Technology Briefs
RECOVERY
OF A RECYCLABLE METAL ALLOY
FROM
HIGH SPEED STEEL GRINDING SWARF
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Key Words |
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Materials: Metal swarf from tool cutting. Technologies: Scrubbing and separation of swarf to recover metal alloy. Applications: Feedstock source for
smelters, tool manufacturers, and specialty steel producers. Abstract:
Develop a scrubbing and separation technology that would produce a
recyclable metal alloy acceptable as a feedstock source for smelters, tool
manufacturers or other consumers of steel.
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This project evaluated the feasibility of the
separation and subsequent recovery of usable steel alloy from grinding swarf
generated as a waste stream from high-speed tool cutting. The primary objective was to develop a
technology that would produce a recyclable metal alloy acceptable as a
feedstock source for smelters, tool manufacturers, or other consumers of
quality steel. Testing and process
development occurred at bench-scale level only; the process was not pilot
tested.
Background
Grinding swarf is a
significant by-product of tool cutting and other metal cutting
technologies. In many cases, swarf is
landfilled, although the metal constituents, oil, and filter media, if
separated, are valuable feedstock materials.
Depending on the cutting and grinding process and type of steel being
cut, residual swarf usually contains steel cuttings, filter media, coolant oil,
burr grit, phosphorus, and other potential contaminants.
The contaminants found in tool grinding swarf cause
technical problems in a remelt process.
Nonmetallics create undesired slag in the metal remelt process. Oil, if present above about 3%, can burn in
the melt. If the oil concentration is
too high, the oil can burn explosively.
Phosphorus, which is present in the cutting oil, typically remains on
the metal alloy particles as well, in levels greater than 0.03%. This level is unacceptable for recycling of
the metal in a smelter or other recovery alternative.
A meeting in August 1996, facilitated by the Center
for Waste Minimization (South Carolina), included three major cutting tool
manufacturers (CTM) and three high speed steel (HSS) producers. This group agreed on the makeup of the
recovered metals, including allowable contaminant levels, that would render the
material useable in their processes.
Those initial contaminant limitations (by weight percentage) were:
Oil Less than or equal to 5%
Nonmetallics Less than or equal to 14%
Phosphorus Less than or equal to 0.10%
Subsequently, the HSS producers stipulated a more
stringent set of target contaminant limitations (by weight percentage) on the
recovered metal:
Oil Less than or equal to 3%
Nonmetallics Less
than or equal to 5%
Phosphorus Less
than or equal to 0.03%
The 0.03% phosphorus limit is non-negotiable, and is
the maximum allowed for the accepted standard for all HSS grades, as stipulated
by the HSS producers and CTMs as buyers.
During the scope of the project, Timken-Latrobe, a
steel manufacturer that uses electric arc furnances to produce their products,
changed the nonmetallic limit to be less than or equal to 3%. This reduced level of allowable contaminants
requires significantly more scrubbing and separation effort than the original
limits of 5% oil, 14% nonmetallics and 0.1% phosphorus.
Under the scope of this project,
bench-scale process development and testing was conducted to optimize a process
design for removal of the higher-value steel cuttings from the swarf, for
reuse, in a pilot-scale separation. The
following parameters were optimized for scrubbing/washing, and separation of
the metal from the remaining constituents by various means:
Percent solids (pulp
density)
Surfactant type and add rate
Number of scrub cycles
Residence time in each
rubbing/washing cycle
Residence time for oil
settling and removal
Foaming reagent type and add
rate
Findings and Recommendations
The perlite-bearing swarf cleaned better than the
DE-bearing swarf using this scrubbing technology. The scrubbing and decanting sequence, through 11 cycles, provides
adequate oil removal for use of the scrubbed solids in Timken-Latrobe’s
processes. 76% of the contained oil was
easily removed during scrubbing and decanting, and may be clean enough for
alternative uses, such as cogeneration.
A magnetic separation technology, called wet high
intensity magnetic separation (WHIMS) produced an acceptable
notmetal removal efficiency in one sample. This, or another technology that produces
less than about 3% nonmetallics in the scrubbed solids is necessary to produce
a feed acceptable for remelt.
The phosphorus content of the samples analyzed
indicate that the level, at an average of 0.031%, is still too high for use by
HSS producers and CTM buyers. Attempts
to remove phosphorus below this level, such as pH alteration, were not successful.
Bench scale testing did not
produce enough clean metal cuttings for evaluation by Timken-Latrobe. They would require 25 tons of metal cuttings
to evaluate in a production furnaces.
Because the production of such a huge quantity of material was not possible
under this project scope, this usability evaluation could not take place.
Additional research is
necessary to develop an efficient pilot scale process, achieve the required
purity of the metal, and determine if the oil and filter media can be recovered
for alternative uses.
The markets for recovered swarf are somewhat
limited. Timken-Latrobe is one
potential buyer, however, since the aforementioned meeting, two of the major
HSS producers are no longer producing HSS in quantity for CTM consumption and
therefore are not viable markets. There
are a few specialty steel producers in the U.S. that may be interested in the
scrubbed swarf, especially since the alloy contains Molybdenum. Typically, 5% to 8% of HSS swarf is
molybdenum. Other HSS producers exist
in the foreign arena. The metal in the
swarf could likely be brokered to several manufacturers/producers overseas,
especially in countries when there is a solid metal working industrial base
(e.g., CTM customers) and specialty steel producer(s).
Report Date:
August 2000