So the first question we have to ask
ourselves is what exactly is it all for

you know that it left
the factory as you can see here.

If not regulated lead acid battery in
typical cell consists of a positive plate

negative played in a absorbent glass mass
separator between the hold feel like your

life electrolyte allows the charge
to transfer between the positive and

negative plates.

The goal of our project is to
replace this absorbent glass not

separator with a polymer alternative.

The reason we want to do this is
mostly due to the compression recovery

as you can see here as a battery charge
and the charges you have a compression

decompression cycle and which the fibers
within the glass mountain break

allowing them not to return to
your to their original state

in which case the electron I will
not be able to reach both electrons.

However with the pole miracle turn
it is the math can reach both

places along the electrolyte
to transfer between

allowing electronic transfer
target between the place.

Additionally we have also found that have
better physical properties as you can see

here with the puncture stream and

the turnstile stream and
it is also less expensive.

However the only problem with it is that
there is a low sulfuric acid What ability

in order to mitigate this problem.

We need to mainly the polypropylene mainly
to poly prickliness hydrophilic graph

polymer with a polypropylene backbone
which in undergoes a radical change of

transfer reaction with a organic
proxy which transfers radical

to the polypropylene
change the double bond and

the Milliken hydride then reacts
with this radical on the back but

in order to mainly as the polypropylene
the addition of the mailing and

hydrate adds to Carbondale groups to
the polypropylene back to increasing

the sulphuric acid What ability not going
to hand it to Devon who's going to discuss

her process for diagrams and.

It was the only

problem related from her vision prostrate
and using to use your full live

reactors in series with your own
process using are not a catalyst for

the liquid propane going on at the reactor
Titian's mentioned right there

records on is based on overall
he transferred coefficient

which the protein production rate and
the rate of limitations.

Those are used to calculate
the area of harpy transfer and

thus the reactor dimensions following
the second reactor the effluence vent to

a probably be fried to which
a liquid propane is vaporized.

And then sent to a settling down and

settling your on with the gas use
propylene to separate from the solid

pipe probably desperately is that overhead
too as they have condensers in and

is then recycled back again in the process
to solve my problem however is going

through a series of Rotary valves here to
a finishing section which is palletized

and then dried and kept for
storage in shipping.

Now we have a jury to discuss more
about the record extrusion for

the reactive extrusion process we
determine that we needed to use the twins

were extruder to for the grafting as you
can see here our twins groups are divided

into three sections the first of
which being the melting section

in the melting section the initiator
D.B.A. may be going to drag in

the polypropylene are fed in and heated up
to the reaction temperature of one hundred

eighty three degrees because we have done
there after the heated up the melt close

close into the grafting section and
which the initiators consumed and

the polypropylene is mainly aided in the
grafting section we optimized the extruder

parameters in order to minimize the amount
of initiator we needed to still reach

a point six five percent of the major
grafted we did this using a minimisation

function with the following constraints we
have listed here with temperature screw.

Rotation speed link length over
diameter ratio and residence time of

the station of the injured leader lead to
these parameters here after the grafting

section the metal clip first to close
to a Melville into the final stage and

which pressures drop and temperatures
increase to two hundred thirty degrees to

boil off the volatile byproduct shuns
going to discuss what we do with

a pipe product as you can see here
the start process the section

you are probably deviated from each good
bit of these your little fundamentals of

the major separations process before we
actually process the B.H.A. breakdown into

primary process does we team you know
in Time magazine today his statement

that post notes you will be increased
attention to her the results you can pull

back to you are all these ball block
products from now a lot of profanity.

You just lived through that you
call today is really time for

Tuesday we are all unit analysis
including financial and

CD concerns this new five hundred say it's
been six windows user streams the first

release thirty seven research
really just set off site.

Waste disposal company and
we're being silly.

To the remaining seven you see it as a
researcher who needs to rationally view on

crime in order to decrease
our cost of crushing weight

upon these actually reduce our costs by
really sixty percent in his other words

if you look in the financial crisis now
the process photogram has been discussed

in details on this because
the financially to delay the process.

Probably a limitation process is a highly
credentialed with a net present value in

a product life of one hundred twenty
million dollars This value is calculate

using a financial basis table Daugherty
five a kilogram or kilogram polypropylene

and have a production cost for
our process with a sixty kilogram

pipeline produced it gives us an eleven
percent profitable profit margin which

decouple average direction costs to
measure the robustness of our process.

