US2259841A - Refrigerant and method of provdj - Google Patents

Refrigerant and method of provdj Download PDF

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US2259841A
US2259841A US2259841DA US2259841A US 2259841 A US2259841 A US 2259841A US 2259841D A US2259841D A US 2259841DA US 2259841 A US2259841 A US 2259841A
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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K5/00Heat-transfer, heat-exchange or heat-storage materials, e.g. refrigerants; Materials for the production of heat or cold by chemical reactions other than by combustion
    • C09K5/02Materials undergoing a change of physical state when used
    • C09K5/06Materials undergoing a change of physical state when used the change of state being from liquid to solid or vice versa
    • C09K5/063Materials absorbing or liberating heat during crystallisation; Heat storage materials
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25CPRODUCING, WORKING OR HANDLING ICE
    • F25C1/00Producing ice
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25CPRODUCING, WORKING OR HANDLING ICE
    • F25C1/00Producing ice
    • F25C1/12Producing ice by freezing water on cooled surfaces, e.g. to form slabs
    • F25C1/14Producing ice by freezing water on cooled surfaces, e.g. to form slabs to form thin sheets which are removed by scraping or wedging, e.g. in the form of flakes

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  • My invention relates to a refrigerant which is suitable for use in a produce package and to a way of providing such refrigerant.
  • Lettuce heads fresh from the growing field customarily are packed in crates containing a predetermined number of lettuce heads and an amount of crushed water-ice to reduce the temperature of the lettuce heads and to keep their temperature reduced during transit and storage,
  • the dimensions of the crate and of the lettuce heads are such that the lettuce heads are compressed within the package when the enclosure is completed.
  • Lettuce has the characteristic of being rather easily bruised mechanicall and, when bruised, of exuding a milky liquid which, upon contact with air, turns brown.
  • the general practice still is to place the lettuce heads in crates, to crush large blocks of water-ice into relatively small size, sometimes screening the ice and sometimes using it just as it comes from the crusher, then to pack the ice in with the lettuce heads and close the crate under pressure.
  • This crushed water-ice is a mass of particles which, when closely examined, are seen to have very sharp edges and piercing points. These are not lost as the ice is kept in mass prior to use and are most efficient in piercing the lettuce, cutting it and otherwise initially bruising it so that exudation and resultant oxidation ensue.
  • I therefore at first attempted to substitute a ball mill and screening devices, believing that if the ice were hammered or differently crushed and were separated into exceedingly small particles the dimculty would be overcome. Such was not the case, however. since the sharp edges of the small particles, although not effective to penetrate as deeply as large pieces of sharp ice, nevertheless bruise the leaves and in many cases perforate them in a greater number of places. No feasible change in the crushing or screening arrangement appeared to make any improvement.
  • a Vilter "Pak-Ice machine manufactured by the Vilter Company, of Milwaukee, Wisconsin.
  • This machine includes a jacketed chamber or cylinder within which are rotating helical knives. A refrigerant is recirculated through the jacket to maintain a low temperature within the cylinder, and water is introduced into the jacketed cylinder and immediatel turns into a snow-like mass. This mass is scraped from the chamber walls and is expelled from the cylinder into a briquetting device which compresses the mass into briquettes or blocks of snow-ice. These briquettes or blocks or snow-ice normally are commercially utilized as a substitute for artificial water-ice.
  • I then mixed the water crystals, after they had been separated from the brine, with fresh water of a higher temperature and permitted the intermixturc to continue until such time as the water crystals were of a temperature of substantially 31.8 Fahrenheit. This temperature is not injurious to lettuce, and the warmed or tempered crystals are not otherwise affected.
  • the package is made by introducing lettuce into a crate and surrounding it immediately with the tempered and separated water crystals, and the crate is then closed under pressure.
  • a machine 6 having the characteristics of a Vilter "Pair-Ice” machine, there being an interior chamber 1 the jacket 8 of which is provided with recirculating refrigerant 9 from a refrigerating machine ll. Within the chamber 1 are rotating. helical blades [3. Into the inlet ll of the machine is introduced a stream of water to which is added an appropriate amount of a salt. usually sodium chloride, although other salts such alum are effective. A representative amount of sodium chloride is 750 lbs. for each 1000 calls. of water in the circuit. This makes what may be termed a light brine, which, when introduced into the chamber 1, causes the deposition on the walls thereof of pure, non-saline water crystals which leave behind a somewhat more concentrated brine. The water crystals are discreet, non-cohesive particles about 4 of an inch in diameter and are devoid of sharp edges or points.
