CN204848306U - System for handle red mud - Google Patents
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- CN204848306U CN204848306U CN201520580308.8U CN201520580308U CN204848306U CN 204848306 U CN204848306 U CN 204848306U CN 201520580308 U CN201520580308 U CN 201520580308U CN 204848306 U CN204848306 U CN 204848306U
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Abstract
The utility model discloses a system for handle red mud, include: first acidleach device has liquid export and solid slag export after red mud entry, sulphuric acid entry, the acidleach, mixing arrangement has liquid entry after the acidleach, quick lime entry and solid crystal export, after the acidleach after liquid entry and the acidleach liquid export link to each other, sintering device has solid crystal entry, solid slag entry and solid products export, and the solid crystal entry links to each other with the solid crystal export, and the solid slag entry links to each other with the solid slag export, separator has solid products entry, iron oxide red export and solid mixture export, and the solid products entry links to each other with the solid products export, second acidleach device has the solid export that solid mixture entered the mouth, aluminum chloride exports and contain calcium sulfate, and solid mixture entry and solid mixture export are continuous. This system can realize ferrallitic comprehensive recovery in the red mud to the iron oxide red productivity is high, thereby fundamentally solves the difficult problem that the red mud utilization ratio is low and store up for a long time.
Description
Technical field
The utility model belongs to field of metallurgy, and specifically, the utility model relates to a kind of system processing red mud.
Background technology
Red mud take bauxite as the fines strong basicity solid waste produced in raw material production alumina process, often produces one ton of aluminum oxide, approximately produces red mud 0.8 ~ 1.5 ton.China is alumina producing big country, within 2009, produces 2,378 ten thousand tons, aluminum oxide, accounts for 30% of Gross World Product, nearly 3,000 ten thousand tons of the red mud of generation.Current China red mud comprehensive utilization ratio is only 4%, and accumulation volume of cargo in storage reaches 200,000,000 tons, per tonly will spend storage expense about 50 yuan every year.Along with the reduction gradually of growth and the bauxite grade year by year of China's aluminum oxide output, the year generation of red mud also will constantly increase, and expect 2015, and red mud adds up volume of cargo in storage will reach 3.5 hundred million tons.Red mud is stored up in a large number, both land occupation, and waste resource, easily causes environmental pollution and potential safety hazard again.Red mud comprehensive utilization is the fundamental policy solving environmental pollution and potential safety hazard, the only way of Ye Shi China aluminum i ndustry sustainable development.
Utility model content
The utility model is intended to solve one of technical problem in correlation technique at least to a certain extent.For this reason, an object of the present utility model is to propose a kind of system processing red mud, this system can realize the synthetical recovery of iron and aluminium in red mud, and gained red iron oxide productive rate is higher, thus fundamentally solves the difficult problem that this trade waste of red mud utilization ratio is low and store up for a long time.
In one of the present utility model, the utility model proposes a kind of system processing red mud.According to embodiment of the present utility model, this system comprises:
First acidleach device, after described first acidleach device has red mud entrance, sulfuric acid entrance, acidleach, liquid outlet and solid slag export;
Mixing device, after described mixing device has acidleach, liquid entrance, unslaked lime entrance and solid crystal export, and after described acidleach, liquid entrance exports with liquid after described acidleach and is connected;
Roasting assembly, described roasting assembly has the outlet of solid crystal entrance, solid slag entrance and solid product, and described solid crystal entrance exports with described solid crystal and is connected, and described solid slag entrance exports with described solid slag and is connected;
Tripping device, described tripping device has solid product entrance, red iron oxide outlet and solid mixture outlet, and described solid product entrance exports with described solid product and is connected; And
Second acidleach device, described second acidleach device has solids mixture inlet, aluminum chloride outlet and the solid outlet containing calcium sulfate, and described solids mixture inlet exports with described solid mixture and is connected.
Thus, the synthetical recovery of iron and aluminium in red mud can be realized according to the system of the process red mud of the utility model embodiment, and gained red iron oxide productive rate is higher, thus fundamentally solves the difficult problem that this trade waste of red mud utilization ratio is low and store up for a long time.
Additional aspect of the present utility model and advantage will part provide in the following description, and part will become obvious from the following description, or be recognized by practice of the present utility model.
