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PuK - Process Technology & Components 2024

A technical trade magazine with a history of more than 60 years.

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Leading article<br />

and frequently attacks sensors, expands<br />

pipes or deforms surfaces.<br />

This often leads to small relative<br />

movements between components<br />

that can degrade the structure. All<br />

other pumps including rotary pumps<br />

also cause pulsation, which can even<br />

be severe under some conditions but<br />

is usually tolerated. To improve the<br />

durability of pumps, we need to optimise<br />

the damping of oscillations and<br />

surges, and of course prevent cavitation.<br />

Since such dampers unfortunately<br />

do not exist yet, this is an engineering<br />

challenge.<br />

leading engineering challenges for<br />

compressors. Leakages may also occur<br />

depending on the type of gas.<br />

This is more of an issue the smaller<br />

the gas molecules are. Hydrogen, for<br />

example, is being discussed a great<br />

deal today. Its lubrication properties<br />

are extremely poor and it gets<br />

warmer, not colder, when the pressure<br />

is relieved at the start of the intake<br />

stroke. A liquid seal is highly suitable<br />

here but does of course require<br />

gas purification on the pressure side.<br />

In view of the energy loss through<br />

heat and leakage close to a factor of<br />

Fig. 2: Compression types of compressors: d1 isothermal; d2 polytropic, adiabatic with efficient<br />

cooling; d3 adiabatic or isentropic; d4 polytropic with additional heat input, e. g. from<br />

seal friction.<br />

The efficiency factor of compressors<br />

is highly dependent on cooling during<br />

the entire compression process.<br />

When seal friction occurs in addition,<br />

this results in polytropic compression<br />

in which the gas is additionally<br />

heated beyond compression heating.<br />

The hotter the gas, the more energy<br />

is needed for conveying. Heating<br />

of the gas during intake into the<br />

working chamber with hot walls is<br />

also problematic since it reduces the<br />

intake volume. Compared to isothermal<br />

compression in which the working<br />

chamber is cooled, ideally using<br />

a liquid, polytropic compression consumes<br />

at least twice the energy. Selecting<br />

appropriate cooling or perfectly<br />

separating coolant droplets<br />

of the internal coolant are thus the<br />

two, gas purification on the pressure<br />

side should be amortised quickly.<br />

The energy demand for a target pressure<br />

also increases the lower the actual<br />

intake pressure is. Therefore,<br />

the pressure loss on the intake side<br />

should be minimised as far as possible.<br />

The same applies for the seal<br />

friction. The area below the curves<br />

and lines in Figure 2 represents the<br />

required compression energy.<br />

The efficiency factor of compressors<br />

depends on the following aspects:<br />

1) A lack of effective cooling results in<br />

adiabatic compression. When relatively<br />

high seal friction on the piston<br />

is added, we have polytropic<br />

compression. The consumption of<br />

energy is 150 % higher compared<br />

to isothermal compression. The<br />

hotter the gas at the end of conveying,<br />

the more conveying energy.<br />

2) Gas heating during intake is also<br />

problematic; compression heating<br />

results in hot working chamber<br />

walls. The incoming gas is heated<br />

and expands during intake. This<br />

considerably reduces the intake<br />

volume.<br />

3) Every piston compressor in the<br />

classic design has a dead space.<br />

This is the remaining space at upper<br />

dead centre, which first has<br />

to be depressurised on the intake<br />

stroke before the intake as such<br />

can begin. When conveying hydrogen,<br />

it also heats up when the<br />

pressure is relieved.<br />

4) The intake with pressure loss<br />

means that the actual intake pressure<br />

is lower than the static intake<br />

pressure. While the difference is<br />

small as a rule, it nevertheless has<br />

a negative effect since compression<br />

starting at a lower pressure<br />

consumes the most energy per<br />

compression stroke.<br />

5) A pressure loss also occurs on the<br />

pressure side. However, it occurs<br />

in the upper pressure range and is<br />

therefore the smallest loss in this<br />

list.<br />

6) Leakage on the piston: Depending<br />

on the gas type and its lubricating<br />

properties, the seal suffers<br />

considerable wear and thus also<br />

an appreciable leakage flow. Both<br />

are particularly high for hydrogen<br />

since it does not lubricate. A lot if<br />

research is therefore being done in<br />

this area as well.<br />

7) With poorly lubricating gases<br />

(such as hydrogen), sliding movements<br />

of the compressor valves<br />

can be expected to occur during<br />

valve closing, from the initial contact<br />

until the final limit of travel is<br />

reached, which can cause wear.<br />

The functionally best solution is a<br />

liquid piston or a layer of liquid over<br />

the metallic piston (piston works upward).<br />

This can reduce the dead space<br />

to zero. Leakage is also zero due to<br />

the barrier effect of the liquid and the<br />

piston seal is lubricated, which can<br />

12<br />

PROCESS TECHNOLOGY & COMPONENTS <strong>2024</strong>

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