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Position: Chinese Standard in English/GB 50530-2010
GB 50530-2010   Code for design of alumina refinery process (English Version)
Standard No.: GB 50530-2010 Status:superseded remind me the status change

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Language:English File Format:PDF
Word Count: 54000 words Price(USD):1620.0 remind me the price change

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Implemented on:2010-7-1 Delivery: via email in 1 business day
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Standard No.: GB 50530-2010
English Name: Code for design of alumina refinery process
Chinese Name: 氧化铝厂工艺设计规范
Chinese Classification: H01    Technical management
Professional Classification: GB    National Standard
Issued by: MOHURD
Issued on: 2010-1-24
Implemented on: 2010-7-1
Status: superseded
Superseded by:GB/T 50530-2022
Superseded on:2023-2-1
Language: English
File Format: PDF
Word Count: 54000 words
Price(USD): 1620.0
Delivery: via email in 1 business day
1 General provisions 1.0.1 This code is developed in order to unify technical requirements for alumina process design, propel technological advance, improve design quality, and make design technologically advanced, economically reasonable, safe and reliable and be in line with national conditions. 1.0.2 This code is applicable to process design of newly constructed, extended and renovated large and medium-sized alumina refinery that produces metallurgical-grade alumina using diasporic bauxite as raw material. 1.0.3 Process design of alumina refinery shall be achieved by actively and prudently applying and promoting advanced technologies at home and abroad, pushing to enhance the level of mechanization and automation upon the actual situation, protecting the environment, and effectively using resources, saving energy, land, water and materials, controlling cost and shortening construction duration to improve labor productivity and civilized production level. 1.0.4 For alumina refinery constructed in phases, a comprehensive plan shall be established, and phased construction scale and scheme shall be defined reasonably to create conditions for long-term construction. 1.0.5 Design for renovation and extension of alumina refinery shall make full use of existing production facilities, utilities and amenities, and shall avoid or reduce the impact on production during construction. 1.0.6 This code specifies the basic requirements for process design of alumina refinery. When it is in contradiction with the provisions of national laws and administrative regulations, the latter shall prevail. 1.0.7 Process design of alumina refinery shall comply with the relevant current national standards, in addition to this code. 2 Terms 2.0.1 alumina an aluminum oxide, with molecular formula Al2O3, that has many different crystal forms and is the main raw material for aluminum smelting 2.0.2 sandy alumina alumina that has large and uniform particle size, large specific surface area, small angle of repose, high strength and good fluidity, and is the optimum raw material for flue gas purification by dry process and for large central-feeding pre-baked anode cell 2.0.3 bauxite a generic term for ores mainly composed of gibbsite, boehmite or diaspore, which, in addition to alumina, mainly contains impurities such as silicon oxide, iron oxide, titanium oxide, and compounds of minor or trace elements, and is the most important ore resource in alumina production at present 2.0.4 gibbsite an aluminum hydroxide, with molecular formula Al(OH)3, that is monoclinic, and has a density of 2.35 g/cm3 to 2.42 g/cm3 and a Mohs hardness of 2.5 to 3.5 2.0.5 diaspore an aluminum oxyhydroxide, with molecular formula AlOOH, that is orthorhomibc, and has a density of 3.3 g/cm3 to 3.5 g/cm3 and a Mohs hardness of 6.5 to 7 2.0.6 Bayer process a process of producing alumina, that is, the alumina in bauxite is directly extracted using caustic solution, to obtain sodium aluminate solution 2.0.7 sintering process a process of producing alumina, that is, aluminum-containing material is sintered using burdening, making the alumina therein convert into aluminate 2.0.8 combination process a generic term for process of producing alumina according to Bayer process and sintering process which are combined in different ways 2.0.9 serial combination process a process of producing alumina, that is, red mud, which is obtained by processing bauxite according to Bayer process, is processed according to sintering process to recycle the alumina and alkaline therein 2.0.10 mixed combination process a process of producing alumina, that is, red mud, which is obtained by processing bauxite according to Bayer process, is blended with an appropriate amount of bauxite and processed according to sintering process
