US3170767A - Apparatus for quantitative determination of fatty material and water in biological tissue - Google Patents
Apparatus for quantitative determination of fatty material and water in biological tissue Download PDFInfo
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- US3170767A US3170767A US994A US99460A US3170767A US 3170767 A US3170767 A US 3170767A US 994 A US994 A US 994A US 99460 A US99460 A US 99460A US 3170767 A US3170767 A US 3170767A
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N33/00—Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
- G01N33/02—Food
- G01N33/12—Meat; fish
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N25/00—Investigating or analyzing materials by the use of thermal means
- G01N25/14—Investigating or analyzing materials by the use of thermal means by using distillation, extraction, sublimation, condensation, freezing, or crystallisation
Definitions
- This invention relates to an apparatus and a process for separating the moisture and fatty material from organic material. Particularly, the invention relates to an apparatus and a process for quantitative extraction of fatty material and moisture from biological material.
- the invention utilizes a unique and novel flask construction and process which permits the quantitative extraction of the fatty material and moisture in a given sample of biological material in a single process.
- FIGURE 1 is a side elevational view of one embodiment of the instant invention.
- FIGURE 2 is an enlarged view of the flask shown at the bottom of FIGURE 1.
- FIGURE 3 is a View taken substantially on line 33 of FIGURE 1 and looking in the direction of the arrows.
- the prior art process for separation of moisture and fatty material and residual materials involves an initial step of removal of water from a sample by a heating for a long period of. time in an oven or the like. Besides being greatly time consuming (such methods often taking as long as 24 hours), this old process requires the comparison of the weight before and after heating to determine the amount of moisture driven oil. The second weighing must be made promptly after removal from the heat to minimize addition of moisture from the air. The heating required also may partially render some of the fatty material in the sample with resultant inaccuracy in the analysis of the fatty material and other substances.
- the vaporized solvent passes up the side of the receiver to the condenser where it condenses and drips back into the receiver over the dried sample of the material, which is placed in the central chamber of the receiver.
- the return solvent rises to a level where it begins flowing through an over-flow tube back to the solvent receiving flask.
- the solvent bearing fatty material extracted from the dried sample is then intermixed with the original solvent and the continuous heating circulates the pure solvent upwardly and return solvent bearing fatty materials until the fatty materials 3,170,767 Patented Feb. 23, 1965 ice from the sample are substantially removed.
- the fat materials content of the sample. is then determined by disconnecting the solvent flask containing the fat materials bearing solvent and driving the solvent off by heat and weighing the fat materials content remaining in the flask.
- an undried raw sample 10 of biological tissue such as a piece of animal fat
- a flask 11 which comprises the unique apparatus of this invention.
- the flask is solvent receiving but is not equivalent to the solvent receiving flask of the prior art because flask 11 is divided into separate chambers 12 and 13 by wall 14. Because Wall 14 does not extend the height of the flask 11 chambers 12 and 13, although completely separated to the top of the wall 14, communicate at the top of wall 14, as illustrated in FIGURES 1, 2 and 3.
- the chambers 12 and 13 are of unequal capacity with the smaller being disposed below the mouth or flask opening 15. Good results are obtained in accordance with the embodiment described herein if compartment 12 has about three times the capacity of the smaller compartment 13. As it will be apparent the dissimilar sizes of chambers 12 and 13 are not critical to the invention. It is critical, however, that there are provided facilitates and factors whereby the level of fatty materials solvent 16 during the process will cause it to spill from chamber 13 into chamber 12. Such factors andtheir relationship will be apparent to those skilled in the art.
- the sample 10 may be placed in an extraction thimble (not shown) before being placed in the compartment 13.
- the flask is then partially filled with fatty materials solvent 16 to a level which is somewhat below the top of the wall 14 which separates the bottom of the flask 11 into two compartments. It is essential to this invention that the level of the solvent in chamber 12 be below the upper edge of wall 14 to permit the spill-over of the solvent from compartment 13 into the compartment 12, as will be more particularly described hereinafter.
