SU520390A1 - Method of oil demulsification - Google Patents
Method of oil demulsificationInfo
- Publication number
- SU520390A1 SU520390A1 SU1759596A SU1759596A SU520390A1 SU 520390 A1 SU520390 A1 SU 520390A1 SU 1759596 A SU1759596 A SU 1759596A SU 1759596 A SU1759596 A SU 1759596A SU 520390 A1 SU520390 A1 SU 520390A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- emulsion
- demulsifier
- oil
- water
- oil demulsification
- Prior art date
Links
Landscapes
- Liquid Carbonaceous Fuels (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Description
или загущенным до т вердого состо ни д&эмульгатором ,or thickened to t verdogo state d & emulsifier,
I Деэмульгатор омьтаетс потоком эмульгсии и вследствие определенной растворимоети постепенно нм наноситс . После смеш& ,ни эмульсии с деэму ьгатором происходит известный процесс деэмульсадии нефти.I The demulsifier is washed with a stream of emulsification and, due to a certain solubility, it is gradually applied to the nm. After mix & Neither the emulsion with the deem generator takes place the well-known oil demulsification process.
В эависимостн от типа деэмульгатора, конструтргивныл. особенностей контейнера, технологии «швани эмульсией деэмульгатора , степени оастворимости реагента и ITJI, твердый или загущенный деэмульгатер мохдао приготовл ть в виде гранул, палочек или сплошной массы.In dependence on the type of demulsifier, constructive. the characteristics of the container, the technology of "shaving emulsion of the demulsifier, the degree of solubility of the reagent and ITJI, solid or thickened demulsifying agent Mohdao prepared in the form of granules, sticks or solid mass.
Расход реагента-деэмульгатора на ед ницу объема или веса эмульсии можно регулировать путем изменени площади омыва НИН эмульсией деэмульгатора или степени растворимости деамульгатора в компонентах эмульсии.The consumption of the demulsifier reagent per unit of volume or weight of the emulsion can be adjusted by changing the area washed by the NIN by the emulsion of the demulsifier or the degree of solubility of the demulsifier in the components of the emulsion.
Пример 1. Деэмупьсаци нефти Бит .киевского нефт ного месторождени со стойкой водонефг ной эмульсией, прошедшей процесс старени в течение 14 дней. Проду ци содержит 23% воды и 35S37 мг/л со лей.Example 1. De-oiling of the Bit. Kiev oil field with a stable water-non-emulsion emulsion that has undergone an aging process for 14 days. Products contain 23% of water and 35S37 mg / l of salt.
На ;.уСт«н6вке Зчз уравнительного бака нефть подают в контейнер, заполненный граOn; .уСт «n6vke Zchz leveling tank oil is fed into a container filled with
нулированным деэмульгатором, при атом нефгь омывает его. Затем ее подзергаюг турбулизации в течение ЗО мин и нахгоавл ют Б емкость на термообработку (50 С) в течение 5 час и отстой. ; После спуска отсто вшейс воды анализы нефти дают следующие резуль-гаты: вода 1,2%; соли 3600 мг/л.a zero demulsifier, with an atom nephgi washes it. Then its subzergation is turbulent for 30 minutes and the B heat container (50 ° C) is charged for 5 hours and sludge. ; After the descent of water from the bottom, the oil analyzes give the following results: water 1.2%; salts 3600 mg / l.
Пример 2. Деэмульсаци нефти со стойкой свежей водонефг ной эмульсией. , Содержание воды 28%, солей 4235 мг/л.Example 2. Oil emulsion with stable fresh water-in-water emulsion. The water content is 28%, salts 4235 mg / l.
Деэмульсадию провод т на установке по примеру 1, а техноло -и процесса отличаетс тем, что омывание нефгью деэму ьгато;ра в контейнере провод т дважды. Посйеотсто и спуска воды анализы нефти показььвают следующие результаты: вода 0,95%; соли 1850 мг/л.The emulsion is carried out in the installation of Example 1, and the process and process is characterized in that it washes nefgyu deem ygato and the container is held twice in the container. The analysis and descent of oil analyzes show the following results: water 0.95%; salts 1850 mg / l.
ФорFore
изобретени the invention
мулаmule
Способ деэмульсации нефти путем кон тактировани дви опцегос потока нефти с деэмульгатором, отличающийс тем, что, с целью упрощени процесса, используют Деэмульгатор в , например гранулированной, форме.The method of oil demulsification by contacting the engine oil stream with a demulsifier, characterized in that, in order to simplify the process, the demulsifier is used in, for example, granulated form.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU1759596A SU520390A1 (en) | 1972-03-14 | 1972-03-14 | Method of oil demulsification |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU1759596A SU520390A1 (en) | 1972-03-14 | 1972-03-14 | Method of oil demulsification |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU520390A1 true SU520390A1 (en) | 1976-07-05 |
Family
ID=20506625
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU1759596A SU520390A1 (en) | 1972-03-14 | 1972-03-14 | Method of oil demulsification |
Country Status (1)
| Country | Link |
|---|---|
| SU (1) | SU520390A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4417976A (en) * | 1981-01-14 | 1983-11-29 | Basf Aktiengesellschaft | Dewatering of petroleum-containing sludges with recovery of the oil component |
-
1972
- 1972-03-14 SU SU1759596A patent/SU520390A1/en active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4417976A (en) * | 1981-01-14 | 1983-11-29 | Basf Aktiengesellschaft | Dewatering of petroleum-containing sludges with recovery of the oil component |
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