Hello again-
I am happy to announce that our facility is now complete, and we just need a couple of safety items before we can start production and testing. I will post pictures in a week or so when we get the final components.
--Derek
Wednesday, October 3, 2007
Monday, August 27, 2007
Biodiesel update
Hello again-
The project has been making good progress (despite my infrequent updates to this blog). I am happy to announce that we have been given the green light by the metro air regulations committee and the VEHS office to start construction of the system. Thanks to Brad Berron and the VEHS office who put together the major components of our application.
Our shed is almost complete now (I will post pictures soon), and we should be able to finish the system construction and start brewing soon. It is very nice and will suit our needs very well. Feel free to stop by and see its current progress on the northwest corner of the power plant lot. We need to think of ideas for the name for the shed (biodiesel shed and brew haus have been suggested), so let me know if you have ideas.
Thanks again to all of you who have helped, and feel free to contact me (derek.riley@vanderbilt.edu) if you are interested in getting involved.
The project has been making good progress (despite my infrequent updates to this blog). I am happy to announce that we have been given the green light by the metro air regulations committee and the VEHS office to start construction of the system. Thanks to Brad Berron and the VEHS office who put together the major components of our application.
Our shed is almost complete now (I will post pictures soon), and we should be able to finish the system construction and start brewing soon. It is very nice and will suit our needs very well. Feel free to stop by and see its current progress on the northwest corner of the power plant lot. We need to think of ideas for the name for the shed (biodiesel shed and brew haus have been suggested), so let me know if you have ideas.
Thanks again to all of you who have helped, and feel free to contact me (derek.riley@vanderbilt.edu) if you are interested in getting involved.
Monday, July 2, 2007
Udall bus tour
Hello again-
Yesterday the UDall biodiesel bus stopped by to see Vanderbilt and the biodiesel initiative, and it was an excellent event. All the biodiesel machinery and the new Wilskills biodiesel van were on display, and everyone seemed to have a great time and learn a few things as well. Keep an eye out in the Vanderbilt Register for an upcoming article about the project!
Monday, May 14, 2007
Biodiesel update
Sorry it has been so long since my last update, but the end of the semester has been exceedingly busy for me. I have several updates to share with the group:
Our biodiesel is currently being used by plant operations equipment and they seem to be quite happy with its performance so far.
We now have bumper stickers supporting the project and advertising its use on the vehicles which use the biodiesel, so keep an eye out on campus for tractors and mowers with our stickers. I have more stickers, so let me know if you want some.
We have started using KOH (caustic potash) instead of NaOH as the reaction catalyst. It has many benefits and adds minimal costs to the final product.
I have been experimenting with soap and degreaser production and I think I have a viable recipe for it now. However, I have significant limitations when it comes to picking out pleasant "scents," so if you are interested in lending your nose to helping choose a smell for our liquid soap, let me know.
Our move onto campus will hopefully be happening sometime during June, so keep your schedules open during that month if you are interested in helping construct the building and moving the equipment.
Our biodiesel is currently being used by plant operations equipment and they seem to be quite happy with its performance so far.
We now have bumper stickers supporting the project and advertising its use on the vehicles which use the biodiesel, so keep an eye out on campus for tractors and mowers with our stickers. I have more stickers, so let me know if you want some.
We have started using KOH (caustic potash) instead of NaOH as the reaction catalyst. It has many benefits and adds minimal costs to the final product.
I have been experimenting with soap and degreaser production and I think I have a viable recipe for it now. However, I have significant limitations when it comes to picking out pleasant "scents," so if you are interested in lending your nose to helping choose a smell for our liquid soap, let me know.
Our move onto campus will hopefully be happening sometime during June, so keep your schedules open during that month if you are interested in helping construct the building and moving the equipment.
Monday, April 16, 2007
First Full Batch!
Hello again-
This last weekend we accomplished several project goals. About 10 members of the biodiesel group congregated in my back yard on Saturday to help brew the first full batch of biodiesel in the processor, and the operation went quite well.