Accompanying drawing explanation
Above-mentioned and/or additional aspect of the present utility model and advantage will become obvious and easy understand from accompanying drawing below combining to the description of embodiment, wherein:
Fig. 1 is the system architecture schematic diagram of the process red mud according to the utility model embodiment;
Fig. 2 is the method flow schematic diagram of the system process red mud of process red mud according to the utility model embodiment.
Embodiment
Be described below in detail embodiment of the present utility model, the example of described embodiment is shown in the drawings, and wherein same or similar label represents same or similar element or has element that is identical or similar functions from start to finish.Be exemplary below by the embodiment be described with reference to the drawings, be intended to for explaining the utility model, and can not be interpreted as restriction of the present utility model.
In description of the present utility model, it will be appreciated that, term " " center ", " longitudinal direction ", " transverse direction ", " length ", " width ", " thickness ", " on ", D score, " front ", " afterwards ", " left side ", " right side ", " vertically ", " level ", " top ", " end ", " interior ", " outward ", " clockwise ", " counterclockwise ", " axis ", " radial direction ", orientation or the position relationship of the instruction such as " circumference " are based on orientation shown in the drawings or position relationship, only the utility model and simplified characterization for convenience of description, instead of indicate or imply that the device of indication or element must have specific orientation, with specific azimuth configuration and operation, therefore can not be interpreted as restriction of the present utility model.
In addition, term " first ", " second " only for describing object, and can not be interpreted as instruction or hint relative importance or imply the quantity indicating indicated technical characteristic.Thus, be limited with " first ", the feature of " second " can express or impliedly comprise at least one this feature.In description of the present utility model, the implication of " multiple " is at least two, such as two, three etc., unless otherwise expressly limited specifically.
In the utility model, unless otherwise clearly defined and limited, the term such as term " installation ", " being connected ", " connection ", " fixing " should be interpreted broadly, and such as, can be fixedly connected with, also can be removably connect, or integral; Can be mechanical connection, also can be electrical connection; Can be directly be connected, also indirectly can be connected by intermediary, can be the connection of two element internals or the interaction relationship of two elements, unless otherwise clear and definite restriction.For the ordinary skill in the art, the concrete meaning of above-mentioned term in the utility model can be understood as the case may be.
In the utility model, unless otherwise clearly defined and limited, fisrt feature second feature " on " or D score can be that the first and second features directly contact, or the first and second features are by intermediary indirect contact.And, fisrt feature second feature " on ", " top " and " above " but fisrt feature directly over second feature or oblique upper, or only represent that fisrt feature level height is higher than second feature.Fisrt feature second feature " under ", " below " and " below " can be fisrt feature immediately below second feature or tiltedly below, or only represent that fisrt feature level height is less than second feature.
In one of the present utility model, the utility model proposes a kind of system processing red mud.According to embodiment of the present utility model, this system comprises: the first acidleach device, described first acidleach device has liquid outlet and solid slag outlet after red mud entrance, sulfuric acid entrance, acidleach, and is suitable for red mud and sulfuric acid to carry out the first acidleach process, so that liquid and solid slag after obtaining acidleach; Mixing device, after described mixing device has acidleach, liquid entrance, unslaked lime entrance and solid crystal export, after described acidleach, liquid entrance exports with liquid after described acidleach and is connected, and be suitable for liquid after described acidleach to mix with unslaked lime, to obtain the solid crystal containing ironic hydroxide and calcium sulfate; Roasting assembly, described roasting assembly has the outlet of solid crystal entrance, solid slag entrance and solid product, described solid crystal entrance exports with described solid crystal and is connected, described solid slag entrance exports with described solid slag and is connected, and be suitable for described solid crystal containing ironic hydroxide and calcium sulfate and described solid slag to carry out calcination processing, to obtain containing red iron oxide, γ-Al
2o
3with the solid product of calcium sulfate; Tripping device, described tripping device has solid product entrance, red iron oxide outlet and solid mixture outlet, and described solid product entrance exports with described solid product and is connected, and is suitable for described containing red iron oxide, γ-Al
2o
3separating treatment is carried out, to obtain red iron oxide and to contain calcium sulfate and γ-Al with the solid product of calcium sulfate
2o
3solid mixture; And the second acidleach device, described second acidleach device has solids mixture inlet, aluminum chloride outlet and the solid outlet containing calcium sulfate, and described solids mixture inlet export with described solid mixture and is connected, and is suitable for containing calcium sulfate and γ-Al by described
2o
3solid mixture and hydrochloric acid carry out the second acidleach process, to obtain aluminum chloride and containing the solid of calcium sulfate.Contriver finds, by red mud and sulfuric acid are carried out acidleach process, the enrichment of iron ion in red mud can be realized, thus the productive rate of red iron oxide can be significantly improved, simultaneously in liquid after gained acidleach, add unslaked lime, not only can play the effect regulating liquid caustic soda degree after acidleach, and can heat be provided, thus promote ironic hydroxide and calcium sulphate solid crystallization, and then improve the productive rate of red iron oxide further, and do not need the external world to provide separately heat, reduce processing cost, in addition, through solid slag is carried out calcination processing, can by the aluminum oxide in solid slag from α-Al
2o
3form transformation is highly active γ-Al
2o
3form, thus can to realize alumina conversion in follow-up acidleach process be aluminum chloride, compared with prior art, present method can realize the synthetical recovery of iron and aluminium in red mud, and can thus fundamentally solve the difficult problem that red mud this trade waste utilization ratio is low and store up for a long time.
