CN101837985B - Preparation method of sodium metasilicate nonahydrate - Google Patents
Preparation method of sodium metasilicate nonahydrate Download PDFInfo
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- CN101837985B CN101837985B CN2010101664209A CN201010166420A CN101837985B CN 101837985 B CN101837985 B CN 101837985B CN 2010101664209 A CN2010101664209 A CN 2010101664209A CN 201010166420 A CN201010166420 A CN 201010166420A CN 101837985 B CN101837985 B CN 101837985B
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- Prior art keywords
- sodium metasilicate
- reaction product
- waste glass
- metasilicate nonahydrate
- total mass
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- PHIQPXBZDGYJOG-UHFFFAOYSA-N sodium silicate nonahydrate Chemical compound O.O.O.O.O.O.O.O.O.[Na+].[Na+].[O-][Si]([O-])=O PHIQPXBZDGYJOG-UHFFFAOYSA-N 0.000 title claims abstract description 25
- 238000002360 preparation method Methods 0.000 title claims abstract description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 30
- 239000011521 glass Substances 0.000 claims abstract description 23
- 239000002699 waste material Substances 0.000 claims abstract description 22
- 239000007795 chemical reaction product Substances 0.000 claims abstract description 18
- 239000000843 powder Substances 0.000 claims abstract description 13
- 238000003756 stirring Methods 0.000 claims abstract description 12
- 239000000203 mixture Substances 0.000 claims abstract description 6
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 claims 1
- 229910052938 sodium sulfate Inorganic materials 0.000 claims 1
- 235000011152 sodium sulphate Nutrition 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 abstract description 10
- 235000011121 sodium hydroxide Nutrition 0.000 abstract description 9
- DBMJMQXJHONAFJ-UHFFFAOYSA-M Sodium laurylsulphate Chemical compound [Na+].CCCCCCCCCCCCOS([O-])(=O)=O DBMJMQXJHONAFJ-UHFFFAOYSA-M 0.000 abstract description 5
- 230000035484 reaction time Effects 0.000 abstract description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract description 4
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 239000000377 silicon dioxide Substances 0.000 abstract description 2
- 235000012239 silicon dioxide Nutrition 0.000 abstract description 2
- KKCBUQHMOMHUOY-UHFFFAOYSA-N sodium oxide Chemical compound [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 abstract description 2
- 229910001948 sodium oxide Inorganic materials 0.000 abstract description 2
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 abstract description 2
- 239000004115 Sodium Silicate Substances 0.000 abstract 1
- 150000004690 nonahydrates Chemical class 0.000 abstract 1
- 235000019795 sodium metasilicate Nutrition 0.000 abstract 1
- 229910052911 sodium silicate Inorganic materials 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 description 6
- 238000001035 drying Methods 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- 239000003513 alkali Substances 0.000 description 4
- 239000013078 crystal Substances 0.000 description 4
- 238000002425 crystallisation Methods 0.000 description 4
- 230000008025 crystallization Effects 0.000 description 4
- 239000002270 dispersing agent Substances 0.000 description 4
- 235000019333 sodium laurylsulphate Nutrition 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 239000005357 flat glass Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000003014 ion exchange membrane Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 235000019353 potassium silicate Nutrition 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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- Detergent Compositions (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
Abstract
一种九水偏硅酸钠的制备方法,将废玻璃清洗干净、烘干、磨成200目以上玻璃粉,然后将浓度为15%~30%的NaOH溶液与废玻璃粉按质量比为4-7∶1混合,加热至90℃~100℃,持续搅拌下反应50min~150min;待反应产物冷却至50℃~60℃时,边搅拌边加入反应产物总质量0.5%~1%的九水偏硅酸钠,并同时加入反应产物总质量0.1%~0.5%的十二烷基硫酸钠,自然降至室温,析晶18小时~68小时;25℃~30℃温度下,烘200min~300min。本发明可以充分利用废玻璃中的主要成分二氧化硅和氧化钠,降低生产中烧碱用量,减少反应时间,降低生产能耗和生产成本。A preparation method of sodium metasilicate nonahydrate, the waste glass is cleaned, dried, and ground into glass powder of more than 200 meshes, and then the NaOH solution with a concentration of 15% to 30% and the waste glass powder are mixed in a mass ratio of 4 - Mix 7:1, heat to 90°C~100°C, and react under continuous stirring for 50min~150min; when the reaction product is cooled to 50°C~60°C, add 0.5%~1% of the total mass of the reaction product nonahydrate while stirring Sodium metasilicate, and at the same time add 0.1% to 0.5% sodium dodecyl sulfate of the total mass of the reaction product, naturally cool down to room temperature, and crystallize for 18 hours to 68 hours; at 25°C to 30°C, bake for 200min to 300min . The invention can make full use of silicon dioxide and sodium oxide, the main components in waste glass, reduce the amount of caustic soda used in production, reduce reaction time, and reduce production energy consumption and production cost.
