UPDATE 1: Fuel selection
Now that I’ve decided to make an RDE I immediately want to jump into CAD and start building the different parts. But because I don’t know what I’m doing, before that I’ll have to determine the minimum dimensions of the motor to ensure stable operation. This is luckily made very easy as the equations to determine this have been not only found before but conveniently packaged in “Small-size rotating detonation engine: scaling and minimum mass flow rate” by S. Connolly-Boutin1. The main take away from this article is that the dimensions of the RDE are determined by the detonation cell size. Detonations are formed out of a whole bunch of cells. The size of these cells will vary based on variables such as the type of gas detonated and the pressure the detonation is under. The smaller the cell size the smaller a mass flow rate I have to run.
Just to remind you I’m trying to have the minimum possible flow rate to reduce the likelihood I make a bomb, decrease the cost of gas per firing and to shrink the size motor making manufacturing easier. The first step in finding the geometry of the motor is to choose what gas I want to use.
What do I need in a fuel?
RDE’s can run on a variety of fuels. Basically, anything that detonates can be used as a fuel for an RDE. Most real examples of RDEs choose to use fuels like hydrogen, ethene, or methane. This is largely because these are fuels already in use in the rocketry industry. They are chosen based on a large number of factors such as their energy density and availability on other planets. However, for my purposes this is all really irrelevant. The properties of a gas that I care about is.
1. Small detonation cell size
The small cell size as previous mentioned is needed to reduce the mass flowrate of motor. However, this is not the only or even the most important factor in the selection of a gas for my project.
2. Availability
Availability is also of key concern. I am an undergrad student who is working on this currently with no affiliation with any other organization. So, I’m going to have to approach gas suppliers and ask for an unreasonably small amount of a highly dangerous gas and hope they don’t ask to many questions. For gases like acetylene or propane this probably isn’t going to be an issue but for the more specialized fuels I might run into some restrictions that prevent me from getting a hold of the fuel.
3. Cost
Another limitation of me being a uni student is that my budget for this project is very low. Remember I’m hoping to keep the total project cost to below $1500. The fact that a single cylinder of ethylene containing 1.8m3 of the gas costs roughly $500 a third of the total budget. Fuel costs seem like they have the potential to be the most expensive part of the project. The cheapest possible fuel would be ideal.
4. Safety
I understand that the very nature of the fuel needing to be explosive makes them inherently dangerous. However, I would like to keep this danger to a minimum. Ideally the gas will only be dangerous because it is explosive and preferably not carcinogenic, generally toxic, or radically unstable.
Which fuel am I going to use?
I don’t know. So, I’m going to assume I’m using all of them. The equations given are very simple and can easily be set up in an excel in a way that will let me do the geometry calculations for every fuel at once. While this may be marginally more work than just picking the fuel with the lowest detonation cell size it will make comparing fuels based on their other characteristics far easier. Also, in the very likely event that I choose the wrong fuel and change my mind later I would have already done all the calculations for the right one.
