PL4938B1 - A method and apparatus for separating the phases of emulsions, especially oil phases, using an electric current. - Google Patents
A method and apparatus for separating the phases of emulsions, especially oil phases, using an electric current. Download PDFInfo
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- PL4938B1 PL4938B1 PL4938A PL493824A PL4938B1 PL 4938 B1 PL4938 B1 PL 4938B1 PL 4938 A PL4938 A PL 4938A PL 493824 A PL493824 A PL 493824A PL 4938 B1 PL4938 B1 PL 4938B1
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- Prior art keywords
- voltage
- emulsions
- phases
- effective
- generator
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- 239000000839 emulsion Substances 0.000 title claims description 21
- 239000003208 petroleum Substances 0.000 claims description 5
- 238000005191 phase separation Methods 0.000 claims 1
- 238000000034 method Methods 0.000 description 6
- 238000000926 separation method Methods 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000001105 regulatory Effects 0.000 description 1
- 231100000486 side effect Toxicity 0.000 description 1
Description
Wynalazek niniejszy dotyczy sposobu rozdzielania emulsyj, a zwlaszcza nafto¬ wych zapomoca pradu elektrycznego, tu¬ dziez odpowiedniego aparatu.Wiadomo juz, ze pewne emulsje, a w szczególnosci emulsje naftowe zatrzymuja czesc zawartej w sobie wody. Czyniono liczne próby celem pokonania trudnosci i oddzielenia wody badzto dzialaniem si¬ ly ciezkosci, badz sposobami innemi. W wielu z tych procesów posilkowano sie pra¬ dem elektrycznym.Znana jest juz metoda rozdzielania emulsyj, w mysl której prad jedno lub wie¬ lofazowy ograniczano i prostowano zapo¬ moca rurki zaworowej. Proces ten opiera sie na zastosowaniu pradu tetniacego jed¬ nokierunkowego o Wysokiem napieciu, któ¬ ry istotnie zapewnia szybkie rozdzielanie emulsyj dzieki szybko nastepujacym po so¬ bie impulsom pradu o znacznem napieciu.Natezenie pradu reguluje sie w celu unie¬ zaleznienia go od oporu obrabianego plynu.Sposób ten posiada powazne zalety, w praktyce jednak napotyka na znaczne trud¬ nosci.Przedewszystkiem pojemnosc zaworów dzisiejszych jest ograniczona, wobec czegobianej emulsji (dla napiecia E), wartosc e- nergji niezbednej do rozdzielenia emulsji czyli energja = — = -^ Gdy rozdzielanie uskuteczni sie zapo- moca pradu zmiennego o przebiegu sinusoi¬ dalnym lub prawie sinusoidalnym, dla któ¬ rego/równa sie J/2, zuzycie energji bedzie sie równalo —^- t. j. skutek techniczny pro¬ cesu wzrasta, jak potega pierwsza, zuzy¬ cie zas energji jest proporcjonalne do kwa¬ dratu zastosowanego napiecia maksymal¬ nego, wskutek czego proces pozostaje ekonomicznie niekorzystnym, dopóki opór emulsji nie jest bardzo wielki, Ta okolicz¬ nosc nie zachodzi jednak wogóle w wy¬ padku obróbki emulsyj wodnych. Stad ply¬ na wady zastosowania znanych sposobów rozdzielania emulsyj.Zgodnie z wynalazkiem niniejszym do rozdzielania emulsyj stosuje sie prad tetnia¬ cy o napieciu maksymalnem przekraczaja- cem co najmniej dwukrotnie, a najpraktycz¬ niej 5 do 10 krotnie napiecie skuteczne; to znaczy, iz wskazany powyzej czynnik moze sie równac okolo 5, Zuzycie energji równa sie przeto wów- czas —— a dla /, równajacego sie 10, zuzy- cie energji wyniesie tylko —— zamiast —— w wypadku zwyklego pradu zmien- 2j nego, Widocznem jest przeto, ze wystar¬ cza 8%, a nawet 2% mocy stosowanej nor¬ malnie.Elektrolityczne zjawisko uboczne, za¬ chodzace w wypadku pradu tetniacego, usu¬ wa tutaj prad zmienny tetniacy w jednym tylko kierunku w sposób taki, ze czesc do¬ datnia krzywej posiada napiecie maksy¬ malne 5 — 10 krotnie wieksze od dodatnie¬ go napiecia skutecznego, a ujemna polowa fali napiecie zlekka zmienne, ale bez wierz¬ cholków, tak iz skuteczne napiecie ujem¬ ne równa sie skutecznemu napieciu dodat¬ niemu.Rzecz prosta, ze sposób i aparat opisa¬ ne powyzej i scharakteryzowane w zastrze¬ zeniach mozna równiez stosowac i do in¬ nych procesów oraz w polaczeniu z apara¬ tami znanemi. PLThe present invention relates to a process for the separation of emulsions, especially petroleum emulsions by means of an electric current, or a suitable apparatus. It is already known that some emulsions, especially petroleum emulsions, retain some of the water they contain. Numerous attempts have been made to overcome the difficulties and to separate the water, either by the action of gravity or by other means. Many of these processes relied on an electric current. There is already an emulsion splitting method in which a single or multi-phase current was limited and straightened by a valve tube. This process is based on the use of a unidirectional high voltage current, which in fact ensures a rapid separation of emulsions due to rapidly successive high voltage pulses. The current intensity is regulated in order to make it independent of the resistance of the processed fluid. This method has considerable advantages, but in practice it faces considerable difficulties. Above all, the capacity of the valves of today is limited, in relation to the emulsion to be processed (for the voltage E), the value of energy necessary to separate the emulsion, i.e. energy = - = - ^ When separating the use of an alternating current with a sinusoidal or almost sinusoidal waveform, for which / is equal to J / 2, the energy consumption will be equal - i.e. the technical effect of the process increases, as the first power, the consumption and the energy is proportional to the square of the maximum applied voltage, so that the process remains economically unfavorable as long as the emulsion resistance is less than It is very great, but this circumstance is not the case at all in the treatment of aqueous emulsions. Hence, there are drawbacks to the use of known emulsion separation methods. In accordance with the present invention, the emulsion separation employs a voltage at a maximum voltage greater than at least twice, and most practically 5 to 10 times the effective voltage; that is, that the factor indicated above may equal about 5, the energy consumption is then equal to —— and for /, equal to 10, the energy consumption will be only —— instead of —— in the case of ordinary alternating current It is therefore evident that 8% or even 2% of the power normally used is sufficient. The electrolytic side-effect of the current, here removes the alternating current in only one direction in such a way that The positive part of the curve has a maximum voltage 5-10 times greater than the positive RMS voltage, and the negative half of the wave has a slightly variable voltage, but without peaks, so that the effective negative voltage equals the effective positive voltage. It is simple, however, that the method and apparatus described above and characterized in the claims may also be used for other processes and in conjunction with known apparatus. PL
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Publication Number | Publication Date |
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PL4938B1 true PL4938B1 (en) | 1926-07-31 |
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