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performance after the upgrade there must be peak

downstream demand conditions that the system has to

be subjected to. In the case of LNG plants, this happens

during purging of loading arms when the ship is docked

in to transfer LNG. Before LNG is transferred through

the pipes to the LNG vessel, nitrogen is used to purge

the pipelines. After the LNG is transferred, nitrogen is

again required to push the remaining LNG out of the

loading arms in a process that is called draining.

The most critical parameter that needs to be

confirmed with the customer is if they have enough air

available from their compressors to support this

upgrade. When compressors are sized right at the edge

or upstream, pressure drops are not fully factored in,

resulting in slightly lower inlet design

pressure conditions than required.

To produce more nitrogen at the

same purity and process conditions,

more molecules of inlet air are

required, which results in an

increased air flow rate. If

downstream demand decreases, the

nitrogen purity will increase and less

air will be consumed as shown in

performance plots (Figures 5 and 6).

These plots can be used as

guidelines to estimate varying

purities that the system can produce

based on fluctuating demand

conditions of nitrogen.

Case study 2 – membrane

system performance for two

different design purities

Sometimes customers can request

two different purities of operation.

For example, 96% nitrogen at

2740 Nm

3

/hr and 98.5% nitrogen at

1731 Nm

3

/hr. For this, Gas Land had

to design for the more stringent

requirement, which was 98.5% N

2

purity at 1731 Nm

3

/hr vs the 96% at

2740 Nm

3

/hr which became the

design point. As the nitrogen purity

in the system is dialled down, the

nitrogen flow rate needed to be at

or above the requirement of

2740 Nm

3

/hr. The performance plot

in Figure 7 shows that once purity

required is reduced from 98.5% to

96% in order to meet nitrogen

demand, the system would be able

to deliver 3068 Nm

3

/hr of nitrogen

at 96% purity, 12% greater than the

original requirement of 2740 Nm

3

/hr

at 96%.

Conclusion

Increased LNG imports have become

a growing trend, especially in

countries such as China and India which are shifting

towards a cleaner and more dependable source of

energy. LNG has become central to the world’s energy

requirement. This has resulted in newer plants being

added to the US’ portfolio and the increasing of its

liquefaction capabilities. Nitrogen plays a vital role in

operation of these plants and in serving its various

applications. Onsite use of membrane technology is a

proven and reliable solution to generate nitrogen for

LNG plants worldwide.

Reference

1. ‘U.S. liquefied natural gas export capacity to more than double

by the end of 2019,’ US Energy Information Administration,

https://www.eia.gov/todayinenergy/detail.php?id=37732

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