RU2003106707A - INSTALLATION FOR DEMULSING OIL PRODUCTS BY POLYURETHANE - Google Patents

INSTALLATION FOR DEMULSING OIL PRODUCTS BY POLYURETHANE

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Publication number
RU2003106707A
RU2003106707A RU2003106707/15A RU2003106707A RU2003106707A RU 2003106707 A RU2003106707 A RU 2003106707A RU 2003106707/15 A RU2003106707/15 A RU 2003106707/15A RU 2003106707 A RU2003106707 A RU 2003106707A RU 2003106707 A RU2003106707 A RU 2003106707A
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RU
Russia
Prior art keywords
phase
stream
anhydrous
polymeric material
aqueous
Prior art date
Application number
RU2003106707/15A
Other languages
Russian (ru)
Other versions
RU2288770C2 (en
Inventor
Амин БЕНАХЕНУ
Жан-Пьер ПАРАН
Original Assignee
Энвайроментл Эплайд Рисерч Текнолоджи Хаус-Эрт (Канада) Корпорэйшн
Мэзон де Ресерш Аплике э де Текноложи ан Матьер Энвироменталь-Корпорасьон Эрт (Канада)
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
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Publication date
Priority claimed from GBGB0022013.7A external-priority patent/GB0022013D0/en
Application filed by Энвайроментл Эплайд Рисерч Текнолоджи Хаус-Эрт (Канада) Корпорэйшн, Мэзон де Ресерш Аплике э де Текноложи ан Матьер Энвироменталь-Корпорасьон Эрт (Канада) filed Critical Энвайроментл Эплайд Рисерч Текнолоджи Хаус-Эрт (Канада) Корпорэйшн
Publication of RU2003106707A publication Critical patent/RU2003106707A/en
Application granted granted Critical
Publication of RU2288770C2 publication Critical patent/RU2288770C2/en

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Claims (9)

