SU361194A1 - METHOD OF CONTINUOUS OIL REFINATION - Google Patents
METHOD OF CONTINUOUS OIL REFINATIONInfo
- Publication number
- SU361194A1 SU361194A1 SU1472837A SU1472837A SU361194A1 SU 361194 A1 SU361194 A1 SU 361194A1 SU 1472837 A SU1472837 A SU 1472837A SU 1472837 A SU1472837 A SU 1472837A SU 361194 A1 SU361194 A1 SU 361194A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- oil
- mixing
- alkali
- refination
- excess
- Prior art date
Links
Landscapes
- Fats And Perfumes (AREA)
Description
1one
Изобретение относитс к области масложирОБОй промышленности, в частности к способам непрерывной рафинации масел.The invention relates to the field of oil and fat industry, in particular to methods for continuous refining of oils.
Известен способ непрерывной рафинации масел, например хлопкового масла, путем смешени .масла или его мисцеллы с водным раствором щелочи, вз тым в избытке против теоретически необходимого количества.A known method for continuous refining of oils, for example cottonseed oil, by mixing oil or miscella with an aqueous solution of alkali, taken in excess against the theoretically necessary amount.
Предлагаемый способ отличаетс от известного тем, что смешение осуществл ют в турбулентном потоке. Это позвол ет интенсифицировать процесс и улучшить качество рафината . Концентраци щелочи составл ет преимущественно 500-600 г1л, а избыток щелочи - 0,3-1,0% от веса масла. Врем смешени желательно поддерживать не более 1 мин.The proposed method differs from the known one in that the mixing is carried out in a turbulent flow. This allows to intensify the process and improve the quality of the raffinate. The alkali concentration is predominantly 500-600 g1l, and the excess alkali is 0.3-1.0% by weight of the oil. Mixing time is desirable to maintain no more than 1 min.
Способ заключаетс в следующем.The method is as follows.
Смещивают .масло или мисцеллу в турбулентном потоке с водным раствором щелочи концентрацией 500-600 г/л, вз тым в избытке 0,3-1%, от веса масла против теоретически необходимого количества при температуре 20- 25°С в течение-неболее 1 мин. Нагревают полученную смесь до также в турбулентном потоке в течение 30-60 сек, обводн ют смесь масла с соапстоком также в турбулентном потоке в течение 30-60 сек (количество воды обводнени определ ют из расчета доведени концентрации до 120-130 г/л) и раздел ют фазы.Oil or miscella is displaced in a turbulent flow with an aqueous solution of alkali with a concentration of 500-600 g / l, taken in an excess of 0.3-1%, by weight of the oil against the theoretically required amount at a temperature of 20-25 ° C for less than 1 min The resulting mixture is heated to also in a turbulent flow for 30-60 seconds, the mixture of oil and soap stock is watered also in a turbulent flow for 30-60 seconds (the amount of water in the flood is determined from the calculation of concentration to 120-130 g / l) and phase separated.
Такой способ рафинации за счет использовани условий турбулентного потока обеспечивает получение нейтрализованного маслаThis method of refining through the use of turbulent flow conditions provides a neutralized oil.
(или мисцеллы) в одну стадию в течение 5-(or miscella) in one stage for 5-
30 мин, при этом цветность масла составл ет30 minutes, while the color of the oil is
5-10 кр. ед. в слое, равном 13,5 см.5-10 cr. units in a layer equal to 13.5 cm
Пример. Исходное масло подвергаетс Example. The original oil is subjected to
однократной рафинации в мисцелле с концен-. трацией масла 40-50% путем смешени в турбулентном потоке при 20-25°С в течение 25-30 сек с раствором щелочи с концентрацией 500 г/л (при расходе ее 12 кг на 1 г .масла ), нагревают до 65-70°С, обводн ют соапсток и раздел ют фазы.single refining in miscella with a concentration of-. Traction of oil 40-50% by mixing in a turbulent flow at 20-25 ° C for 25-30 seconds with an alkali solution with a concentration of 500 g / l (at a flow rate of 12 kg per 1 g. oil), is heated to 65-70 ° C, water flow is flooded and the phases are separated.
Полученные результаты приведены в таблице .The results are shown in the table.
Предмет изобретени Subject invention
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU1472837A SU361194A1 (en) | 1970-09-07 | 1970-09-07 | METHOD OF CONTINUOUS OIL REFINATION |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU1472837A SU361194A1 (en) | 1970-09-07 | 1970-09-07 | METHOD OF CONTINUOUS OIL REFINATION |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU361194A1 true SU361194A1 (en) | 1972-12-07 |
Family
ID=20456949
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU1472837A SU361194A1 (en) | 1970-09-07 | 1970-09-07 | METHOD OF CONTINUOUS OIL REFINATION |
Country Status (1)
| Country | Link |
|---|---|
| SU (1) | SU361194A1 (en) |
-
1970
- 1970-09-07 SU SU1472837A patent/SU361194A1/en active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| FR772811A (en) | Process for the production of non-detonating gasoline | |
| SU361194A1 (en) | METHOD OF CONTINUOUS OIL REFINATION | |
| SU386907A1 (en) | METHOD FOR ISOLATION OF FORMIC ACID | |
| SU87455A1 (en) | Method for the production of pasteurized oil in a sealed container | |
| FR597408A (en) | Continuous process of juice extraction by diffusion | |
| DE653201C (en) | Process for the production of hydroquinone | |
| SU404458A1 (en) | METHOD OF MANUFACTURE OF HEATED OIL | |
| SU982641A1 (en) | Method of preparing sugar colour for production brandy-type alcohol | |
| SU94628A1 (en) | A method of making sour butter | |
| SU475144A1 (en) | The method of obtaining butter from high fat cream | |
| SU98874A1 (en) | Method of making artificial parchment for sausages from vegetable parchment | |
| SU61254A1 (en) | The method of preparation of butter substitute for the production of ice cream | |
| SU81082A1 (en) | The method of cleaning juice with a reduced amount of lime | |
| US1749463A (en) | Process for obtaining sulphonation products from polymerized fats or oils or the acids thereof | |
| GB426049A (en) | Improvements in or relating to the improvement of cream | |
| SU439473A1 (en) | The method of obtaining the mixed phosphates of sodium, potassium and aluminum | |
| GB671656A (en) | Improvements in or relating to butter and butter process | |
| FR1027650A (en) | Process for the production of vat dyes of the phthalocyanine series | |
| JPS574924A (en) | Production of reddened ginseng | |
| FR580790A (en) | Process for the preparation of vat dyes starting from 2. 2-dibenzanthronyls or dibenzanthrones | |
| FR779459A (en) | Process and apparatus perfected for the saturation, by carbonic acid, of all liquids and beverages | |
| GB575160A (en) | A milk food product and process of manufacturing same | |
| GB508471A (en) | Improved manufacture of butter | |
| GB638370A (en) | Improvements in or relating to apparatus for producing milk fat concentrate | |
| FR597242A (en) | Process for the preparation of new dyes for tanks of the perylene series |