EP0891404A1 - Procede pour le broyage et le sechage du lignite - Google Patents
Procede pour le broyage et le sechage du ligniteInfo
- Publication number
- EP0891404A1 EP0891404A1 EP97916398A EP97916398A EP0891404A1 EP 0891404 A1 EP0891404 A1 EP 0891404A1 EP 97916398 A EP97916398 A EP 97916398A EP 97916398 A EP97916398 A EP 97916398A EP 0891404 A1 EP0891404 A1 EP 0891404A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- fluidized bed
- vapors
- comminution
- bed drying
- drying
- 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
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10F—DRYING OR WORKING-UP OF PEAT
- C10F5/00—Drying or de-watering peat
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10F—DRYING OR WORKING-UP OF PEAT
- C10F7/00—Working-up peat
- C10F7/02—Disintegrating peat
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B1/00—Preliminary treatment of solid materials or objects to facilitate drying, e.g. mixing or backmixing the materials to be dried with predominantly dry solids
- F26B1/005—Preliminary treatment of solid materials or objects to facilitate drying, e.g. mixing or backmixing the materials to be dried with predominantly dry solids by means of disintegrating, e.g. crushing, shredding, milling the materials to be dried
Definitions
- the invention relates to a method for comminuting and drying lignite, in which the lignite is subjected to at least two comminution steps and is dried in an indirectly heated fluidized bed dryer, at least one first comminution step taking place before the fluidized bed drying and vapors being withdrawn from the fluidized bed drying.
- the dedusted vapors are compressed and used for the indirect heating of the fluidized bed dryer.
- the fluidized bed dryer is heated with steam and the vapors are condensed and the heat extracted is used for other purposes.
- the fluidized bed dryer works with an atmosphere of slightly superheated steam, the vapors can be used to screen the ground material without any safety problems.
- the fines separated by the screening can be fed to the fluidized bed drying or the dust separator, using the vapors themselves.
- Subclaims 2 - 10 are directed to preferred procedures.
- Fig. 2 shows a procedure in which the crushing in a
- Shredding device with recycling of coarse material is carried out before the fluidized bed drying
- Fig. 3 shows a method in which the fluidized bed drying is preceded by a first comminution device and a second comminution device with a downstream vapor classifier is followed by the fluidized bed drying and
- FIG. 4 shows a process control, comparable to the process control according to FIG. 3, but with the omission of a separate classifier, the fluidized bed drying system itself is used as a classifier.
- raw lignite RK is fed to a first comminution device 2.
- the comminuted coal 3 is introduced into a separator 5 by means of a feeder into a vapor stream B fed via line 4.
- the coarse material of the classifier 5 is introduced into a second comminution device 7 via an allocator 6.
- the comminution material of the comminution device 7 is fed to a fluidized bed dryer 9 via a line 8 'with the aid of a vapor stream brought in via line 8.
- the fluidized bed dryer 9 is indirectly heated via at least one heating surface 10 which, for. B. in the WTA process with compressed vapors.
- the fluidized bed dryer 9 is acted upon by a schematically illustrated nozzle 11 with a fluidizing agent.
- Dried brown coal GK is drawn off from the fluidized bed dryer, as is shown schematically by the extraction device 12.
- the vapors drawn off from the fluidized bed dryer 9 via line 13 are dedusted in a vapor electrostatic filter 14.
- the dust coal SK is drawn off via a discharge device 15.
- the line 4 with the branch line 8 is connected to the outlet of the vapor electrostatic precipitator and a vapor blower 16 is arranged in the line.
- a vapor withdrawal line 17 is also connected to the output of the electrostatic filter 14. As in the WTA process, this can be led to a vapor compressor (not shown) or, as in the DWT process, to a vapor condenser (not shown) or can be released into the atmosphere.
- shredding devices that are suitable for shredding wet coal are suitable as shredding devices.
