WO2006074888A1 - Verfahren und vorrichtung zur elektrostatischen aufladung und abscheidung schwierig abzuscheidender partikel - Google Patents
Verfahren und vorrichtung zur elektrostatischen aufladung und abscheidung schwierig abzuscheidender partikel Download PDFInfo
- Publication number
- WO2006074888A1 WO2006074888A1 PCT/EP2006/000106 EP2006000106W WO2006074888A1 WO 2006074888 A1 WO2006074888 A1 WO 2006074888A1 EP 2006000106 W EP2006000106 W EP 2006000106W WO 2006074888 A1 WO2006074888 A1 WO 2006074888A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- ionization
- region
- deposition
- particles
- high voltage
- Prior art date
Links
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
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/02—Plant or installations having external electricity supply
-
- 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
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/34—Constructional details or accessories or operation thereof
- B03C3/40—Electrode constructions
- B03C3/45—Collecting-electrodes
- B03C3/455—Collecting-electrodes specially adapted for heat exchange with the gas stream
-
- 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
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/02—Plant or installations having external electricity supply
- B03C3/025—Combinations of electrostatic separators, e.g. in parallel or in series, stacked separators, dry-wet separator combinations
-
- 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
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/34—Constructional details or accessories or operation thereof
- B03C3/40—Electrode constructions
- B03C3/45—Collecting-electrodes
-
- 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
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/34—Constructional details or accessories or operation thereof
- B03C3/40—Electrode constructions
- B03C3/45—Collecting-electrodes
- B03C3/51—Catch- space electrodes, e.g. slotted-box form
Definitions
- the invention relates to a method and apparatus for electrostatic charging and deposition of difficult to be separated particles of a gas fluid according to the preambles of independent claims 1 and 5. It is in other words an electrostatic precipitator and an electrostatic precipitator, and in particular those Electrostatic precipitator or electrostatic filter, which are suitable for filtering industrial emissions.
- the reason that some particles are difficult to separate, may be due to the electrical properties of the particles, which lead due to their chemical-physical nature of the collecting electrodes to an insulating layer.
- the physically effective charging mechanisms namely the so-called shock or field charging and the diffusion charging, a more or less pronounced minimum of the particle fraction separation efficiency occurs.
- an electrostatic working separator for dedusting industrial waste gases which works with a negative spray system.
- a method is known in which electrostatically charged and deposited by means of only one high voltage source for a high voltage zone difficult to separate particles are removed from a Casfluid, which in contrast to the so-called Cottrell electrostatic precipitates the particles within the high voltage zone successively and not simultaneously and be deposited.
- it is set in this method and in the apparatuses for method embodiment in lonticiansbe- reaching a greater distance than in the separation lanes geometric, whereby the field strength of the 'is smaller lonisier Schemees, when the field strength of the separation region.
- the lane width for the ionization region was therefore made larger in the known filters than the lane width of the separation region, since it was expected that in the comparatively low charge or ionization region the expected very high, nevertheless necessary specific current flow to relatively early onset and consequently the electrical Performance limiting rollover activity will result.
- the presence of a sufficiently high field strength should be ensured in the separation area by reducing the width of the lanes.
- Air filters and industrial filters are not comparable because air filters must meet completely different requirements than the large industrial electrostatic precipitators involved, and therefore they can not be used to clean industrial gases.
- electrostatic precipitators for industrial emissions, lane widths of 200 to 500 mm are usually used. This, together with the composition of the exhaust gases and their flue gas temperature, it follows that in industrial electrostatic precipitators usually field strengths in the range of 2 to 4 kV / cm and specific currents in the range of 0.2 to 1.2 mA / m 2 be used.
- Air filters are also known, each working with a positive spray system and two high voltages.
- air filters have a rectifier with two outputs for ionization and deposition.
- the field strengths in the known air filters are the same in the ionization and deposition area, but provided with different voltage potentials. Both areas must be carried out electrically isolated from each other.
- positive discharge electrodes are provided, which cause a moderate ionization.
- the invention has for its object to avoid the disadvantages of the above-described electric fiiter and electrostatic precipitator method and to reduce the energy consumption in the filtration of industrial waste gases.
- the separator according to the invention and the deposition process according to the invention thus work with a negative spray system, in which with the help of only one high voltage source in each high-voltage zone just sufficient charge of the particles is performed. Accordingly, the transport of the charged particles and their deposition takes place with the least additional energy expenditure on the oppositely poled precipitation electrodes, the individual passages known from the conventional filters having a negative spray system being left unchanged.
- the efficient and as complete as possible charging of the particles is carried out at an applied high voltage in the ionization region, which in turn generates a field strength in the subsequent deposition region with the lowest current flow, which is sufficient for transport and deposition of the particles.
- a low, defined current flow in the deposition area ensures that a certain tracking of charge carriers to the positive collecting electrode is achieved in order to largely prevent the re-entrainment of already deposited particles.