Below with reference to Fig. 1, the system of the process red mud of the utility model embodiment is described in detail.According to embodiment of the present utility model, this system comprises:
First acidleach device 100: according to embodiment of the present utility model, after first acidleach device 100 has red mud entrance 101, sulfuric acid entrance 102, acidleach, liquid outlet 103 and solid slag export 104, and be suitable for red mud and sulfuric acid to carry out the first acidleach process, thus liquid and solid slag after acidleach can be obtained.Contriver finds, by red mud and sulfuric acid are carried out acidleach process, can realize the enrichment of iron ion in red mud, thus can significantly improve the productive rate of red iron oxide.
According to an embodiment of the present utility model, the content of the ferric oxide in red mud is also not particularly limited, those skilled in the art can select according to actual needs, and according to specific embodiment of the utility model, in red mud, the content of ferric oxide can be 40 ~ 70wt%.Thus, the productive rate of red iron oxide can be significantly improved, thus improve the utility value of red mud.
In this step, concrete, the ferric oxide contained in red mud and sulfuric acid reaction generate ferric sulfate and after entering acidleach in liquid, the Alpha-alumina in red mud is then stayed in solid slag.
Mixing device 200: according to embodiment of the present utility model, after mixing device 200 has acidleach, liquid entrance 201, unslaked lime entrance 202 and solid crystal export 203, after acidleach, liquid entrance 201 and liquid after acidleach export 103 and are connected, and liquid mixes with unslaked lime after being suitable for acidleach just obtained above, thus the solid crystal containing ironic hydroxide and calcium sulfate can be obtained.Contriver finds, by adding unslaked lime in liquid after gained acidleach, not only can play the effect regulating liquid caustic soda degree after acidleach, and can heat be provided, thus promote ironic hydroxide and calcium sulphate solid crystallization, and then improve the productive rate of red iron oxide further, and do not need the external world to provide separately heat, thus can processing cost be reduced.
According to an embodiment of the present utility model, after acidleach liquid and unslaked lime blending ratio and be not particularly limited, those skilled in the art can select according to actual needs, according to specific embodiment of the utility model, after the calcium in unslaked lime and acidleach, in liquid, the mol ratio of iron level can be 1.1 ~ 1.5:1.Contriver finds, with this understanding, can realize calcium oxide and all be precipitated by iron ion, thus improves the productive rate of red iron oxide, and if unslaked lime addition is less, then precipitation of iron ions is incomplete, affects red iron oxide productive rate.
Roasting assembly 300: according to embodiment of the present utility model, roasting assembly 300 has solid crystal entrance 301, solid slag entrance 302 and solid product outlet 303, solid crystal entrance 301 and solid crystal export 203 and are connected, solid slag entrance 302 and solid slag export 104 and are connected, and be suitable for the solid crystal containing ironic hydroxide and calcium sulfate and solid slag to carry out calcination processing, thus can obtain containing red iron oxide, γ-Al
2o
3with the solid product of calcium sulfate.Contriver finds, by the solid crystal containing ironic hydroxide and calcium sulfate and solid slag are carried out calcination processing, ironic hydroxide not only can be made to resolve into red iron oxide, and can by the aluminum oxide in solid slag from α-Al
2o
3form transformation is highly active γ-Al
2o
3form, thus can to realize alumina conversion in follow-up acidleach process be aluminum chloride.
