Advancing decarbonisation and hydrogen targets for ENI

With state-of-the-art catalyst technologies, proven decarbonisation solutions and market-leading catalyst portfolio, we at Shell Catalysts & Technologies are well-positioned to support ENI’s interests.

HEAR FROM OUR PRESIDENTTALK TO OUR TEAM

Advancing decarbonisation and hydrogen targets for ENI

With state-of-the-art catalyst technologies, proven decarbonisation solutions and market-leading catalyst portfolio, we at Shell Catalysts & Technologies are well-positioned to support ENI’s interests.

HEAR FROM OUR PRESIDENTTALK TO OUR TEAM

Leverage affordable blue hydrogen production technologies

Hear from Nan Liu, Licensing Technology Manager Gasification, who shares the economic advantages of blue hydrogen production using the Shell Blue Hydrogen Process. Learn what ENI stands to gain by licensing best-in-class hydrogen production technologies.

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Hello, everyone.

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I'd like to welcome all of
you to today's webinar on

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affordable blue hydrogen production.
My name is Lee Nichols,

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and I'm the editor in chief
and associate publisher of

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hydrocarbon
processing magazine,

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and I will be your
moderator today.

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With carbon dioxide costs at
twenty five dollars to thirty

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five dollars per ton,

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blue hydrogen is already
competitive against gray hydrogen.

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And according to the
International Energy Agency,

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Green Hyrogen will remain
more expensive beyond two thousand

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and thirty. For
greenfield projects,

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oxygen based hydrogen
production systems offer

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advantages over steam methane
reforming. In a recent example,

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the Shell Blue hydrogen process
cut the levelized cost of

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hydrogen by twenty two percent
compared with auto thermal

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reforming through reduced
capital expenditure by

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seventeen percent and operating
expenditure by thirty four

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percent. So joining us for
today's event is Nan Liu,

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the licensing technology
manager, gasification, from

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Shell, catalysts
and Technologies.

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So a little bit more
about our speaker today.

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Nan is, like I mentioned,

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the licensing technology
manager for gasification.

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It's fulfillrolls throughout the
project life cycle from

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initial feasibility and front
end development to project

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execution and plant operations
on major capital projects

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around the globe.

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These include the startup of
the gasification unit at the

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Fuzhan refinery ethylene
project in China and

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performance optimization at the
gasification hydrogen plant at

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Shell's Pernis Refinery
in the Netherlands.

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This has a strong commercial
mindset and is a key advocate

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of gasification as a value
adding investment. Now,

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just some general housekeeping
notes before we get started.

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Following the presentation,

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we will have a short
question and answer session,

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and you can participate in the
Q and A session by asking a

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question at any time
during this presentation.

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All you have to do type in
your question in the Q and A box,

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which is located at the bottom
left hand corner of your

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screen. Once you type
in that question,

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simply hit the submit button.

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You can enlarge your slide
window at any time by clicking

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on the arrows on the top
right hand corner of the slide area,

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and the slides will
advance automatically throughout the event.

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If you do experience
any problems with the program,

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please press the F5 on
your keyboard to refresh the presentation.

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You can also visit the webcast
help guide by clicking on the

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help button, which is located
below the slide window.

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Now with that, let's go
ahead and get started.

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I will hand the
presentation over to you.

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Thanks Lee.

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Hello, everyone.

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Hope you all stay safe and
keep away from COVID-nineteen

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wherever you are dealt
into this webinar.

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And thanks for your
interest in this topic.

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Energy transition imposed a huge challenge
for the oil and gas industry,

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how to decarbonize our
existing operations.

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And how to make sure the
products we produce is low in

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carbon intensity,

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which can meet the
future market demand.

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In this presentation,

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I'm going to talk about how
to turn those challenges into

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opportunities for our industry.

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And how shell blue
hydrogen process can provide affordable

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blue hydrogen products, which
can help decarbonizing our industry.

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So this is a cautionary
notes. It's not readable.

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But what it says is don't
buy share shares based on what I'm

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going to talk about
in this presentation.

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So about the outline
of the presentation,

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I'm going to start with
the general challenges that our

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industry are facing
in energy transition.

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And then talk about why
hydrogen is the solution and

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why blue hydrogen plays
an important role.

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To meet the hydrogen demand
by two thousand and fifty,

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the majority of the hydrogen
capacity will be based on

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greenfield projects

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I will introduce the
different hydrogen manufacturing technologies

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and then discuss which
technology is best suited for

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greenfield applications.

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I will then talk about the
specific benefits of the Shell

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Blue hashkin process.

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In terms of affordability,

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the maturity, and then
give some proof points.

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Finally,

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I will introduce what
other technologies and capabilities

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share offers across
the CU2 value chain.

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And then summarize the presentation
with a few key takeaways.

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My talk will take about thirty
to thirty five minutes and I

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will leave sufficient time for
questions and discussions at the end.

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And its transition

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is coming with an
accelerative pace,

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which impose a huge challenge
to the oil and gas industry.

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Just to name a few.

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As existing oil
and gas producers,

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how to become low carbon
or even net zero producers

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and how to maximize the
use of existing gas based infrastructure.

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On the other hand, as
carbon intensive industry,

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how to reduce the CO2 footprint
of our existing operations

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while maintaining a
high energy efficiency.

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We think hydrogen
is the solution.

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So to meet Paris agreement,

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the shelf guide scenario
predicts that hydrogen will be

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a growing part of the
future energy mix.

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And the hydrogen console
predict that the hydrogen

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demand will increase by
tenfold by twenty fifteen.

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Hydrogen can be used to
decarbonize energy sectors that

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are difficult to
decarbonize otherwise.

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Such as power generations,

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heavy transport

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and industry energy uses.

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So the question is, how to meet
the large hydrogen demand in the future?

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So talking about
supply of hydrogen,

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there are few
color definitions.

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Great hydrogen on the
left stands for hydrogen produced

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from fossil source, mainly
natural gas. Where all the

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CO2 from the process
goes to the air.

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On the other spectrum,

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Green hydrogen stands
for hydrogen produced via

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electrolysis of water

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powered by green electricity.

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So what we want to focus
today is blue hydrogen in the middle,

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which means hydrogen produced
from fossil source, but with

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you to captured and stored
via carbon capture and storage CCS,

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or enhance oil recovery EOR.

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So blue hydrogen in general
also stands for low carbon hydrogen.

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So the question is, why are
we focusing on Blue hydrogen today?

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So if you compare the
production cost of green

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hydrogen versus blue hydrogen,

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the key advantage of Blue
hydrogen is that it's currently

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two to three times cheaper
than green hydrogen

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and is commercially
proven at a large scale.

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Blue and Green hydrogen share the
same supply chain and customer base.

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The blue hydrogen production
uses mature technology,

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both technically and commercially
proven at large scale.

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Therefore,

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Blue hydrogen presents a great
opportunity for investors

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because it provides a low
cost low carbon hydrogen source,

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which minimize the technical
and economical risk.

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For some regions,

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gray hydrogen is
still being produced.

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Because reducing carbon
emission, is not yet on some

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company's agenda.

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At the CO2 price of twenty five
dollars to thirty five dollars per tonne,

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Blue hydrogen is already
competitive against green hydrogen.

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So it is all depends on
what's due to price scenario company

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assumes in their
investment cases.

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So as such, we see Blue
hydrogen plays a significant

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role in the energy transition.

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So by now, we have to
talk about why hydrogen is an

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opportunity to
decarbonize our industry

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and why blue hydrogen plays
an important role in it.

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So let's now move into
how we produce it.

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Today,

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the majority of refining
hydrogen manufacturing unit are

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based on steam meeting
reformer SMR technology.

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If you have an SMR
unit in your asset,

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and are under pressure
to decarbonize.

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Shell has both pre and
post combustions due to capture technologies.

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To help you decarbonize
your existing assets.

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However,

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to meet the tenfold hydrogen
demand by two thousand and fifty,

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The majority of the new
hydrogen capacity will be based

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on large scale
greenfield applications.

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Therefore,

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this presentation today is
focused on greenfield applications.

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So the big question is

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is SMS still the best
option for greenfield Blue hydrogen applications?

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What are the alternatives

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and how do they compare with
each other in the blue hydrogen space?

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So there are three
leading mature technologies for blue

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hydrogen production.

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From left to right, the
Steam meeting reformer SMR,

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which takes natural gas and
react with Steam through a

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reforming reaction.

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It is a catalytic process
in a multi tubular reactor.

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Because the process
itself is endosmic

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heat must be supplied.

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For SMR reactors, it is done
by external firing at the low

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pressure side of the reactor.

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The resulting flue gas account for
forty percent of the CO2 emission.

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SMRs are generally cheap
for smaller scale and for

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green hydrogen production.

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In the middle,
autothermal reforming ATR.

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It is similar as SMR in
the sense that it is thin

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gas with the steam
over catalyst,

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but it is over one bed.

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The heat is provided as direct
heating using pure oxygen.

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Therefore, air separation
unit ASU is required.

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This come the cost,

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but this avoided large amount
of low pressure flue gas,

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which makes the CO2 capture
more cost effective.

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For large scale blue
hydrogen production,

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this is more favorable
than the SMRs.

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So to the right, SGP,
Shell gets pox with pox,

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meaning partial oxidation.

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It makes the feedstock with
oxygen and partially combusted.

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Similar as ATR,

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the SGP using oxygen,

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which means the CO2 can
be captured via more cost

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effective pre combustions
due to capture technologies.

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So the key difference compared
to the re forming process is

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that it is non catalytic.

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And that's not required
steam addition.

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HGP reactors operate at much
higher pressure than ATR,

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which reduces the
downstream equipment size

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and safe power to
compress hydrogen product.

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So for five hundred tons
per day hydrogen production,

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SGP compared to ATR can save
up to thirty million dollars

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per year of OpEx.

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As such,

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we believe SGD is the best
Blue and hydrogen technology.

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So let's take a look of
what is Shell's offering in this space.

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Let me give a quick overview
on Shell Blue hydrogen Forces as BHP.

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SVHP is hydrogen manufacturing
from natural gas,

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utilizing shell gas PoX
technology for single gas manufacturing.

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And the CO2 is captured by
a pre combatant shell Adip

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Ultra CU2 capture technology.

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As Shell Blue hydrogen process,

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we offer a end to end
line up by integrating

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both shell in house and
third party technologies.

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We are using Shell's experience
and know how from own projects.

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To maximize the integration
between each block

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and deliver a end product,
hydrogen, and CO2, up pressure

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and on spec.

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Since Shell is also an
owner and operator, for both

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SGP based hydrogen plant,

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as well as CU2
sequestration plant.