- the solvent 16 is an azeotropic fat solvent, that is, a fat solvent immiscible with water in the liquid state but miscible with water in the vapor stage.
- azeotropic fat solvent that is, a fat solvent immiscible with water in the liquid state but miscible with water in the vapor stage.
- solvents for normal operation of the process are toluene, xylol-and octanol.
- solvents of the above type can be selected having lower or higher boiling points, depending upon the temperature limits desired.
- a solvent having a boiling point below the alteration or destruction temperature should be used.
- a receiver such as for example, that known in the art as a Bidwell and Sterling receiver.
- the receiver 17 has a bottom portion comprising a vertical collection tube 18 which may he graduated and also has a condenser receiving joint 19 at its upper end portion. Between the joint 13 and the vertical collection tube 17 the receiver 17 has a central chamber 20 and a conduit or tube 21 which is disposed outwardly and downwardly. The lower end portion 22 of conduit or tube 21 is adapted to fit into the mouth 15 of the sample-containing flask 11.
- a reflux condenser 23 is disposed above the joint 19 of the receiver 17 with the lower end portion 24 of the said condenser fitted into the said joint.
- the flask 11, receiver 17 and condenser 23 are connected, as illustrated in FIGURE 1, after the sample and solvent are in place, to form a sealed unit.
- Heat from the heat source which is directed against the bottom of flask 11, causes the solvent in the flask to boil and causes evaporation of the water in the sample.
- the solvent 16 and the water from the sample, in a vapor state, form an 3, azeotropic mixture and pass upwardly through the coriduit or tube 21 of the receiv er 17 and continue upwardly through the upper chamber 26 and joint 19 of the receiver 17 into the vertical collection tube 18.
- tube 21 functions as a two-way conduit in which the azeotropic vapor comprising water and solvent is directed into condenser 23 and condensed pure solvent is directed into chamber 13.
- the solvent dripping over and circulating around the sample extracts the fatty material 27.
- the compartment 13 is full, the fatty materials laden solvent spills over into the compartment 12, which in this embodiment of the invention contains the greater proportion of the raw solvent.
- the condensed solvent continues to drip into the sample-containing compartment 13 and causes circulation over and around the meat sample continually to extract the fatty materials from the sample. Accordingly, a continuous and self-sustaining flow of the condensed solvent circulates over and around the sample with a relatively high degree of agitation which assists considerably in the dissolving of fatty materials.
- An apparatus for simultaneous and quantitative extraction of fatty material and water from biological tissue comprising a flask having an upper opening; a wall in said flask providing therein two chambers separated by said wall and communicating above said wall, one of said chambers aligned with said opening and adapted to contain the biological tissue; a tube providing a two-way path disposed in the opening in said flask; acondense'r in non-alignment with said flasks and communicatively connected to said tube, said condenser adapted to condense water and solvent delivered thereby; and a separator communicatively connected to said tube and adapted to stratify condensed water and solvent and return the solvent through said tube to said first chamber, said separator dis posed below the connection thereof with said tube.
- An apparatus for simultaneous and quantitative extraction of fatty material and water from biological tissue comprising a flask having an upper opening; a spill Wall in said flask dividing said flask into separate chambers whereby liquid in each chamber below the top of said wall is retained in the respective chamber and will spill from one chamber to the other upon reaching the top of said wall; one of said chambers adapted to contain biological tissue and aligned with the opening in said flask; a conduit providing a two-way path, said conduit having its lower end secured in the opening of said flask and extending upwardly therefrom at an angle; a reflux condenser and a water and solvent separator communicatively connected to the upper end of said conduit in non-alignment with said flask, the reflux condenser disposed above the separator whereby water and solvent in the vapor phase is delivered through said conduit to said reflux condenser and thereafter is stratified in the condensed phase in the separator with the solvent spilling into said conduit and returned to one of said chambers from which it spills in the
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Description
BY at? %z m s I T L A m H mum ET. m r/ N 5 7 a Wm 2 5mm w H w U H L A I R E m APPARATUS FOR QUANTITATIVE DETERMINATION OF FATTY Feb. 23, 1965 I .n. n m
INVENTOR. 7 0 Wiiteicfi a, it
United States Patent 3,170,767 APPARATUS FOR QUANTITATIVE DETERMINA- TION 0F FATTY MATERIAL AND WATER IN BIOLOGICAL TISSUE Hugo'E. Wistreich, Chicago, 11]., assignor to Reliable Packing Company, Chicago, Ill.