According to an embodiment of the present utility model, the temperature of calcination processing is also not particularly limited, and those skilled in the art can select according to actual needs, and according to specific embodiment of the utility model, the temperature of calcination processing can be 550 ~ 800 degrees Celsius.Contriver finds, if when temperature is lower than 550 DEG C, and α-Al
2o
3form transformation is incomplete, causes aluminum chloride in follow-up acidleach process to leach aluminium low; And if temperature higher than 800 DEG C time, aluminum oxide form transformation be other be difficult to leach form, be difficult to the recovery realizing aluminum oxide.Thus, under this calcining temperature, ironic hydroxide not only can be made to resolve into red iron oxide, and can ensure that aluminum oxide is from α-Al
2o
3form transformation is highly active γ-Al
2o
3form, thus can to realize alumina conversion in follow-up acidleach process be aluminum chloride.
Tripping device 400: according to embodiment of the present utility model, tripping device 400 has solid product entrance 401, red iron oxide outlet 402 and solid mixture outlet 403, solid product entrance 401 and solid product export 303 and are connected, and are suitable for obtained above containing red iron oxide, γ-Al
2o
3carry out separating treatment with the solid product of calcium sulfate, thus red iron oxide can be obtained and contain calcium sulfate and γ-Al
2o
3solid mixture.In this step, concrete, red iron oxide, γ-Al can be contained to what obtain
2o
3carry out ore grinding and magnetic separation after carrying out fragmentation with the solid product of calcium sulfate, thus realize the red iron oxide of magnetic and nonmagnetic containing calcium sulfate and γ-Al
2o
3the separation of solid mixture.
Second acidleach device 500: according to embodiment of the present utility model, second acidleach device 500 has solids mixture inlet 501, aluminum chloride outlet 502 and the solid outlet 503 containing calcium sulfate, solids mixture inlet 501 and solid mixture export 403 and are connected, and are suitable for just gained and contain calcium sulfate and γ-Al
2o
3solid mixture and hydrochloric acid carry out the second acidleach process, thus aluminum chloride can be obtained and containing the solid of calcium sulfate.
According to the system of the process red mud of the utility model embodiment by red mud and sulfuric acid are carried out acidleach process, the enrichment of iron ion in red mud can be realized, thus the productive rate of red iron oxide can be significantly improved, simultaneously in liquid after gained acidleach, add unslaked lime, not only can play the effect regulating liquid caustic soda degree after acidleach, and can heat be provided, thus promote ironic hydroxide and calcium sulphate solid crystallization, and then improve the productive rate of red iron oxide further, and do not need the external world to provide separately heat, reduce processing cost, in addition, through solid slag is carried out calcination processing, can by the aluminum oxide in solid slag from α-Al
2o
3form transformation is highly active γ-Al
2o
3form, thus can to realize alumina conversion in follow-up acidleach process be aluminum chloride, compared with prior art, present method can realize the synthetical recovery of iron and aluminium in red mud, realize turning harm into good simultaneously, turn waste into wealth, and can thus fundamentally solve the difficult problem that red mud this trade waste utilization ratio is low and store up for a long time.
Conveniently understand, below with reference to Fig. 2, the method for the system process red mud of the process red mud of the utility model embodiment is described in detail.According to embodiment of the present utility model, the method comprises:
S100: red mud and sulfuric acid are carried out the first acidleach process
According to embodiment of the present utility model, red mud and sulfuric acid are carried out the first acidleach process, thus liquid and solid slag after acidleach can be obtained.Contriver finds, by red mud and sulfuric acid are carried out acidleach process, can realize the enrichment of iron ion in red mud, thus can significantly improve the productive rate of red iron oxide.
According to an embodiment of the present utility model, the content of the ferric oxide in red mud is also not particularly limited, those skilled in the art can select according to actual needs, and according to specific embodiment of the utility model, in red mud, the content of ferric oxide can be 40 ~ 70wt%.Thus, the productive rate of red iron oxide can be significantly improved, thus improve the utility value of red mud.
