GB2094334A - Extracting oil, protein and flour from fresh coconut meat - Google Patents
Extracting oil, protein and flour from fresh coconut meat Download PDFInfo
- Publication number
- GB2094334A GB2094334A GB8129503A GB8129503A GB2094334A GB 2094334 A GB2094334 A GB 2094334A GB 8129503 A GB8129503 A GB 8129503A GB 8129503 A GB8129503 A GB 8129503A GB 2094334 A GB2094334 A GB 2094334A
- Authority
- GB
- United Kingdom
- Prior art keywords
- coconut
- oil
- coconut meat
- protein
- range
- 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.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B1/00—Production of fats or fatty oils from raw materials
- C11B1/10—Production of fats or fatty oils from raw materials by extracting
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23J—PROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
- A23J1/00—Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites
- A23J1/14—Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites from leguminous or other vegetable seeds; from press-cake or oil-bearing seeds
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B1/00—Production of fats or fatty oils from raw materials
- C11B1/06—Production of fats or fatty oils from raw materials by pressing
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Biochemistry (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Fats And Perfumes (AREA)
- Meat, Egg Or Seafood Products (AREA)
- Peptides Or Proteins (AREA)
Abstract
A process for extracting oil, protein and flour from fresh coconut meat without boiling, refrigeration, action of enzymes, acidification, use of salt or brine, electrolytic action or shock waves includes drying the coconut meat at 60-70 DEG C to break coconut milk emulsion, grinding the dried coconut meat, pressing the ground meat to extract part of its oil content, mixing the residue with heated tap and coconut water at 55- 65 DEG C and further grinding into a finer size, mixing and agitating the slurry at 55-65 DEG C, separating the solid from the liquid, drying the solid to recover the flour content, separating further an oil phase from an aqueous phase to segregate the water clear coconut oil and water-protein slurry, processing the water clear oil into edible oil and processing the water-protein into protein powder. <IMAGE>
Description
SPECIFICATION
Extracting oil, protein and flour from fresh
coconut meat
This invention relates to processes for the
isolation of useful substances from vegetable
sources. More particularly, it relates to a process
for extracting oil, protein and flour from fresh
coconut meat.
The conventional method for the recovery of oil
from the coconut meat has not changed much
during the past 200 years. This method involves
the drying of the immaculately white, edible and
clean coconut meat to dirty, unedible and brown
copra for subsequent pressing in expellers to
obtain the oil by mechanical action. The oil thus
obtained is dirty, needing to be refined, bleached,
filtered and deodorized. The residual copra meal is
fit only for animal feeds. Proteins and flour are not
recovered for human consumption and most of
the proteins are eaten by the bacteria. About 30%
of the oil content is lost in this process.
Studies made by the Tropical Products
Institute (TPI) of England, concluded that the main
stumbling blocks in the extraction of high quality
coconut oil and protein from wet coconut meat,
involve chronologically:
a) optimizing coconut milk emulsion extraction
from wet coconut meat; and
b) breaking the coconut milk emulsion to
separate the oil, protein and water.
TPI also noted "at least part of the cause of the
economic failure of the modern wet processes
must be attributed to the kinds of milling system
used. These processes, which employ mills
incapable of grinding the coconut the subcellular
dimensions, will not achieve high extractions of
oil and protein. The crux of the whole problem of wet-processing of fresh coconut, is the separation
of the emulsion into its constituents. This cannot
be done simply by boiling, as with the primitive
methods, because a protracted boiling process
would seriously damage the quality of the protein
and of oil".
The aim of the present invention is to provide a method of extracting oil, protein and flour from fresh coconut meat taking into consideration the aforementioned problem areas.
Accordingly the invention provides a process for extracting flour, oil and/or protein from fresh coconut meat comprising: drying continuously the coconut meat at a temperature in the range 600C to 700C to break the coconut milk emulsion; grinding the coconut meat into the size range 80 to 100 mesh pressing the ground coconut meat to separate at least some of the oil content thereof from a residue; immersing and mixing the residue in heated tap and coconut water at a temperature in the range 550C to 650C; grinding further the immersed ground coconut meat to form a 200 to 250 mesh slurry; mixing and agitating the slurry continuously for from 1 5 to 20 minutes at a temperature in the range 550C to 650C; and separating a solid from the liquid in the agitated slurry mixture, whereby flour can be extracted from the solid and oil and/or protein can be extracted from the liquid.
