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How Does “Automatic Flow Compensation” Work? Why Is It Needed?

We often receive questions  about “Automatic Flow Compensation.”  Automatic Flow Compensation was designed into MIG gas delivery systems since the  introduction of MIG welding in the 1950's.  It maintains the desired preset flow when spatter builds in the MIG gun nozzle, the gun cable or gas delivery hoses are bent and twisted, etc.  The following Q&A provides an explanation of how it works:

Question:  With no apparent feedback circuits or moving parts;  how does "Automatic Flow Compensation" work?

Answer: The needle valve or fixed orifice is controlling the gas flow and indirectly the pressure downstream of the flow control.   This occurs as long as the downstream pressure  is less than about 1/2  the upstream pressure (actually 2.1 times to be exact, but 2:1 provides sufficient accuracy for our purposes.)  This is called critical flow or choked flow.  Note all pressures are measured as absolute pressure which is gauge pressure reading plus atmospheric pressure or 14.7 psi (15 psi is sufficient  for our purposes.)

For a typical MIG system the pressure needed to flow gas through a feeder and gun will be only about 5 psi or 20 psia (absolute pressure.)  Therefore the minimum pressure upstream of the flow control (needle valve or orifice) needed to achieve critical flow is twice 20 psia or 40 psia.  40 psia stated as gauge pressure is 40 psia - 15 psi= 25 psi.  Then 25 psi is the minimum regulator or pipeline pressure needed upstream of the flow control orifice or needle valve.

Note: Although referred to as "Choked Flow" or "Critical Flow" it would be more accurate to call this phenomenon  "Choked Velocity!"  That is because the Velocity is fixed at the speed of sound but as the upstream pressure increases the gas density so the flow volume will increase-more on that below.

Question:  Intuitively, both the upstream and downstream pressure  should control flow; why when downstream pressure is less than 2.1 times upstream pressure does that no longer apply?

Answer:  It is correct that until the upstream pressure is 2.1 times the downstream pressure both pressures determine flow.  The flow equations are rather complex but flow rate can be calculated given both pressures, orifice size and gas type. 

However the gas velocity in the needle valve or fixed orifice can not exceed the speed of sound.  Therefore, for a given upstream pressure, once the gas velocity reaches the speed of sound in the orifice a further reduction in downstream pressure has no influence on flow.  Using flow equations the downstream  pressure that causes this "choked flow" to exist occurs when it reaches 1/(2.1) = 0.48 times the upstream pressure (both measured as absolute pressure, i.e. gauge reading + 14.7 psi at sea level. )  

Question:  Why is velocity limited to the speed of sound?

Answer: I recall an explanation given many years ago by my Fluid Flow Professor that may help  explain this phenomena.  When asked why the flow doesn't increase with a continued reduction in downstream pressure?  He said "It might if it knew the pressure was lower but the pressure wave telling it the pressure is reduced can only travel at the speed of sound so it never gets there to let it know!"   Not a technical explanation but it helps me remember what is occurring!

The pressure wave causing  sound only travels at a limited speed.  That is why you see lightening before you hear the resulting thunder!  The lightening is seen first since light travels at 300,000,000 m/sec while the sound produced travels at only 345 m/sec!

Question:    How does "Automatic Flow Compensation" control the downstream pressure?

Answer: The drop in pressure from pipeline or regulator pressure to achieve the desired flow  rate is controlled by the needle valve or orifice.  The pressure drops as gas flows through is very small passage.

When choked flow exists, the downstream pressure is controlled automatically by the fact that flow rate is being established in the needle valve or fixed orifice.  The downstream pressure will be whatever it takes to flow the gas coming through the orifice as long as the downstream pressure is less than about 1/2 the upstream pressure. The orifice flow is controlled only by the pressure upstream in that situation. Therefore as restrictions occur in the system, due to spatter build-up, twisted gun cables etc, the pressure will automatically raise to delivery that flow (or automatically fall when spatter is removed or MIG gun cables have less twist.)

Question:  If the speed of sound in the orifice determines flow, why does flow rate change with a change in upstream pressure?

Answer:  Even though the maximum velocity is the speed of sound  the density of the gas increases with pressure.  Velocity is  still the speed of sound but the volume of gas measured at Standard Pressure and Temperature (that is what is set in welding procedures and what is paid for) increases.

Question:  What happens when the pressure upstream of the orifice is  less than 25 psi, as is the case when low pressure devices are employed to reduce gas surge?