Filed Jan. 7, 1960, Ser. No. 994
2 Claims. (Cl. 23-263) This invention relates to an apparatus and a process for separating the moisture and fatty material from organic material. Particularly, the invention relates to an apparatus and a process for quantitative extraction of fatty material and moisture from biological material.
The invention utilizes a unique and novel flask construction and process which permits the quantitative extraction of the fatty material and moisture in a given sample of biological material in a single process.
It is an object of this invention to provide a closed system for complete simultaneous quantitative removal from samples of organic tissue, particularly, chunks of meat and fatty material; and simultaneous quantitative separation of the fatty material and moisture from the samples and from each other, and from the proteinous or fibrous residual material left in the sample when the fatty material and moisture have been removed.
By utilizing a closed system in accordance with the instant invention, a high degree of accuracy and a substantially fool-proof arrangement results for the accomplishment of the objects hereof when compared with the prior are devices and procedures as will become more apparent hereinafter.
Other and further objects of the invention will be apparent from the following description and appended claims.
On the drawings:
FIGURE 1 is a side elevational view of one embodiment of the instant invention.
FIGURE 2 is an enlarged view of the flask shown at the bottom of FIGURE 1.
FIGURE 3 is a View taken substantially on line 33 of FIGURE 1 and looking in the direction of the arrows.
The prior art process for separation of moisture and fatty material and residual materials involves an initial step of removal of water from a sample by a heating for a long period of. time in an oven or the like. Besides being greatly time consuming (such methods often taking as long as 24 hours), this old process requires the comparison of the weight before and after heating to determine the amount of moisture driven oil. The second weighing must be made promptly after removal from the heat to minimize addition of moisture from the air. The heating required also may partially render some of the fatty material in the sample with resultant inaccuracy in the analysis of the fatty material and other substances.
In the process of the prior art, after the dried sample has been weighed, it is placed in an apparatus such as a solvent receiver which is intermediate between a flask containing a fatty material solvent and a reflux condenser.
By heating the solvent flask the vaporized solvent passes up the side of the receiver to the condenser where it condenses and drips back into the receiver over the dried sample of the material, which is placed in the central chamber of the receiver. As the condensed solvent collects in the central chamber the return solvent rises to a level where it begins flowing through an over-flow tube back to the solvent receiving flask. The solvent bearing fatty material extracted from the dried sample is then intermixed with the original solvent and the continuous heating circulates the pure solvent upwardly and return solvent bearing fatty materials until the fatty materials 3,170,767 Patented Feb. 23, 1965 ice from the sample are substantially removed. The fat materials content of the sample. is then determined by disconnecting the solvent flask containing the fat materials bearing solvent and driving the solvent off by heat and weighing the fat materials content remaining in the flask.
Inaccordance with the instant invention, an undried raw sample 10 of biological tissue, such as a piece of animal fat, is placed into a flask 11, which comprises the unique apparatus of this invention. The flask is solvent receiving but is not equivalent to the solvent receiving flask of the prior art because flask 11 is divided into separate chambers 12 and 13 by wall 14. Because Wall 14 does not extend the height of the flask 11 chambers 12 and 13, although completely separated to the top of the wall 14, communicate at the top of wall 14, as illustrated in FIGURES 1, 2 and 3.
