USRE22629E - Process for concentrating carotene - Google Patents
Process for concentrating carotene Download PDFInfo
- Publication number
- USRE22629E USRE22629E US22629DE USRE22629E US RE22629 E USRE22629 E US RE22629E US 22629D E US22629D E US 22629DE US RE22629 E USRE22629 E US RE22629E
- Authority
- US
- United States
- Prior art keywords
- carotene
- water
- concentrate
- particles
- carrots
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 150000001746 carotenes Chemical class 0.000 title description 41
- 235000005473 carotenes Nutrition 0.000 title description 41
- 238000000034 method Methods 0.000 title description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 21
- 239000012141 concentrate Substances 0.000 description 16
- 239000002245 particle Substances 0.000 description 11
- 240000002860 Daucus carota Species 0.000 description 9
- 235000002767 Daucus carota Nutrition 0.000 description 8
- 239000005418 vegetable material Substances 0.000 description 7
- 230000001112 coagulant Effects 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- 235000013311 vegetables Nutrition 0.000 description 6
- 229940045997 Vitamin A Drugs 0.000 description 4
- FPIPGXGPPPQFEQ-BOOMUCAASA-N Vitamin A Natural products OC/C=C(/C)\C=C\C=C(\C)/C=C/C1=C(C)CCCC1(C)C FPIPGXGPPPQFEQ-BOOMUCAASA-N 0.000 description 4
- FPIPGXGPPPQFEQ-OVSJKPMPSA-N all-trans-retinol Chemical compound OC\C=C(/C)\C=C\C=C(/C)\C=C\C1=C(C)CCCC1(C)C FPIPGXGPPPQFEQ-OVSJKPMPSA-N 0.000 description 4
- 239000000701 coagulant Substances 0.000 description 4
- 239000000835 fiber Substances 0.000 description 4
- 239000002657 fibrous material Substances 0.000 description 4
- 235000013305 food Nutrition 0.000 description 4
- 235000019645 odor Nutrition 0.000 description 4
- 238000004537 pulping Methods 0.000 description 4
- 229960003471 retinol Drugs 0.000 description 4
- 235000019155 vitamin A Nutrition 0.000 description 4
- 239000011719 vitamin A Substances 0.000 description 4
- 239000000796 flavoring agent Substances 0.000 description 3
- 235000019634 flavors Nutrition 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N HCl Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 239000002274 desiccant Substances 0.000 description 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- 238000010790 dilution Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 235000002243 Daucus carota subsp sativus Nutrition 0.000 description 1
- 240000003613 Ipomoea batatas Species 0.000 description 1
- 235000002678 Ipomoea batatas Nutrition 0.000 description 1
- 235000007688 Lycopersicon esculentum Nutrition 0.000 description 1
- 240000004658 Medicago sativa Species 0.000 description 1
- 240000003768 Solanum lycopersicum Species 0.000 description 1
- 240000008529 Triticum aestivum Species 0.000 description 1
- 238000007792 addition Methods 0.000 description 1
- 235000017585 alfalfa Nutrition 0.000 description 1
- 235000017587 alfalfa Nutrition 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 235000012970 cakes Nutrition 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 238000010908 decantation Methods 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000000576 food coloring agent Substances 0.000 description 1
- 238000005755 formation reaction Methods 0.000 description 1
- 238000010297 mechanical methods and process Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000000825 pharmaceutical preparation Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 235000021307 wheat Nutrition 0.000 description 1
- 235000005765 wild carrot Nutrition 0.000 description 1
Definitions
- One object of the invention is to provide a process for the economical concentration of carotene from vegetable sources. Another object i to provide a stable dry vegetable concentrate having high carotene content. Still another object is to provide an aqueous carotene concentrate.
- the carotene content of thoroughly pulped fresh vegetables such as carrots may be almost completely removed by a suitable water elutriation process, and when the process is carried outwith a minimum amount of water, followed by subsequent coagulation, the carotene may be concentrated to as much as 50 to 200 or more times the original concentration in the carrots.
