DE2253591A1 - PROCESS FOR THE PURIFICATION AND RECOVERY OF INGREDIENTS OF EXHAUST GASES FROM METALLURGICAL MELTING PROCESSES - Google Patents
PROCESS FOR THE PURIFICATION AND RECOVERY OF INGREDIENTS OF EXHAUST GASES FROM METALLURGICAL MELTING PROCESSESInfo
- Publication number
- DE2253591A1 DE2253591A1 DE2253591A DE2253591A DE2253591A1 DE 2253591 A1 DE2253591 A1 DE 2253591A1 DE 2253591 A DE2253591 A DE 2253591A DE 2253591 A DE2253591 A DE 2253591A DE 2253591 A1 DE2253591 A1 DE 2253591A1
- Authority
- DE
- Germany
- Prior art keywords
- exhaust gases
- water
- ingredients
- recovery
- purification
- 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.)
- Pending
Links
- 239000007789 gas Substances 0.000 title claims description 16
- 238000000034 method Methods 0.000 title claims description 16
- 238000010309 melting process Methods 0.000 title claims description 6
- 239000004615 ingredient Substances 0.000 title claims description 3
- 238000011084 recovery Methods 0.000 title claims description 3
- 238000000746 purification Methods 0.000 title description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 18
- 239000010802 sludge Substances 0.000 claims description 12
- 238000005406 washing Methods 0.000 claims description 8
- 238000001556 precipitation Methods 0.000 claims description 6
- 239000003575 carbonaceous material Substances 0.000 claims description 5
- 238000003723 Smelting Methods 0.000 claims description 4
- 238000004140 cleaning Methods 0.000 claims description 4
- 239000000470 constituent Substances 0.000 claims description 4
- 239000007787 solid Substances 0.000 claims description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 3
- 239000000571 coke Substances 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 3
- 150000002825 nitriles Chemical class 0.000 claims description 3
- 230000003647 oxidation Effects 0.000 claims description 3
- 238000007254 oxidation reaction Methods 0.000 claims description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 2
- 230000003197 catalytic effect Effects 0.000 claims description 2
- 239000003245 coal Substances 0.000 claims description 2
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 claims description 2
- 230000000717 retained effect Effects 0.000 claims description 2
- 239000011572 manganese Substances 0.000 description 8
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 7
- 229910052748 manganese Inorganic materials 0.000 description 7
- 239000000428 dust Substances 0.000 description 6
- 238000001914 filtration Methods 0.000 description 4
- 241000196324 Embryophyta Species 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 229910015136 FeMn Inorganic materials 0.000 description 2
- 238000005054 agglomeration Methods 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 229910000616 Ferromanganese Inorganic materials 0.000 description 1
- 229910000914 Mn alloy Inorganic materials 0.000 description 1
- 241000209504 Poaceae Species 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 239000003657 drainage water Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- DALUDRGQOYMVLD-UHFFFAOYSA-N iron manganese Chemical compound [Mn].[Fe] DALUDRGQOYMVLD-UHFFFAOYSA-N 0.000 description 1
- 238000009925 jellying Methods 0.000 description 1
- 231100000518 lethal Toxicity 0.000 description 1
- 230000001665 lethal effect Effects 0.000 description 1
- PYLLWONICXJARP-UHFFFAOYSA-N manganese silicon Chemical compound [Si].[Mn] PYLLWONICXJARP-UHFFFAOYSA-N 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 150000002736 metal compounds Chemical class 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B7/00—Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
- C22B7/02—Working-up flue dust
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/18—Nature of the water, waste water, sewage or sludge to be treated from the purification of gaseous effluents
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- Hydrology & Water Resources (AREA)
- Water Supply & Treatment (AREA)
- Mechanical Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Treating Waste Gases (AREA)
- Treatment Of Sludge (AREA)
- Removal Of Specific Substances (AREA)
Description
Slkem A/S, Oslo 3, Majorstua.Slkem A / S, Oslo 3, Majorstua.
Verfahren zur Reinigung und Rückgewinnung der Inhaltsstoffe von Abgasen metallurgischer SchmelzprozesseoMethods for cleaning up and recovering the ingredients of exhaust gases from metallurgical smelting processes o
Die Erfindung betrifft ein Verfahren zur Reinigung und Rückgewinnung der Inhaltsstoffe von Abgasen metallurgischer Schmelzprozesse, bei dem die Abgase mit den in ihnen enthaltenen feststoffen in Wasser eingeführt werden und ein schlammhaltiges Waschwasser bilden, das aufgearbeitet wird.The invention relates to a method for cleaning and recovering the constituents of metallurgical exhaust gases Melting processes in which the exhaust gases with the solids they contain are introduced into water and a Form sludge-containing washing water that is processed.
