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13 May 2015

Turn it Up! Putting the 100 PSI Pump Pressure Myth to the Test

For many years, as I have taken pump courses, participated in training sessions and taught pump programs I come across a disturbing phenomenon with regard to what pressures pump operators are using when flowing to their handlines.  Many times in the discussions, someone throws out there that they pump the preconnects at 100 PSI and allow the nozzleman to choose to have the pressure increased or decreased upon request.  This "works" for alot of departments, but it doesn't really work well if you consider that an attack hoseline system should be something designed and implemented with alot of different considerations made.  Some of these considerations should include your desired hose diameter, length, type of nozzle, typical staffing, desired maximum nozzle flow and backpressure and more.  It is a decision making process given little to no attention in many fire departments which often results in a terrible mismatch of hose and nozzles and firefighters who struggle to use the end result either because the inadequate water flow cannot extinguish the fire or because they cannot handle the backpressure off the fire stream.

I have been lucky to participate in many good discussions, review alot of good data and obtain alot of my own data about hose and nozzle selection in the past few years.  As I am writing this, I have to admit that 5 years ago, I feel like I knew not even half of what I know now, and I still feel like there's much to learn to evaluate and implement a good combination of hose and nozzles for a functional and effective attack hoseline system.

In this article I want to address the specific issue of under pumping attack lines.  Preconnected attack lines in particular.  There isn't any solid data, nor is there a way to gather it, but I feel pretty confident that many engine companies are under performing in GPM delivery because they haven't put the pieces of the system together and/or done the tests to determine the proper flow of their attack hose/nozzle systems.

The end goal of our tests is a 150 GPM fire stream.  The relative comparisons are meant to see how close we can get to the starting benchmark of 150 GPM with improper and then proper PDP.  I consider the 100 PSI PDP test results failing if they do not meet 150 GPM, and there should be no surprise that they didn't.

I want to make it very clear that the goal here is not to discredit the nozzles.  Each nozzle worked exactly as designed, when it was used properly and pumped properly.  This article is a comparison of three different nozzles being improperly utilized, on purpose, to illustrate the impact it has on total water flow delivery.  I have my preference in nozzles, but that isn't relevant to this piece of work.

Earlier this week I gathered several nozzles to evaluate how they would perform when pumped at the 100 PSI pump discharge pressure (PDP). The three nozzles evaluated were the 50-350 GPM Automatic Task Force Tip, 7/8" smoothbore tip and SM-30 Elkhart Automatic.  With the help of several firefighters we set up a series of tests, while we also conducted testing for our preconnected attack lines.

The test setup was 200 feet of rubber lined double jacket 1 3/4" fire hose.  Test gauge was installed at the front bumper connection, and at the inlet of the nozzle.  There was no elevation and no other influencing factors.  I chose 200', as it represents a very typical length preconnected attack hoseline.  Its important to note that different brands of hose will vary in internal diameter, and different lengths of hose will yield different results.  There are many variables which make the collection of data for your individual department important.  The results we have represent fairly accurate numbers, but I like to say that its not perfect.  The relative differences between each PDP for the given nozzle are the most important part of this comparison.

The hose we used has a known internal diameter of 1.81" per the manufacturer.  The hose was connected to the front bumper discharge of the rig, which is a typical connection for our fire department operations and represents what I feel is a realistic amount of plumbing loss.  When utilizing a crosslay with swivel, it is typical to have at least two 90 degree bends in the piping.  The rig used was found to have approx 10-15 PSI of loss in the piping to this discharge at 150 GPM.

The three nozzles tested were the second third and fourth from the left
Once the hose was laid out and the gauges installed, the testing commenced.  The rig was connected to a hydrant via 25' front soft sleeve.  The hydrant pressure and flow were greater than necessary for the low volume testing.  Initial flows were gated  at the discharge valve to achieve 100 PSI.  Proper pump pressures required increasing the RPM via the electronic governor to obtain the desired PDP.