- the fresh carrots are reduced to a pulp by any suitable mechanical process, such as by Passin them through a hammer mill preferably without using added water or other liquid. It is important thatthe structure be well broken down so that the carotene particles are released from the fiber and other materials.
- the semi-liquid mass or pulp is distributed in a thin layer on a moving i'oraminous belt such as a screen belt. and jets of water are forced against the pulp on the belt.
- the carotene and carotene-containing particles are insoluble in water, and are small enoughsome being of colloidal dimensio'ns -to be carried through the screen openings with the water.
- the amount ofrial is merely a harmless diluent.
- the coagulum is separated from the water medium by decantation, filtration, centrifuging, or other suitable method, and the resulting concentrate is in the form of a moist cake having 50 times or more, the carotene content of the original carrots.
- the concentrate may be brought to an apparently dry state by thoroughly mixing with a normally dry food or feed material, for example wheat by-products such as-middlings or. shorts," which act as a desiccant for the carotene concentrate.
- a normally dry food or feed material for example wheat by-products such as-middlings or. shorts," which act as a desiccant for the carotene concentrate.
- the process 01 making a carotene concentrate comprising pulping a carotene-containing vegetable material, elutriating with water to separate the carotene particles from the fibrous material, coagulating the carotene particles, and
Landscapes
- Coloring Foods And Improving Nutritive Qualities (AREA)
- Fodder In General (AREA)
Description
Reissued Apr. 17, 1945 PROCESS FOR CONCENTRATING CAROTENE Harold M. Barnett, Long Beach, Calif.
No Drawing. Original No. 2.348443, dated May 9, 1944, Serial No. 489,989, June "I, 1943. Application for reissue June 28', 1944, Serial No.
4 Claims.
' This-invention relates to the preparation of carotene in concentrated form from vegetable materials.
One object of the invention is to provide a process for the economical concentration of carotene from vegetable sources. Another object i to provide a stable dry vegetable concentrate having high carotene content. Still another object is to provide an aqueous carotene concentrate.
I have discovered that the carotene content of thoroughly pulped fresh vegetables such as carrots may be almost completely removed by a suitable water elutriation process, and when the process is carried outwith a minimum amount of water, followed by subsequent coagulation, the carotene may be concentrated to as much as 50 to 200 or more times the original concentration in the carrots.
My process will be illustrated by the preparation of carotene from carrots, although the process is applicable to other vegetable materials having carotene content such as tomatoes, alfalfa, sweet potatoes, and the like.
The fresh carrots are reduced to a pulp by any suitable mechanical process, such as by Passin them through a hammer mill preferably without using added water or other liquid. It is important thatthe structure be well broken down so that the carotene particles are released from the fiber and other materials. The semi-liquid mass or pulp is distributed in a thin layer on a moving i'oraminous belt such as a screen belt. and jets of water are forced against the pulp on the belt. The carotene and carotene-containing particles are insoluble in water, and are small enoughsome being of colloidal dimensio'ns -to be carried through the screen openings with the water. The action of the jets is to'physically disentangle the carotene particles from the fiber and to carry them through the screen, with avoidance of formation of a mat of fibers on the screen which would act as'a fllter and hold back or entrap the carotene particles. I have found that a screen of about 40 mesh is satisfactory for carrots, but the screen opening may be -varied for diiferent' pulps. The minimum amount of water is used which will separate out a high percentage of the carotene particles A moving belt has been found advantageous to keep the amount of water to a minimum, but obviously other means may be used than those described here for i1lus-.
ilar means for this purpose. The amount ofrial is merely a harmless diluent.
water to be used varies with different vegetables and with different lots of varying qualities and textures. I have actually used up to 25 gallons of water to pounds of carrot pulp. The carotene in the water from this elutriation or extraction process is then coagulated by heating with or without a coagulant, or by means of an added coagulant such as hydrochloric acid. When coagulated by heating alone, provided the dilution is not too great, the carotene with some other colloidal or line materials collects at the top, while a precipitate forms when acid is used as the coagulant. If the dilution is too great, de-
pendent upon the particular vegetable material being treated, an added coagulant is required. The coagulum is separated from the water medium by decantation, filtration, centrifuging, or other suitable method, and the resulting concentrate is in the form of a moist cake having 50 times or more, the carotene content of the original carrots.