In this step, concrete, the ferric oxide contained in red mud and sulfuric acid reaction generate ferric sulfate and after entering acidleach in liquid, the Alpha-alumina in red mud is then stayed in solid slag.
S200: liquid after acidleach is mixed with unslaked lime
According to embodiment of the present utility model, liquid after acidleach obtained above is mixed with unslaked lime, thus the solid crystal containing ironic hydroxide and calcium sulfate can be obtained.Contriver finds, by adding unslaked lime in liquid after gained acidleach, not only can play the effect regulating liquid caustic soda degree after acidleach, and can heat be provided, thus promote ironic hydroxide and calcium sulphate solid crystallization, and then improve the productive rate of red iron oxide further, and do not need the external world to provide separately heat, thus can processing cost be reduced.
According to an embodiment of the present utility model, after acidleach liquid and unslaked lime blending ratio and be not particularly limited, those skilled in the art can select according to actual needs, according to specific embodiment of the utility model, after the calcium in unslaked lime and acidleach, in liquid, the mol ratio of iron level can be 1.1 ~ 1.5:1.Contriver finds, with this understanding, can realize calcium oxide and all be precipitated by iron ion, thus improves the productive rate of red iron oxide, and if unslaked lime addition is less, then precipitation of iron ions is incomplete, affects red iron oxide productive rate.
S300: the solid crystal containing ironic hydroxide and calcium sulfate and solid slag are carried out calcination processing
According to embodiment of the present utility model, the solid crystal containing ironic hydroxide and calcium sulfate and solid slag are carried out calcination processing, thus can obtain containing red iron oxide, γ-Al
2o
3with the solid product of calcium sulfate.Contriver finds, by the solid crystal containing ironic hydroxide and calcium sulfate and solid slag are carried out calcination processing, ironic hydroxide not only can be made to resolve into red iron oxide, and can by the aluminum oxide in solid slag from α-Al
2o
3form transformation is highly active γ-Al
2o
3form, thus can to realize alumina conversion in follow-up acidleach process be aluminum chloride.
According to an embodiment of the present utility model, the temperature of calcination processing is also not particularly limited, and those skilled in the art can select according to actual needs, and according to specific embodiment of the utility model, the temperature of calcination processing can be 550 ~ 800 degrees Celsius.Contriver finds, if when temperature is lower than 550 DEG C, and α-Al
2o
3form transformation is incomplete, causes aluminum chloride in follow-up acidleach process to leach aluminium low; And if temperature higher than 800 DEG C time, aluminum oxide form transformation be other be difficult to leach form, be difficult to the recovery realizing aluminum oxide.Thus, under this calcining temperature, ironic hydroxide not only can be made to resolve into red iron oxide, and can ensure that aluminum oxide is from α-Al
2o
3form transformation is highly active γ-Al
2o
3form, thus can to realize alumina conversion in follow-up acidleach process be aluminum chloride.
S400: will containing red iron oxide, γ-Al
2o
3separating treatment is carried out with the solid product of calcium sulfate
According to embodiment of the present utility model, by obtained above containing red iron oxide, γ-Al
2o
3carry out separating treatment with the solid product of calcium sulfate, thus red iron oxide can be obtained and contain calcium sulfate and γ-Al
2o
3solid mixture.In this step, concrete, red iron oxide, γ-Al can be contained to what obtain by step S300
2o
3carry out ore grinding and magnetic separation after carrying out fragmentation with the solid product of calcium sulfate, thus realize the red iron oxide of magnetic and nonmagnetic containing calcium sulfate and γ-Al
2o
3the separation of solid mixture.
S500: will containing calcium sulfate and γ-Al
2o
3solid mixture and hydrochloric acid carry out the second acidleach process
According to embodiment of the present utility model, gained is contained calcium sulfate and γ-Al
2o
3solid mixture and hydrochloric acid carry out the second acidleach process, thus aluminum chloride can be obtained and containing the solid of calcium sulfate.
