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EN 14359 Gas-Loaded Accumulators — Scope, and Where Gas-Law Sizing Fits

EN 14359 — Gas-loaded accumulators for fluid power applications

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EN 14359 is the European standard that defines the requirements and test methods for hydraulic accumulators used in fluid power systems — covering bladder, piston and diaphragm types from small pilot accumulators to large energy-storage vessels. It is a pressure-equipment construction and testing standard: design, materials, temperature limits, pressure testing and conformity under the Pressure Equipment Directive (PED) 2014/68/EU. Choosing the SIZE of accumulator for a duty is a separate engineering calculation — the gas law on real nitrogen (in its ideal low-pressure form, P·Vⁿ = constant), which describes how the nitrogen charge expands and compresses as system pressure cycles between the minimum working pressure P₁ and the maximum working pressure P₂ — and the P₀ ≈ 0.9 × P₁ precharge is manufacturer guidance.

It is the reference document for accumulator construction across European hydraulic machine design — used for PED conformity of the vessel. MechanixCalc does NOT implement EN 14359: its accumulator calculator performs the gas-law application sizing (an engineering estimate), returning the total gas volume V₀ over the operating temperature range (the precharge defined at the maximum temperature, the size taken at the temperature that delivers least), the gas volumes at the band limits (V₁, V₂), the gas-temperature range of the cycle, the fill pressure at the workshop temperature, a nominal size, every limit check with its source, the PED category per Annex II Table 2 for the nitrogen side (PS = the larger of P₂ and the relief setting), and a branded PDF engineering report with the substituted formulas. The vessel itself must still be selected from a maker whose accumulators conform to EN 14359.

Video walkthrough (6:16)

  1. 0:00 Why the ideal gas law isn't good enough
  2. 0:30 The job: 10 L between 150 and 250 bar
  3. 0:47 Where does the precharge go?
  4. 1:40 How fast does it run? Same press, double the vessel
  5. 2:47 What it caught: −28 °C gas and a nitrile bladder
  6. 3:37 Why 72 L of gas needs a 100 L unit
  7. 4:04 Will the 80 L unit on the shelf do?
  8. 4:32 What a senior engineer checks before signing
  9. 5:38 The report, and what the tool doesn't do
Read the transcript

A lot of accumulator calculators use the ideal gas law. Between 90 and 400 bar, nitrogen doesn't behave that way. It's stiffer.

The ideal law overstates the oil you get by 4 to 58 percent, and it's on the unsafe side every time.

This is the MechanixCalc accumulator calculator. It sizes bladder, piston, diaphragm and bellows accumulators on real nitrogen, and shows every check with its source. So let's size one properly, and see what changes.

Here's the job. A press needs 10 litres of oil, between 150 and 250 bar. The shop runs from 10 °C in winter to 50 °C beside the power pack in summer.

A bladder accumulator, nitrile bladder, hydraulic oil. The usual choice.

First question. Where does the precharge go? For energy storage, the makers' rule is no more than 90 % of the minimum pressure, at the hottest temperature. Here, 135 bar at 50 °C.

Why the hot end? Gas pressure rises with temperature. Set it on a cool day, and by summer the precharge is above your minimum pressure. Then the bladder closes on the poppet at the bottom of every stroke.

Nobody fills an accumulator at 50 °C, though. So the tool gives you the workshop number. At 20 °C, with the oil side drained, fill to 119.4 bar. And there's a gauge table for whatever day you check it.

The other side of that coin. On a 10 °C morning the same charge reads 114 bar, and the accumulator gives less oil. So the size is taken at the cold end.

Next question. How fast does it run?

If the oil came and went slowly, the gas would stay at room temperature. That's the slow, isothermal case. 36.5 litres of gas.

Cycle it fast, back to back, and the gas heats on the way in and cools on the way out. It's a stiffer spring. 62 litres.

But a press does neither. It charges, then sits there, and the gas settles back to room temperature. Then the cylinder takes the oil in one fast stroke, and the gas expands and chills. 72 litres.

Same machine. Same 10 litres. 36 or 72, just from how fast it runs. That's double the vessel.

If you know your real cycle times, the timed model sits in between. About 65 litres with these times. When in doubt, take slow charge, fast discharge. It's the conservative one.

And for comparison, the catalogue short-cut, a fast compression straight from the precharge, says 48 litres. For a press that sits charged and fires, that's a third too small.

Now the checks. Precharge, fine. Pressure ratio, 2.2 to 1 against a limit of 4. Fine.

But one says CHECK.

After the press has sat charged, a fast discharge drops the gas to −28 °C. A standard nitrile bladder is good to −15 °C.

The bladder wall won't follow the gas all the way down. But do that every stroke, and nitrile goes brittle and cracks. And it's the expansion that does it, not the weather.