  • a salt usually sodium chloride, although other salts such alum are effective.
  • a representative amount of sodium chloride is 750 lbs
  • the crystals are scraped from the walls of the chamber 1 by the blades l3 and are discharged, together with the brine, through an outlet pipe l8.
  • the outlet about to of the material is water crystals, while the remaining amount is a somewhat concentrated brine, so that the entire mass is fluid and can readily be pumped from the Vilter machine 6 to a separating tank 2
  • the tank 2i is open at the top and is of sufficient dimensions, preferably, that the material therein is relatively quiescent. Since this is the case, the water crystals, having a lesser specific gravity than the accompanying brine, rise to the surface of the liquid within the tank 2
  • the brine, somewhat concentrated is removed from the tank 2i through an outlet 22 and is'returned through a pipe 23 which joins the inlet l4, so that the brine is recirculated.
  • the supernatant water crystals are removed from the tank 2
  • the crystals moving on the conveyor 24 are substantially pure water crystals, but a small amount of salt is carried over with them in the adhering brine. The amount is entirely negligible in commercial operation and is an exceedingly small fraction of one per cent of all of the salt utilized in the process.
  • the temperature of the crystals on the conveyor 24 ranges between 29 and 31 degrees Fahrenheit. Since there is practically no brine adhering to the crystals, their temperature begins to approach 32 degrees, and if fresh water at 32 degrees is added, a very close approximation of this temperature is obtained, all of which is quite satisfactory. But the tap water ordinarily available is warmer, ranging through to degrees Fahrenheit, and hence there is introduced into the tank 26, along with the crystals from the conveyor 24', an amount of relatively warm fresh Water through a conduit 21, the water and crystals being intimately admixed by an agitator 2B driven by an electric motor 29. Some washing of the adhering brine from the crystals occurs.
  • This intcrmixturc is carried on in such a Way as to provide a resulting slush of water and discreet artificial ice or snow particles and in such a Way that the temperature of the water crystals is changed, either a small amount or a relatively large amount but, for use with lettuce, being raised until it is substantially 31.8 degrees Fahrenheit.
  • the tempered slush is pumped through a conduit 3
  • the conduit 3! discharges the tempered slush into a separator 32 which conveniently includes a tank having :i perforated partition 33 extending thcrcacross. of such a nature that the terntures such as the pered water crystals are retained and supported thereon in a pile 34 available for use in packaging.
  • This pile has the appearance of a pile of very fine soapsuds or of cotton'y material.
  • has acquired a very small salt content and drains through the partition 33 into a sump 36 from whence it is withdrawn through a conduit 31 and is discharged through a pipe 39 into the pipe 23, therein admixing with the returning brine from the pipe 22 on the way to the inlet l4. Since this returning liquid is made up of the somewhat concentrated brine and virtually fresh water, it may be necessary to add a little make-up salt to maintain the preferred brine concentration, and hence the salt addition mechanism I6 is operated to maintain the proportions described.
  • the tempered water crystals in the pile 34 can be utilized in the immediate packaging of lettuce or comparable produce. 1 have found it advisable in commercial practice not to have a very large pile 3d of water crystals available at any one time, but I prefer to have two strucseparator 32 from one of which the water crystals are utilized while the other one is being filled with slush and the carrying water is being drained therefrom. If about a tenor fifteen-minute supply is provided in each of the two structures, and the supplies are alternately used and replenished, an entirely satisfactory result is obtained.
  • a package of lettuce containing water crystals. as described, is maintained at substantially 31.8 degrees temperature throughout the entire melt ing time of the crystals.
  • the particles, being so small, are of virtually uniform temperature entirely therethrough, and this temperature can be established at virtually any selected level.