- shredding devices include, in particular, hammer mills, in which the crushing takes place by impact on impact edges.
- hammer mills in which the crushing takes place by impact on impact edges.
- impact wheel mills e.g. B. impact wheel mills and impact splitter.
- the raw lignite RK is fed via a feeder 18 to a comminution device 19.
- the comminution device is designed such that it can suck in vapors not dedusted from dust via a line 20 which is connected directly to the fluidized bed dryer 9.
- the coal comminuted in the comminution device 19 becomes a classifying separator via a line 21 '
- the coarse material of the separating separator 21 is via line
- a self-priming beater wheel mill can be used here as the comminution device, in which the comminution and conveyance of the transport gas take place in one step. If necessary, it is possible to additionally overheat the vapors sucked in via line 19 with steam brought in from a turbine (not shown), as is shown schematically by FIG. The operation of this arrangement is similar to the operation of a Schiagrad mill on a raw lignite furnace.
- the raw lignite RK comminuted in the first comminution device 2 is fed directly to the fluidized bed dryer 9 via the apportioning device.
- the dried lignite GK drawn off via the extraction device 12 is fed to a comminution device 25 with a separator 25 'connected downstream via a line 25 ", the function of which is comparable to that of the separator according to FIG. 2.
- the comminution device 25 is shown in FIG. 3 Shown as a non-self-priming comminution device, so that vapors dedusted from dust are fed to it via a line 26 with the fan switched on.
- the fine material of the separating separator 25 ' is fed via a line 29 not to the fluidized bed dryer 9 but to the vapor electrostatic precipitator 14, which therefore not only removes dust from the vapors emerging from the fluidized bed dryer, but also from the vapors.
- a hammer mill here.
- the shredding device 25 is not followed by a sifter, but via a line 32 directly into the ground material discharged from the shredding device 25 by means of the vapor stream B fed via line 26 the fluidized bed dryer is blown in, preferably above the fluidized bed which arises in the fluidized bed dryer, the top side O of which is shown schematically in FIG. 4.
- the coarse material sinks into the fluidized bed and is conveyed again to the extraction device 12.
- a baffle plate 33 is arranged in the free space above the fluidized bed, onto which the gas / solid mixture stream emerging from line 32 impinges.
- each teat of the fluidized bed dryer 9 or the vapor electrostatic precipitator 14 can be assigned a withdrawal device.
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Drying Of Solid Materials (AREA)
- Beans For Foods Or Fodder (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19612187A DE19612187C2 (de) | 1996-03-27 | 1996-03-27 | Verfahren zur Zerkleinerung und Trocknung von Braunkohle |
DE19612187 | 1996-03-27 | ||
PCT/EP1997/001547 WO1997035944A1 (fr) | 1996-03-27 | 1997-03-26 | Procede pour le broyage et le sechage du lignite |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0891404A1 true EP0891404A1 (fr) | 1999-01-20 |
EP0891404B1 EP0891404B1 (fr) | 2001-10-24 |
Family
ID=7789638
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP97916398A Expired - Lifetime EP0891404B1 (fr) | 1996-03-27 | 1997-03-26 | Procede pour le broyage et le sechage du lignite |
Country Status (7)
Country | Link |
---|---|
EP (1) | EP0891404B1 (fr) |
AU (1) | AU721894B2 (fr) |
DE (2) | DE19612187C2 (fr) |
ES (1) | ES2166534T3 (fr) |
PL (1) | PL329156A1 (fr) |
TR (1) | TR199801936T2 (fr) |
