Recovery of Helium from Natural Gas
Background:
Helium is one of the basic chemical
elements. In its natural state, helium is a colorless gas known for its low
density and low chemical reactivity. It is chemically inert, it is also used as
a gas shield in robotic arc welding and as a non-reactive atmosphere for
growing silicon and germanium crystals used to make electronic semiconductor
devices. Liquid helium is often used to provide the extremely low temperatures
required in certain medical and scientific applications, including
super-conduction research.
Discovery:
Helium wasn't discovered until 1868, when
French astronomer Pierre Janssen and English astronomer Sir Joseph Lockyer were
independently studying an eclipse of the Sun. Using spectrometers, which
separate light into different bands of color depending on the elements present,
they both observed a band of yellow light that could not be identified with any
known element. The name “Helium” was
suggested.
Discovery
from Natural Gas:
After an oil drilling operation in 1903 in Dexter, Kansas produced a gas geyser that would not burn, Kansas state geologist Erasmus Haworth collected samples of the escaping gas and took them back to the University of Kansas at Lawrence where, with the help of chemists Hamilton Cady and David McFarland, he discovered that the gas consisted of, by volume, 72% nitrogen, 15% methane (a combustible percentage only with sufficient oxygen), 1% hydrogen, and 12% unidentifiable gas. With further analysis, Cady and McFarland discovered that 1.84% of the gas sample was helium. This showed that despite its overall rarity on Earth, helium was concentrated in large quantities available for extraction as a byproduct of natural gas.
The
Manufacturing Process
Helium is usually produced as a byproduct of natural gas processing. Natural gas contains methane and other hydrocarbons, which are the principal sources of heat energy when natural gas is burned. Most natural gas deposits also contain smaller quantities of nitrogen, water vapor, carbon dioxide, helium, and other non-combustible materials, which lower the potential heat energy of the gas. In order to produce natural gas with an acceptable level of heat energy, these impurities must be removed. This process is called upgrading.
There are several methods used to upgrade
natural gas. When the gas contains more than about 0.4% helium by volume, a
cryogenic distillation method
is often used in order to recover the helium content. Once the helium has been
separated from the natural gas, it undergoes further refining to bring it to
99.99+% purity for commercial use.
Here is a typical sequence of operations
for extracting and processing helium.
Pretreating
Because this method utilizes an extremely
cold cryogenic section as part of the process, all impurities that might
solidify—such as water vapor, carbon dioxide, and certain heavy
hydrocarbons—must first be removed from the natural gas in a pretreatment
process to prevent them from plugging the cryogenic piping.
1) The natural gas is pressurized to about 800 psi
(5.5 MPa or 54 atm.). It then flows into a scrubber where it is subjected to a
spray of mono-ethanolamine, which absorbs the carbon dioxide and carries it
away.
2)
The gas stream passes through a molecular sieve,
which strips the larger water vapor molecules from the stream while letting the
smaller gas molecules pass. The water is back-flushed out of the sieve and
removed.
3)
Any heavy hydrocarbons in the gas stream are
collected on the surfaces of a bed of activated carbon as the gas passes
through it. Periodically the activated carbon is recharged. The gas stream now
contains mostly methane and nitrogen, with small amounts of helium, hydrogen,
and neon.
Separating
Natural gas is separated into its major
components through a distillation process known as fractional distillation. Sometimes this name is shortened to
fractionation, and the vertical structures used to perform this separation are
called fractionating columns. In the fractional distillation process, the
nitrogen and methane are separated in two stages, leaving a mixture of gases
containing a high percentage of helium. At each stage the level of
concentration, or fraction, of each component is increased until the separation
is complete.
In the natural gas Industry, this process is sometimes called nitrogen rejection, since its primary function is to remove excess quantities of nitrogen from the natural gas.
4) The gas stream passes through one side of a plate
fin heat exchanger while very cold methane and nitrogen from the cryogenic
section pass through the other side. The incoming gas stream is cooled, while
the methane and nitrogen are warmed.
5) The gas stream then passes through an expansion valve, which allows the gas to expand rapidly while the pressure drops to about 145-360 psi (1.0-2.5 MPa or 10-25 Atm.). This rapid expansion cools the gas stream to the point where the methane starts to liquefy.
6) The gas stream—now part liquid and part
gas—enters the base of the high-pressure fractionating column. As the gas works
its way up through the internal baffles in the column, it loses additional
heat. The methane continues to liquefy, forming a methane-rich mixture in the
bottom of the column while most of the nitrogen and other gases flow to the
top.
The liquid methane mixture, called crude
methane, is drawn out of the bottom of the high-pressure column and is cooled
further in the crude Sub cooler. It then passes through a second expansion
valve, which drops the pressure to about 22 psi (150 kPa or 1.5 atm.) before it
enters the low-pressure fractionating column. As the liquid methane works its
way down the column, most of the remaining nitrogen is separated, leaving a
liquid that is no more than about 4% nitrogen and the balance methane. This
liquid is pumped off, warmed, and evaporated to
become upgraded natural gas. The gaseous nitrogen is piped off the top of the
low-pressure column and is either vented or captured for further processing.
Meanwhile, the gases from the top of the high-pressure column are cooled in a condenser. Much of the nitrogen condenses into a vapor and is fed into the top of the low-pressure column. The remaining gas is called crude helium. It contains about 50-70% helium, 1-3% un-liquefied methane, small quantities of hydrogen and neon, and the balance nitrogen.
Purifying
Crude helium must be further purified to
remove most of the other materials. This is usually a multi-stage process
involving several different separation methods depending on the purity of the
crude helium and the intended application of the final product.
9) The crude
helium is first cooled to about -315° F (-193° C). At this temperature, most of
the nitrogen and methane condense into a liquid and are drained off. The
remaining gas mixture is now about 90% pure helium.
10 Air is
added to the gas mixture to provide oxygen. The gas is warmed in a preheater
and then it passes over a catalyst, which causes most of the hydrogen in the
mixture to react with the oxygen in the air and form water vapor. The gas is
then cooled, and the water vapor condenses and is drained off.
11 The gas mixture enters a pressure swing
adsorption (PSA) unit consisting of several adsorption vessels operating in
parallel. Within each vessel are thousands of particles filled with tiny pores.
As the gas mixture passes through these particles under pressure, certain gases
are trapped within the particle pores. The pressure is then decreased and the
flow of gas is reversed to purge the trapped gases. This cycle is repeated
after a few seconds or few minutes, depending on the size of the vessels and
the concentration of gases. This method removes most of the remaining water
vapor, nitrogen, and methane from the gas mixture. The helium is now about
99.99% pure.
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