  • the blocks are usually in 300-lb. sizes and are held for protracted periods in cold storage at temperatures around 25 or 26 degrees Fahrenheit. Then, when the blocks are removed from storage and crushed, the surface of the crushed particles may fairly rapidly attain a temperature of 32 degrees, but the interior thereof remains much lower. Since 31.? or 31.8 degrees is a safe shipping temperature for lettuce but 31.4 or 31.5 degrees will freeze the lettuce, it often results that after packing with crushed of the lettuce drops far below a safe shipping temperature and freezing of the lettuce occurs.
  • a method of providing a refrigerant comprising freezlng water crystals from brine in contact with chamber walls at a freezing temperature, discharging said crystals and said brine from said chamber, separating said water crystals from said brine, and increasing the temperature of said separated Water crystals to a temperature just below the melting temperature of water.
  • a method of providing a refrigerant comprising freezing water crystals from a light brine having a selected concentration, separating said water crystals from said brine, mixing said crystals and fresh water, separating said crystals from said fresh water, mixing said separated fresh water and said separated brine, adding salt to said mixture to reestablish said selected concentration, and repeating the process using said mixture.
  • a method of providing a refrigerant comprising freezing water crystals from a light brine, separating said crystals from said brine, and changing the temperature of said separated crystals while keeping said temperature below 32 degrees Fahrenheit.
  • a refrigerant comprising water crystals which have been frozen from and carry a trace of a light brine, which are about three-thouandths of an inch in diameter, which are discreet, non-cohering particles, and which in mass feel soft and not sharp to the touch.
  • a refrigerant comprising artificially manufactured water crystals which carry a trace of salt, which are about three-thousandths of an inch in diameter and which in mass are non-cohesive and feel soft to the touch.
  • a refrigerant comprising artificially manufactured water crystals which carry a trace of salt and which are substantially non-cohesive and devoid of sharp edges or points.
  • a refrigerant comprising artificially manufactured ice particles which carry a. trace of salt and which at atmospheric pressure are discreet. smooth particles approximately three-thou- 'sandths of an inch in diameter.
  • a method of providing a refrigerant comprising providing a light brine, freezing water crystals from said brine, separating said crystals from said brine. then augmenting said brine by adding fresh water to said brine, then freezing additional water crystals from said augmented brine, separating said additional crystals from said augmented brine, and adding said additional separated crystals to said separated crystals thereby forming a refrigerant.

Description

Oct. 21, 1941. E. H. SPIEGL REFRIGERANT AND METHOD OF PROVIDING Filed July 5, 1959 THE SAME INVENTOR ELL/i H- JP/EGL ATTORNEY Patented Oct. 21, 1941 REFRIGERANT AND METHOD OF PROVID- ING THE SAME Ellis H. Splegl, Salinas, Calif.
Application July 5, 1939, Serial No. 282,874
9 Claims.
My invention relates to a refrigerant which is suitable for use in a produce package and to a way of providing such refrigerant.
While the scope of my invention is to be limited only by the claims, one example of it can be considered as it has been developed in connection with the packaging of lettuce. Lettuce heads fresh from the growing field customarily are packed in crates containing a predetermined number of lettuce heads and an amount of crushed water-ice to reduce the temperature of the lettuce heads and to keep their temperature reduced during transit and storage, The dimensions of the crate and of the lettuce heads are such that the lettuce heads are compressed within the package when the enclosure is completed. Lettuce has the characteristic of being rather easily bruised mechanicall and, when bruised, of exuding a milky liquid which, upon contact with air, turns brown. Not only is the lettuce actually so damaged, but its appearance is adversely affected; so that a serious commercial problem exists in refrigerating lettuce and yet minimizing adverse effects upon its condition and appearance. Many solutions of this problem have been attempted, some of them of some value and others of no value, but in the main the problem still exists. Some of the solutions have involved wrapping each individual head of lettuce in some sort of an envelope or container, but this not only is expensive but reduces the effect of the refrigerant. I myself have, as shown in my CD- pending application Serial No. 246,661, filed December 19, 1938, entitled Lettuce pack and method of packing lettuce, endeavored to prevent the appearance of damage by largely eliminating contact between the lettuce and the atmosphere so that oxidation does not occur. Nev ertheless. the general practice still is to place the lettuce heads in crates, to crush large blocks of water-ice into relatively small size, sometimes screening the ice and sometimes using it just as it comes from the crusher, then to pack the ice in with the lettuce heads and close the crate under pressure.
