnace to determine its ESP static
pressure rating. This is often the maximum amount of static
pressure
or resistance that the fan can handle on the Supply and Return
Sides and
still
deliver 400 cfm per ton
on high speed. Residential Centrifugal Blowers begin to unload when
static pressures get too high.
To
measure in-duct air pressures, drill two
3/8-in. holes in the duct to insert the static pressure tip.
Third,
connect the static pressure tip to the hose, and
attach the hose to the pressure connection on the Magnehelic®
gauge. The top (or high connection) is for positive or supply pressure.
The bottom (or low connection) is for the negative or return pressure.
Fourth,
level and zero the pressure gauge to ensure
accurate repeatable readings. Then insert the static pressure tip into
the duct with the tip facing into the airflow.
Fifth,
read the pressure on the gauge, and record the
reading on the supply side, then on the return side. These readings can
be taken at one time, but diagnostic ability increases when each side
is read separately.
Use
a (+) sign before the positive or supply side reading to show where it
was taken, and a (-) sign before the negative or return side reading.
Add
the two pressures. Disregard the positive and negative signs before the
pressures, because each pressure is an absolute number;
each pressure is "seen" and affects the fan as a force, so they must be
added together to determine the total resistance the fan sees. For
example a +.23 w.c. plus a -.19 w.c. equals a total static pressure
reading of .42-in. w.c.
The
gauges used now days measure both + & - at the same time giving the
Total SP reading or pressure drop across the various components.
Record
the pressure readings on your diagnostic report
or on your service ticket. Our techs often write the pressures on the
cooling coil for future use. Any change in static pressure reveals a
change in the system that should be addressed for the system to operate
properly.
Most
residential and light commercial systems five tons
and under are rated to deliver 400-CFM at a static pressure of
0.50-IWC.
Maximum static pressure increases with larger units.
Certain
mfg’ers of equipment will rate the AHU with ESPs external to the built
in
components (coils & occasionally clean filters) & others will
rate the
blower alone. [Your job is to Figure the required blower ESP & CFM
for your specific
application.]
Now
when you add all of the required elements to an air conditioning system
you are
adding pressure drops, which reduce velocity pressure, but increase
static
pressure, therefore, Total System Pressure (TSP) remains the same.
If
the External
Static Pressure is exceeded because of poor
installation, or other
conditions, then the CFM produced by the
system will drop.
If
you leave out
the area
up to & including the A-Coil where does that leave you? The area to
the
coil & including the coil can represent major Static Pressure
problems, "especially in oil furnace applications." If there are any
existing heating or cooling airflow problems, you can & should
measure & record the static pressure on each branch run.
Darrell - Bloomington
====================
Be
certain
to always read the nameplate data to determine the ESP that the unit
was manufactured for. Also, obtaining a
copy of the manufacturer's fan curve data can be very helpful in
interpreting static pressure and airflow readings
Measure
the Components
Static
Pressure Drop (PD) can be measured over each component of a system by
taking a
pressure reading on each side of the component, including a possible poor
transition to the cooling coil. Subtract the readings
from each other to determine to drop through that component.
Total Static
pressure can be traced from the grilles all the
way back to the fan. Try adding together the pressure drops over each
of the components of the system. This isn't the usual
procedure for
measuring pressure, but it is a learning opportunity.
For
example, a
cooling coil
may
have a reading on one side of +.35-in. and a reading on the other
side of +.20-in. Subtract and the the coil's pressure
drop is .15-in.
Measure
the Static Pressures on
each side of the blower, add the - negative reading to the+
positive reading to get the Total Static Pressure.
When designing or
redesigning duct
systems; finding TEL, ASP, & FR:
Find
the Total Return and Supply
Lengths by measuring
duct, runouts, transitions, turning elbows with or without
turning vanes, trunk take-offs, and boots, etc.
Once
you have the correct Pressure
Drops (PDs) for those lengths, use the
manufacturer's nameplate
pressure (IWC) and subtract all airstream device pressure losses
(filters, wet
coil, etc. all available in manual D) from that given value. That
will leave the "Available
Static Pressure" - ASP, for design purposes.