The test nozzles had a 1 1/2" inline gauge installed at the inlet with a 0-300 PSI gauge
Nozzle readings were obtained at the inlet gauge, with the understanding that this represents a slight inaccuracy.
The line was operated from a discharge which is manifolded through a Hale foam system, with a paddlewheel flow sensor.  The flow sensor was checked and found to be fairly close to accurate by use of a pitot tube.
Test 1.
The testing began with the TFT automatic nozzle.  As I mentioned, the goal was to pump the lines at 100 PSI at the discharge gauge and see what the yield GPM was.  When evaluating the TFT, little nozzle reaction was noted, however we did not measure reaction force.  One firefighter was able to handle the hose easily.  The stream shows the focus point of the water fairly close to the baffle, which is a good visual indicator of low flow.  We "trimmed" the stream back a bit from the stop point where it would be as close to a solid column of water as possible without the water colliding and crossing over itself.  Anyone who works with automatics knows that you have to tweak the nozzle pattern adjustment as the flow increases and decreases to keep the straight stream ideal, since the movement of the baffle changes the pattern slightly.

A flow of 85 GPM was registered on the flow meter at 100 PSI PDP
The TFT automatic flow increased to 150 GPM at a PDP of 180 PSI
It is fair to say the TFT performed as expected.  The nozzle did what it is designed to do in both tests, adjust its baffle to make a usable stream with the given inlet pressure and flow.  It worked "wrong" at first because we used it "wrong" at first.  We knew that would happen, but we want you to know it, and we want you to see it.  If you run the math based on old school theoretical values, the TFT should have been pumped at around 170 PSI.  The piping loss would result in about 10 PSI extra, putting us at the 180 PDP we got.  I expected the pressure to be a bit lower with the larger ID of the hose, but the slight variables in the testing equipment, piping and flow meter cannot pinpoint the actual number, nor is it necessary to.

Test 2.  
The nest test subject was the 7/8" smooth bore at 100 PSI PDP.  The stubby Akron tip was attached to a standard Akron full ball valve shutoff.  We noted a flow of approximately 120 GPM on the flow meter, with the use of a handheld pitot tube, we got a reading of approx 32 PSI (124 GPM) which corresponds to the flow meter with only a 4 GPM difference.  The hose was expectedly soft at the nozzle inlet and prone to kinks without care being used but the stream of water delivered was still effective with a decent reach and continuity.  
The 7/8" tip yielded 120 GPM at 100 PSI PDP
The 7/8 Tip was increased to 150 GPM, and we noted a 145 PSI PDP.  We recognized the tip was 10 GPM under pumped, but we wanted to keep the flows equal from nozzle to nozzle.  The net improvement from test 1 to test 2 was a gain of 35 GPM by switching nozzles and using the same PDP.  The nozzleman had no notable issue controlling this hoseline in either test.

Test 3.
The last test subject was the Elkhart SM-30 Automatic nozzle.  We expected similar results to the TFT.  The automatic nozzle had a usable stream and was manageable for the single firefighter holding it in the first part of the test.

The Elkhart SM-30 yielded 75 GPM at 100 PSI PDP
When we performed the SM-30 test, the results ended up surprising me.  It flowed 10 GPM less than the TFT at 100 PDP.  When we boosted the pump pressure to achieve 150 GPM, it required a PDP of 160 GPM.  This was certainly more favorable than the higher 180 PSI for the TFT.  The nozzleman had more difficulty controlling this hoseline at 150 GPM

The test results are good data to review.  Please remember to do your own testing and verification.  I want to remind everyone we did not evaluate these nozzles for the sake of creating a matched hose and nozzle system, but simply to see how they would perform when improperly pumped as well as properly pumped.

When looking at all 3 nozzles, it is apparent that the smooth bore was more forgiving with low hoseline pressures and can be expected to provide the highest flow under such circumstances, regardless of the reason for the low pressure.  This is an important factor you should consider.  The 7/8" tip yielded 35 GPM more than the TFT and 45 GPM more than the Elkhart at 100 PSI PDP.  If we tested a low pressure fixed orifice combination tip, we could expect some very similar results to the smooth bore.