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We understand the true value
of the integrated schemes.

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And we are now including it
into our scope as master licenser.

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And offer it to the market.

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So how does show blue
hygiene process compared with the SMRs

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and ATR lineups.

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I have here a typical
process line up comparison

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between three technologies.

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So if you look at the
back end of the process,

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the building blocks of the
CEO shift that's due to capture

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and hydrogen purification

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are common for all
three technologies.

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So the difference are in
the front end single manufacturing part.

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And let me highlight
a few key differences.

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00:15:05,540 --> 00:15:07,480
So for blue
hydrogen production,

244
00:15:08,740 --> 00:15:11,160
maximize CO2 capture
is important.

245
00:15:12,575 --> 00:15:17,055
For SMR, there is a large
flue gas stream, which will

246
00:15:17,055 --> 00:15:21,635
require you to be captured by
a post combustion CU to capture technology.

247
00:15:22,880 --> 00:15:26,660
Which is more expensive than
pre combustants you to capture.

248
00:15:28,400 --> 00:15:33,555
Therefore, for blue hydrogen, we
are focusing on oxygen based technologies,

249
00:15:34,495 --> 00:15:36,355
the AGRs under the SGPs.

250
00:15:37,750 --> 00:15:41,370
So both need oxygen,
therefore ASU is required.

251
00:15:42,470 --> 00:15:46,585
But the advantage is that the
CO2 can be captured via pre

252
00:15:46,585 --> 00:15:50,045
combustions due to
capture technologies, which

253
00:15:50,905 --> 00:15:54,125
helps to reduce the overall
due to capture cost.

254
00:15:56,060 --> 00:15:58,160
Compared with ATR and SGP.

255
00:15:59,420 --> 00:16:02,080
ATRs still need heating
over the figures.

256
00:16:02,805 --> 00:16:04,345
Hence the CO2 emission.

257
00:16:05,205 --> 00:16:07,625
For FTP, it is not required.

258
00:16:10,170 --> 00:16:14,570
The other key difference
between ATR and SGP is that the

259
00:16:14,570 --> 00:16:17,630
steam reforming process
is a catalytic process.

260
00:16:18,745 --> 00:16:22,345
The natural gas needs to
be pretreated before entering the

261
00:16:22,345 --> 00:16:25,725
ATR reactor to meet the
reforming catalyst conditions.

262
00:16:27,090 --> 00:16:29,830
For SGP, we do
not have catalyst.

263
00:16:30,690 --> 00:16:33,910
Therefore, fit put
treatment is not required.

264
00:16:35,495 --> 00:16:36,475
And for HTTP,

265
00:16:37,175 --> 00:16:39,195
we do not need steam
for the reaction.

266
00:16:39,975 --> 00:16:40,475
Instead,

267
00:16:41,095 --> 00:16:45,000
high pressure steam is
produced using the heat from

268
00:16:45,000 --> 00:16:46,380
gasification reaction

269
00:16:47,640 --> 00:16:51,260
and steam can be used to
satisfy internal consumers.

270
00:16:53,985 --> 00:16:57,365
So I've now explained
the benefit of SGP

271
00:16:57,985 --> 00:17:01,285
compared to the
two main alternative technologies.

272
00:17:01,880 --> 00:17:05,100
The SMRs and ADRs for
Blue HASH in production.

273
00:17:06,840 --> 00:17:09,420
So the question is
can we quantify those benefits?

274
00:17:11,395 --> 00:17:16,375
We have done a comparison of
FGP with SMR and ATR technology

275
00:17:17,155 --> 00:17:21,320
respectively and that will take
you through the results in the

276
00:17:21,320 --> 00:17:22,460
next two slides.

277
00:17:24,600 --> 00:17:25,580
So first,

278
00:17:26,685 --> 00:17:29,665
SMR is the most common
hydrogen production technology,

279
00:17:30,285 --> 00:17:32,705
but it is also the
best for blue hydrogen.

280
00:17:34,300 --> 00:17:39,100
Here, we want to understand
how does SMR based technology with

281
00:17:39,100 --> 00:17:41,440
different degree
of CO2 capture.

282
00:17:42,045 --> 00:17:45,345
Compared with SGP with
a force you to capture.

283
00:17:47,805 --> 00:17:49,185
From left to right,

284
00:17:50,050 --> 00:17:52,950
The first three columns,
SMR based technologies

285
00:17:53,970 --> 00:17:57,190
with no suit caption.
So, basically, query hydrogen

286
00:17:57,995 --> 00:18:02,255
to maximize CU2 capture
via a post combustion technology.

287
00:18:03,515 --> 00:18:07,430
And compare that with the last
column, which is SGP based

288
00:18:08,710 --> 00:18:10,330
So here are the key findings.

289
00:18:12,470 --> 00:18:13,210
First column,

290
00:18:14,310 --> 00:18:18,135
SMR is very common. And
considered as the cheapest.

291
00:18:18,915 --> 00:18:20,775
But as you can see
from the graph,

292
00:18:21,395 --> 00:18:24,935
it is only true for
a certain C2 price.

293
00:18:25,960 --> 00:18:26,940
In this comparison,

294
00:18:27,800 --> 00:18:29,740
we use forty dollars per tonne,

295
00:18:31,320 --> 00:18:36,275
which shows in the last column
with FTHP is already more attractive.

296
00:18:39,455 --> 00:18:42,920
And if you add post
combustance view to capture solution for

297
00:18:42,920 --> 00:18:45,500
SMR, which is shown
in column three.

298
00:18:46,840 --> 00:18:50,305
A above ninety percent view
to capture can be achieved

299
00:18:51,425 --> 00:18:55,745
As you can see, both CapEx
and OpEx are higher than SGP

300
00:18:55,745 --> 00:18:57,285
based, the BlueHASH solution.

301
00:18:59,000 --> 00:18:59,500
Therefore,

302
00:19:00,280 --> 00:19:04,200
what we typically recommend is
that if you already have an

303
00:19:04,200 --> 00:19:08,555
SMR based hydrogen plant, and
want to reduce the C2 footprint.

304
00:19:09,575 --> 00:19:13,495
Shell can offer both a
deep Ultra technology for break, a

305
00:19:13,495 --> 00:19:15,275
pre combustance you to capture.

306
00:19:15,880 --> 00:19:20,700
And kinds of C2 for post
combustion C2 capture to help you decarbonize.

307
00:19:22,120 --> 00:19:24,655
But if there is a
greenfield application,

308
00:19:24,655 --> 00:19:26,515
with new Blue
Hargin facilities.

309
00:19:27,615 --> 00:19:32,015
It is more cost effective
to go for SGP based Blue

310
00:19:32,015 --> 00:19:33,075
Hargin solution.

311
00:19:38,250 --> 00:19:40,270
With some of the
customers we engage,

312
00:19:40,890 --> 00:19:43,825
ATR was highlighted
as a preferred choice.

313
00:19:44,785 --> 00:19:48,225
Therefore, we have also
compared our SGP technology

314
00:19:48,225 --> 00:19:49,925
with ATR based technology.

315
00:19:51,320 --> 00:19:55,560
The data we use for
ATR is based on public available

316
00:19:55,560 --> 00:19:57,180
data for real project.

317
00:19:58,075 --> 00:19:59,535
And here are the key findings.

318
00:20:01,675 --> 00:20:03,215
In the blue hydrogen space,

319
00:20:03,755 --> 00:20:06,735
the levelized cost of
hydrogen is a key metric.

320
00:20:08,060 --> 00:20:09,020
Overall,

321
00:20:09,020 --> 00:20:13,420
we found the levelized cost
of hydrogen for our technology is

322
00:20:13,420 --> 00:20:17,200
twenty two percent lower than
the base case in this report.

323
00:20:18,175 --> 00:20:22,595
And that is mainly contributed
by the seventeen percent lower CapEx

324
00:20:23,295 --> 00:20:25,235
and thirty four
percent lower OpEx.

325
00:20:28,190 --> 00:20:30,690
If you move on to
the CapEx comparison,

326
00:20:31,870 --> 00:20:35,355
the seventeen percent lower
CapEx is mainly because we

327
00:20:35,355 --> 00:20:37,215
operated at higher pressure,

328
00:20:38,475 --> 00:20:41,055
which leads to smaller
hydrogen compressor,

329
00:20:41,755 --> 00:20:43,615
smaller CO2 capture unit.

330
00:20:44,360 --> 00:20:46,060
And smaller co2 compressors.

331
00:20:47,640 --> 00:20:48,380
In addition,

332
00:20:49,320 --> 00:20:53,725
the simplicity of the SGP
process due to the minimum fit

333
00:20:53,725 --> 00:20:57,265
gas per treatment gives the
car tax benefits as well.

334
00:20:59,600 --> 00:21:02,660
On the OpEx, we are
thirty four percent lower.

335
00:21:03,280 --> 00:21:05,520
So besides the
smaller compressors,

336
00:21:05,520 --> 00:21:07,540
result in less
compression duties,

337
00:21:08,475 --> 00:21:12,555
The key difference compared to
reforming technology is that we

338
00:21:12,555 --> 00:21:14,175
do not consume steam.

339
00:21:15,035 --> 00:21:15,535
Instead,

340
00:21:16,460 --> 00:21:19,520
The high pressure steam
is generated from the process.

341
00:21:20,860 --> 00:21:24,000
It largely reduced the
power input to the unit.

342
00:21:24,695 --> 00:21:27,275
Hence gives significant
OPEC saving.

343
00:21:29,255 --> 00:21:33,575
On the last bar, so we do
consume about six percent more

344
00:21:33,575 --> 00:21:36,950
natural gas in the reaction
because the reaction is at a

345
00:21:36,950 --> 00:21:38,570
higher temperature
than the reformers.

346
00:21:39,910 --> 00:21:44,635
But when we cover the reaction
heat, and use it to generate steam.

347
00:21:46,375 --> 00:21:50,235
The OPEC saving offset
the additional natural gas cost.

348
00:21:51,050 --> 00:21:55,130
Therefore, overall, you will see
a twenty percent lower of

349
00:21:55,130 --> 00:21:56,590
levelized cost of hydrogen.

350
00:21:58,385 --> 00:21:59,125
In addition,

351
00:21:59,905 --> 00:22:03,745
we have ideas to further
optimize our lineup to reduce

352
00:22:03,745 --> 00:22:04,885
the natural gas consumption.

353
00:22:06,000 --> 00:22:08,740
I will come back on this
point in the later slides.

354
00:22:10,000 --> 00:22:10,740
So overall,

355
00:22:11,680 --> 00:22:16,455
I believe our technology is very
competitive in the blue hydrogen space.