You can figure
the Total Equivalent Length (TEL) by using the
Manual D length additives for the various fittings, then use your Duct
Designer Ductulator to properly size the duct system to meet the
velocities and CFMs required in respect to the blower's Nameplate ESP
and its performance graph data.
There are charts
available to determine what the total pressure drop
will be when
you figure the total equivalent run of
the longest Supply duct runs; ALL lengths of
duct
and ALL fittings
for turning, reductions, etc., have a Total Effective Length (TEL) of
duct - that must
be added to
the regular length of that duct run!
Designing
or Redesigning Duct Systems Chart Print
TEL ASP FR
Chart Graph Loads slow using dailup - Save
both the pdf to a quick access PC folder for review
The above is an
example at .7" ESP which is too high for most residential air handler
blowers!
It will deliver the required CFM with some blowers,but at a higher
operating cost, use .5" ESP to subtract Device Losses.
If
there
are any ductwork air leaks, it will throw everything off.
Nearly all
duct systems have a percentage of air leaks.
Check for
& minimize air leaks.
Blower
wheels, evaporator coils, etc., everything has to be clean.
Get
copies
of the ACCA Worksheet; below is my math involved with the
linked Graph:
The
.45-Device Pressure Loss (DPL) should be subtracted from the
furnace nameplate max ESP which was .5"-ESP, leaving a mere .05"-ASP
(Available
Static Pressure).
According
to the way I figured it, (with a .45-DPL), .05"-ASP / 3.3-TEL =
.015-Friction Rate is required, it's way off the Graph!
In the
above example, there should be around 30-DPL or .20-ASP / 3.3 -TEL = .06-FR
-the
minimum FR graphed.
Though many do use
.05-Friction Rate (FR) or less especially for the Return Air
Side.
Otherwise,
it needs a much shortened TEL to function to design!
Air
Turning vanes in 90-ELLs greatly reduce the TEL.
Large transitions on all take-offs, etc.
Other
changes could also help reduce the TEL.
Oversized Return-Air Filter areas, etc.
Look at
the above TEL, FR, ASP Graphed Chart!
It would
have to have a .20-ASP Available Static Pressure with a
330-TEL to get a (FR) Friction Rate of .06.
First find
330-TEL graph, then look at the ASP at the bottom the the FR
shown.
Also, a
.06-FR is the lowest Friction Rate shown on that graph; though
many use .05-FR on the Return Side.
Once
the ESP has been determined, look at the fan curve for
that particular
blower and determine the CFM from that chart.
In the heating mode,
looking at the
product data
chart, what temp-rise does the mfg'er recommend?
Measure
the temp rise, and see what you get.
Unless the
proper CFM heatload goes through the evaporator coil it is
nearly impossible to achieve an accurate & proper refrigerant
charge, and BTU/HR along with efficiency will be way below Ratings!
CFM
formula per room:
Use the load-calc for that room
divided by the total system BTUH for cooling. Say that room's load calc
calls for 3500-BTUH / 24000-BTUH = 0.1458333 * 800-CFM = 116.6-CFM to
that room, a 6" metal duct should be around 600-fpm velocity.
(24,000-btuh / Ave of 3500-btuh = 7 Runs.)
I.E.,
a 4-Ton System: 48,000-btuh @ 400-cfm per-ton= 1600-cfm | Load calc says room requires 3600-btuh /
48000=
0.075 * 1600-cfm = 120-cfm, or a 6" RD metal duct, close to 611-fpm
velocity.
You must know & record
the operating feet per minute
(FPM)
velocity & the CFM to each room & the Total CFM airflow! Every
tech should be using an anemometer to check operating airflow
velocities in FPM & then figure the CFM airflow's.
