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Adding a new 550 tpd rotary kiln more than doubled lime production
capacity at Linwood Mining and Minerals Corporation's Buffalo Plant,
located near Davenport, IA...but it also raised the problem of what
to do with a greatly increased output of fines. Realizing that landfilling
its plant property with waste fines at rates of up to 100 tpd would
not be a good long-term solution, the company not only dodged that
alternative but also gained a way to keep new fines in the product
stream at full value with the help of an automated roll press briquetter.
Considered one of the country's largest underground limestone
mines, producing aggregate and chemical lime products for more than
60 years, the Buffalo Plant currently mines approximately two million
tons per year, with enough proven reserves to continue at that rate
well into the 22nd century. Located along the west bank of the Mississippi
River, straddling both a railroad line and a state highway, the
company enjoys three handy alternatives for shipping to customers
across its Iowa-Illinois-Wisconsin marketplace.
Blessed with two different high-quality deposits, the Buffalo
plant supplies an unusually wide range of products. From the Davenport
Seam, about 120 feet (36 m) below the surface, Linwood brings up
stone with approximately 97% calcium and low iron/silica content.
This results in chemical lime products with high appeal for steelmaking,
water treatment, and production of glass and asphalt shingles as
well as animal feed-grade granules and agricultural lime.
Working the Otis Seam as far as 200 feet (61 m) down yields a
different stone that makes excellent aggregate for concrete and
asphalt paving. This bodes well for Linwood sister-firm McCarthy
Improvement Company, which for more than 103 years has been a major
supplier to the highway and heavy construction markets of the Midwest.
McCarthy Improvement was the founding member of what has become
the parent McCarthy Bush Corporation of Bettendorf, IA, a diversified,
family-owned enterprise that includes Linwood Mining & Minerals
as well as various operations in dirt excavation, steel fabrication,
residential & commercial real estate and other subsidiaries.
As with most aggregate quarries, Linwood's mine output is crushed
and screened to produce various sizes of stone...but here, only
about 40% of it ends up as construction aggregate products. The
larger portion, screened to -1¾" +3" (-44.4 +6.4mm),
is conveyed over to the chemical side of the business. Once there,
about half of it gets crushed to produce 16-mesh granules for making
glass and animal feed, or dustlike 200-mesh particles for use as
filler in asphalt roofing shingles. The other half goes into the
lime kilns.
According to Assistant Lime Plant Manager Dennis Jones, growing
market demand and the appeal of more efficient production led Linwood
to add the new kiln in 1998, raising the 350 tpd combined capacity
of the plant's three earlier kilns to a total of 900 tpd. "The
minute we started planning the expansion," he says, "we
knew we'd get into trouble with fines."
He explains that calcined lime (calcium oxide) coming out of the
kilns is screened to -7/8" +3/16" (-22.2 +4.8mm) to derive
pebble lime as specified by the steel and water treatment industries.
Oversize material is crushed to -7/8" and returned to the screen.
In this process, about 20% of the material screens out as -3/16" fines. "Nearly
all of the fines produced by the earlier three kilns has been hydrated
on-site and sold in powder form for such uses as stack purification
(desulfurizing), or making asphalt for paving," Jones points
out, "but our fines market just isn't big enough to consume
the additional load that would come from the new kiln."
Briquetting the fines for sale as the equivalent of pebble had
been considered earlier, recalls Plant Manager Jeff Dahl, but that
never became a viable option because of the relatively small amount
left over after satisfying buyer demand for hydrated lime. Plans
to add the fourth kiln finally made it feasible. "Briquetting
always looked like the only way to reclaim fines in this quantity,
and the only company we saw that could supply the kind of equipment
we needed was K.R. Komarek, Inc., located near Chicago."
"Our main concern," Dahl says, "was that the hardness
of our lime might prevent it from briquetting well. Most pebble
lime breaks easily by hand, like chalk, but with our pebble, you
need a hammer to break it." Addressing that concern first,
Linwood sent several barrels of calcined fines to K.R. Komarek Research,
Inc., a subsidiary headquartered in Anniston, AL, for testing on
specially instrumented laboratory versions of Komarek's production
machines. Tests there confirmed that under about 50,000 psi (345
MPa) pressure, the material forms good briquets at a density of
about 2.25 g/cm, with no need for binders.
Although Anniston data showed that briquet hardness could be increased
a bit more with the addition of Calcium Stearate as an internal
lubricant, it wasn't seen as necessary. In a crushing-strength test,
in which briquets are crushed between parallel platens, the force
needed to crush Linwood's briquets ran up to 290 lbs (1290 N), compared
to the 156-246 lbs range typical of lime briquets.
Guided by the results of Anniston's evaluation, plus screen-fines
volume projections from Linwood and design considerations generally
associated with calcium oxide briquetting operations, Komarek proposed
a roll-press briquetter engineered to produce an oval-shaped 0.43
in3 / 6oz (7.1cc / 17g) briquet approximately 1-2/5" long,
7/8" wide and 9/16" thick (34.9 x 22.2 x 15.9mm), at throughputs
of up to 10,000 lbs (4,500 Kg) per hour.