356
00:22:19,235 --> 00:22:20,935
In addition to
the cost benefit,

357
00:22:21,635 --> 00:22:24,215
there are other important
benefits to consider.

358
00:22:25,380 --> 00:22:26,680
Let me highlight a few

359
00:22:27,700 --> 00:22:29,400
first on feed flexibility

360
00:22:30,740 --> 00:22:32,920
because our process
is non catalytic

361
00:22:34,015 --> 00:22:36,435
It is robust against
the feed contaminants.

362
00:22:38,175 --> 00:22:40,355
Take refinery fuel
gas as an example.

363
00:22:41,270 --> 00:22:44,730
It contains software
OIFIN C2 plus.

364
00:22:45,830 --> 00:22:49,985
SGP is very robust against
this type of difficult fee

365
00:22:51,745 --> 00:22:52,485
In addition,

366
00:22:53,265 --> 00:22:56,805
some of the natural gas
field contains high amount of CO2.

367
00:22:58,280 --> 00:23:02,600
We have commercial reference
in operating SGP using up to

368
00:23:02,600 --> 00:23:04,700
eight percent C2
in the figures.

369
00:23:06,135 --> 00:23:10,375
So removals Q2 in the seed
gas or in the same gas

370
00:23:10,375 --> 00:23:12,235
becomes an economical choice.

371
00:23:15,250 --> 00:23:17,670
Second, on lower meeting sleep.

372
00:23:18,930 --> 00:23:21,990
Because FTP reactor opened
at a higher temperature,

373
00:23:23,065 --> 00:23:26,605
the unconverted mesin in
the zincas is very low.

374
00:23:27,545 --> 00:23:30,685
It is not only means that
we have a higher conversion.

375
00:23:31,930 --> 00:23:35,690
But also means that there
is less impurity in hydrogen

376
00:23:35,690 --> 00:23:37,870
products that needs
to be removed.

377
00:23:38,965 --> 00:23:42,585
Therefore enhanced the overall
process energy efficiency.

378
00:23:45,525 --> 00:23:46,745
On energy efficiency,

379
00:23:47,850 --> 00:23:52,110
We have shown a thirty
four percent lower OpEx for FTP

380
00:23:52,730 --> 00:23:53,790
compared to ADR.

381
00:23:54,865 --> 00:23:58,805
It is mainly due to SGP has
lower power consumption.

382
00:24:00,625 --> 00:24:03,840
The savings on power
consumption is mainly because

383
00:24:03,840 --> 00:24:07,600
the possibility of producing
high pressure steam from our

384
00:24:07,600 --> 00:24:09,140
zinc as ethylene cooler.

385
00:24:10,320 --> 00:24:13,985
This is Dean is then
further superheated in the shift unit.

386
00:24:14,845 --> 00:24:17,505
And it's not only used
in the shift reaction,

387
00:24:18,285 --> 00:24:21,630
but also can be used for
other internal consumers.

388
00:24:22,890 --> 00:24:23,690
Therefore,

389
00:24:23,690 --> 00:24:28,670
the Shell Blue hydrogen process
shows very good overall energy efficiency.

390
00:24:32,385 --> 00:24:34,885
So what are the benefits
on the product side?

391
00:24:36,065 --> 00:24:36,565
First,

392
00:24:37,660 --> 00:24:41,820
higher opening pressure of
the SGP reactor reduces the

393
00:24:41,820 --> 00:24:43,360
downstream equipment size.

394
00:24:44,165 --> 00:24:46,425
Improved the CO2
capture efficiency

395
00:24:48,165 --> 00:24:52,425
and saves compression power
for the hydrogen compressors.

396
00:24:54,750 --> 00:24:56,050
On the CO2 pressure,

397
00:24:57,470 --> 00:24:59,010
in our deep Ultra technology,

398
00:24:59,950 --> 00:25:02,210
we have implemented an intermediate

399
00:25:03,495 --> 00:25:07,995
which fifty percent CO2 can
be produced at a medium pressure

400
00:25:08,535 --> 00:25:12,395
and that has significantly reduced
the size of the CO2 compression.

401
00:25:15,160 --> 00:25:17,260
On the hydrogen
purification step,

402
00:25:18,120 --> 00:25:20,700
we have chosen a mid
donation line up.

403
00:25:21,695 --> 00:25:26,815
The key advantage of methanator instead
of PSA is that it does

404
00:25:26,815 --> 00:25:29,155
not result in any
offgas streams.

405
00:25:30,250 --> 00:25:32,670
Which reduced the
direct co2 emission.

406
00:25:34,650 --> 00:25:35,310
In addition,

407
00:25:36,010 --> 00:25:40,325
the off gas stream is mainly
hydrogen which is the main product,

408
00:25:41,105 --> 00:25:43,285
but lost via the PSA offerings.

409
00:25:44,705 --> 00:25:49,430
By applying resonator line up, there
is no losses of hydrogen products.

410
00:25:50,050 --> 00:25:52,870
Therefore, reduced the
natural gas consumption.

411
00:25:55,635 --> 00:25:59,795
Perity of the hydrogen product
from a metadata line up is

412
00:25:59,795 --> 00:26:02,055
slightly lower
than PSA line up.

413
00:26:03,060 --> 00:26:08,280
But it's satisfying most of the
hydrogen purity requirement for industry uses.

414
00:26:09,220 --> 00:26:10,120
For example,

415
00:26:10,785 --> 00:26:13,685
This is a typical lineup
for ammonia production.

416
00:26:14,865 --> 00:26:19,285
A secondary benefit of ASU
is that nitrogen as a byproduct

417
00:26:19,820 --> 00:26:22,080
can be made available
at high purity.

418
00:26:23,580 --> 00:26:27,280
Combined shell blue hash
in process with ammonia synthesis

419
00:26:27,995 --> 00:26:30,815
enables the production
of blue ammonia

420
00:26:31,755 --> 00:26:32,975
and it makes transportation

421
00:26:33,595 --> 00:26:35,775
of blue hydrogen much cheaper.

422
00:26:37,760 --> 00:26:41,200
So I hope by now
you are convinced that shell blue

423
00:26:41,200 --> 00:26:44,880
hygiene process is a
very competitive blue hydrogen

424
00:26:44,880 --> 00:26:46,020
manufacturing technology.

425
00:26:47,345 --> 00:26:51,045
How about technical
maturity and these skills?

426
00:26:55,240 --> 00:26:58,380
XGP is probably new to
them Blue Hux market,

427
00:26:59,080 --> 00:27:02,620
but the technology itself is
more than sixty years old.

428
00:27:03,985 --> 00:27:07,685
Shell has a long
history of developing gasification technology

429
00:27:08,545 --> 00:27:11,925
beginning with our researches
in 1950s in Amsterdam.

430
00:27:13,890 --> 00:27:14,390
Today,

431
00:27:15,010 --> 00:27:18,450
we have over thirty active
licensees and more than one

432
00:27:18,450 --> 00:27:20,310
hundred gasifiers
built worldwide.

433
00:27:22,995 --> 00:27:25,735
After over sixty years
of research and development,

434
00:27:26,995 --> 00:27:30,535
we have built extensive
operational experience in gasification

435
00:27:31,550 --> 00:27:32,370
both globally

436
00:27:33,470 --> 00:27:35,330
and also with our
own operations.

437
00:27:36,430 --> 00:27:38,850
For example, Purney's
refinery in the Netherlands.

438
00:27:39,795 --> 00:27:42,055
And ProGTL plant in Qatar.

439
00:27:43,475 --> 00:27:47,075
And we use our own operating
experience to continue to

440
00:27:47,075 --> 00:27:48,295
develop the technology.

441
00:27:49,200 --> 00:27:51,620
And to improve the
operational efficiency.

442
00:27:53,520 --> 00:27:57,860
Over the years, we have
developed a new bonus, large franchises

443
00:27:58,765 --> 00:28:01,265
So let me give two
specific examples.

444
00:28:05,405 --> 00:28:09,170
First example is poor gas
to liquid plant in term.

445
00:28:10,270 --> 00:28:14,110
Large same gas manufacturing
capacity is required to get

446
00:28:14,110 --> 00:28:16,450
economical skill
of GTL products.

447
00:28:17,965 --> 00:28:21,965
We have eighteen large SG
train operating in Pro since

448
00:28:21,965 --> 00:28:23,025
twenty eleven.

449
00:28:23,965 --> 00:28:28,480
Each has equivalent hydrogen
capacity of five hundred tons

450
00:28:28,480 --> 00:28:30,020
per day of pure hydrogen.

451
00:28:31,605 --> 00:28:35,465
So to meet the world
and hydrogen demand by twenty fifteen.

452
00:28:36,085 --> 00:28:39,685
We believe commercially
demonstrated large shrink size

453
00:28:39,685 --> 00:28:40,825
is very important.

454
00:28:43,410 --> 00:28:47,190
Second example is my favorite
point is refinery in the Netherlands.

455
00:28:48,265 --> 00:28:51,225
I was technologist there
looking after the gasification

456
00:28:51,225 --> 00:28:55,965
based hydrogen plant, which is
a part of the refinery complex.

457
00:28:57,560 --> 00:29:01,580
And the CO2 produced from the
hydrogen plant is at a high purity.

458
00:29:02,760 --> 00:29:05,025
And for more than
fifteen years,

459
00:29:05,025 --> 00:29:08,545
It has been transported
to greenhouses to fast track

460
00:29:08,545 --> 00:29:09,525
vegetable growth.

461
00:29:11,185 --> 00:29:12,005
Moving forward,

462
00:29:12,730 --> 00:29:16,970
This CO2 stream is planned
to be sequestrated in an offshore

463
00:29:16,970 --> 00:29:18,110
empty gas field.

464
00:29:19,345 --> 00:29:24,005
Which is an important part of
the potos CCS project near Rotterdam.

465
00:29:25,265 --> 00:29:26,325
After potos,

466
00:29:27,200 --> 00:29:30,420
The hydrogen will produce
at Purnace is real blue.

467
00:29:34,135 --> 00:29:38,635
Shell is also a market
leader in large scale CCS project.

468
00:29:39,895 --> 00:29:43,355
Here is a list of CCS project
that Shell is involved.

469
00:29:44,920 --> 00:29:48,140
Without going into depth
into each individual project,

470
00:29:48,760 --> 00:29:50,940
there are a few
points to note there.

471
00:29:53,085 --> 00:29:56,465
There are multiple value
chains that CTS can enable.