- Fig. 1 shows the general particle separation behavior in an electrostatic precipitator
- FIG. 3 shows an overview arrangement of a first embodiment of a single separation gate of the separation device according to the invention
- FIG. 4 shows an overview arrangement of a second exemplary embodiment of a single separation gate of the separation device according to the invention
- FIG. 5 shows a first embodiment of an electrostatic precipitator according to the invention with two separation gates and one ionization area
- FIG. 6 shows a second embodiment of an electrostatic filter according to the invention with three separation gates and two ionization areas
- Fig. 7 shows a third embodiment of an electrostatic precipitator according to the invention with two Abscheidegassen with cooled precipitation electrodes in the ionization region.
- Fig. 1 shows the particle separation behavior in an electrostatic precipitator.
- Fig. 2 shows how far the individual characteristics of the candidate negative electrode geometries must differ, so that the objective of the invention can occur.
- the characteristics in the left-hand diagram part correspond to the high-current electrode shapes (A, B and C-type) for the ionization region, while the characteristics shown in the right-hand part of the diagram correspond to the low-current electrode shapes (D, E and F types) for the deposition region correspond.
- Fig. 3 shows the overview of a single Abscheidegasse with the working sections ionizing and deposition. Neighboring analogue streets are not shown.
- a high voltage power source 1 a high voltage system 2 is connected, which is provided with power-intensive discharge electrodes 6 and voltage-intensive or low-current negative electrodes 7.
- the spray electrodes 6 are located in an ionization region 4, which is formed by the grounded collecting electrodes 3.
- the negative electrodes 7 are located in a deposition region 5, which is likewise formed by the precipitation electrodes 3. 11 marks the entire high-voltage zone.
- ionization region 4 also referred to as ionization region, a sufficient charge of the particles is achieved, which are then optimally deposited in the following deposition region 5 with greatly reduced turbulence or nearly missing electrical wind.
- the ionization region 4 and the deposition region 5 can be followed by a further ionization region 4a with a deposition region 5a.
- Fig. 5 shows a schematic representation of a horizontally arranged electrostatic precipitator, a so-called horizontal field.
- a plurality of rows of collecting electrodes 3 are provided within a filter housing 8 with the ground 12, which form several Abscheidegassen 13, which in turn have a Ionisations Suite4 with the power-intensive discharge electrodes 6 and a deposition area with low-current negative electrodes 7.
- the embodiment shown here has two Abscheidegassen 13, but more Abscheidegassen 13 can follow, as indicated by the dashed lines 14.
- Fig. 6 shows another embodiment of the electrostatic precipitator according to the invention, wherein within the three separation trays 13 shown two ionization regions 4 and 4a and two deposition regions 5 and 5a are arranged.
- the negative electrodes 7 having an elliptic shape shown in Fig. 6 have another candidate geometry.
- Fig. 7 shows a third embodiment with an ionization region 4, in which the grounded with 12 precipitation electrodes 9 are designed as a hollow body (cooling chamber 10), which are flowed through by a coolant 9. This cooling is one, also known as back corona, "back ionization due to an extreme electric resistance of separated particles in loni- stechniks Symposium 4 avoided.
Landscapes
- Electrostatic Separation (AREA)
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2007550738A JP2008526499A (ja) | 2005-01-11 | 2006-01-09 | 分離困難な粒子を静電的に帯電させて分離する方法および装置 |
KR1020077018468A KR101238619B1 (ko) | 2005-01-11 | 2006-01-09 | 분리되기 어려운 파티클을 정전기적으로 하전하여 분리하는방법 및 장치 |
US11/794,960 US8002876B2 (en) | 2005-01-11 | 2006-01-09 | Method and apparatus for electrostatically charging and separating particles that are difficult to separate |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP05000380.5 | 2005-01-11 | ||
EP05000380A EP1679123A1 (de) | 2005-01-11 | 2005-01-11 | Verfahren und Vorrichtung zur elektrostatischen Aufladung und Abscheidung schwierig abzuscheidender Partikel |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2006074888A1 true WO2006074888A1 (de) | 2006-07-20 |
Family
ID=34933241
