Process for removing oil from metal chips

Claim 2

A process for removing oil from metal chips with an aqueous stream comprising disposing a bed of metal chips coated with oil within a pressure vessel provided with inlet conduit means and discharge opening means, passing through said inlet conduit means a continuous stream of liquid feed water at a superatmospheric pressure sufficiently high to maintain the water in said inlet conduit means substantially in the liquid phase, passing said stream of water into said vessel and through said bed of metal chips, the temperature and velocity of the water being sufficiently high to remove oil from the chips without substantial vaporization of said oil or said liquid water, maintaining a superatmospheric pressure within said vessel, said oil being removed from said chips and forming an oil-water mixture, and continously removing said oil-water mixture from said vessel through said discharge opening means.

Claim 3

The process of claim 1 wherein the water in said inlet conduit means and said pressure vessel is substantially entirely in the liquid phase.

Claim 4

A process for removing oil from metal chips with an aqueous stream comprising disposing a bed of metal chips coated with oil within a pressure vessel provided with liquid water inlet conduit means and aqueous liquid-vapor discharge opening means, passing through said inlet conduit means a continuous stream of liquid feed water at a pressure sufficiently high to maintain the water in said inlet conduit means substantially in the liquid phase, passing said stream of water into said vessel and through said bed of metal chips, the temperature of the water being sufficiently high to remove oil from said chips without substantial vaporization of said oil, an amount up to 50 weight percent of the liquid water in said inlet conduit means being vaporized during passage from said inlet conduit means and through said bed of chips, said vaporization causing the density of the aqueous stream at said bed of metal chips to be less than 50 percent of the density of the liquid water in said inlet conduit means, said oil being removed from said chips and forming an oil-water mixture, and removing water vapor and said oil-water mixture from said vessel through said discharge opening means.

Claim 5

A process for removing oil from metal chips with an aqueous stream comprising disposing a bed of metal chips coated with oil within a pressure vessel provided with liquid water inlet conduit means and aqueous liquid-vapor discharge opening means, passing through said inlet conduit means a continuous stream of liquid feed water at a pressure sufficiently high to maintain the water in said inlet conduit means substantially in the liquid phase, passing said stream of water into said vessel and through said bed of metal chips, the temperature of the water being sufficiently high to remove oil from said chips without substantial vaporization of said oil, an amount up to 50 weight percent of the liquid water in said inlet conduit means being vaporized during passage from said inlet conduit means and through said bed of chips, said vaporization causing the density of the aqueous stream at said bed of metal chips to be less than 50 percent of the density of the liquid water in said inlet conduit means, said oil being removed from said chips and forming an oil-water mixture, and removing water vapor and said oil-water mixture from said vessel through said discharge opening means.

Claim 6

The process of claim 3 wherein a superatmospheric pressure is maintained throughout said vessel.

Claim 7

The process of claim 3 wherein the stream of water in said inlet conduit means is substantially entirely in the liquid phase.

Claim 8

The process of claim 3 wherein said vaporization causes the density of said aqueous stream to decrease from a level above 50 lbs/ft 3 to a level below 20 lbs/ft 3 .

Claim 9

The process of claim 3 wherein said vaporization causes the density of said aqueous stream to decrease from a level above 50 lbs/ft 3 to a level below 10 lbs/ft 3 .

Claim 10

The process of claim 3 wherein the ratio of the pressure outside said discharge opening means to the pressure inside said discharge opening means is no more than 0.7.

Claim 11

The process of claim 3 wherein the ratio of the pressure outside said discharge opening means to the pressure inside said discharge opening means is no more than 0.6.

Claim 12

The process of claim 3 which is essentially adiabatic.

Claim 13

The process of claim 3 including vacuum inducing means to lower the pressure outside said discharge opening means.

Claim 14

The process of claim 3 including a chip preheating step wherein the chips are preheated prior to said process.

Claim 15

The process of claim 12 wherein the chips are preheated with hot water.

Claim 16

The process of claim 12 wherein the chips are preheated with heated air.

Claim 17

The process of claim 12 wherein the chips are preheated with steam.

Claim 18

The process of claim 3 including a chip drying step at the end of said process.

Claim 19

The process of claim 16 wherein the chips are dried with a stream of air.

Claim 20

The process of claim 3 wherein the water in said inlet conduit means is at a temperature of at least 250° F.

Claim 21

The process of claim 3 wherein the water in said inlet conduit means is at a temperature of at least 300° F.

Claim 22

The process of claim 3 wherein the water in said inlet conduit means is at a temperature of at least 325° F.

Claim 23

The process of claim 3 wherein less than 10 weight percent of the water in said inlet conduit means vaporizes during said vaporization.

Claim 24

The process of claim 3 wherein less than 15 weight percent of the water in said inlet conduit means vaporizes during said vaporization.

Claim 25

The process of claim 3 wherein less than 20 weight percent of water in said inlet conduit means vaporizes during said vaporization.

Claim 26

The process of claim 3 wherein the density of the aqueous stream at said bed of metal chips is less than 10 percent of the density of the liquid water in said inlet conduit means.

Claim 27

The process of claim 3 wherein the density of the aqueous stream at said bed of metal chips is less than 5 percent of the density of the liquid water in said inlet conduit means.

Claim 28

The process of claim 3 wherein the pressure outside said discharge opening means is atmospheric and the pressure immediately inside said discharge opening means is not greater than 1.83 atmospheres.

Claim 29

The process of claim 3 wherein said water vapor and said oil-water mixture removed from said vessel are passed to an oil-water receiver, condensing said water vapor in said receiver and pumping an oil-water mixture from said receiver.

Claim 30

The process of claim 27 wherein the pumped oil-water mixture is pumped by means of a constant displacement pump to draw a vacuum in said receiver.

Claim 31

The process of claim 27 wherein said pumped oil-water mixture is pumped to an oil-water separator, and removing separate oil and water streams from said separator.

Claim 32

The process of claim 29 wherein said separate water stream is passed through coil means in said receiver to remove heat and condense water vapor therein.

Claim 33

The process of claim 29 wherein said separate water stream is passed to a hot water heater where it is reheated and then recycled to said pressure vessel containing metal chips.

Claim 34

The process of claim 3 wherein said vaporization is performed at substantially constant enthalpy.

Claim 35

The process of claim 3 wherein said liquid feed water is saturated.

Claim 36

The process of claim 3 wherein said liquid feed water is subcooled.

Claim 37

The process of claim 3 wherein the chips in said bed move continuously through said vessel.

Claim 38

The process of claim 35 wherein said chips move cocurrently with respect to said aqueous stream.

Claim 39

The process of claim 35 wherein said chips move countercurrently with respect to said aqueous stream.