CN203529952U - Aluminum chloride crystal roasting system - Google Patents
Aluminum chloride crystal roasting system Download PDFInfo
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- CN203529952U CN203529952U CN201320591901.3U CN201320591901U CN203529952U CN 203529952 U CN203529952 U CN 203529952U CN 201320591901 U CN201320591901 U CN 201320591901U CN 203529952 U CN203529952 U CN 203529952U
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- 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
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
Abstract
The utility model relates to an aluminum chloride crystal roasting system. The aluminum chloride crystal roasting system comprises a first fluidized bed roasting furnace used for roasting a feed aluminum chloride crystal to obtain crude aluminum oxide, a second fluidized bed roasting furnace used for further roasting the crude aluminum oxide obtained from the first fluidized bed roasting furnace so as to obtain aluminum oxide product, a material conveying device used for conveying the materials from the first fluidized bed roasting furnace to the second fluidized bed roasting furnace, and a smoke channel used for transferring the smoke from the second fluidized bed roasting furnace into the first fluidized bed roasting furnace. According to the roasting system, the aluminum chloride crystal is processed by the first fluidized bed roasting furnace to form a fluidized bed under the effects of high-temperature smoke and hot air, and the fluidized bed can be quickly dried and decomposed to avoid sinking as blocks or blocking on a wind distribution plate, thus smooth production can be realized.
Description
Technical field
The utility model relates to a kind of crystal aluminum chloride roasting system.
Background technology
Adopting " a step acid pasting " from flyash, to extract in the process of aluminum oxide, the calcination of crystal aluminum chloride is the operation of one key.Rotary kiln is one of at present conventional roasting apparatus, when adopting rotary kiln to carry out roasting to material, it mainly relies on hot gas flow in kiln to heat the material of exposure, rely on hot kiln wall to heat the material of pressing close to kiln wall simultaneously, yet middle a large amount of materials but can not be directly contact with hot air-flow or hot kiln wall, make that rotary kiln baking thermal effect is low, the high (19.5MJ/Kg-Al of energy consumption
2o
3), restricted the development of its Technology.
At present, in Aluminium hydroxide roasting field, mainly both at home and abroad adopt energy-saving fluosolids roasting technology, the widely used type of furnace has three kinds, fluidization flash roaster (Alcoa), circulating fluidized bed roasting furnace (German Lu Qi company), gas suspension calcination stove (F.L.Smith).These three kinds of type of furnace Technologies all, for Aluminium hydroxide roasting design, during operation, are carried out the high-temperature flue gas of autonomic response stove after treatment, send into venturi drier and aluminium hydroxide are carried out predrying, and the aluminium hydroxide after predrying is sent to subsequent processing again.
Yet, above-mentioned three kinds of stoving ovens are when for roasting crystal aluminum chloride, because crystal aluminum chloride is larger at low thermophase drying and dehydrating institute energy requirement, venturi drier is difficult to make crystal aluminum chloride rapid drying dehydration, cause crystal aluminum chloride to be heated and become sticky, lump, when dropping to venturi drier bottom, can stop up flue, affect stoving oven production capacity, What is more can cause blowing out and industrial accident.If solve the problem of crystal aluminum chloride rapid drying dehydration by improving main furnace temperature and then raising venturi drier flue-gas temperature and flow velocity, can cause main furnace temperature too high, aluminum oxide overcook, air velocity is too fast, and internal circulating load strengthens, and increases energy consumption.Therefore, the technique of above-mentioned three kinds of type of furnaces is all not suitable for the sinter process of crystal aluminum chloride.
Utility model content
In view of this, the purpose of this utility model is for the deficiencies in the prior art, provides a kind of energy-efficient and adapt to the crystal aluminum chloride roasting system that the processing requirement of aluminum oxide is prepared in crystal aluminum chloride calcining.