Calculations
The equations I will need to use are the following. Where
λ = detonation cell size (all cell sizes were found from GALCIT Explosion Dynamics Laboratory Detonation Database)
Detonation database reference | Chemical formula | Fuel – Oxidiser | Cell size | Pressure | Cell size at 101kpa | Annulus thickness min | Critical fill height min | Chamber length | Min chamber diameter | M dot min | M dot max |
mm | kPa | mm | mm | mm | mm | mm | kg/s | kg/s | |||
at5a | H2 | hydrogen-air | 9.21 | 101.45 | 9.06 | 12.68 | 63.42 | 616.06 | 245.12 | ||
at57d | CH4 | methain-O2 | 2.38 | 101.30 | 2.34 | 3.27 | 16.35 | 158.81 | 63.19 | 2.74 | 16.15 |
at21a | H2 | hydrogen-O2 | 1.39 | 99.00 | 1.34 | 1.87 | 9.37 | 90.98 | 36.20 | 0.90 | 5.30 |
at154a | C3H8 | propane – O2 | 8.25 | 13.87 | 1.11 | 1.55 | 7.77 | 75.49 | 30.04 | 0.62 | 3.65 |
at128b | C2H4 | ethene – O2 | 4.72 | 11.43 | 0.52 | 0.73 | 3.66 | 35.54 | 14.14 | 0.14 | 0.81 |
at57f | C2H2 | acetylene – O2 | 0.17 | 102.64 | 0.17 | 0.24 | 1.18 | 11.50 | 4.57 | 0.01 | 0.08 |
Finding an optimal fuel
Comparing the selection of 6 different fuel/oxidizer combinations gives us a good place to start when choosing a fuel. The smallest cell size comes from acetylene. This is fantastic news. With a minimum diameter of only 4.5mm and mass flowrate of 10-80g per second creating a small scale RDE within my desired specifications seems not only possible but conveniently easy. This is because acetylene has the added benefit of being very common meaning you can purchase it in small amount for a relatively low cost ($131 per m3). Its ubiquity in industry also means that there is an abundance of gas piping equipment such as mass flow rate regulators and check valves available for it. Acetylene being the best choice in terms of cell size is for my purposes the best outcome I could have hoped for.
Unfortunately, there is a catch. After jumping for joy at the prospect of being able to use such a common gas I found a problem. Acetylene is relatively unique in that it is not compressed into pressure vessels. Instead, it is dissolved into acetone and kept under pressure. Once that pressure is released the acetylene comes out of solution and out the top of the bottle. The issue with this is that this severely limits the maximum mass flow rate that these bottles are capable of. A rule of thumb is that you should not let out more than 1/15th of the volume of the cylinder per hour of use. For most industrial applications this is not an issue however for my application I need a small volume of gas to be released very quickly at very high pressures. To achieve this with acetylene without a pump requires a manifold cylinder array. From BOC this starts at $3187. More than doubling the budget on fuel alone as well as making the logistics of transport much more difficult this unfortunately eliminates acetylene from the feasible options.
Moving up the list the two next best options in terms of cell size are ethene and propane. Propane would be the more ideal option of the two. This is largely because it is cheap, readily available as LPG and has acceptable minimum geometry requirements. However, one of the reasons that LPG is so reasonably priced and easily accessible is because it is stored in relatively low-pressure cylinders. BOC’s LPG cylinders only hold the gas at 700kpa. This is an issue as part of my design requirements is that I will not be using an external pump and will be relying entirely on bottle pressure to run the system. Having such a low pressure increases the likelihood of back flash in the engine and decreases its ability to deliver an adequate mass flowrate. Ethene (AKA ethylene) remedies this problem being stored at 6900kpa significantly increasing its ability to resist back flash and gives the best chance of supplying an adequate sustained mass flow rate. However (there is always a however) ethene comes with the minor drawback that it’s a controlled substance. Only available for agricultural and scientific purposes not amateur rocket programs.
Not with a bang but a whimper
Throughout this update we have identified the characteristics of an ideal fuel for our use case. Completed calculations for the approximate geometry of a small scale RDE and compared these criteria against actual fuels available. The results of this are that there currently isn’t a fuel that meets all the criteria that is needed for my application. To be clear small scale RDEs are not an unproven technology. Universities and research institutions make them all the time. However, the major difference between myself and them is that I was a little optimistic with the budget required for this project. Having also briefly looked into the cost of safe and appropriate plumbing system for this system I found the project budget fall far short of what would be required. For the reason that with the current resources available to me I would not be able to create a safe system that follows the theory, I’m going to put this project on the back burner. Who knows maybe when I start working in industry, I might be able to throw $10,000 at this project and see it become a reality. But for the minute with a uni budget this doesn’t seem feasible.
3 Responses
Id put money in don’t have to buy everything at once.
🤯 would love to get in on this.
Hi, my name is Mario Cestari, it wold be a pleasure try to help you. Find my LinkedIn, I am an undergraduate mechanical engineering student from Brazil.