Die aus Oefen für metallurgische Schmelzprozesse abgehenden G-ase führen feste Partikeln mit sich, die teils aus Staub von den Rohmaterialien und teils aus Stoffen bestehen, die aus den Ofengasen ausfallen. Der Staub kann in Fasswäschern konventionellen Typs niedergeschlagen werden, und die Abwässer dieser Wäscher werden üblicherweise in Gewässer geleitet. Unmittelbares Ablassen von Gasen oder Abflusswässern führt zu Verunreinigung von Luft bzw» Wasser, und hinzu kommt noch der Verlust wertvoller Rohmaterialien und herabgesetzter Ertrag des Prozesses.The gases leaving furnaces for metallurgical smelting processes carry solid particles with them, some of them from dust consist of the raw materials and partly of substances that precipitate from the furnace gases. The dust can in barrel washers conventional type, and the effluents from these scrubbers are usually discharged into bodies of water. Immediate discharge of gases or runoff water leads to contamination of air or water, and in addition still comes the loss of valuable raw materials and degraded ones Output of the process.
Bei einigen Schmelzverfahren, z. B. bei der Herstellung von Manganlegierungen, wie Ferromangan, Siliciummangan, enthält der Staub beträchtliche Mengen Mangan in sowohl Form von mitgerissenen als auch ausgefällten Partikeln. Beispiels-In some melting processes, e.g. B. in the production of manganese alloys, such as ferromanganese, silicon manganese contains the dust contained significant amounts of manganese in the form of both entrained and precipitated particles. Example
309821/0703309821/0703
weise entwickelt ein Ofen zur Herstellung von hochgekohltem FeMn etwa 85o Hm'' Gas pro Tonne produzierter Legierung,, Die Grase enthalten etwa 25 g Staub pro Nm . Der Staub enthält wiederum 30 - 4o Gew„$ Mangan» Somit gehen groase Mengen wertvollen Mangans mit dem Staub oder dem Schlamm verloren,.Weise developed a furnace for the production of high-carbon FeMn about 85o Hm "gas per ton of produced alloy, the grasses contain about 25 g of dust per Nm. The dust in turn contains 30 - 40 wt. "$ Manganese". Thus, large amounts of valuable manganese are lost with the dust or sludge.
Es sind mehrere Versuche gemacht worden, um den Metallgehalt des Schlammes aus Reinigungsanlagen für Gase von metallurgischen Schmelzprozessen zurückzugewinnen, wobei Nassanlagen betrieben wurden« Man hat u. ao den Schlamm zu Briketts oder Pellets agglomeriert 9 die dann zum Schmelzofen zurückgeführt wurden. Derartige Agglomerierungsprozesse sind jedoch nicht nur kompliziert, sondern auch teuer, weil sie sowohl das Fällen des Schlammes als auch das Trocknen und die Agglomerierung aov/ie gegebenenfalls das Härten der Agglomerate umfassenοThere have been several attempts to the metal content of the sludge from cleaning plants for gases of metallurgical melting processes recover, wherein wet plants were operated "It has u. A o the sludge into briquettes or pellets agglomerated 9 which were then returned to the furnace. Such agglomeration processes are not only complicated, but also expensive, because they include both the precipitation of the sludge and the drying and agglomeration, or possibly the hardening of the agglomerates o
Es wurde nun ein einfaches und wirksames Verfahren zur Aufsammlung und Rückführung des Metallgehaltes im Schlamm aum Schmelzofen gefunden.It has now become a simple and effective method of collecting and recycling the metal content in the sludge Found around the furnace.
Das Verfahren der Erfindung zur Reinigung und Rückgewinnung der Inhaltsstoffe von Abgasen metallurgischer Schmelzprozesse durch Einführung der Feststoffs enthaltenden Abgase in Wasser ist dadurch gekennzeichnet, dass das schlammhaltige Waschwasser durch wenigstens ein Filter aus carbonhaltigem Material, wie Kohle oder Koks, hindurchgeführt wird, worauf das so gereinigte Waschwasser abgelassen oder weiter zum Waschen der Abgase verwendet und das carbonhaltige Material zusammen mit den von ihm zurückgehaltenen Inhaltsstoffen einem metallurgischem Schmelzprozess zugeführt wird·The method of the invention for purifying and recovering the constituents of exhaust gases from metallurgical smelting processes by introducing the solid-containing exhaust gases into water is characterized in that the sludge-containing Wash water is passed through at least one filter made of carbonaceous material, such as coal or coke, whereupon the so cleaned washing water is drained or further used for washing the exhaust gases and the carbon-containing material is fed to a metallurgical melting process together with the constituents retained by it
Nach einer Ausführungaform der Erfindung wird zur Rückgewinnung von Mangan der pH-Wert des Waschwassers auf :;ur optimalen Fällung geeignete Werte eingestellt.According to one embodiment of the invention, for recovery of manganese, the pH of the washing water is set to:; values suitable for optimal precipitation.