The tool gives you the ways out. A lower pressure ratio, a slower discharge, or a low-temperature compound. And it says to confirm with the maker. Which is what you'd do anyway.

So let's take one. Low-temperature nitrile, good to −35 °C.

And the check clears.

72 litres of gas. So you order an 80-litre accumulator. And you'd be short.

The number on the nameplate isn't the gas volume. The bladder and the poppet take up room, and a datasheet can list as little as 85 % of it as gas. 80 litres can mean as little as 68 litres of gas. So the tool recommends the next size up, 100. And the datasheet's effective gas volume is the number that counts.

Which brings up the question you get on site. There's an 80-litre unit already on the shelf. Will it do?

If this press cycled back to back, yes. 11 litres.

But it sits charged and fires. Taking 85 % as gas, it gives 9.4. About half a litre short at the cold end. Put in the datasheet's real gas volume before you write it off.

The 100-litre unit gives 11.8. With the low-temperature bladder, that's the one to buy.

Before you sign it off, the safety step. On the gas side this is a PED category IV vessel. The test pressure has to be at least 393 bar.

Now a trap. Pressurise it on a cool morning, valve it off, and let the plant warm up to 50 °C. The trapped gas and oil climb to about 319 bar. The system relief can't see it, it's on the other side of the valve. And this vessel is set up for 275.

So it sits on a safety block. An isolating valve, a relief between that valve and the accumulator, and an unloading valve that dumps the oil at shut-down.

Through a 1.5 mm bleed orifice, that takes about four minutes. Then the oil side reads zero. The gas side doesn't. It still holds its precharge. Never take the accumulator off until the nitrogen is let down through the charging kit.

It also covers who inspects it and how often, and the nitrogen bottles to charge it.

Working in psi and gallons? One click, and every number follows.

All of it goes into the PDF. The method, every check with its source, the fill table, and that hot-day FAIL, in red, until you deal with it.

What it doesn't do: it doesn't design the shell. That's the vessel maker's job, under the construction standard, and the tool says so.

Real nitrogen. The right cycle. The cold end. The nameplate read properly. And the cold-gas check and the hot-day trap dealt with. Those are numbers you can put your name to. Size your next accumulator on MechanixCalc.com.

What EN 14359 covers

  • NOT in EN 14359, which is a pressure-equipment construction and testing standard: APPLICATION sizing — the total gas volume V₀ needed for a usable delivery ΔV between P₁ and P₂, via the gas law along the isotherm (slow cycles) or the isentrope (fast cycles) — on REAL nitrogen, since the ideal-gas form P·Vⁿ = const undersizes by 4–58 % at hydraulic pressures. This is the calculation the MechanixCalc accumulator tool performs, with the Span et al. (2000) reference equation of state
  • Gas precharge selection — the P₀ ≤ 0.9 × P₁ rule that keeps the bladder or piston off full extension is long-standing MANUFACTURER guidance rather than a clause this hub can cite to EN 14359; the makers define P₀ at the MAXIMUM operating temperature; the tool follows that, evaluates the sealed charge at both ends of the operating range on real nitrogen and sizes on the end that delivers least, and gives the fill pressure at the workshop temperature
  • Accumulator types — bladder (most common; gas and fluid separated by a flexible elastomeric bladder), piston (separated by a sliding piston; handles larger volumes and higher flow rates) diaphragm (separated by a metal or elastomeric diaphragm; compact, low-volume applications) and welded metal bellows (no elastomer, gas-tight; the bellows' stroke limits the usable volume)
  • Pressure testing and safety margins — hydraulic proof-test pressure and pneumatic precharge test requirements; maximum allowable working pressure (MAWP); safety valve setting guidance
  • PED 2014/68/EU conformity assessment — EN 14359 is a HARMONISED standard under the PED, so compliance with it supports presumption of conformity; the CATEGORISATION itself (Category I self-declaration through Category IV notified-body assessment) is set by PED Annex II from the pressure-volume product and fluid group, not by EN 14359
  • Materials and temperature ratings — bladder and seal material compatibility with hydraulic fluids; operating temperature range

Governing formulas

One gas mass on real nitrogen — application sizing basis (not an EN 14359 clause)
V₁ = V₀ · ρ₀/ρ₁ ; V₂ = V₀ · ρ₀/ρ₂

where All pressures ABSOLUTE (gauge + 1.013 bar). ρ₀ = nitrogen density of the charge (the precharge P₀ at the maximum operating temperature); ρ₁, ρ₂ = density at P₁ and P₂ on the cycle's path at the governing temperature — the isotherm (slow), the steady isentrope of continuous fast cycling (fast), the isotherm to P₂ then the isentrope from P₂ (slow charge, fast discharge), or the energy balance with heat exchange through the shell for a timed cycle — from a real-gas equation of state (Span et al. 2000). The textbook ideal-gas form P·Vⁿ = const (n = 1.0 / 1.4) is the low-pressure limit of this; at 200 bar nitrogen is 5 % stiffer (Z = 1.053) and its isentropic exponent is about 2, not 1.4

