SU59845A1 - The method of obtaining drying oils - Google Patents
The method of obtaining drying oilsInfo
- Publication number
- SU59845A1 SU59845A1 SU876A SU876A SU59845A1 SU 59845 A1 SU59845 A1 SU 59845A1 SU 876 A SU876 A SU 876A SU 876 A SU876 A SU 876A SU 59845 A1 SU59845 A1 SU 59845A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- superheated steam
- drying oils
- fat
- obtaining drying
- acids
- Prior art date
Links
- 238000000034 method Methods 0.000 title description 12
- 238000001035 drying Methods 0.000 title description 8
- 239000003921 oil Substances 0.000 title description 7
- 239000003925 fat Substances 0.000 description 11
- 235000019198 oils Nutrition 0.000 description 6
- 239000003054 catalyst Substances 0.000 description 5
- 239000002253 acid Substances 0.000 description 4
- 150000007513 acids Chemical class 0.000 description 4
- 235000014113 dietary fatty acids Nutrition 0.000 description 4
- 229930195729 fatty acid Natural products 0.000 description 4
- 239000000194 fatty acid Substances 0.000 description 4
- 150000004665 fatty acids Chemical class 0.000 description 4
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 3
- 239000011630 iodine Substances 0.000 description 3
- 229910052740 iodine Inorganic materials 0.000 description 3
- 238000004821 distillation Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 239000000344 soap Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 1
- 235000010676 Ocimum basilicum Nutrition 0.000 description 1
- 240000007926 Ocimum gratissimum Species 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 238000003776 cleavage reaction Methods 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 230000002255 enzymatic effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 235000021323 fish oil Nutrition 0.000 description 1
- 229940013317 fish oils Drugs 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 235000021388 linseed oil Nutrition 0.000 description 1
- 239000000944 linseed oil Substances 0.000 description 1
- 239000011702 manganese sulphate Substances 0.000 description 1
- 235000007079 manganese sulphate Nutrition 0.000 description 1
- SQQMAOCOWKFBNP-UHFFFAOYSA-L manganese(II) sulfate Chemical compound [Mn+2].[O-]S([O-])(=O)=O SQQMAOCOWKFBNP-UHFFFAOYSA-L 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000007127 saponification reaction Methods 0.000 description 1
- 230000007017 scission Effects 0.000 description 1
- 239000011973 solid acid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000002966 varnish Substances 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Manufacture And Refinement Of Metals (AREA)
- Fats And Perfumes (AREA)
Description
Известен р д патентов, например, герм., пат. № 272465 и № 273347, в которых предлагаетс , путем обработки рыбьих жиров и Борваии перегретым паром, получать высыхающие масла и заменителИ льн ной олифы.A number of patents are known, for example, Germ., Pat. No. 272465 and No. 273347, in which it is proposed, by treating fish oil and Borvaia with superheated steam, to obtain drying oils and replaceable drying oil.
Процесс предлагали осуществл ть nyTeiM расщеплени жиров и перегонки жировых кислот перегретым паром (температура 375-400°) в течение 25- 30 часов. Согласно герм, пат/ № 282306 дл ускорени процесса и увеличени выхода рекомендуетс проводить процесс под вакуумом. Мо-жно также жир, до обработки перегретым парам, подвергать расщеплеиню в автоклаве в присутствии или сульфата марганца или щелочных земель и тому подобных веществ (герм. пат. № 273347), т. е. в данном случае обработке перегретым паром предществует са1М осто тельный лроцесс нагревани ма-сел с водой под давлением.The process suggested nyTeiM splitting fats and distilling fatty acids with superheated steam (temperature 375-400 °) for 25-30 hours. According to Germany, Pat. No. 282306, it is recommended to carry out the process under vacuum to speed up the process and increase the yield. Fat can also be applied, before treatment with superheated vapors, to undergo splitting in an autoclave in the presence of either manganese sulphate or alkaline earths and similar substances (germ. Pat. No. 273347), i.e., in this case, pre-treatment with superheated steam The process of heating ma-sat with water under pressure.
Точ1но так же согласно герм, патенту Ao 276430 предлагаетс предварительное расщепление ферментативным путем.Similarly, according to Germ, patent Ao 276430 proposes a preliminary digestion by enzymatic means.
Известна также обработка жиров перегретым паром в присутствии катали зат орав.The treatment of fats with superheated steam in the presence of catalysts is also known.
Согласно предлагаемому способу, при котором процесс предварительногоAccording to the proposed method, in which the process of preliminary
расщеплени и обработка перегретым паром совмещаютс одной операции, обработка перегретым паром проводитс в присутствии катализаторов СаО, ZnO, МпОг или РЬО.splitting and treatment with superheated steam are combined in a single operation; treatment with superheated steam is carried out in the presence of CaO, ZnO, MpOg or PHO catalysts.
