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Preface
Following
technically productive careers in coatings, and
then polymers, the author turned to paper in the early 1970s. This soon led to a position as Contributing
Editor, Chemistry, at Paper Trade Journal, the
principal industry publication until TAPPI
started the TAPPI
JOURNAL.
My
driving ambition was to learn how best to fully optimize
the papermaking process. In the course
of doing this I helped to invent five different means of measuring
electrostatic
charge on particulates, culminating in the on-line Zeta Data which uses
the
streaming potential principle to measure zeta potential, and also
measures
conductance and specific filtration resistance, a parameter fundamental
to
drainage.
Oddly
enough, the most productive line of investigation
turned out to be the apparent anomalies to normal systemic behavior. Some of them took years and were very costly
to explore, but the total picture slowly emerged.
The
fundamental technical rationale to wet end chemistry is
nanotechnology, which is the application of nanoscience principles to
nanoparticles, those on the order of a billionth of a meter in size.
Nanotechnology
is a game changer that will enable great improvements
in the cost and quality of papermaking: 90%
reduction in chemical cost; 40-60%
reduction in energy usage for
water removal; minimum raw material cost, maximum productivity,
unsurpassed quality
and sustainability.
The
process consists essentially of a series of well
established unit engineering processes, conducted under computer
control in the
most efficient way. The only serious
functional uncertainty is that of scaling each process to an existing
or (much
less expensive) new machine or re-build.
The
following process description is not submitted as
definitive; it is simply intended to connect all the principal dots,
and
provide a coherent explanation for those interested in licensing on
exceptionally attractive terms.
Introduction
Paper
was made on a continuous wire for a century and a half
prior to the introduction of synthetic organic chemicals on the wet end. The use of “retention and drainage aids” was
so revolutionary that machine management delegated supervision to their
chemical
supplier.
No
analogy exists in modern industry. One
could think in terms of a bakery in which
recipes for the breads, cakes and other pastries are assembled and
prepared by
one chef, then baked by another. Such a
division
of duties is so inappropriate to the task, it inevitably leads to
dysfunction.
Our
research over decades has led to the definition of
papermaking as a nanotechnology. A brief
review of the defining differences between the ‘conventional wisdom’,
as
practiced by the specialty chemical suppliers, and papermaking
nanotechnology
reveals the gross inefficiencies that have developed because of the
cultural split
between physics and chemistry.
Mixing
to Homogeneity
In
the ‘conventional wisdom’ process, a decrease in positive
charge with time is observed, characterized as “cationic decay.”
On
the other hand, papermaking nanotechnology first reduces
the interfacial by about two-thirds. It
then
exposes the stock to vigorous agitation, such as ultrasonication. The bundles of chemicals are dispersed on a
molecular
scale, creating a homogeneous stock.
Not
only does “cationic decay” disappear, but chemical
efficiency increases by one to two orders of magnitude, resulting in
chemical
cost savings in the range of 90-99%.
Macroflocculation
vs. Nanoflocculation
In
the ‘conventional process’ a “retention aid” polymer is
used to flocculate the fillers, fines and fibers so they are retained
in the
web of stock on the rapidly moving mesh surface. The
resultant macroflocculation is effective
in retention, but imposes a cost of major loss in smoothness and
strength.
In
the nanoflocculation process, mono-functional chemicals
rather than polymers are used, with the result that flocculation is on
a
nanoscale. The result is a smoother,
thinner, stronger sheet.
Computer
Control of Zeta Potential
The
electrostatic charge is conventionally measured by an
off-line assessment of cationic demand, using a charge analyzer with a
Teflon
tube that adsorbs colloidal particles and is exceptionally difficult to
clean.
There
are two decisive problems with this methodology: it
is not reproducible, with a low correlation
coefficient of 0.17 vs. zeta potential; and it is not the most
appropriate
measurement to begin with. The most
desirable parameter would be zero zeta potential; it bears a
correlation coefficient
of 0.72 with sizing.
The
nanoflocculation process
ideally uses no polymeric retention aid and achieves a zeta potential
of zero
millivolts. This form of electrostatic
flocculation is sensitive to agitation. It
requires a homogeneous state entering the
headbox and quiescence
thereafter, to support aggregation.
Zeta
potential is measured by the online assessment of
streaming potential, sampling from the downstream recirculation leg of
the
headbox, and continuously returning the measured stream to the white
water
system.
Zeta
potential is controlled by a computer which serves to adjust
chemical feed rates to maintain a headbox zeta potential of 0 mV, using
a
chemical balance that maximizes productivity at minimum raw materials
cost.
The
result is unparalleled quality and uniformity, at
minimum raw materials cost. Software
provides
the actual cost of each roll, to the penny.
Increased
Water Removal and Energy Savings
Process
chemicals include an anionic nanoparticle, such as
colloidal silica; and a mono-functional cationic chemical such as
cationic
starch. Under zeta potential control
they yield the best possible balance between retention and formation,
and result
in a structure that maximizes water removal on the wire, press section
and in
the dryer.
Our
nanotechnology process employs a water immiscible
hydrocarbon catalyst which, at low concentrations, reduces interfacial
tension;
and at higher levels can azeotrope with water, greatly reducing the
amount of
energy required for water removal. It is
easily re-cycled, using standard engineering unit processes.
The
hydrocarbon is innocuous, and approved for use in food
packaging. It is fully retained within
the process; none exits with the product.
Sophisticated
techniques have
been used to explore the
dimensions of water removal, including differential scanning
calorimetry,
thermogravimetric analysis, variable and fixed speed pilot plants, and
azeotropic efficiency. Some of the
physical parameters we measure are interdependent and some are
concentration
dependent. Quantitative analysis is
complex indeed.
It
is important to understand
that the faster the machine,
the greater the water removal in the press section; the hydrodynamics
and
reduced interfacial tension reduces water rewetting; and also recognize
that
increased press section consistency has a multiplier effect on dryer
efficiency.
Finally, one
must realize the
large effect of reduced
interfacial tension in reducing the hydrogen bonding of liquid water,
and
thereby saving energyOur best conservative estimates of energy saving
are 20% in a high speed press section; and 20-40% in the dryer, or a
total range of 40-60%.
John G. Penniman
www.papermaking-chemistry.com
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