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    • 3. 发明授权
    • Granular detergent builder
    • 颗粒洗涤剂助剂
    • US5874397A
    • 1999-02-23
    • US675991
    • 1996-07-09
    • Gunther SchimmelAlexander TapperVolker Thewes
    • Gunther SchimmelAlexander TapperVolker Thewes
    • C11D3/06C11D3/08C11D3/10C11D3/12
    • C11D3/1273C11D3/10
    • The invention relates to a granular detergent builder in the form of cogranules of a mixture of sodium bicarbonate and crystalline sheet silicates of the formula NaMSi.sub.x O.sub.2x+1 *yH.sub.2 O, where M is sodium or hydrogen, x is a number from 1.9 to 4, and y is a number from 0 to 20, whereina) the granular detergent builder contains 5 to 50% by weight of crystalline sheet silicate and 50 to 95% by weight of sodium bicarbonate;b) has a pH of .ltoreq.10 in 1% strength solution in distilled water;c) has a calcium-binding capacity of .gtoreq.150 mg Ca/g (30.degree. German hardness) and a magnesium-binding capacity of .gtoreq.4 mg Mg/g (3.degree. German hardness), andd) has an apparent density of .gtoreq.850 g/l.The invention likewise relates to a process for the production of such a granular detergent builder, and to its use in detergents and cleaners.
    • 本发明涉及碳酸氢钠和式NaMSixO 2 x + 1 * yH 2 O的结晶片状硅酸盐的混合物形式的颗粒状洗涤剂助洗剂,其中M为钠或氢,x为1.9至4的数,y为 是0至20的数,其中a)颗粒洗涤剂助洗剂含有5至50重量%的结晶硅酸盐和50至95重量%的碳酸氢钠; b)在1%浓度的蒸馏水溶液中具有 / = 150mg Ca / g(30德国硬度)和≥4mgMg / g(3德国硬度)的镁结合能力的钙结合能力,以及d)具有 表观密度> 850g / l。 本发明同样涉及一种生产这种颗粒状洗涤剂助洗剂的方法及其在洗涤剂和清洁剂中的应用。
    • 4. 发明授权
    • Process for producing amorphous sodium silicate
    • 无定形硅酸钠的制备方法
    • US5229095A
    • 1993-07-20
    • US839008
    • 1992-02-14
    • Gunther SchimmelMichael KotzianHerbert PanterAlexander Tapper
    • Gunther SchimmelMichael KotzianHerbert PanterAlexander Tapper
    • C01B33/32
    • C01B33/325C01B33/32
    • A process for producing amorphous sodium silicates having a water content of 0.3 to 6% by weight and an SiO.sub.2 /Na.sub.2 O molar ratio of (1.9 to 2.8) : 1 from a waterglass solution containing at least 20% by weight of solids, the water-glass solution is obtained by reacting quartz sand with sodium hydroxide solution at an SiO.sub.2 /Na.sub.2 O molar ratio of (2.0 to 2.8) : 1 at temperatures of 180 to 240.degree. C. and pressures of 10 to 30 bar. This waterglass solution is treated in a spray-drying zone with hot air at 200 to 300.degree. C. for a residence time of 10 to 20 seconds and at a temperature of the exit gas leaving the spray-drying zone of 90.degree. to 130.degree. C., to form a pulverulent amorphous sodium silicate having a water content (determined as the loss on ignition at 700.degree. C.) of 15 to 23% by weight and a bulk density of more than 300 g/l. The pulverulent sodium silicate is introduced into an obliquely arranged rotary kiln fitted with devices for moving solids and treated therein with flue gas in countercurrent at temperatures from 250.degree. up to 500.degree. C. for 1 to 60 minutes. The rotary kiln is here insulated in such a way that its outside wall temperature is less than 60.degree. C. Finally, the amorphous sodium silicate emerging from the rotary kiln is comminuted by means of a mechanical crusher to grain sizes of 0.1 to 12 mm.