Катализатор в виде суспензии ввод т в жир в количестве до %, далее подогре1вают жир и начинают пропускать перегретый до 300-400° пар. Со временем введенные окислы раствор ютс (образу соли: жирных кислот ) « начинает происходить Интенсивна отгонка более предельных кислот.The catalyst in the form of a suspension is introduced into the fat in an amount up to%, then the fat is heated and the steam that is overheated to 300-400 ° C is started to pass. Over time, the introduced oxides dissolve (to form the salt: fatty acids) "begins to occur. Intensive distillation of more limiting acids occurs.
Вместе продолжительной обработки, предусмотренной указанными германскими патентами, процесс по предлагаемому способу заканчиваетс в 3- 5 часов. В результате получают оксло хорощо высыхающего жира в остатке и ОКОло 35-40% твердых жировых кислот (титр 34°), пригодных дл мыловарени .Together, the lengthy processing provided for by said German patents, the process according to the proposed method ends in 3-5 hours. As a result, an oxlo horosho drying oil is obtained in the residue and OKO is 35-40% of solid fatty acids (titer 34 °) suitable for soap making.
Этот процесс, как показали опыты, пригоден также и дл обработки полувысыхающих и невысыхающих растительных масел, например, хлопкового и др.Experiments have shown that this process is also suitable for the treatment of semi-drying and non-drying vegetable oils, for example, cotton and other oils.
Пример. В алюминиевый куб, снабженный электрообогрево(м и подводом перегретого пара, загружают 1000 г ивасевого жира с йодным числом 164,8 и 10 г ОКИСИ1 циика н включают нагрев. После того, как температура жира достигнет 180°, в куб пускают перегретый пар с температурой 300-310°. Через 20 мин. температура жира достигает 285°, после чего при непрекращающейс по|даче перегрето, го пара температуру поддерживают в пределах 275-285°. Процесс селективного расщеплени жира и отгонки более Насыщенных кислот продолжаетс около 3 часов.Example. An aluminum cube equipped with electrical heating (m and supply of superheated steam is charged with 1000 g of ivase fat with an iodine number of 164.8 and 10 g of OXID) and heat is turned on. 300-310 ° C. After 20 minutes the temperature of the fat reaches 285 °, after which, with an uninterrupted superheated steam, the temperature is maintained within 275-285 ° .The process of selective cleavage of fat and distillation of more saturated acids lasts about 3 hours.
В результате обработки жира получаетс 42,5% твердых кислот и 52,5% остатка в кубе (полимеризат).As a result of fat processing, 42.5% of solid acids and 52.5% of the residue in the bottom are obtained (polymerizate).
Кислоты характеризуютс белым цветОМ, титром 34°, числом омылени 197,7 и иод ым числом 77,6; содержание неомыл емых 1,54%. Из этих кислот можно получить светлое твердое мыло, отличающеес хорошей пенистостью .- ; Acids are characterized by white color, titer 34 °, saponification number 197.7 and iodine number 77.6; the neat content is 1.54%. From these acids it is possible to obtain a light solid soap, characterized by good foaminess. -;
XapaKfepHCtHKa остатка в кубе: ,13, число омыле .Л«XapaKfepHCtHKa residue in the cube:, 13, the number of saponified .L "
ни - 172,04, йодное ЧИСЛО - 97,07; цвет продукта аналогичен исходному ивасевому жиру. Дл получени олифы к полимеризату добавл ют сиккативы и уайт-спирит 1ДО мал рной в зкости . Получаема таким образом олифа высыхает менее, чем за 20 часов и дает прозрачную аветлую пленку, по твердости превышающую таковую из льн ного масла.neither - 172.04, iodine NUMBER - 97.07; the color of the product is similar to the original and basil fat. Siccativa and mineral spirit 1DO of low viscosity are added to the polymer to obtain a varnish. The drying oil obtained in this way dries in less than 20 hours and gives a transparent cast film, which is more hard than that of linseed oil.
Предмет изобретени .The subject matter of the invention.
Способ получени высыхающих масел из рыбьих жиров, ворвапи и тому подобных жирав путем обработки их перегретым паром дл отгонки насыщенных фракций жировых кислот вприсутствии Катализаторов, о т л и ч а ю щи йен тем, что в качестве катализаторов примен ют ZnO, СаО, МпО., ил« РЬО.The method of obtaining drying oils from fish oils, blubber and the like fats by treating them with superheated steam to distill the saturated fractions of fatty acids in the presence of Catalysts, in particular, using ZnO, CaO, MnO as catalysts. , silt "PYO.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU876A SU59845A1 (en) | 1937-05-13 | 1937-05-13 | The method of obtaining drying oils |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU876A SU59845A1 (en) | 1937-05-13 | 1937-05-13 | The method of obtaining drying oils |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU877A Division SU58073A1 (en) | 1938-07-11 | 1938-07-11 | Device for automatically feeding stamped writing pens from store to machine for further processing |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU59845A1 true SU59845A1 (en) | 1940-11-30 |
Family
ID=48241866
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU876A SU59845A1 (en) | 1937-05-13 | 1937-05-13 | The method of obtaining drying oils |
Country Status (1)
| Country | Link |
|---|---|
| SU (1) | SU59845A1 (en) |
-
1937
- 1937-05-13 SU SU876A patent/SU59845A1/en active
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