DE529384C - Process for dewatering and decomposition of iron vitriol (Fe S Oíñ 7H O) - Google Patents
Process for dewatering and decomposition of iron vitriol (Fe S Oíñ 7H O)Info
- Publication number
- DE529384C DE529384C DEI33158D DEI0033158D DE529384C DE 529384 C DE529384 C DE 529384C DE I33158 D DEI33158 D DE I33158D DE I0033158 D DEI0033158 D DE I0033158D DE 529384 C DE529384 C DE 529384C
- Authority
- DE
- Germany
- Prior art keywords
- decomposition
- iron
- drainage
- oíñ
- dewatering
- 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.)
- Expired
Links
- 238000000354 decomposition reaction Methods 0.000 title claims description 13
- 238000000034 method Methods 0.000 title claims description 13
- SURQXAFEQWPFPV-UHFFFAOYSA-L iron(2+) sulfate heptahydrate Chemical group O.O.O.O.O.O.O.[Fe+2].[O-]S([O-])(=O)=O SURQXAFEQWPFPV-UHFFFAOYSA-L 0.000 title claims description 3
- 229910000359 iron(II) sulfate Inorganic materials 0.000 title claims description 3
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 claims description 12
- 230000003647 oxidation Effects 0.000 claims description 8
- 238000007254 oxidation reaction Methods 0.000 claims description 8
- 229910000287 alkaline earth metal oxide Inorganic materials 0.000 claims description 4
- 238000001035 drying Methods 0.000 claims description 3
- 239000003513 alkali Substances 0.000 claims description 2
- 150000004649 carbonic acid derivatives Chemical class 0.000 claims description 2
- 150000004679 hydroxides Chemical class 0.000 claims description 2
- 238000005979 thermal decomposition reaction Methods 0.000 claims description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims 1
- 159000000014 iron salts Chemical class 0.000 claims 1
- -1 iron salts Iron compounds Chemical class 0.000 claims 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 4
- 239000000203 mixture Substances 0.000 description 3
- 239000005569 Iron sulphate Substances 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 229910000358 iron sulfate Inorganic materials 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 235000003891 ferrous sulphate Nutrition 0.000 description 1
- 239000011790 ferrous sulphate Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G49/00—Compounds of iron
- C01G49/02—Oxides; Hydroxides
- C01G49/06—Ferric oxide [Fe2O3]
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Processing Of Solid Wastes (AREA)
- Compounds Of Iron (AREA)
Description
Verfahren zur Entwässerung und Zersetzung von Eisenvitriol (Fe S 04. 7 H2 0) Alle bisherigen Verfahren zur Darstellung von Eisenoxyd aus Eisensulfat durch thermische Zersetzung leiden daran, daß das Eisensulfat sowohl beim Trocknen als auch bei der nachherigen Oxydation stark zum Sintern neigt, wodurch ein Teil der Rasse der Oxydationswirkung des Sauerstoffs entzogen wird und die vollständige Zersetzung erst bei höherer Temperatur stattfindet; außerdem tritt bei sämtlichen Verfahren infolge der notwendigen hohen Temperaturen eine nachträgliche Zersetzung des gebildeten SO, ein, so daß bisher die Ausbeuten recht unbefriedigend waren.Process for the dehydration and decomposition of iron vitriol (Fe S 04.7 H2 0) All previous processes for the preparation of iron oxide from iron sulphate by thermal decomposition suffer from the fact that the iron sulphate has a strong tendency to sinter both during drying and during subsequent oxidation Part of the race of the oxidative effect of oxygen is withdrawn and complete decomposition only takes place at a higher temperature; In addition, in all processes, as a result of the high temperatures required, subsequent decomposition of the SO formed occurs, so that the yields have hitherto been quite unsatisfactory.
Es wurde nun ein Verfahren gefunden, das diese Mängel dadurch beseitigt, daß z. ein Magerungsmittel zugesetzt wird, wodurch die gesamte Masse locker und porös bleibt und die Durchführung der Entwässerung, Oxydation und Zersetzung in einem Arbeitsgange möglich wird, ohne daß z. B. bei Dr ehöfen ein Anbacken an der Drehofenwandung zu befürchten wäre; Z. durch die Zugabe von Eisenoxyd, das bei den angewandten Temperaturen als Katalysator wirkt, die Rückbildung des SO., aus OZ und SO, befördert wird.A method has now been found which overcomes these shortcomings in that, for. a lean agent is added, whereby the entire mass remains loose and porous and the implementation of the drainage, oxidation and decomposition is possible in one operation without z. B. in dr ehöfen caking on the rotary kiln wall would be feared; Z. by adding iron oxide, which acts as a catalyst at the temperatures used, the regression of SO., From OZ and SO, is promoted.
