|
|
General Liquid/Water Cooling Discussion For discussion about Full Cooling System kits, or general cooling topics. Keep specific cooling items like pumps, radiators, etc... in their specific forums. |
Thread Tools |
07-18-2002, 12:02 PM | #51 | |
Responsible for 2%
of all the posts here. Join Date: May 2002
Location: Texas, U.S.A.
Posts: 8,302
|
Quote:
I think that what we're talking about here involves 2 things: 1-The efficient part of the pump (say 70%), which moves the water, which heats up due to friction. 2-The inefficient part of the pump (the remaining 30%), which includes (but not limited to) heat, which heats up the water through the pumps housing. This is reduced if the pump is in-line. |
|
07-18-2002, 12:16 PM | #52 |
Cooling Savant
Join Date: May 2002
Location: home
Posts: 365
|
The tubing portion is pretty easy to explain. It acts very much like a spring in a mechanical system. It will stretch (dilate) when a pressure gets applied. This stretch is very minor, but represents some finite change in system volume. The storage energy is simply delta-P (running versus stopped) times the system volume. It's not so easy to calculate, but is completely immaterial. Once you reach steady-state, stored energy has no bearing on the matter.
|
07-18-2002, 12:35 PM | #53 | |
Responsible for 2%
of all the posts here. Join Date: May 2002
Location: Texas, U.S.A.
Posts: 8,302
|
Quote:
So that leaves what I was saying, which is that the energy (efficient part) supplied by the pump, fights friction, which turns into heat. I'm at the end of the tunnel now... I think! Let me try to apply this info: Let's say that I set up a rig. It doesn't matter what it is, as long as it's the same. In rig A, I use a 1000 gph pump, and I achieve a 200 gph effective flow rate. In rig B, I use a 400 gph pump, and achieve a 100gph flow rate. (pump sized accounting roughly for the increased restriction at the higher flow rate) I get a higher flow rate in rig A than in rig B, but I'll have induced twice as much energy in the water. Does that look about right? |
|
07-18-2002, 01:59 PM | #54 |
Responsible for 2%
of all the posts here. Join Date: May 2002
Location: Texas, U.S.A.
Posts: 8,302
|
Another bit, while I'm walking out of the tunnel...
Some people at OC (from the link posted in this thread) seem to think that an increased mass of water would make a difference. I disagree. Since we're inducing heat, in the form of a heat source (say 7 watts, for our little 1048), from its efficient part, the heat is "applied" to the water over time, regardless of the mass of the water, which can be translated into work. This heat will be dissipated by the rad, as it achieves the balance point, between ambiant air, and the water temp. Since the rad dissipates the same heat, and reaches the same balance point, the increase in mass of the water would only delay reaching that balance point. My other step-outside-the-tunnel is this: couldn't we calculate this heat, if we knew the exact (effective) flow rate? Let's say that we have 100 gph. The work performed by moving 100 gallons of water over a time period of 1 hour, that can be calculated, can't it? What if the density of the coolant was less (or more) than that of water? Would it make any difference? I'm guessing no, but why? |
07-18-2002, 02:20 PM | #55 |
Cooling Savant
Join Date: May 2002
Location: home
Posts: 365
|
Yeah, I'd say you're reaching daylight now.
First let's look at your 1000 vs 400 gph pump example. Simply because one pumps 200 gph while the other does 100 gph doesn't tell us too much. What you need to know is how much energy the motor uses. We can assume that the 1000 producing 200 gph is running at a lower efficiency since it is pumping 20% of "rated" flow vs 25% for the other. This may be a bad assumption, however, as flow vs head (and efficiency) curves differ for different pumps. If you have a chart of efficiency vs flow (commonly efficiency gets graphed right along with head vs flow), then you can answer the question. If not, you must measure power consumed by the motor. Regarding your "volume of water present" bit, you are entirely correct. Ultimately, volume has zero bearing if we run the system long enough to reach steady-state. All it does is factor into how long it takes to reach steady-state. If you want to pick nits, you can argue that more volume requires more surface area (tubing, reservoir, etc) and this added surface area aids the radiator in dispelling heat. Yeah, whatever. Unless the reservoir is relatively large, its convective heat loss will be peanuts next to a good radiator with sufficient flow of ambient air. Finally, for your question of calculting "the power of moving 100 gph". Sure, power is nothing more than flow rate multiplied by delta-P. If you can measure delta-P (ala BillA's manometer explaination a few days back), then you can determine the useful work of the pump. You also asked about density. Density alone doesn't have much bearing on flow power. In an open system where suction and discharge are at different elevations, sure, but not in a closed system. Viscosity really determines flow for a given pump and piping system. Lower viscosity = higher flowrate. As viscosity increases, pressure drop versus flowrate decreases. Total pressure drop tends should remain reasonably constant as the lower viscosity gets offset by higher flow. |
07-18-2002, 02:20 PM | #56 |
Responsible for 2%
of all the posts here. Join Date: May 2002
Location: Texas, U.S.A.
