DE19707339A1 - Treating red sludge from mining operations, by mixing with chalk and water - Google Patents

Treating red sludge from mining operations, by mixing with chalk and water

Info

Publication number
DE19707339A1
DE19707339A1 DE1997107339 DE19707339A DE19707339A1 DE 19707339 A1 DE19707339 A1 DE 19707339A1 DE 1997107339 DE1997107339 DE 1997107339 DE 19707339 A DE19707339 A DE 19707339A DE 19707339 A1 DE19707339 A1 DE 19707339A1
Authority
DE
Germany
Prior art keywords
water
chalk
red mud
limestone
red sludge
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.)
Ceased
Application number
DE1997107339
Other languages
German (de)
Inventor
Helmut Ziehe
Juergen Pfeiffer
Volker Liebmann
Detlef Lemke
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Vattenfall Europe Generation AG and Co KG
Original Assignee
VEAG Vereinigte Energiewerke AG
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by VEAG Vereinigte Energiewerke AG filed Critical VEAG Vereinigte Energiewerke AG
Priority to DE1997107339 priority Critical patent/DE19707339A1/en
Publication of DE19707339A1 publication Critical patent/DE19707339A1/en
Ceased legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/529Processes or devices for preparing lime water
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/48Sulfur compounds
    • B01D53/50Sulfur oxides
    • B01D53/501Sulfur oxides by treating the gases with a solution or a suspension of an alkali or earth-alkali or ammonium compound
    • B01D53/502Sulfur oxides by treating the gases with a solution or a suspension of an alkali or earth-alkali or ammonium compound characterised by a specific solution or suspension
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/80Semi-solid phase processes, i.e. by using slurries
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/04Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium
    • B01J20/043Carbonates or bicarbonates, e.g. limestone, dolomite, aragonite
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/06Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5236Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/20Heavy metals or heavy metal compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/20Heavy metals or heavy metal compounds
    • C02F2101/203Iron or iron compound
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/10Nature of the water, waste water, sewage or sludge to be treated from quarries or from mining activities

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Analytical Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Water Supply & Treatment (AREA)
  • Biomedical Technology (AREA)
  • Health & Medical Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Treating Waste Gases (AREA)
  • Treatment Of Sludge (AREA)

Abstract

In a process to treat red sludge discharged with water from mining operations and render it fit for disposal at an associated coal-fired power station, the novelty is that:(a) the red sludge is mixed with other substances promoting the desulphurisation of smoke gases and a suspension of chalk; (b) the resulting mixture is employed in a smoke gas washer at a coal-fired power station; (c) the red sludge and ground chalk are placed in a holding basin or tank containing an absorption agent where they are mixed; (d) the red sludge is mixed with the chalk in a wet mill together with additional chalk and water as required, before discharge to the absorption agent basin.

Description

Die Erfindung betrifft ein Verfahren zur Verwertung von Rot­ schlamm aus einer Grubenwasser-Behandlungsanlage.The invention relates to a method for recycling red sludge from a mine water treatment plant.

Für die Entsorgung des bei der Grubenwasser-Behandlung an­ fallenden Rotschlammes sind erhebliche Aufwendungen für Ab­ setzbecken, Transport und Deponie sowie Deponieflächen er­ forderlich.For the disposal of the mine water treatment Falling red mud is a significant expense for Ab settling basin, transport and landfill as well as landfill areas conducive.

Zur Vermeidung derartiger Aufwendungen und Nachteile ist es bekannt, den Rotschlamm in Verbindung mit Bindemitteln und Zuschlagstoffen als Baustoff zu verwenden (DE 195 03 142; DD-PS 244 545), wobei ebenfalls erhebliche Aufwendungen für den Transport sowie für die Bereitstellung von Binde- und Dichtmitteln zur Vermeidung von Auswaschungen erforderlich sind.It is to avoid such expenses and disadvantages known, the red mud in connection with binders and To use aggregates as building material (DE 195 03 142; DD-PS 244 545), whereby also considerable expenses for the transport as well as for the provision of binding and Sealants required to avoid leaching are.

Der Erfindung liegt die Aufgabe zugrunde, den Rotschlamm am Kraftwerksstandort ohne zusätzliche Aufwendungen und bei Wegfall der bisherigen Aufwendungen für die Entsorgung zu verwerten.The invention is based, the red mud on the task Power plant location without additional expenses and at Elimination of previous disposal costs recycle.