The concentrate thus produced has an equivalent vitamin A content of from 2 to 10 million units per pound, and is free from undesirable odors or flavors which are encountered in the usual process in which carrots after dehydrating are extracted with a solvent such as'petroleum ether. It is also free from the oxidation products or carotene or the materials associated with it. This concentrate contains beside carotene small amounts of cellulosic fiber, protein, oil, etc., but for most uses of carotene this extraneous mate- Because of the nature of the concentrate as above made, it is dimcult to remove the last portion of the water, but this may be done by the use of reduced pressure evaporation, or by the use of or addition of desiccants. Ihave found that where the concentrate is to be used in foods and feeds, it may be brought to an apparently dry state by thoroughly mixing with a normally dry food or feed material, for example wheat by-products such as-middlings or. shorts," which act as a desiccant for the carotene concentrate. The
moisture content of the mixture is so reduced moist concentrate containing eight million vitamin A units per pound, to seven parts of shorts,"
- producing a feed concentrate having carotene content equivalentto about one million vitamin A units per pound, which concentrate is dry, does not easily spoil, and readily mixes with other feed materials, in the preparation of mixed and fortified feeds. Other foods capable of taking up the extra moisture to give an apparently dry product may be used.
By avoiding the drying of the carrots, as commonly practiced, I greatly decrease the cost of getting the carotene from vegetable sources, and also make a product which is free from odors and flavors from the incompletely removed extracting solvents which have heretofore been employed, or the odors and flavorsfrom dehydrated vegetables. Because of this freedom from undesired odors and flavors, my concentrate may be used as a food coloring material or as a source separating the coamlum from the excess water.
2. The process 01' making a carotene concentrate comprising pulping a carotene-containing vegetable material, elutriating with water to separate the carotene particles from the fibrous material, coagulating the carotene particles, separating the coagulum from the excess water, and then desiccating the coagulum.
3. The process of making a carotene concentrate comprising pulping a, carotene-containing vegetable material, elutriating with water to of vitamin A in the fortification of pharmaceutical products, foods, and feeds.
I claim:
1. The process 01 making a carotene concentrate comprising pulping a carotene-containing vegetable material, elutriating with water to separate the carotene particles from the fibrous material, coagulating the carotene particles, and
separate the carotene particles from the fibrous material, adding sufiicient acid to form a coagulum containing the carotene, and separating the coagulum from the excess water.
4. The process of making a carotene concentrate comprising'pulping a carotene-containing vegetable material, elutriating with water to separate the carotene particles from fibrous material, heating to form a coagulum containing the carotene, and separating the coagulum from the excess water.
HAROLD M. BARNETT.
Publications (1)
Publication Number | Publication Date |
---|---|
USRE22629E true USRE22629E (en) | 1945-04-17 |
Family
ID=2089328
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US22629D Expired USRE22629E (en) | Process for concentrating carotene |
Country Status (1)
Country | Link |
---|---|
US (1) | USRE22629E (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2739145A (en) * | 1952-01-07 | 1956-03-20 | Harold M Barnett | Method for recovering carotene, fiber, and serum from vegetable material |
US5157132A (en) * | 1990-05-18 | 1992-10-20 | Carotech Associates | Integrated process for recovery of carotenoids and tocotrienols from oil |
-
0
- US US22629D patent/USRE22629E/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2739145A (en) * | 1952-01-07 | 1956-03-20 | Harold M Barnett | Method for recovering carotene, fiber, and serum from vegetable material |
US5157132A (en) * | 1990-05-18 | 1992-10-20 | Carotech Associates | Integrated process for recovery of carotenoids and tocotrienols from oil |
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