COUPLING SYSTEM OF COPPER SLAG RECYCLING AND CO2 MINERALIZATION BASED ON INDUSTRIAL SOLID WASTE
20230323490 · 2023-10-12
Assignee
- Greenore Cleantech (Shanghai) Co., Ltd (Shanghai, CN)
- Shanghai Yuanhan Energy & Chemical Technology Co.,Ltd (Shanghai, CN)
- GreenOre Technology (Shanghai) Co.,Ltd (Shanghai, CN)
Inventors
Cpc classification
C21B2100/26
CHEMISTRY; METALLURGY
International classification
Abstract
A coupling system of copper slag recycling and CO.sub.2 mineralization process based on industrial solid waste includes the following steps: obtaining copper slags, performing a slag forming treatment, obtaining reforming slags, obtaining sponge iron, coupling the reforming slag with a CO.sub.2 mineralization process based on industrial solid waste, and coupling the CO.sub.2 generated in the process of obtaining sponge iron with the CO.sub.2 mineralization process based on industrial solid waste. The system includes a slag forming treatment device, a secondary treatment device, a first coupling device, and a second coupling device. The coupling system couples the recycling of copper slag with the existing CO.sub.2 mineralization process based on industrial solid waste. Various production lines can be organically integrated in a green and clean manner for both reforming slag and flue gas.
Claims
1. A coupling method of copper slag recycling and CO.sub.2 mineralization process based on industrial solid waste, comprising the following steps: obtaining copper slags; performing a slag forming treatment based on the copper slags; obtaining reforming slags based on the slag forming treatment; obtaining sponge iron based on the reforming slag; coupling the reforming slag with a CO.sub.2 mineralization process based on industrial solid waste; and coupling CO.sub.2 generated in a process of obtaining the sponge iron with the CO.sub.2 mineralization process based on the industrial solid waste.
2. The coupling method according to claim 1, wherein CO.sub.2 produced in the slag forming treatment is coupled with the CO.sub.2 mineralization process based on the industrial solid waste.
3. The coupling method according to claim 1, wherein the carbonate products obtained from the CO.sub.2 mineralization process based on the industrial solid waste are partially recycled and participate in the slag forming process.
4. The coupling method according to claim 1, where in the process of obtaining the sponge iron based on the reforming slag also comprises a step of inputting at least one gas selected from the group consisting of syngas, CO, and H.sub.2.
5. The coupling method according to claim 1, wherein before coupling the reforming slag with the CO.sub.2 mineralization process based on the industrial solid waste, a desulfurization treatment is applied to the reforming slag.
6. The coupling method according to claim 1, wherein the CO.sub.2 mineralization process based on the industrial solid waste comprises the following steps: performing a mixing reaction process based on industrial solid waste, auxiliary reagent, and CO.sub.2 to obtain a slurry; performing a solid-liquid separation treatment based on the slurry produced in the mixing reaction process; and obtaining a supernatant and unreacted solid particles.
7. The coupling method according to claim 6, the CO.sub.2 mineralization process based on the industrial solid waste further comprises preparing a carbonate product is prepared based on the supernatant; and/or, recycling the unreacted solid particles to the mixing reaction process.
8. The coupling method according to claim 6, wherein the carbonate product comprises calcium carbonate, magnesium carbonate or calcium magnesium carbonate.
9. A coupling system of copper slag recycling and CO.sub.2 mineralization process based on industrial solid waste, comprising: a slag forming treatment device, configured to obtain reforming slag from the copper slag; a secondary treatment device, configured for secondary treatment of the reforming slag to obtain sponge iron; a first coupling device, configured to convey the obtained reforming slag to the CO.sub.2 mineralization device based on industrial solid waste; a second coupling device, configured to transport the CO.sub.2 generated by the secondary treatment device to the CO.sub.2 mineralization device based on industrial solid waste.
10. The coupling system according to claim 9, wherein the first coupling device transports the CO.sub.2 generated by the slag forming treatment device to the CO.sub.2 mineralization device based on the industrial solid waste.
11. The coupling system according to claim 9, comprising a third coupling device, wherein the third coupling device is configured to transport part of carbonate products generated by the CO.sub.2 mineralization device based on the industrial solid waste to the slag forming device.
12. The coupling system according to claim 9, comprising a desulfurization device, where the desulfurization device is configured to desulfurize the reforming slag before the reforming slag is moved into to the CO.sub.2 mineralization device based on the industrial solid waste.
