So they're fast groupies to Devon so
we have over there today and

the ferocity of the group even so
nice to be in your presentation.

They said we're going to love it when
we've been sitting on our process for

the production of a mallet a pipe probably
in for use in felde regulated lead acid

batteries to some background
first very related.

Let us a very traditionally more
expensive to reduce them flutter

that acid batteries due to the high cost
of use or glass must separate within them.

Therefore we try to lower
the cost by finding

a different Hill to use in the separator
we chose copper pulling due to its

low cost as well as its mechanical
properties which are suitable for

use in the batteries however it has
much lower but ability then the A.G.M.

Therefore we decided to graft Milligan
hundred on to the pipe probably

to increase its one ability of
a sulfuric acid with in the battery.

This is our overall process
will die down first.

We have are two of the actors which
produce twenty thousand kilograms an hour

of point providing from the reactors
the slurry is fed is he didn't enter into

a flash to favor I.C. unreactive
probing which is then cooled and

recycled back to the reactors
some probably is pelletised and

sent to storage for
either commercial scale the excess or

use in our sugar forty kilograms an hour.

Essentially sugar and
combined with Mike in hybrid N.D.B. ha.

Which has a rate of forty kilograms an
hour based on average three hundred thirty

days for twenty four hours a day and
to produce thirty five one hundred meters

Q per year of the math
separator Inside Edition.

I don't think opponents are heated and

they ran the graphing reaction occurs in
the last barrel did more in a surprise to

Favorite the UN reacted like it had read
as well as the degraded initiator products

this paper is then called in a portion
is recycled back to the shooter to.

The cost of fresh milk and
hydrated the Malaita fight for

a billion leaves they sure
as a melt pelletised and

then can be used to be spun into five
years for use in the mad separator.

As far as implication of proofing goes
is establishing the second phase of this

project we're looking for
a home with the following characters.

We've ever familiar weight of one
hundred thousand grams from will

not flow rate of four hundred grams for
ten minutes in a pot is pretty and

makes it to whoever we found in this
commercial group reactors produce a poem

of a much higher molecular weight as
a result of falling kinetic equations or

modeled in matlab we manipulate
initial concentrations of hydrogen and

Co callus for the reaction to Ethel other
many to increase the rate at which growing

chains were terminated this had a direct
influence unlike the rate of a polymer

we decided that we want to be able to use
both the polymer that we required and

also a polymer that can be sold
commercially as the majority of our annual

production rate would be sold on
the market this graph serves to

attain polymers with different starting
conditions the noting factors also that if

we need to preserve any other polymer
we can simply manipulate the initial

conditions to produce any desired polymer
as far as the design of the reactor went

the recycle ratio is the first thing
we looked at as far as producing it.

We found that a minimum recycle ratio of
thirty was necessary to maintain C.S.E.

our behavior within the reactor as
a result we calculated the highest

single pass conversion that we could
attain from start up although it is steady

state on this graph it is shown that
has a respective cycle ratio of thirty.

The volume of the reactor was sized off
of a specific polypropylene production of

four hundred kilograms per hour per meter
cubed This resulted in a total volume size

of forty meters cubed for
fifteen years skewed by that and

the dimensions of the reactor
were based off of heat transfer

as you need to maintain a constant
temperature within the reactor and

over all heat transfer coefficient between
the cooling jacket around the reactor and

the reactor itself was key in
determining the diameter of the reactor

the overall he transfer coefficient
was deemed to depend on

the diameter of the reactor the velocity
of the fluid within the reactor and

the velocity of the fluid on the exterior
the reactor using high velocities.

Both fluids we're able to maintain
turbulent flow and height heat dissipation

in between or it within the fluid
The following the overall heat transfer

coefficient is found in literature for
a diameter of point eight five meters

this diameter was used for any further
reactor sizing in order to obtain them

what ability that we require we
Mally added the propylene chain with

like a hundred we did this in
a twin skirts trigger to attain

a weight percent of point six percent
of hydrated on the final product.

The first portion of the extruder
raises the temperature of our reactance

two hundred eighty degrees Celsius.

This allowed us to decrease the amount
of the P.H.A. which is the initiator

of it decrease the use of our initiator
and which was a very expensive

the next portion is where our reaction we
assume by reaction actually took place.

It's eleven times longer than the
beginning fortune and the final portion.

If our portion is two hundred
thirty degrees Celsius and

is heated that high to help
separate the products stream

to design our exit or
we look at mean residents time.

Screw speed helix angle length
the ratio of length in diameter and

the with of the Screws we
found these optimal ranges by

looking at literature and
commercially available extruder and

we optimize them to decrease costs in
utilities and decrease costs of right.