In summary, I urge you to carefully consider your hose and nozzle setup and consult with experts oin the field of this science.  Sales associates aren't always as educated as you trust them to be, and it is important to seek out your own information and set up testing.  It is even more critical to assure you're pumping the proper amount of water when performing structural firefighting.  The minimum goal you should aim for is 150 GPM, as it represents a flow that has been proven to have effective fire knockdown power and is manageable for a 1 or 2 person nozzle team.


I wish to extend a thank you to the firefighters I work with for their assistance gathering this great data.  Please feel free to comment on the Facebook page.

-Mike G.


22 April 2014

CAFS Pressurized Water Extinguisher Modification

Without a doubt, one of the most common inquiries I have gotten is about how to modify a pressurized water extinguisher to create the "CAF" extinguisher featured in the video on our YouTube channel. Here is a brief article explaining it. 

With any tool modification, you need to remember that the manufacturer may not advocate or sanction the modification.  Do so at your own risk.  




The modification came to us from one of the guys I used to work with. He had worked with these extinguishers in his volunteer company and they found them to work well.  The principle of the modification is to create a class A foam extinguisher that provides a more aerated foam when discharged.  The total liquid volume of the extinguisher is only 1 3/4 gallons as opposed to the standard 2 1/2 gallons. The extra air helps to aerate the stream and expel the solution. The foam is good for increasing the effectiveness of the extinguisher as well as for laying down a barrier to help slow and stop brush fires when hose lines cannot be stretched fast enough. Every engine in our firehouse has one of these extinguishers along with standard water and other special agent extinguishers. Our brush rig has two of them. 

The modification is fairly simple. The steps are as follows.

  1. Mark the extinguisher properly.  Since we do not carry AFFF foam extinguishers, we marked them red with "FOAM" on the tape stripe
  2. Discharge the entire extinguisher and disassemble it
  3. Remove the pickup tube and head assembly
  4. Drill a single 1/16" hole at the top of the pickup tube, no more than 2" from the top where it connects to the head.
  5. Measure 1 3/4 gallons of water in a pail and fill the extinguisher with it.  A large funnel helps.
  6. Add 4-8 Oz Class A foam (depending on how bubbly you want it)
  7. Reassemble the extinguisher
  8. Shake vigorously
  9. Repressurize to the recommended pressure (usually 100 PSI)
  10. Deploy your CAF extinguisher!
Take note that you do not need a foam tip for this to work, although the use of an aerating foam tip that is normally supplied with pressurized AFFF extinguishers will create even better foam.

*Follow appropriate refilling precautions as recommended by the manufacturer*
Place a marking band of tape on the body of the extinguisher.  We chose red and lettered it as "Foam". 

Drill a single 1/16" Hole in the pickup tube about 1-2 inches from the top.  This hole must be above the water line.

Mark a pail or bucket at the 1 3/4 gallon mark (7 quarts or 6.62 Liters).

Mark the handles with colored take to indicate the agent.  Here blue is water, red is foam and purple is Purple-K
Thanks for stopping by and be safe out there.  -MG

06 October 2013

Water Transfer Testing-Jet Siphon Flow Rates



Fairmount Fire Company
Water Transfer Exercise
9/24/2013
About a week and a half ago a good friend invited me along to observe a series of tests of the potential to transfer water using jet siphon devices.  The following results are our non-scientific data that were collected.  It was a great opportunity to get some baseline data on a topic that has little published information.
The Fairmount Fire Company protects a portion of Washington Township, in Morris County NJ.  Their response district includes some areas with hydrants, but is largely unhydranted.  The company operates two engines a tender and a support rig.  You can learn more about them at www.34fire.org