When fresh coconut meat is dried at temperatures in the range 600C to 700C to less than 5% moisture content, oil separates permanently from water and protein without the need for boiling. Thus continuous drying of the wet coconut meat results in breaking or deemulsionizing the coconut milk emulsion. While this is a solution to the TPI problem (b) discussed above, it is conducted as the first phase in the process of my invention.
Cellular structures which hold the oil are ruptured and cut into two to five pieces when dried coconut meat is ground to about 100 mesh.
This enables a proportion of the oil to be extracted by pressing. Further mechanical grinding treatment by a grinder-macerator to grind the coconut meat residue to particles of about 250 mesh results in the cell walis being broken, thereby liberating the oil. In the process of the invention this additional grinding of the residue is performed in heated water so that most of the residual oil is released into the water. Thus almost 100% recovery of the oil from fresh coconut meat is achieved. These steps, the second phase in my invention comprises the solution to the TPI problem (a).
It has been found that a process in accordance with the present invention provides a means for extracting oil, protein and flour from the fresh coconut meat, wherein the products obtained through said process are fit for human comsumption without the need for further refining or processing.
It has been further found that a process in accordance with the invention is economical in terms of reducing the high capital and operating costs of the traditional recovery of oil by dispensing with some of the tradditional process steps and substantially simplifying the process.
It has also been found that a process in accordance with the present invention enables the recovery of solids of oil, protein, sugar and chlorides from coconut water.
Other features and advantages of this invention will become apparent upon reading the description and with reference to the accompanying drawing which is a process flowchart.
The process of the invention involves two main phases, first the breaking or de-emulsionizing of the coconut milk emulsion in the fresh coconut meat, and secondly the extraction of water-free coconut oil, protein and flour. The first phase, comprises the breaking up of the coconut milk emulsion, preferably also includes recovering the crude acid, crude tar, crude methanol and crude gas from coconut shells.
In the preferred embodiment, the shells of the coconut are removed and the fresh meat is chopped lengthwise, into about 20 pieces. The coconut water is stored in a stainless steel tank.
The chopped coconut meat is then washed with chlorine to check bacterial contamination during the pre-drying stage. Breaking or deemulsionizing of the coconut milk emulsion starts within five minutes thereafter in a pre-heated drier. The chopped fresh coconut meat is dried at a temperature ranging from 600C to 700C for about 24 hours until the moisture content is less than 5%.
The second phase follows the breaking or de
emulsionizing phase. From the drier, the coconut
meat is immediately ground to 80-100 mesh.
The ground coconut meat is then pressed to
separate about 85% of its oil content. In order to
minimize undue build-up of heat, this treatment
should not be undertaken in an oil speller. The oil thus derived is stored in a storage tank. The
residue is then immersed and agitated in a mixing
tank with coconut and tap water and heated at 550C to 650Cforfive minutes. Preferably the weight of the coconut and tap water in the tank is four times the weight of the residue. The immersed ground coconut meat residue is then comminuted in a colloid mill or grinder/macerator, to produce a slurry of 200 to 250 mesh. The slurry is then transferred to a mixing tank which is provided with a heater at the bottom.In the mixing tank, the slurry is further mixed and agitated continuously for 1 5 to 20 minutes while maintaining the temperature at 550C to 65 C.
The agitated mixture is then conveyed to a solid-liquid centrifuge to separate the liquid from the solid which comes out in paste form. This paste is actually the wet flour. The wet flour is then dried. This may be accomplished in two ways-with or without the addition of tap water.
Without adding water, the wet flour can be dried in a suspension, pneumatic or splash drier.
Alternatively, after the addition of tap water, the wet flour may be dried using a spray drier. When this is desired, an amount of tap water, two times the weight of the wet flour and heated to 550C to 650C, is added to the wet flour prior to the drying stage. Drying occurs when the product is sprayed into a stream of warm air in spray drier, the influent air having a temperature of about 1000C to 1 500C.
The remaining liquid oil, protein and water obtained from the solid-liquid centrifuge is fed to a liquid-liquid centrifuge where the liquid is separated into an oil phase and an aqueous phase, the aqueous phase being a water-protein slurry. The oil thus obtained is deoderized with activated carbon to make it edible and is subsequently deposited in a stainless steel tank.