13. The coupling system according to claim 9, further comprising: a mixing reaction device, where the industrial solid waste, auxiliary reagent, and CO.sub.2 are reacted in the mixing reaction device; a solid-liquid separation device, wherein a slurry generated by the mixing reaction is subjected to a solid-liquid separation.
14. The coupling system according to claim 13, further comprising a product preparation device for producing carbonate products based on a clear liquid phase obtained after the solid-liquid separation device.
15. The coupling method according to claim 2, wherein the CO.sub.2 mineralization process based on the industrial solid waste comprises the following steps: performing a mixing reaction process based on the industrial solid waste, auxiliary reagent, and CO.sub.2 to obtain a slurry; performing a solid-liquid separation treatment based on the slurry produced in the mixing reaction process; and obtaining a supernatant and unreacted solid particles.
16. The coupling method according to claim 3, wherein the CO.sub.2 mineralization process based on the industrial solid waste comprises the following steps: performing a mixing reaction process based on the industrial solid waste, auxiliary reagent, and CO.sub.2 to obtain a slurry; performing a solid-liquid separation treatment based on the slurry produced in the mixing reaction process; and obtaining a supernatant and unreacted solid particles.
17. The coupling method according to claim 4, wherein the CO.sub.2 mineralization process based on the industrial solid waste comprises the following steps: performing a mixing reaction process based on the industrial solid waste, auxiliary reagent, and CO.sub.2 to obtain a slurry; performing a solid-liquid separation treatment based on the slurry produced in the mixing reaction process; and obtaining a supernatant and unreacted solid particles.
18. The coupling method according to claim 5, wherein the CO.sub.2 mineralization process based on the industrial solid waste comprises the following steps: performing a mixing reaction process based on the industrial solid waste, auxiliary reagent, and CO.sub.2 to obtain a slurry; performing a solid-liquid separation treatment based on the slurry produced in the mixing reaction process; and obtaining a supernatant and unreacted solid particles.
19. The coupling system according to claim 10, further comprising: a mixing reaction device, where the industrial solid waste, auxiliary reagent, and CO.sub.2 are reacted in the mixing reaction device; a solid-liquid separation device, wherein a slurry generated by the mixing reaction is subjected to a solid-liquid separation.
20. The coupling system according to claim 11, further comprising: a mixing reaction device, where the industrial solid waste, auxiliary reagent, and CO.sub.2 are reacted in the mixing reaction device; a solid-liquid separation device, wherein a slurry generated by the mixing reaction is subjected to a solid-liquid separation.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0039] To explicitly illustrate the characteristics, purposes, and advantages of this invention, a brief description of the drawings is presented.
[0040]
[0041]
[0042]
[0043]
DETAILED DESCRIPTION OF THE EMBODIMENTS
[0044] The technical scheme in the embodiment of the invention will be described clearly and comprehensively in combination with the attached drawings in the embodiment of the invention. Obviously, the described embodiments are only part of all the embodiments of the invention. Based on the embodiments in the invention, all other embodiments obtained by technicians belong to the scope of protection of this application, unless other creative breakthrough can distinguish its work significantly and fundamentally different from this technology.
[0045] As shown in
[0052] In this embodiment, the separation and desulfurization of raw materials are realized through slag forming and other treatments of copper slag, which not only ensures the purity and quality of products, but also enables a green and efficient production. Moreover, the invention can couple the recycling of copper slag with the existing CO.sub.2 mineralization process based on industrial solid waste. Various production lines can be organically integrated in a green and clean manner for both reforming slag and flue gas. At the same time, the selection range and acquisition mode of CO.sub.2 source are expanded for CO.sub.2 mineralization process based on industrial solid waste, and the engineering cost of CO.sub.2 mineralization process based on industrial solid waste is reduced.
[0053] The above reaction steps, as one of the examples, can be carried out continuously or simultaneously in the actual production process.
[0054] In this embodiment, the slag forming treatment based on copper slag includes but is not limited to treatments such as melting.
[0055] In order to further realize the internal circulation and reuse of resources, the CO.sub.2 generated in the slag forming treatment process is preferably coupled with the CO.sub.2 mineralization process based on industrial solid waste. In this embodiment, in addition to the CO.sub.2 produced in the process of obtaining sponge iron as one of the CO.sub.2 sources in the CO.sub.2 mineralization process based on industrial solid waste, the CO.sub.2 produced in the slag forming process can also be used as another way to obtain CO.sub.2 in the CO.sub.2 mineralization process based on industrial solid waste.