The goals of this drill were to;
  1. Test the potential flow rate of jet siphon devices using one and two devices
  2. Test the potential to transfer water up a grade through a jet siphon device
The setup for the first part of the test included;
  • (1) 3500 Gallon folding tank (Tank #1)
  • (1) 2000 Gallon folding tank (Tank #2)
  • (1) Kochek “JS60” power jet siphon device connected to (2) 15’ x 6” suction hose
  • (1) Kochek “JS60 power jet siphon device connected to (2) 10’ x 6” suction hose
  • Clamp-on hose bracket with (2) 2 ½” hose connection elbows on the 3500G tank
Preparation for tests #1-4
  • Two tanks were set up approx 3-4 feet apart, on flat asphalt, with a slight incline
  • The 3500 gallon tank sat on the “downhill” side
  • The 2000 gallon tank sat slightly “uphill” from the larger tank
  • E34-62 pumped its 1000 gallons of booster tank water into the 3500 gallon tank through the clamp on hose bracket.
  • Once the booster tank had been emptied, a mark was made on the sidewall of the tank indicating the 1000 gallon water level
  • Using a tape measure, corresponding marks were added for 500, 1500 and 2000 gallons along the tank sidewall.  It should be noted that the 3500 Gallon tank was only able to hold about 2000 gallons due to the pitch of the parking lot
  • (2) 15’ sections of hard sleeve were connected together and the Kochek jet siphon was attached.  The intake for the siphon was placed at the lowest “downhill” point in the 3500 gallon tank
  • 50’ of double jacket-rubber lined hose was connected from the pump panel discharge of Tender 34 to the jet siphon
  • A stopwatch was set to 00:00
  • After each test, water was pumped back into tank #1 by E34-62, utilizing the clamp-on 2 ½” hose connection bracket.
  • Time was recorded at each 500 gallon interval 
Preparation for test #5
  • 3500 Gallon tank on the "downhill side"
  • 2000 Gallon tank on the "uphill side"
  • 50' of 6" hard sleeve with an approximate 7' elevation

Test #1
Objective: Determine flow rate of water from nozzle of jet siphon at different pump pressures through 50’ of 1 ½” hose.



The “JS60” Siphon used

The jet siphon was evaluated and noted to have a single ¾” nozzle orifice with a 1 ½” NH hose connection.  It has 6” male NH thread to connect to the hard sleeve hose.  A check of a smooth bore discharge chart shows the ¾” nozzle listed and therefore we can deduct the measurements taken with the handheld pitot gauge are generally accurate.
Water transfer back to original tank
The jet siphon was held by a firefighter and aimed into the portable tank.  The handheld pitot gauge was used to measure the pressure of the stream exiting the nozzle.

Results of Test #1
The flow test resulted in the following performances. 
  • PDP - 75 PSI = 50 PSI nozzle pressure or approximately 120 GPM
  • PDP - 100 PSI = 70 PSI nozzle pressure or approximately 140 GPM
  • PDP of 125 PSI =  80 PSI nozzle pressure or approximately 150 GPM
  • PDP of 150 PSI = unknown nozzle pressure – not tested
It should be noted that the sharp 90 degree bend of the nozzle pipe in the device results in a very broken stream, with fluctuations on the pitot gauge.  The values measures represent a good “average assessment” while holding the pitot gauge in the stream for approx 10-15 seconds.

The following table lists the flow data collected
PDP                 Flow                 Friction Loss (Hose) Approx.     Tip PSI             Device Loss (estimated)
75 PSI              120 GPM          34.6 PSI/100’ or 17.3 PSI/50’      50 PSI Tip         7.7 PSI
100 PSI             140 GPM          47 PSI/100’ or 23.5 PSI/50’         70 PSI Tip         6.5 PSI
125 PSI             150 GPM          54 PSI/100’ or 27 PSI/50’           80 PSI Tip         18 PSI
150 PSI             160 GPM          61.4 PSI/100’ or 30.7 PSI/50’      100 (estimate)   19.3 (estimate)


Test #2
Objective: Determine flow rate of single jet siphon to transfer 1000 gallons of water from one folding tank to another at 100 PSI pump discharge pressure.