472
00:29:57,725 --> 00:29:59,990
For example, the Quest project

473
00:30:00,790 --> 00:30:05,030
We are capturing CO2 from
a hydrogen unit using a deep

474
00:30:05,030 --> 00:30:06,010
electron technology

475
00:30:06,630 --> 00:30:08,650
producing low carbon hydrogen.

476
00:30:09,765 --> 00:30:13,365
We have safely captured and
stored more than one million

477
00:30:13,365 --> 00:30:16,185
ton per annum of CO2
since twenty fifteen.

478
00:30:18,610 --> 00:30:21,190
In the net zero T side
project, we are working

479
00:30:21,810 --> 00:30:25,410
together with our project
partners on a large scale gas

480
00:30:25,410 --> 00:30:28,065
power plant. With
CCS facilities.

481
00:30:30,445 --> 00:30:32,525
And in the Northern
Life project,

482
00:30:32,525 --> 00:30:35,405
we are working with our
partners to offer you to

483
00:30:35,405 --> 00:30:37,890
storage solutions to
industrial emitters.

484
00:30:40,110 --> 00:30:44,190
Purnace and Gordon demonstrate the
role of CCS to reduce our

485
00:30:44,190 --> 00:30:45,490
own asset emissions.

486
00:30:49,705 --> 00:30:54,580
By now, I have introduced
the key benefits and proof points

487
00:30:54,580 --> 00:30:56,280
of shell blue hydrogen process.

488
00:30:57,460 --> 00:31:00,740
And I'm very proud to say
that since the launch of the

489
00:31:00,740 --> 00:31:05,155
licensing of shell blue hydrogen
process about six months ago.

490
00:31:05,695 --> 00:31:09,875
We have received huge
interest from various customers globally.

491
00:31:11,710 --> 00:31:15,310
Going back to the challenges
that oil and gas industry are

492
00:31:15,310 --> 00:31:16,690
facing in any transition.

493
00:31:17,845 --> 00:31:22,165
We think there is also
an opportunity for refiners to

494
00:31:22,165 --> 00:31:25,385
transform into a carbon
neutral energy hub.

495
00:31:26,440 --> 00:31:30,860
Shell catalysts and technology
has been partnering with refiners

496
00:31:31,880 --> 00:31:36,075
or other customers to evaluate
ways to become carbon neutral.

497
00:31:37,175 --> 00:31:38,635
Let me give a few examples.

498
00:31:40,730 --> 00:31:43,790
First, on decarbonizing
existing operations.

499
00:31:44,970 --> 00:31:49,255
As I mentioned earlier, the
show has both pre combustion,

500
00:31:49,255 --> 00:31:50,395
a deep Ultra technology,

501
00:31:51,495 --> 00:31:53,415
as well as pool of combustion,

502
00:31:53,415 --> 00:31:57,530
cans of CO2 technology
to capture CO2 from refineries

503
00:31:58,550 --> 00:32:01,130
and hence reduce
existing CO2 footprint.

504
00:32:02,710 --> 00:32:07,485
The CO2 captured can be
transported via a CO2 network

505
00:32:07,485 --> 00:32:08,865
in the industry area

506
00:32:10,445 --> 00:32:14,350
and captures you to can then
be utilized in agriculture

507
00:32:15,290 --> 00:32:19,470
or inject back to
reservoir for CCS or EOR.

508
00:32:21,855 --> 00:32:25,055
The second point I want
to highlight here is the

509
00:32:25,055 --> 00:32:28,195
opportunity of using
low value streams

510
00:32:28,820 --> 00:32:33,220
such as refinery fuel gas
and the pitch from the bottom

511
00:32:33,220 --> 00:32:37,240
of the barrel into high
value blue hydrogen products.

512
00:32:38,985 --> 00:32:40,105
Captures you to

513
00:32:40,745 --> 00:32:42,925
can go into the
same you to network.

514
00:32:44,025 --> 00:32:45,245
And the blue hydrogen

515
00:32:45,880 --> 00:32:48,700
can be used to
decarbonize own refinery

516
00:32:49,320 --> 00:32:50,700
as fuel to boilers

517
00:32:52,040 --> 00:32:53,900
or to other heavy industry.

518
00:32:54,605 --> 00:32:56,465
Such as steel and power,

519
00:32:57,485 --> 00:33:02,865
as well as export as product
to other regions via liquefied hydrogen

520
00:33:03,530 --> 00:33:04,990
or ammonia shipping.

521
00:33:06,410 --> 00:33:07,070
In general,

522
00:33:07,930 --> 00:33:12,325
Shop tablets and technology
can support you with a range of

523
00:33:12,325 --> 00:33:16,965
technologies and services to
enable refiners to transform

524
00:33:16,965 --> 00:33:19,945
towards a carbon
neutral energy hub.

525
00:33:24,900 --> 00:33:27,080
I'm approaching to
the end of my story.

526
00:33:27,675 --> 00:33:30,975
Let me summarize the presentation
with a few key takeaways.

527
00:33:32,795 --> 00:33:33,695
So first,

528
00:33:34,475 --> 00:33:37,420
hydrogen will be part
of the future energy mix

529
00:33:38,220 --> 00:33:41,520
and blue hydrogen has
an important role to play

530
00:33:42,140 --> 00:33:48,035
because it is lower carbon, lower
cost and available at a large scale.

531
00:33:49,695 --> 00:33:51,315
For greenfield applications,

532
00:33:52,335 --> 00:33:57,250
SMR seems to be and less
effective method to produce blue hydrogen

533
00:33:58,110 --> 00:34:01,410
because of the poor
due to recovery and scalability.

534
00:34:03,935 --> 00:34:08,995
Instead shell has a competitive technology
offer in the Blue hydrogen space.

535
00:34:09,910 --> 00:34:13,210
And our Shell Blue
hydrogen process offers key advantages

536
00:34:13,830 --> 00:34:15,450
compared to alternative
technologies.

537
00:34:16,855 --> 00:34:18,475
Especially on its lower

538
00:34:19,095 --> 00:34:20,715
levelized cost of hydrogen,

539
00:34:21,335 --> 00:34:24,955
lower CapEx, OpEx and
overall simplicity.

540
00:34:27,290 --> 00:34:31,690
Last but not the least. Shell
has long track record on large

541
00:34:31,690 --> 00:34:32,990
scale hydrogen facilities.

542
00:34:33,695 --> 00:34:36,035
And is a market leader for CCS.

543
00:34:37,295 --> 00:34:41,535
We can provide the expertise
in developing integrated Blue

544
00:34:41,535 --> 00:34:43,315
Hatchstream solutions for you.

545
00:34:44,290 --> 00:34:45,510
Thanks for your attention.

546
00:34:49,250 --> 00:34:53,405
So now let's open up for Q and
A. Hand it over back to you, Lee.

547
00:35:03,620 --> 00:35:05,380
Alright. Thank you, Anantra,

548
00:35:05,380 --> 00:35:07,480
that that very
informative presentation.

549
00:35:08,455 --> 00:35:09,175
Like she mentioned,

550
00:35:09,175 --> 00:35:13,275
we are now going to transition
into the question and answer session.

551
00:35:13,815 --> 00:35:16,970
I know a lot of you have
sent in a a lot of questions questions.

552
00:35:16,970 --> 00:35:19,370
So I I know they definitely
sparked a lot of interest in

553
00:35:19,370 --> 00:35:23,050
this topic. So if you do
wanna ask a question, simply type

554
00:35:23,050 --> 00:35:26,545
your question into the Q and A
box that you see located at the

555
00:35:26,545 --> 00:35:28,305
bottom left hand
corner of your screen.

556
00:35:28,305 --> 00:35:29,745
Once you type in your question,

557
00:35:29,745 --> 00:35:32,865
just simply hit the submit
button, in that way,

558
00:35:32,865 --> 00:35:35,150
we'll we'll try to get
to those questions,

559
00:35:35,150 --> 00:35:38,430
during the Q and A session.
Also, I do wanna announce that,

560
00:35:38,430 --> 00:35:41,310
joining us for the Q and
A session today is also Justin

561
00:35:41,310 --> 00:35:44,255
Swane, He is the strategic
marketing manager,

562
00:35:44,255 --> 00:35:46,735
from Shell Catalyst
and Technologies.

563
00:35:46,735 --> 00:35:49,990
So Justin and Anne will be
able to answer those questions.

564
00:35:49,990 --> 00:35:53,130
So with that, let's go ahead
and jump into our first question.

565
00:35:55,910 --> 00:35:59,935
So Justin on, can you
expand on how you see blue

566
00:35:59,935 --> 00:36:02,675
hydrogen helping refiners
and their decarbonization

567
00:36:03,215 --> 00:36:07,875
objectives and how this links
to upgrading low value BOB product.

568
00:36:10,330 --> 00:36:13,930
Hi, Lee. Thanks for the
question. Yeah. It's a very

569
00:36:13,930 --> 00:36:14,890
good one. I mean,

570
00:36:14,890 --> 00:36:17,690
I worked in a refinery
for a while and actually

571
00:36:17,690 --> 00:36:19,135
manufacturing refiners,

572
00:36:19,755 --> 00:36:23,755
not new. So about one third
of the world hydrogen demand today

573
00:36:23,755 --> 00:36:26,255
is consumed by
refiners at C stop.

574
00:36:27,230 --> 00:36:30,450
But the refiners are under
quite a lot of challenge recently.

575
00:36:31,150 --> 00:36:32,590
So first of all,

576
00:36:32,590 --> 00:36:36,185
the refiners need more hydrogen
today to upgrade product due to

577
00:36:36,185 --> 00:36:37,805
more stringent product
specifications.

578
00:36:38,345 --> 00:36:42,425
And on the other hand, the
AMO twenty twenty is pushing the

579
00:36:42,425 --> 00:36:46,350
refiners to find a solution for
their bottom of the barrel products.

580
00:36:47,370 --> 00:36:50,650
So we think blue hydrogen
provide a very nice opportunity

581
00:36:50,650 --> 00:36:54,250
for the refiners to utilize
the bottom of the barrel as

582
00:36:54,250 --> 00:36:56,315
feedstock. And to
produce hydrogen.

583
00:36:57,495 --> 00:37:00,455
So while the SGP based
hydrogen manufacturing route,

584
00:37:00,455 --> 00:37:04,150
this this u two can be
captured by a more cost effective pre

585
00:37:04,150 --> 00:37:05,210
combustion technologies.

586
00:37:05,830 --> 00:37:06,710
And in this way,

587
00:37:06,710 --> 00:37:10,470
we can utilize the cheapest
feedstocks and then produce the

588
00:37:10,470 --> 00:37:12,015
high value hydrogen.