The water-protein slurry is allowed to settle in a settling tank for 30 minutes. About 20% by volume of the top portion of water is removed for recycling and recovery of more oil. Then 60% of the next or middle portion of water phase is discarded. The remaining 20% of water, the bottom portion, together with the precipitate, which is protein, is slowly dried, at a temperature of about 650C to 700C using a spray drier, to recover the water-soluble protein powder.
The flour and protein thus extracted may then be weighed and packed individually.
It has been found that in order to obtain
maximum yields of oil, protein and flour, water
used as a solvent must be pre-heated to 550C to 6500. This temperature is critical since it has
been found that at a temperature lower than
550C, or higher than 650C a reduction in the quality and extraction rate of oil, protein and flour
occurs. Air entering the enclosed processing area
should be washed by means of a suitable air
water washing machine to prevent contamination
of the extracted oil, protein and flour by
microorganisms such as bacteria.
Using a process in accordance with the
invention it has been found to be possible to
break or de-emulsionize the coconut milk
emulsion in fresh coconut meat without boiling,
refrigeration, action of enzymes, acidification, use
of salt or brine, electrolytic action or shock waves.
It has also been found that more than 99% of the
oil content of fresh meat can be recovered. It can
be concluded therefore, that my invention has
successfully hurdled the main stumbling blocks in
the extraction of high quality oil, protein and flour
from fresh coconut meat.
Claims (12)
1. A process for extracting flour, oil and/or protein from fresh coconut meat comprising:
drying continuously the coconut meat at a
temperature in the range 600C to 700C to break
the coconut milk emulsion; grinding the coconut
meat into the size range 80 to 100 mesh;
pressing the ground coconut meat to separate at
least some of the oil content thereof from a
residue; immersing and mixing the residue in
heated tap and coconut water at a temperature in
the range 550C to 650C; grinding further the
immersed ground coconut meat to form a 200 to
250 mesh slurry; mixing and agitating the slurry
continuously for from 1 5 to 20 minutes at a
temperature in the range 550C to 650C; and
separating a solid from the liquid in the agitated
slurry mixture, whereby flour can be extracted
from the solid and oil and/or protein can be
extracted from the liquid.
2. A process according to claim 1, in which
said solid is dried to produce coconut flour.
3. A process according to claim 1 or claim 2, in
which said liquid is separated further into an oil
phase and an aqueous phase:
4. A process according to claim 3, in which the
oil phase is deodorized to produce edible coconut
oil.
5. A process according to claim 1, in which a
protein precipitate in said liquid is allowed to
settle out.
6. A process according to claim 3, in which a
protein precipitate in said aqueous phase is
allowed to settle out.
7. A process according to claim 5 or claim 6, in
which said precipitate is dried to obtain a protein
powder.
8. A process for extracting flour from fresh
coconut meat comprising: drying continuously the
coconut meat at a temperature in the range 600C to 700C to break the coconut milk emulsion; grinding the dried coconut meat into the size range 80 to 100 mesh; pressing the ground coconut meat to separate at least some of the oil content thereof from a residue; immersing and mixing the residue with heated tap and coconut water at a temperature in the range 550C to 650C; grinding further the immersed ground coconut meat to form a 200 to 250 mesh slurry; mixing and agitating the slurry continuously from 1 5 to 20 minutes at a temperature in the range 550C to 650C; separating a solid from a liquid in the agitated mixture; and drying the solid to produce coconut flour.
9. A process for extracting oil from fresh coconut meat comprising: drying continuously the coconut meat at a temperature in the range 600C to 70"C to break the coconut milk emulsion; grinding the dried coconut meat into the size range 80 to 100 mesh; pressing the ground coconut meat to separate at least some of the oil content thereof from a residue; immersing and mixing the residue with heated tap and coconut water at a temperature in the range 550C to 650 C; grinding further the immersed ground coconut meat to form a 200 to 250 mesh slurry; mixing and agitating the slurry continuously from 1 5 to 20 minutes at a temperature in the range
550C to 650C; separating the solid from the
liquid in the agitated mixture; separating further
an oil phase from an aqueous phase liquid; and
deodorizing the oil phase to produce edible oil.
1 0. A process for extracting protein from
coconut meat comprising: drying continuously the
coconut meat at a temperature in the range 600C
to 700C to break the coconut milk emulsion; grinding the dried coconut meat into the size range 80 to 100 mesh; pressing the ground coconut meat to separate at least some of the oil content thereof from a residue; immersing and mixing the residue with heated tap and coconut water at a temperature in the range 550C to 650C; grinding further the immersed ground coconut meat to form 200 to 250 mesh slurry; mixing and agitating the slurry continuously from 1 5 to 20 minutes at a temperature in the range 550C to 650C; separating the solid from the liquid in the agitated mixture; allowing the waterprotein slurry to settle to obtain a precipitate; and drying the precipitate to obtain the protein.