So next we need to remove the unreactive
and hydrate integrated G.B.H. say.

From the produced million a polypropylene
and in our evaluation we assume that

deviates a degraded into five
compounds was integrated into ethylene

which was assumed to pull in rights to
form polyethylene the exterior acetone

to metal do you know into five
dimethyl hexane to five dial.

We then looked at three main design
schemes our first design scheme

included distillation column.

We recycle the bottoms product
containing the lake and I dried.

Next we looked at sin all by products
to a waste disposal system and

finally our chosen process
of condensing the vapor and

recycling some portion of
that back to the exterior.

Our chosen design that uses the last
barrel the extruder operate it.

Two hundred thirty degrees Celsius to
vapor to vaporize unreactive Milliken

hydrate integrated deviate say that they
perceive is then called in a portion of

that is recycled back to make sure we
then found the optimum recycle ratio

by determining the cost of manufacture
versus recycle ratio and their analysis

included tradeoffs including feedstock
costs waste costs utility costs and

the capital cost of a larger exchanger in
the end we found our recycle ratio to be

about eighty percent on this side we look
at the benefits of using eighty percent

recycle versus the waste disposal system
in both cases we assume two operators for

a solid liquid waste
process processing our M.H.

feedstock costs are reduced by about
thirteen thousand dollars per year from

twenty thousand dollars a year to about
seven thousand three hundred dollars

a year waste disposal costs are also
reduced to about seventeen thousand six

hundred dollars per year about
ten thousand dollars per year.

One of the trade offs is
the increase electricity costs

used to heat the reach of
the recycle stream in the extrude

that would require an extra
eight hundred dollars per year.

And finally our exterior
capital cost increases of about

thirteen thousand dollars.

Like any industrial facility we are going
to have safety concerns the majority of

ours are chemical related all of our
chemicals used are hydrocarbons and

are extremely flammable.

We also have again hydride which is
closer to your skin long and eyes and

then we have our initiator for
the plumber zation reaction which ignites

spontaneously in air and wrecks of water
to form flammable gases to mitigate these

concerns we designed our process to have
relief elves' that lead to players in case

of over over pressurization a valve we
designed our storage to have an psychoses.

Warning and should have an inert gas
covering the reactor species we also have

need to have valves that protect other
comment like our pumps from back flow and

all of our equipment were designed
to be fire and explosion proof.

We also suggest extensive employee
training on the use of these chemicals and

advanced hazard and
operability analysis in the next for

over a week current economic analysis and
first here you will see the raw material

prices we use the raw material prices
were up to and from different sources and

most of them have different ranges in the
case of the propylene monomer we decided

to use the highest cost which is a dollar
forty three per kilogram just for

worst case scenario analysis in the case
of M.A.S.H. we had several sources and

we decided to use an average of the price
ranges we found for deviate and

we only found the last gold price which is
about one hundred thirty particular gram

from seem all of age.

So what with these words we use
an estimation equation to determine or

estimate the ball price which came out of
the air on eleven dollars per kilogram

finally in the case of Holyfield billing
We did a special no I says to determine

the price we will use and this was mainly
done because of the high production rate

of P.P.
of twenty thousand kilograms per hour.

What we did was we found the worst case
and best case M.P.V. assuming a process

life of twenty years and also assuming
that excite has said B two B.

plus rating for a fifty fifty
borrowing to equity relationship

as you can see the two worst and best case
M.P.'s differ about a billion dollars And

again these has to do with the production
rate of P.P. what we did was we were

giving a benchmark we were giving
a benchmark our While forty percent.

So what we decided to do was we
determine the price of polypropylene

that will be required to
obtain this benchmark.

We also want to point out under previous
cases we our previous faces we analyze and

thought about blending the Malaita
political impel this week.

Pelley at building
pallets to reduce costs.

However if you see here where the F.X.
is the way percent of the focal length.

You can see it up here P.P.
Matt has the lowest learnt raw material

costs associated with it and so
we base our design our on this case.

We also heard on several
profitability analysis again

soon enough lots of life of twenty years
and we don't benchmark our are you.

Forty percent.

Here you can see that I rely on N.P.V.
for the five cases we analyze where P.P.A.

refers to just producing and selling
polypropylene kind of like a base case.

P.P.S. refers to prove to seem
polypropylene on side drafting it and

selling that extra P.P. and the malleable
liberal billing I finally G.S.

refers to buying the full you
probably from ass I source and

grafting it on side the forty four hundred
the first two production race we studied

so we have a forty kilo gas for
our production of Mallya to police.

