Skip to main content

Uncertainties and their estimated maximum errors in field measurements using Pitot tube for air flowrate calculations

Introductory

Air balancing, trouble-shooting, and system evaluation in dust collection and industrial ventilation systems all require accurate measurements of air flowrates.

Normally, the Pitot tube and magnehelic gauge (or manometer) are used to measure the velocity pressure and static pressure inside of a duct (round or rectangular), and then the air flowrates are calculated based on the measured values.

This article talks about 5 kinds of uncertainties that always happen in field measurements using Pitot tube, the estimated maximum errors with some of them, and how to avoid some uncertainties with recommendations from manuals and standards (ISO 3966 and NF X 10-113).

Pitot tube and magnehelic gauge to measure static pressure and velocity pressure



 

Uncertainties, maximum errors, and how to avoid some of them

In addition to the inherent errors from Pitot tube and gauges themselves (calibration, resolution, drift, etc., sometimes with the correction factor of Pitot tube involved), there are other errors we have to pay attention to in the process of measurements.

  • The uncertainty in the positioning of the Pitot tube inside the duct. This component can be significant in some cases, so precautions must be taken to minimize this uncertainty component.

a. The stem diameter of the Pitot tube should not exceed 1/30 (1/20 from another source) of the test duct diameter.

   If the stem diameter exceeds 1/30 of the test duct diameter alone, it will introduce at least 0.1% increase of the air flowrate, while 1/20 will introduce at least 0.25% increase of the air flowrate.



b. The misalignment of the probe end with airflow should not be more than 5 degrees. When the Pitot tube is correctly aligned, the pressure indication will be at a maximum.

    If the misalignment of the probe end with airflow is more than 5 degrees, it will introduce at least 0.8% decrease of air flowrate.

So, the air flowrate measurement is more sensitive to misalignment than to the stem diameter of the Pitot tube.

c. A complete and accurate Traverse has to be made. The Pitot tube should move back and forth in line up with the diameter line of the duct.

 

  • The uncertainty in picking traverse position.

a. Some manuals state that the readings should be taken 7.5 duct diameters or more downstream and 2 duct diameters or more upstream from any major air disturbance, such as an elbow, hood, transition, takeoff, damper, or branch entry.

  Most of the time, even this recommendation is difficult to apply for measurements on site, because conditions of straight lengths are often not available, and because it’s not always possible due to reasons of size, space, set-up cost etc.

b. ISO 3966 and NF X 10-113 standards recommend the minimum number of points and minimum distance away from disturbances required for circular and rectangular ducts. However, practical ventilation systems rarely have straight lengths able to comply with the conditions described in the standards.

c. An empirical formula was developed to evaluate the maximum error accompanied with the uncertainty of traverse position.

For example, on a 12” diameter duct, the table below shows clearly that, if conditions of straight lengths are not available, then two or more traverses and more measuring points on each traverse can be applied as kind of a compensation to reduce error in the measurements.

In the table:

k is traverse number,

p is measuring point on each traverse,

L is distance between the traverse position to the disturbance upstream, and,

D is the diameter of the duct.

k

p

L/D

Max Error

1

8

7.5

4%

2

8

7.5

1.9%

1

8

20

2%

2

8

20

1%

1

8

4

6%

1

10

4

5%

2

8

4

3%

2

8

2

4.9%

 

  • The uncertainty caused by not knowing the humidity in the air flow. Most of the time, humidity is not measured on site, and air flowrate calculations are simply based on the assumption of dry air.

a. For example, saturated air at 135 F, elevation of 719ft, and static pressure of -15” H2Og, if assumed as dry air, then the calculated air flowrate will be about 1.2% lower than the real value.

b. The higher the air flow temperature, the lower the calculated flowrate of the saturated air than the real value.

  • The uncertainty of knowledge of the inner duct section

a. Blockages, dirt, ruptures, etc. inside the duct also contribute to wrong Velocity Pressure measurement. VP is a vital parameter and most essential input for proper flow computation.

  • The air flowrate measurement scheme proposed in standards is often time-consuming and field technicians prefer to simplify them.

a. Measure only one traverse (most of time, with rotation angle and tilt angle, sometimes not in line up with the diameter line of the duct).

b. Move the Pitot tube inch by inch to get readings without consideration of duct diameters, sometimes, only measure the center velocity pressure.

c. Insert the flexible hose end into the hole to measure static pressure, and this is definitely wrong.

d. Pick a traverse location by experience, sometimes, at random.

In these cases, measurement errors occur, and the estimation of measurement error is not known.

Air Balancing, Trouble-shooting, and System Evaluation services by Airvate

Due to the importance of field measurements using the Pitot tube, it’s important to spend time accurately measuring with it. Airvate LLC offers reliable Pitot tube measuring and also the following services, so feel free to email Airvate at info@airvate.com to get the help you need:

·  Dust collection system and industrial ventilation system testing and Air Balancing

·   Dye test for bag leak

·  Technical services: field survey and dust collection system evaluation and trouble-shooting

·   New system start-up

·   Dust sample analysis

·  Dust collector selection and sizing: baghouse, wet scrubber, cyclone, settling chamber, drop-out box, etc.

 

Comments

Popular posts from this blog

What you have to know when applying blast gate damper

  Introduction A damper is a device that adjusts the volume of airflow passing through the outlet, inlet or duct. By proper adjustment of all dampers in a system, a desired distribution of airflows in all the branches can be obtained, while minimizing the total airflow of the system to save energy— this is also termed air balancing. The most common dampers used in industrial ventilation and dust collection systems to balance airflows are slide gate dampers (The slide gate, also called “blast gate or cut-off” damper). In a slide gate damper (see Figure 1 of a straight flat slide gate damper), the slide is inserted perpendicular to the flow. Figure 1 A sample of straight flat slide gate damper As the gate is sliding into the duct, it will add resistance to the airflow and consequently reduce the volume of airflow, while increasing airflows in all other branches. Withdrawing the gate has the reverse effect on that branch and all the others in a system. Interaction between a fan ...

Push-pull ventilation system for open surface tank saves air flow

  Three sections in this blog: Push-pull ventilation system and its advantages Disadvantages of general ventilation and side exhaust systems Methods to design a push-pull ventilation system Push-pull ventilation system and its advantages Open surface tanks used in industrial processes often need ventilating to remove harmful pollutants (vapors, fumes or aerosols) from the working environment. One method of removing pollutants is the so-called side push-pull ventilation system, in which a jet of air is blown (or pushed) from one side of the tank and collected (or pulled) by an exhaust hood on the opposite parallel side. This system is particularly useful for large tanks where access requirements preclude the use of an overhead canopy, and the size of the tank makes side (or rim) exhaust systems prohibitively expensive. Most agree that a push-pull ventilation system can yield air savings of up to 50% compared to a side suction only hood. An illustration of a push-pull system for an o...

Baghouse Dye Test for leak detection

  We did a Dye test for a customer in a newly installed baghouse. In this standard dye test procedure, green fluorescent dye powder was applied. No leaks were found in the clean plenum of the baghouse. All the bags were properly installed and no breach between the clean air and dirty air plenums was found either. View of Clean Plenum after Dye applied Per the request of our customer, we also got inside the dirty side of the baghouse through the inspection door on the hopper and visually checked dye powder distribution on the bags. From the picture below, it is apparent that the dye powder evenly distributed on all the bags, which means that the airflow was evenly distributed too. Customer was very happy about this visual check. Bottom View of Bags after Dye Applied