[0056] Furthermore, in the specific implementation process, the CO.sub.2 source of the CO.sub.2 mineralization process based on industrial solid waste can also come from power plant flue gas, blast furnace, converter, refining furnace, lime kiln flue gas, coal chemical tail gas or petrochemical tail gas. The content of carbon dioxide is between 15%-98%.
[0057] Furthermore, in this embodiment, the carbonate products produced from the CO.sub.2 mineralization process based on industrial solid waste can be partially recycled to the slag forming treatment process, as slag forming agents or a supplement to the slag forming agent that needs to be added, such as limestone. In this way, another internal circulation system is constructed. Compared with the prior art, the circulation process is advantageous in that the calcium and magnesium elements in the existing industrial solid waste can be fully utilized, and the resources can be well reused. The internal circulation process can also ensure the continuity of the reaction process and improve the reaction efficiency.
[0058] The above method for obtaining sponge iron based on the reforming slag also includes a step of inputting syngas or CO or H.sub.2 or a mixture of CO and H.sub.2. In the direct reduction iron process, the as-mentioned gas reacts with the reforming slag to obtain high-purity sponge iron.
[0059] In order to treat the SiO.sub.2 and sulfur-bearing substances during the iron making and slag making process, slag forming treatment is generally carried out by applying slag forming agents (such as limestone or carbonate product in this embodiment). The as-mentioned substances react with limestone to form calcium silicate, calcium sulfide, etc. (The reforming slag described below includes but is not limited to calcium silicate, calcium sulfide, etc.) The above substances and carbonate products react to generate calcium silicate, magnesium silicate or calcium magnesium silicate. When sulfur is present, the reaction products also include calcium sulfide, magnesium sulfide or calcium magnesium sulfide. Therefore, before the reforming slag is coupled with the CO.sub.2 mineralization process based on industrial solid waste, a desulfurization treatment of the reforming slag is included to reduce the impact of sulfur on the CO.sub.2 mineralization process based on industrial solid waste. Notably, the above desulfurization treatment is not necessary if the reforming slag does not contain sulfur or the content of sulfur is very low. The configuration of desulfurization treatment depends on the specific composition of raw materials.
[0060] Furthermore, in this embodiment, the above CO.sub.2 mineralization process based on industrial solid waste includes the following steps: [0061] a mixing reaction process, where the industrial solid waste, auxiliary reagent and CO.sub.2 are reacted in the mixing reaction device; [0062] a solid-liquid separation treatment, where the slurry generated by the above mixing reaction is subjected to a solid-liquid separation. [0063] a process where the supernatant and unreacted solid particles are obtained.
[0064] In this embodiment, the industrial solid waste includes but is not limited to steel slag, raw ore materials or tailings, other industrial wastes, etc. The raw ore materials include calcium magnesium ores. Other industrial wastes include iron slag, fly ash, bottom ash, red mud, construction waste/waste cement, tailings, etc.
[0065] A carbonate product is prepared based on the obtained supernatant, wherein the carbonate product includes calcium carbonate, magnesium carbonate or calcium magnesium carbonate. The carbonate products can partially participate in the slag forming treatment, as slag forming agents or as a supplement to slag forming agents (such as limestone) that need to be added, resulting in another internal circulation system.
[0066] Furthermore, the unreacted solid particles are recycled to the mixing reaction process, to fully extract and reuse the effective components in the unreacted solid particles.
[0067] In this embodiment, the auxiliary reagent comprises at least one organic acid, or one salt based on an organic acid radical or a combination of both. The organic acid includes but is not limited to oxalic acid, citric acid, picolinic acid, gluconic acid, glutamic acid, formic acid, acetic acid, propionic acid, butyric acid, valeric acid, lactic acid, succinic acid, phosphoric acid, pyrophosphoric acid, ascorbic acid, or phthalic acid. In this embodiment, by adjusting the pressure of carbon dioxide, the proportion of auxiliary reagents and the reaction temperature, the use of strong acid or highly corrosive acid (such as nitric acid, hydrochloric acid, sulfuric acid, and hydrofluoric acid) is avoided, and a continuous leaching of the target component is realized.
[0068] As shown in
[0073] The technical features of this coupling system have been described above and will not be repeated here.
