DE3114068A1 - Process for purifying high-temperature and high-pressure gases - Google Patents
Process for purifying high-temperature and high-pressure gasesInfo
- Publication number
- DE3114068A1 DE3114068A1 DE19813114068 DE3114068A DE3114068A1 DE 3114068 A1 DE3114068 A1 DE 3114068A1 DE 19813114068 DE19813114068 DE 19813114068 DE 3114068 A DE3114068 A DE 3114068A DE 3114068 A1 DE3114068 A1 DE 3114068A1
- Authority
- DE
- Germany
- Prior art keywords
- gas
- filter
- cleaning
- cleaned
- pressure
- 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.)
- Withdrawn
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/02—Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
- B01D46/04—Cleaning filters
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/66—Regeneration of the filtering material or filter elements inside the filter
- B01D46/70—Regeneration of the filtering material or filter elements inside the filter by acting counter-currently on the filtering surface, e.g. by flushing on the non-cake side of the filter
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/66—Regeneration of the filtering material or filter elements inside the filter
- B01D46/70—Regeneration of the filtering material or filter elements inside the filter by acting counter-currently on the filtering surface, e.g. by flushing on the non-cake side of the filter
- B01D46/71—Regeneration of the filtering material or filter elements inside the filter by acting counter-currently on the filtering surface, e.g. by flushing on the non-cake side of the filter with pressurised gas, e.g. pulsed air
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/90—Devices for taking out of action one or more units of multi-unit filters, e.g. for regeneration or maintenance
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/20—Combinations of devices covered by groups B01D45/00 and B01D46/00
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2273/00—Operation of filters specially adapted for separating dispersed particles from gases or vapours
- B01D2273/20—High temperature filtration
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
Description
Beschreibung und Erläuterung zur PatentanmeldungDescription and explanation of the patent application
"Verfahren zur Reinigung von Gasen mit hoher Temperatur und hohen Drücken Es ist bekannt, Heißgasfilter mit hohem Durck zu beaufschlagen."Process for the purification of gases with high temperature and high Pressing It is known to apply high pressure to hot gas filters.
Die Schwierigkeit ist, die Filter in sehr kurzer Zeit zu reinigen, wenn insbesondere feinste Stäube von um lEm abgereinigt werden müssen, wobei zum Beispiel das spezifische Gewicht eines solchen Staubes bei ca. 1,5 liegt und das Gas selber bei sehr hohem Druck eine spezifische Wichte von z.B. 15 - 20 kp/m3 besitzt.The difficulty is to clean the filters in a very short time, if in particular the finest dusts have to be cleaned off by lEm, with the Example the specific gravity of such a dust is around 1.5 and that Gas itself has a specific gravity of e.g. 15-20 kp / m3 at very high pressure.
Bisher mußten diese Filter aus dem Gasstrom abgeschaltet und durch Druckschock, z.B. über Inertgas, gereinigt werden. Eine relativ lange Verweilzeit war notwendig, um das Absinken der Feinststäube in dem abgeschalteten Filter zu ermöglichen und sie über den Staubaustrag auszutragen.Previously, these filters had to be switched off from the gas flow and passed through Pressure shock, e.g. using inert gas. A relatively long dwell time was necessary to prevent the particulate matter from sinking into the switched-off filter enable and discharge them via the dust discharge.
Erfindungsgemäß wird vorgeschlagen, die Spülzeit des Filters auf ein Minimum zu begrenzen.According to the invention it is proposed that the flushing time of the filter be reduced to one Limit minimum.
Diese wird erfindungsgemäß durch folgendes Verfahren ermöglicht.According to the invention, this is made possible by the following method.