Basically it says what the spread between
the cost of proclaim and the selling price

upon problem has to be in or from this
process to have a positive cash flow.

This is further described in
this waterfall chart here as you

can see this is the.

Down to the selling price of
piper when per our process.

You can tell this is the cost of feed
stocks and dog of the five on top of that

is decouple the average production cost or
the cost added based on manufacturing and

then to get to dawn on the seven
in the eleven Step profit.

This gives a financial settlement of
investors return on investment and

a twenty percent pay back
period of less than a year and

investors rate of return
to seventy four percent.

I give it to rediscuss direct extrusion
economics as you can see here

the financial feasibility of Rex
extrusion is not as nice as the home or

station section.

We have a net present value at the end
of the projects life of six point five

million dollars And this is mostly do as
you can see up here to a financial basis.

The cost of polypropylene is a dollar
eighty six a kilogram all of the selling

price of Malay polypropylene is two
dollars a kilogram in our production.

It cost four dollars and
fifty six cents a kilogram to make

made about profiling which is a couple the
average production cost of two dollars and

seventy cents as you can see in
a waterfall chart here as we said the cost

of college propane is a dollar eighty six
and the decoupled average production cost

is two dollars and seventy cents which
comes out to four dollars and fifty six

cents over the selling price of the Malay
to pull it propane is only two dollars.

Therefore we have a two dollar and
fifty six cent loss for

every kilogram of Malay to polypropylene
we make this process this yields

a return on investment of
negative sixty six percent.

I'm not going to have to back
to court process alternatives.

The one process the term that we
considered was to have a flash valve

downstream of the program vaporizer is
director from would be here to a certain

temperature and in fact across about to
vaporisation this process was discarded

because the energy requirements for
flashing rashly higher than if they'd just

been vapor and then if it were proven had
just been vaporized inside probably favor

either Additionally one hundred percent
pavers ation of the liquid could not occur

across the valve thus again this
process was discarded the next

section that we looked at alternatives and
would be reactive extrusion section.

As you can see in the pie chart of our
base case here where we are operating at

three hundred thirty days a year
at forty three kilograms an hour.

Operations make up forty three percent of
our cost breakdown which leads to a N.P.V.

of negative six point five million dollars
in order to mitigate the operational cost

we tried reducing the operation days a
year to thirty an increasing flow rate to

four hundred seventy five kilograms
an hour to make up for that

this indeed reduces operations cost only
seventy percent of our cost breakdown and

feedstocks increase to sixty nine percent.

However we still have a negative N.P.V. of
negative three point seven million dollars

a third way we try to negate this
operations cost less keep operating

at three hundred thirty days a year but
increase production one hundred fold.

During this makes operations cost
negligible but feedstock in total

eighty six percent of our cost breakdown
which leads to a negative impede of

negative fifty two million dollars due
to the low profit margin of the process.

There are two doctors you want
to look at you believe deep

separations of recovery section
versus change the reasonable ratio.

She talks utilized to do we respond to
the calls in the linkage I received

degrees is no longer going to be
economically feasible research so

you send your way as he walked away or

should be concentrating on just
the injuries is not the increase of these

are the ratios we want to try to minimize
the time here is that we've been Streeter

subsequently of the cosmetic really
reasonable and would potentially it's

going to slip Paul Eaton purity of your
political right as well as the reach of

the Republicans however with this specific
snoops a day because of the way it hard it

is not only because just because it
is not with costs and letting it run.

So we don't recommend
it on the dissolution.

It's not a new deal or some safety
concerns consideration there and safety

issues of the pipeline from production
process there are using a high pressure

high pressure material I.E.
liquid propane mitigation procedures and

Harry safety risk is to have
a system a safety valve and

a flare system installed to handle any
kind of process upsets dish and we did

last utilities analysis around the process
to determine a worst case scenario.

Namely steam and

cooling water cooling Mars this could lead
to a runaway reaction inside the surface.

Reactor.

This can lead to a dangerous build
up of temperature and pressure and

thus a dangerous situation
a mitigation procedure would be

have a dedicated cooling water
supply to the cooling water jacket.

Additionally if Steam or lost the propane
paper riser this could lead to system

failing in a program release because
liquid propane were NOT be vaporized and

would thus fill up the settling
drum that would follow the drum

Additionally at the bottom of the said
Lingard at the bottom of the sideline drum

there's a rotary valve that spans if
it were in the drum it would release

liquid probably medication procedures we
would be to have emergency electrical

heating along the pipes to vaporize
the propylene in addition to having proper

control systems in place to
stop the valve from spinning.