Durch Einstellung auf optimalen pH-Wort wird :;. B. ManganBy setting to optimal pH word,:;. B. Manganese
709821/0701 BAD ORfGiNAL709821/0701 BAD ORfGiNAL
annähernd quantitativ ausgefällt„ Im lalle des Ausfällens von Mangan soll der pH-Wert grosser als 7 sein» Durch-Justierung des pH-Werts und eventuelle Zugabe von Alkalien zum Wasser vor dem Filtern kann ein Ausfällen auch von gelösten Metallverbindungen etc. bewirkt werden, die dann nach der Ausfällung von den Filtern aufgenommen werden.almost quantitatively precipitated “In the course of precipitation the pH of manganese should be greater than 7 »through adjustment The pH value and the eventual addition of alkalis to the water before filtering can cause precipitation of dissolved water Metal compounds etc. are brought about, which are then taken up by the filters after the precipitation.
Beim Filtrieren kann auch das Abflusswasser von schädlichen Stoffen, Zo B. Cyaniden, befreit werden, da die Cyanide auf Grund der katalytischen Wirkung des Carbonmaterials oxydiereno Die Oxydation kann gegebenenfalls durch Einblasen von luft in die Filter gesteigert werden,,When filtering, the drainage water can also be freed of harmful substances, such as cyanides, as cyanides Oxidation due to the catalytic effect of the carbon material to be increased by air in the filter,
Eine kontinuierliche Reinigung des Abwassers wird die Verwendung von zwei oder mehreren Filteranlagen fordern, damit ein Filtersatz entfernt werden kann, während der andere oder die anderen Sätze in Betrieb sindo Jede Filteranlage müsste dann selbstverständlich mit Vorrichtungen für ein rasches Ein- und Ausschalten ausgerüstet sein»Continuous purification of the wastewater will require the use of two or more filter systems one filter set can be removed while the other or the other sets are in operation o Each filter system would then of course have to be equipped with devices for quick switching on and off »
Das Abwasser von einer Reinigungsanlage zum 7feschen der Gase von einem Ofen zur Herstellung von FeMn wurde durch Koksfilter filtrierte iJs wurden dem Wasser vor und nach den Filtern Proben entnommen. Die Proben wurden auf die in Jackson Trubidity Units (J.ToUo) angegebene Trübung sowie auf den Schlamm- und Mangangehalt analysierteThe wastewater from a purification plant to remove the gases from a furnace for the production of FeMn was filtered through coke filters iJs were the water before and after the filters Samples taken. The samples were tested for the turbidity given in Jackson Trubidity Units (J.ToUo) as well as for the sludge and Analyzed manganese content
Tor dem Filtern Bach dem FilternGate to the filtering brook to the filtering
Trübung (J.ToU.) 1ooo 3-5Turbidity (J.ToU.) 1ooo 3-5
Schlammgehalt (mg/l Wasser) I800 5Sludge content (mg / l water) I800 5
Mn-Gehalt (mg/l Wasser) 265 1 1Mn content (mg / l water) 265 1 1
Die Trübung wird demnach auf os5 fo des ursprünglichen Wertes reduziert, während 99 S7 cß> des Schlammes und 99?6 $ des Mangans zurückgewonnen xverden konnten«The turbidity is accordingly reduced to o s 5 fo of the original value, while 99 S 7 c ß> of the sludge and 99? 6 $ of the manganese could be recovered "
jjio CarbonfiJ.tcr können nach beendetem Gebrauch dem Schmelzofen ».Ι« ifod uktionuinat ο rial zugeführt worden» Dadurch wirdjjio CarbonfiJ.tcr you can use the melting furnace ».Ι« ifod uktionuinat ο rial been supplied »thereby becomes
309821/0103309821/0103
auch die Letallausbeute des Verfahrens gesteigert. Die Garbonfilter können gegebenenfalls auch einem anderen Sci'unelzprozess zugeführt werden, bei dem das Carbonmaterial als Reduktionsmittel und der ausgefällte Schlamm als Zusatzmaterial Verwendung finden können 0 the lethal yield of the process is also increased. The Garbonfilter may optionally also another Sci'unelzprozess be fed, wherein the carbon material as the reducing agent and the precipitated sludge can be used as additive material 0
