EP0808216B1 - Verfahren und apparat zur elektrostatischen reinigung von organischen flüssigkeiten - Google Patents
Verfahren und apparat zur elektrostatischen reinigung von organischen flüssigkeiten Download PDFInfo
- Publication number
- EP0808216B1 EP0808216B1 EP96900694A EP96900694A EP0808216B1 EP 0808216 B1 EP0808216 B1 EP 0808216B1 EP 96900694 A EP96900694 A EP 96900694A EP 96900694 A EP96900694 A EP 96900694A EP 0808216 B1 EP0808216 B1 EP 0808216B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- liquid
- impurities
- purified
- strips
- water content
- 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.)
- Expired - Lifetime
Links
- 239000007788 liquid Substances 0.000 title claims description 50
- 238000000034 method Methods 0.000 title claims description 27
- 239000012535 impurity Substances 0.000 claims description 23
- 238000000746 purification Methods 0.000 claims description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 15
- 238000001035 drying Methods 0.000 claims description 13
- 230000005684 electric field Effects 0.000 claims description 10
- 239000002245 particle Substances 0.000 claims description 7
- 230000007246 mechanism Effects 0.000 claims description 3
- 239000006185 dispersion Substances 0.000 claims description 2
- 238000010981 drying operation Methods 0.000 claims 1
- 229910052500 inorganic mineral Inorganic materials 0.000 claims 1
- 239000002184 metal Substances 0.000 claims 1
- 239000011707 mineral Substances 0.000 claims 1
- 239000003921 oil Substances 0.000 description 8
- YEJRWHAVMIAJKC-UHFFFAOYSA-N 4-Butyrolactone Chemical compound O=C1CCCO1 YEJRWHAVMIAJKC-UHFFFAOYSA-N 0.000 description 6
- 239000010635 coffee oil Substances 0.000 description 6
- 238000009434 installation Methods 0.000 description 4
- 238000005352 clarification Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 235000013311 vegetables Nutrition 0.000 description 3
- 239000010779 crude oil Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000008030 elimination Effects 0.000 description 2
- 238000003379 elimination reaction Methods 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000004519 manufacturing process Methods 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
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 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
- 239000003463 adsorbent Substances 0.000 description 1
- 238000004458 analytical method Methods 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
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 239000002173 cutting fluid Substances 0.000 description 1
- 230000001086 cytosolic effect Effects 0.000 description 1
- 238000010908 decantation Methods 0.000 description 1
- 239000002274 desiccant Substances 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
- 238000011043 electrofiltration Methods 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 239000000686 essence Substances 0.000 description 1
- 239000000284 extract 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
- 239000012530 fluid 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
- 125000004435 hydrogen atom Chemical class [H]* 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
- 210000000056 organ Anatomy 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 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
- 239000002699 waste material Substances 0.000 description 1
Images
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 continuously electrostatically purify liquids organic of plant, animal or synthetic origin, namely industrial solvents, hydraulic fluids, cutting fluids for machine tools, lubricating oils and heating, fuels, oils and gasolines vegetable or animal, edible or not, and the like.
- liquids organic of plant, animal or synthetic origin namely industrial solvents, hydraulic fluids, cutting fluids for machine tools, lubricating oils and heating, fuels, oils and gasolines vegetable or animal, edible or not, and the like.
- the impurities contained in such liquids are generally consisting of fibrous, resinous substances, polymers, amorphous or not, carbohydrates, lipids complexes, unsaponifiable compounds, polypeptides and other materials of cytoplasmic origin. Elimination of these impurities by conventional channels, in particular filtering, decantation and centrifugation is generally very difficult and expensive or even impossible, the liquid remaining opaque despite all the efforts made. So we tried to resolve these problems by applying known techniques of electrostatic purification and clarification.