[0074] In this embodiment, a dual internal circulation can be achieved through the first coupling device 30 and the second coupling device 40, and the recycling of copper slag can be coupled with the existing CO.sub.2 mineralization process based on industrial solid waste. Various production lines can be organically integrated for both reforming slag and flue gas, leading to a green and clean production.
[0075] The first coupling device 30 also transports the CO.sub.2 generated by the slag forming treatment device 10 to the CO.sub.2 mineralization device based on industrial solid waste.
[0076] As shown in
[0077] This embodiment also includes a desulfurization device, which is used to desulfurize the reforming slag before it moves into to the CO.sub.2 mineralization device 50 based on industrial solid waste. Notably, the desulfurization treatment is not necessary if the reforming slag does not contain sulfur or the content of sulfur is very low. The configuration of desulfurization treatment depends on the specific composition of raw materials.
[0078] In this embodiment, as shown in
[0081] Through the above mixing reaction, solid-liquid separation and other processes, the target carbonate products can be obtained, such as calcium carbonate, magnesium carbonate or calcium magnesium carbonate.
[0082] This embodiment also includes a product preparation device 53 for producing carbonate products based on the clear liquid phase after the solid-liquid separation device 52. The clear liquid contains target ions, such as calcium ions, magnesium ions or a mixture of both. The target product is calcium magnesium carbonate, calcium carbonate or magnesium carbonate.
[0083] The embodiment also includes a recovered water circulation device 54. After the clear liquid phase generates the products, the recovered water is circulated to the mixing reaction device 51 through the recovered water circulation device 54, and the recovered water will be circulated at least two times (m≥2).
[0084] Furthermore, the mixing reaction device 51 is also continuously fed with steel slag, auxiliary reagent and water at a certain proportion, and the slurry is obtained after well mixing. Carbon dioxide is continuously injected into the mixing reaction device 51 under a certain pressure and reacts with the slurry. The reacted slurry is continuously discharged out of the mixing reaction device 51. The steel slag can also be replaced with other industrial wastes, such as iron slag, fly ash, bottom ash, red mud, construction waste/waste cement, tailings, etc. The steel slag can also be replaced with raw ore materials or tailings, and the raw ore materials include calcium magnesium ores.
[0085] The specific classification of the auxiliary reagent is described above. In this embodiment, by adjusting the pressure of carbon dioxide, the proportion of auxiliary reagents and the reaction temperature, the use of strong acid or highly corrosive acid (such as nitric acid, hydrochloric acid, sulfuric acid, and hydrofluoric acid) is avoided, and a continuous leaching of the target component is realized.
[0086] The slurry out of the mixing reaction device 51 is subjected to at least one stage of solid-liquid separation treatment through the solid-liquid separation device 52, and the unreacted solid particles obtained from the solid-liquid separation will be recycled as raw materials for the next stage of reaction and separation.
[0087] The solid-liquid separation device 52 preferably adopts a two-stage solid-liquid separation configuration. Specifically, the solid-liquid separation device 52 includes a primary coarse separation unit and a secondary fine separation unit. The primary coarse separation unit is used to remove particle of sizes≥5-10 μm in diameter. The secondary fine separation unit is used to remove solid particles with a particle size≤1-5 μm in diameter. Through the multi-stage separation, the optimized separation scheme for particles of different sizes ensures that the solid-liquid separation can be carried out stably and continuously under the optimal load conditions. Such configuration effectively shortens the overall separation time, prolongs the stable operation of the separation system, and effectively avoids the technical problems caused by a single-stage separation.
[0088] Further preferably, the solid-liquid separation device 52 is also provided with a three-stage solid-liquid separation unit based on the two-stage solid-liquid separation. In this setup, the clear liquid phase containing target ions can be obtained by a disc centrifuge, a plate and frame filter press or a filter. The clear liquid containing the target ions is transported to the product preparation device 53.
[0089] When the clear liquid phase contains a high concentration of iron elements, the iron hydroxide precipitation is collected through enrichment and in this way, the irons can be reasonably and effectively recovered and utilized.
[0090] The above embodiments are only used to illustrate the technical scheme of the invention with reference to the preferred embodiments, but the invention is not limited by these embodiments. It should be understood by technicians in this field that the embodiments of the present invention can be modified or equivalently replaced without departing from the spirit and scope of this invention which shall be all included in the claims of the invention.