Abstract: A mixture of cooling liquids and solid pieces of waste from machine tools drop onto an inclined bottom wall of the upper, generally vertically disposed section of an inverted, generally Y-shaped feed chute. One of the two lower, diverging chute sections extends downwardly and rearwardly beneath the upper chute section to a chip wringer, and has its upper end positioned beneath the lower edge of the inclined bottom wall of the upper section to receive the liquids and lighter pieces of waste which tend to drop by gravity into this one lower section. The other lower section of the chute is in general alignment with the inclined bottom wall of the upper section to receive the larger pieces of waste which, because of their momentum or size pass beyond the one lower section and into the other lower section. A stream of air which is directed transversely across the lower end of the upper section blows the remaining liquids and light waste into the one lower section.

Abstract: A method of reducing the effects of fluctuating fluid pressure differential between the inlet and the outlet of a filtering unit operating in a system for filtering metal contaminants from a lubricating coolant and for recycling a constant volume flow of filtered lubricating coolant to a workpiece to be subsequently machined by pumping metal-contaminated lubricating coolant from a holding vessel to a filtering unit-modulator valve combination, monitoring the pressure or flow rate of filtered lubricating coolant downstream of the filtering unit-modulator valve combination, and operating the modulator valve in response to any changes in the downstream monitored flow parameter so as to maintain a predetermined constant fluid pressure differential across the filtering unit-modulator valve combination, thus compensating for fluctuations across the filtering unit during filtering operation, resulting in the maintenance of constant head pressure at the outlet of the pump, as well as for maintenance of a constant vol

Abstract: A plurality of filter housing are arranged around a hollow hub section the interior of which is divided into an inlet chamber for receiving fluid under pressure to be filtered, an outlet chamber for receiving filtered fluid, and a backwash chamber that is connected to a waste line. Each filter housing contains an inverted, frustoconically shaped filter element having a closed lower end, and an open upper end connected to the outlet chamber of the hub section. Fluid that is to be filtered normally flows from the inlet chamber through a first series of valves to the lower ends of the filter housings, and then radially inwardly through the walls of the filter elements and out of the upper ends thereof and through a second series of valves to the outlet chamber.

Abstract: A plurality of open trenches or sluices is suspended from the underside of the forming floor of a glass factory to register with the lower, discharge ends of hot gob reject or cullet chutes. Each sluice is suspended with one end higher than the other, and with their lower, discharge ends communicating with one end of a large quenching tank, which is mounted on the floor beneath the forming floor. The tank contains a supply of cooling water, which is continuously pumped to the upper ends of the sluices, so that as hot gobs drop from the chutes into the sluices they are immersed in the cooling water and travel by gravity with the cooling water downwardly in the sluices to the quenching tank. A conveyor in the tank transports the cullet through the cooling water to a discharge point adjacent the opposite end of the tank. The bottom of each sluice is generally V-shaped in configuration so that frictional engagement of the hot cullet with opposite sides of a sluice is minimized.

Abstract: In a system having a fluid filter that is automatically backwashed each time the differential pressure thereacross reaches a predetermined value, the desired base rate at which the drop across the filter should increase during its initial filtering sequence (i.e., before backwash) is determined and stored in digital format in a process controller along with a preset maximum differential pressure at which backwash is set to occur. During use of the filter the actual rate of change of the pressure drop thereacross is monitored continuously and compared with the rate that is stored in the controller. Whenever the actual rate of change of the pressure drop across the filter differs from the base rate, which is the usual case, the present backwashing pressure is automatically adjusted--usually downwardly. This reduction continues until the actual drop across the filter finally reaches the adjusted value of the preset backwashing pressure, at which time backwashing of the filter is automatically commenced.