Description
技术领域 technical field
本发明属于无机非金属材料制备领域。涉及一种生产九水偏硅酸钠的方法,特别涉及一种利用废玻璃生产九水偏硅酸钠的方法。The invention belongs to the field of preparation of inorganic non-metallic materials. It relates to a method for producing sodium metasilicate nonahydrate, in particular to a method for producing sodium metasilicate nonahydrate by using waste glass.
背景技术 Background technique
九水偏硅酸钠在造纸、机械、电子、化工、建筑材料、食品、油田、采矿、陶瓷等领域具有广泛的用途,特别是在洗涤剂工业已成为严重污染环境的含磷助剂的最好替代产品。而目前九水偏硅酸钠的生产通常用水玻璃和氢氧化钠为主要原料,经蒸发浓缩、冷却结晶、离心分离、干燥等工艺制得,不仅能耗大、生产成本高,资源消耗量也较大。Sodium metasilicate nonahydrate is widely used in papermaking, machinery, electronics, chemical industry, building materials, food, oil field, mining, ceramics and other fields, especially in the detergent industry, which has become the best choice for phosphorus-containing additives that seriously pollute the environment Good alternative product. At present, the production of sodium metasilicate nonahydrate usually uses water glass and sodium hydroxide as the main raw materials, and is obtained through processes such as evaporation and concentration, cooling and crystallization, centrifugal separation, and drying. larger.
发明内容 Contents of the invention
本发明的目的是利用废玻璃生产九水偏硅酸钠,以降低九水偏硅酸钠的生产能耗、节约资源,降低成本。The purpose of the present invention is to use waste glass to produce sodium metasilicate nonahydrate, so as to reduce the production energy consumption of sodium metasilicate nonahydrate, save resources and reduce costs.
本发明是通过以下技术方案实现的。The present invention is achieved through the following technical solutions.
将废玻璃清洗干净、烘干、磨成200目以上玻璃粉,然后按以下步骤:Clean the waste glass, dry it, and grind it into glass powder of more than 200 mesh, and then follow the steps below:
(1)将浓度为15%~30%的NaOH溶液与废玻璃粉按质量比为4~7混合,加热至90℃~100℃,持续搅拌下反应50min~150min;(1) Mix NaOH solution with a concentration of 15% to 30% and waste glass powder at a mass ratio of 4 to 7, heat to 90°C to 100°C, and react for 50min to 150min under continuous stirring;
(2)待反应产物冷却至50℃~60℃时,边搅拌边加入反应产物总质量0.5%~1%的九水偏硅酸钠作为晶种,并同时加入反应产物总质量0.1%~0.5%的十二烷基硫酸钠作为分散剂,然后自然降至室温,析晶18小时~68小时;(2) When the reaction product is cooled to 50°C to 60°C, add sodium metasilicate nonahydrate with a total mass of 0.5% to 1% of the total mass of the reaction product as a seed crystal while stirring, and simultaneously add 0.1% to 0.5% of the total mass of the reaction product % sodium lauryl sulfate as a dispersant, then naturally lowered to room temperature, and crystallized for 18 hours to 68 hours;
(3)25℃~30℃温度下,烘干200min~300min,即得到九水偏硅酸钠产品。(3) Dry at 25°C-30°C for 200min-300min to obtain sodium metasilicate nonahydrate.
本发明以废玻璃为主要原料制备九水偏硅酸钠,可以充分利用废玻璃中的主要成分二氧化硅和氧化钠,充分利用废弃资源,降低生产中烧碱用量;废玻璃粉与NaOH反应活性高,可以减少反应时间,降低生产能耗。具有节能、降耗、降低生产成本的优点。The present invention uses waste glass as the main raw material to prepare sodium metasilicate nonahydrate, which can make full use of silicon dioxide and sodium oxide, the main components in waste glass, make full use of waste resources, and reduce the amount of caustic soda used in production; the reactivity of waste glass powder and NaOH High, can reduce reaction time and reduce production energy consumption. It has the advantages of energy saving, consumption reduction and production cost reduction.
具体实施方式 Detailed ways
本发明将通过以下实施例作进一步说明。The invention will be further illustrated by the following examples.
实施例1:Example 1:
以废平板玻璃和工业烧碱为主要原料。将废玻璃清洗干净、烘干,磨成200目玻璃粉;将工业烧碱配成浓度为25%的NaOH溶液,与废玻璃粉按质量比为4.8∶1混合,并加热至95℃使它们进行反应,加热反应过程持续搅拌,反应时间为70min;反应完毕后待粘稠状的反应产物冷却至50℃,边搅拌边加入反应产物总质量0.5%的九水偏硅酸钠作为晶种,并同时加入反应产物总质量0.1%的十二烷基硫酸钠作为分散剂,然后自然降至室温,九水偏硅酸钠缓慢析晶。九水偏硅酸钠析晶需38小时。将多余水份烘干,烘干温度为30℃,烘干时间220min左右,即得到九水偏硅酸钠产品。The main raw materials are waste flat glass and industrial caustic soda. Clean the waste glass, dry it, and grind it into 200-mesh glass powder; make industrial caustic soda into NaOH solution with a concentration of 25%, mix it with waste glass powder at a mass ratio of 4.8:1, and heat them to 95°C to make them Reaction, heating and stirring continuously during the reaction process, the reaction time is 70min; after the reaction is completed, the viscous reaction product is cooled to 50°C, and sodium metasilicate nonahydrate with 0.5% of the total mass of the reaction product is added as a seed crystal while stirring, and At the same time, 0.1% sodium lauryl sulfate of the total mass of the reaction product was added as a dispersant, and then naturally cooled to room temperature, sodium metasilicate nonahydrate slowly crystallized. It takes 38 hours for the crystallization of sodium metasilicate nonahydrate. Dry the excess water, the drying temperature is 30°C, and the drying time is about 220 minutes, and the product of sodium metasilicate nonahydrate is obtained.