1. Непрерывный способ разделения потока водной эмульсии, состоящей из однородной водной фазы и безводной дисперсионной фазы с целью получения первого потока, содержащего собранную безводную фазу, и получения второго потока, содержащего собранную водную фазу с приемлемым уровнем содержания безводной фазы, при этом в ходе осуществления названного непрерывного способа:1. A continuous method for separating a stream of an aqueous emulsion consisting of a homogeneous aqueous phase and an anhydrous dispersed phase in order to obtain a first stream containing a collected anhydrous phase and obtaining a second stream containing a collected aqueous phase with an acceptable level of anhydrous phase, while during the implementation named continuous method: (a) поток водной эмульсии вводят в контакт с первым веществом на основе полимерного материала в большой площадью поверхности;(a) the aqueous emulsion stream is contacted with a first material based on a polymeric material in a large surface area; (b) первое вещество на основе полимерного материала достигает состояния насыщенности безводной фазой потока эмульсии;(b) the first substance based on a polymeric material reaches a saturation state of the anhydrous phase of the emulsion stream; (c) подача потока водной эмульсии не прекращается до момента формирования раздельной безводной фазы;(c) the flow of the aqueous emulsion stream does not stop until a separate anhydrous phase is formed; (d) отделяют отделенную безводную фазу, полученную на стадии (с) без остановки потока водной эмульсии;(d) separating the separated anhydrous phase obtained in step (c) without stopping the flow of the aqueous emulsion; (e) осуществляют сбор отделенной безводной фазы, полученной на стадии (d) без остановки потока водной эмульсии;(e) collecting the separated anhydrous phase obtained in step (d) without stopping the flow of the aqueous emulsion; (f) осуществляют сбор потока очищенной водной фазы без остановки потока водной эмульсии; и(f) collecting the purified aqueous phase stream without stopping the aqueous emulsion stream; and (g) повторно осуществляют стадии (а)-(f) с целью введения потока очищенной водной фазы в контакт с, по меньшей мере, вторым веществом на основе полимерного материала с большой площадью поверхности до тех пор, пока содержание безводной фазы в потоке собранной водной фазы не достигнет приемлемого уровня.(g) steps (a) to (f) are repeated to bring the purified aqueous phase stream into contact with at least a second polymer material material with a large surface area until the anhydrous phase content in the collected aqueous stream phase will not reach an acceptable level. 2. Способ по п.1, в котором полимер, используемый в полимерном материале, выбирают из группы, включающей полиуретан, полипропилен, полистирол, полиэфир и полиэтилен.2. The method according to claim 1, in which the polymer used in the polymeric material is selected from the group comprising polyurethane, polypropylene, polystyrene, polyester and polyethylene. 3. Способ по п.2, в котором полимер, используемый в полимерном материале, представляет собой полиуретан.3. The method according to claim 2, in which the polymer used in the polymer material is a polyurethane. 4. Способ по п.1, в котором полимерный материал с большой площадью поверхности имеет форму, выбранную из группы, включающей пену и крошку с большой площадью поверхности.4. The method according to claim 1, in which the polymer material with a large surface area has a shape selected from the group comprising foam and crumb with a large surface area. 5. Способ по п.4, в котором полимерный материал с большой площадью поверхности представляет собой полимерную пену в виде частиц.5. The method according to claim 4, in which the polymer material with a large surface area is a polymer foam in the form of particles. 6. Способ по п.1, в котором используют множество веществ на основе полимерного материала, в контакт с каждым из которых последовательно вступает поток, а сбор отделенной безводной фазы осуществляют после прохождения через каждое вещество на основе полимерного материала.6. The method according to claim 1, in which a variety of substances based on a polymeric material are used, a stream comes into contact with each of them, and the collection of the separated anhydrous phase is carried out after passing through each substance based on a polymeric material. 7. Способ по п.1, в котором используют множество веществ на основе полимерного материала, поток последовательно контактирует с каждым из них, а сбор отделенной безводной фазы осуществляют после прохождения через каждое вещество на основе полимерного материала за исключением последнего вещества, из которого осуществляют сбор отделенной безводной фазы.7. The method according to claim 1, in which a plurality of substances based on a polymeric material are used, the flow is in contact with each of them sequentially, and the collection of the separated anhydrous phase is carried out after passing through each substance based on a polymeric material with the exception of the last substance from which they are collected separated anhydrous phase. 8. Способ по п.1, в котором используют последовательность веществ на основе полимерных материалов, при этом, по меньшей мере, последнее вещество на основе полимерного материала представляет собой пенополиуретан Kozlowski.8. The method according to claim 1, in which a sequence of substances based on polymeric materials is used, at least the last substance based on a polymeric material is Kozlowski polyurethane foam. 9. Способ по п.1, дополнительно включающий осуществляемые перед стадией (а) стадии предварительной очистки, на которых:9. The method according to claim 1, further comprising pre-treatment steps carried out before step (a), in which: (h) из капель безводной фазы достаточного для коалесценции размера формируют раздельную безводную фазу;(h) a separate anhydrous phase is formed from droplets of an anhydrous phase of sufficient size for coalescence; (i) собирают раздельную безводную фазу; и(i) collecting a separate anhydrous phase; and (j) собирают водную фазу и используют ее в качестве потока на стадии (а).(j) collecting the aqueous phase and using it as a stream in step (a).
RU2003106707/15A 2000-09-07 2001-09-07 Method of separation of water emulsion flow and plant for realization of this method RU2288770C2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GBGB0022013.7A GB0022013D0 (en) 2000-09-07 2000-09-07 Polyurethane oil de-emulsification unit
CA0022013.7 2000-09-07

Publications (2)

Publication Number Publication Date
RU2003106707A true RU2003106707A (en) 2004-09-20
RU2288770C2 RU2288770C2 (en) 2006-12-10

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US (4) US7416667B2 (en)
EP (1) EP1322393B1 (en)
JP (1) JP3619824B2 (en)
KR (1) KR100493812B1 (en)
CN (1) CN1289166C (en)
AT (1) ATE385846T1 (en)
AU (1) AU2001291548A1 (en)
BR (1) BR0113888A (en)
CA (1) CA2421076C (en)
DE (1) DE60132792D1 (en)
DZ (1) DZ3436A1 (en)
GB (1) GB0022013D0 (en)
MX (1) MXPA03002001A (en)
NO (2) NO329083B1 (en)
RU (1) RU2288770C2 (en)
WO (1) WO2002020115A2 (en)

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