Better Mixer Maintenance Ensures Cleaner Effluent at Smurfit-Stone
By
Patrick Grella paperloop.com
Posted 10-20-03
The pulping process at any mill involves large amounts
of water and generates significant process effluent. The
containerboard
mill operated by Smurfit-Stone Container Corp. in Stevenson,
Ala., is no exception. With environmental regulations becoming
increasingly strict, every link in the mill's effluent
treatment process is critical to returning water to the
Tennessee River
at the same quality level it was prior to intake.
| At the Stevenson, Ala., mill, a rebuilt mixer is installed
on one of 16 rafts, while the raft is held ashore by cables.
Once installed, the raft will be repositioned in the aerated
stabilization basin |
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At the Stevenson mill, mixers are used to agitate the effluent
and keep the organic solids in suspension. This action complements
the work of 13 low-speed fixed aerators and 17 high-speed
floating aerators in aerated stabilization basins (ASBs)
at the head of the mill's multi-stage secondary treatment
chain.
A preventive maintenance program adopted at the mill
has clearly improved the reliability of 16 raft-mounted
mixers that help
stimulate the biological treatment process removing organic
solids from process effluent. The proactive approach to maintaining
the mixers, utilizing factory-authorized service, has corrected
problems with the previously rebuilt units and delivered
significant savings to the mill.
WASTEWATER TREATMENT: NOW AND THEN. The mill produces approximately
2,400 tpd of containerboard (830,000 tpy) from recycled corrugated
stock and from virgin hardwood fiber subjected to the neutral
sulfite pulping process. Primary screening and clarification
remove the fiber and other settling solids in an onsite wastewater
treatment plant. The supporting infrastructure for the biological
treatment process now consists of a bar screen, two primary
and two secondary clarifiers, four ASBs, an activated sludge
unit (ASU), and three settling lagoons for final polishing.
Screw presses dewater the primary sludge, which is burned later
as boiler fuel.
The mill originated in 1974 with a 600-tpd capacity and a
4.2-mgd wastewater treatment capacity. At that time, the process
consisted of one primary and one secondary clarifier designed
to handle a biological oxygen demand (BOD) loading of 20,000
lb/day. The secondary clarifier effluent was designed for a
maximum overflow rate of 50 mg/l solids measured as total suspended
solids. The biological sludge off the secondary clarifier was
wasted to a 165,000-gal clarifier thickener before a belt press
dewatered the organic waste prior to disposal.
In 1998, the Stevenson mill increased its production capacity
to 2,400 tpd, leading to additional investment in the wastewater
treatment facilities. A second primary and secondary clarifier
increased the flow rate to 8.1 mgd. The ASBs remained the same
but received additional high-speed aerators and mixers, along
with a new gravity-fed 3.6-mgd ASU, an additional screw press
to process the primary sludge, and upgraded transfer piping.
After the upgrades, the effluent flow off the two secondary
clarifiers averaged approximately 620 mg/l, with a BOD loading
of 70,000 lb/day. In 2002, this resulted in 38 million gal
of secondary sludge off the thickener, 8 million gal of return
activated sludge, and 46 million additional gal cleaned from
the ASBs and effluent ponds.
| View of aerated stabilization basin No. 3 at the
Stevenson mill, with two mixer rafts and two high-speed
aerators in operation |
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MIXERS MAXIMIZE TREATMENT PROCESS. For the biological treatment
process to work at peak efficiency at the head of the multi-stage
treatment chain, the flow entering the four 22-mgd ASBs demanded
higher reliability from the mixers and aerators. Sixteen ITT
Flygt Model 4660 mixers, mounted aboard custom-made rafts by
Clark Technology Systems Inc., were installed in 1998 to help
with the circulation of wastewater throughout the ASBs.
Anchored at various points in each of the four ASBs, agitation
by the mixers, combined with the action of the aerators, maintain
the vitality of the biological process as it breaks down the
lignin, fibers, and other suspended solids in the effluent.
The process removes up to 80% of the organic solids during
this initial round of treatment before the effluent flows through
the ASU. The secondary treatment then removes another 70-90%
of any residuals.
By the time the 14- to 21-day process fully cycles, the 70,000
lb originally introduced into the ASBs have now been, on average,
reduced to less than 7,000 lb when the effluent exits the three
polishing ponds, says Bill Roddy, environmental manager at
the Stevenson mill.