589
00:37:12,015 --> 00:37:15,315
And then capture the CO2 in
a very cost effective way.

590
00:37:16,415 --> 00:37:18,575
But the premise refinery,
which I mentioned,

591
00:37:18,575 --> 00:37:20,755
setting the presentation,
is a very good example.

592
00:37:21,350 --> 00:37:25,510
And the feedstock to
the SGP unit is the SDA

593
00:37:25,510 --> 00:37:29,915
teach. So the hydrogen produced
from the unit is used in

594
00:37:29,915 --> 00:37:31,375
hydrocracking in
the refineries.

595
00:37:33,355 --> 00:37:36,280
And I think another opportunity
for the refiner is really the

596
00:37:36,280 --> 00:37:40,040
refinery fuel gas stream as
feedstock via the Shell Blue

597
00:37:40,040 --> 00:37:44,525
Hachin process line up. And
the Hachin produced can be also

598
00:37:44,525 --> 00:37:46,705
used as few in the boilers.

599
00:37:47,325 --> 00:37:48,045
And in this way,

600
00:37:48,045 --> 00:37:51,505
the c u two is also captured
in a more cost effective way.

601
00:37:52,570 --> 00:37:56,650
And in using the refund of
you guys, yeah, the HVITION

602
00:37:56,650 --> 00:37:58,670
project in Rotterdam
is a good example.

603
00:37:59,535 --> 00:38:02,895
A feedstock to the blue
hydrogen unit, it is a mixture

604
00:38:02,895 --> 00:38:05,395
of a refinery fuel
gas and natural gas.

605
00:38:06,180 --> 00:38:09,140
And the blue hydrogen produced
can be used to decarbonize the

606
00:38:09,140 --> 00:38:11,640
heavy industry in
the hub of rotterdam.

607
00:38:12,420 --> 00:38:13,860
So it's a bit of a long answer,

608
00:38:13,860 --> 00:38:16,785
but I hope the the
address the question on the integration

609
00:38:16,785 --> 00:38:20,085
between bottom of the barrel
upgrading and blue hash manufacturing?

610
00:38:21,905 --> 00:38:23,285
No. Yeah. That was perfect.

611
00:38:24,340 --> 00:38:27,540
So I got another quick question
from a viewer. They are asking,

612
00:38:28,900 --> 00:38:30,580
kind of a a a generic question,

613
00:38:30,580 --> 00:38:34,715
but can you please elaborate a
bit on the Shell pre and post

614
00:38:34,715 --> 00:38:36,175
carbon capture technology.

615
00:38:38,075 --> 00:38:39,615
Yeah. I can take that one.

616
00:38:40,630 --> 00:38:43,510
Okay. So, yeah, so we
have two technologies,

617
00:38:43,510 --> 00:38:46,230
one for high pressure, which
is our adept technology,

618
00:38:46,230 --> 00:38:51,325
and one for low pressure
post combustion that cancels technology.

619
00:38:51,325 --> 00:38:54,605
So the added technology has
been around fifty years,

620
00:38:54,605 --> 00:38:57,505
and constantly being developed
and improved during that process

621
00:38:58,220 --> 00:39:02,220
whereas the Shell Cancer
Technology has been around for

622
00:39:02,220 --> 00:39:03,520
around twenty years.

623
00:39:04,620 --> 00:39:08,975
So we look at the scenario
and what we're trying to capture

624
00:39:08,975 --> 00:39:10,415
which process stream.

625
00:39:10,415 --> 00:39:13,295
And then we do a techno
economic evaluation as to which

626
00:39:13,295 --> 00:39:15,715
one we think is the best
one to put in place.

627
00:39:16,790 --> 00:39:21,290
So, yeah, so there's a
long history there. You know, the

628
00:39:22,070 --> 00:39:24,970
the aiming technologies
are proven at scale.

629
00:39:25,755 --> 00:39:27,995
You have an absorber,
you have a regenerator,

630
00:39:27,995 --> 00:39:32,910
and it comes down to selecting
the right aiming for the

631
00:39:32,910 --> 00:39:36,030
process that you're going to be
looking to treat the gas stream

632
00:39:36,030 --> 00:39:38,030
and what you're trying the
specification you're trying to

633
00:39:38,030 --> 00:39:39,090
get down to. So

634
00:39:39,710 --> 00:39:41,410
shell has sixty years of

635
00:39:42,245 --> 00:39:46,885
know how in terms of gas
treating and selecting the right process,

636
00:39:46,885 --> 00:39:50,810
the right process conditions and the
right aiming for that So with this,

637
00:39:50,810 --> 00:39:53,930
we have quite a bit of
flexibility to help decarbonize

638
00:39:53,930 --> 00:39:55,850
many streams, removing CO2,

639
00:39:55,850 --> 00:39:59,070
whether it be a process stream
or from a low pressure stream.

640
00:40:02,605 --> 00:40:03,745
Great. Thank you, Justin.

641
00:40:04,525 --> 00:40:07,400
So I got another question
from a a major association.

642
00:40:08,340 --> 00:40:09,160
They're asking

643
00:40:09,940 --> 00:40:11,640
with regards to Shell SGP,

644
00:40:12,260 --> 00:40:14,545
they're asking if it's
such a well established technology?

645
00:40:14,545 --> 00:40:18,305
Why are people still talking
about SMR and ATR for

646
00:40:18,305 --> 00:40:19,825
greenfield blue hydrogen?

647
00:40:19,825 --> 00:40:22,305
And so why they're kinda just
asking why are you you provide

648
00:40:22,305 --> 00:40:23,445
this webinar today?

649
00:40:24,510 --> 00:40:26,350
Yeah. If I may take this one,

650
00:40:26,350 --> 00:40:28,270
thanks a lot for
asking the question.

651
00:40:28,270 --> 00:40:31,790
I think that's one of the
main reason why we want to, yeah,

652
00:40:31,790 --> 00:40:34,945
reach a bigger amount of
audience and introduce our technology.

653
00:40:35,725 --> 00:40:39,185
I mean, the SGP technology
is indeed well established.

654
00:40:40,100 --> 00:40:45,220
But primarily has been used in
the past for shell owned GTL process.

655
00:40:45,220 --> 00:40:48,179
So we've been keeping it
for shell owned projects for

656
00:40:48,179 --> 00:40:52,675
decades And only since last year,
we got the, if you go

657
00:40:52,675 --> 00:40:56,659
ahead from, from shell to
that licensing, basically,

658
00:40:56,659 --> 00:40:59,700
promoting this technology
to the third party space.

659
00:40:59,700 --> 00:41:05,565
And and that's where, yeah, we started
this journey kind of half year ago.

660
00:41:05,565 --> 00:41:08,044
And that's why we did this
comparison in the presentation

661
00:41:08,044 --> 00:41:11,165
because we want to know
whether we are competitive compared to

662
00:41:11,165 --> 00:41:13,645
SMR and APR, which is
more known for the market,

663
00:41:13,645 --> 00:41:16,590
external market. So
did our homework.

664
00:41:16,590 --> 00:41:19,150
And we believe this is a
very competitive technology,

665
00:41:19,150 --> 00:41:22,830
and that's why today we are
doing after we have done all

666
00:41:22,830 --> 00:41:25,504
this homework and we start
promoting it to to the third

667
00:41:25,504 --> 00:41:27,744
party market. So
in short, yeah,

668
00:41:27,744 --> 00:41:29,665
we've been keeping it for
too long for ourselves,

669
00:41:29,665 --> 00:41:33,365
and now we basically make it
also available for the third party space.

670
00:41:35,789 --> 00:41:37,490
Actually, that was that
was a great explanation.

671
00:41:38,829 --> 00:41:41,809
So kinda kinda sticking
with that thing. This,

672
00:41:42,509 --> 00:41:44,174
yours actually
asking too about,

673
00:41:44,974 --> 00:41:46,894
commercial use of it.
So they're asking,

674
00:41:46,894 --> 00:41:50,569
did did you use the shell
SGP process at the Quest

675
00:41:51,129 --> 00:41:53,069
CCUS project in Canada.

676
00:41:56,489 --> 00:41:58,829
So, yeah, so building
on the same theme.

677
00:41:59,690 --> 00:42:00,190
The

678
00:42:01,675 --> 00:42:02,175
The

679
00:42:03,115 --> 00:42:05,434
facility in Canada where
we produce the hydrogen,

680
00:42:05,434 --> 00:42:08,254
consumers all of hydrogen.
And when it was built

681
00:42:09,309 --> 00:42:13,069
at the time, it was gray
hydrogen. And the SMR process

682
00:42:13,069 --> 00:42:15,729
was what was seen best
for that facility.

683
00:42:16,315 --> 00:42:17,934
And then later in the

684
00:42:19,595 --> 00:42:23,780
operation of the facility, the site
wanted to go and they Blue

685
00:42:23,780 --> 00:42:27,780
hydrogen and the help to
decarbonize the footprint of

686
00:42:27,780 --> 00:42:28,980
the facility there.

687
00:42:28,980 --> 00:42:33,264
And also that facility had
an opportunity for EOR close

688
00:42:33,264 --> 00:42:38,784
by, to to the plant. So when
we assess the plant at the time,

689
00:42:38,784 --> 00:42:41,520
there's two routes you can go
you can go to high pressure

690
00:42:41,520 --> 00:42:45,760
route, putting an added Ultra
unit or capture all the CO2

691
00:42:45,760 --> 00:42:47,540
emissions at the low pressure

692
00:42:48,324 --> 00:42:51,144
exhaust and used to cancel CO2.

693
00:42:51,764 --> 00:42:52,744
At that time,

694
00:42:53,284 --> 00:42:56,519
the high pressure root was
preferred I think there was

695
00:42:56,519 --> 00:42:59,639
sufficient CO two could
be captured at that point.

696
00:42:59,639 --> 00:43:01,479
And without the tax incentives,

697
00:43:01,479 --> 00:43:03,819
then there wasn't a drive
to go for the fullest,

698
00:43:04,519 --> 00:43:06,234
catcher level, which is,

699
00:43:06,234 --> 00:43:09,914
coming from the high the
low pressure canceled. So I think,

700
00:43:09,914 --> 00:43:14,769
you know, Quest is a
good example of, you know, how

701
00:43:14,769 --> 00:43:16,849
things are done in the past
and how things can go in the

702
00:43:16,849 --> 00:43:19,569
future. If that plant
was being built from you,

703
00:43:20,450 --> 00:43:23,329
the hydrogen facility and we
want to go for blue hydrogen

704
00:43:23,329 --> 00:43:25,445
directly, I think
in that situation,

705
00:43:25,445 --> 00:43:27,365
when we do the economics
and what we've seen from the

706
00:43:27,365 --> 00:43:28,645
presentation today,

707
00:43:28,645 --> 00:43:32,004
that the combination of one
single lineup being built from

708
00:43:32,004 --> 00:43:34,860
scratch then you
would look at the,

709
00:43:34,860 --> 00:43:37,600
the Shell Blue Hygiene
process combining the PoX technology

710
00:43:38,220 --> 00:43:41,405
with the high pressure added
technology and the other technologies,

711
00:43:42,105 --> 00:43:45,865
processes associated with
making the right specification

712
00:43:45,865 --> 00:43:48,290
of hydrogen and
capturing the CO2.