Answer: Comparative flow tests were made with a typical system having a delivery pressure of 25 psi (Photo Left) and a commercial low pressure system (Photo Right) that required a pressure of only 9 psi to flow the 31 CFH.  This particular low pressure system mounts at the wire feeder and includes a flow calibrated pressure gauge (note it does not say it uses low pressure to limit gas surge!)

In these tests both devices were set at 31 CFH with a restriction in the feeder/MIG gun system requiring 5 psi to flow that amount of shielding gas.  Restrictions were varied simulating spatter build-up in the gun nozzle, partially blocked gas diffuser, twisted cables and debris accumulation in the wire conduit which is often used as a gas passage in the MIG gun cable. These restrictions were added and removed.

The restriction pressure drop varied from 3 psi to 8 psi.  The flow settings in both cases were not changed, as if  flow controls were locked.

See flow results in table below:

Flow Control System

<Typical Production Restriction Range> 

3 psi

4 psi

5 psi

6 psi

7 psi

8 psi

Conventional = 25 psi

31 CFH

31 CFH

31 CFH

31 CFH

31 CFH

31 CFH

Low Pressure = 9 psi

37 CFH

34 CFH

31 CFH

27 CFH

23 CFH

16 CFH

 

Note actual flow was measured with a WAT PFM portable flowmeter at the gun nozzle (see photo right.)  As noted, the flow control device with upstream pressure exceeding 25 psi held the same preset flow of 31 CFH as the restrictions were varied from 3 to 8 psi. With the low pressure system, without any change in flow setting the flow actually varied from a high of 37 CFH to a low of 16 CFH!  This range is much larger than any acceptable Welding Procedure Specification would allow.  No wonder welders complain when flow drops below 20 CFH. 

The flow calibrated pressure gauge included with the low pressure "Surge Control" device read a constant 31 CFH while the flow varied from 37 CFH to 16 CFH.  The gauge is not reading flow but pressure above an orifice - which didn't change!  In this instance the pressure was only 9 psi well below the 25 psi needed to achieve  "choked flow."  Therefore the actual shielding gas flow changes when the inevitable flow restrictions occur while welding such as spatter build-up in the nozzle and gas diffuser.

In fact welders are smart and when the poor weld results are observed they increase the gas flow!  The flow calibrated  gauge included with this "Surge Guard" device may say 30 CFH  but that is NOT the actual flow, as observed in our test, can be only 16 CFH!   Welders logically increase the flow setting.  When restrictions are reduced they do not turn it back!  The "boss" may get mad an install a pad lock on the device believing the inaccurate flow calibrated pressure gauge!  Welder attitude is blamed for setting excess flows and wasting gas- when they were probably right in making adjustments! 

Sidebar:

Does that mean my regulator/flowgauge does not read accurately? NO IT DOES NOT!  These devices operate above 25 psi (typically 40 to 60 psi at practical flow rates) and in the "Choked Flow Range."  Preset flow is "Automatically Compensated" and the gauge reads accurately.  Note the red circle in the picture shows output gauge is calibrated in CFH NOT psi.

Some low pressure ad-on devices use even lower pressures and can create even larger flow variations.  The one shown in the photo right (yellow arrow) attaches to a standard flowmeter and sets flow by setting pressure.  Where the low pressure device test mentioned above changed 4 CFH with a 1 psi increase in flow resistance; in tests of this device the equivalent of a 1 psi increase in resistance caused the flow to reduce 8 CFH! 

Unfortunately some fabricators who have tried and rejected these devices are fearful our Gas Saver System (GSS)) may cause similar problems or welder rejection.  Our patented GSS  does not alter pressures and will not cause flow variations!  Welders appreciate the starting benefits!  See Overview of GSS

BE CAREFUL SOME OF THESE DEVICES DO NOT MENTION THAT THEY EMPLOY LOWER PRESSURE!! THEY MAY SAY THEY STOP OR "GUARD" AGAINST SURGE.  ALSO ANY DEVICE THAT MOUNTS DIRECTLY AT THE FEEDER WILL NOT PROVIDE SUFFICIENT EXTRA START GAS. 

EMAIL IF YOU HAVE A QUESTION ABOUT A SPECIFIC MODEL.

Question:  Are there production examples where low pressure devices have caused problems?