The 3500 Gallon tank was marked at 500 gallon intervals with the top mark being 2000 gallons. 

The stopwatch was started when the discharge valve was opened.  The water level started at the 2000 gallon mark.  When the water level reached the 1500 gallon mark the time was recorded.  It was recoded again at the 1000 gallon mark.

The jet siphon was attached to (2) 15’ sections of 6” lightweight suction hose






 Tank Markings made using a tape measure and a measured quantity of water (1000 Gallons)


Results of Test #2
With a pump discharge pressure of 100 PSI the following results were achieved.

Water level at the 1500 Gallon mark (500 gallons transferred):      1:27

Water level at the 1000 Gallon mark (1000 gallons transferred):    3:22

Average flow rate for 1000 Gallons         4.95 Gallons/second or 297 GPM

Average flow rate for first 500 Gallons    5.74 Gallons/second or 344 GPM

Average flow rate for last 500 Gallons    4.34 Gallons/second or  260 GPM


The discharge gauge readings between the main pump and the line gauge were virtually identical at the 100 PSI test
Summary of Test #2
It appeared that the first 500 gallons of water transferred at a higher flow rate, while the last 500 gallons of the test transferred at a lower rate.  The difference in flow between the first and last 500 gallons was an 84 GPM decrease.  We felt that because the siphon action does not use the advantage of positive pressure that as the water level in the tank lowers that it requires more energy to raise the water up the suction hose, thus showing the decline in flow. 

The average flow of 297 GPM also did not account for “prime time” of the siphon, so the actual true flow rate might be slightly higher

Because the known flow of the jet siphon nozzle at the 100 PSI pump pressure is approximately 140 GPM, the average net flow rate of the transfer device is actually 157 GPM.  This could be considered the flow rate of a single 1 ¾” handline


Test #3
Objective: Determine the flow rate of two jet siphons to transfer 1000 gallons of water from one folding tank to another at 100 PSI Pump discharge pressure

The 3500 Gallon tank was marked at 500 gallon intervals with the top mark being 2000 gallons. 

The stopwatch was started when the discharge valve was opened.  The water level started at the 2000 gallon mark.  When the water level reached the 1500 gallon mark the time was recorded.  It was recoded again at the 1000 gallon mark.

The first jet siphon (#1) was attached to (2) 15’ sections of 6” lightweight suction hose.  The 50’ section of 1 ½” hose was connected to the pump panel discharge of Tender 34, shown below.




The second jet siphon (#2) was attached to (2) 10’ sections of 6” lightweight suction hose.  The 50’ section of 1 ½” hose was connected to the rear discharge of Tender 34.  The discharge is located to the lower right of the dump chute.
       




The photos show the piping and location (lower right) of the rear discharge on T34

Results of Test #3
With a pump discharge pressure of 100 PSI the following results were achieved.

Water level at the 1500 Gallon mark (500 gallons transferred):                  1:02 (62s)

Water level at the 1000 Gallon mark (1000 gallons transferred):                2:12 (132s)

Average flow rate for 1000 Gallons         7.57 Gallons/second or             454 GPM

Average flow rate for first 500 Gallons    8.06 Gallons/second or             483 GPM

Average flow rate for last 500 Gallons    7.14 Gallons/second or              428 GPM

Summary of Test #3
It appeared that the first 500 gallons of water transferred at a higher flow rate, while the last 500 gallons of the test transferred at a lower rate, as in test #2.  The difference in flow between the first and last 500 gallons was a 55 GPM decrease.  We felt that because the siphon action does not use the advantage of positive pressure that as the water level in the tank lowers that it requires more energy to raise the water up the suction hose, thus showing the decline in flow. 