11. A process for extracting flour, oil and/or protein from coconut meat, substantially as herein described with reference to the accompanying drawing.
12. Every novel feature and every novel combination of features described herein.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PH25335A PH20606A (en) | 1981-03-09 | 1981-03-09 | Process for extracting oil,protein and flour from fresh coconut meat |
Publications (2)
Publication Number | Publication Date |
---|---|
GB2094334A true GB2094334A (en) | 1982-09-15 |
GB2094334B GB2094334B (en) | 1985-01-03 |
Family
ID=19934705
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB8129503A Expired GB2094334B (en) | 1981-03-09 | 1981-09-30 | Extracting oil protein and flour from fresh coconut meat |
Country Status (4)
Country | Link |
---|---|
JP (1) | JPS57149398A (en) |
DE (1) | DE3137449A1 (en) |
GB (1) | GB2094334B (en) |
PH (1) | PH20606A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2603776A1 (en) * | 1986-09-12 | 1988-03-18 | Aubourg Raymond | Process for the industrial preparation of a coconut flour and new industrial food products prepared from this flour |
DE19857582B4 (en) * | 1998-12-14 | 2004-12-16 | ÖHMI Engineering GmbH | Process for the extraction of vegetable oils from oil-containing vegetable products |
EP1530909A1 (en) * | 2003-11-11 | 2005-05-18 | Werner Baensch | Process for making a vegetable food product from coconut |
US7364765B2 (en) * | 2003-07-18 | 2008-04-29 | Werner Baensch | Process for defatting coconut meat |
CN104824746A (en) * | 2015-04-13 | 2015-08-12 | 统一企业(中国)投资有限公司昆山研究开发中心 | Coconut juice beverage and production method thereof |
FR3034429A1 (en) * | 2015-04-02 | 2016-10-07 | Tahiti Bio | PROCESS FOR PRODUCING COCONUT OIL |
WO2018044232A1 (en) * | 2016-08-31 | 2018-03-08 | Integrated Food Processing Machinery Pte Ltd | Process of producing edible coconut products |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108395925A (en) * | 2018-03-22 | 2018-08-14 | 东莞市椰乡小镇实业发展有限公司 | A kind of preparation method of coconut oil |
-
1981
- 1981-03-09 PH PH25335A patent/PH20606A/en unknown
- 1981-09-21 DE DE19813137449 patent/DE3137449A1/en not_active Withdrawn
- 1981-09-30 GB GB8129503A patent/GB2094334B/en not_active Expired
- 1981-11-06 JP JP56178231A patent/JPS57149398A/en active Pending
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2603776A1 (en) * | 1986-09-12 | 1988-03-18 | Aubourg Raymond | Process for the industrial preparation of a coconut flour and new industrial food products prepared from this flour |
DE19857582B4 (en) * | 1998-12-14 | 2004-12-16 | ÖHMI Engineering GmbH | Process for the extraction of vegetable oils from oil-containing vegetable products |
US7364765B2 (en) * | 2003-07-18 | 2008-04-29 | Werner Baensch | Process for defatting coconut meat |
EP1530909A1 (en) * | 2003-11-11 | 2005-05-18 | Werner Baensch | Process for making a vegetable food product from coconut |
FR3034429A1 (en) * | 2015-04-02 | 2016-10-07 | Tahiti Bio | PROCESS FOR PRODUCING COCONUT OIL |
CN104824746A (en) * | 2015-04-13 | 2015-08-12 | 统一企业(中国)投资有限公司昆山研究开发中心 | Coconut juice beverage and production method thereof |
WO2018044232A1 (en) * | 2016-08-31 | 2018-03-08 | Integrated Food Processing Machinery Pte Ltd | Process of producing edible coconut products |
Also Published As
Publication number | Publication date |
---|---|
DE3137449A1 (en) | 1982-09-23 |
PH20606A (en) | 1987-02-24 |
GB2094334B (en) | 1985-01-03 |
JPS57149398A (en) | 1982-09-14 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PCNP | Patent ceased through non-payment of renewal fee |