WO (1) | WO1997035944A1 (fr) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109374383A (zh) * | 2018-12-20 | 2019-02-22 | 长沙开元仪器有限公司 | 自动制样系统及方法 |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19946517C2 (de) * | 1999-09-28 | 2001-09-06 | Bbp Energy Gmbh | Verfahren zur Zerkleinerung und Trocknung von feuchtem Brennstoff |
CN102553708B (zh) * | 2012-01-19 | 2013-06-05 | 中国矿业大学 | 一种高灰高水易泥化褐煤洗选工艺 |
DE102012010078A1 (de) * | 2012-05-23 | 2013-11-28 | Rwe Power Ag | Verfahren zur Aufbereitung von grubenfeuchter Rohbraunkohle |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE830375C (de) * | 1949-04-03 | 1952-02-04 | Grosskraftwerk Mannheim A G | Kohlenstaubfeuerung mit Mahltrocknung |
AT367447B (de) * | 1980-04-28 | 1982-07-12 | Voest Alpine Ag | Verfahren zur herstellung eines veredelungsproduktes aus braunkohle |
US4403996A (en) * | 1982-02-10 | 1983-09-13 | Electric Power Development Co. | Method of processing low rank coal |
DD224648A1 (de) * | 1984-06-21 | 1985-07-10 | Inst Energetik Zre Leipzig | Verfahren zur rohkohletrocknung und mahlung zu brennstaub |
US4725337A (en) * | 1984-12-03 | 1988-02-16 | Western Energy Company | Method for drying low rank coals |
DE3644806C1 (en) * | 1986-12-31 | 1993-05-13 | Rheinische Braunkohlenw Ag | Process and plant for drying crude lignite in a fluidized-bed dryer |
-
1996
- 1996-03-27 DE DE19612187A patent/DE19612187C2/de not_active Expired - Fee Related
-
1997
- 1997-03-26 EP EP97916398A patent/EP0891404B1/fr not_active Expired - Lifetime
- 1997-03-26 ES ES97916398T patent/ES2166534T3/es not_active Expired - Lifetime
- 1997-03-26 WO PCT/EP1997/001547 patent/WO1997035944A1/fr active IP Right Grant
- 1997-03-26 AU AU25059/97A patent/AU721894B2/en not_active Ceased
- 1997-03-26 TR TR1998/01936T patent/TR199801936T2/xx unknown
- 1997-03-26 PL PL97329156A patent/PL329156A1/xx unknown
- 1997-03-26 DE DE59705088T patent/DE59705088D1/de not_active Expired - Fee Related
Non-Patent Citations (1)
Title |
---|
See references of WO9735944A1 * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109374383A (zh) * | 2018-12-20 | 2019-02-22 | 长沙开元仪器有限公司 | 自动制样系统及方法 |
CN109374383B (zh) * | 2018-12-20 | 2024-02-27 | 长沙开元仪器有限公司 | 自动制样系统及方法 |
Also Published As
Publication number | Publication date |
---|---|
DE59705088D1 (de) | 2001-11-29 |
DE19612187C2 (de) | 2001-11-15 |
TR199801936T2 (xx) | 1999-01-18 |
WO1997035944A1 (fr) | 1997-10-02 |
PL329156A1 (en) | 1999-03-15 |
AU2505997A (en) | 1997-10-17 |
DE19612187A1 (de) | 1997-10-02 |
EP0891404B1 (fr) | 2001-10-24 |
AU721894B2 (en) | 2000-07-13 |
ES2166534T3 (es) | 2002-04-16 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0384101B1 (fr) | Séparateur pneumatique pour trier des matériaux granulaires et installation de broyage comportant un tel séparateur | |
DE19512509B4 (de) | Verfahren zur Zerkleinerung von Erzmaterial | |
EP0603481B1 (fr) | Procédé et installation pour le broyage de matière à moudre | |
EP3292912B1 (fr) | Procédé de fonctionnement d'un multicyclone pour la séparation de grains fins et ultrafins ainsi que multicyclones | |
EP1084769B1 (fr) | Séparateur pour trier des matériaux granulaires | |
EP3079828A1 (fr) | Système de broyage à circulation à pré-tamis et broyeur à galets | |
WO1991012892A1 (fr) | Broyeur a chocs vertical a triage de matiere accouple | |
EP0629448A2 (fr) | Installation et procédé de broyage et de tamisage de matériau friable | |
EP0548647B1 (fr) | Procédé et dispositif pour la séparation de fibres de cÔtes de tabac et de fibres de feuilles de tabac collées ensemble | |
DE2100235B2 (de) | Verfahren und Mahlanlage zum Trockenvermahlen von Rohmaterialien | |
EP0891404B1 (fr) | Procede pour le broyage et le sechage du lignite | |