Foreword ii 1 General provisions 2 Terms 3 General requirements 4 Raw materials and fuels 4.1 Raw materials 4.2 Fuels 5 Storage and handling of raw materials and fuels, bauxite crushing 5.1 Unloading facilities of raw materials and fuels 5.2 Material stockyard 5.3 Bauxite crushing 5.4 Storage and delivery of caustic soda 5.5 Storage silo of soda 6 Lime burning and lime milk slaking 6.1 Lime burning 6.2 Lime milk slaking 7 Bauxite dressing 7.1 Grinding and classification 7.2 Flotation 7.3 Storage, preparation and addition of agent 7.4 Dewatering 7.5 Maintenance facilities 7.6 Automatic control, measuring and weighing 8 Slurry preparation 8.1 Bauxite grinding 8.2 Bauxite slurry preparation of dressing-Bayer process 8.3 Raw mix slurry adjustment of sintering process 9 Autoclave digestion 9.1 Pre-desilication of bauxite 9.2 Feeding pump to autoclave digester 9.3 Autoclave digestion 10 Sintering and sinter crushing 10.1 Preparation of coal powder 10.2 Sintering 10.3 Sinter crushing 11 Sinter leaching 12 Red mud settling, washing and control filtration 12.1 Red mud settling and washing 12.2 Control filtration 13 Desilication in sintering process 13.1 Desilication 13.2 Separation of desilication product 14 Decomposition of sodium aluminate solution 14.1 Seed precipitation 14.2 Carbonization 15 Hydrate separation, washing and storage 15.1 Hydrate separation and washing 15.2 Hydrate storage 16 Spent liquor evaporation, causticization and recycled spent liquor proportioning 16.1 Spent liquor evaporation 16.2 Separation of soda crystal 16.3 Causticization of soda crystal 16.4 Caustic solution proportioning 17 Hydrate calcination, product packing and stacking 17.1 Hydrate calcination 17.2 Alumina storage 17.3 Product packing and stacking Explanation of wording in this code List of quoted standards
Code of China
Standard
GB 50530-2010  Code for design of alumina refinery process (English Version)
Standard No.GB 50530-2010
Statussuperseded
LanguageEnglish
File FormatPDF
Word Count54000 words
Price(USD)1620.0
Implemented on2010-7-1
Deliveryvia email in 1 business day
Detail of GB 50530-2010
Standard No.
GB 50530-2010
English Name
Code for design of alumina refinery process
Chinese Name
氧化铝厂工艺设计规范
Chinese Classification
H01
Professional Classification
GB
ICS Classification
Issued by
MOHURD
Issued on
2010-1-24
Implemented on
2010-7-1
Status
superseded
Superseded by
GB/T 50530-2022
Superseded on
2023-2-1
Abolished on
Superseding
Language
English
File Format
PDF
Word Count
54000 words
Price(USD)
1620.0
Keywords
GB 50530-2010, GB/T 50530-2010, GBT 50530-2010, GB50530-2010, GB 50530, GB50530, GB/T50530-2010, GB/T 50530, GB/T50530, GBT50530-2010, GBT 50530, GBT50530
Introduction of GB 50530-2010
1 General provisions 1.0.1 This code is developed in order to unify technical requirements for alumina process design, propel technological advance, improve design quality, and make design technologically advanced, economically reasonable, safe and reliable and be in line with national conditions. 1.0.2 This code is applicable to process design of newly constructed, extended and renovated large and medium-sized alumina refinery that produces metallurgical-grade alumina using diasporic bauxite as raw material. 1.0.3 Process design of alumina refinery shall be achieved by actively and prudently applying and promoting advanced technologies at home and abroad, pushing to enhance the level of mechanization and automation upon the actual situation, protecting the environment, and effectively using resources, saving energy, land, water and materials, controlling cost and shortening construction duration to improve labor productivity and civilized production level. 1.0.4 For alumina refinery constructed in phases, a comprehensive plan shall be established, and phased construction scale and scheme shall be defined reasonably to create conditions for long-term construction. 1.0.5 Design for renovation and extension of alumina refinery shall make full use of existing production facilities, utilities and amenities, and shall avoid or reduce the impact on production during construction. 