In überraschender Weise wurde gefunden, daß der mit anderen entschwefelungswirksamen Substanzen versetzte Rotschlamm zur Herstellung einer Kalkstein-Suspension für die Entschwefe­ lung von Rauchgasen eines Kohlekraftwerkes in einem Gas­ wäscher verwendet wird.Surprisingly, it was found that with others Desulphurizing substances added red mud Production of a limestone suspension for desulphurization development of flue gases from a coal-fired power plant in one gas scrubber is used.

Für die Rauchgasentschwefelung in einem Gaswäscher wird mit hohen Aufwendungen für die Gewinnung und für den Transport des Kalksteins sowie für dessen Aufbereitung eine Kalkstein-Sus­ pension hergestellt. Es hat daher nicht an Versuchen ge­ fehlt, diese Aufwendungen für die Herstellung einer Absorp­ tionsmittel-Suspension zu mindern.For flue gas desulfurization in a gas scrubber high costs for extraction and transportation of the limestone and a limestone sus for its preparation pension manufactured. There has therefore been no attempt at it missing, these expenses for the production of an absorber reducing agent suspension.

So ist es bekannt, die bei der Entkarbonisierung der Dampf­ kraftwerkswässer entstehenden Schlämme und die bei der Naß­ entaschung anfallenden Schlämme direkt als Absorptionsmittel zu verwenden (DE 35 04 775, DD 213 358). Ebenso ist be­ kannt, die bei der Vorreinigung von Wässern mit Eisensalz- Aufschwemmungen entstehenden Abprodukte als Absorptionsmit­ tel für die Rauchgasentschwefelung einzusetzen (DE 43 19 461 DD 289 932). Diese Verfahrensweisen sind jedoch nur dann an­ wendbar, wenn in einem Kraftwerk derartige Wasserbehand­ lungstechnologien durchgeführt werden.So it is known to decarbonize the steam Power station water sludge and the wet Ash removal from the sludge directly as an absorbent to be used (DE 35 04 775, DD 213 358). Likewise, be knows that when pre-cleaning water with iron salt  Wastes created as an absorption medium tel for flue gas desulfurization (DE 43 19 461 DD 289 932). However, these procedures are only on reversible when such water treatment in a power plant technologies are carried out.

Weiterhin wird für die Herstellung der Absorptionsmittelsus­ pension eine erhebliche Menge an Wasser sowie Aufwendungen für dessen Aufbereitung benötigt.Furthermore, for the manufacture of the absorbent pension a significant amount of water as well as expenses needed for its preparation.

An einem Ausführungsbeispiel wird die Erfindung näher erläu­ tert. Die Zeichnung zeigt das Anlagenschema für die Verwer­ tung des Rotschlammes zur Entschwefelung der Rauchgase eines Kohlekraftwerkes im Gaswäscher.The invention is explained in more detail using an exemplary embodiment tert. The drawing shows the system diagram for the recycling company treatment of the red mud to desulfurize the flue gases Coal-fired power plant in the scrubber.

Der Grubenwasserzuleiter 1 ist in die Wasserbehandlungsanla­ ge 2 des Kohlekraftwerkes eingebunden. Die Wasserbehand­ lungsanlage 2 ist zum einen mit dem Absetzbecken 3 und zum anderen mit der Kalkstein-Naßmühle 4 verbunden. Der Austrag der Kalkstein-Naßmühle 4 ist in den Absorptionsmittelbehäl­ ter 5 des Gaswäschers 6 eingebunden.The pit water supply 1 is integrated into the water treatment plant 2 of the coal-fired power plant. The water treatment plant 2 is connected on the one hand to the sedimentation basin 3 and on the other hand to the limestone wet mill 4 . The discharge of the limestone wet mill 4 is included in the absorption medium container 5 of the scrubber 6 .

Die Wirkungsweise ist folgende:
Das Grubenwasser 7 gelangt aus dem Grubenwasserzuleiter 1 zur Enteisenung in die Wasserbehandlungsanlage 2. Durch Zu­ gabe von Kalkmilch 8 und falls erforderlich Flockungshilfs­ mittel wird durch den chemischen Wirkungsmechanismus der Rotschlamm 10 zur Verwertung gebildet und Rohwasser 9 für den Kraftwerksprozeß erzeugt bzw. in ein Gewässer abgegeben. Der Rotschlamm 10 enthält aufgrund der Grubenwasser-Inhalts­ stoffe und der Kalkmilch-Inhaltsstoffe entschwefelungswirk­ same Stoffe, wie Eisen-III-Hydroxid, sowie Wasser. Der Rot­ schlamm 10 wird in die Kalkstein-Naßmühle 4 aufgegeben.
The mode of action is as follows:
The pit water 7 passes from the pit water feeder 1 for iron removal into the water treatment plant 2 . By adding lime milk 8 and, if necessary, flocculation aids, the red mud 10 is formed for recycling by the chemical mechanism of action and raw water 9 is generated for the power plant process or released into a body of water. The red mud 10 contains due to the mine water content substances and the milk of lime ingredients desulfurization active substances, such as ferric hydroxide, and water. The red mud 10 is abandoned in the limestone wet mill 4 .