Answer: We have encountered a number of examples where  problems have been observed with low pressure devices and they were removed and discarded.  The following are four specific reported problems:

First Case.  A Welding Engineer at a large automotive parts supplier installed low pressure devices that mounted at the feeder and included a pressure calibrated flow gauge (the same device used in the tests mentioned above.)  Here are his quotes about the experience:

“After purchasing and using 32 low pressure gas saving devices (the same product used in our tests mentioned above) that mounted at the wire feeders we decided to discard all of them!  There were two major problems:

1) Lack of sufficient extra gas at the start made inferior starts and

2) Large flow variations from preset levels were evident when flow was checked at the MIG gun.  In fact as he stated; "Even if the flow was blocked, the flow calibrated pressure gauge supplied with these devices had the same preset reading!"

Second Case. A Welding Engineer at a major Midwest heavy construction equipment company was observing porosity in the same weldment in one plant and not in another.  He performed a very careful, systematic  analysis of the problem.  A fishbone troubleshooting diagram was developed with over 30 items considered in attempt to solving the problem.  It appeared to be a nitrogen porosity problem so he looked at all the possible causes.  He checked for pipeline, solenoid, feeder plumbing leaks, tested a cylinder gas supply to validate the quality of shielding gas and many others items.  He even tried a different type and manufacturer of the solid wire they were using. 

After all this testing and elimination of differences he found one major cause was the plant with the porosity problem was using low pressure surge reducing devices on their welders!  The same device as shown in the comparison test mentioned above. These were removed and the problems went away!!   Variability in flow was probably allowing nitrogen to enter the shielding gas stream.  If shielding gas flow rate is too high or too low this can occur. 

We find fabricators often use too high a flow rate.  Flow settings above approximately 50 CFH with a typical 5/8 inch ID gun nozzle are just pulling air with it's 70% nitrogen and moisture into the weld due to turbulence in the shielding stream.

Third Case: When evaluating the fittings needed for adding GSS's to 45 MIG welders at a bar joist manufacturer, it was observed that one installation had a low pressure regulator/flow control device mounted at the feeder (same device used in case 1 and case 2).  It had an output pressure gauge calibrated in CFH.  The maintenance manager indicated these had been installed on all welders several years before at a cost much higher than the GSS  and had to be removed due to inconsistent results!  The one remaining was adjusted at a very high flow rate according to the flow gauge reading. The maintenance manager indicated it would not be reinstalled and was surprised it was still there!

Fourth Case: A fabricator making Catalytic Converters had 70 new MIG Robots installed.  The systems integrator used a "surge guard" low pressure device mounted at the pipeline drop (this is a model of the device used in the above cases that mounts at the pipeline.)  Experiencing flow variations and seeing the information on our web site they were removed and replaced with conventional 50 psi calibrated flowmeters.  Flows at the MIG gun measured the same as the flowmeter reading even when spatter and other restrictions occurred in production.

Bottom Line: Low pressure at first appears to offer a solution to MIG weld start gas surge, as do flow restriction orifices  mounted at the feeder.  But both approaches create other larger, but less obvious problems!

You'll note the comments about lack of sufficient extra gas making inferior starts in one of the reported problem cases.  That will occur with any device that controls gas flow at the feeder, low pressure devices, flowmeters or simple orifices.  We have seen a number of problems caused by the use of this flow control location. 

A recent survey of a shop with 100 MIG welders having flowmeters mounted at the feeder showed all set with excess flow.  The shop uses 0.045 diameter solid wire.  No flowmeter was set below 50 CFH, about 25% were set at the highest reading on the flowmeter (65 to 70 CFH) and approximately 25% had the flow indicator ball pinned to the top of the flow tube!  Our tests show shielding gas flow can be as high as 125 to 150 CFH when the flowmeter needle valve is fully opened.  THE WELDERS WERE NO DOUBT TRYING TO COMPENSATE FOR THE LACK OF SUFFICIENT EXTRA GAS NEEDED TO PURGE THE WELD START AREA.

See a Technical Article About "Automatic Flow Compensation" Published in The American Welding Societies Technical Journal?     Click Link Below:

 

See Technical Article discussing Automatic Flow Compensation Published in AWS Journal April 2007

See Other Questions and Answers; Click Link Below:

Q&A About Extra Gas Needed at Weld Start

Q&A About Ideal Gas Delivery Systems

 

 

 

 

 

Save over $1000 per year per welder and improve weld starts with Payback measured in weeks!!
* US Patent  # 6,610,957;  "Welding Shielding Gas Saver Device" August 26, 2003,  Patent Pending in other countries.  
 The "Flow Rate Limiter" device is covered by 2008 US patent # 7,462,709.  Other site material may be covered under  Patents # 7,015,412 or # 7,019,248 .
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Last modified: 01/30/12

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