1.0.6 This code specifies the basic requirements for process design of alumina refinery. When it is in contradiction with the provisions of national laws and administrative regulations, the latter shall prevail. 1.0.7 Process design of alumina refinery shall comply with the relevant current national standards, in addition to this code. 2 Terms 2.0.1 alumina an aluminum oxide, with molecular formula Al2O3, that has many different crystal forms and is the main raw material for aluminum smelting 2.0.2 sandy alumina alumina that has large and uniform particle size, large specific surface area, small angle of repose, high strength and good fluidity, and is the optimum raw material for flue gas purification by dry process and for large central-feeding pre-baked anode cell 2.0.3 bauxite a generic term for ores mainly composed of gibbsite, boehmite or diaspore, which, in addition to alumina, mainly contains impurities such as silicon oxide, iron oxide, titanium oxide, and compounds of minor or trace elements, and is the most important ore resource in alumina production at present 2.0.4 gibbsite an aluminum hydroxide, with molecular formula Al(OH)3, that is monoclinic, and has a density of 2.35 g/cm3 to 2.42 g/cm3 and a Mohs hardness of 2.5 to 3.5 2.0.5 diaspore an aluminum oxyhydroxide, with molecular formula AlOOH, that is orthorhomibc, and has a density of 3.3 g/cm3 to 3.5 g/cm3 and a Mohs hardness of 6.5 to 7 2.0.6 Bayer process a process of producing alumina, that is, the alumina in bauxite is directly extracted using caustic solution, to obtain sodium aluminate solution 2.0.7 sintering process a process of producing alumina, that is, aluminum-containing material is sintered using burdening, making the alumina therein convert into aluminate 2.0.8 combination process a generic term for process of producing alumina according to Bayer process and sintering process which are combined in different ways 2.0.9 serial combination process a process of producing alumina, that is, red mud, which is obtained by processing bauxite according to Bayer process, is processed according to sintering process to recycle the alumina and alkaline therein 2.0.10 mixed combination process a process of producing alumina, that is, red mud, which is obtained by processing bauxite according to Bayer process, is blended with an appropriate amount of bauxite and processed according to sintering process
Contents of GB 50530-2010
Foreword ii 1 General provisions 2 Terms 3 General requirements 4 Raw materials and fuels 4.1 Raw materials 4.2 Fuels 5 Storage and handling of raw materials and fuels, bauxite crushing 5.1 Unloading facilities of raw materials and fuels 5.2 Material stockyard 5.3 Bauxite crushing 5.4 Storage and delivery of caustic soda 5.5 Storage silo of soda 6 Lime burning and lime milk slaking 6.1 Lime burning 6.2 Lime milk slaking 7 Bauxite dressing 7.1 Grinding and classification 7.2 Flotation 7.3 Storage, preparation and addition of agent 7.4 Dewatering 7.5 Maintenance facilities 7.6 Automatic control, measuring and weighing 8 Slurry preparation 8.1 Bauxite grinding 8.2 Bauxite slurry preparation of dressing-Bayer process 8.3 Raw mix slurry adjustment of sintering process 9 Autoclave digestion 9.1 Pre-desilication of bauxite 9.2 Feeding pump to autoclave digester 9.3 Autoclave digestion 10 Sintering and sinter crushing 10.1 Preparation of coal powder 10.2 Sintering 10.3 Sinter crushing 11 Sinter leaching 12 Red mud settling, washing and control filtration 12.1 Red mud settling and washing 12.2 Control filtration 13 Desilication in sintering process 13.1 Desilication 13.2 Separation of desilication product 14 Decomposition of sodium aluminate solution 14.1 Seed precipitation 14.2 Carbonization 15 Hydrate separation, washing and storage 15.1 Hydrate separation and washing 15.2 Hydrate storage 16 Spent liquor evaporation, causticization and recycled spent liquor proportioning 16.1 Spent liquor evaporation 16.2 Separation of soda crystal 16.3 Causticization of soda crystal 16.4 Caustic solution proportioning 17 Hydrate calcination, product packing and stacking 17.1 Hydrate calcination 17.2 Alumina storage 17.3 Product packing and stacking Explanation of wording in this code List of quoted standards
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Keywords:
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