For Room
Return Air balancing, i.e., -.01"
IWC = approximately -2.48 Pascals, which is a more precise easier incremental
scale to read. One inch water
column (IWC) equals rounded to > 250 pascals, 0.5" IWC is about 125 pascals; 0.25"
WC = 62.5 pascals; 0.125 = 31.25 pa.; 1 / 250 pascals =0.0040322
*X's -2.50 pascals = -0.01003657696655" IWC or
make
it - 0.01"
IWC for low Return Air room
pressure differentials; - use pascals.
Here
are some
examples of residential or light commercial in Inches Water Column
(IWC) Pressure
Drops. Check the engineering data as you design, and you
may be surprised. This is mainly only the example of the Device
pressure losses.
|
Component
|
Pressure Drops IWC
|
|
Cooling coil
|
0.15 to 0.50-IWC
|
|
Pleated filters
|
0.10-in. to 0.45-in.
|
|
Electrostatic filters.
|
0.20-in. to 0.80-in.
|
|
RA Grilles and SA difusers
|
0.02-in. to 0.15-in.
Man. D 0.03-IWC
|
|
Transitions, Boots
|
0.05-in. to 0.35-in.
|
|
Elbows, - Use Turning Vanes!
|
0.01-in. to 0.10-in.
|
|
Disposable filters
|
0.05-in. to 0.30-in.
|
Diagnostics
Clues
There
are many combinations of different static
pressure readings found over the years. The basic premise is that
if static pressure is high, there may be blockage, or the duct may
be undersized.
If
static pressure is low,
there's a good chance that there may be duct leakage, or that the fan
blades are dirty, or motor malfunctioning.
Keep
in mind that with about one in 20 field static
pressure readings you'll get what we call a "goofy" reading (I realize
that's not a very technical term, but it's accurate). Where do these
readings come from? Pressure equalizes immediately, but air also
"rolls" and "bounces" around as it passes through ductwork.
Occasionally, the turbulence of the air inside will give a false
reading. It
will just be way too high, or way too low. Because perfect conditions
don't exist in the field, the answer is to drill another hole
a few inches away and try again.
My brother Don has
a 2-ton A-coil with a TXV and a 1.5-ton Heil
condenser, and because they
mounted
the coil directly on top of the oil furnace, it does not have enough
air
flow! The
140,000-btuh furnace has a belt-drive small Quarter 1/4HP motor. It needs
a Third
1/3HP motor and the coil moved up 6" on rails with preferably a
transition between the
A-Coil
and the top of the furnace so the air is directed into the entry area
of the
coil, thus eliminating the blocking of more portions of the velocity
force!
My Scan of My ThermoPride OL 11 "Oil
Furnace" Graphed Blower-Curve-Chart
(Same as my brother's Oil furnace)
Thermopride
OL 11
Graph ipg
image - Thank you Dave Staso, CA. for
the better expandable image!
"After it loads Right click "Show Original Images" -
Move cursor arrow over graph - Click +
when 'over graph' for expanded image," then print on the highest
quality setting.
Notice at 700-RPM with a quarter 1/4HP motor, I checked his actual
airflow at less than 300-CFM (no appreciable duct air leaks). the graph
shows 5.24" SP.
Now, we switch to a 1/3HP motor @800-RPM, the graph shows 6.85" SP
& only 400-CFM, not nearly enough airflow for 1.5-Ton of cooling.
Therefore we have to raise the evaporator coil 6" above the furnace on
rails & then check the airflow. Eliminating that restriction using
a 1/3HP motor, hopefully that will be adequate at
+800-rpm & say
+5.5" SP & +700-CFM. Formula: SP2= (SP2/SP1)2 X's SP1
======================================================
*You could ballpark the CFM
using the static test & a air handler graph. You could measure
the CFM delivered to each room with a hood Alnor Balometer, it's
usually the best instrument to use, but not cheap. Measuring the air
velocity is a bit tricky because you have to use the
diffuser data which you don't always have available.
A rough ballpark formula to get the CFM: CFM = (velocity in (FPM) Feet
per Minute times the square footage of the duct area, you have to have
& use the diffuser data & get velocity there -for operating
conditions.) Taking the manifold gage head pressure & gage
condensing temp, is important data. Coupled with a TH condenser
temp-reading, if the condenser gage
pres/temp is too high compared to the TH reading, there may be
non-condensibles in the system.
