That is a problem I do not understand since PSI is a pressure unit and not a force unit.
Do you need to work at the given pressure or do you want to have a force? In the second case please indicate the units so that the pressure can be computed.
I worked on a similar system 6"id X 1 1/2" stroke 1800psi [hydraulic pressure] 20 strokes per minute.
20hp running a 20gpm pump & a 30 gallon reservoir. A air cooled heat exchanger was utilized since the cylinder was mounted in a fairly hot location, for the same reason 20 wt oil.
All the valves, flow controls & pump were Vickers. This set-up was very reliable, most of the problems were related to the heat & that the cylinder was also moving back & forth @ the same 20 cycles.
These units ran 24hrs, 6 1/2days/week, 360 day/yr.
I think the cooler was not so much a result of the ambient temperature but the friction of the continuously forced oil.
We had a machine that bends steel sheets into shapes and it also suffered from the oil heating up although the volumetric calculations were correct. The type of valves used make a lot of difference. In the end we had a lot of air cavitation which can cause considerable damage. The cooler was perfect as it did the job and reduced the heating needed for the operator as he stood in the hot wind from the fan all day long
This particular cooler set up was the worst part of the system, when the relief valve was by-passing the oil flowed through the cooler. @ 20 stroke/min this wasn't enough. [around 1/4-1/3 sec/cycle]
The operating conditions included a cylinder about 6 meters [of pipe] away from the valves.
The cylinder was mounted on top of [2] 1square meter platens @ about 350 degrees F
the oil in the area of the cylinder, didn't have enough flow, contributing to thermal breakdown. The cylinders had metal rings allowing a small amount of blow by. We tryed cheveron seals [rubber]on the pistons and the oil would overheat & boil in the vicinity of the cylinder.
the oil only lasted about 6 months.
The check valve in the bypass/cooler circuit would some times allow pressure spikes to the heat exchanger, the HE's would be good for a couple of years, before the welds would stress crack. A couple of rounds of repairs were about it, after that you were just junkies chasing crack!
Given the option I would have used a small auxillary pump to cool & filter the oil
Even with these limitations, still a very reliable set up, the failures were mostly heat or vibration related. There are 10 of these lines @ this production facility & hundrends corporate wide.
A cylinder of 2.5" ID will usually have a rod of 1.5" dia.
15 x Vol of cylinder extending = 5.43 Lt/min
15 x Vol of Cylinder retracting = 3.475 Lt/min (anulus vol)
Vol required = 8.905 Lt/min
Area of cylinder = 4.909 in2
1750/4.909 = 356.5psi = 24.59 Bar (THIS MIGHT BE A WRONG ASSUMPTION)
(24.59 x 8.905)/600 = 0.365kW
Mec Eff = 0.8 therefore = 0.456kW
Direct drive, Single Phase Motor of 2,900 RPM would require (gear) pump of 3.07 cc/rev conected to a reservoir of about 20Lts Vol (not including air space).
Anyway, what was the question?
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"A common mistake people make when trying to design something completely foolproof is to underestimate the ingenuity of complete fools!" Douglas Adams 1952-2001. E&OE!
Your solution based on considering 1750 as a force (lb) not pressure (psi), why? may be there is a mistake in data given by our friend bwire.
I know your assumption, but what will happen if we considered it as a pressure, 1750 psi = 120.658 bar, it will be 5 times your figure 24.59 Bar. I interest to hear from bwire the exact unit psi or lb.
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It is better to be defeated on principles, than to win on lies!
I have got tons of engineering programs on my computer and somewhere I have actually seen PSI Force. I've spent half the night looking but I'm buggered if I can find it!
Your perfectly correct in saying that my assumptions would be a factor of five out if incorrect and I did think of giving the answer with PSI as a pressure. It might have been the logical solution.
At least the volume of the reservoir should be 'good to go' dependant if this is a mobile or factory based system, with or without cooler etc, etc!
I think that, at least if we are 'transparent' with our workings, they can be accepted or disputed rationally. This question is a bit like using a calculator, sh*t in, sh*t out!
Many thanks for your comments though!
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"A common mistake people make when trying to design something completely foolproof is to underestimate the ingenuity of complete fools!" Douglas Adams 1952-2001. E&OE!
I expect will be cylinder pressure about 800 psi and force of 1.875 ton. I think I think I can do all well with 1.250 ton force but want extra 4 testing.
Thank you for contributing.
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If death came with a warning there would be a whole lot less of it.
Unless you get your cylinder built as a special size, you probably won't get a 1" rod on a 2.5" bore. The standard would be either:-
a) 2.5" Bore to 1.5" rod.
b) 2" Bore to 1.25" rod.
c) 1.5" Bore to 7/8" rod.
If you expect a working pressure of 800psi then you have the scope to reduce the size of the cylinder and increase the pressure of the pump and still maintain the working force required. A standard gear pump should be good for a little over 3000psi.
This would also reduce the amount of stored oil required in the reservoir although I would agree with a previous commentator that it is better to cool with convection (dependant on local ambient temperatures) so, probably keep reservoir volumes higher rather than lower.
If you do reduce the size of the cylinder, you may need to consider the 'slenderness ratio' although with a 4.5" stroke it is probably irrelevant!
Good luck with it!
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"A common mistake people make when trying to design something completely foolproof is to underestimate the ingenuity of complete fools!" Douglas Adams 1952-2001. E&OE!
I assume that pressure is 1750 PSI. Considering losses the system pressure has to be at least 2000. Based on 2.5"cylinder and in the assumption that the cylinder is NOT symmetrical with a rod 1.5" the pump has to deliver at least 9 L/min =2.4 gpm.
Motor power for a global efficiency of 0.8 is 2.6 kW.
If the reservoir has a capacity of more than 30 L it is possible to avoid a cooler since free convection over the reservoir lateral area can evacuate the 20% losses by an oil /air temp. difference of 40°C. A bigger reservoir has the advantage that oil is less stressed and will maintain a longer time its characteristics. Convection area has to be > 1.5m^2
In order to avoid not necessary losses it would be positive to have a small accumulator able to take the pump delivery during the commutations at each end of stroke. Care has to be taken for choice of valves and filtration of the oil. For a system running as mentioned it is most important to filter as low as possible( 1µ) since the very small particles of dirt in oil are the most aggressive and the most wear generating. Although pressure is not high it would be positive to use a ram with servoseals low friction and also long life. V-cups could present a too fast wear and require maintenance. The summ of strokes/year is over 1100 miles so that seals have to be able to accept it.