According to the method for the system process red mud of the process red mud of the utility model embodiment by red mud and sulfuric acid are carried out acidleach process, the enrichment of iron ion in red mud can be realized, thus the productive rate of red iron oxide can be significantly improved, simultaneously in liquid after gained acidleach, add unslaked lime, not only can play the effect regulating liquid caustic soda degree after acidleach, and can heat be provided, thus promote ironic hydroxide and calcium sulphate solid crystallization, and then improve the productive rate of red iron oxide further, and do not need the external world to provide separately heat, reduce processing cost, in addition, through solid slag is carried out calcination processing, can by the aluminum oxide in solid slag from α-Al
2o
3form transformation is highly active γ-Al
2o
3form, thus can to realize alumina conversion in follow-up acidleach process be aluminum chloride, compared with prior art, present method can realize the synthetical recovery of iron and aluminium in red mud, realize turning harm into good simultaneously, turn waste into wealth, and can thus fundamentally solve the difficult problem that red mud this trade waste utilization ratio is low and store up for a long time.
Below with reference to specific embodiment, be described the utility model, it should be noted that, these embodiments are only descriptive, and limit the utility model never in any form.
Embodiment 1
Mixed with sulfuric acid by red mud and carry out the first acidleach process, obtain liquid and the solid slag containing Alpha-alumina after the acidleach of sulfur acid iron after separation, wherein, in red mud, the content of ferric oxide is 40wt%, after acidleach, add unslaked lime in liquid, and wherein, the consumption of unslaked lime presses Ca
2+with Fe
3+mol ratio be that 1.1:1 adds, in unslaked lime and pickling liquor, water reacts and generates slaked lime, and release heat, slaked lime and ferric sulfate react, and the solid crystal generated under sensible heat effect containing ironic hydroxide and calcium sulfate, then, after solid crystal and liquid separation, calcine at 550 DEG C by the solid crystal containing ironic hydroxide and calcium sulfate and containing the solid slag of Alpha-alumina, ironic hydroxide resolves into red iron oxide, α-Al
2o
3form transformation is highly active γ-Al
2o
3form, finally obtains containing red iron oxide, γ-Al
2o
3with the solid product of calcium sulfate, then will containing red iron oxide, γ-Al
2o
3carry out fragmentation, fine grinding with the solid product of calcium sulfate, and after magnetic separation is separated, obtain magnetic product red iron oxide product and nonmagnetic containing calcium sulfate and γ-Al
2o
3solid mixture; Finally contain calcium sulfate and γ-Al by non magnetic
2o
3solid mixture and mixed in hydrochloric acid carry out the second acidleach, γ-Al
2o
3generate liquor alumini chloridi with hydrochloric acid reaction, after solid-liquid separation, obtain the solid of liquor alumini chloridi and sulfur acid calcium respectively.
Embodiment 2
Mixed with sulfuric acid by red mud and carry out the first acidleach process, obtain liquid and the solid slag containing Alpha-alumina after the acidleach of sulfur acid iron after separation, wherein, in red mud, the content of ferric oxide is 50wt%, after acidleach, add unslaked lime in liquid, and wherein, the consumption of unslaked lime presses Ca
2+with Fe
3+mol ratio be that 1.3:1 adds, in unslaked lime and pickling liquor, water reacts and generates slaked lime, and release heat, slaked lime and ferric sulfate react, and the solid crystal generated under sensible heat effect containing ironic hydroxide and calcium sulfate, then, after solid crystal and liquid separation, calcine at 600 DEG C by the solid crystal containing ironic hydroxide and calcium sulfate and containing the solid slag of Alpha-alumina, ironic hydroxide resolves into red iron oxide, α-Al
2o
3form transformation is highly active γ-Al
2o
3form, finally obtains containing red iron oxide, γ-Al
2o
3with the solid product of calcium sulfate, then will containing red iron oxide, γ-Al
2o
3carry out fragmentation, fine grinding with the solid product of calcium sulfate, and after magnetic separation is separated, obtain magnetic product red iron oxide product and nonmagnetic containing calcium sulfate and γ-Al
2o
3solid mixture; Finally contain calcium sulfate and γ-Al by non magnetic
2o
3solid mixture and mixed in hydrochloric acid carry out the second acidleach, γ-Al
2o
3generate liquor alumini chloridi with hydrochloric acid reaction, after solid-liquid separation, obtain the solid of liquor alumini chloridi and sulfur acid calcium respectively.