In the preferred embodiment of the invention the chambers 12 and 13 are of unequal capacity with the smaller being disposed below the mouth or flask opening 15. Good results are obtained in accordance with the embodiment described herein if compartment 12 has about three times the capacity of the smaller compartment 13. As it will be apparent the dissimilar sizes of chambers 12 and 13 are not critical to the invention. It is critical, however, that there are provided facilitates and factors whereby the level of fatty materials solvent 16 during the process will cause it to spill from chamber 13 into chamber 12. Such factors andtheir relationship will be apparent to those skilled in the art.
In practice the sample 10 may be placed in an extraction thimble (not shown) before being placed in the compartment 13. The flask is then partially filled with fatty materials solvent 16 to a level which is somewhat below the top of the wall 14 which separates the bottom of the flask 11 into two compartments. It is essential to this invention that the level of the solvent in chamber 12 be below the upper edge of wall 14 to permit the spill-over of the solvent from compartment 13 into the compartment 12, as will be more particularly described hereinafter.
The solvent 16 is an azeotropic fat solvent, that is, a fat solvent immiscible with water in the liquid state but miscible with water in the vapor stage. Among the preferred solvents for normal operation of the process are toluene, xylol-and octanol. Of course, solvents of the above type can be selected having lower or higher boiling points, depending upon the temperature limits desired. Forexample, to preserve certain characteristics of the ele ments of the sample which may be altered or destroyed byhigher heat a solvent having a boiling point below the alteration or destruction temperature should be used.
Above the flask is mounted a receiver, generally designated as 17, such as for example, that known in the art as a Bidwell and Sterling receiver. The receiver 17 has a bottom portion comprising a vertical collection tube 18 which may he graduated and also has a condenser receiving joint 19 at its upper end portion. Between the joint 13 and the vertical collection tube 17 the receiver 17 has a central chamber 20 and a conduit or tube 21 which is disposed outwardly and downwardly. The lower end portion 22 of conduit or tube 21 is adapted to fit into the mouth 15 of the sample-containing flask 11.
A reflux condenser 23 is disposed above the joint 19 of the receiver 17 with the lower end portion 24 of the said condenser fitted into the said joint.
The flask 11, receiver 17 and condenser 23 are connected, as illustrated in FIGURE 1, after the sample and solvent are in place, to form a sealed unit. Heat from the heat source which is directed against the bottom of flask 11, causes the solvent in the flask to boil and causes evaporation of the water in the sample. The solvent 16 and the water from the sample, in a vapor state, form an 3, azeotropic mixture and pass upwardly through the coriduit or tube 21 of the receiv er 17 and continue upwardly through the upper chamber 26 and joint 19 of the receiver 17 into the vertical collection tube 18.
The condensed water, being heavier than the solvent 16, collects at the bottom of the tube 18 with the condensed solvent stratified above the condensed water. Substantially pure solvent 16 which reaches the level of orifice 25 spills through said orifice outwardly and downwardly through the side tube 21 into chamber 13 which is aligned below the mouth 14 of flask 11.
As the process continues and the level of water 26 in receiver 17 rises, this causes an increase in the speed of the process because of the more rapid delivery of solvent 16 into chamber 13. It is apparent that tube 21 functions as a two-way conduit in which the azeotropic vapor comprising water and solvent is directed into condenser 23 and condensed pure solvent is directed into chamber 13.
As the spill-over solvent from the receiver tube 21 drips down through the mouth 15 of the flask 11 into the sample which is in the compartment 13, the solvent dripping over and circulating around the sample extracts the fatty material 27. When the compartment 13 is full, the fatty materials laden solvent spills over into the compartment 12, which in this embodiment of the invention contains the greater proportion of the raw solvent.
As the circulation continues due to the boiling and subsequent condensation, the condensed solvent continues to drip into the sample-containing compartment 13 and causes circulation over and around the meat sample continually to extract the fatty materials from the sample. Accordingly, a continuous and self-sustaining flow of the condensed solvent circulates over and around the sample with a relatively high degree of agitation which assists considerably in the dissolving of fatty materials.