713
00:43:48,290 --> 00:43:50,690
So it's a nice example
to look at, you know,

714
00:43:50,690 --> 00:43:52,770
how things were done in the
past and how we would do things

715
00:43:52,770 --> 00:43:55,330
if we're doing from
scratch. And like we say,

716
00:43:55,330 --> 00:43:58,615
when we talk about other
refiners and those that have and,

717
00:43:59,555 --> 00:44:01,875
which are making today
gray, then, you know, yes,

718
00:44:01,875 --> 00:44:04,595
there are options that do
the similar one. And again,

719
00:44:04,595 --> 00:44:06,035
looking at high pressure
and low pressure,

720
00:44:06,035 --> 00:44:08,070
we're down to the
individual economics or

721
00:44:08,790 --> 00:44:10,810
of the opportunity
and the site.

722
00:44:11,590 --> 00:44:13,030
And, yes, you know,

723
00:44:13,030 --> 00:44:15,930
we would love to support in
in looking at those as well.

724
00:44:18,935 --> 00:44:23,175
Hey. Thanks, Justin. So here's
a question from a, an operator.

725
00:44:23,175 --> 00:44:24,695
They're asking, basically,

726
00:44:24,695 --> 00:44:27,770
just what of types of feeds
that can be used with SGP,

727
00:44:27,770 --> 00:44:31,530
and they kinda follow-up with
natural gas, naphtha, RFPG, LPG.

728
00:44:31,530 --> 00:44:34,375
So if you can just kinda Give
a little detail that on on the

729
00:44:34,375 --> 00:44:36,795
type of feeds that can be
used on this in this process.

730
00:44:38,135 --> 00:44:40,180
Yeah. Thanks for the questions.

731
00:44:40,180 --> 00:44:43,860
So one of the key advantage
of the SGP technology is that it's

732
00:44:43,860 --> 00:44:45,700
very flexible in
terms of, yeah,

733
00:44:45,700 --> 00:44:48,580
feed intake because we
don't have catalyt catalyst,

734
00:44:48,580 --> 00:44:49,720
in our reactor.

735
00:44:50,235 --> 00:44:53,675
So this, feedstock, your
address can be processed in

736
00:44:53,675 --> 00:44:55,435
SGP. So natural gas,

737
00:44:55,435 --> 00:44:58,015
not refinery fuel gas
specifically I mentioned.

738
00:44:58,520 --> 00:45:02,600
LPG. And also, yeah, when
I mentioned that the the

739
00:45:02,600 --> 00:45:05,320
potential of upgrading the
bottom of barrel product into

740
00:45:05,320 --> 00:45:07,515
hydrogen, basically,
liquid residue,

741
00:45:07,515 --> 00:45:11,035
very heavy from the refineries
can be upgraded as well.

742
00:45:11,035 --> 00:45:16,490
So using the same process, but
slightly different, yeah, FTP, let's say,

743
00:45:17,450 --> 00:45:21,355
building blocks. But, all
these feedstocks, basically,

744
00:45:21,355 --> 00:45:23,595
any low value streams that,

745
00:45:23,595 --> 00:45:27,435
you consider that week have
a solution to upgrade that into,

746
00:45:27,435 --> 00:45:28,735
hydrogen and temperature

747
00:45:29,370 --> 00:45:33,070
the c u two, you know,
cost effective for precompassion way. Excellent.

748
00:45:36,650 --> 00:45:37,465
Thanks.

749
00:45:37,465 --> 00:45:40,585
So the next question here I
need you to put on your on your

750
00:45:40,585 --> 00:45:44,905
economist hat, but, this question
from viewer asked, just basically,

751
00:45:44,905 --> 00:45:48,140
what are your views on
small scale blue hydrogen production,

752
00:45:48,140 --> 00:45:50,000
and does it make
sense economically?

753
00:45:52,780 --> 00:45:54,780
Yeah. So I'm not economists,

754
00:45:54,780 --> 00:45:56,995
but let me try to
address this one.

755
00:45:56,995 --> 00:46:01,235
The key advantage of the
SGP technology is that it's already

756
00:46:01,235 --> 00:46:03,395
available to the
the large scale.

757
00:46:03,395 --> 00:46:06,210
So we don't have to start from
small scale and demo rate,

758
00:46:06,210 --> 00:46:09,090
the economic feasibility
before going to large scale.

759
00:46:09,090 --> 00:46:12,370
I would know that in any of
the development, yet normally,

760
00:46:12,370 --> 00:46:14,230
if you go on large
scale, the economic

761
00:46:14,865 --> 00:46:17,445
possibility will, yeah,
be more favorable.

762
00:46:18,145 --> 00:46:19,985
So that's why, you know,

763
00:46:19,985 --> 00:46:23,125
when we are looking at
the blue hydrogen versus green hydrogen,

764
00:46:23,640 --> 00:46:26,920
we think blue hydrogen will
be more favorable for a large

765
00:46:26,920 --> 00:46:29,960
scale application because
it's already proven and

766
00:46:29,960 --> 00:46:32,855
commercialized today.
And for small scale,

767
00:46:32,855 --> 00:46:35,895
there are many green hydrogen, put, yeah,

768
00:46:35,895 --> 00:46:38,775
productions start from small scale
and trying to prove the

769
00:46:38,775 --> 00:46:42,570
the economic feasibility.
So I think Yeah. In short,

770
00:46:42,570 --> 00:46:45,610
the large scale will be
more favorable for blue hydrogen and

771
00:46:45,610 --> 00:46:48,250
the small scale, yeah,
there are many developers,

772
00:46:48,250 --> 00:46:51,755
trying to develop a green
hydrogen solution. We are not,

773
00:46:51,755 --> 00:46:55,274
excluding each other. It's
more, like, which one is more,

774
00:46:55,274 --> 00:46:59,135
complimentary in the transformation
of the hydrogen value chain.

775
00:47:02,560 --> 00:47:03,860
Excellent. Thanks, hun.

776
00:47:04,560 --> 00:47:04,960
Alright.

777
00:47:04,960 --> 00:47:08,455
So I have a these two
questions are are are are regarding more

778
00:47:08,455 --> 00:47:12,875
about, hydrogen purity. So the
first one here is there's many,

779
00:47:13,815 --> 00:47:16,280
potential outlets for produce
hydrogen with differing,

780
00:47:16,280 --> 00:47:19,000
specifications on purity.
So the viewer asked,

781
00:47:19,000 --> 00:47:22,280
can you expand a little
bit more on hydrogen purity

782
00:47:22,280 --> 00:47:24,684
optimization? In
technology selection.

783
00:47:26,585 --> 00:47:31,065
Yeah. Also, very good one.
So talking about different hash

784
00:47:31,065 --> 00:47:34,339
impurity, we typically
classify as, say,

785
00:47:34,339 --> 00:47:37,139
two two two categories.
So the first,

786
00:47:37,139 --> 00:47:40,335
we call high grade hydrogen.
So, typically, Yeah.

787
00:47:40,335 --> 00:47:44,095
Ninety nine point nine seven
plus based on ISO standard for

788
00:47:44,095 --> 00:47:45,154
fuel cell application.

789
00:47:45,855 --> 00:47:49,234
And the second category is
we call industrial grade hydrogen.

790
00:47:49,819 --> 00:47:52,799
Which is suitable for
large industrial hygiene consumers.

791
00:47:54,059 --> 00:47:56,700
And the difference in blue
hydrogen technology selection

792
00:47:56,700 --> 00:47:58,719
is in the hydrogen
purification technology.

793
00:47:59,984 --> 00:48:02,625
So for the high
grade hydrogen spec,

794
00:48:02,625 --> 00:48:05,845
a pressure swing absorption,
so PSA unit is required.

795
00:48:06,385 --> 00:48:10,500
And that results in the PSA off
gas stream. This can be used as

796
00:48:10,500 --> 00:48:13,240
fuel but result
in co2 emissions.

797
00:48:14,659 --> 00:48:17,139
So, typically, for
industrial grade,

798
00:48:17,139 --> 00:48:19,525
we select the machination step.

799
00:48:19,525 --> 00:48:24,025
So the the advantage of this is that
is that it's no direct due to emission.

800
00:48:24,805 --> 00:48:27,445
And it can save also the
natural gas consumption because

801
00:48:27,445 --> 00:48:30,480
we do not have this
hydrogen loss via the PSFTS.

802
00:48:31,060 --> 00:48:32,620
So, therefore,

803
00:48:32,620 --> 00:48:35,580
for the industrial grade
hydrogen and the hydrogen

804
00:48:35,580 --> 00:48:36,685
purity typically,

805
00:48:36,685 --> 00:48:39,805
we can reach ninety six to
ninety eight percent depending

806
00:48:39,805 --> 00:48:43,245
on the type of feedstock that
we get. Yeah. And for instance,

807
00:48:43,245 --> 00:48:46,480
it's a good example here,
because Yeah. As I mentioned,

808
00:48:46,480 --> 00:48:50,000
the machination is already
in the hydrogen production line

809
00:48:50,000 --> 00:48:53,920
up. And if hydrogen produced
is used in the industry for

810
00:48:53,920 --> 00:48:56,165
decades. So, Yeah.

811
00:48:56,785 --> 00:48:58,065
There are different,

812
00:48:58,065 --> 00:49:01,265
hydrant beauty requirement
as the technology needs to be

813
00:49:01,265 --> 00:49:02,470
selected accordingly.

814
00:49:02,470 --> 00:49:04,890
But we see
advantage of applying machination,

815
00:49:05,990 --> 00:49:08,410
step for a industrial
grade hydrogen.

816
00:49:10,715 --> 00:49:11,515
Yeah. Thanks, Nadia.

