1. Field of the Invention
The present invention relates to an improved method for manufacturing a crystalline layered sodium disilicate and more particularly, to the improved method for manufacturing the crystalline layered sodium disilicate comprising the steps including the preparation of granules in a certain ratio of anhydrous sodium silicate cullet, a starting material, in the presence of some binders such as water and aqueous solution of sodium silicate, followed by a crystallization step of the granules, wherein a small amount of final product is recycled to the prior crystallization step in order to prevent the attachment of granules to an inner crystallization device, which occurs due to local sintering in a high-temperature crystallization condition of continual process and also to further enhance the unit productivity during the mass production of crystalline layered sodium disilicate.
2. Description of the Related Art
The term xe2x80x9cculletxe2x80x9d used as a starting material of this invention, which has been frequently used as a raw material in a field involved in the manufacture of sodium silicate solution, refers to a compound in a small lump or piece derived from amorphous sodium silicate, prepared in such a manner that a mixture of silica and sodium carbonate in an appropriate molar ratio (ratio of SiO2O, to Na2O, namely SiO2/Na2O) is heated at the temperature of 1000-1400xc2x0 C., melted and cooled.
In addition, the term xe2x80x9clayered sodium silicatexe2x80x9d refers to crystalline silica compounds expressed by xe2x80x9c(Na2O)x(SiO2)yxe2x80x9d (where y/x varies differently depending on the crystal structure and has the common values ranging from 2 to 11); among them, the crystalline layered sodium silicate expressed by Na2Si2O5 is reported to have various crystal forms such as xcex1, xcex2, xcex3 and xcex4-phases and with its excellent adsorptivity and ion-exchange capacity originated from structural specificity, the crystalline layered sodium disilicate has been useful as a catalytic carrier or in a variety of chemical processes such as separation and purification. With its higher binding capacity on the hardness components in water such as Ca2+ and Mg2+ in particular, the crystalline layered sodium disilicate in xcex4-phase, the crystalline layered sodium disilicate has been recently used as a water softener or detergent composition builder.
However, the process for manufacturing the crystalline layered sodium disilicate in xcex4-phase has recognized some disadvantages in that severe foaming induced by a leakage of remaining water is generated in the initial crystallization step, and with sintering and shrinkage of particles, they are deposited in the crystallization device.
To comply with this matter, U.S. Pat. No. 5,211,930 has added a method for recycling 10-50 wt % of final product to the crystallization step, thus preventing deposit of products in a calcination device.
However, the above method has proven to be uneconomical with poor unit productivity during mass production, since a large amount (10-5 wt %) of final product is recycled to the device; the reduction of unit productivity cannot be overcome in a process where powders containing a large amount of water is fed.
Under such circumstances, in an effort to prevent the deposits of final product in the crystallization device, the inventor et al. in their respective patents (U.S. Pat. No. 5,567,404, its corresponding Korea Patent No. 13997 and Korea Patent Appln. No. 97-33207) have disclosed some methods for manufacturing the crystalline layered sodium disilicate in such a manner that water or aqueous solution of sodium silicate in a small amount for agglomeration is added to a cullet powder, a starting material, thereby preparing granules with a small amount of water and then the granules are crystallized in calcination furnace, thus ensuring more simplification of manufacturing process, reduction in energy consumption, and removal of deposits remaining in the device. Notwithstanding this, these methods have still failed to eliminate the deposits of some granules in the device during the crystallization step, when a continual process for mass production is operated.
To overcome the aforementioned shortcoming that reactants are deposited in a crystallization device, the inventor et al. have found that a process recycling a small amount of final product to the device may not only eliminate the deposit of product in a calcination furnace associated with local sintering occurring at a higher temperature during continual process, but also recycle less amount than that of the U.S. Pat. No. 5,211,930, thus resulting in significant increase of unit productivity during mass production. In consequence, the inventor et al. have completed this invention.
Therefore, an object of this invention is to provide an improved method for manufacturing a crystalline layered sodium disilicate, being characterized in that some defects found in the crystallization device have been completely removed by specifying the agglomeration and recycling steps for possible continual process, thereby improving unit productivity during mass production.
This invention is characterized by an improved method for manufacturing crystalline layered sodium disilicate comprising the subsequent steps of a) preparing granules with the addition of water as binder to anhydrous sodium silicate cullet powder; b) drying and crystallizing the granules by heat calcination to prepare sodium disilicate, wherein 3-5 wt % of final product, sodium disilicate, is recycled to the prior crystallization step.
Also, this invention is characterized by an improved method for manufacturing the crystalline layered sodium disilicate comprising the subsequent steps of a) preparing granules with the addition of an aqueous solution of sodium silicate as binder to anhydrous sodium silicate cullet powder; b) drying and crystallizing the granules by heat calcination to prepare sodium disilicate, wherein 3-5 wt % of final product, sodium disilicate, is recycled to the prior crystallization step.
This invention is explained in detail as follows:
This invention relates to a method for manufacturing a crystalline layered sodium disilicate, performed in such subsequent steps that a certain amount of water or aqueous solution of sodium silicate is added to an anhydrous sodium silicate cullet powder comprising a certain ratio of chemical composition for the preparation of granules, followed by drying and calcining for their crystallization, wherein a step of recycling some final products to the crystallization device has contributed much to settlement of several problems associated with the continual operation, since the recycling process makes it possible to separate the reactants, which may be sintered in the device at a high temperature (500-800xc2x0 C.), from inner wall of the crystallization device. According to this invention, the recycling step of final product in small amounts is available in that from the step of preparing granules, the round-form agglomeration may minimize the contact area in the crystallization device.