From the foregoing it is apparent that for proper operation of the process the apparatus employed must insure that the fatty materials laden solvent 27 does not rise to a level above the wall 14 and also that the fluids build up in chamber 13 to a point where they will spill over the wall 14 into the chamber 12. Attention is invited to the fact that a number of aspects, readily apparent to those skilled in the art, could be employed to achieve this result. However, the one which is most obvious to me and probably the most simple, is by making chambers 12 and 13 of unequal dimension with chamber 13 substantially smaller than chamber 12 to insure a greater volume of evaporation of solvent from chamber 12 than occurs from chamber 13 to permit the build-up and continuous spillover from chamber 13 into chamber 12.
It is also apparent, of course, that after all of the fatty materials and water have been removed from the sample 10 and the solvent extracted or removed in any suitable fashion that the residue in chamber 13, as well as the fatty material in chamber 12 and the water in receiver 17, can be quantitatively determined by simple direct measurement.
To insure the best result it would appear preferable 4 that the solvent returning through the tube or conduit 21 should be precluded from dropping into chamber 12 and directed into chamber 13.
Inasmuch as many changes could be made in the abovedescribed construction and process, and inasmuch as many apparently widely different embodiments of the invention within the scope of the claims could be constructed without departing from the scope and spirit thereof, it is intended that all matter contained in the accompanying specification shall be interpreted as being illustrative and not in a limiting sense.
I claim: I
1. An apparatus for simultaneous and quantitative extraction of fatty material and water from biological tissue comprising a flask having an upper opening; a wall in said flask providing therein two chambers separated by said wall and communicating above said wall, one of said chambers aligned with said opening and adapted to contain the biological tissue; a tube providing a two-way path disposed in the opening in said flask; acondense'r in non-alignment with said flasks and communicatively connected to said tube, said condenser adapted to condense water and solvent delivered thereby; and a separator communicatively connected to said tube and adapted to stratify condensed water and solvent and return the solvent through said tube to said first chamber, said separator dis posed below the connection thereof with said tube.
2. An apparatus for simultaneous and quantitative extraction of fatty material and water from biological tissue comprising a flask having an upper opening; a spill Wall in said flask dividing said flask into separate chambers whereby liquid in each chamber below the top of said wall is retained in the respective chamber and will spill from one chamber to the other upon reaching the top of said wall; one of said chambers adapted to contain biological tissue and aligned with the opening in said flask; a conduit providing a two-way path, said conduit having its lower end secured in the opening of said flask and extending upwardly therefrom at an angle; a reflux condenser and a water and solvent separator communicatively connected to the upper end of said conduit in non-alignment with said flask, the reflux condenser disposed above the separator whereby water and solvent in the vapor phase is delivered through said conduit to said reflux condenser and thereafter is stratified in the condensed phase in the separator with the solvent spilling into said conduit and returned to one of said chambers from which it spills in the liquid phase into the other thereof.
References Cited in the file of this patent UNITED STATES PATENTS 2,295,912 Pagenkoff Sept. 15, 1942 2,324,088 Jewett July 13, 1943 2,491,115 Kincaide Dec. 13, 1949 2,752,377 McDonald et al June 26, 1956 2,782,104 Glinka Feb. 19, 1957 2,847,282 Dunning et al Aug. 12, 1958
Claims (1)
1. AN APPARATUS FOR SIMULTANEOUS AND QUANTITATIVE EXTRACTION OF FATTY MATERIAL AND WATER FROM BIOLOGICAL TISSUE COMPRISING A FLASK HAVING AN UPPER OPENIN; A WALL IN SAID FLASK PORVIDING THEREIN TWO CHAMBERS SEPARATED BY SAID WALL AND COMMUNICATING ABOVE SAID WALL, ONE OF SAID CHAMBERS ALIGNED WITH SAID OPENING AND ADAPTED TO CONTAIN THE BIOLOGICAL TISSUR; A TUBE PROVIDING A TWO-WAY PATH DISPOSED IN THE OPENING IN SAID FLASK; A CONDENSSER IN NON-ALIGNMENT WITH SAID FLASKS AND COMMUNICATIVELY CONNECTED TO SAID TUBE, SAID CONDENSER ADAPTED TO CONDENSE WATER AND SOLVENT DELIVERED THEREBY; AND A SEPARATOR COMMUNICATIVELY CONNECTED TO SAID TUBE AND ADAPTED TO STRATIFY CONDENSED WATER AND SOLVENT AND RETURN THE SOLVENT THROUGH SAID TUBE TO SAID FIRST CHAMBER, SAID SEPARATOR DISPOSED BELOW THE CONNECTION THEREOF WITH SAID TUBE.