Embodiment 3
Mixed with sulfuric acid by red mud and carry out the first acidleach process, obtain liquid and the solid slag containing Alpha-alumina after the acidleach of sulfur acid iron after separation, wherein, in red mud, the content of ferric oxide is 70wt%, after acidleach, add unslaked lime in liquid, and wherein, the consumption of unslaked lime presses Ca
2+with Fe
3+mol ratio be that 1.5:1 adds, in unslaked lime and pickling liquor, water reacts and generates slaked lime, and release heat, slaked lime and ferric sulfate react, and the solid crystal generated under sensible heat effect containing ironic hydroxide and calcium sulfate, then, after solid crystal and liquid separation, calcine at 800 DEG C by the solid crystal containing ironic hydroxide and calcium sulfate and containing the solid slag of Alpha-alumina, ironic hydroxide resolves into red iron oxide, α-Al
2o
3form transformation is highly active γ-Al
2o
3form, finally obtains containing red iron oxide, γ-Al
2o
3with the solid product of calcium sulfate, then will containing red iron oxide, γ-Al
2o
3carry out fragmentation, fine grinding with the solid product of calcium sulfate, and after magnetic separation is separated, obtain magnetic product red iron oxide product and nonmagnetic containing calcium sulfate and γ-Al
2o
3solid mixture; Finally contain calcium sulfate and γ-Al by non magnetic
2o
3solid mixture and mixed in hydrochloric acid carry out the second acidleach, γ-Al
2o
3generate liquor alumini chloridi with hydrochloric acid reaction, after solid-liquid separation, obtain the solid of liquor alumini chloridi and sulfur acid calcium respectively.
In the description of this specification sheets, specific features, structure, material or feature that the description of reference term " embodiment ", " some embodiments ", " example ", " concrete example " or " some examples " etc. means to describe in conjunction with this embodiment or example are contained at least one embodiment of the present utility model or example.In this manual, to the schematic representation of above-mentioned term not must for be identical embodiment or example.And the specific features of description, structure, material or feature can combine in one or more embodiment in office or example in an appropriate manner.In addition, when not conflicting, the feature of the different embodiment described in this specification sheets or example and different embodiment or example can carry out combining and combining by those skilled in the art.
Although illustrate and described embodiment of the present utility model above, be understandable that, above-described embodiment is exemplary, can not be interpreted as restriction of the present utility model, those of ordinary skill in the art can change above-described embodiment, revises, replace and modification in scope of the present utility model.
Claims (1)
1. process a system for red mud, it is characterized in that, comprising:
First acidleach device, after described first acidleach device has red mud entrance, sulfuric acid entrance, acidleach, liquid outlet and solid slag export;
Mixing device, after described mixing device has acidleach, liquid entrance, unslaked lime entrance and solid crystal export, and after described acidleach, liquid entrance exports with liquid after described acidleach and is connected;
Roasting assembly, described roasting assembly has the outlet of solid crystal entrance, solid slag entrance and solid product, and described solid crystal entrance exports with described solid crystal and is connected, and described solid slag entrance exports with described solid slag and is connected;
Tripping device, described tripping device has solid product entrance, red iron oxide outlet and solid mixture outlet, and described solid product entrance exports with described solid product and is connected; And
Second acidleach device, described second acidleach device has solids mixture inlet, aluminum chloride outlet and the solid outlet containing calcium sulfate, and described solids mixture inlet exports with described solid mixture and is connected.
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105152224A (en) * | 2015-08-04 | 2015-12-16 | 江苏省冶金设计院有限公司 | Method and system for processing red mud |
| US20240034639A1 (en) * | 2021-07-20 | 2024-02-01 | Guangdong Brunp Recycling Technology Co., Ltd. | Nickel-iron wet treatment method and application thereof |
-
2015
- 2015-08-04 CN CN201520580308.8U patent/CN204848306U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105152224A (en) * | 2015-08-04 | 2015-12-16 | 江苏省冶金设计院有限公司 | Method and system for processing red mud |
| US20240034639A1 (en) * | 2021-07-20 | 2024-02-01 | Guangdong Brunp Recycling Technology Co., Ltd. | Nickel-iron wet treatment method and application thereof |
| US12006227B2 (en) * | 2021-07-20 | 2024-06-11 | Guangdong Brunp Recycling Technology Co., Ltd. | Nickel-iron wet treatment method and application thereof |
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