The crystal aluminum chloride roasting system that the utility model provides comprises:
First fluidized bed stoving oven, for the crystal aluminum chloride to charging be dried, roasting, obtain first product aluminum oxide;
The second fluidized-solids roaster, carries out further roasting for the first product aluminum oxide to from first fluidized bed stoving oven, obtains alumina product;
Device for transporting objects, for being transported to the second fluidized-solids roaster by first product aluminum oxide from described first fluidized bed stoving oven;
Flue, for sending into described first fluidized bed stoving oven from the flue gas of second bed stoving oven.
According to roasting system of the present utility model, preferably, described first fluidized bed stoving oven comprises:
The first body of heater, described the first upper of furnace body is provided with exhanst gas outlet;
Be arranged in the first air distribution plate of the first lower portion of furnace body, for described the first body of heater being divided into the inlet plenum that is positioned at the roasting chamber of the first air distribution plate top and is positioned at the first air distribution plate below;
The first hot air apparatus, for providing warm air to make it enter described roasting chamber from inlet plenum by the first air distribution plate, so that the goods fluid in described roasting chamber;
The first particle separator, for receiving from the flue gas of the first body of heater exhanst gas outlet and the granule materials of carrying secretly thereof and described granule materials being separated from flue gas;
The first pay-off, for sending the isolated material of described the first particle separator back to first body of heater roasting chamber.
According to roasting system of the present utility model, preferably, described the second fluidized-solids roaster comprises:
The second body of heater, described the second upper of furnace body is provided with exhanst gas outlet;
Be arranged in the second air distribution plate of the second lower portion of furnace body, for described the second body of heater being divided into the inlet plenum that is positioned at the roasting chamber of the second air distribution plate top and is positioned at the second air distribution plate below;
The second hot air apparatus, for providing warm air to make it enter described roasting chamber from inlet plenum by the first air distribution plate, so that the goods fluid in described roasting chamber;
The second particle separator, for receiving from the flue gas of the second body of heater exhanst gas outlet and the granule materials of carrying secretly thereof and described granule materials being separated from flue gas;
The second pay-off, for sending the isolated material of described the second particle separator back to second body of heater roasting chamber.
Preferably, described first, second pay-off is screw feeder; Described device for transporting objects is venturi-type eductors.
According to roasting system of the present utility model, preferably, the second particle separator is cyclonic separator, the top exit UNICOM of one end of described flue and described cyclonic separator, the other end and described the first body of heater roasting chamber UNICOM and link position are positioned on the sidewall of the first body of heater opening for feed below.
According to roasting system of the present utility model, preferably, described the second fluidized-solids roaster is also provided with the 3rd hot air apparatus, and described the 3rd hot air apparatus is connected with described the second body of heater roasting chamber, and link position is positioned on the sidewall of the second body of heater opening for feed below; Described first fluidized bed stoving oven is also provided with the 4th hot air apparatus, and described the 4th hot air apparatus is connected with described flue.
According to roasting system of the present utility model, preferably, described roasting system also comprises waste heat boiler, and described waste heat boiler is arranged on flue, for reducing the flue-gas temperature in described flue.
According to roasting system of the present utility model, preferably, described roasting system also comprises:
Fluidized bed cooler, for the cooling product aluminum oxide from described the second fluidized-solids roaster;
The 3rd particle separator, for separating of the particulate matter in the flue gas from described fluidized bed cooler.Preferably, described the 3rd particle separator is cyclonic separator, and its top exit is connected to the inlet mouth of described the 4th hot air apparatus by pipeline.
According to roasting system of the present utility model, preferably, described roasting system is also provided with first product aluminum oxide warehouse, for collecting from the first product aluminum oxide of described first fluidized bed stoving oven and being sent to the second fluidized-solids roaster through described device for transporting objects.