817
00:49:11,515 --> 00:49:14,315
Because that that would
actually answer two questions with,

818
00:49:14,315 --> 00:49:17,755
with one answer because there
was an exact same question that

819
00:49:17,755 --> 00:49:19,970
had to do with the they
wanna know the different impact a

820
00:49:19,970 --> 00:49:23,110
hydrogen period between methination
and PSA process. So,

821
00:49:23,730 --> 00:49:26,130
I think he got to
that one. So, yeah.

822
00:49:26,130 --> 00:49:29,075
Let's move on to the
next question here from from an

823
00:49:29,075 --> 00:49:32,215
operator. They're asking,
with all the foreseen,

824
00:49:35,235 --> 00:49:36,275
atrina storage,

825
00:49:36,275 --> 00:49:39,780
is there enough capacity to store
if we go if we all go

826
00:49:39,780 --> 00:49:41,240
blue slash green.

827
00:49:45,060 --> 00:49:45,675
Yeah,

828
00:49:45,675 --> 00:49:48,715
So I need to guess a
little bit what exactly the question is

829
00:49:48,715 --> 00:49:50,015
meant, but I think

830
00:49:51,035 --> 00:49:52,955
for blue and
hydrogen production,

831
00:49:52,955 --> 00:49:56,820
you need to capture and the
stores you to So I think, this

832
00:49:56,820 --> 00:50:00,600
is probably talking about the
the c u two storage, capacity.

833
00:50:01,540 --> 00:50:05,695
Yeah. So I see this as a
little bit chicken to add

834
00:50:05,695 --> 00:50:08,735
question. So we know
from to reach the,

835
00:50:08,735 --> 00:50:11,135
the net zero goal
by twenty fifteen.

836
00:50:11,135 --> 00:50:15,270
The carbon capture and storage is
a crucial part to reach this ambition.

837
00:50:15,270 --> 00:50:18,470
And therefore, recently, we see there's
a lot of, yeah, let's say,

838
00:50:18,470 --> 00:50:21,670
encouragement also from the
government to invest in CCS

839
00:50:21,670 --> 00:50:26,005
project. So once the large
scale CCS facilities in place

840
00:50:26,005 --> 00:50:28,885
and coupled with the
blue hash in production,

841
00:50:28,885 --> 00:50:30,740
there'll be a nature feed.

842
00:50:30,740 --> 00:50:33,700
Because the hygiene can be used
as a clean fuel to decarbonize

843
00:50:33,700 --> 00:50:37,220
the industry where the co two
is captured in a cost effective

844
00:50:37,220 --> 00:50:41,524
way and can be stored.
So in terms of storage,

845
00:50:42,145 --> 00:50:46,465
capacity limitation, so that's
really an upstream question.

846
00:50:46,465 --> 00:50:50,280
So to to a lot of
the upstream colleagues has been looking at

847
00:50:50,280 --> 00:50:53,160
that. So it really depends on
where you are in the world, but,

848
00:50:54,280 --> 00:50:57,160
that's why a lot of those
projects are positioned near

849
00:50:57,160 --> 00:50:59,505
those so called
industrial clusters,

850
00:50:59,505 --> 00:51:03,025
which people has already
assessed the c u two storage

851
00:51:03,025 --> 00:51:06,240
capability, and then
build on top of that.

852
00:51:06,240 --> 00:51:10,020
Capacity will be a really
value adding, yeah, project.

853
00:51:12,639 --> 00:51:16,054
And maybe if I can add
to that is it's gonna be interesting,

854
00:51:17,954 --> 00:51:18,694
to see

855
00:51:19,554 --> 00:51:23,740
where the CO2 is gonna come
from in terms of some of the

856
00:51:23,740 --> 00:51:27,899
clients that we are engaging
with talking about hydrogen production.

857
00:51:27,899 --> 00:51:31,040
We're also talking about
co2 capture from industrial facilities.

858
00:51:31,745 --> 00:51:33,745
And the debate will
come in, I guess,

859
00:51:33,745 --> 00:51:37,045
in terms of how will
people want to decarbonize

860
00:51:37,665 --> 00:51:41,510
their industrial facility Is it
going to be doing CO2 capture

861
00:51:41,510 --> 00:51:45,349
at the plant and then send that
CO2 for storage, or will it be

862
00:51:45,349 --> 00:51:49,865
capturing the CO2 from the fuel
source that would have been

863
00:51:49,865 --> 00:51:51,865
provided to those plants, say,

864
00:51:51,865 --> 00:51:54,505
taking the methane and
converting that to blue

865
00:51:54,505 --> 00:51:56,880
hydrogen and doing
the CO2 capture there.

866
00:51:56,880 --> 00:52:00,160
So I do wonder in the scenarios
when we talk about how much CA2

867
00:52:00,160 --> 00:52:03,280
is required if hydrogen
would not necessarily be incremental,

868
00:52:03,280 --> 00:52:06,315
it would be maybe displacing some
of that CO2 would come as

869
00:52:06,315 --> 00:52:08,635
well. And I guess
also, you know,

870
00:52:08,635 --> 00:52:11,995
whilst technology maturation
improvement and, you know,

871
00:52:11,995 --> 00:52:14,820
our aim is to try
and reduce cost of hydrogen production,

872
00:52:16,240 --> 00:52:18,320
whether it be
through, you know,

873
00:52:18,320 --> 00:52:21,525
the technology to convert the
hydrogen or the processes and

874
00:52:21,525 --> 00:52:25,765
infrastructure to deal with the
CO2 that's produced, you know,

875
00:52:25,765 --> 00:52:28,970
maybe more science and
engineering and understanding

876
00:52:28,970 --> 00:52:29,870
about the reservoirs,

877
00:52:30,490 --> 00:52:33,710
will help build capacity beyond
what we think it is today.

878
00:52:34,490 --> 00:52:36,970
I'm sure we've seen lots
of things happening in terms of

879
00:52:36,970 --> 00:52:38,235
oil and gas production,

880
00:52:39,095 --> 00:52:41,175
new technologies coming
in to increase it.

881
00:52:41,175 --> 00:52:44,695
So hopefully those same sort
of technologies will help us to

882
00:52:44,695 --> 00:52:47,034
increase the capacity
to store the CO2

883
00:52:47,720 --> 00:52:51,260
that comes from the combustion
of those fuels. Excellent.

884
00:52:54,355 --> 00:52:57,315
Thank you, Don. Justin, so
moving on to the next question

885
00:52:57,315 --> 00:52:58,994
from, from a viewer, they,

886
00:52:58,994 --> 00:53:01,234
I know earlier you talked a
little bit about bottom of the

887
00:53:01,234 --> 00:53:04,480
barrel configuration. So this
viewer is asking Actually,

888
00:53:04,480 --> 00:53:08,659
how can SGP be integrated
with bottom of the barrel configurations?

889
00:53:11,904 --> 00:53:12,784
Yeah. So,

890
00:53:13,984 --> 00:53:16,944
yeah, I answered how as
a refiners that can integrate

891
00:53:16,944 --> 00:53:19,124
SGP. So I think maybe the,

892
00:53:20,129 --> 00:53:20,869
the questions

893
00:53:21,489 --> 00:53:24,289
from this viewer is more
like the throughout the

894
00:53:24,289 --> 00:53:26,629
presentation, we'll be
introducing the technology

895
00:53:27,249 --> 00:53:29,429
by taking the natural
gas as a feedstock.

896
00:53:30,115 --> 00:53:31,875
Because most of
those, yeah, comp

897
00:53:32,514 --> 00:53:33,954
comparable technologies,

898
00:53:33,954 --> 00:53:36,969
in this space is using
natural gas as a sea stock.

899
00:53:36,969 --> 00:53:40,089
But the other advantage which
we're trying to explain to the

900
00:53:40,089 --> 00:53:42,509
audience is also the
fit flex flexibility.

901
00:53:43,129 --> 00:53:47,244
And therefore, the SGP
technology can also be taking

902
00:53:47,244 --> 00:53:50,605
the liquid feedstock from
a refinery residue stream.

903
00:53:50,605 --> 00:53:53,325
And that's why we say,
yeah, the bottom of barrel upgrading,

904
00:53:53,325 --> 00:53:57,299
there is the very heavy residue
streams that in the future will

905
00:53:57,299 --> 00:53:58,579
be lower in value.

906
00:53:58,579 --> 00:54:03,059
And then taking that as a
feedstock fit in into the SGP unit,

907
00:54:03,059 --> 00:54:06,044
and then the rest of the line
up can remain the same to make

908
00:54:06,044 --> 00:54:10,845
yeah, Blue hydrogen. So that is
exactly the lineup that we are,

909
00:54:10,845 --> 00:54:14,550
operating already for, yeah,
more than twenty years in

910
00:54:14,550 --> 00:54:15,530
Purney's refinery.

911
00:54:16,070 --> 00:54:19,429
We are taking the, let's say,
the bottom of the bottom.

912
00:54:19,429 --> 00:54:20,950
So the pitch from the SDA unit,

913
00:54:20,950 --> 00:54:23,050
so in the asset voting
unit of the refinery,

914
00:54:23,655 --> 00:54:27,495
And then, yeah, feed
that stream into a, yeah,

915
00:54:27,495 --> 00:54:29,575
gasification unit, SGP unit,

916
00:54:29,575 --> 00:54:32,910
and then produce hydrogen
capturing c u two.

917
00:54:32,910 --> 00:54:35,950
And then hydrogen is feed
back into the hydrocracker in the

918
00:54:35,950 --> 00:54:40,755
refinery. So by this means,
we are integrating SGP based blue

919
00:54:40,755 --> 00:54:43,395
hydrogen plant into the
bottom of our upgrading in the

920
00:54:43,395 --> 00:54:47,335
refinery. I hope that this explanation
is a bit more clear now.

921
00:54:49,560 --> 00:54:51,340
No. No. Fantastic. So

922
00:54:52,200 --> 00:54:55,240
let's talk a little bit
about, the competitiveness of SGP.

923
00:54:55,240 --> 00:54:56,840
So this viewer is asking,

924
00:54:56,840 --> 00:55:00,565
how can competitive as Shell
Blue hydrogen process against pyrolysis.

925
00:55:03,825 --> 00:55:05,765
Yeah. So I guess
the question is,

926
00:55:06,590 --> 00:55:07,810
how do you convert,

927
00:55:08,670 --> 00:55:10,530
methane into hydrogen? So

928
00:55:11,550 --> 00:55:13,790
we have talked in this
presentation as your blue

929
00:55:13,790 --> 00:55:14,690
hydrogen process.

930
00:55:15,485 --> 00:55:19,805
Which is a mature technology
that has been out there

931
00:55:19,805 --> 00:55:23,485
operating a large scale,
yeah, since twenty eleven in,

932
00:55:23,485 --> 00:55:24,785
in growing Qatar.