In der beiliegenden Zeichnung ist dargestellt mit (1) ein Filter mit (2) der Rohgaseintritt mit (3) der Reingasaustritt mit (4) die Abreinigungsvorrichtung, z.B. Druckschocksystem mit (5) der Gasstrahl-Antrieb mit (6) der Zyklon mit (7) ein nachgeschalteter, kleiner Staubabsaugfilter mit (8) Gasdruckerhöhung für das Spülgas (9) und (lo), welches zum Leerspülen des Filters (1) vorgesehen ist.In the accompanying drawing, (1) shows a filter with (2) the raw gas inlet with (3) the clean gas outlet with (4) the cleaning device, e.g. pressure shock system with (5) the gas jet drive with (6) the cyclone with (7) a downstream, small dust extraction filter with (8) gas pressure increase for the Purge gas (9) and (lo), which is provided for flushing the filter (1).
Arbeitsweise des erfindungsgemäßen Verfahrens: Das Rohgas, welches bei (2) in den Filter eintritt, wird solange durch den Filter gereinigt, bis daß sich der max. zulässige Widerstand im Filter eingestellt hat.Operation of the method according to the invention: The raw gas, which at (2) enters the filter, the filter is cleaned until that the maximum permissible resistance in the filter has been set.
Bei Erreichen dieses max. Widerstandes wird das Rohgas auf einen oder mehrere Parallelfilter umgeschaltet, und der genannte Filter (1) wird aus dem Rohgasstrom abgeschaltet.When this maximum resistance is reached, the raw gas is switched to an or several parallel filters are switched over, and said filter (1) is made from the raw gas flow switched off.
In diesem Moment wird über dem Injektor (5) ein Sog in dem Filter (1) erzeugt, der dazu dient, daß die Abreinigung durch Druckschock (4) und Spülgas (9) und (lo) saugseitig erfaßt wird, um dieses beschleunigte, abgereinigte Staubmedium einem Zyklon (6) und/oder nachgeschalteten Filter (7) zuzuführen.At this moment there is suction in the filter via the injector (5) (1) generated, which serves that the cleaning by pressure shock (4) and purge gas (9) and (lo) is detected on the suction side to this accelerated, cleaned dust medium a cyclone (6) and / or downstream filter (7).
Der Staub ist durch die Vorrichtung Filter (1) agglomeriert und wird sich zum sehr großen Teil im Zyklon (6) bereits abscheiden, so daß die Belastung im Filter (7) relativ gering ist. Der Filter (7) wird über Druckschock oder über ein ähnlich arbeitendes Filterreinigungs-System gereinigt.The dust is agglomerated through the device filter (1) and becomes to a very large extent already deposit in the cyclone (6), so that the load in the filter (7) is relatively low. The filter (7) is via pressure shock or via a similarly working filter cleaning system cleaned.
über (8) wird das Gas aus dem Filter (7) angesaugt und druckseitig, wunschgerecht für das Ausblasen über (9) und (lo), im Filter (1) fähig gestaltet.The gas is sucked in from the filter (7) via (8) and on the pressure side, as desired for blowing out through (9) and (lo), designed to be capable in the filter (1).
Durch diese erfindungsgemäße Verfahrensanordnung und Vorrichtung zur Durchführung des Verfahrens ist es möglich, Prozessgas in sehr kurzer Zeit zu reinigen.By this inventive method arrangement and device for Carrying out the process, it is possible to purify process gas in a very short time.
Die bekannten Filter des Entstaubers mit sogenannter Jet-oder Strahl- Paratabreinigung sind diesem System im Zeitablauf wesentlich unterlegen.The well-known filters of the dust extractor with so-called jet or jet Parate cleaning are significantly inferior to this system over time.