Also,
there is a legitimate formula I use to determine the operating BTUH it
is delivering at all the data taken. All the mfg'ers ought to list the
condenser temp-split (it varies with EER & SEER) just like they
list the indoor split, it is valuable trouble shooting info.
You can also use the condenser temp-split (it contains both Latent
& sensible heat) combined with the indoor data to plot the indoor CFM. I
was never good at math, but those
equations have to balance, & they do work!
============================
*You could
ballpark the CFM
using the static test & the air handler's graph. You could measure
the CFM delivered to each room with a hood Alnor Balometer, it's
usually the best instrument to use, but not cheap. Measuring
the air velocity from diffuser's is
a bit tricky because you should use the
diffuser mfg'ers data which you should always have with you.
You
can
usually get the diffuser mfg'ers data, say its a 1.5-Ton system that
already has 6"rd branch duct runs & to achieve enough CFM airflow,
U need 700-FPM velocity in the ducts.
I would want to use a diffuser with a little more free open sq.ft area
than the 6" duct which area is 0.19635-sq.ft., say middle of the
room in the ceiling;
Hart & Cooley 2-way curved blade 12x6 has Ak .235-sq.ft. Free-Area
delivering 140-CFM at 600-FPM - diffuser face velocity.
This would help lower the velocity of the duct through the
diffuser & reduce air
noise.
Throw is 7.5-ft toward each wall. Terminal velocity at the occupant
level is 75-FPM.
One duct yields140-CFM times 5 outlet yields 687-CFM *X's 30-BTUH per
CFM = 20,616-BTUH, about right.
A rough ballpark formula to get the CFM: CFM = (velocity in (FPM) Feet
per Minute times the square footage of the duct area, you have to have
& use the diffuser data & get velocity there -for operating
conditions.) Taking the manifold gage head pressure & gage
condensing temp, is important data. Coupled with a TH condenser
temp-reading, if the condenser gage
pres/temp is too high compared to the TH reading, there may be
non-condensibles in the system.
Also,
there is a legitimate formula I use to determine the operating BTUH it
is delivering at all the data taken. All the mfg'ers ought to list the
condenser temp-split (it varies with EER & SEER) just like they
list the indoor split, it is valuable trouble shooting info.
You can also use the condenser temp-split (it contains both Latent
& sensible heat) combined with the indoor data to plot the indoor CFM. I
was never good at math, but those
equations have to balance, & they do work!
======================================
Formula
for finding CFM Air Flow from Velocity in FPM
If you can measure the air velocity coming
from a known size duct or
open area of a SA
register, here is a rough ballpark formula to get the CFM:
CFM = (velocity in (FPM) Feet per Minute times the Square Footage of
the duct area). To
convert sq.ins. multiply by 0.00694 for sq.ft., or divide sq.ins. by
144.
Converting square duct inches to round duct size, Figuring the
Square Inches of
Round Ducts, an 8" x 8" duct = 64-sq.ins. x .7854 = 50.26 sq. ins. You
round off
to 50 sq. ins. for an 8" duct. Or,
simply
getting the square inches of round ducts: a 7" duct; 7" x 7" = 49 x
.7854 =
38.48-sq.ins. or divide / by 144 = .2672222-sq.ft. X's a velocity of
500-fpm = 133.6-cubic
feet per minute delivered to the room; 133.6-cfm x 30-BTUH per cfm
ratio= 4,008-BTUH.
(12,000-BTUH
/400-cfm per-ton = 30-BTU per cfm ratio | / 450 = 26.666-BTUH per-cfm)
Sized for in the chart below - BTU/hr per CFM figures "are figured for
heatpumps at
450-CFM per ton of cooling."
Use 800 to 900-FPM MAINS' VEL. Use an optimum of 500-FPM VEL for Supply
Branch Runs | Air
speed Face of Return.