It was a cool morning, so the oil started at about 60 degrees, so I used the centerfuge to heat and filter the oil until it was was 120 degrees which took about 2.5 hours. Robin is currently building us a small heater for the system so we can more precicely control the temperature without the use of the centerfuge. The rest of the process went well, although it took a long time to get the lye to dissolve in the methanol.
That being said, we decided to discuss the design of the methoxide mixing system, and I picked up a damaged washing machine for its pump and motor. We took apart the machine and tested its functionality (which was fine), but we decided that we will need to make some adjustments to the plumbing and wiring to make it ideal for a methoxide mixing system. In the next few weeks we will build the mixer and test it.
To avoid the problem of the glycerol congealing, I drained the glycerol in stages (every 30 minutes or so). The glycerol flowed well, although to avoid this problem in the future and to improve the soap-making prospects, we are going to investigate the use of KOH instead of NaOH as a catalyst. KOH will cost more than double (adding $.07/gallon to the final product cost), but it won't congeal with poor oil, and it will produce a liquid soap which is easier to work with than the soap bars from the lye byproduct. Keep checking here to see our progress on this task.
After the biodiesel was finished reacting and draining, I added .5% magnesol by weight (about 10 cups worth), and I mixed it completely. I then ran the centerfuge for 1.5 hours to clean out the magnesol. To run it optimally, I actually used the porportioning valve to decrease the pressure to 40psi. I did this because the normal 90psi that the pump produces causes the centerfuge to spin at very high speeds and eventually it slows (most likely due to friction). It seems that running it at 40psi alleviates this issue.
I had to clean the centerfuge once and it was obvious that it needed cleaning because I could hear that it was slowing down and almost stopped. When I took it apart, it was almost completely full of magnesol, so it performed its task properly and it was pretty easy to clean. Once I have drained the tank and I have taken apart the final filter, I will get a better idea of how much magnesol the centerfuge didn't remove. So far, it looks like adding more centerfuges will significantly increase the speed and contamination capacity of the filtering system. Our 1.5 HP pump should be able to drive several centerfuges at 40 psi if that is necessary. I am also testing the filtration waste product as a fertilizer in my garden. Keep posted for those results as well.
This last weekend we accomplished several project goals. About 10 members of the biodiesel group congregated in my back yard on Saturday to help brew the first full batch of biodiesel in the processor, and the operation went quite well.
It was a cool morning, so the oil started at about 60 degrees, so I used the centerfuge to heat and filter the oil until it was was 120 degrees which took about 2.5 hours. Robin is currently building us a small heater for the system so we can more precicely control the temperature without the use of the centerfuge. The rest of the process went well, although it took a long time to get the lye to dissolve in the methanol.
That being said, we decided to discuss the design of the methoxide mixing system, and I picked up a damaged washing machine for its pump and motor. We took apart the machine and tested its functionality (which was fine), but we decided that we will need to make some adjustments to the plumbing and wiring to make it ideal for a methoxide mixing system. In the next few weeks we will build the mixer and test it.
To avoid the problem of the glycerol congealing, I drained the glycerol in stages (every 30 minutes or so). The glycerol flowed well, although to avoid this problem in the future and to improve the soap-making prospects, we are going to investigate the use of KOH instead of NaOH as a catalyst. KOH will cost more than double (adding $.07/gallon to the final product cost), but it won't congeal with poor oil, and it will produce a liquid soap which is easier to work with than the soap bars from the lye byproduct. Keep checking here to see our progress on this task.
After the biodiesel was finished reacting and draining, I added .5% magnesol by weight (about 10 cups worth), and I mixed it completely. I then ran the centerfuge for 1.5 hours to clean out the magnesol. To run it optimally, I actually used the porportioning valve to decrease the pressure to 40psi. I did this because the normal 90psi that the pump produces causes the centerfuge to spin at very high speeds and eventually it slows (most likely due to friction). It seems that running it at 40psi alleviates this issue.