The average flow of 454 GPM also did not account for “prime time” of the siphon, so the actual true flow rate might be slightly higher

Because the known flow of the jet siphon nozzle at the 150 PSI pump pressure is approximately was not tested, the average net flow rate of the transfer devices is estimated at 174 GPM.  This could be considered the flow rate of a single 1 ¾” handline.

After reviewing the piping on Tender 34, we noted that the rear discharge contains several sharp bends, and that the pressure gauge line is affixed close to the pump.  It can be deducted that because of this, that jet siphon #2 was somewhat underpowered due to pressure loss in piping.  In addition, due to the difference in length of the two hard suction lines it can be deducted that there may have been a slightly lower level of efficiency in the longer of the two lines.  There were (4) 90 degree elbows and (2) 45 degree elbows identified within the pump house.  It is assumed once the piping reaches the last visible bend that it runs straight to the rear along the frame, but this was not certain.

The flow rate of approximately 280 GPM (140 GPM ea.) is required to support the two jet siphon devices, and thus makes this water unavailable for the fire site.  This must be considered in the pumps total capacity, especially since operating at draft as well as the required pump pressure (100 PSI) to achieve the flow.


Test #4
Objective: Determine the flow rate of one jet siphons to transfer 1000 gallons of water from one folding tank to another at 150 PSI pump discharge pressure

The 3500 Gallon tank was marked at 500 gallon intervals with the top mark being 2000 gallons. 

The stopwatch was started when the discharge valve was opened.  The water level started at the 2000 gallon mark.  When the water level reached the 1500 gallon mark the time was recorded.  It was recoded again at the 1000 gallon mark.

The jet siphon (#1) was attached to (2) 15’ sections of 6” lightweight suction hose.  The 50’ section of 1 ½” hose was connected to the pump panel discharge of Tender 34

Results of Test #4
With a pump discharge pressure of 150 PSI the following results were achieved.

Water level at the 1500 Gallon mark (500 gallons transferred):                  1:11 (71s)

Water level at the 1000 Gallon mark (1000 gallons transferred):                2:18 (138s)

Average flow rate for 1000 Gallons         7.24 Gallons/second or             434 GPM

Average flow rate for first 500 Gallons    7.04 Gallons/second or             422 GPM

Average flow rate for last 500 Gallons    7.46 Gallons/second or              447 GPM

Summary of Test #4
It appeared that the first 500 gallons of water transferred at a lower flow rate, while the last 500 gallons of the test transferred at a higher rate, as compared to the other tests.  This represents an inverse result to the previous pattern. The difference in flow between the first and last 500 gallons was a 25 GPM increase.  As stated, this is the opposite result of previous tests.  We can theorize that the higher velocity of water from the jet may have impacted this result, but have no other data to explain this difference.

The average flow of 434 GPM also did not account for “prime time” of the siphon, so the actual true flow rate might be slightly higher

The estimated flow of the jet siphon nozzle at the 150 PSI pump pressure is approximately 167 GPM, the average net flow rate of the transfer devices is actually 267 GPM.  This could be considered the flow rate of a single 2 1/2” handline or two 1 ¾” handlines.


Test #5
Objective: Determine the flow rate of one jet siphon to transfer 1000 gallons of water from one folding tank to another at 150 PSI Pump discharge pressure up an approximate 7’ elevation.

The 3500 Gallon tank was marked at 500 gallon intervals with the top mark being 2000 gallons. 

The two tanks were 3500 gallons each.  The lower tank was filled to capacity; the upper tank retained its water level markings.

50 total feet of hard sleeve were connected together (2) 10’ and (2) 15’ sections

E34-62 was connected to a 6’ low level strainer in tank #2 (uphill tank) and had approx 500 gallons of on board tank water.  The level of water in tank #2 was at the top of the opening to the strainer, and unsuitable to draft at the start of the test.

The stopwatch was started when the discharge valve on E34-62 was opened.



Test #5

Results of Test #5
Water was discharged from the 6” hard sleeve into tank #2 (uphill), but it was noted to have a low volume, and did not fill the entire hose coupling opening.

