EP0808216A1 - Verfahren und Apparat zur elektrostatisch Reinigung von organische Flüssigkeiten - Google Patents
Verfahren und Apparat zur elektrostatisch Reinigung von organische FlüssigkeitenInfo
- Publication number
- EP0808216A1 EP0808216A1 EP96900694A EP96900694A EP0808216A1 EP 0808216 A1 EP0808216 A1 EP 0808216A1 EP 96900694 A EP96900694 A EP 96900694A EP 96900694 A EP96900694 A EP 96900694A EP 0808216 A1 EP0808216 A1 EP 0808216A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- liquid
- impurities
- purified
- electrodes
- electric field
- Prior art date
- Legal status (The legal status 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 status listed.)
- Granted
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 60
- 238000000034 method Methods 0.000 title claims description 28
- 239000012535 impurity Substances 0.000 claims abstract description 23
- 230000005684 electric field Effects 0.000 claims abstract description 13
- 238000001035 drying Methods 0.000 claims abstract description 12
- 238000000746 purification Methods 0.000 claims description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- 239000002245 particle Substances 0.000 claims description 6
- 238000009434 installation Methods 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 3
- 239000006185 dispersion Substances 0.000 claims 1
- 229910052500 inorganic mineral Inorganic materials 0.000 claims 1
- 239000011707 mineral Substances 0.000 claims 1
- 239000002184 metal Substances 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 7
- 235000019198 oils Nutrition 0.000 description 7
- YEJRWHAVMIAJKC-UHFFFAOYSA-N 4-Butyrolactone Chemical compound O=C1CCCO1 YEJRWHAVMIAJKC-UHFFFAOYSA-N 0.000 description 6
- 239000010635 coffee oil Substances 0.000 description 5
- 238000005352 clarification Methods 0.000 description 3
- 230000008030 elimination Effects 0.000 description 3
- 238000003379 elimination reaction Methods 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000003463 adsorbent Substances 0.000 description 2
- 239000010779 crude oil Substances 0.000 description 2
- 239000002274 desiccant Substances 0.000 description 2
- 239000000686 essence Substances 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000035515 penetration Effects 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 230000008929 regeneration Effects 0.000 description 2
- 238000011069 regeneration method Methods 0.000 description 2
- 239000008158 vegetable oil Substances 0.000 description 2
- 235000013311 vegetables Nutrition 0.000 description 2
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000010775 animal oil Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 210000001124 body fluid Anatomy 0.000 description 1
- 239000010839 body fluid Substances 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000001086 cytosolic effect Effects 0.000 description 1
- 238000010908 decantation Methods 0.000 description 1
- FPAFDBFIGPHWGO-UHFFFAOYSA-N dioxosilane;oxomagnesium;hydrate Chemical compound O.[Mg]=O.[Mg]=O.[Mg]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O FPAFDBFIGPHWGO-UHFFFAOYSA-N 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000011043 electrofiltration Methods 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000004108 freeze drying Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000004434 industrial solvent Substances 0.000 description 1
- 150000007529 inorganic bases Chemical class 0.000 description 1
- 150000002632 lipids Chemical class 0.000 description 1
- 230000001050 lubricating effect Effects 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- 238000004949 mass spectrometry Methods 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000037361 pathway Effects 0.000 description 1
- 235000020030 perry Nutrition 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 239000002952 polymeric resin Substances 0.000 description 1
- 229920001184 polypeptide Polymers 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 102000004196 processed proteins & peptides Human genes 0.000 description 1
- 108090000765 processed proteins & peptides Proteins 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 239000012261 resinous substance Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C5/00—Separating dispersed particles from liquids by electrostatic effect
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C5/00—Separating dispersed particles from liquids by electrostatic effect
- B03C5/02—Separators
Definitions
- the present invention relates to a method and a device for electrostatically purifying and clarifying organic liquids of plant, animal or synthetic origin, namely industrial solvents, hydraulic liquids, cutting liquids for machine tools, lubricating oils and for heating, fuels, vegetable and animal oils and essences, edible or not, and the like.
- purification and clarification we mainly mean the elimination of particulate impurities suspended in the liquid, or substances of relatively high molecular weight in the more or less dissolved state, in particular in colloidal solutions.
- the nature of these impurities can be arbitrary; it may be dust, particles resulting from wear of moving parts, lubricating particles, extraction products, fibers or other components of plant or animal origin, residual impurities, etc.
- the impurities contained in such liquids generally consist of fibrous, resinous substances, polymers, amorphous or not, carbohydrates, complex lipids, unsaponifiable compounds, polypeptides and other materials of cytoplasmic origin.
- the elimination of these impurities by conventional means, in particular filtering, decantation and centrifugation is generally very difficult and expensive or even impossible, the liquid remaining opaque despite all the efforts made. We have therefore tried to resolve these problems by applying known techniques for electrostatic purification and clarification.
- the method according to the invention only consists in significantly reducing the water content of the liquid to be purified before subjecting it to treatment by electrostatic means. Indeed, it has been found that, for the electrostatic purification to take place, it is necessary and sufficient that the water content of the liquid to be purified is not greater than 0.3 percent. It is even preferable that it does not exceed 0.1 percent, or in some cases 0.03 percent. The lower the water content, the better the electrostatic purification takes place. It is therefore possible to control the degree of effectiveness thereof as required by adjusting the water content (degree of drying) of the liquid before the application of the electric field.
- the single figure shows, schematically and by way of example, the device for purifying organic liquids comprising a drying installation.
- the apparatus according to the present invention makes it possible to carry out the method according to the claims.