DE4039079A1 (de) | Zweistufige vorzerkleinerung bei mahlanlagen | |
DE10054418A1 (de) | Verfahren zum Entfernen von staubförmigen und faserigen Beimengungen aus Schüttgut | |
DE4306930A1 (de) | Anlagentechnische Schaltung zur Zerkleinerung von Mahlgut, vorzugsweise Zementklinker | |
DE102015101530A1 (de) | Zerkleinerungsvorrichtung zur Rückgewinnung von Sekundärrohstoffen aus entsorgtem Material sowie Verfahren zu deren Steuerung | |
DE19946517C2 (de) | Verfahren zur Zerkleinerung und Trocknung von feuchtem Brennstoff | |
DE2804548A1 (de) | Verfahren und vorrichtung zum trennen feuchten papiers von muell | |
EP1090686A1 (fr) | Installation de broyage | |
EP1018371A1 (fr) | Procédé et dispositif pour le traitement de déchets avec broyage ultérieur des fractions de criblage séchées et exemptes de métaux | |
WO2019016031A1 (fr) | Circuit de broyage à deux niveaux et procédé pour la fabrication d'un produit broyé au moyen d'un broyage à deux niveaux | |
DE4034739C2 (de) | Anlage zum Schälen und zur Schalenseparation von Ölsaaten und Verfahren zum Betreiben einer Schäl- und Schalenseparationsanlage für Ölsaaten | |
DE19524711A1 (de) | Verfahren und Vorrichtung zur Verbrennung von Braunkohle | |
WO1996025551A1 (fr) | Procede de recuperation de matieres premieres dans un flux evacue de materiaux residuaires ou collectes lors de la fabrication du papier, et installation utilisee a cet effet | |
DE3815763A1 (de) | Verfahren und anlage zur trocknung feuchter materialien wie z. b. zementrohstoffe mittels eines gasstromes | |
DE10358440B4 (de) | Verfahren zur Aufbereitung von Polstermöbeln in Nutzfraktionen und eine Vorrichtung dazu |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
17P | Request for examination filed |
Effective date: 19981021 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): DE ES GR |
|
GRAG | Despatch of communication of intention to grant |
Free format text: ORIGINAL CODE: EPIDOS AGRA |
|
17Q | First examination report despatched |
Effective date: 20010116 |
|
RAP1 | Party data changed (applicant data changed or rights of an application transferred) |
Owner name: BBP ENERGY GMBH |
|
GRAG | Despatch of communication of intention to grant |
Free format text: ORIGINAL CODE: EPIDOS AGRA |
|
GRAH | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOS IGRA |
|
GRAH | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOS IGRA |
|
GRAH | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOS IGRA |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
RBV | Designated contracting states (corrected) |
Designated state(s): DE ES GR |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): DE ES GR |
|
REF | Corresponds to: |
Ref document number: 59705088 Country of ref document: DE Date of ref document: 20011129 |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FG2A Ref document number: 2166534 Country of ref document: ES Kind code of ref document: T3 |
|
REG | Reference to a national code |
Ref country code: GR Ref legal event code: EP Ref document number: 20010402651 Country of ref document: GR |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed | ||
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: ES Payment date: 20030326 Year of fee payment: 7 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: ES Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20040327 |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FD2A Effective date: 20040327 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GR Payment date: 20090320 Year of fee payment: 13 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20090331 Year of fee payment: 13 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20101001 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20101004 |