Showing posts with label Savanick. Show all posts
Showing posts with label Savanick. Show all posts

Tuesday, July 23, 2013

Waterjetting 11b - Abrasives and cutting depth

In the past few posts I have been discussing the use of abrasive in waterjet cutting, and in this and the next two posts I would like to talk a little about the abrasive feed rate (AFR), abrasive size and the selections for the best cutting performance. As with my other posts I can only write in general terms about these because the combination of waterjet system, nozzle design and abrasive selection will change the best values to use, and the results on different systems will differ in some way or other from the results I will mention. However in all cases the overall principles remain the same, and can be applied as general rules.

In the last post I noted that cutting performance fell as the average size of the abrasive fed into the system dropped below 100 microns. As part of that study we looked at the amount of abrasive that survived going through the mixing chamber in that size range. A simplified average of the results obtained are shown in the following table:


Figure 1. Percentages of the initial feed that survive at larger than 100 microns, for differing feed conditions.

In an earlier post I had mentioned the “Green Tube” test that was used at Missouri S&T as a way of measuring the particle size and speed, after the particles had passed through the nozzle, but without hitting a target. Because the distance that the particles travel is a function of the energy they obtained during mixing, some idea of the overall particle energy can also be obtained.

However, when the particle sizes were analyzed at different distances from the nozzle we noted that there was a large percentage of small particles in the short distances from the nozzle, but that as the particles were collected at greater distances from the nozzle, so the average particle size grew larger.

After thinking about this for a short while, the reason became obvious, and – at the same time – made it a little more difficult to draw simple conclusions from the test.

The reason for the greater collection of smaller particles nearer the nozzle is that they are decelerated more rapidly than the larger particles, once they start traveling through the air. If we go back to the basic equation that we learned in school:

Force = mass x acceleration

For a given particle, the force to accelerate the particle in the mixing chamber will, simplistically, be the pressure exerted on the particle by the water, multiplied by the cross-sectional area of the particle. If the particle is a sphere, with a diameter d, then the area be π x(d/2)^2. But the mass of the particle is a function of the volume, which is related to the cube of the diameter. Thus the acceleration, for a given particle size and at constant fluid pressure, will vary inversely with the diameter of the particle. In other words the smaller particles will accelerate faster in the mixing chamber and focusing nozzle.

Once the particle leaves the nozzle, however, the acceleration from the water is replaced by a deceleration as the particle is now moving through air that is relatively stationary. Now the situation is reversed and it is the smaller particle that decelerates faster, and thus will have a shorter effective range than particles that survived the mixing process in a larger size. This was therefore the explanation for the results that we saw in our tests.

Unfortunately life becomes a little more complicated than this when the nozzle is held close to the target. This is because, while the air between the nozzle and the target may be relatively stationary, at greater distances, the small gap means that the surrounding air is also drawn into the slot and flows with the stream along the cut. There is thus less resistance to the particles, which retain their energy to a greater distance – improving cutting depth. However that also changes if the jet is cutting through layers where there may be water or air in the gaps between the layers.

This work was carried out initially by Dr. George Savanick during work carried out at the then US Bureau of Mines, on cutting rock. It applies in other cases, however, since there are often times when cuts are needed between two work pieces with a gap between them. (The example in mind is cutting through the different tubes that bring oil out of a well. This casing can be made up of several different diameters of pipe, ranging perhaps from a 20-inch diameter outer pipe to a 3.5-inch diameter inner one, with other tubes between). What Dr. Savanick showed was that if the gap between the layers was filled with some relatively soft material that provided little resistance to cutting, but held its shape and provided confining walls on either side of the jet, that the range of the jet could be extended beyond that where the jet was cutting water or air between the layers. These factors then play a part in determining how far an abrasive jet will cut through material.

Often it is not just the ability of the jet to cut through the material, but also the straightness of the cut and the quality of the edge that are important. If, for example, one can be sure that there are no burrs on the edges of a cut between two overlapping layers of material, then the parts may not have to be separated, cleaned and re-assembled before being fastened together. This elimination of several manufacturing steps can significantly lower the cost of assembling, for the sake of discussion, aircraft components. In turn this may then justify the use of the AWJ system as the better manufacturing tool, even when it does not seem that the initial cutting process is much cheaper than the alternative.

I mention these considerations, because as I go through the different applications of these tools I can only be somewhat general in discussion of overall effects. The way in which the abrasive mixes with the water, the amount of particle breakup and the different speeds of the abrasive leaving the nozzle vary with the nozzle design and operating conditions. They are also tailored to an extent by the particular job that has to be completed. Thus a recurring piece of advice in this series will be to find a test piece of material and test out a range of options before committing to the final cut. The series will try and suggest where that range might be, but in the final decision I do not have the equipment or other conditions that exist in your shop, and thus only you can be the final judge.

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Tuesday, January 29, 2013

Waterjetting 5c - flow straighteners

One of the advantages that became clear, even in the early days of waterjet use in mining, was that the jets cut into the rock away from the miner. It was thus a safer method of working, since it moved the person away from the zone of immediate risk. Rock has a tendency to fall when the rock under it is removed, and by using the jets to carry out the removal, so the miner is no longer as vulnerable.