- This device includes a device for drying the liquid to be purified, disposed upstream of the purification device. electrostatic. As shown schematically in fig,
- the device according to the first embodiment comprises the following elements:
- the actual electrostatic purification device comprises a tank 1 containing the liquid to be purified and at least two electrodes, respectively 2 and 3, to create the necessary electric field inside the tank 1.
- the electrodes are connected to a source of high -tension 4.
- the electrodes 2 and 3 are mobile and are extracted from the liquid in an alternative or continuous manner.
- the electrodes 2 and 3 consist of a flexible, metallized, endless strip mounted between two rollers 5 and 6.
- the central core 7 fixed, disposed in the space separating the two branches of the flexible strip, ie 2, or 3, is provided to force the liquid to be purified through the passage in the center where the electric field is established as a function of the high voltage applied to the electrodes.
- rollers 6 While the rollers 6 rotate freely, the rollers 5 are driven by a mechanism not shown.
- Each movable electrode, 2 and 3 is associated with a scraper 8 which serves to rid the material of impurities which has deposited on it under the influence of the electric field.
- the scrapers 8 are connected to a tray 9 which receives the waste.
- a heating installation 10 makes it possible, if necessary, to carry out the purification of the oils at a temperature higher than ambient temperature.
- the drying device 11 which precedes the purification device proper can be an apparatus containing a 7 rotating cylinder 12 where the liquid which is sprayed on it spreads forming a thin layer.
- a vacuum pump 13 dries the liquid very effectively.
- the installation is completed by a supply tank 14, a tank for recovering the clean liquid 15, as well as the necessary conduits and pumps connecting the various elements.
- the first example of application of the process relates to the purification of a crude oil, obtained by pressure extraction of oil seeds from coffee.
- This coffee oil is presented in the raw state as a liquid of dark color and is opaque.
- the light from a 3 mW HeNe laser beam is immediately dispersed where it enters the liquid and forms a luminous ball.
- the scattering of light must be attributed to the colloidal particles which are the impurities which have to be removed.
- the penetration distance of the laser beam determined with the naked eye, reaches 16 to 20 mm.
- the oil On leaving the device, the oil is clarified.
- the impurities in the coffee oil are only deposited on the positive electrode which is connected to the earth's potential. This considerably facilitates the removal of deposits on the conveyor belt serving as an electrode.
- the strip circulating at a speed of 12 mm / min. is covered with a layer of residue about 1 mm thick. The losses, most of which are impurities, amount to 16% compared to the quantity of crude oil.
- the second example of application of the process relates to an organic liquid used in the electronic industry, ⁇ -butyrolactone.
- This liquid is used as a solvent to dissolve the uncured epoxy resin in the manufacture of printed circuits.
- the liquid is recovered after this operation and is regenerated for reuse. Regeneration according to the traditional method takes place by distillation, which means a significant energy expenditure.
- the contaminated liquid is introduced into the device described in the previous example where the contaminating material is deposited on the electrodes in the form of a conveyor belt under the effect of the electric field. Due to the lower viscosity of ⁇ -butyrolactone the flow rate reaches 4 to 5 liters per hour. The degree of clarification is sufficient for the liquid to be reusable as a solvent.
Landscapes
- Electrostatic Separation (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CH33595 | 1995-02-07 | ||
CH335/95 | 1995-02-07 | ||
PCT/IB1996/000101 WO1996024438A1 (fr) | 1995-02-07 | 1996-02-07 | Procede et dispositif de purification electrostatique de liquides organiques |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0808216A1 true EP0808216A1 (de) | 1997-11-26 |
EP0808216B1 EP0808216B1 (de) | 1999-05-06 |
Family
ID=4184676
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP96900694A Expired - Lifetime EP0808216B1 (de) | 1995-02-07 | 1996-02-07 | Verfahren und apparat zur elektrostatischen reinigung von organischen flüssigkeiten |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP0808216B1 (de) |
JP (1) | JPH11500657A (de) |
DE (1) | DE69602350T2 (de) |
ES (1) | ES2138804T3 (de) |
WO (1) | WO1996024438A1 (de) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPWO2011007820A1 (ja) * | 2009-07-15 | 2012-12-27 | 国立大学法人 名古屋工業大学 | 粒子回収方法および粒子回収装置 |
CA2947806A1 (en) * | 2016-11-07 | 2018-05-07 | Sandoz Canada Inc. | Visual inspection of difficult to inspect fluids |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1050074A (de) * | 1964-05-25 | |||
FR2688146B1 (fr) * | 1992-03-05 | 1994-05-20 | Charles Frei | Procede et dispositif de purification d'un liquide electriquement non conducteur. |
DE4344828A1 (de) * | 1993-12-28 | 1995-06-29 | Oehmi Forsch & Ingtech Gmbh | Verfahren und Vorrichtung zum Reinigen von Feststoffpartikeln enthaltenden Flüssigkeiten |
-
1996
- 1996-02-07 DE DE69602350T patent/DE69602350T2/de not_active Expired - Fee Related
- 1996-02-07 WO PCT/IB1996/000101 patent/WO1996024438A1/fr active IP Right Grant
- 1996-02-07 JP JP8524108A patent/JPH11500657A/ja active Pending
- 1996-02-07 ES ES96900694T patent/ES2138804T3/es not_active Expired - Lifetime
- 1996-02-07 EP EP96900694A patent/EP0808216B1/de not_active Expired - Lifetime
Non-Patent Citations (1)
Title |
---|
See references of WO9624438A1 * |
Also Published As
Publication number | Publication date |
---|---|
ES2138804T3 (es) | 2000-01-16 |
JPH11500657A (ja) | 1999-01-19 |
DE69602350D1 (de) | 1999-06-10 |
WO1996024438A1 (fr) | 1996-08-15 |
DE69602350T2 (de) | 2000-06-15 |
EP0808216B1 (de) | 1999-05-06 |
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