Air
Filter Rack
Sizing
I
realize this will
never happen if you use the furnace filter size; however, Air
Filter Rack Sizing for efficient operation - Size Gross Return
Air filter grille
area for 200-sq. ins. per ton; or 2-CFM per square inch of filter area.
A 4-Ton (425-cfm-per-ton) with 1700-CFM
/2=850-Sq.Ins. For a
5-Ton system @ 2000-CFM,
that would mean Two filter racks
25X20's each, I would go with Two
30X18" RA filter
racks for 1080-sq.ins for a 5-Ton
system.
(Darrell - Bloomington)
=====================
Quick
Check for Sizing Units to enough Airflow
Actually, even on service calls where there are cooling
problems the ductwork should have a quick Manual D performed.
Then take the
ESP
static pressure & compare to blower graph or chart, also take the
FPM duct velocity.
Then do a quick
estimate of airflow
per equipment tonnage.
To find area of
a
round duct; Duct diam is 7"; 7"X7"= 49-sq.ins., X's .7854 =
38.04845-sq.ins divided/ by 144= 0.2672541-sq.ft. area X's FPM Velocity
600-FPM = 160.35246-CFM X30 = 4,810.5738
each 7" run X's 6 branch runs
= 28,863-BTUH, or airflow for 2.4-ton.
That would also
be
good for 2-ton; at 550-FPM velocity X's 0.2672541= 147-CFM X 30-BTUH
Per-CFM =
4,410-BTUH each run X 6-runs = airflow for 26,460-BTUH. (12,000-BTUH
/400-cfm per-ton = 30-BTU per cfm ratio | / 450 = 26.666-BTUH per-cfm)
Never sell
units requiring more airflow than the duct system will support! - Darrell udarrell
=========================
Ductwork Retrofitting - An Excellent
Economic
Opportunity - Don't
Miss IT!
"More
than 80% of the
duct
systems in residential and light commercial applications 'do not' work
as
designed." Do your service agreements include the duct system?
If
not, this
is an important & significant business opportunity that you are
missing!
Your
best access into the duct renovation market is to
include the duct system in your service agreements. What this includes
is having the service tech measure static pressure on each service
visit. Remember, this takes five minutes or less. If pressures are very
high, or very low, send out a tech competent salesperson with a
flow-hood and a
manometer to identify the problem, and propose a bid to do the
necessary ductwork fix.
One
reason we have service agreements is to gain
additional income from repairs, "so start
repairing the real problem
with
the system," and not just the equipment. In most areas
of the country there is very little competition for quality duct
renovation and air balancing.
Prescribing
HVAC repairs without competition from other
contractors in a way that will greatly improve performance and
efficiency, will delight your customers - that's our
definition of opportunity.
Rob
Falke is an owner of Saunders
Air Conditioning, as well as Balancing Ltd., an air balancing company.
Falke, an NEBB-certified air balancer, is also president of the
National Balancing Institute, which provides air balancing training as
well as complete air balancing business startup packages for HVAC
contractors. To reach Rob, call the National Balancing Institute at
800/633-7058.
Diagnostics
Clues
There
are hundreds of combinations of different static
pressure readings we've found over the years. The basic premise is that
if static pressure is high,
there may be blockage, or the duct may
be undersized.
If
static pressure is low,
there's
a good chance that there may be duct leakage, or that the fan is
dirty or damaged.
Keep
in mind that with about one in 20 field static
pressure readings you may get what is called a "goofy" reading. Where
do these
readings come from? Pressure equalizes immediately, but air also
"rolls" and "bounces" around as it passes through ductwork.
Occasionally, the turbulence of the air inside will give a false
reading. It
will just be way too high, or way too low. Because perfect conditions
don't exist in the field, the answer is to drill another hole
a few inches away and try again.
==============================================================
Measuring
Static Pressure is a sure Thing -
by Tony Doyle
Would you consider doing something that takes less than five
minutes to do that could generate, oh, let us say, more than $90,000 in
revenue? Read on and see how measuring static pressure on every service
call
could conservatively earn you $98,000 in new revenue this next year.