But, in the early days of jet use the range of the jet was quite limited. Part of the reason for this is that the water is generally brought to the working place along the floor. It then has to be raised, through bent pipes, to the level of the nozzle, and then turned so that the water in the pipe is flowing in the direction in which the nozzle is pointing.


Figure 1. Sketch of an early Russian waterjet mining monitor

Even though the pressure of the jet is relatively low, the volume flow rates were high, and the bends leading into the nozzle set up considerable turbulence in the jet, so that the range of the jet was quite limited beyond the nozzle. There are a number of different ways of improving the range of the jet, and I will discuss these in later posts, and many of these techniques apply whether the jet is being used at high volume and low pressure for mining, or at higher pressures and lower flow rates for cutting into materials. But today the technique that I will discuss is the use of flow straighteners.

The two most dramatic instances that I immediately recall for their use were at the Sparwood mine in British Columbia, where the collimated jet was able to mine coal up to more than 100 ft. from the nozzle, and in an underground borehole mining application where a Bureau of Mines commissioned system was able to cut a cavity to more than 30 ft. from the nozzle, which was centrally located.

Collimating jets to get better performance is not restricted to the mining industry. A visit to Disney, for example, will find jumping jets that appear to bounce from place to place (video here) (this one shows the start of the surface waves along the jet, known as Taylor instability, which grow and cause the jet to break up; and if you want to make one Zachary Carpenter has two instructional videos on how they are made. (here and here.)

Essentially, as those Youtube segments show, the flow straightness is achieved by dispersing the water – using a sponge – so that it flows through a large number of drinking straws. These straws act to collimate the water flow, and it emerges as a glassy rod, which even acts as a light path so that light shone down it emerges at the far end. This can be used for a variety of different purposes, other than just for entertainment.

This then is the basic idea behind a flow collimator, although for larger mining flows drinking straws are too weak, and the flow volumes need to be larger. There are various designs that have been used for mining applications. Some of the earlier trials were at the Trelewis Drift mine, where the then British National Coal Board set up an experimental operation.


Figure 2. Sketch of Monitor used in the NCB Trials (after Jenkins, R.W., "Hydraulic Mining" The National Coal Board Experimental Installation at Trelewis Drift Mine in the No 3 Area of the South Western Division, M.Sc. Thesis, University of Wales, 1961.)

A number of different designs were used for the flow straighteners that were located at the nozzle end of the straight pipe section leading into the nozzle:


Figure 3. Designs for the initial flow straighteners used at Trelewis Drift (after Jenkins, R.W., "Hydraulic Mining" The National Coal Board Experimental Installation at Trelewis Drift Mine in the No 3 Area of the South Western Division, M.Sc. Thesis, University of Wales, 1961.)

More recent designs, which vary according to pressure, flow rate and pipe diameter, are a combination of those on the left above, and those on the right. It was such a combination that allowed the Canadian miners at Sparwood to achieve production rates of 3,000 tons of coal per shift as an average over the operation of a mining section.

While the use of flow straighteners does not give any gain over having a long straight section of pipe leading into the nozzle, it can bring the flow condition up to that level in places where the geometry (or the resulting unwieldiness of the pipe) would make the long entry impractical.

One of the more interesting applications of this is in the borehole mining of minerals. Simplistically a hole is drilled, from the surface down to the seam of valuable mineral. Then a specially designed pipe is lowered through the hole with the pipe having a nozzle set on the side. Then, as the pipe rotates, and is raised and lowered, the jet mines out the valuable mineral, which flows to the cavity under the pipe, where it is sucked into a jet pump and carried to the surface.


Figure 4. Schematic of a borehole mining operation (George Savanick)

As I mentioned at the top of the article, the jet cut a cavity some 30 ft in radius, with the jet issuing through a nozzle some 0.5 inches in diameter. In order to achieve this range it was important that the jet was properly collimated, yet the nozzle was set so that there could be no straight section.


Figure 5. Section showing the feed into the borehole miner nozzle. Note the vanes in the section leading into the nozzle (George Savanick).

The turning vanes to achieve the flow collimation were designed by Lohn and Brent (4th Jet Cutting Symposium) to produce a jet equivalent to that achieved had the nozzle been attached to a straight feed.


Figure 6. Turning vanes used to achieve a jet capable of cutting coal to 30-ft from the nozzle. (P.D. Lohn and D.A. Brent “Design and Test of an Inlet Nozzle Device” paper D1, 4th Int Symp on Jet Cutting Technology, Canterbury, BHRA 1978)

Tests of the performance of the nozzle showed that it produced a jet that was at least equal in performance to a nozzle with a straight feed, up to a standoff distance of 45 ft.

In simpler applications the designs do not need to be that complicated, for many simple spraying nozzles, for example, the straightener is made up of a simple piece of folded metal.


Figure 7. Simple flow straightener for use in low pressure and flow applications.

The water has now reached the nozzle, but that is not the end of the story of the feed system, as I will start to explain, next time.

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