The utility model has adopted first fluidized bed stoving oven and the second fluidized-solids roaster combination roasting crystal aluminum chloride, makes full use of from the heat in the high-temperature flue gas of the second fluidized-solids roaster, has improved energy utilization efficiency, reduces the discharge of exhausted air quantity; Crystal aluminum chloride forms fluidized-bed in first fluidized bed stoving oven under the effect of high-temperature flue gas and warm air, and by dry, decomposition rapidly, can not lump sinking, stop up air distribution plate, guarantee to produce and carry out smoothly, be suitable for crystal aluminum chloride calcining completely and prepare aluminum oxide.
Accompanying drawing explanation
The schematic flow sheet of the crystal aluminum chloride roasting system that Fig. 1 provides for the utility model.
Embodiment
Below with reference to accompanying drawing, further illustrate crystal aluminum chloride roasting system provided by the utility model, but therefore the utility model is not subject to any restriction.
As shown in Figure 1, crystal aluminum chloride roasting system of the present utility model comprises: first fluidized bed stoving oven 1, for the crystal aluminum chloride to charging be dried, roasting, obtain first product aluminum oxide; The second fluidized-solids roaster 2, carries out further roasting for the first product aluminum oxide to from first fluidized bed stoving oven 1, obtains alumina product; Device for transporting objects 3, for being transported to the second fluidized-solids roaster 2 by first product aluminum oxide from described first fluidized bed stoving oven 1; With flue 4, for sending into described first fluidized bed stoving oven 1 from the flue gas of second bed stoving oven 2.
In the utility model, described first fluidized bed stoving oven 1 can be existing fluidized-solids roaster, in body of heater, form fluidized-bed, so that air-flow fully contacts with material, carry out mass transfer, heat transfer rapidly, such as disclosed fluidized-solids roaster in CN201074208Y, CN102515231A.In an embodiment of the present utility model, described first fluidized bed stoving oven 1 comprises: the first body of heater 11, be arranged in the first air distribution plate 12, the first hot air apparatus 15, the first particle separator 16 and first pay-off 17 of the first body of heater 11 bottoms.
Wherein, described the first body of heater 11 tops are provided with exhanst gas outlet, and flue gas and entrained particles material thereof in the first body of heater 11 are drawn by this exhanst gas outlet, and certainly, described body of heater is also provided with opening for feed and discharge port.Described opening for feed place can also setting party the just pay-off of crystal aluminum chloride charging, such as scroll feeder etc., repeat no more here.
Described the first air distribution plate 12 is arranged in the first body of heater 11, such as the first air distribution plate 12 is flatly connected on the sidewall of the first body of heater 11 by welding or bolt.Described the first air distribution plate 12 is divided into described the first body of heater 11 to be positioned at the roasting chamber 13 of the first air distribution plate 12 tops and to be positioned at the inlet plenum 14 of the first air distribution plate 12 belows, and the air-flow that enters described the first body of heater roasting chamber 13 is evenly distributed.Described the first air distribution plate 12 has open-celled structure, from the air-flow of the first body of heater inlet plenum 14, can enter the first body of heater roasting chamber 13 through the first air distribution plate 12.Hole shape, size and distribution concrete on described air distribution plate can be according to practical situation by common process calculative determinations.The discharge port of described the first body of heater 11 both can be arranged on the sidewall of 13 bottoms, described the first body of heater roasting chamber, also can be arranged on the bottom of described the first body of heater roasting chamber 13, such as in the same plane with described the first air distribution plate 12, can guarantee the material discharge smoothly in described the first body of heater roasting chamber 13, repeat no more here.
Described the first hot air apparatus 15 is for providing warm air to make it enter the first body of heater roasting chamber 13 from the first body of heater inlet plenum 14 by the first air distribution plate 12, so that the goods fluid in the first body of heater roasting chamber 13.Particularly, described the first hot air apparatus 15 can be arranged on the burner of the first body of heater inlet plenum 14 lower ends, in the first body of heater inlet plenum 14, provides warm air, by regulating the flow velocity of warm air can make material form fluidized-bed in the first body of heater roasting chamber 13.Described warm air both provided power for forming fluidized-bed, again for material roasting provides heat.Consider that crystal aluminum chloride decomposition needs a large amount of heats, described burner can be made as a plurality of, such as two, jointly in the first body of heater inlet plenum 14, provides warm air.