933
00:55:25,490 --> 00:55:28,150
So I think there is
a very different,

934
00:55:28,930 --> 00:55:31,890
in terms of maturity of
the technology. So the parallels

935
00:55:31,890 --> 00:55:35,110
is, of methane. It is,
yeah, and and the research.

936
00:55:35,695 --> 00:55:39,455
So it is not comparable at
the the skill that we are talking

937
00:55:39,455 --> 00:55:43,180
about and also the, the
maturity of the technology.

938
00:55:43,180 --> 00:55:45,180
So I don't exclude
it in the future.

939
00:55:45,180 --> 00:55:47,180
This may become a
viable solution,

940
00:55:47,180 --> 00:55:51,685
but then also the way
how the carbon is is separated,

941
00:55:51,685 --> 00:55:54,245
and then you you were talking
about a very different way of

942
00:55:54,245 --> 00:55:55,765
disposal this carbon.

943
00:55:55,765 --> 00:55:58,860
Although carbon black can
be a good outlet But, yeah,

944
00:55:58,860 --> 00:56:01,820
we're potentially talking about a
huge amount of carbon black.

945
00:56:01,820 --> 00:56:05,500
So I think there's also
gas from a technology maturity and

946
00:56:05,500 --> 00:56:08,045
also the market following
this technology.

947
00:56:08,045 --> 00:56:12,525
Needs to be developed. So,
yeah, as as for today, the

948
00:56:12,525 --> 00:56:15,345
technology we are promoting
is mature at large scale.

949
00:56:16,600 --> 00:56:18,360
I think that is the,

950
00:56:18,360 --> 00:56:20,460
key difference in terms
of a competitiveness.

951
00:56:23,315 --> 00:56:25,155
Excellent. Thank you, Naut. So,

952
00:56:25,155 --> 00:56:26,515
we're getting
close to top hour.

953
00:56:26,515 --> 00:56:29,475
I might be one or two
quick questions here.

954
00:56:29,475 --> 00:56:31,300
One of these from a viewer is,

955
00:56:31,300 --> 00:56:34,660
is you already seem to
have reduced cost of producing blue

956
00:56:34,660 --> 00:56:35,960
hydrogen currently.

957
00:56:36,580 --> 00:56:37,300
So they're asking,

958
00:56:37,300 --> 00:56:42,565
do you see a potential to
reduce cost further and if so, how?

959
00:56:45,185 --> 00:56:47,825
Yeah. So also very
good question.

960
00:56:47,825 --> 00:56:49,840
So throughout these
presentations,

961
00:56:49,840 --> 00:56:53,600
We've been talking about
our commercial size unit. Basically,

962
00:56:53,600 --> 00:56:57,060
single train gives five hundred
tons per day of pure hydrogen.

963
00:56:57,645 --> 00:57:01,245
So this is the standard train
size we deploy in the pro Qatar

964
00:57:01,245 --> 00:57:04,705
project with eighteen of those
trains operating for almost ten years.

965
00:57:05,440 --> 00:57:08,340
So we believe this
is a commercial,

966
00:57:09,200 --> 00:57:14,080
yeah, good reference size that
we've been deployed for for

967
00:57:14,080 --> 00:57:18,145
many years. And we have over
the years reached a optimum in

968
00:57:18,145 --> 00:57:21,365
terms of a technical,
an economical, skill.

969
00:57:22,040 --> 00:57:25,160
So moving forward, of course,
we don't want to, yeah,

970
00:57:25,160 --> 00:57:29,500
stop here and also looking at the
large blue hedging demand in the future.

971
00:57:30,065 --> 00:57:33,825
We do have ambition to
further reduce the levelized cost of

972
00:57:33,825 --> 00:57:36,005
hydrogen by another
thirty percent.

973
00:57:36,865 --> 00:57:40,890
And this will be
done by standardization and modernization

974
00:57:41,510 --> 00:57:42,950
of this already, yeah,

975
00:57:42,950 --> 00:57:45,430
proven five hundred
thousand per day train size.

976
00:57:45,430 --> 00:57:47,530
So that is our ambition
moving forward.

977
00:57:50,455 --> 00:57:53,735
Great. Can I make a
general comment? Oh, yeah. Absolutely.

978
00:57:53,735 --> 00:57:56,775
Just gonna go ahead. Yeah.
I was just gonna say there's,

979
00:57:56,775 --> 00:58:00,260
quite a few people I
think inquiring about, you know,

980
00:58:00,260 --> 00:58:03,700
Shell's view on hydrogen and
the challenges that there are

981
00:58:03,700 --> 00:58:07,345
in trying to develop a hydrogen economy
And just to say that, you know,

982
00:58:07,345 --> 00:58:12,625
sadly we can't really represent showing
that context in this, forum, you know,

983
00:58:12,625 --> 00:58:15,270
we're talking about just the
technology that we have to

984
00:58:15,270 --> 00:58:16,330
produce the hydrogen,

985
00:58:17,270 --> 00:58:19,690
from, you know, from methane
and other feedstocks.

986
00:58:21,030 --> 00:58:24,145
But maybe if people want to
see what shell policy is on

987
00:58:24,145 --> 00:58:25,845
hydrogen and views about

988
00:58:26,545 --> 00:58:29,025
helping to deal with the
energy transition and what our

989
00:58:29,025 --> 00:58:32,260
ambitions are, to reduce the
emissions from our own operations,

990
00:58:32,260 --> 00:58:35,140
I could steer people to
the Shell Investor web pages,

991
00:58:35,140 --> 00:58:37,300
where there's quite a lot
of content there where people can

992
00:58:37,300 --> 00:58:40,675
find out where Shell stands on
this And I'm sure that there

993
00:58:40,675 --> 00:58:42,915
will be more coming from Shell,

994
00:58:42,915 --> 00:58:45,735
broader Shell on that
regards in the coming months.

995
00:58:47,970 --> 00:58:51,490
Yeah. Excellent. Thank you, Justin,
for mentioning that. And, yeah,

996
00:58:51,490 --> 00:58:55,170
I do recommend going to the
show show has a very robust area.

997
00:58:55,170 --> 00:58:57,645
I'm gonna talking about,
energy transition.

998
00:58:57,645 --> 00:58:59,645
I've looked through
that extensively. So, yeah,

999
00:58:59,645 --> 00:59:02,765
thank you for mentioning that
because it does provide a lot

1000
00:59:02,765 --> 00:59:07,090
of information on on on
Shell's view on on, hydrogen, energy

1001
00:59:07,090 --> 00:59:10,210
transmit, and and transition
in in items like that.

1002
00:59:10,210 --> 00:59:12,770
And and and speak on the
kind of topic like that,

1003
00:59:12,770 --> 00:59:15,305
I'm kinda curious as
my last question is,

1004
00:59:15,305 --> 00:59:17,465
You have sparked a lot
of interest, of course,

1005
00:59:17,465 --> 00:59:18,745
in this technology.

1006
00:59:18,745 --> 00:59:21,565
And I'm curious if people
want to learn more,

1007
00:59:22,680 --> 00:59:25,740
more find out more
information about Shell's SGP.

1008
00:59:26,360 --> 00:59:28,940
Where's the best place they
can go look real quick?

1009
00:59:33,595 --> 00:59:36,795
So, we content will be,

1010
00:59:36,795 --> 00:59:39,935
going on to the Shell
Catalyst and Technology website very soon.

1011
00:59:41,320 --> 00:59:42,140
We basically

1012
00:59:42,840 --> 00:59:45,080
have been preparing material
for the launch of the

1013
00:59:45,080 --> 00:59:47,480
technologies through this
platform, and we thank you for

1014
00:59:47,480 --> 00:59:49,820
that. So, yeah,
coming to our website,

1015
00:59:50,365 --> 00:59:52,605
shortly will be the content
that people are looking for.

1016
00:59:52,605 --> 00:59:53,905
We'll have some white papers,

1017
00:59:54,925 --> 00:59:57,410
some fact sheets and
other information regarding that.

1018
00:59:57,410 --> 01:00:01,010
And at that site, you can
also reach out to representatives of,

1019
01:00:01,010 --> 01:00:04,950
of the organization in the
regions where people may have queries.

1020
01:00:06,985 --> 01:00:09,465
Excellent. Well, we're right
up at the top of the hour.

1021
01:00:09,465 --> 01:00:11,245
So I think we'll
we'll end it here.

1022
01:00:12,400 --> 01:00:14,960
We can't really get to all
the questions because you you all

1023
01:00:14,960 --> 01:00:17,200
really sparked a lot of
interest because we've received

1024
01:00:17,200 --> 01:00:19,985
well over two hundred and
fifteen questions. So,

1025
01:00:20,705 --> 01:00:22,405
you'd end up be getting hoarse,

1026
01:00:23,025 --> 01:00:26,225
but we had to answer all
of those. But don't worry.

1027
01:00:26,225 --> 01:00:27,480
If you did ask a question,

1028
01:00:27,480 --> 01:00:31,100
all of these questions will
be sent to the speakers,

1029
01:00:31,720 --> 01:00:33,560
right after this
webcast. And, of course,

1030
01:00:33,560 --> 01:00:35,820
they will they'll try
to answer those offline

1031
01:00:36,495 --> 01:00:37,875
as soon as they can.

1032
01:00:38,495 --> 01:00:42,335
But definitely, we really wanna
thank our speakers today. Nan,

1033
01:00:42,335 --> 01:00:43,615
we wanna thank you, Justin,

1034
01:00:43,615 --> 01:00:46,130
for for jumping in during
the Q and A session.

1035
01:00:46,130 --> 01:00:49,090
We really wanna thank for
Shell Catalyst and Technologies for

1036
01:00:49,090 --> 01:00:51,090
putting together this
timely and perform,

1037
01:00:51,090 --> 01:00:52,230
informative presentation.

1038
01:00:52,930 --> 01:00:56,115
Now there will be an on demand
version of this webcast.

1039
01:00:56,115 --> 01:00:58,915
Gonna be made available
in the coming days.

1040
01:00:58,915 --> 01:01:02,435
You will receive an email
on that. So if you have any,

1041
01:01:02,435 --> 01:01:04,435
if you have any other
colleagues in the industry that

1042
01:01:04,435 --> 01:01:06,330
might be interested
in this technology.

1043
01:01:07,030 --> 01:01:09,510
Please definitely forward
that to them. Again,

1044
01:01:09,510 --> 01:01:12,865
we wanna thank all of you,
for joining us for webcast today,

1045
01:01:12,865 --> 01:01:15,125
and we hope you have a
great rest of your week.

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