It is an object, of my invention to improve considerably upon the stated standard practice.
In the drawing the figure i a diagrammatic representation of my invention.
After a very extensive experience in packaging hundreds of thousands of crates of lettuce and in trying virtually all of the commercially available manners of packaging represented in the patent literature and otherwise, it occurred to me that ill the source of a major part of the trouble was the character of the crushed ice.
This crushed water-ice, as it results from the ordinary crushing mechanisms, is a mass of particles which, when closely examined, are seen to have very sharp edges and piercing points. These are not lost as the ice is kept in mass prior to use and are most efficient in piercing the lettuce, cutting it and otherwise initially bruising it so that exudation and resultant oxidation ensue. For the ordinary crushing machines I therefore at first attempted to substitute a ball mill and screening devices, believing that if the ice were hammered or differently crushed and were separated into exceedingly small particles the dimculty would be overcome. Such was not the case, however. since the sharp edges of the small particles, although not effective to penetrate as deeply as large pieces of sharp ice, nevertheless bruise the leaves and in many cases perforate them in a greater number of places. No feasible change in the crushing or screening arrangement appeared to make any improvement.
I then endeavored to utilize an intermediate product produced by a Vilter "Pak-Ice machine, manufactured by the Vilter Company, of Milwaukee, Wisconsin. This machine includes a jacketed chamber or cylinder within which are rotating helical knives. A refrigerant is recirculated through the jacket to maintain a low temperature within the cylinder, and water is introduced into the jacketed cylinder and immediatel turns into a snow-like mass. This mass is scraped from the chamber walls and is expelled from the cylinder into a briquetting device which compresses the mass into briquettes or blocks of snow-ice. These briquettes or blocks or snow-ice normally are commercially utilized as a substitute for artificial water-ice.
I attempted to utilize the snow-like product which is expelled immediately from the cylinder, taking it before it went into the briquetting device, but I found that such product is useless for packing purposes since the particles are tenaciously cohesive and, while excellent for briquetting form otherwise such a tenacious, rubbery mass as to be commercially unusable. Then, after a great deal of further experimenting, I found that by adding salt to the water entering the Vilter machine and therefore making a light brine. the machine would furnish discreet water crystals of approximately 33 of an inch diameter, which were smooth and relatively round and hence very satisfactory, and, further, which were substantially noncohcsive and hence distinctly usable in the packaging operations.
As an interesting indication that these discreet particles are distinctly different from those furnished by the machine when operated upon ordinary water, it is found that when the discreet particles removed from the brine are put in the briquetting attachment they do not form briquettes. Upon analysis, the water crystals separated from the brine are substantially pure water, there being only an infinitesimal amount of brine adhering thereto. The remaining or separated brine is, of course, somewhat more concentrated after the crystals of water have been removed therefrom.
But a practical trial of such water crystals removed from the brine as a packing refrigerant was unsatisfactory, since lettuce is readily frozen, and the temperature of the separated water crystals ranges from substantially 29 to about 31 Fahrenheit, depending somewhat upon the concentration of the brine and other factors in the freezing operation.
I then mixed the water crystals, after they had been separated from the brine, with fresh water of a higher temperature and permitted the intermixturc to continue until such time as the water crystals were of a temperature of substantially 31.8 Fahrenheit. This temperature is not injurious to lettuce, and the warmed or tempered crystals are not otherwise affected. The package is made by introducing lettuce into a crate and surrounding it immediately with the tempered and separated water crystals, and the crate is then closed under pressure.