Gleichzeitig wird Kalksteinschotter und gegebenenfalls Was­ ser der Kalkstein-Naßmühle 4 aufgegeben. At the same time limestone gravel and what water the limestone wet mill 4 is abandoned.

Falls aus bestimmten Gründen der Rotschlamm 10 nicht im er­ forderlichen Umfang für die Rauchgasentschwefelung benötigt wird, so wird dieser in das Absetzbecken 3 gefördert und als Deponiegut 11 entsorgt bzw. zur weiteren Verwertung abgela­ gert. Durch den Naßmahlprozeß wird die Kalkstein-Rotschlamm-Sus­ pension 14 erzeugt und in den Absorptionsmittelbehälter 5 gefördert. Dabei gelangt die Suspension 15 in die Düsenebe­ nen des Gaswäschers 6.If, for certain reasons, the red mud 10 is not required to the extent necessary for the flue gas desulfurization, this is conveyed into the settling basin 3 and disposed of as landfill material 11 or stored for further use. By the wet grinding process, the limestone-red mud Sus pension 14 is generated and promoted in the absorbent container 5 . The suspension 15 passes into the nozzle plane of the scrubber 6 .

Durch den chemischen Wirkungsmechanismus, vor allem im in­ ternen Kreislauf des Gaswäschers 6 wird aus dem Rotschlamm farbloses Eisensulfat gebildet, daß mit dem REA-Wasser zur Ascheanfeuchtung ausgeschleust wird. Somit hat der verwende­ te Rotschlamm keinen negativen Einfluß auf die aus dem Kreislauf des Gaswäschers auszuschleusende Suspension für die Gipsgewinnung, so daß eine Gipsqualität mit hohem Weiß­ grad erzeugt wird.Due to the chemical mechanism of action, especially in the internal cycle of the gas scrubber 6 , colorless iron sulfate is formed from the red mud, which is removed with the FGD water for moistening the ash. Thus, the used red mud has no negative influence on the suspension for gypsum extraction to be removed from the circuit of the gas scrubber, so that a gypsum quality with a high degree of whiteness is produced.

Ebenso ist es möglich, den Rotschlamm 10, jedoch dann mit Kalksteinmehl und gegebenenfalls Wasser, direkt in den Ab­ sorptionsmittelbehälter 5 aufzugeben.It is also possible to give the red mud 10 , but then with limestone powder and optionally water, directly into the sorbent container 5 .

Durch die Erfindung treten folgende wesentliche Vorteile auf:
The following significant advantages arise from the invention:

  • 1. Der Aufwand für die Entsorgung des Rotschlammes, z. B. durch das Kraftwerk, entfällt.1. The effort for the disposal of the red mud, eg. B. due to the power plant.
  • 2. Der Aufwand für die Bereitstellung von Deponieflächen und deren Betrieb entfällt.2. The effort for the provision of landfill areas and their operation is eliminated.
  • 3. Der Aufwand für die Vermeidung von Auswaschungen aus dem Deponiekörper oder aus Baukörpern entfällt.3. The effort to avoid leaching from the Landfill bodies or buildings are no longer required.
  • 4. Der Aufwand für die Bereitstellung des Kalksteines wird wesentlich vermindert4. The effort required to provide the limestone significantly reduced
  • 5. Die Aufwendungen für das bereitzustellende Wasser werden wesentlich reduziert bzw. entfallen.5. The expenses for the water to be provided significantly reduced or eliminated.
  • 6. Der Abwasseranfall wird reduziert.6. The amount of wastewater is reduced.
BezugszeichenlisteReference list