"The mixers are important in maintaining the aerobic
process within our ASBs," explains Roddy. "We use
them as flow developers to reintroduce the liquid material
back into the aerators and heighten exposure to the biological
treatment process. We can raise and lower the mixers so that
the propeller angle keeps the solids from collecting and infilling
the bottom of the ASBs."
Concern arose, therefore, when the rebuilt mixers began failing
with increased frequency soon after their return from an outside
motor shop that repairs many different types of motors for
the Stevenson mill. It quickly became apparent that the shop
personnel responsible for rebuilding the mixers required specialized
training.
After the raft is pulled ashore and its mixer removed
for maintenance, a rebuilt replacement unit is ready for "drop-in" replacement,
minimizing costly downtime.
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STRENGTHENING LINKS WITH MAINTENANCE.
The importance of enacting a preventive maintenance program
for the mixers by a properly
trained repair source became apparent when many of the
rebuilt motors in the mixers failed before their projected
service
life, recounts Robert Sims, who manages a 10-member group
of electrical instrumentation (E&I) technicians at the
Stevenson mill.
"We had run the newly installed mixers in the ASBs for
more than two years without any maintenance program," he
said. "When a unit would fail, our people would send it
out to the designated motor repair shop just as we did with
the other equipment. The practice appeared to offer savings
but did more harm than good. That motor shop simply wasn't
trained in rebuilding the mixers and went about it totally
wrong."
The rash of recurring failures began impacting the mill's
E&I maintenance budget bottom line. A breakdown often required
four journeymen E&I technicians to take up to six hours
to put on safety equipment, launch a boat to pull the mixer
platform to the shoreline of the ASB, and then retrieve the
failed mixer with a heavy hoist. If the rebuilt unit was beyond
repair a second time, it took eight to 12 weeks to receive
a replacement. Meanwhile, the level of agitation sought in
the ASB was compromised while the unit was out of service.
"The replacement for nearly a dozen of the mixers exclusive
of man-hour costs eventually exceeded $150,000," Sims
describes.
The staff called in Jim House & Associates, an authorized
factory representative that had supplied the ITT Flygt mixers,
to help assess the problem and develop appropriate recommendations.
Working as a team with the mill, the supplier attributed the
unacceptable failure rate of the rebuilt mixers to improper
procedures followed by the motor shop and the absence of a
regularly scheduled preventive maintenance program, according
to Ed Swain, planner for power & recovery, E&I group,
at the mill.
Shore of aerated stabilization basin No. 3, which used
to be coated with settled solids, is no longer unsightly
and is relatively clean because of consistent mixer/ aerator
action.
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In order to provide greater agitation in the harsh environment
of the ASBs, the team installed propellers with a different
pitch and removed their jet rings (propeller shrouds) to
prevent limbs, wood, and other floating debris from jamming
the mixers and burning out the motors.
Under the preventive maintenance program now enacted for the
equipment, the mill pulls one mixer each month and immediately
substitutes it with a previously rebuilt unit that is kept
on site. The mixer that is pulled is sent off site to the factory
representative. In a disciplined sequence, factory-trained
technicians inspect the mixer, fully noting visible damage
or missing pieces. The equipment is then cleaned with a high-pressure
sprayer and inspected again for damage.
The cable is inspected next and tested for any possible electrical
shorts. If the shop technicians detect a short, they remove
and individually test the cable and stator windings. If the
stator itself reveals an electrical short, a specialized press
is used to remove and replace the watertight housing. The previous
motor shop had frequently cut the stator housings and then
welded them back together, often failing to achieve a watertight
seam. The mixer factory representative also discovered other
errors in how the previous motor shop had reassembled other
parts of the mixers.
Shop technicians for the factory representative also inspect
the integrity of the oil seal, including pressure testing the
units to 8 psi, before adding a precisely measured amount of
fresh lubricant. If any of these previous steps detect problems,
they disassemble the unit and compile a complete list of the
components and labor hours necessary to restore the mixer back
to factory standards. If the cost to rebuild and retest a unit
appears prohibitive, the mill replaces it with a new mixer
kept in stock at the factory representative's site, which is
a term in the agreement.
Since enacting the proactive program, all of the mixers at
the Stevenson mill have now gone through one and a half maintenance
cycles, resulting in greatly improved performance records. "The
more preventive maintenance you do, the less reactive work
you have to do later on," Sims says. "We've experienced
100% uptime since we adopted the preventive maintenance program
and gained the consistent reliability needed for the effluent
treatment process."
Patrick Grella is industrial market manager for ITT Flygt
Corp., Trumbull, Conn.
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