Properly and four hundred kilograms per
hour of mallet a pulley probably in

production as you can see none of
the cases we studied actually meet there

are oil quoted per cent and

in some cases are negative meaning that
the venture is not profitable at all.

Additionally for the N.P.V. when you
compare these three cases where the P.P.

is produced as opposed to just
producing Malaita politically.

You can see that there is a significant
difference in them over twenty years and

I guess he has mainly to do with the fact
that the police Brooklynese produces such

a high rate.

We also determine the prices that
we would need to sell our May P.P.

pellets in order to obtain an M.P.V.
of zero and an audio forty percent.

Consider the current market price
of Mallett of filling these two

dollars These prices are relatively high.

Lastly we determine the effect of
reducing the base of operation.

Our initial analysis was based on
the assumption that we will operate three

hundred thirty days per year.

However when you decrease the production
days from three thirty to

one fifty you can see that the cost of
manufacture for both cases decreases and

be becomes less negative.

This has to do mainly with the fact that
a large portion of the cost of manufacture

cars from the operators and wages and
benefits and the like and so all the R.

and B. these are negative for
the graft in process is what

is actually happening is that to produce
one kilogram of M A P P Your cost

is actually decreasing when you
increase your production rate so

going from forty to four hundred
kilograms of our produce cost you from.

The cost decreases from eight dollars
to about three dollars three kilograms.

He says mainly to do as you can see in the
pipe as with the fact that as you increase

the production rate your sales increase
relative to your annual cost of

manufacture and general expenses a benefit
of producing our own Maliana polypropylene

we can control the grass to make sure we
obtain where our project we were told we

are eight point six percent valuation
ratio However most of the commercial

ones we found a way between point
eight to one point two eight percent.

However there actually is associated
with a higher production rate and these

have mainly to do with the higher capital
costs and there's also the uncertainty

about whether there is that the man for
any people in that market.

Having seen a economic analysis you may be
wondering why more people aren't producing

polypropylene well appropriately market
is in fact growing and two thousand and

eight roughly fifty million tons of play
propylene are produced that is expected

to increase a perfect twenty percent
to sixty two million times by or

within five years by two thousand and
thirteen.

However it is a well established
market highly competitive and

the current polypropylene producers are
building sufficient reactors not only to

meet the forecast of the men but
to surpass it.

That brings to our next point their
very volatile prices on one and

the main feedstock to building play
propylene is propylene as it comes from

oil its price is predicted to increase as
oil prices continue go up on the other

hand as the current supply applied propane
is increasing faster than the demand

the price appropriately is continuing
to drop until a balance is met

this means that currently prices are
dropping to the point that the Palmer is

at times cheaper to buy than
the monorail to make it.

Furthermore at the scale
of design exams annual

sales were posted as three point
three billion on their website.

We are prepared producing for the
polypropylene reactors is producing enough

polypropylene to sell with an annual sale
of roughly three hundred million dollars.

This represents roughly nine to ten
percent of exiles total sales which is

a high risk for the company incorporate

therefore we discourage supply
prevent production for exit.

Family we do encourage
looking at the million and

probably propylene production
process in the producing.

In the pipeline in larger quantities or
do some number of days of operation and

either case we need to optimize
the grafting process for

these new production rates.

We also recommend looking at the bigger
they should mechanism of deviate say or

finding less expensive initiator

in effect side does decide to pursue
a pipeline production process we also

recommend looking at a less dangerous
Co catalyst and try at the aluminum So

that concludes our presentation and
thank you for your attention.

I mean you know

it's just really easy.

We have basically anything that we did so
we decided to send everything the way for

total waste costs would be about seventeen
thousand six hundred dollars a year and

that's assuming a waste of about one
hundred forty five dollars per barrel.

We'd have about seventy
barrels per year produced so

if we recycle back we're going to
use more RAM age not drastically or

cuts our way it's cost
about ten thousand dollars.

Well if you're

a pricing one that really
stands out right now.

Well I used to be you when
you hear a little bit.

I love to write a cell phone right now do

you make any assumptions
on the processing hosts

that you know possibility of some sort of
human emotions all on the front of that.

Well the one we actually use right
now this is eleven dollars a kilogram

I get that an estimation and actually
I mean definitely the most significant

cost in terms of raw material at least for
the grass you session because every time.

Rise but at the same time it's a
relatively low production rate of any P.P.

for either forty two asked for our four
hundred kilograms per hour in salt as

a price goes down to like two luxury
kilogram which doesn't seem possible since

it's relatively expensive and

I will not that we will not think he will
have a such a big effect on our results.

So this is Steve has to be
with you in your mission

and not.

Thank you very much.