Described the first particle separator 16 connects the exhanst gas outlet on the first body of heater 11 tops, for receiving from the flue gas of the first body of heater 11 exhanst gas outlets and the granule materials of carrying secretly thereof and granule materials being separated from flue gas.Preferably, described the first particle separator 16 is cyclonic separator.Utilize the centrifugal force that swirling eddy produces that granule materials is separated from flue gas stream, the flue gas after separation is drawn by its top exit, is sent to sour absorption system 6, reclaims aluminum chloride and decomposes the hydrogen chloride gas producing.
One end of described the first pay-off 17 is connected with the solid materials outlet of the first particle separator 16, and in the embodiment that is cyclonic separator at the first particle separator 16, this solid materials outlet is the outlet at bottom of cyclonic separator; The other end of described the first pay-off 17 is connected with the first body of heater roasting chamber 13, for sending the isolated material of described the first particle separator 16 back to first body of heater roasting chamber 13.Preferably, described the first pay-off 17 is scroll feeder.
Described the second fluidized-solids roaster 2 can be existing fluidized-solids roaster equally, in body of heater, form fluidized-bed, so that air-flow fully contacts with material, carry out mass transfer, heat transfer rapidly, as disclosed fluidized-solids roaster in CN201074208Y, CN102515231A.In another embodiment of the present utility model, described the second fluidized-solids roaster 2 comprises: the second body of heater 21, and described the second body of heater 21 tops are provided with exhanst gas outlet; Be arranged in the second air distribution plate 22 of the second body of heater 21 bottoms, for described the second body of heater 21 being divided into the roasting chamber 23 that is positioned at the second air distribution plate 22 tops and the inlet plenum 24 that is positioned at the second air distribution plate 22 belows; The second hot air apparatus 25, for providing warm air to make it enter the second body of heater roasting chamber 23 from the second body of heater inlet plenum 24 by the second air distribution plate 22, so that the goods fluid in the second body of heater roasting chamber 23; The second particle separator 26, for receiving from the flue gas of the second body of heater 21 exhanst gas outlets and the granule materials of carrying secretly thereof and described granule materials being separated from flue gas; The second pay-off 27, sends the isolated material of described the second particle separator 26 back to second body of heater roasting chamber 23.One of ordinary skill in the art will readily recognize that and above-mentionedly about the possible of first fluidized bed stoving oven 1 or preferred design, be equally applicable to the second fluidized-solids roaster 2.Further preferably, described the second fluidized-solids roaster 2 is also provided with the 3rd hot air apparatus 28, described the 3rd hot air apparatus 28 is connected with described the second body of heater roasting chamber 23, its link position is positioned on the sidewall of the second body of heater 21 opening for feed belows, to the second interior introducing crossflow in body of heater roasting chamber 23, further to improve the roasting effect of material.
Preferably, described device for transporting objects 3 is venturi-type eductors, and its one end connects the discharge port of the first body of heater roasting chamber 11, and the other end connects the opening for feed of the second body of heater roasting chamber 21.After first fluidized bed stoving oven is processed, no longer there is adhesion problem in crystal aluminum chloride, therefore can use Venturi handling machinery effectively first product aluminum oxide to be transported to the second fluidized-solids roaster 2 from described first fluidized bed stoving oven 1.
One end of described flue 4 is communicated with the exhanst gas outlet of the second particle sorting apparatus 26, and in the embodiment that is cyclonic separator at the second particle separator 26, this exhanst gas outlet is the top exit of cyclonic separator; The other end of described flue 4 can be connected to the first body of heater inlet plenum 14, the warm air providing with the first hot air apparatus 15 together enters the first body of heater roasting chamber 13, or be preferably connected directly on the sidewall that described the first body of heater roasting chamber 13 and link position be positioned at the first body of heater 11 opening for feeds belows, to the first interior introducing crossflow in body of heater roasting chamber 13, further to improve the roasting effect of material, also alleviate the burden of sour absorption system 6 simultaneously.