Selbstverständlich ist die Erfindung nicht auf die vorstehend im einzelnen dargestellten und beschriebenen Ausbildungsformen beschränkt, sondern es sind zahlreiche Abänderungen möglich, ohne jedoch von dem Grundgedanken abzuweichen, vorzugsweise Prozessgase, die unter hohem Druck und mit hoher Temperatur Abscheider beaufschlagen und die gereinigt werden sollen, in die Filter zu führen, die für die Reinigung vom Gasstrom abgetrennt sind und durch Unterdruckerzeuger im Innenraum schnellstmöglich evakuiert werden und der evakuierte Staub, konzentriert und voragglomeriert, in einem nachgeschalteten Abscheidesystem, vorzugsweise bestehend aus zweistufiger Abscheidung a) Zyklon und b) Filter gereinigt wird und die Prozessgase selber die Vorrichtungen zum Evakuieren und Schocken bedienen, wobei vorzugsweise über ein Druckerhöhungsgebläse die notwendige Prozeßsteuerung des erfindungsgemäßen Verfahrens geschaffen wird, wobei weiterhin im erfindungsgemäßen Verfahren zugrunde liegt, daß ein kontinuierlicher Spülgasumlauf vorgesehen ist, um Propfenbildung zu vermeiden.Of course, the invention is not limited to the above in detail Forms of training shown and described are limited, but there are numerous Modifications are possible without, however, deviating from the basic idea, preferably Process gases which act on separators under high pressure and at high temperature and that are to be cleaned, lead into the filters that are used for cleaning are separated from the gas flow and as quickly as possible by vacuum generators in the interior be evacuated and the evacuated dust, concentrated and pre-agglomerated, in a downstream separation system, preferably consisting of two-stage Separation a) cyclone and b) filter is cleaned and the process gases themselves Operate devices for evacuation and shock, preferably via a The pressure booster fan provides the necessary process control of the invention Method is created, with the method according to the invention still being based lies that a continuous purge gas circulation is provided to plug formation to avoid.
Patentanspruch : Claim:
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19813114068 DE3114068A1 (en) | 1981-04-08 | 1981-04-08 | Process for purifying high-temperature and high-pressure gases |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19813114068 DE3114068A1 (en) | 1981-04-08 | 1981-04-08 | Process for purifying high-temperature and high-pressure gases |
Publications (1)
Publication Number | Publication Date |
---|---|
DE3114068A1 true DE3114068A1 (en) | 1982-11-04 |
Family
ID=6129597
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE19813114068 Withdrawn DE3114068A1 (en) | 1981-04-08 | 1981-04-08 | Process for purifying high-temperature and high-pressure gases |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE3114068A1 (en) |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3611700A1 (en) * | 1986-04-08 | 1987-10-15 | Hoelter Heinz | Process for cleaning off a hot gas filter |
US4909814A (en) * | 1988-08-18 | 1990-03-20 | Sisk David E | Dust filtering and collection system |
US5053063A (en) * | 1988-08-18 | 1991-10-01 | Sisk David E | Dust filtering and collection system |
EP0554886A2 (en) * | 1992-02-05 | 1993-08-11 | Asahi Glass Company Ltd. | A filtering method of flue gas of a boiler and a filter apparatus for hot gas |
EP0774289A1 (en) * | 1995-11-20 | 1997-05-21 | Kvaerner Bison GmbH | Filter installation and use thereof |
WO2007041955A1 (en) * | 2005-10-11 | 2007-04-19 | Zimmer, Sebastian | A cleaning process for filtration material of gas filter |
WO2010046210A1 (en) * | 2008-10-23 | 2010-04-29 | Siemens Vai Metals Technologies Gmbh & Co | Method and device for separating particulate solids from a gas flow |
CN102961945A (en) * | 2012-11-29 | 2013-03-13 | 中南大学 | System with integrated functions of high-temperature flue gas dedusting, desulfurization and denitrification |
CN103002967A (en) * | 2010-07-20 | 2013-03-27 | 西门子Vai金属科技有限责任公司 | Method for cleaning a gas flow loaded with dust |
