SU577201A1 - Method of separating monoatomic aliphatic alcohols - Google Patents
Method of separating monoatomic aliphatic alcoholsInfo
- Publication number
- SU577201A1 SU577201A1 SU7502148533A SU2148533A SU577201A1 SU 577201 A1 SU577201 A1 SU 577201A1 SU 7502148533 A SU7502148533 A SU 7502148533A SU 2148533 A SU2148533 A SU 2148533A SU 577201 A1 SU577201 A1 SU 577201A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- separating
- aliphatic alcohols
- extraction
- monoatomic
- sample
- Prior art date
Links
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
Цепь изобреге ш - певышэние creneiffl извлечени спиртов и уменьшение энергетических затрат. Дл этого в качестве экстра гента - сложного эфира используют дибутилфталат . Способ осуществл ют следующим образом Экстракцию провод т в экстракционных делительных воронках емкостью ЗОО мл, Снабженных мешалкой. Посто нную температуру , колебани которой не превышают t.l°C поддерживают упьтра гермостатом. В чистую термостатированную делительную воронку загружают определенное количество исходной смеси и экстрагента. Воронку закр шают и содержимое ее в течение 30 мин перемешивают. По окончании экстракции до. биваютс установлени равновеси , т. е.Circuit izrebge sh - perene creneiffl extraction of alcohols and reducing energy costs. For this, dibutyl phthalate is used as an extragent of ester. The method is carried out as follows. Extraction is carried out in extraction separating funnels with a capacity of 50 ml, supplied with a stirrer. A constant temperature, the fluctuations of which do not exceed t.l ° C is maintained by a pressure thermostat. A certain amount of the initial mixture and extractant is loaded into a clean thermostated separating funnel. The funnel is closed and its contents are stirred for 30 minutes. At the end of the extraction before. equilibria, i.e.
Приход пробыThe arrival of the sample
Объем пробы, млSample volume, ml
Вес пробы, г полного расслоени и установлени резкой границы Между ними. Длительность этого процесса 2-3 часа. Фазы экстракта и рафината отдел ютс во взвешенные сухие колбы. Дл п тиступенчатой экстракции взвешенный ,измеренный, на каждой из п ти ступеней рафинат вновь загружают в депгительную воронку с новой порцией экстрагента . Материальный баланс одноступенчатой экстракции 3,7%-ного водного раствора метанола с кратностью дибутилфталата равной п ти, при 50°С, приведен IB табл. 1-3. Таблица 1The weight of the sample, g complete stratification and the establishment of a sharp boundary between them. The duration of this process is 2-3 hours. The extract and raffinate phases are separated into suspended dry flasks. For a five-step extraction weighted, measured, at each of the five stages, the raffinate is again loaded into a depressive funnel with a new batch of extractant. The material balance of a single-stage extraction of a 3.7% aqueous solution of methanol with a multiplicity of dibutyl phthalate equal to five, at 50 ° C, shows IB table. 1-3. Table 1
Исходна смесь № 1 Содержание метанола Дибу тилфталаг ПотериInitial mixture No. 1 Methanol content Dibu tilftalag Losses
Расход пробыSample flow
РафинатRaffinate
Содержание метанолаMethanol content
ЭкстрактExtract
Содержание метанолаMethanol content
Коэффициент распределевга Distribution coefficient
30,530.5
148,0 1.3148.0 1.3
Таблица 2,Table 2,
Объем пробъ, млVolume Try, ml
Вес пробы, гSample weight, g
2929
148,2148.2
О,3114Oh 3114
Материальный баланс одноступенчатой экстракции 3,96%-ного водного раствораThe material balance of single-stage extraction of a 3.96% aqueous solution
Таблица ЭTable E
этанола с кратностью дибутилфталата,рав. ной п ти, при 80 С, приведен в табл. 4-6,ethanol with the multiplicity of dibutyl phthalate, equ. Noah five, at 80 ° C, is given in Table. 4-6,
Таблица 4Table 4
Расход пробыSample flow
Раф,Rough,
«нет"not
Содержашге пропанолаContains propanol
ЭкстрактExtract
Содержание пропанолаPropanol content
Таблица 6Table 6
Тйбйица 7Tybyitsa 7
Таблица 8Table 8
Вес пробы, гSample weight, g
Объем npofei, млVolume of npofei, ml
16sixteen
101,7101.7
Материальный баланЬ одноступенчатой экстракции 5,bl7%-Boro водного раствора пропанола с кратностью йнбуталфталата, равной п т , при 80 С, приведен в табл. 20 7-9.The material balance of single-stage extraction 5, bl7% -Boro of an aqueous solution of propanol with an nbutalphthalate ratio of nt at 80 ° C is given in Table. 20 7-9.
Claims (3)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU7502148533A SU577201A1 (en) | 1975-06-23 | 1975-06-23 | Method of separating monoatomic aliphatic alcohols |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU7502148533A SU577201A1 (en) | 1975-06-23 | 1975-06-23 | Method of separating monoatomic aliphatic alcohols |
Publications (1)
Publication Number | Publication Date |
---|---|
SU577201A1 true SU577201A1 (en) | 1977-10-25 |
Family
ID=20624109
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU7502148533A SU577201A1 (en) | 1975-06-23 | 1975-06-23 | Method of separating monoatomic aliphatic alcohols |
Country Status (1)
Country | Link |
---|---|
SU (1) | SU577201A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4260836A (en) * | 1980-01-10 | 1981-04-07 | Sidney Levy | Solvent extraction of alcohols from water solutions with fluorocarbon solvents |
US4692432A (en) * | 1981-07-15 | 1987-09-08 | Georgia Tech Research Corporation | Two cycle process for producing fuel-grade ethanol from dilute aqueous mixtures |
-
1975
- 1975-06-23 SU SU7502148533A patent/SU577201A1/en active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4260836A (en) * | 1980-01-10 | 1981-04-07 | Sidney Levy | Solvent extraction of alcohols from water solutions with fluorocarbon solvents |
US4692432A (en) * | 1981-07-15 | 1987-09-08 | Georgia Tech Research Corporation | Two cycle process for producing fuel-grade ethanol from dilute aqueous mixtures |
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