As described in the respective patents (U.S. Pat. No. 5,567,404, its corresponding Korea Patent No. 139976 and Korea Patent Appln. No. 97-33207) disclosed by the inventor et al, the agglomeration step highlighted by this invention, which has several advantages in that a) unlike the conventional method with crystallization process for powder material, high-density materials supplied to crystallization device may cause no dust with a higher unit productivity; b) minimization of contact area with the device due to agglomeration may significantly prevent any attachment caused by the sintering of reactants. However, the manufacturing method using the agglomeration step has failed to efficiently prevent the attachment of reactants to the inner wall of calcination device during mass production of continual operation.
To efficiently prevent the attachment of granules to the device, a small amount of final product (less than 5 wt %) is recycled to separate the reactants sintered from inner wall of the crystallization device.
The process for manufacturing a crystalline layered sodium disilicate of this invention is briefly illustrated in FIG. 1 and each process step is explained in more detail as follows:
First, a cullet (the molar ratio of SiO2 to Na2O is 1.80-2.20) is pulverized to make a cutlet powder having less than 0.8 mm (D50≈0.3 mm) in its particle size;
Second, water and aqueous solution of sodium silicate (the molar ratio of SiO2 to Na2O used as a binder is 2.0-3.3, solid content: 15-40 wt %) is added to the cullet powder to prepare a granule having 1-30 mm (volumetric density: 1.1-1.6 g/cm) in its diameter; hence, the water used for the agglomeration of cullet powder acts not only as a binder, but also as an indispensable component for the phase transfer due to hydration. In view of the fact that the manufacturing conditions for granules vary differently depending upon the amount of water, water may be directly used but the use of aqueous solution of sodium silicate may enhance the adhesive power of solid component in the binder composition of cullet powder, thus making it easier to adjust the amount of water.
It is preferred that 5-30 wt % of water is added to an anhydrous sodium silicate cullet powder, when water is directly used as a binder. Further, it is preferred that an aqueous solution of sodium silicate containing 15-40 wt % of solid component is used as a binder for the adjustment of water contents; the amount of sodium silicate in aqueous solution is in the range of 10-30 wt % to the anhydrous sodium silicate cullet powder.
Hence, the agglomeration device includes any type of agglomeration device such as a round type, a cylindrical type, fluidized type and molding press.
Then, the step of drying the granules is performed, followed by calcination to finally prepare the crystalline layered sodium disilicate.
According to this invention, granules are subjected to a drying step before it is delivered to a continual calcination device, since such drying step may effectively prevent the combining of granules induced by the adhesiveness of aqueous solution of sodium silicate present in the surface of granules, while making it easier not only to deliver the granules, but also to form the phase variation during crystallization by facilitating the hydration in the granules.
However, the drying step at extremely high temperature is responsible for generation of any impurities, thus reducing the purity of final product. In this respect, it is preferred that the drying step is performed at 80-200xc2x0 C. until the amount of evaporated water becomes 0.2-1.0 wt %. The volumetric density of the granules, so dried, should be maintained at 1.1-1.6 g/cmxe2x80x2.
The granules are placed at a rotary calcination furnace, crystallized for 0.1-1 hour at 650-800xc2x0 C. to form a material with 0.1-0.5 g/cmxe2x80x2 of volumetric density, and pulverized with a crusher.
Meantime, the recycling step highlighted by this invention is to re-supply some of final product to a crystallization device, together with dried granules. Hence, the particle size of final product for recycling is of little significance but the step of recycling some micropowders may cause the occurrence of dusts, which will result in heavy load to a bag filter during continual operation. Therefore, it is preferred that the particle size of final product for recycling is in the range of 0.2-1.0 mm (D50≈0.6 mm).
The recycling step using a larger amount of final product is advantageous in preventing any attachment or formation of mass in the device but this may adversely affect the unit productivity. To achieve the objective of this invention, therefore, a priority should be given to the limitedness of the recycling amount of final product. Therefore, the recycling amount of final product is less than 5 wt % at maximum in proportion to the total amount of granule, preferably 3-5 wt %. Hence, if the recycling amount is less than 3 wt %, a sintering occurs in some granules which are momentarily attached to or detached from the inner wall of a calcination furnace, or a mass of granules is formed or sintered. At this time, the xcex1-type crystal phase occurs partially in the final product.
Further, if the recycling amount of final product exceeds 5 wt %, the individual rotation of granules impedes their swift delivery, when contacted with an excessive recycling amount of final product during the crystallization. Under such circumstances, any retention time of granules cannot be constantly maintained in addition to possible occurrence of dusts and furthermore, the unit productivity becomes significantly reduced thereto.
As such, the product prepared by recycling an appropriate amount of final product exhibits an excellent physical property as a xcex4-phase crystalline layered sodium disilicate in high purity.
The salient points relating to the process for manufacturing a crystalline layered sodium disilicate of this invention may be summarized as follows:
First, the homogeneous crystallization of granules may be ensured by recycling a small amount of final product together with granules, and the coagulation of granules and the inner wall of the device due to local sintering during crystallization may be prevented by the recycling powder.
Second, since the attachment of granules in the device may be prevented, the continual process is available and by recycling a small amount of final product, a higher unit productivity may also lead to an optimization of the process thereto.
USPTO Backgrounds
USPTO Backgrounds