In another kind of embodiment of the present utility model, described roasting system also comprises waste heat boiler 5, and described waste heat boiler 5 is arranged on flue 4, for making the flue gas cool-down of pipeline 4.Preferably, the temperature of flue gas is reduced to 400-600 ℃; Further preferably, the temperature of flue gas is reduced to 400-500 ℃.
In another embodiment of the present utility model, described roasting system also comprises the 4th hot air apparatus 18, for to the first interior introducing crossflow in body of heater roasting chamber 13, further to improve the fluidized drying effect of material.Described the 4th hot air apparatus 18 can be connected with described the first body of heater roasting chamber 13, and its link position is positioned on the sidewall of the first body of heater 11 opening for feeds belows, can be with described flue 4 on sustained height, or be with flue 4 on or under.Preferably, described the 4th hot air apparatus 18 is connected with described flue 4, by described flue 4 to delivery air in the first body of heater roasting chamber 13.
In another embodiment of the present utility model, described roasting system is also provided with fluidized bed cooler 7, for the cooling aluminum oxide from described the second fluidized-solids roaster 2, such as disclosed fluidized bed cooler in CN102435080A; With the 3rd particle separator 8, for separating of the material of carrying secretly in the flue gas from described fluidized bed cooler 7.Preferably, described the 3rd particle separator 8 is cyclonic separator, isolated material and alumina product converge, flue gas is delivered to sour absorption system and/or described the 4th hot air apparatus by its top exit by pipeline, when the 4th hot air apparatus operation, for described the 4th hot air apparatus provides part source of the gas.Further preferably, described roasting system is also provided with first product aluminum oxide warehouse 9, described first product aluminum oxide warehouse 9 is connected with described device for transporting objects 3 with the discharge port of the first body of heater roasting chamber 11 respectively, for collecting from the first product aluminum oxide of described first fluidized bed stoving oven 1 and being sent to the second fluidized-solids roaster 2 through described device for transporting objects 3.In the utility model, described first product aluminum oxide refers to the aluminum oxide that also contains the aluminum chloride decomposing not yet completely.
Below by embodiment, further describe roasting system provided by the utility model, but therefore the utility model is not subject to any restriction.
Embodiment
The crystal aluminum chloride of 4-5wt% attached water will be contained, with 5t/h continuously feeding to first fluidized bed stoving oven 1, the warm air being provided by the high-temperature flue gas from flue 4 and described the first hot air apparatus 15 in dropping process dispels, and dry rapidly, wherein the speed of high-temperature flue gas is 25-40m/s, the speed of warm air is about 3m/s, crystal aluminum chloride forms fluidized-bed above the first air distribution plate 12, bed temperature is controlled at 300-450 ℃, the mean residence time of material is controlled at 6-10 minute, crystal aluminum chloride is decomposed into hydrogenchloride substantially, water vapour and aluminum oxide, partial material rises with flue gas (comprising hydrogenchloride and water vapour), and enter the first particle sorting apparatus 16 through the first body of heater 11 exhanst gas outlets, isolated solid materials returns to by the first pay-off 17 roasting that circulates in first fluidized bed stoving oven 1, after separated, flue gas is delivered to sour absorption system 6 through top exit, reclaim hydrogen chloride gas.The first product aluminum oxide that comprises the undecomposed aluminum chloride of part is by entering first product aluminum oxide feed bin 9 through the first body of heater 11 discharge ports.
