CO4700336A1 - PROCEDURE FOR EXTRACTING OIL FROM PLANT PARTS - Google Patents
PROCEDURE FOR EXTRACTING OIL FROM PLANT PARTSInfo
- Publication number
- CO4700336A1 CO4700336A1 CO96023633A CO96023633A CO4700336A1 CO 4700336 A1 CO4700336 A1 CO 4700336A1 CO 96023633 A CO96023633 A CO 96023633A CO 96023633 A CO96023633 A CO 96023633A CO 4700336 A1 CO4700336 A1 CO 4700336A1
- Authority
- CO
- Colombia
- Prior art keywords
- oil
- reactor vessel
- solvent
- plant material
- combination
- Prior art date
Links
- 238000000034 method Methods 0.000 title abstract 3
- 239000002904 solvent Substances 0.000 abstract 10
- 239000003921 oil Substances 0.000 abstract 8
- 241000196324 Embryophyta Species 0.000 abstract 7
- 239000000463 material Substances 0.000 abstract 6
- 239000007788 liquid Substances 0.000 abstract 4
- 235000017060 Arachis glabrata Nutrition 0.000 abstract 1
- 244000105624 Arachis hypogaea Species 0.000 abstract 1
- 235000010777 Arachis hypogaea Nutrition 0.000 abstract 1
- 235000018262 Arachis monticola Nutrition 0.000 abstract 1
- 235000014698 Brassica juncea var multisecta Nutrition 0.000 abstract 1
- 240000002791 Brassica napus Species 0.000 abstract 1
- 235000011293 Brassica napus Nutrition 0.000 abstract 1
- 235000006008 Brassica napus var napus Nutrition 0.000 abstract 1
- 240000000385 Brassica napus var. napus Species 0.000 abstract 1
- 235000006618 Brassica rapa subsp oleifera Nutrition 0.000 abstract 1
- 235000000540 Brassica rapa subsp rapa Nutrition 0.000 abstract 1
- 235000004977 Brassica sinapistrum Nutrition 0.000 abstract 1
- 240000002943 Elettaria cardamomum Species 0.000 abstract 1
- 244000068988 Glycine max Species 0.000 abstract 1
- 235000010469 Glycine max Nutrition 0.000 abstract 1
- 240000007594 Oryza sativa Species 0.000 abstract 1
- 235000007164 Oryza sativa Nutrition 0.000 abstract 1
- 244000044822 Simmondsia californica Species 0.000 abstract 1
- 235000004433 Simmondsia californica Nutrition 0.000 abstract 1
- 240000008042 Zea mays Species 0.000 abstract 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 abstract 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 abstract 1
- 235000005300 cardamomo Nutrition 0.000 abstract 1
- 239000000470 constituent Substances 0.000 abstract 1
- 235000005822 corn Nutrition 0.000 abstract 1
- 238000004925 denaturation Methods 0.000 abstract 1
- 230000036425 denaturation Effects 0.000 abstract 1
- 239000011261 inert gas Substances 0.000 abstract 1
- 239000000203 mixture Substances 0.000 abstract 1
- 239000002245 particle Substances 0.000 abstract 1
- 239000013618 particulate matter Substances 0.000 abstract 1
- 235000020232 peanut Nutrition 0.000 abstract 1
- 239000010773 plant oil Substances 0.000 abstract 1
- 235000009566 rice Nutrition 0.000 abstract 1
- 238000000926 separation method Methods 0.000 abstract 1
- 230000008016 vaporization Effects 0.000 abstract 1
- 238000009834 vaporization Methods 0.000 abstract 1
Landscapes
- Fats And Perfumes (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Abstract
Un proceso para extraer aceite de plantas que contienen aceite,el procedimiento que comprende los pasos de: - Colocar material de plantas que contiene aceite seleccionado a partir de un grupo que consiste de salvado de arroz, maíz, naba/canola, soya, cardamomo, torta de cacahuate preprensada, torta de jojoba pre-pensada y benaf. - Retirar aire del recipiente reactor para establecer un primer vació parcial de 58.5 a 60.6 kPa absolutos (8.5 a 8.8.Psia) introduciendo un gas inerte bajo presión para desechar o descargar aire adicional, y estableciendo un segundo vacío parcial de 58.5 a 60.6 kPa absolutos (8.5 a 8.8.psia). - Introducir dentro del recipiente reactor un solvente líquido que tiene la capacidad por disolver aceite de material de plantas, el solvente líquido se mantiene a una temperatura entre 20 y 22.2°C (68 y 72°F). - Permitir que el solvente líquido contacte el material de plantas un tiempo suficiente para disolver una porción sustancial del aceite de material de plantas. - Introducir vapores de solvente presurizados al fondo del recipiente reactor para ocacionar la mezcla del material de plantas en la combinación de solvente y aceite, facilitando de esta manera la separación de materia particulada fina de las partículas más pesadas en el recipiente reactor. - Introducir vapores de solvente calentados a presión en la parte superior del recipiente reactor, mientras que la combinación de solvente líquido y aceite se retira del fondo del recipiente reactor.- transferir la combinación de solvente y aceite de material de plantas del recipiente reactor a un recipiente separador y luego, evaporar el solvente dentro del recipiente reactor a una temperatura suficiente para provocar vaporización del solvente, mientras se previene la desnaturalización de los componentes constituyentes del aceite de plantas.A process to extract oil from oil-containing plants, the procedure comprising the steps of: - Placing oil-containing plant material selected from a group consisting of rice bran, corn, turnip / canola, soybean, cardamom, pre-pressed peanut cake, pre-thought jojoba cake and benaf. - Remove air from the reactor vessel to establish a first partial vacuum of 58.5 to 60.6 kPa absolute (8.5 to 8.8 psia) by introducing an inert gas under pressure to discard or discharge additional air, and establishing a second partial vacuum of 58.5 to 60.6 kPa absolute (8.5 to 8.8.psia). - Introduce into the reactor vessel a liquid solvent that has the capacity to dissolve oil from plant material, the liquid solvent is kept at a temperature between 20 and 22.2 ° C (68 and 72 ° F). - Allow the liquid solvent to contact the plant material long enough to dissolve a substantial portion of the plant material oil. - Introduce pressurized solvent vapors to the bottom of the reactor vessel to bring the mixture of plant material into the combination of solvent and oil, thus facilitating the separation of fine particulate matter from the heavier particles in the reactor vessel. - Introduce pressurized solvent vapors into the top of the reactor vessel, while the combination of liquid solvent and oil is removed from the bottom of the reactor vessel - transfer the combination of solvent and plant material oil from the reactor vessel to a separator container and then evaporate the solvent inside the reactor vessel at a temperature sufficient to cause vaporization of the solvent, while preventing denaturation of the constituent components of the plant oil.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CO96023633A CO4700336A1 (en) | 1996-05-10 | 1996-05-10 | PROCEDURE FOR EXTRACTING OIL FROM PLANT PARTS |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CO96023633A CO4700336A1 (en) | 1996-05-10 | 1996-05-10 | PROCEDURE FOR EXTRACTING OIL FROM PLANT PARTS |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CO4700336A1 true CO4700336A1 (en) | 1998-12-29 |
Family
ID=40930051
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CO96023633A CO4700336A1 (en) | 1996-05-10 | 1996-05-10 | PROCEDURE FOR EXTRACTING OIL FROM PLANT PARTS |
Country Status (1)
| Country | Link |
|---|---|
| CO (1) | CO4700336A1 (en) |
-
1996
- 1996-05-10 CO CO96023633A patent/CO4700336A1/en unknown
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