In-line lin slush making for concrete cooling

Claim 2

A process for producing a flowable liquid-solid mixture comprising a continuous liquid phase and a discontinuous solid phase, the solid being discrete, frozen particles of the liquid, which process comprises flowing a stream of the liquid through a closed conduit, introducing a liquid cryogen into the flowing liquid stream so as to flow cocurrently therewith, whereby the liquid-solid mixture is formed, and discharging the mixture from the conduit, the temperature of the liquid stream into which the cryogen is introduced being established within the range from about 2° F. above the freezing point of the liquid to about 10° F. above the freezing point of the liquid, the contact time between introduction of the cryogen and discharge of the mixture being maintained from about 0.001 to about 10 seconds, the superficial velocity of the flowing liquid being at least about 1.5 feet per second, and the weight ratio of cryogen to liquid being maintained from about 0.05:1 to about 2:1.

Claim 3

The process of claim 1 wherein the contact time is from about 0.002 to about 9 seconds.

Claim 4

The process of claim 1 wherein the contact time is at least about 0.005 seconds.

Claim 5

The process of claim 1 wherein the superficial flow velocity is from about 2 to about 15 feet per second.

Claim 6

The process of claim 1 wherein the ratio of cryogen to liquid is at least about 0.1:1.

Claim 7

The process of claim 1 wherein the ratio of cryogen to liquid is at least about 0.2:1.

Claim 8

The process of claim 1 wherein the liquid is water, the cryogen is liquid nitrogen, the temperature of the liquid stream is less than about 40° F., the contact time is from about 0.005 to about 5 seconds, the superficial flow velocity is at least about 2.5 feet per second and the ratio of liquid nitrogen to water is at least about 0.2:1.

Claim 9

The process of claim 1 wherein the liquid is flowed at a rate from about 20 to about 200 gallons per minute and the cryogen is flowed at a rate from about 3 to about 100 gallons per minute.

Claim 10

An improved process for the production of concrete of reduced temperature which comprises obtaining in predetermined quantities the ingredients for making concrete including cement, sand, aggregate and water, cooling the water to a temperature in the range from about 34° to about 38° F., flowing the cooled water through a closed conduit, introducing a predetermined quantity of a cryogen into the flowing water so as to flow cocurrently therewith, whereby at least 10% by weight of the water is frozen to form a slush comprising a discontinuous ice phase within the flowing water, the cocurrent flow of cryogen and water being maintained from about 0.005 to about 2 seconds, the superficial velocity of the flowing water being at least about 3 feet per second, the weight ratio of cryogen to water being from about 0.2:1 to about 1:1, discharging the mixture from the conduit into a concrete mixing chamber, introducing the other predetermined quantities of ingredients into the concrete mixing chamber and mixing the slush and other ingredients to produce concrete of reduced temperature.

Claim 11

An improved process for the production of concrete of reduced temperature which comprises obtaining in predetermined quantities the ingredients for making concrete including cement, sand, aggregate and water, cooling the water to a temperature in the range from about 34° to about 38° F., flowing the cooled water through a closed conduit, introducing a predetermined quantity of a cryogen into the flowing water so as to flow cocurrently therewith, whereby at least 10% by weight of the water is frozen to form a slush comprising a discontinuous ice phase within the flowing water, the cocurrent flow of cryogen and water being maintained from about 0.005 to about 2 seconds, the superficial velocity of the flowing water being at least about 3 feet per second, the weight ratio of cryogen to water being from about 0.2:1 to about 1:1, discharging the mixture from the conduit into a concrete mixing chamber, introducing the other predetermined quantities of ingredients into the concrete mixing chamber and mixing the slush and other ingredients to produce concrete of reduced temperature.

Claim 12

The process of claim 9 wherein the cryogen is liquid nitrogen, the temperature of the cooled water being less than about 36° F. and the flow rate of the water being maintained in the range from about 30 to about 100 gallons per minute.