Required total gas volume
V₀ = ΔV / [ρ₀/ρ₁ − ρ₀/ρ₂]

where ΔV = required usable fluid delivery volume (L); all other symbols as above. As (P₂ − P₁) → 0 the denominator → 0 and V₀ → ∞ — a degenerate pressure band that requires an infinitely large accumulator; the calculator detects and warns on this condition

Adiabatic gas temperature at maximum compression
s(P₂, T₂) = s*, the isentrope on which the cycle-mean of c_v·(T_amb − T)/T is zero (continuous fast cycling) [K]

where T₂ = gas temperature at P₂ (K); T_amb = ambient/precharge temperature (K); s = specific entropy of nitrogen from the real-gas equation of state (the ideal-gas estimate T₂ = T_amb·(P₂/P₀)^(0.4/1.4) is its low-pressure limit); T₂ must remain within the accumulator's temperature rating — check against the manufacturer's data sheet

Frequently asked questions

What is EN 14359 used for?

EN 14359 is the European standard for gas-loaded accumulators in fluid power systems. It is a construction and testing standard — design, materials, pressure testing and conformity of the vessel under the Pressure Equipment Directive (PED) 2014/68/EU. It is not the source of the application sizing: the gas volume for a duty comes from the gas law on real nitrogen, and the precharge P₀ ≈ 0.9 × P₁ is manufacturer guidance. Engineers cite it when specifying a conforming vessel for peak-flow buffering, emergency actuation, pulsation dampening or energy recovery in hydraulic machinery.

What is the difference between isothermal and adiabatic accumulator sizing?

Gas-law sizing (an engineering method, not an EN 14359 clause) follows one of two limits depending on cycle speed, on real nitrogen. Isothermal sizing applies when the charge/discharge cycle is slow enough for the gas to exchange heat with its surroundings and remain at ambient temperature. Adiabatic (isentropic) sizing applies to fast cycles where no appreciable heat exchange occurs during compression or expansion; cycled continuously, the gas settles on the isentrope whose small heat exchange balances over each cycle. When the times are known, the energy balance with the gas's thermal time constant gives the cycle in between. Many machines do both: a pump charges slowly and a consumer draws fast — the gas cools back to ambient when full, then expands on the isentrope; that cycle needs the largest vessel of the three and cools the gas the most. For the same usable volume ΔV and the same pressures, a fast cycle needs a LARGER gas volume V₀ — the stiffer adiabatic gas delivers less ΔV per litre (e.g. P₀ = 90, P₁ = 100, P₂ = 150 bar g at 20 °C on real nitrogen: V₀ = 3.48·ΔV slow, 5.59·ΔV fast and continuous, 6.15·ΔV slow charge / fast discharge — the ideal gas law would say 3.35·ΔV for the slow case, too small), so a slow charge with a fast discharge is the conservative basis when the discharge may be fast. The gas also heats on a fast charge and cools on a fast discharge — the calculator reports both ends so you can check them against the bladder compound's range.

How does EN 14359 relate to PED 2014/68/EU?

EN 14359 is a harmonised product standard under the Pressure Equipment Directive (PED) 2014/68/EU. Accumulators designed and tested to EN 14359 are presumed to comply with the relevant PED essential requirements. The PED then assigns a conformity-assessment category from Annex II, which depends on the fluid group and vessel type as well as pressure and volume. An accumulator's nitrogen side is a vessel for a group 2 gas — Annex II Table 2: above 1 L, up to PS·V = 50 bar·L there is no category (sound engineering practice, Art. 4(3)), Category I to 200, II to 1000, III to 3000 and IV above (a vessel at PS ≤ 4 bar stays Category III); at 1 L or less, no category up to PS 1000 bar, Category III to 3000 and IV above. MechanixCalc reads the category from that table with PS = the larger of P₂ and the relief setting, and gives the minimum hydrostatic test pressure 1.43 × PS (Annex I §7.4). The conformity assessment itself — and the notified body from Category II up — remains the vessel maker's.

Why must the precharge pressure P₀ be set below P₁?

The gas precharge P₀ is the nitrogen pressure in the accumulator with no oil in it. The makers define it at the MAXIMUM operating temperature: P₀ = 0.9 × P₁ for energy storage (guidance from the accumulator makers, not a clause this page can cite to EN 14359), so that even on the hottest day the separator never touches the fluid port. The sealed charge reads lower when colder, so the pressure to fill to in a cool workshop is lower than P₀. If the precharge reaches P₁ at some operating temperature, the bladder is driven onto the poppet valve every cycle — the most common accumulator failure. Too low a precharge raises the ratio P₂ : P₀ beyond what the bladder tolerates (4 : 1) and wastes gas volume.

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