So wird z. B. bei Zusatz von Eisenoxyd zum Eisensulfat eine Mischung erhalten, die nicht im Drehofen schmiert oder läuft, jeden beliebigen Oxydationsverlauf gestattet und die fast restlose Rückgewinnung der Schwefelsäure in Form von SO, ermöglicht.So z. B. when iron oxide is added to the iron sulfate, a mixture is obtained that does not smear or run in the rotary kiln, allows any oxidation process and enables almost complete recovery of the sulfuric acid in the form of SO.
Unter gewissen Umständen, beispielsweise bei anhaftender Schwefelsäure, ist es vorteilhaft, der Mischung kleine Mengen Alkali-oder Erdalkalioxyde, -hydroxyde oder -carbonate zuzufügen, wodurch einerseits ein Verdampfen der Säure beim Trocknen verhindert und andererseits die Zersetzungstemperatur selbst herabgesetzt wird. Beispiel r Eisensulfat mit 7 aq wird mit 2o bis 3o °@" Eisenoxyd, das bei der Zersetzung erhalten wurde, vermischt und zunächst in einem Drehofen bei Temperaturen von Zoo bis 300° entwässert. Zweckmäßig wird hierbei für oxydierende Atmosphäre Sorge getragen. Von hieraus gelangt die Mischung in einen zweiten Drehofen, wo sie in oxydierender Atmosphäre auf .4oo bis 5oo° erhitzt wird. \lach Beendigung des Oxydationsprozesses passiert das Material einen dritten Ofen, der beispielsweise auf 75o bis 85o° erhitzt werden muß. Natürlich können auch die einzelnen Stufen derart zusammengelegt werden, daß z. B. die Oxydation und Entwässerung in einem Ofen oder die Oxydation in einem anderen Ofen stattfindet, bzw. daß der gesamte P4ozeß in einem einzigen Ofen vor sich geht.Under certain circumstances, for example with adhering sulfuric acid, it is advantageous to add small amounts of alkali or alkaline earth oxides or hydroxides to the mixture or to add carbonates, whereby on the one hand an evaporation of the acid during drying prevented and on the other hand the decomposition temperature itself is lowered. Example r iron sulfate with 7 aq is with 2o to 3o ° @ "iron oxide, which in the decomposition was obtained, mixed and first in a rotary kiln at Zoo temperatures dehydrated up to 300 °. In this case, care is expediently taken to ensure an oxidizing atmosphere. From here the mixture goes into a second rotary kiln, where it is oxidized Atmosphere is heated to .4oo to 5oo °. \ laughing termination of the oxidation process the material passes through a third furnace, which heats to between 75o and 85o °, for example must become. Of course, the individual stages can also be combined in such a way that that z. B. the oxidation and dehydration in one furnace or the oxidation in one others Oven takes place, or that the entire process takes place in a single oven.
Beispiel e Ferrosulfat mit 7 aq (evtl. unter Zusatz von Fe S 0, oder, Fe S O,, 1 aq) wird mit i °/" Soda und- je nach der Menge FeSO, bzw. FeSO, i aq mit 10 bis 30 °/o Eisenoxyd vermischt und wie in Beispiel i weiterbehandelt.Example e Ferrous sulphate with 7 aq (possibly with the addition of Fe S 0, or, Fe SO ,, 1 aq) is mixed with 100% soda and - depending on the amount of FeSO or FeSO, i aq with 10 to 30 % Iron oxide mixed and treated further as in Example i.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEI33158D DE529384C (en) | 1928-01-10 | 1928-01-10 | Process for dewatering and decomposition of iron vitriol (Fe S Oíñ 7H O) |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEI33158D DE529384C (en) | 1928-01-10 | 1928-01-10 | Process for dewatering and decomposition of iron vitriol (Fe S Oíñ 7H O) |
Publications (1)
Publication Number | Publication Date |
---|---|
DE529384C true DE529384C (en) | 1931-07-11 |
Family
ID=7188340
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DEI33158D Expired DE529384C (en) | 1928-01-10 | 1928-01-10 | Process for dewatering and decomposition of iron vitriol (Fe S Oíñ 7H O) |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE529384C (en) |
-
1928
- 1928-01-10 DE DEI33158D patent/DE529384C/en not_active Expired
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