- US-4,155,924 has proposed a method for improving the quality of organic liquids of animal or vegetable origin containing impurities whereby this liquid is subjected to a refining step using an inorganic aqueous base forming a purified organic liquid containing moisture and residual soap formed by the aqueous inorganic base, mix this purified organic liquid with particles adsorbents, this mixture is dehydrated and degasified at high temperature and finally subjected to electrofiltration.
- Such a method comprises a large number of steps and is by therefore complex to implement.
- the present invention also relates to a device (illustrated by the attached drawing) to implement the present process, such as defined by claim 4.
- the method according to the invention consists solely in reducing notably the water content of the liquid to be purified before submit to electrostatic treatment. Indeed, we found that in order for electrostatic purification to to take place, it is necessary and sufficient that the water content of the liquid to be purified is not more than 0.3 percent. he it is even preferable that it does not exceed 0.1 percent, or still in some cases 0.03 percent. The higher the water content is low, the better the electrostatic purification takes place. We can therefore control the degree of effectiveness of the following the needs by adjusting the water content (degree of drying) of the liquid before applying the electric field.
- the single figure represents, schematically and in drawing example, the device for purifying liquids organic including a drying installation.
- the apparatus according to the present invention makes it possible to set up implements the process according to the claims.
- This apparatus includes a device for drying the liquid to purifier located upstream of the purification device electrostatic. As shown schematically in FIG. 1, the apparatus according to the first embodiment comprises the following elements :
- the actual electrostatic purification device has a tank 1 containing the liquid to be purified and at least two electrodes, respectively 2 and 3, to create the field necessary inside the tank 1.
- the electrodes are connected to a high-voltage source 4.
- the electrodes 2 and 3 are mobile and are continuously extracted from the liquid.
- the electrodes 2 and 3 consist of a strip flexible, metallized, endless, mounted between two rollers 5 and 6.
- the fixed central core 7, arranged in the space separating the two branches of the flexible band, either 2 or 3, is provided to force the liquid to be purified to take the passage to the center where the electric field is established according to the high voltage applied to the electrodes. While the rollers 6 rotate freely, the rollers 5 are driven by a mechanism not shown.
- Each mobile electrode, 2 and 3 is associated with a scraper 8 which serves to rid the material impurities that have settled on it under the influence of electric field.
- the scrapers 8 are connected to a tank 9 which receives the waste.
- a heating installation 10 allows, if necessary, to purify the oils at a temperature higher than room temperature.
- the drying device 11 which precedes the purification itself can be a device containing a rotating cylinder 12 where the liquid which is projected on it spreads out in a thin layer.
- a vacuum pump 13 presenting great surface the vacuum created using a vacuum pump 13 dries the liquid very effectively.
- the installation is completed by a supply tank 14, a tank for collecting the clean liquid 15, as well as necessary conduits and pumps connecting the various elements.
- the first example of application of the method relates to the purification of a crude oil, obtained by extraction with pressure of coffee oil seeds.
- This coffee oil comes in the raw state as a dark colored liquid and is opaque.
- the light from a 3 mW HeNe laser beam is immediately dispersed to where it enters the liquid and forms a luminous ball.
- the dispersion of the light should be assigned to the colloidal particles which are the impurities that need to be removed.
- the laser beam penetration distance determined by eye naked, 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 method relates to a organic liquid used in the electronics industry, ⁇ -butyrolactone.
- This liquid serves as a solvent to dissolve the uncured epoxy resin in circuit manufacturing prints.
- the liquid is recovered after this operation and it is regenerated for reuse. Regeneration according to the traditional method takes place by distillation, which means a significant energy expenditure.
- drying products such as 4 ⁇ molecular sieves, calcium chloride (CaCl 2 ), silica gel, Sicapent® (Merck brand).
- the water content is reduced to a value less than 300 ppm after the liquid has been brought into contact with one of the drying agents mentioned above for one to two hours. It should be noted that the regeneration of siccative products reduces the energy efficiency of all operations, which nevertheless remains always very favorable.