It has been found, as a practical matter, that the refrigeration qualities of the package are considerably enhanced over standard practice and that there is no mechanical injury whatsoever to the lettuce, since the water crystals are devoid of points or sharp edges and hence do not in any wise mechanically injure the produce. As a convincing test of this, a mass of the separated water crystals, when held in the hand and squeezed. feels perfectly soft to the touch, whereas a comparable mass of crushed ice particles, when held in the hand and squeezed, is sharp and unpleasant. The difference in sensation so far as the touch is concerned is very much like the difference between grasping and squeezing a mass of cotton and grasping and squeezing a mass of crushed pebbles. The col:- ton analogy is further of interest in that a large pile of separated ice crystals looks very much like a pile of loose cotton or is somewhat suggestive of a mass of fine soapy lather. In effect, therefore. I have provided a refrigerant which has at least all of the cooling properties of crushed watcr ice but which is devoid of injurious points or edges and in effect provides a cotton-like surrounding or packing for the produce.
In a typical commercial installation, there is.
provided a machine 6 having the characteristics of a Vilter "Pair-Ice" machine, there being an interior chamber 1 the jacket 8 of which is provided with recirculating refrigerant 9 from a refrigerating machine ll. Within the chamber 1 are rotating. helical blades [3. Into the inlet ll of the machine is introduced a stream of water to which is added an appropriate amount of a salt. usually sodium chloride, although other salts such alum are effective. A representative amount of sodium chloride is 750 lbs. for each 1000 calls. of water in the circuit. This makes what may be termed a light brine, which, when introduced into the chamber 1, causes the deposition on the walls thereof of pure, non-saline water crystals which leave behind a somewhat more concentrated brine. The water crystals are discreet, non-cohesive particles about 4 of an inch in diameter and are devoid of sharp edges or points.
The crystals are scraped from the walls of the chamber 1 by the blades l3 and are discharged, together with the brine, through an outlet pipe l8. In the outlet about to of the material is water crystals, while the remaining amount is a somewhat concentrated brine, so that the entire mass is fluid and can readily be pumped from the Vilter machine 6 to a separating tank 2| into which the fluid mixture is discharged. The tank 2i is open at the top and is of sufficient dimensions, preferably, that the material therein is relatively quiescent. Since this is the case, the water crystals, having a lesser specific gravity than the accompanying brine, rise to the surface of the liquid within the tank 2|, thereby effectuating a Stratification or segregation of the two components. The brine, somewhat concentrated, is removed from the tank 2i through an outlet 22 and is'returned through a pipe 23 which joins the inlet l4, so that the brine is recirculated.
The supernatant water crystals are removed from the tank 2| bya conveyor 24 or other suitable device and are deposited in an open tank 26 for tempering. The crystals moving on the conveyor 24 are substantially pure water crystals, but a small amount of salt is carried over with them in the adhering brine. The amount is entirely negligible in commercial operation and is an exceedingly small fraction of one per cent of all of the salt utilized in the process.
But the temperature of the crystals on the conveyor 24 ranges between 29 and 31 degrees Fahrenheit. Since there is practically no brine adhering to the crystals, their temperature begins to approach 32 degrees, and if fresh water at 32 degrees is added, a very close approximation of this temperature is obtained, all of which is quite satisfactory. But the tap water ordinarily available is warmer, ranging through to degrees Fahrenheit, and hence there is introduced into the tank 26, along with the crystals from the conveyor 24', an amount of relatively warm fresh Water through a conduit 21, the water and crystals being intimately admixed by an agitator 2B driven by an electric motor 29. Some washing of the adhering brine from the crystals occurs. This intcrmixturc is carried on in such a Way as to provide a resulting slush of water and discreet artificial ice or snow particles and in such a Way that the temperature of the water crystals is changed, either a small amount or a relatively large amount but, for use with lettuce, being raised until it is substantially 31.8 degrees Fahrenheit.
From the tank 26 the tempered slush is pumped through a conduit 3| to any convenient point. preferably vcry closely adjacent the point of use since the temperature of a mass of the Water crystals cannot be expected to be maintained when part of the mass is exposed to the atmoshcre [or more than fifteen or twenty minutes. The conduit 3! discharges the tempered slush into a separator 32 which conveniently includes a tank having :i perforated partition 33 extending thcrcacross. of such a nature that the terntures such as the pered water crystals are retained and supported thereon in a pile 34 available for use in packaging. This pile has the appearance of a pile of very fine soapsuds or of cotton'y material.