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US994A US3170767A (en) | 1960-01-07 | 1960-01-07 | Apparatus for quantitative determination of fatty material and water in biological tissue |
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US994A US3170767A (en) | 1960-01-07 | 1960-01-07 | Apparatus for quantitative determination of fatty material and water in biological tissue |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3627796A (en) * | 1964-11-02 | 1971-12-14 | Viobin Corp | Continuous process for producing fat and solids from wet biological substance |
US3742001A (en) * | 1964-11-02 | 1973-06-26 | Vio Bin Corp | Rendering process |
US3867416A (en) * | 1966-07-15 | 1975-02-18 | French Oil Mill Machinery | Continuous process for drying and extracting oils from solid materials |
EP0762115A1 (en) * | 1995-09-04 | 1997-03-12 | Büchi Labortechnik AG | Method for determining the fat content of organic samples |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2295912A (en) * | 1940-06-03 | 1942-09-15 | Teletype Corp | Dehydrating and treating apparatus |
US2324088A (en) * | 1940-04-16 | 1943-07-13 | American Cyanamid Co | Distillation of high boiling esters |
US2491115A (en) * | 1943-11-27 | 1949-12-13 | Charles R Kincaide | Method for solvent extraction |
US2752377A (en) * | 1950-12-04 | 1956-06-26 | Barber Greene Co | Solvent extraction process |
US2782104A (en) * | 1953-05-11 | 1957-02-19 | Buttner Werke Ag | Apparatus for the continuous lixivation, extraction or the like of vegetable matter |
US2847282A (en) * | 1954-11-12 | 1958-08-12 | Int Basic Economy Corp | Countercurrent extraction apparatus |
-
1960
- 1960-01-07 US US994A patent/US3170767A/en not_active Expired - Lifetime
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2324088A (en) * | 1940-04-16 | 1943-07-13 | American Cyanamid Co | Distillation of high boiling esters |
US2295912A (en) * | 1940-06-03 | 1942-09-15 | Teletype Corp | Dehydrating and treating apparatus |
US2491115A (en) * | 1943-11-27 | 1949-12-13 | Charles R Kincaide | Method for solvent extraction |
US2752377A (en) * | 1950-12-04 | 1956-06-26 | Barber Greene Co | Solvent extraction process |
US2782104A (en) * | 1953-05-11 | 1957-02-19 | Buttner Werke Ag | Apparatus for the continuous lixivation, extraction or the like of vegetable matter |
US2847282A (en) * | 1954-11-12 | 1958-08-12 | Int Basic Economy Corp | Countercurrent extraction apparatus |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3627796A (en) * | 1964-11-02 | 1971-12-14 | Viobin Corp | Continuous process for producing fat and solids from wet biological substance |
US3742001A (en) * | 1964-11-02 | 1973-06-26 | Vio Bin Corp | Rendering process |
US3867416A (en) * | 1966-07-15 | 1975-02-18 | French Oil Mill Machinery | Continuous process for drying and extracting oils from solid materials |
EP0762115A1 (en) * | 1995-09-04 | 1997-03-12 | Büchi Labortechnik AG | Method for determining the fat content of organic samples |
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