Good afternoon.
Further to my last posting of February 02, 2009, and later posts from Mr. Guest, I offer the following comments and clarifications.
Hopefully, Mr Guest’s posts will reappear for clarification.
The subject matters noted below follow the same layout as my earlier noted post.
1. Glycol as a lubricant in a steam engine.
The comments that I posted on 02/02/2009, indicating that glycol in the steam could either prevent the steam oil from emulsifying with the moisture in the steam, or cause the oil to disassociate from the water/oil emulsion are valid, and in accordance to discussions with a manufacturer of specialty steam oils.
If, in fact, the oil does separate (disassociate) from the emulsion either in part, or in whole, the steam oil will not be able to provide an adhesive oil coating on the sliding parts. It will simply pass through the engine and exhaust as separated oil.
This concern can be verified by anyone who wishes to do so by placing a telephone call directly to any such oil manufacturer, such as I did.
Rather than influence the outcome of such a call by providing the name of the specific manufacturer that I consulted, I suggest that anyone who wishes to pursue an indepedant verification simply google “steam oil”, or “steam engine oil”, and place a call to any listed manufacturer in order to discuss the issue.
2. Glycol enhancing the visible steam discharge.
Mr Guest’s most recent posts of February 05, 2009, questioned the validity of my comments detailing why little, if any, glycol would actually be carried out of the boiler in the steam discharge. He indication that this reasoning “appears to be based on a memory of distillation from school science lessons”, and also notes that “When two liquids are miscable then the resulting solution usually has properties that are markedly different from the seperate liquids”.
In point of fact, the principle of separating water from a glycol/water solution by heat is scientifically proven, well known, and is a common practice in industry.
For example:
The company I work for is a leading designer, manufacturer and supplier of, amongst other products, glycol dehydration equipment that is utilized in the process of refining and purifying natural gas.
Natural gas, when extracted from the ground, contains various impurities that must be removed prior to the release of the gas into public, or industrial markets. Most natural gas, when extracted, is water saturated. As such, the water must be removed through a dehydration process.
One of the most effective methods for this is the process of glycol dehydration, where the water saturated gas is passed through ethylene glycol which has a very high natural affinity for water. During this process, virtually 100% of the water present in the gas is absorbed by the glycol, permitting the now dry natural gas to be moved off into another part of it’s refining process.
The resultant glycol/water solution is then sent into a boiler, and heated to a temperature not exceeding 260 degrees F. As I noted in my earlier post, the water, having a much lower boiling point than ethylene glycol, vaporizes, and is drawn off as low pressure steam. The remaining liquid in the boiler has now reverted to near 100% glycol, and is then cooled, and cycled back into the dehydration process. The validation of the effectiveness of this process is the fact that the separated glycol rarely needs to be topped up, or compensated, for a loss of it’s original volume, or quality.
The above process is, as I have noted earlier, scientifically proven.
It is also virtually identical to the operation of a model steam boiler.
When Mr Guest experiences a trace of glycol, either visibly, or by smell in the steam discharge of his boiler, it is likely due to “carry over”. Carry over is the result of turbulance in the boiler which occurs at the water surface. As a bubble is formed on the water surface, the outer surface skin of the bubble contains a film that includes glycol. This miniscule ammount of glycol is carried into the steam above the water surface when the bubble bursts.
This would also explain why doubling the ammount of glycol in the boiler does not appear to double the increase in the visible steam discharge.
It should also be noted that ethylene glycol starts to breakdown, or decompose, when heated to temperatures of over 260 degrees F, which is why the temperature of the described dehydration process is limited.
If anyone wishes to examine the actual chemical process for the above, and the characteristics of water and glycol when mixed into a common solution, please note that there is an abundance of scientific data available on the web from various accredited sources. Simply google “natural gas dehydration”, dehydration process”, ethylene glycol”, etc.
3. Glycol contamintion in the steam dischage to atmosphere.
I believe my comments stand.
If a person googles “commercial fog machines”, etc., they will not only find descriptions of various fog generators, but also comments concerning the release of ethylene glycol into an