The proposed mill, a variation of Komarek's Model B400 design,
forms briquets with two counter-rotating rolls, vertically opposed
and fed from one side by a horizontal infeed screw. Capable of roll
separation forces up to 120 tons, the B400 is a cantilevered design
with rolls mounted outside one end of the machine. This cantilevered
design allows quicker, easier roll changes, which Komarek recommended
because the abrasiveness of lime will require periodic replacement
of worn-out rolls.
In Linwood's briquetter, the rolls are 18" (457.2mm) in diameter
and 6" (152.4 mm) wide, with half-briquet cavities (pockets)
machined into their circumference faces. Each roll has three rows
of pockets across its face arranged in an offset, or staggered pattern,
with each row containing 60 pockets around the roll circumference.
Both rolls are synchronously driven by a single 100 hp / 75 KW electric
motor through a dual-output reducing gearbox. The rolls are indexed
so the pockets on opposing rolls match as the rolls turn, with upper
and lower halves closing to form whole briquet-shaped cavities as
they pass through the vertical centerline between rolls.
The horizontal infeed screw, independently driven by a 15 hp /11.25
KW motor delivers fines between the rolls at their "nip" region
(where the rolls come together), filling the roll pockets just prior
to closure. Horizontal infeed provides more consistent material
flow into the pockets than conventional gravity-feed systems, and
the Linwood machine's infeed screw drive has a variable-speed control
to allow fine-tuning of briquet density.
In this application, hydraulic pressure at 2,000 psi (13.8 MPa)
applies a roll separation force of 80 tons to achieve the prescribed
50,000 psi briquetting pressure as the pockets close while passing
through roll centerline to compress the material into a solid mass.
As each pocket advances beyond roll centerline, its two halves naturally
retreat, allowing the formed briquettes to drop out of the press
and slide down a chute onto a belt conveyor that delivers them to
a nearby 35-ton storage tank.
Because the briquetter is positioned outdoors, midway up an open-frame
104-ft. (32 m) tower, all parts of the system carrying either fines
or briquets are completely enclosed to protect the lime from being
ruined by environmental moisture.
Fines arrive at the briquetter's infeed hopper by gravity chute
from a 30-ton tank overhead, which is kept full by an inclined screw
(auger) conveyor that brings up a continuous flow of fines from
the kiln-output screen, and drops them into the briquetting supply
tank through an opening in the bottom of the conveyor trough. Like
the kilns, the conveyor runs continuously, so it is designed with
a simple but effective mechanism for automatic "overflow" protection
against the possibility that the briquetter might need to stop.
If the briquetter supply tank fills to the point where the fines
can no longer drop through, the fines simply continue moving up
to the end of the screw conveyor to a fines storage tank, where
they are held for sale to the various fines markets.
Standing next to the fines storage tank is a 500-ton silo-like
tank that receives pebble lime at the top, separately conveyed up
from the kiln screen, and empties at the bottom for drive-through
truck load-out.
The 35-ton storage tank that receives the briquets empties onto
a weigh-belt conveyor that feeds a "super-sack" loader
on ground level below, adjacent to the silo structure. Four other
storage tanks feed weigh-belt conveyors on the same deck that also
converge at the sack loader drop-chute, permitting measured amounts
of various customer-specified additives to be blended into 2-ton,
nylon-mesh bags along with the lime briquets. Mixtures are metered
according to blending programs stored in a proprietary computerized
control panel at the sack-loading station. "The bagged mixtures
are primarily for steelmaking customers," Jones says. "The
mills save time and money by simply dropping the entire bag into
the molten metal, instead of metering in the various ingredients
separately."
Linwood's briquetting operation is fully automated, Electrician
Mike Truninger explains. "The system starts and stops itself
by PLC control, triggered by briquet-level indicators in the bagging
storage tank. When the supply gets low, the PLC will start the equipment
in a backward sequence, first the transfer conveyor, then the briquetter
rolls, then the briquetter infeed screw and the vibrators in the
drop chutes that bring fines down to the briquetter. A control panel
on the briquetter deck allows manual override, but that's rarely
needed except for maintenance purposes."
Likewise, he adds, sensors in the briquetter supply tank will
stop the system if the level of fines gets too low, then start the
system again when the supply of fines is replenished.
"The entire lime plant operation is supervised from a central
control room," he continues. "There, four PCs display
various plant operations graphically, alert operators to any problems
and allow them to take appropriate actions. As long as everything
is running normally, no one has to worry about the briquetting system," he
says. "It runs itself."
Although Linwood's briquetter has the capacity to process more
fines than the new kiln typically produces, the machine currently
runs only about half of the time, says Plant Manager Jeff Dahl. "This
was intended to give us plenty of room for growth potential in bagged
orders. Right now, we're bagging only five days a week, but production
is running 'round the clock, seven days a week, with crews alternating
three- and four-day schedules of 12-hour shifts."
"Growth potential aside," he continues, "our primary
goal was to reduce the cost of waste. If 20 percent of our material
comes through as fines and gets dumped, then we're throwing away
20 percent of the cost of mining the stone, crushing, screening,
handling and calcining it. That makes those fines too valuable to
end up on a landfill. While capturing their value with briquetting
required a significant initial investment, we figure this system
paid for itself within a year or so."

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