Bei dem Verfahren der Erfindung wird die Errichtung von i^lllungsgruben bzwe jyällungskeaoel ersparte Auch wird somit eine erhebliche Platzoinsparung zuzüglich zu den technischwirtsch'.t.ftlichen Vorteilen erzielteIn the method of the invention, the construction of filling pits or jellying oil is saved. A considerable saving in space is thus achieved in addition to the technical and economic advantages
309821/0703309821/0703
Claims (3)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| NO04087/71*[A NO126745B (en) | 1971-11-05 | 1971-11-05 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| DE2253591A1 true DE2253591A1 (en) | 1973-05-24 |
Family
ID=19880062
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DE2253591A Pending DE2253591A1 (en) | 1971-11-05 | 1972-11-02 | PROCESS FOR THE PURIFICATION AND RECOVERY OF INGREDIENTS OF EXHAUST GASES FROM METALLURGICAL MELTING PROCESSES |
Country Status (11)
| Country | Link |
|---|---|
| JP (1) | JPS5327682B2 (en) |
| CA (1) | CA983727A (en) |
| DE (1) | DE2253591A1 (en) |
| ES (1) | ES408280A1 (en) |
| FI (1) | FI55640C (en) |
| FR (1) | FR2158516B1 (en) |
| GB (1) | GB1371113A (en) |
| IT (1) | IT968980B (en) |
| NO (1) | NO126745B (en) |
| SE (1) | SE383360B (en) |
| ZA (1) | ZA727262B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0040643A1 (en) * | 1980-05-24 | 1981-12-02 | AMSTED Industries Incorporated | Method for separating particulate matter into soluble and insoluble portions and apparatus for performing said method |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA975876A (en) * | 1972-09-27 | 1975-10-07 | Universite De Sherbrooke | Purification of metal polluted waters |
| NO330140B1 (en) * | 2008-12-12 | 2011-02-21 | Gosta Larssons Mek Verkst Ab | Process for the preparation of a manganese alloy |
| CN108928999A (en) * | 2018-08-13 | 2018-12-04 | 武汉新天达美环境科技股份有限公司 | A kind of purifying treatment method for basin sewage |
-
1971
- 1971-11-05 NO NO04087/71*[A patent/NO126745B/no unknown
-
1972
- 1972-01-04 ES ES408280A patent/ES408280A1/en not_active Expired
- 1972-10-11 ZA ZA727262A patent/ZA727262B/en unknown
- 1972-10-16 IT IT3052672A patent/IT968980B/en active
- 1972-10-25 FI FI295972A patent/FI55640C/en active
- 1972-10-26 GB GB4948772A patent/GB1371113A/en not_active Expired
- 1972-11-02 JP JP10959172A patent/JPS5327682B2/ja not_active Expired
- 1972-11-02 CA CA155,448A patent/CA983727A/en not_active Expired
- 1972-11-02 DE DE2253591A patent/DE2253591A1/en active Pending
- 1972-11-03 FR FR7239025A patent/FR2158516B1/fr not_active Expired
- 1972-11-03 SE SE1426672A patent/SE383360B/en unknown
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0040643A1 (en) * | 1980-05-24 | 1981-12-02 | AMSTED Industries Incorporated | Method for separating particulate matter into soluble and insoluble portions and apparatus for performing said method |
Also Published As
| Publication number | Publication date |
|---|---|
| IT968980B (en) | 1974-03-20 |
| FR2158516B1 (en) | 1976-04-23 |
| JPS4853903A (en) | 1973-07-28 |
| ZA727262B (en) | 1974-05-29 |
| GB1371113A (en) | 1974-10-23 |
| SE383360B (en) | 1976-03-08 |
| FI55640C (en) | 1979-09-10 |
| FI55640B (en) | 1979-05-31 |
| ES408280A1 (en) | 1975-11-01 |
| CA983727A (en) | 1976-02-17 |
| JPS5327682B2 (en) | 1978-08-10 |
| NO126745B (en) | 1973-03-19 |
| FR2158516A1 (en) | 1973-06-15 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| OHA | Expiration of time for request for examination |