Method of treating and conditioning circulated rolling oil

Details Method of treating and conditioning circulated rolling oil Method of treating and conditioning circulated rolling oil

2000-02-09

2002-03-19

Hruskoci, Peter A. (Department: 1724)

Liquid purification or separation

Processes

Making an insoluble substance or accreting suspended...

C072S042000, C210S712000, C210S729000, C210S778000, C508S268000, C508S506000

Reexamination Certificate

active

06358423

ABSTRACT:

BACKGROUND OF THE INVENTION
1. Field of the Invention
This invention relates to a method for treating and conditioning circulated rolling oil, such as rolling oil for aluminum foil rolling mills. The method includes removing dirt and abrasion particles from the returned rolling oil by filtering the oil with controlled addition of auxiliary filtering media (filter aids), and adjusting conductivity to prevent electrostatic charging in the purified rolling oil.
2. The Prior Art
In the rolling of metal foils, rolling oil consisting of a mineral oil fraction with adequate thermal stability is normally used for cooling and lubricating. To reduce the consumption of rolling oil, the oil is usually circulated and continuously purified to an adequate degree and conditioned for reuse. The circulated rolling oil has contaminants that consist substantially of metallic particles from abrasion of the rolled stock, and their oxidation products. The rolling oil is usually cleaned in settling filters such as filter presses, where the abrasion and dirt particles are removed from the rolling oil to the greatest. possible extent.
To enhance the filtration process and in order to obtain a rolling oil that is as pure as possible, diatomaceous or bleaching earth is commonly added to the rolling oil as a filter aid prior to the filtration process. The separation efficiency of the settling filters is distinctly improved by such filtration aids. When conventional filter aids such as diatomaceous and bleaching earth are employed, additional amounts of filtration media are metered into each filtration cycle in addition to basic settling. Dirt particles are embedded in the porous volume of the auxiliary filtration media and their intermediate spaces, and gradually clog the free pores and ducts in the course of a filtration cycle. Since the filter cake is usually not loosened up or reflushed in the course of a current cycle, the relative porosity of the filter cake constantly decreases. Because the volume of the stream is maintained constant, this causes the difference in pressure above the filter cake to rise and the clarification sharpness to increase. The filtrate consequently becomes. cleaner and cleaner.
It is also known to employ a filter aid containing 50% cellulose fibers and 50% citric acid. This filter aid is quite effective. However, its mode of action can be controlled only with difficulty. The filter aid is settled on the filter fleece in the form of a filter cake. Since the interaction of the acid and the contaminants cause chemical effects when this medium is employed, the dwelling time of the participating components plays an important role. This dwelling time is relatively short, so that the mechanism acting in this purification process is relatively slow. Therefore, to obtain a high rate of reaction it is consequently necessary to add a large amount of acid to the filter cake.
For an enhanced separation of the finest of particles, a flocculating agent can be added as a filtering aid to the rolling oil prior to the filtration. The flocculating agent causes the finest particles to be agglomerated to larger agglomerates, so that the particles can be retained in the settling filter in a superior manner.
A substantial problem in the treatment and use of such rolling oils arises from the fact that in its initial state, and also in the purified state, the rolling oil has practically no electric conductivity, i.e. it is a good insulator. This poses the risk of electrostatic charging and the hazard of fire, explosion or deflagration in the rolling mill caused by discharge sparks, which could affect the treatment plants as well.
In order to prevent electrostatic charging, it is also known to admix adequate amounts of conductivity additives. with the rolling oil. These additives raise the conductivity of the rolling oil to such a degree that the electric charge potential addressed above cannot develop. However, such conductivity additives are hazardous to the environment and health, so that any admixing of such agents as a preventive “lump-sum” measure will cause high contamination loads on the environment as well as disposal problems.
SUMMARY OF THE INVENTION
It is therefore an object of the invention to provide a method for treating rolling oil in which the harmful conductivity additives can be omitted without increasing the hazards resulting from electric charging.
This and other objects are accomplished according to the invention by employing a flocculating agent as the filter aid, and controlling the amounts in which the agent is added depending on the residual contamination remaining in the filtrate, so that a preset minimum conductivity caused by the remaining residual contamination is kept preserved in the filtrate.
The invention is based on the idea that an adequate conductivity of the rolling oil can be obtained not only by adding conductivity additives but also by maintaining a sufficiently high residual contamination in the filtrate in a controlled manner, because the abrasion and dirt particles remaining in the rolling oil after the filtration can act just as effectively as a conductivity additive.
The residual contamination is adjusted sufficiently high to prevent electrostatic charging of the rolling oil, on the one hand, and sufficiently low to avoid the formation of stains on the rolled stock, on the other hand.
Diatomaceous or bleaching earth are not used as filter aids in the method according to the invention. Instead, the method according to the invention uses a flocculating agent, so that it is possible to increase the concentration of dirt in the filtrate, if required for control purposes, by reducing the amount of flocculating agent added accordingly. When diatomaceous or bleaching earth are employed as filter aids, the concentration of dirt in the. filtrate can only be reduced further, but not increased again without changing the filters. Likewise, if citric acid were used as filter aid as explained above, overdosing in the filter cake as required for the function could not be reduced again at a sufficiently high rate. Therefore, only the use of a flocculating agent as a filter aid according to the invention permits a controlled adjustment of the residual contamination.
In addition to raising the electric conductivity as explained above, the controlled adjustment of the residual contamination remaining in the rolling oil offers the advantage that superior grip is achieved between the rolls and the stock being rolled. Therefore, not only the electric but also the mechanical properties of the rolling oil are improved.
Finally, with the method according to the invention, the overall consumption of filter aids, i.e., flocculating agent in the present case—is clearly lower than with the methods according to the prior art because complete purity of the filtrate is intentionally waived.
The conductivity in the filtrate is usefully adjusted to values between k1=50 pS/m and k2=5000 pS/m and preferably to between k3=100 ps/m to k4=1000 pS/m, where pS/m=10
−12
/&OHgr;·m. It has been found that at these values, electrostatic charging of the rolling oil and thus fire, explosion or deflagation caused by such charging are reliably prevented. On the other hand, within this conductivity range, the residual contamination is so low that it will not interfere with the rolling process, and the grip between the surfaces of the rolls and the rolling stock is optimal.
Preferably a dicarbonic acid with the general formula
HOOC—A—COOH
is used as the flocculating agent, wherein A is a straight and branched chain of 5 to 15 carbon atoms, or phenylene. The method as defined by the invention works best with such a flocculating agent. Alternatively, of course, other flocculating agents can be employed for the method as defined by the invention as well.


REFERENCES:
patent: 5032303 (1991-07-01), Bondpä
patent: 5200086 (1993-04-01), Shah et al.
patent: 5973503 (1999-10-01), Kuipers

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