The water component of the slush as it has been pumped through the conduit 3| has acquired a very small salt content and drains through the partition 33 into a sump 36 from whence it is withdrawn through a conduit 31 and is discharged through a pipe 39 into the pipe 23, therein admixing with the returning brine from the pipe 22 on the way to the inlet l4. Since this returning liquid is made up of the somewhat concentrated brine and virtually fresh water, it may be necessary to add a little make-up salt to maintain the preferred brine concentration, and hence the salt addition mechanism I6 is operated to maintain the proportions described.
The tempered water crystals in the pile 34 can be utilized in the immediate packaging of lettuce or comparable produce. 1 have found it advisable in commercial practice not to have a very large pile 3d of water crystals available at any one time, but I prefer to have two strucseparator 32 from one of which the water crystals are utilized while the other one is being filled with slush and the carrying water is being drained therefrom. If about a tenor fifteen-minute supply is provided in each of the two structures, and the supplies are alternately used and replenished, an entirely satisfactory result is obtained.
A package of lettuce containing water crystals. as described, is maintained at substantially 31.8 degrees temperature throughout the entire melt ing time of the crystals. The particles, being so small, are of virtually uniform temperature entirely therethrough, and this temperature can be established at virtually any selected level. During the entire shipping period, a number of days. the lettuce is uniformly held at a constant temperature and hence arrives at market in optimum condition. This is in great distinction to the result with crushed block ice. The blocks are usually in 300-lb. sizes and are held for protracted periods in cold storage at temperatures around 25 or 26 degrees Fahrenheit. Then, when the blocks are removed from storage and crushed, the surface of the crushed particles may fairly rapidly attain a temperature of 32 degrees, but the interior thereof remains much lower. Since 31.? or 31.8 degrees is a safe shipping temperature for lettuce but 31.4 or 31.5 degrees will freeze the lettuce, it often results that after packing with crushed of the lettuce drops far below a safe shipping temperature and freezing of the lettuce occurs.
But with the water crystals the temperatures of manufacture and use are susceptible of such close control, and the temperature variation within a single crystal is so small, that satisfactory packing and shipping temperatures are readily obtained and maintained.
I claim:
1. A method of providing a refrigerant, comwater ice the temperature prising subjecting a light brine to a freezing temperature to deposit crystals having a temperature in the neighborhood of 30 degrees Fahrenheit, separating said crystals from said brine, mixing said crystals with fresh water of a higher temperature in the neighborhood of 40 to 60 degrees Fahrenheit, and separating said water from said crystals to leave said crystals as a refrigerant.
2. A method of providing a refrigerant, comprising freezlng water crystals from brine in contact with chamber walls at a freezing temperature, discharging said crystals and said brine from said chamber, separating said water crystals from said brine, and increasing the temperature of said separated Water crystals to a temperature just below the melting temperature of water.
3. A method of providing a refrigerant, comprising freezing water crystals from a light brine having a selected concentration, separating said water crystals from said brine, mixing said crystals and fresh water, separating said crystals from said fresh water, mixing said separated fresh water and said separated brine, adding salt to said mixture to reestablish said selected concentration, and repeating the process using said mixture.
4. A method of providing a refrigerant, comprising freezing water crystals from a light brine, separating said crystals from said brine, and changing the temperature of said separated crystals while keeping said temperature below 32 degrees Fahrenheit.
5. A refrigerant comprising water crystals which have been frozen from and carry a trace of a light brine, which are about three-thouandths of an inch in diameter, which are discreet, non-cohering particles, and which in mass feel soft and not sharp to the touch.
6. A refrigerant comprising artificially manufactured water crystals which carry a trace of salt, which are about three-thousandths of an inch in diameter and which in mass are non-cohesive and feel soft to the touch.
7. A refrigerant comprising artificially manufactured water crystals which carry a trace of salt and which are substantially non-cohesive and devoid of sharp edges or points.
8. A refrigerant comprising artificially manufactured ice particles which carry a. trace of salt and which at atmospheric pressure are discreet. smooth particles approximately three-thou- 'sandths of an inch in diameter.
9. A method of providing a refrigerant comprising providing a light brine, freezing water crystals from said brine, separating said crystals from said brine. then augmenting said brine by adding fresh water to said brine, then freezing additional water crystals from said augmented brine, separating said additional crystals from said augmented brine, and adding said additional separated crystals to said separated crystals thereby forming a refrigerant.