After exhausting approximately 500 gallons of remaining tank water, E34-62 was unable to establish an effective transfer and the operation stopped.

Summary of Test #5
The test failed.

While attempting to prime the siphon, E34-62 operator increased pump pressure to near 200 PSI, with no appreciable results.  It was also noted that tank #1 (downhill) began to overflow, leading us to believe that the tank water from E34-62 was simply being exhausted into this tank and backflowing out of the siphon. A small stream of water exited the uphill end of the suction hose, but never gained enough water to establish a draft with the low level strainer.

We believe that the action of the jet siphon is limited to very slight elevation differences.  It would seem logical that because the action of the siphon it requires more energy to “prime” itself and flow than if the water were being pumped through the hard sleeve.  With that conclusion, we felt that dump site setup is critical when elevation is a factor and that the following options exist in such a situation;
  • Portable pumps
  • Drafting out of tanks directly and pumping back into other tanks

Overall Conclusions
After running the previous tests, we came to a few conclusions, which are listed below.  Understanding that without additional test gauges and more precise testing parameters, that the results have a known “approximation” built in, however, we can still consider the data is fairly consistent to use for “real world” purposes.

  • Regarding the pressure to pump the jet siphons at, we felt that the best results were at the 150 PSI PDP and that a flow of 125-150 PSI PDP will yield best results in most cases
  • Regarding how many jet siphons to use for water transfer, we felt that no less than two should be used as a standard practice between each tank
  • Regarding the hose supplying the jet siphons, we used 1 ½” hose, 1 ¾” hose may yield better performance due to lower friction loss
  • The use of the primary fireground supply pumper for water transfer beyond 2-3 jet siphons will impact its ability to deliver higher volumes to the fire scene.  With a flow of 160+/- GPM per siphon, this can add up quickly.  The operator should consider the flow of a jet siphon as equivalent to a typical 1 ¾” handline when factoring in total water supply.  Also, this water being used in each siphon is “recirculated” and never delivered to the fire, hence why we mentioned the “net” flow of each siphon.
  • Using a separate pumper for water transfer may be a preferable option at large scale fire events, to allow the primary supply pumper to flow its best possible capacity to the fire site.
  • When elevation is an issue, water can be transferred downhill, but not uphill beyond slight elevations when using jet siphons.  Dump site setup should consider this factor
  • The discharge end of the hard sleeve must remain above the static water line in the folding tank, failure to maintain this position will result in high likelihood of back flow, as when the flow stops from the jet, the transfer will tend to reverse itself and return the water back to the original tank.
  • Portable tanks on uneven ground will not hold their capacity, and additional tanks may need to be deployed on inclines to compensate for the lowered overall capacity
  • You can mark the liquid level of folding tanks, but doing so must be done on level ground and there must be an understanding that if the tank is uneven that the level will be inaccurate.  One way to make this issue more apparent is to mark opposite sides and compare the levels.  If nothing else, it serves to indicate an approximate liquid level, as most fires don’t happen on flat, level ground.
  • Water supply officers have a dity to collect additional suction hose, strainers and jet siphon devices from tanker and engine companies assigned to the operation, in order to be able to build an effective dump site.  Be familiar with thread size of hose and appliances used by mutual aid companies.
At the time we ran this rtest, we had no good information reporting the potential performance of jet siphons.  We were made aware that www.gotbigwater.com did some comprehensive tests in 2012, which you can find on their site.  http://www.gotbigwater.com/content/data/file/Jet%20Siphon%20Flowtests.pdf

Fairmount Fire Co. should be commended for quickly unloading and setting up all the required equipment and taking the time out of their evening to run these tests.  -Mike G.

19 August 2013

Protecting The Boardwalk in Ocean City New Jersey

The fire service is no stranger to overcoming adversity and challenges.  We have always been great at adapting and overcoming unusual situations with a combination of talent and now with the phenomenal technology we have access to these days.  The Ocean City Fire Department, in New Jersey is no stranger to doing just this.