    • 从含有至少20重量%固体的水玻璃溶液制备水含量为0.3-6重量%和SiO 2 / Na 2 O摩尔比为(1.9至2.8):1的无定形硅酸钠的方法, 通过在180-240℃的温度和10至30巴的压力下使石英砂与氢氧化钠溶液以(2.0至2.8):1的SiO 2 / Na 2 O摩尔比反应获得玻璃溶液。 该水玻璃溶液在200〜300℃的热风喷雾干燥区中处理10〜20秒的停留时间,离开喷雾干燥区的出口气体的温度为90〜130℃ 以形成15〜23重量%的含水量(在700℃下测定为灼烧损失)的粉末状无定形硅酸钠,堆积密度大于300g / l。 将粉状硅酸钠引入倾斜布置的旋转窑中,该回转窑装有用于移动固体的装置,并在250℃至500℃的温度下逆流处理烟道气1至60分钟。 回转窑的外壁温度低于60℃,最后将回转窑出现的无定形硅酸钠粉碎成0.1〜12mm的粒径。
    • 6. 发明授权
    • Process for the production of crystalline sodium disilicate in an
externally heated rotary kiln having temperature zones
    • 在具有温度区域的外部加热回转窑中生产结晶二硅酸钠的方法
    • US5308596A
    • 1994-05-03
    • US986983
    • 1992-12-08
    • Michael KotzianGunther SchimmelAlexander TapperKnut Bauer
    • Michael KotzianGunther SchimmelAlexander TapperKnut Bauer
    • C01B33/32C01B33/38
    • C01B33/38
    • To prepare crystalline sodium disilicates having a laminar structure, a molar ratio of SiO.sub.2 to Na.sub.2 O of (1.9 to 2.1) 1 and a water content of less than 0.3% by weight, a water glass solution is first obtained by reacting sand with sodium hydroxide solution in a molar ratio of SiO.sub.2 to Na.sub.2 O of (2.0 to 2.3) : 1 at temperatures of 180.degree. to 240.degree. C. and pressures of 10 to 30 bar. This water glass solution having at least 20% by weight of solids is treated in a spray drier with hot air at 200.degree. to 300.degree. C. with the formation of a pulverulent amorphous sodium disilicate having a water content (determined as loss on heating at 700.degree. C.) of 15 to 23% by weight and a bulk density of at least 300 g/l. The spray-dried pulverulent, amorphous sodium disilicate is ground. The ground sodium disilicate is introduced into a rotary kiln equipped with devices for moving solids, externally heated via the wall and having in its interior a plurality of different temperature zones, and is treated therein at temperatures of 400.degree. to 800.degree. C. for 1 to 60 minutes with formation of crystalline sodium disilicate.
    • 为了制备具有层状结构,SiO 2与Na 2 O的摩尔比(1.9-2.1)1和含水量小于0.3重量%的结晶二硅酸钠,首先通过使沙子与氢氧化钠溶液 在180至240℃的温度和10至30巴的压力下,SiO 2与Na 2 O的摩尔比为(2.0至2.3):1。 具有至少20重量%固体的水玻璃溶液在喷雾干燥器中用200-300℃的热空气处理,形成具有水分含量的粉状无定形二硅酸钠(确定为在 700℃)为15〜23重量%,堆积密度为300g / l以上。 将喷雾干燥的粉状无定形二硅酸钠研磨。 将磨碎的二硅酸钠引入装备有用于移动固体的装置的回转窑,其外部经由壁加热并在其内部具有多个不同的温度区域,并在400℃至800℃的温度下处理1 至60分钟,形成结晶二硅酸钠。
    • 8. 发明授权
    • Process for producing crystalline sodium silicates having a layered
structure
    • 具有层状结构的结晶硅酸钠的制造方法
    • US5236682A
    • 1993-08-17
    • US846758
    • 1992-03-05
    • Gunther SchimmelMichael KotzianHerbert PanterAlexander Tapper
    • Gunther SchimmelMichael KotzianHerbert PanterAlexander Tapper
    • C01B33/32C01B33/38
    • C01B33/325C01B33/32C01B33/38
    • For producing crystalline sodium silicates having a layer structure, an SiO.sub.2 /Na.sub.2 O molar ratio of (1.9 to 2.1):1 and a water content of less than 0.3% by weight from a waterglass solution containing at least 20% by weight of solids, the waterglass solution is obtained by reacting quartz sand with sodium hydroxide solution at an SiO.sub.2 /Na.sub.2 O molar ratio of (2.0 to 2.3):1 at temperatures of 180.degree. to 240.degree. C. and pressures of 10 to 30 bar. This waterglass solution is treated in a spray-drying zone with hot air at 200.degree. to 300.degree. C. for a residence time of 10 to 25 seconds and at a temperature of the exit gas leaving the spray-drying zone of 90.degree. to 130.degree. C., to form a pulverulent amorphous sodium silicate having a water content (determined as the loss on ignition at 700.degree. C.) of 15 to 23% by weight and a bulk density of more than 300 g/l. The pulverulent, amorphous, water-containing sodium silicate is introduced into an obliquely arranged rotary kiln fitted with devices for moving solids and treated therein with flue gas in countercurrent at temperatures from more than 500.degree. up to 850.degree. C. for 1 to 60 minutes to form crystalline soidium silicate. The rotary kiln is here insulated in such a way that its outside wall temperature is less than 60.degree. C. Finally, the crystalline sodium silicate emerging from the rotary kiln is comminuted by means of a mechanical crusher to grain sizes of 0.1 to 12 mm.