DE102013011758A1 (en) * | 2013-07-13 | 2015-01-15 | Gerhard Kemper | Device for extracting and filtering fine dust polluted air |
CN105642055A (en) * | 2015-05-09 | 2016-06-08 | 刘国义 | High efficient multifunctional cleaning-free gas pollution purifying and separating device |
WO2017076392A1 (en) * | 2015-11-02 | 2017-05-11 | Esta Apparatebau Gmbh & Co. Kg | Dust removal system |
CN109011869A (en) * | 2018-08-10 | 2018-12-18 | 徐明杰 | A kind of enviroment protective ceramic grain bed for high temperature fume dust removal |
-
1981
- 1981-04-08 DE DE19813114068 patent/DE3114068A1/en not_active Withdrawn
Cited By (23)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3611700A1 (en) * | 1986-04-08 | 1987-10-15 | Hoelter Heinz | Process for cleaning off a hot gas filter |
US4909814A (en) * | 1988-08-18 | 1990-03-20 | Sisk David E | Dust filtering and collection system |
US5053063A (en) * | 1988-08-18 | 1991-10-01 | Sisk David E | Dust filtering and collection system |
EP0554886A2 (en) * | 1992-02-05 | 1993-08-11 | Asahi Glass Company Ltd. | A filtering method of flue gas of a boiler and a filter apparatus for hot gas |
EP0554886A3 (en) * | 1992-02-05 | 1993-10-20 | Asahi Glass Co Ltd | A filtering method of flue gas of a boiler and a filter apparatus for hot gas |
US5348568A (en) * | 1992-02-05 | 1994-09-20 | Asahi Glass Company Ltd. | Filtering method of flue gas of a boiler and a filter apparatus for hot gas |
EP0754486A2 (en) * | 1992-02-05 | 1997-01-22 | Asahi Glass Company Ltd. | A filtering method of flue gas of a boiler and a filter apparatus for hot gas |
EP0754486A3 (en) * | 1992-02-05 | 1997-09-24 | Asahi Glass Co Ltd | A filtering method of flue gas of a boiler and a filter apparatus for hot gas |
EP0774289A1 (en) * | 1995-11-20 | 1997-05-21 | Kvaerner Bison GmbH | Filter installation and use thereof |
EP1951405A1 (en) * | 2005-10-11 | 2008-08-06 | Zimmer, Sebastian | A cleaning process for filtration material of gas filter |
WO2007041955A1 (en) * | 2005-10-11 | 2007-04-19 | Zimmer, Sebastian | A cleaning process for filtration material of gas filter |
EP1951405A4 (en) * | 2005-10-11 | 2009-09-23 | Sebastian Zimmer | A cleaning process for filtration material of gas filter |
AU2006301780B2 (en) * | 2005-10-11 | 2010-12-16 | Sebastian Zimmer | A cleaning process for filtration material of gas filter |
US8021467B2 (en) | 2005-10-11 | 2011-09-20 | Sebastian Zimmer | Cleaning process for cleaning filtration material of a gas filter and a device for carrying out the process |
WO2010046210A1 (en) * | 2008-10-23 | 2010-04-29 | Siemens Vai Metals Technologies Gmbh & Co | Method and device for separating particulate solids from a gas flow |
CN103002967A (en) * | 2010-07-20 | 2013-03-27 | 西门子Vai金属科技有限责任公司 | Method for cleaning a gas flow loaded with dust |
US8882893B2 (en) | 2010-07-20 | 2014-11-11 | Siemens Vai Metals Technologies Gmbh | Method for cleaning a gas flow loaded with dust |
CN103002967B (en) * | 2010-07-20 | 2016-01-20 | 首要金属科技奥地利有限责任公司 | The purification method of dust-containing air stream |
CN102961945A (en) * | 2012-11-29 | 2013-03-13 | 中南大学 | System with integrated functions of high-temperature flue gas dedusting, desulfurization and denitrification |
DE102013011758A1 (en) * | 2013-07-13 | 2015-01-15 | Gerhard Kemper | Device for extracting and filtering fine dust polluted air |
CN105642055A (en) * | 2015-05-09 | 2016-06-08 | 刘国义 | High efficient multifunctional cleaning-free gas pollution purifying and separating device |
WO2017076392A1 (en) * | 2015-11-02 | 2017-05-11 | Esta Apparatebau Gmbh & Co. Kg | Dust removal system |
CN109011869A (en) * | 2018-08-10 | 2018-12-18 | 徐明杰 | A kind of enviroment protective ceramic grain bed for high temperature fume dust removal |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
OR8 | Request for search as to paragraph 43 lit. 1 sentence 1 patent law | ||
8139 | Disposal/non-payment of the annual fee |