ELLIS H. SPIEGL.
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Cited By (31)

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US2418746A (en) * 1941-09-27 1947-04-08 Texas Res Corp Food freezing machine
US2706385A (en) * 1951-11-19 1955-04-19 Frank W Topping Ice and water dispensers
US2735275A (en) * 1956-02-21 Inyentor
US2753694A (en) * 1952-09-17 1956-07-10 Queen Stove Works Inc Ice disintegrating and chip delivering spiral ice chip producing machine
US2787133A (en) * 1954-06-22 1957-04-02 Clarence M Moe Ice making and ejecting machine
US2825209A (en) * 1954-04-21 1958-03-04 Queen Stove Works Inc Apparatus for producing compressed ice chips
US2877632A (en) * 1955-05-12 1959-03-17 Chaplik Rubin Machine for making and flaking ice
US2919561A (en) * 1954-08-31 1960-01-05 Gerald M Lees Ice harvesting means for flaked ice machines
US2942432A (en) * 1950-08-09 1960-06-28 Muffly Glenn Defrosting of evaporator
US3004395A (en) * 1956-07-25 1961-10-17 Morris And Gorrell Inc Method of handling refrigerant
US3073131A (en) * 1955-06-28 1963-01-15 Carrier Corp Method and apparatus for rendering saline water potable
US3101598A (en) * 1959-06-24 1963-08-27 Anthony J Ross Method and apparatus for freezing liquids
US3319436A (en) * 1965-11-29 1967-05-16 Phillips Petroleum Co Ice slush dispenser
US3340701A (en) * 1964-06-03 1967-09-12 Struthers Scientific Int Corp Crystallization
US3425235A (en) * 1955-05-26 1969-02-04 Robert B Cox Solvent purification
US3501924A (en) * 1955-06-28 1970-03-24 Carrier Corp Water wash of ice formed in vacuum freezing
US4305203A (en) * 1980-01-18 1981-12-15 General Dynamics, Convair Division Tool for installing shrink fit parts
US4345439A (en) * 1980-02-20 1982-08-24 Vencraft Corp. Snowmaking method and apparatus
US4551159A (en) * 1979-04-03 1985-11-05 Vladimir Goldstein Ice making machine and method
EP0168537A2 (en) * 1984-07-17 1986-01-22 Sunwell Engineering Company Limited Ice making machine
WO1986000692A1 (en) * 1984-07-17 1986-01-30 Sunwell Engineering Company Limited Ice making machine (mark i & mark ii)
US4669277A (en) * 1986-08-19 1987-06-02 Sunwell Engineering Company Ltd. Corrugated plate heat exchanger
US4796441A (en) * 1985-05-30 1989-01-10 Sunwell Engineering Company Limited Ice making machine
FR2630197A1 (en) * 1988-04-19 1989-10-20 Frigofrance Improved machine for manufacturing flakes of ice
WO1991010104A1 (en) * 1990-01-02 1991-07-11 Alfio Bucceri Snow making apparatus
AU642696B2 (en) * 1990-01-02 1993-10-28 Alfio Bucceri Snow making apparatus
EP1311331A2 (en) 2000-08-10 2003-05-21 Crytec Ltd Method and installation for continuous crystallization of liquids by freezing
US20140311178A1 (en) * 2013-04-22 2014-10-23 Leslie A. Field Generation and Deployment of Ice with modified Optical and/or Thermal Properties
US20150052931A1 (en) * 2013-08-22 2015-02-26 King Fahd University Of Petroleum And Minerals Heat exchanger
WO2015174156A1 (en) * 2014-05-13 2015-11-19 株式会社MARS Company Ice-making device
US20210018238A1 (en) * 2018-03-13 2021-01-21 Thorsteinn I Viglundsson Method & Apparatus for making wet snow

Cited By (40)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2735275A (en) * 1956-02-21 Inyentor
US2418746A (en) * 1941-09-27 1947-04-08 Texas Res Corp Food freezing machine
US2942432A (en) * 1950-08-09 1960-06-28 Muffly Glenn Defrosting of evaporator
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