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2006/000106 WO2006074888A1 (de) | 2005-01-11 | 2006-01-09 | Verfahren und vorrichtung zur elektrostatischen aufladung und abscheidung schwierig abzuscheidender partikel |
Country Status (7)
Country | Link |
---|---|
US (1) | US8002876B2 (de) |
EP (1) | EP1679123A1 (de) |
JP (1) | JP2008526499A (de) |
KR (1) | KR101238619B1 (de) |
CN (1) | CN101137442A (de) |
WO (1) | WO2006074888A1 (de) |
ZA (1) | ZA200706171B (de) |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8625253B2 (en) * | 2007-01-25 | 2014-01-07 | Goudy Research, Llc | Fluid cooled electrical capacitor and methods of making and using |
WO2010048223A2 (en) * | 2008-10-20 | 2010-04-29 | Carrier Corporation | Electrically enhanced air filtration system using rear fiber charging |
KR101610854B1 (ko) * | 2008-12-11 | 2016-04-21 | 삼성전자 주식회사 | 전기집진장치 및 그 고전압 전극 |
WO2012055110A1 (zh) * | 2010-10-29 | 2012-05-03 | 南京师范大学 | 一种单区板式高温静电除尘器 |
US20120192713A1 (en) * | 2011-01-31 | 2012-08-02 | Bruce Edward Scherer | Electrostatic Precipitator Charging Enhancement |
US9682384B2 (en) * | 2014-09-11 | 2017-06-20 | University Of Washington | Electrostatic precipitator |
US9595884B2 (en) | 2014-12-18 | 2017-03-14 | General Electric Company | Sub-sea power supply and method of use |
US10399091B2 (en) | 2016-01-08 | 2019-09-03 | Korea Institute Of Machinery & Materials | Electrostatic precipitation device for removing particles in explosive gases |
KR101973018B1 (ko) * | 2016-11-29 | 2019-04-26 | 한국기계연구원 | 폭발성 배기가스 입자의 정전 제거 장치 |
US20210331006A1 (en) * | 2020-04-22 | 2021-10-28 | Mukundakumar Rajukumar | Head-mounted Air Purifier |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1343285A (en) * | 1913-03-05 | 1920-06-15 | Int Precipitation Co | Means for separating suspended matter from gases |
US4264343A (en) * | 1979-05-18 | 1981-04-28 | Monsanto Company | Electrostatic particle collecting apparatus |
US6004376A (en) * | 1996-12-06 | 1999-12-21 | Apparatebau Rothemuhle Brandt & Kritzler Gmbh | Method for the electrical charging and separation of particles that are difficult to separate from a gas flow |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3518462A (en) * | 1967-08-21 | 1970-06-30 | Guidance Technology Inc | Fluid flow control system |
US3907520A (en) * | 1972-05-01 | 1975-09-23 | A Ben Huang | Electrostatic precipitating method |
JPS5929302B2 (ja) * | 1976-07-05 | 1984-07-19 | メタルゲゼルシヤフト・アクチエンゲゼルシヤフト | 高抵抗ダスト集塵方法 |
DK141541B (da) * | 1977-08-04 | 1980-04-14 | Niels Brundbjerg | Luftrenser af regenerationstypen omfattende en ozonlampe. |
US4225323A (en) * | 1979-05-31 | 1980-09-30 | General Electric Company | Ionization effected removal of alkali composition from a hot gas |
EP0314811B1 (de) * | 1987-05-21 | 1994-03-30 | Matsushita Electric Industrial Co., Ltd. | Staubsammelelektrode |
JP3155775B2 (ja) * | 1991-07-19 | 2001-04-16 | 東芝キヤリア株式会社 | 電気集塵機 |
US5302190A (en) * | 1992-06-08 | 1994-04-12 | Trion, Inc. | Electrostatic air cleaner with negative polarity power and method of using same |
US6524369B1 (en) * | 2001-09-10 | 2003-02-25 | Henry V. Krigmont | Multi-stage particulate matter collector |
-
2005
- 2005-01-11 EP EP05000380A patent/EP1679123A1/de not_active Withdrawn
-
2006
- 2006-01-09 KR KR1020077018468A patent/KR101238619B1/ko active IP Right Grant
- 2006-01-09 US US11/794,960 patent/US8002876B2/en not_active Expired - Fee Related
- 2006-01-09 JP JP2007550738A patent/JP2008526499A/ja active Pending
- 2006-01-09 WO PCT/EP2006/000106 patent/WO2006074888A1/de active Application Filing
- 2006-01-09 CN CNA2006800078495A patent/CN101137442A/zh active Pending
-
2007
- 2007-07-25 ZA ZA200706171A patent/ZA200706171B/en unknown
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1343285A (en) * | 1913-03-05 | 1920-06-15 | Int Precipitation Co | Means for separating suspended matter from gases |
US4264343A (en) * | 1979-05-18 | 1981-04-28 | Monsanto Company | Electrostatic particle collecting apparatus |
US6004376A (en) * | 1996-12-06 | 1999-12-21 | Apparatebau Rothemuhle Brandt & Kritzler Gmbh | Method for the electrical charging and separation of particles that are difficult to separate from a gas flow |
Also Published As
Publication number | Publication date |
---|---|
EP1679123A1 (de) | 2006-07-12 |
ZA200706171B (en) | 2008-04-30 |
US8002876B2 (en) | 2011-08-23 |
US20090165648A1 (en) | 2009-07-02 |
JP2008526499A (ja) | 2008-07-24 |
CN101137442A (zh) | 2008-03-05 |
KR101238619B1 (ko) | 2013-02-28 |
KR20070095405A (ko) | 2007-09-28 |
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