If you had three service techs doing three calls each that would total
nine
service calls per day. In a week's worth of service calls (45), if only 25% had
high static pressure, (a safe bet), you would have a
potential for
11 diagnostics a week. Of the
11 potential
diagnostics, if only 3 of these customers bought one and only one of
those
customers agreed to a duct renovation you'd be on your way to $98,000
of new
revenue this year.
Three
diagnostic tests and one duct renovation job a week! That's
all it
takes. Let's review the numbers:
3 - Service techs.
3 - Calls per day.
45 - Service
calls per week, measuring static pressure on every one of them.
3 - Diagnostics per week. ($395 for the diagnostic).
1 - Duct renovation job per week. (average $1,275 for each one).
40 - Weeks of service calls.
Results:
40 weeks x 3
diagnostics a week x $ 395 per diagnostic = $47,400
40 weeks x one duct renovation
a week x $1,275 avg. renovation price =
$51,000
Total new revenue: $98,400
The number of technicians, service calls, diagnostics
sell price and
average duct renovation price used in this example are
conservative. Use the
formulas in this example and estimate the potential for your company.
What else do you have at your fingertips that will bring in $98,000 or
more in
new revenue this year? By the way, you should be able to perform the
diagnostic
and duct renovation work at a gross margin of at least 70%. Even if
your
overhead is a whopping 40%, that drops about $30,000 to the bottom
line. How
are the plans for the new boat coming along?
- Tony Doyle
===================================
Supply Static Test Hole
When measuring supply static
on a
non-condensing gas furnace, if the area between the furnace outlet and
the coil
is hard to drill into, carefully remove and isolate the fan
control/high limit
switch on the furnace, put some electrical tape over the opening and
poke your
static pressure tip through the tape. The reading will be virtually
identical
to measuring just before the coil. If your reading seems unstable or
out of
line, you might need to measure it elsewhere. [IAQ – Indoor Air
Quality]
=========
TOOLS OF
THE TRADE
There are many
fair, good,
and excellent quality digital
manometers on the market. Some are more than $1,500 for use daily in
commercial air balancing, but many fall into the $300
to $500 range. For less than $150 (excluding a drill) you can assemble
the following items and have a terrific starter kit with everything
you need to begin measuring pressures.
-
Dwyer
Model 2001AV Magnehelic® Gauge
-
8-ft. of
1/4-in. (ID) neoprene or rubber tubing
-
Static
pressure tip
-
1-
3/8-in. drill bit
-
100-
3/8-in. plastic test hole plugs
-
1- 6-in.
x 1/8-in. stainless steel tube
-
1- Drill
bit sheath (for drilling into coil housings,
and not the coil)
-
- My scan
& Dave Staso's image work on my Thermopride OL 11 Graph
Thermopride
OL 11
Graph ipg
image - Thank you Dave Staso, CA. for
your image work!
"After it loads - Move cursor arrow over graph - Click +
when 'over graph' for expanded image."
Example
of improper Duct Design on
an Oil Furnace Name Plate Max., .5"
ESP:
Quarter
HP belt drive blower with
horrible big loss NO transition to
the Cooling Coil
The
Figures showed, it would have
to be designed at .43-ESP, it shows
700-CFM on Blower Graph.
A Major Oil Furnace Airflow
Problem Fix
Regal
& Hallmark
& nearly all Oil Furnaces - Installation manuals
http://www.boyertownfurnace.com/ProductDocuments/index.aspx
Download the installation & service manuals
http://www.boyertownfurnace.com/ProductDocuments/HallmarkONLYManual042909.pdf
If the oil furnace
is used in connection with summer air conditioning the evaporator coil
must be
installed at least
6” above the oil
furnace for proper airflow. Distances
less than 6” will result in decreased airflow. Make sure outlet supply
takeoffs are NOT blocked by the coil. In all cases, refer to the
manufacturers’
data for static pressure losses to ensure the total system static
pressure does
not exceed 0.5” WC.