    • 为了生产具有层状结构的结晶硅酸钠,SiO 2 / Na 2 O摩尔比为(1.9-2.1):1,水含量小于含有至少20重量%固体的水玻璃溶液的0.3重量% 通过使SiO 2 / Na 2 O摩尔比为(2.0〜2.3):1的石英砂与氢氧化钠溶液在180〜240℃的温度和10〜30巴的压力下反应获得水玻璃溶液。 该水玻璃溶液在200℃至300℃的热空气的喷雾干燥区中处理,停留时间为10至25秒,并且在离开喷雾干燥区的出口气体的温度为90°至130° 以形成具有15至23重量%的含水量(以700℃测定的点火损失确定)的粉末状无定形硅酸钠,堆积密度大于300g / l。 将粉末状,无定形含水硅酸钠引入倾斜布置的回转窑中,该回转窑装有固体移动装置,并在大于500℃至850℃的温度下逆流处理烟气1至60分钟 以形成硅酸的结晶硅酸盐。 回转窑的外壁温度低于60℃,最后将回转窑中出现的结晶硅酸钠粉碎成0.1〜12mm的粒度粉碎机。
    • 10. 发明授权
    • Process for the peparation of cogranulates comprising aluminosilicates
and sodium silicates
    • 用于分离包含硅铝酸盐和硅酸钠的颗粒的方法
    • US5814289A
    • 1998-09-29
    • US688354
    • 1996-07-30
    • Alexander TapperGunther SchimmelGerd WingefeldHans-Peter Rieck
    • Alexander TapperGunther SchimmelGerd WingefeldHans-Peter Rieck
    • C11D3/12C01B33/26C11D7/14
    • C11D3/128C11D3/1273
    • Cogranulates of high bulk density which easily disintegrate in water and comprise aluminosilicates and crystalline sodium silicates having a layered structure. The aluminosilicates contained therein are those of the formula M.sub.2/n O.Al.sub.2 O.sub.3. XSiO.sub.2. yH.sub.2 O in which M is an alkali metal or alkaline earth metal, n indicates the valency of the cation, x is.gtoreq.2 and y has a value of between 0 and 8. The sodium silicates have an SiO.sub.2 /Na.sub.2 O ratio of (1.8 to 4.2):1. These cogranulates are prepared by mixing the pulverulent aluminosilicates and sodium silicates with one another and introducing the mixture into a zone in which it is compacted between two rolls rotating in opposite directions to form a compact. After comminution of the compact, the desired particle sizes are finally separated off from the oversize and undersize material. The cogranulates can be used in detergents and cleaning agents.
    • 高堆积密度的钙质,其容易在水中分解并且包含具有层状结构的硅铝酸盐和结晶硅酸钠。 其中含有的硅铝酸盐是式M2 / nO.Al2O3的硅铝酸盐。 XSiO2。 yH 2 O,其中M是碱金属或碱土金属,n表示阳离子的化合价,x是≥2,y的值在0和8之间。硅酸钠的SiO 2 / Na 2 O比为(1.8 至4.2):1。 通过将粉状硅铝酸盐和硅酸钠彼此混合并将混合物引入到在相反方向上旋转的两个辊之间被压实的区域中以形成压块,来制备这些cogranulate。 粉碎粉碎后,最终从尺寸过大和尺寸过小的材料中分离所需的粒径。 可以在洗涤剂和清洁剂中使用。