11

Grubenwasserzuleiter
Mine water supply

22nd

Abwasserbehandlungsanlage
Wastewater treatment plant

33rd

Absetzbecken
Sedimentation tanks

44th

Kalkstein-Naßmühle
Limestone wet mill

55

Absorptionsmittelbehälter
Absorbent container

66

Gaswäscher
Gas scrubber

77

Grubenwasser
Mine water

88th

Wasserbehandlungsmittel
Water treatment agent

99

Rohwasser
Raw water

1010th

Rotschlamm
Red mud

1111

Deponiegut
Landfill

1212th

Kalksteinschotter
Limestone gravel

1313

Wasser
water

1414

Kalkstein-Rotschlamm-Suspension
Limestone-red mud suspension

1515

Suspension
suspension

Claims (3)

1. Verfahren zur Verwertung von Rotschlamm aus einer Gruben­ wasser-Behandlungsanlage, gekennzeichnet dadurch, daß der mit anderen entschwefelungswirksamen Substanzen ver­ setzte Rotschlamm zur Herstellung einer Kalkstein-Suspension für die Entschwefelung von Rauchgasen eines Kohlekraftwerkes in einem Gaswäscher verwendet wird.1. A process for the recovery of red mud from a mine water treatment system, characterized in that the red mud with other desulfurizing substances is used to produce a limestone suspension for the desulfurization of flue gases from a coal-fired power plant in a gas scrubber. 2. Verfahren nach Anspruch 1, gekennzeichnet dadurch, daß der Rotschlamm mit Kalksteinmehl und gegebenenfalls Wasser in einen Absorptionsmittel-Behälter aufgegeben und gemischt wird.2. The method according to claim 1, characterized in that the red mud with limestone flour and, if necessary, water placed in an absorbent container and mixed becomes. 3. Verfahren nach Anspruch 1, gekennzeichnet dadurch, daß der Rotschlamm einer Kalkstein-Naßmühle mit Zugabe neu zu mahlenden Kalksteinschotters und gegebenenfalls Wasser auf­ gegeben und in einen Absorptionsmittelbehälter gefördert wird.3. The method according to claim 1, characterized in that the red mud of a limestone wet mill with an addition grinding limestone gravel and, if necessary, water given and conveyed into an absorbent container becomes.
DE1997107339 1997-02-14 1997-02-14 Treating red sludge from mining operations, by mixing with chalk and water Ceased DE19707339A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DE1997107339 DE19707339A1 (en) 1997-02-14 1997-02-14 Treating red sludge from mining operations, by mixing with chalk and water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE1997107339 DE19707339A1 (en) 1997-02-14 1997-02-14 Treating red sludge from mining operations, by mixing with chalk and water

Publications (1)

Publication Number Publication Date
DE19707339A1 true DE19707339A1 (en) 1998-08-20

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Country Link
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102008018854A1 (en) 2008-04-15 2009-10-22 Conny Brachmann Processing sulfate-containing mine seepage- and mine sewage-water, comprises collecting water in container, conducting sulfate-containing water in reaction container, collecting mine seepage water and neutralizing chloride-containing water
US20200299207A1 (en) * 2019-03-22 2020-09-24 Kunming University Of Science And Technology Method for ammonium-enhanced flue gas desulfurization by using red mud slurry
CN113398749A (en) * 2021-05-14 2021-09-17 国能宿州热电有限公司 Feeding process of calcium-containing sludge recycling system of water purification system of coal-fired power plant

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102008018854A1 (en) 2008-04-15 2009-10-22 Conny Brachmann Processing sulfate-containing mine seepage- and mine sewage-water, comprises collecting water in container, conducting sulfate-containing water in reaction container, collecting mine seepage water and neutralizing chloride-containing water
US20200299207A1 (en) * 2019-03-22 2020-09-24 Kunming University Of Science And Technology Method for ammonium-enhanced flue gas desulfurization by using red mud slurry
US11535572B2 (en) * 2019-03-22 2022-12-27 Kunming University Of Science And Technology Method for ammonium-enhanced flue gas desulfurization by using red mud slurry
CN113398749A (en) * 2021-05-14 2021-09-17 国能宿州热电有限公司 Feeding process of calcium-containing sludge recycling system of water purification system of coal-fired power plant
CN113398749B (en) * 2021-05-14 2024-05-31 国能宿州热电有限公司 Throwing process of calcium-containing sludge recycling system of water quality purification system of coal-fired power plant

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Owner name: VATTENFALL EUROPE GENERATION AG & CO. KG, 10115 BE

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Owner name: VATTENFALL EUROPE GENERATION AG & CO. KG, 03050 CO

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