First product aluminum oxide is sent into the second fluidized-solids roaster 2 by device for transporting objects 3, in dropping process, by the hot blast from second, third hot air apparatus 25,28, dispelled, wherein the speed of the air inlet of second, third hot air apparatus 25,28 is about 3m/s, first product aluminum oxide forms fluidized-bed above the second air distribution plate 22, bed temperature is controlled at 750-1100 ℃, the mean residence time of material is controlled at 6-10 minute, and aluminum chloride decomposes completely, and aluminum oxide is gradually by γ-Al
2o
3change α-Al into
2o
3.Partial material rises with flue gas, and enter the second particle separator 26 through the second body of heater 21 exhanst gas outlets, isolated solid materials returns to by the second pay-off 27 roasting that circulates in the second fluidized-solids roaster 2, separated after flue gas through top exit, by flue 4, deliver to first fluidized bed stoving oven 1.The product aluminum oxide obtaining enters fluidized bed cooler 7 from the second roasting fluidized-bed 2 discharge ports, is lowered the temperature with air heat-exchange, and air is sent to sour absorption system 6 after dedusting.
In the present embodiment, the energy consumption of described roasting system when processing 420 tons of crystal aluminum chlorides is in Table 1.
Table 1
Wherein, diesel oil is the fuel of first, second, and third hot air apparatus.
Energy consumption of the present utility model is about 15MJ/Kg-Al
2o
3, than traditional rotary kiln 19.5MJ/Kg-Al
2o
3 energy Intensity Reduction 23%.
Claims (8)
1. a crystal aluminum chloride roasting system, comprising:
First fluidized bed stoving oven, for the crystal aluminum chloride to charging be dried, roasting, obtain first product aluminum oxide;
The second fluidized-solids roaster, carries out further roasting for the first product aluminum oxide to from first fluidized bed stoving oven, obtains alumina product;
Device for transporting objects, for being transported to the second fluidized-solids roaster by first product aluminum oxide from described first fluidized bed stoving oven;
Flue, for sending into described first fluidized bed stoving oven from the flue gas of second bed stoving oven.
2. roasting system as claimed in claim 1, is characterized in that, described first fluidized bed stoving oven comprises:
The first body of heater, described the first upper of furnace body is provided with exhanst gas outlet;
Be arranged in the first air distribution plate of the first lower portion of furnace body, for described the first body of heater being divided into the inlet plenum that is positioned at the roasting chamber of the first air distribution plate top and is positioned at the first air distribution plate below;
The first hot air apparatus, for providing warm air to make it enter described roasting chamber from inlet plenum by the first air distribution plate, so that the goods fluid in described roasting chamber;
The first particle separator, for receiving from the flue gas of the first body of heater exhanst gas outlet and the granule materials of carrying secretly thereof and described granule materials being separated from flue gas;
The first pay-off, for sending the isolated material of described the first particle separator back to first body of heater roasting chamber.
3. roasting system as claimed in claim 1 or 2, is characterized in that, described the second fluidized-solids roaster comprises:
The second body of heater, described the second upper of furnace body is provided with exhanst gas outlet;
Be arranged in the second air distribution plate of the second lower portion of furnace body, for described the second body of heater being divided into the inlet plenum that is positioned at the roasting chamber of the second air distribution plate top and is positioned at the second air distribution plate below;
The second hot air apparatus, for providing warm air to make it enter described roasting chamber from inlet plenum by the second air distribution plate, so that the goods fluid in described roasting chamber;
The second particle separator, for receiving from the flue gas of the second body of heater exhanst gas outlet and the granule materials of carrying secretly thereof and described granule materials being separated from flue gas;
The second pay-off, for the device of sending the isolated material of described the second particle separator back to second body of heater roasting chamber.
4. roasting system as claimed in claim 3, it is characterized in that, described the second particle separator is cyclonic separator, the top exit UNICOM of one end of described flue and described cyclonic separator, the other end and described the first body of heater roasting chamber UNICOM and link position are positioned on the sidewall of the first body of heater opening for feed below.