实施例2:Example 2:
以废玻璃酒瓶和浓度为25%的离子膜碱为主要原料。将废玻璃清洗干净、烘干,将其磨成粉(200目以上);将离子膜碱与废玻璃粉按质量比为5.2∶1混合,并加热至100℃使它们进行反应,加热反应过程持续搅拌,反应时间为85min;反应完毕后待粘稠状的反应产物冷却至60℃,边搅拌边加入反应产物总质量0.6%的九水偏硅酸钠作为晶种,并同时加入反应产物总质量0.1%的十二烷基硫酸钠作为分散剂,然后自然降至室温,九水偏硅酸钠缓慢析晶。九水偏硅酸钠析晶需42小时。将多余水份烘干,烘干温度为30℃,烘干时间260min左右,即得到九水偏硅酸钠产品。The main raw materials are waste glass wine bottles and ionic membrane alkali with a concentration of 25%. Clean the waste glass, dry it, and grind it into powder (above 200 mesh); mix the ion-exchange membrane alkali and waste glass powder at a mass ratio of 5.2:1, and heat them to 100°C to make them react, and heat the reaction process Continue to stir, and the reaction time is 85min; after the reaction is completed, the viscous reaction product is cooled to 60°C, and sodium metasilicate nonahydrate with 0.6% of the total mass of the reaction product is added as a seed crystal while stirring, and the total mass of the reaction product is added at the same time. 0.1% sodium lauryl sulfate was used as a dispersant, and then naturally cooled to room temperature, sodium metasilicate nonahydrate slowly crystallized. It takes 42 hours for the crystallization of sodium metasilicate nonahydrate. Dry the excess water, the drying temperature is 30°C, and the drying time is about 260 minutes, and the product of sodium metasilicate nonahydrate is obtained.
实施例3:Example 3:
以废平板玻璃和浓度为25%的隔膜碱为主要原料。将废玻璃清洗干净、烘干,将其磨成粉(200目以上);将隔膜碱与废玻璃粉按质量比为5.8∶1混合,并加热至95℃使它们进行反应,加热反应过程中应持续搅拌,反应时间为75min;反应完毕后待将粘稠状的反应产物冷却至55℃,边搅拌边加入反应产物总质量0.6%的九水偏硅酸钠作为晶种,并同时加入反应产物总质量0.2%的十二烷基硫酸钠作为分散剂,然后自然降至室温,九水偏硅酸钠缓慢析晶。九水偏硅酸钠析晶需40小时。将多余水份烘干,烘干温度为30℃,烘干时间230min,即得到九水偏硅酸钠产品。The main raw materials are waste flat glass and diaphragm alkali with a concentration of 25%. Clean the waste glass, dry it, and grind it into powder (more than 200 mesh); mix the diaphragm alkali and waste glass powder at a mass ratio of 5.8:1, and heat them to 95°C to make them react. Stirring should be continued, and the reaction time is 75 minutes; after the reaction is completed, cool the viscous reaction product to 55°C, and add sodium metasilicate nonahydrate with 0.6% of the total mass of the reaction product as a seed crystal while stirring, and add the reaction product at the same time 0.2% sodium lauryl sulfate in the total mass of the product was used as a dispersant, and then naturally cooled to room temperature, and sodium metasilicate nonahydrate slowly crystallized. It takes 40 hours for the crystallization of sodium metasilicate nonahydrate. Dry the excess water at 30°C for 230 minutes to obtain the sodium metasilicate nonahydrate product.
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CN102190310B (en) * | 2011-01-06 | 2013-03-06 | 内蒙古大唐国际再生资源开发有限公司 | Method for manufacturing sodium metasilicate nonahydrate with fly ashes |
CN102826562B (en) * | 2012-09-14 | 2014-03-26 | 天津理工大学 | Method for preparing water glass by utilizing waste lead-containing glass and separating lead-containing compound |
CN102951652A (en) * | 2012-12-05 | 2013-03-06 | 朔州市润泽投资发展有限公司 | Method for producing sodium metasilicate by low-concentration sodium silicate solution |
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CN113277519B (en) * | 2021-06-22 | 2022-09-16 | 清华大学 | Silica mesoporous material using waste glass as raw material and its preparation method and use |
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