Posts: 8,302
|
For those with a knack for physics, check this out.
Let's see... Watts can be calculated as Joules/seconds. I'm moving 100 gallons of water, over 1 hour, or 60 minutes, or 3'600 seconds. How do I get the Joules? |
07-18-2002, 02:36 PM | #57 |
Cooling Savant
Join Date: May 2002
Location: home
Posts: 365
|
As the old commercial says, "Sorry Charlie". You can't get there from here. You need delta-P.
It may help to take a gander at the units in their base form. Energy has units of force * length. Power has units of force * length / time. Flow has units of length^3 / time. In order to get power based on flow, the units need to come out right. What are the missing units? Well, divide power by flow and you have (force * length / time) / (length^3 / time) = force / length^2. Recognize that? What if I said lbf / in^2 (psi)? To calculate flow power you require flow rate and pressure rise. No two ways around it. |
07-18-2002, 02:41 PM | #58 |
Cooling Savant
Join Date: Jun 2001
Location: Connecticut
Posts: 140
|
Actually my statement was based on experience as well as common sense. I have run waterblocks all nite with just a pump and no radiator and there is a noticeable amount of heat in the water after some time. On the other hand, by running the same test setup with a radiator, the difference between water temps. and ambient is not even noticeable.
Like I said, a good radiator makes this whole debate really a moot point. Unless you are approaching or at the limits of your radiator, pump heat is nothing to be concerned about. bigben, I love how you keep your systems updated with the latest technology. I have a clawhammer CPU I will send you when I am done. |
07-18-2002, 02:45 PM | #59 | |
Responsible for 2%
of all the posts here. Join Date: May 2002
Location: Texas, U.S.A.
Posts: 8,302
|
Quote:
|
|
07-18-2002, 02:50 PM | #60 |
Cooling Neophyte
Join Date: Jul 2002
Location: TX
Posts: 54
|
I'm pretty sure that if your density is greater and your volume is the same your mass will be greater which means you will be doing more work. (well at least most of the time it does, in some cases mass can get canceled out ( I've learned this after many tricky engineering physics ))
It seems that density is very closely tied to viscousity also, I'd be interested in a liquid that is more dense than another but yet less viscous. -Sidney |
07-18-2002, 02:52 PM | #61 |
Cooling Neophyte
Join Date: Jul 2002
Location: TX
Posts: 54
|
Also the point about pump heat being fairly moot with a radiator may be true for ambient cooling, but it's not for sub ambient cooling, you want the least amount of heat into your system as possible so you can have the coldest temps going to your components.
|
07-18-2002, 02:57 PM | #62 | |
Responsible for 2%
of all the posts here. Join Date: May 2002
Location: Texas, U.S.A.
Posts: 8,302
|
Quote:
So I need to know the pressure drop between the pump inlet and outlet, as well as the effective flow rate. |
|
07-18-2002, 03:04 PM | #63 | |
Responsible for 2%
of all the posts here. Join Date: May 2002
Location: Texas, U.S.A.
Posts: 8,302
|
Quote:
I need a viscosity table! I believe that mercury, although lots denser, might have a similar viscosity as water. Does anyone know? (It doesn't mean that mercury is a better coolant, we can look into that some other time!) |
|
07-18-2002, 03:08 PM | #64 |
Cooling Neophyte
Join Date: Jul 2002
Location: TX
Posts: 54
|
Mercury is a much better coolant it is about 16 times better than water... just really dangerous and I think pretty hard to pump, but maybe not.
-Sidney |
07-18-2002, 03:10 PM | #65 | |
Cooling Savant
Join Date: May 2002
Location: home
Posts: 365
|
Quote:
Actually, there's plenty of examples. Water is more dense than oil, yet has far less viscosity (especially at low temperatures). Water is actually pretty unique in its cooling abilities. Its heat transfer characteristics are better than darn near everything and its viscosity is also lower than darn near everything else. Too bad it doens't do well below 0°C. But that's where additives come into play. |
|
07-18-2002, 03:16 PM | #66 |
Responsible for 2%
of all the posts here. Join Date: May 2002
Location: Texas, U.S.A.