- 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)
Claims (4)
- Verfahren zur kontinuierlichen elektrostatischen Reinigung von organischen Flüssigkeiten, welche mit mineralischen oder organischen Substanzen, die als Lösung oder als Dispersion kolloidaler oder nicht-kolloidaler Teilchen vorliegen, verunreinigt sind, dadurch gekennzeichnet, dassman zunächst die besagte Flüssigkeit einem Trocknungsprozess unterwirft, bis der Wassergehalt den Wert von 0.3% nicht mehr überschreitet, undman anschliessend diese Flüssigkeit zwischen mindestens zwei parallelen Streifen von mindestens zwei aus Endlosbändern bestehenden Elektroden leitet, wobei die Elektroden mit den entsprechenden Anschlüssen eines Hochspannungsgerätes verbunden sind, so dass zwischen den Elektrodenstreifen ein elektrisches Feld entsteht, welches die Verunreinigungen auf einem der besagten Elektrodenstreifen ablagert, undman die besagten endlosen Elektrodenstreifen so in Bewegung versetzt, dass gleichzeitig die auf der Oberfläche befindlichen Verunreinigungen entsorgt und die von den Verunreinigungen befreiten Elektrodenstreifen wieder in die zu reinigende Flüssigkeit hineingeführt werden.
- Verfahren gemäss Patentanspruch 1, dadurch gekennzeichnet, dass man die besagte, zu reinigende Flüssigkeit einem Trocknungsprozess unterwirft, bis der Wassergehalt den Wert von 0.1% unterschreitet.
- Verfahren gemäss Patentanspruch 1, dadurch gekennzeichnet, dass man die besagte, zu reinigende Flüssigkeit einem Trocknungsprozess unterwirft, bis der Wassergehalt den Wert von 0.03% unterschreitet.
- Vorrichtung zur Verwirklichung des Verfahrens gemäss Patentanspruch 1, dadurch gekennzeichnet, dass sie aus folgenden Teilen bestehteinem Aggregat (11, 12) zum Trocknen der zu reinigenden Flüssigkeit bis der Wassergehalt den Wert von 0.3% nicht mehr überschreitet,einem Aggregat zum Reinigen (1), welches zwei Endlosbänder (2, 3) mit einer metallischen Oberfläche enthält, die von zwei Walzen (5, 6) geführt werden, deren eine an ein Antriebsgerät gekoppelt ist, diese beiden Endlosbänder (2, 3) sind als Elektroden mit den entsprechenden Anschlüssen eines Hochspannungsgerätes verbunden, so dass zwischen den Elektrodenstreifen ein elektrisches Feld entsteht, welches die Verunreinigungen auf einem der besagten Elektrodenstreifen ablagert,einem Rohrwerk, welches die Apparatur zum Trocknen der zu reinigenden Flüssigkeit (11, 12) mit dem Reinigungsaggregat (1) verbindet, undeinem Gerät zum Ablösen der Verunreinigungen, welche auf der Oberfläche des besagten Endlosbandes (2, 3) im Verlauf der Bewegung abgelagert werden.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CH335/95 | 1995-02-07 | ||
| CH33595 | 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 EP0808216A1 (de) | 1997-11-26 |
| EP0808216B1 true 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 |
|---|---|---|---|---|
| WO2011007820A1 (ja) * | 2009-07-15 | 2011-01-20 | 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 JP JP8524108A patent/JPH11500657A/ja active Pending
- 1996-02-07 WO PCT/IB1996/000101 patent/WO1996024438A1/fr not_active Ceased
- 1996-02-07 ES ES96900694T patent/ES2138804T3/es not_active Expired - Lifetime
- 1996-02-07 EP EP96900694A patent/EP0808216B1/de not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| WO1996024438A1 (fr) | 1996-08-15 |
| DE69602350D1 (de) | 1999-06-10 |
| EP0808216A1 (de) | 1997-11-26 |
| DE69602350T2 (de) | 2000-06-15 |
| ES2138804T3 (es) | 2000-01-16 |
| JPH11500657A (ja) | 1999-01-19 |
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