Shore towns face their share of challenges with fire suppression duties, with limited access for full size apparatus and significant target hazards, particularly on boardwalks.  Modern fire codes have substantially reduced the number of major fires, but there still exists the potential for such an occurrence.  With these unique hazards being known, several east coast fire departments have a special purpose rigs designed to accommodate emergencies along the boardwalks in their response districts.  Ocean City NJ is the focus of this article, other such rigs can be found in Wildwood New Jersey, Rehoboth Beach Delaware and Ocean City Maryland, to name a few.

Ocean City NJ is approximately 10.7 square miles with a resident population of just over 11,000.  The summer vacation season brings an estimated 115,000-130,000 "residents" and visitors.  The city has everything from 1 story bungalows to multi-story high rise buildings and includes a sizable number of 2 and 3 story wood frame vacation homes with very limited spacing in between.  The city is protected by a very adequate public water supply system. The fire department in Ocean City is a fulltime department, and operates out of 3 fire stations in the city, manning 3 engine companies, a truck company and two ambulances, while utilizing off duty "recall" personnel to staff several reserve rigs and other specialty apparatus as necessary.

The City has a stretch of boardwalk that spans about 2 1/2 miles, roughly 10 of those blocks are heavily invested by the usual beach concession shops, restaurants, amusement parks and other tourist venues.  The boardwalk is fairly wide in much of its most populated areas, but narrows down as you get past those sections.  Several fires have struck in the boardwalk area in the past decade or so.  In 1893, a large fire devastated one of the original amusement parks built there, and again in 1927, a larger fire destroyed several blocks in the boardwalk vicinity.  A significant fire also struck at the Playland amusement park in 1961. They are no strangers to these types of fires.

Ocean City NJ 2005 Ford / Pierce Boardwalk Response Rig

The Boardwalk Rig in Ocean City New Jersey is a 2005 Ford Super Duty/Pierce.  It is what I refer to as a manifold wagon, where it has no pump or tank, rather it relies on a sustained water supply from a source pumper at street level.  The rig is designed to bring any of the critical necessary initial suppression and forcible entry equipment from the street, right up to the boardwalk.  The boardwalk rig is housed in fire station 1 at 6th St and West Avenue, which is in close proximity to much of the boardwalk.  It is manned as necessary based on its need.

Some of the highlights of what it carries are;
  • 800' 4" Supply Hose
  • 200' 2" Attack Line
  • 200' 2 1/2" Attack Line
  • Elkhart Portable "R.A.M." monitor
  • Elkhart 1000 GPM Rig Mounted Prepiped deluge set with portable base for deployment at ground level
  • (3) SCBA
  • Honda 3500W generator
  • (2) Rig mounted telescopic flood lights
  • (2) portable flood lights
  • Chain Saw
  • K-12 Saw
  • PPV Fan
  • Little Giant ladder
  • Tarps
  • Hand Tools
Floodlights and hooks can be seen here on the body

Gasoline powered equipment and other "Truck Company" equipment

The hosebed.  Note the LDH intake and gated discharges at bottom left

SCBA, additional lights and "Engine Company" tools on the drivers side
As you can see, this rig is well suited for its designed purpose.  Rigs like this are also valuable assets for locations where long narrow driveways or tight alleys can prevent access by full sized apparatus.

Fire departments must be diligent and identify the needs within their response districts and design apparatus and operating policies to best serve these needs.

Authors Notes;

Special Thank you to the Ocean City Professional Firefighters FMBA Local 27 for providing details and photos of this rig.  ~Mike G.

Visit the OCFD at www.ocfire.org
Visit the OCFMBA Local 27 at www.facebook.com/ocfmba27

You can also check out rigs from;
Wildwood NJ: http://www.wildwoodfirerescue.com/app396photos.php
Reboboth Beach De.: http://www.rehobothbeachfire.com/apparatus.cfm?a=4