Posts: 8,302
|
Ok, fluid viscosity, measured in Pa*s for
Water at 0C=1.8 * 10^-3 Water at 20C=1.0 * 10^-3 Mercury = 1.55 * 10^-3 Note: Liquid viscosities tend to decrease with increasing temperature From http://www.phys.virginia.edu/classes...ds2/node2.html and http://www.mas.ncl.ac.uk/~sbrooks/bo...01/node13.html |
07-18-2002, 03:19 PM | #67 |
Cooling Neophyte
Join Date: Jul 2002
Location: TX
Posts: 54
|
Hmm yeah thats true I forgot about water and oil. Well I guess density doesn't necessarily affect viscosity. I have tried looking up better liquids and the only one that I could find was mercury it's thermal conductivty is 8.something and water is about 0.6
|
07-18-2002, 03:24 PM | #68 |
Responsible for 2%
of all the posts here. Join Date: May 2002
Location: Texas, U.S.A.
Posts: 8,302
|
Yeah, mercury is nasty stuff!
http://danpatch.ecn.purdue.edu/~epad...src/poison.htm http://www.healthyvermonters.info/hp.../mercury.shtml |
07-18-2002, 03:27 PM | #69 |
Cooling Savant
Join Date: May 2002
Location: home
Posts: 365
|
*sigh* Nothing is ever as cut and dried as you would like. There are two measures of viscosity, dynamic (absolute) and kinematic. The difference between the two is inclusion or exclusion of the material's density. In dynamic terms, the viscosity of mercury and water isn't so different and if water didn't freeze they would be equal at ~ -5 to -10°C. In kinematic terms, mercury's density makes its viscosity much, much lower than water's.
IIRC, its the absolute viscosity that goes into calculating pump flow rates, but don't quote me on that one. |
07-18-2002, 03:27 PM | #70 |
Cooling Neophyte
Join Date: Jul 2002
Location: TX
Posts: 54
|
Hmm well if mass doesn't affect the pump then I guess you can use mercury no problem (except for the toxicity problem). Maybe someone should try that, would look really neat in some tygon tubing, just make sure that your tubing won't absorb it (You sure don't want mercury vapor around you).
-Sidney |
07-18-2002, 03:30 PM | #71 | |
Responsible for 2%
of all the posts here. Join Date: May 2002
Location: Texas, U.S.A.
Posts: 8,302
|
Quote:
Mercury is very, very nasty stuff! If you spill it, it will be released in the form of vapors, and your body can absorb a lot of it, very quickly!!! You can't even pick it up with a paper towel, because if you touch it, you'll absorb even more!!! |
|
07-18-2002, 03:35 PM | #72 |
Cooling Neophyte
Join Date: Jul 2002
Location: TX
Posts: 54
|
Yeah I know, although I don't think it's as bad as they make it sound because I personally have played with the stuff and didn't get sick or anything (touching it pushing it around messing with it quite a bit), and that was when I was only about 7 or 8 so I should have been affected much quicker than an adult. (What can I say I was a curious kid and found a mercury filled thermometer).
Edit: Although I don't suggest that anyone do what I did, or that anyone actually mess around with mercury. -Sidney Last edited by 000; 07-18-2002 at 03:40 PM. |
07-18-2002, 03:54 PM | #73 |
Responsible for 2%
of all the posts here. Join Date: May 2002
Location: Texas, U.S.A.
Posts: 8,302
|
It certainly would take care of a few problems though: corrosion, algae, ...
(Note: don't even think about it!) |
07-18-2002, 04:04 PM | #74 |
Cooling Neophyte
Join Date: Jul 2002
Location: TX
Posts: 54
|
Hehe, that's very true. And for the people using chillers they wouldn't have to worry about it freezing And you could see really easily if you were leaking any.... or you could just do a self evaluation (am I going mad... am I going mad...) hmm might not work for some people though
I imagine it's fairly hard to get a large amount of the stuff though (probably a good thing ) |
07-18-2002, 04:15 PM | #75 |
Responsible for 2%
of all the posts here. Join Date: May 2002
Location: Texas, U.S.A.
Posts: 8,302
|
Well, I found an internet link, but I don't want to post it.
They sell it for over $260 per pound, and seeing that a cubic foot of it weighs about 850 (eight hundred and fifty) pounds, I'm sure that it's not a lot, in volume. Also, since it is hazardous, it'd be VERY expensive to ship. |
Currently Active Users Viewing This Thread: 1 (0 members and 1 guests) | |
|
|