My
page on the Oil furnace ESP problems should be read & carefully
addressed by everyone that works on them.
http://www.udarrell.com/oil_furnace_heating.html
You never want to lose the velocity force or run the static way up
before the airflow ever gets through the E-Coil!
Checking the SP after the E-Coil will show how much of the static is
occurring before the Coil.
You want the velocity forces & static at the diffusers to get
adequate throw and air movement in the rooms NOT before the E-Coil!
The
"Total
Pressure" required to move the required amount of CFM of air through
the
duct system is composed of Two Elements, "Static pressure and Velocity
pressure." Velocity Pressure is pressure in the direction of the flow.
It
is the push force needed to bring the air up to the required FPM Speed.
"Total
Pressure" is the sum of the Static Pressure and
Velocity Pressure at that specific point of measurement. The manometer
can record
Static, Velocity, and Total
Pressures.
Manufacturers
know the resistance inside the equipment. The ESP reading tells
us what resistance the coil, ductwork, filter, and diffusers
& grilles need to be designed at , so that the blower can deliver
the required airflow through the Supply-Side and Return-Side duct
systems.
Air
moves in
what is called "turbulent Flow," as it is constantly churning and
mixing. Constrictions, duct changes of shape, turning, or banging
against
something that stops its velocity will greatly increase the force
required by
the blower.
This
is why
oil furnaces with the blower to the side and with huge round or octagon
(eight
sided) shaped heat exchangers that come close to the top of the furnace
"can have tremendous
increases 'in both' Velocity
and Static Back Pressures." If the A-Coil is not mounted
high
enough
above the furnace on rails on the plenum, the airflow system will never
achieve
the required CFM.
Let
us take
an engineer's view of this horrible scenario. The blower is set to the
side at
right angles to the huge H.E., therefore from the get-go, the velocity
is
blocked & turbulence is also maximized, thus generating tremendous
forces
that the blower is required to overcome.
Then
here in
Wisconsin where I now live, it appears many install the A-Coil directly
on top
of the furnace, therefore we have a major restriction along with most
of the
airflow
hitting other than the entry area of the coil, another block to
velocity! This is the area where we want the back pressures to be
as low as possible so that there will be more velocity pressures and
static pressures at the supply diffusers. This will provide the proper
throw into the rooms and proper mixing of the room's air.
- Darrell
============================
HVAC Techs
This should be helpful.
CFM X change in enthalpy X 4.5 = BTUH (Ballpark)
Operating Performance
"U Must
Right Click Link & open in New Tab"
Wet Bulb
Enthalpy Chart
=================
MY HVAC BLOG - YOUR QUESTIONS &
COMMENTS WELCOME - Go to my blog for the required
trouble-shooting Data to collect
Evacuation
Procedures -
Pulling a Deep Vacuum pdf
Too
many do not properly purge & evacuate contaminated central air
conditioning systems.
First, the piping should b checked for proper oil return to the
compressor, if not adequate do that before proceeding.
----------------
Determining
which metering device the system has without physically looking
If you do not absolutely know whether the metering device is a TXV, or a fixed orifice device or cap tube.
Hook up your manifold gauges, block off considerable condenser air intake for a short time. If the suction pressure starts rising, you have a piston, or a cap tube. If only the high side goes up, you have a TXV. Double check using Superheat, if Superheat stays relatively stable when the pressures change it's a TXV.
Have things with you in your van or truck to block-off the entering condenser air for a short time. Check every time you are not certain what metering device it has. There will be a lot of guessing in the future
=============================================
DISCLAIMER:
I assume
NO responsibility for how anyone uses the information I
provide in posts or on my websites.
I provide
information for better understanding, edification &
communication between contractors, techs & customers'.
A licensed
Contractor & licensed Techs should always do all HVAC/R
work! You are responsible for your diagnostics and resultant
decisions! Darrell
Udelhoven Darrell's
Refrigeration Heating and Air Conditioning -
Federal Refrigerant Licensed - Retired
Licensed Contractor
Darrell
Udelhoven | Posted:
08/01/04 (Darrell - Bloomington) |