If the steam rate drop
below a certain level.

This is a consideration or

to react structural failure
to the hole in the lake.

If I drive down metal heavy tile T.V. all
specifically all reasonable compounds and

flatness will be already conditioned
room within the executer So

it's clearly meant to be actually
go on this newer better oxygen for

mixing with any of these will cause
potentially violent causing fire or

an explosion has essentially created your
fire EDITION both teams you know and

age can cause of your
respiratory problems.

Therefore in order that harms
were already in person.

Now we need to have a problem which
isn't installed in the system a worst

case scenario would be if we
lost the ability to remove or

to vaporize our all the wires products
as well as move them from the sphere

subsequently recommend that post condenser
as well has been easier we have the right

to leave that says don't do these units
that are in order for any excess by

frost any kind of accumulation of
the bottleneck is mighty hard right.

Should the need arise in the worst
case scenario when it is all who's in

recommendations and economic Not

if you know there.

You know you're going
to hear me hear things

from the from that

you Series here is on the radio rituals.

You know I wouldn't believe
you give a single good

amount of energy out of the actual entire
flow rate through the by a cross Mike and

I tried to bypass the system in a time of
the maximum about five kilograms an hour

and so if you're not going to look to one
that is the right to use that as an energy

source of me or you want to separate it
out on sight is in the case near which

you had actually failure
that well the two.

Yes and for

the zero cost analysis thing to look for
the soul of

yourself was the drawing there are three

scenarios that I have to go to the first
is that copies of producing the way.

Get the value of what I wrote when Joe
who's a much larger scale than ours and

it's like so what we are talking over
through the second is labor costs.

This is the price of what
we got was from pay for

coffee the labor costs in this building
creased in the United States decreasing

their costs by hangovers last and
Sarah isn't necessarily a viable option

is author of the if there
are outsource Now that is the old.

The third option is that reactor extrusion
isn't the only way to add a call.

I will come down to a whole or battle
other companies your theory is that is

it is a rain or shine real radical
rather than using radical these years.

If you change our view saucer high and
that's a war has a lot of work to do.

To D.J.

is expensive the radiation method instead
of reacting to that actually costs more.

When you get the price if
you're not you know I was

founded on line it was from
a distributor overseas chain.

Maybe it could be lower the cost of

U R D B H I was about twelve
dollars a kilogram we use the same

messages from a script to scale
the price to both from a lot of scales.

So it's very dependent on what exact
lab scale price you got for the scaling

procedure so ours is slightly different
but it's the same order of magnitude.

If you do goodness of the health and

then you know you fill in those costs and

it was just

your brains you know the call did
not because it was all rather

spend time I mean I assume that's
factored into its base cost on

the most cost or slightly overestimated
due to the small scale of the process.

So there is a little leeway in the costing
However we did not cost nitrogen

blankets and that type safety stuff
as we did not have touristic on hand

cost them their worst piece of news just
getting used to cost the process more play

less problems were solved it is as
we were already not a guesstimate

you know there's no question.

You assume to be an issue
broke down the aisle.

You know.
Yes.

You broke down into something else.

Cool kinds of problems.

We don't need so one of the reasons
we pace is if we keep you know I see

no reason to do one of
the worst case scenarios.

If you go to a couple slots for it.

We actually have a slight up here
which actually has to bring down

a view and we soon.

Thanks enough.

With this one right here and

there is you know those who were placed
near is the other on the other by Iraq

you look at it is definitely I mean if
you soften that during the process of

working in the presence of a rat
with a shield you need security.

I don't care that it's very likely I think
a little all the other reactors are all

the other byproducts are easily
condensed acetone I think set you

know on your cell phone but essentially
all these little test condenser in

addition are condensers actually prices
that are processed as actually larger

that we got as well to
a minimum to do this.

Reza the area of truth where the which
is much higher than the fire for

this process.

So we believe that we have to ask for
preachers of those who are offering

temperature condensed everything
down to one hundred the results and

it's about one hundred years or
less of the very pressure of acetone or

something like recess part of atmospheric
and so so what would happen then

in that case that if you have a liquid or
you have a response to a product.

If you don't you know if you
don't reduce the time for

that are two solutions that are degrees of
local water heating this residential or

the area of the desert or the devil
that would last until recently after

the last you can test the acetone edition
that you are seeing is like talking to

vaporize my process by running through
history as to the Syrian border.

So that's vital for any

other Thank you very much.

Thank you.