5. roasting system as claimed in claim 4, it is characterized in that, described the second fluidized-solids roaster is also provided with the 3rd hot air apparatus, and described the 3rd hot air apparatus is connected with described the second body of heater roasting chamber, and link position is positioned on the sidewall of the second body of heater opening for feed below; Described first fluidized bed stoving oven is also provided with the 4th hot air apparatus, and described the 4th hot air apparatus is connected with described flue.
6. roasting system as claimed in claim 5, is characterized in that, described roasting system also comprises waste heat boiler, and described waste heat boiler is arranged on flue, for reducing the flue-gas temperature in described flue.
7. roasting system as claimed in claim 6, is characterized in that, described roasting system also comprises:
Fluidized bed cooler, for the cooling product aluminum oxide from described the second fluidized-solids roaster;
The 3rd particle separator, for separating of the particulate matter in the flue gas from described fluidized bed cooler.
8. roasting system according to claim 7, is characterized in that, described roasting system is also provided with first product aluminum oxide warehouse, for collecting from the first product aluminum oxide of described first fluidized bed stoving oven and being sent to the second fluidized-solids roaster through described device for transporting objects.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201320591901.3U CN203529952U (en) | 2013-07-04 | 2013-09-24 | Aluminum chloride crystal roasting system |
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| CN201320396551.5 | 2013-07-04 | ||
| CN201320396551 | 2013-07-04 | ||
| CN201320591901.3U CN203529952U (en) | 2013-07-04 | 2013-09-24 | Aluminum chloride crystal roasting system |
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| CN201320591901.3U Expired - Lifetime CN203529952U (en) | 2013-07-04 | 2013-09-24 | Aluminum chloride crystal roasting system |
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| CN102435080A (en) * | 2011-09-09 | 2012-05-02 | 哈尔滨工业大学 | Stepped differential-velocity fluidized bed cooler |
| CN102502744B (en) * | 2011-10-26 | 2013-11-06 | 北京航天动力研究所 | Slagging-free type and multilevel differential temperature fluidized roasting system for crystallized aluminum salt and method thereof |
| CN102515231B (en) * | 2011-12-22 | 2014-03-05 | 东北大学设计研究院（有限公司） | Apparatus and method for production of high temperature alumina with circulating fluidized bed roasting furnace |
| CN103466672B (en) * | 2013-07-04 | 2016-01-20 | 中国神华能源股份有限公司 | A kind of crystal aluminum chloride roasting system and method |
-
2013
- 2013-09-24 CN CN201310439973.0A patent/CN103466672B/en active Active
- 2013-09-24 CN CN201320591901.3U patent/CN203529952U/en not_active Expired - Lifetime
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103466672A (en) * | 2013-07-04 | 2013-12-25 | 中国神华能源股份有限公司 | Crystallized aluminum chloride roasting system and method |
| CN103466672B (en) * | 2013-07-04 | 2016-01-20 | 中国神华能源股份有限公司 | A kind of crystal aluminum chloride roasting system and method |
| CN104344741A (en) * | 2014-10-28 | 2015-02-11 | 中冶南方工程技术有限公司 | System for performing hydrochloric acid waste fluid spray roasting through industrial waste heat and control method |
| CN104344741B (en) * | 2014-10-28 | 2016-06-01 | 中冶南方工程技术有限公司 | One utilizes industrial exhaust heat to carry out hydrochloride waste spray roasting system and control method |
| CN107265488A (en) * | 2017-07-20 | 2017-10-20 | 辽宁东大粉体工程技术有限公司 | The process unit and method of a kind of two step method production γ type aluminum oxide |
| CN110194475A (en) * | 2019-06-24 | 2019-09-03 | 北京航天石化技术装备工程有限公司 | A kind of the high/low temperature roasting system and method for crystal aluminum chloride production aluminium oxide |
| CN110194475B (en) * | 2019-06-24 | 2024-05-14 | 北京航天石化技术装备工程有限公司 | High-low temperature roasting system and method for producing alumina from crystalline aluminum chloride |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103466672A (en) | 2013-12-25 |
| CN103466672B (en) | 2016-01-20 |
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