I had to clean the centerfuge once and it was obvious that it needed cleaning because I could hear that it was slowing down and almost stopped. When I took it apart, it was almost completely full of magnesol, so it performed its task properly and it was pretty easy to clean. Once I have drained the tank and I have taken apart the final filter, I will get a better idea of how much magnesol the centerfuge didn't remove. So far, it looks like adding more centerfuges will significantly increase the speed and contamination capacity of the filtering system. Our 1.5 HP pump should be able to drive several centerfuges at 40 psi if that is necessary. I am also testing the filtration waste product as a fertilizer in my garden. Keep posted for those results as well.
Sunday, April 1, 2007
First batch of biodiesel
Hello again-
Last Thursday we brewed our first batch of biodiesel (20 gallons), and I am proud to announce that it was a complete success. We had a few issues with the glycerol solidifying in the pipes, but once they were heated, the glycerol drained and we ended up with a good batch.
We used .5% magnesol by weight without heating and it seems to have sufficiently cleaned the biodiesel although it wasn't the super clean biodiesel that we were able to get using 2% magnesol. The centrifuge cleaned out the magnesol, but some residue was left in the bottom of the tank, which means that a cone-bottom tank will be necessary for optimality.
I have put 10 gallons of the clean biodiesel in my diesel truck, and after driving around with it yesterday (to pick up more components for the system), it seems to perform well. It seems that there is a slight power loss, but not enough to effect normal driving. The engine definately runs smoother and quieter, and the exhaust has the distinct smell of a fryer. We will be delivering the balance of the biodiesel to Plant Operations at Vanderbilt for testing in their equipment.
--Derek
Last Thursday we brewed our first batch of biodiesel (20 gallons), and I am proud to announce that it was a complete success. We had a few issues with the glycerol solidifying in the pipes, but once they were heated, the glycerol drained and we ended up with a good batch.
We used .5% magnesol by weight without heating and it seems to have sufficiently cleaned the biodiesel although it wasn't the super clean biodiesel that we were able to get using 2% magnesol. The centrifuge cleaned out the magnesol, but some residue was left in the bottom of the tank, which means that a cone-bottom tank will be necessary for optimality.
I have put 10 gallons of the clean biodiesel in my diesel truck, and after driving around with it yesterday (to pick up more components for the system), it seems to perform well. It seems that there is a slight power loss, but not enough to effect normal driving. The engine definately runs smoother and quieter, and the exhaust has the distinct smell of a fryer. We will be delivering the balance of the biodiesel to Plant Operations at Vanderbilt for testing in their equipment.
--Derek
Monday, March 26, 2007
System Update
Sorry, it has been a while since my last post, so I will use this opportunity to get everyone up to speed on our current progress.We found out that we did not win the MTVU grant, but we have found a few sources of funding at Vanderbilt, so we have actually started construction.
I ordered the components and the design and construction comittee met over the weekend to put a preliminary system together. I am happy to announce that we have a fully functional processor, although it has several improvements that need to be made. Here is a picture of the full system (it is currently located in my shed).
It is designed so it is compact and easy to move. The blue drum has a capacity of 55 gallons, so the system will initially be able to process 40 gallon batches. We are using this as a pilot so we can better understand the process and tweak the design for a larger processor in the future.
The black pump below the blue tank is a 1.5 HP pump that is used both for recirculation and powering the centrifuge. The white cylinder to the left of the pump is the final filter to ensure that no contamination will be in the final product.
In this picture you can the the pump (with the yellow wire coming out of it) and the white filter. There are a series of valves to allow us to use the pump to recirculate the oil, draw in oil from an outside source, and run the centrifuge. The valves also allow us to drain the glycerol after it settles.
The next picture is a picture of the top valves. The left side recirculates the oil (at about 15 GPM), and the right side sends the oil to the centrifuge. It also has a pressure gauge to help us monitor the system and centrifuge performance. Currently the centrifuge runs at about 85psi which is in it's optimal filtering band. It filters about 2GPM and spins at almost 9000RPM, although it actually doesn't make much noise surprisingly. The centrifuge is designed to be a replacement for a filter on large diesel engines, so it is quite rugged and well built.
Running the centrifuge also heats the oil about 20-30 degrees (F), and given that it is currently summer, we have decided to not worry about adding a heater to the system for now. We hope to run our first batch of biodiesel sometime this week.
Subscribe to:
Posts (Atom)
