Process for preparing olivine sand cores and molds

Abstract

An inorganic cement binder for a foundry aggregate comprising, in combination, potassium olivine phosphate and as a hardener therefor, water, aqueous sodium silicate, or aqueous phosphoric acid.

Description

This invention relates to an improved process for preparing foundry cores and molds. In a particular aspect this invention relates to an improved binder for the aggregate and process for preparing it.

Binders for foundry aggregates used for making foundry cores and molds for metal castings are usually organic in nature, i.e. organic polymers and resins. These organic compounds are decomposed or volatilized when the molten metal contacts the core or mold and the resulting fumes and vapors cause a problem of air pollution. There is, therefore, a need to provide an all inorganic, non-volatile binder which is non-contaminating to the environment.

SUMMARY OF THE INVENTION

It is an object of this invention to provide an improved process for preparing foundry molds and cores using a foundry aggregate and an inorganic cement binder therefor.

It is another object of this invention to provide an improved binder for foundry aggregate and a process for preparing it.

Other objects of this invention will be apparent to those skilled in the art from the disclosure herein.

It is the discovery of this invention to provide an improved process for preparing foundry cores and molds using a foundry aggregate and an inorganic cement binder therefor. The improvement is provided by using as a binder the reaction product of a silico-phosphate, such as the reaction product of a metal dihydrogen phosphate, e.g. the zinc, or preferably, the potassium compound, with a mineral silicate, including but not limited to zeolites, nepheline syenite and preferably olivine. The preferred compound, the reaction product of potassium dihydrogen phosphate with olivine has, for convenience, been designated potassium olivine phosphate, or simply KOP. Water, aqueous sodium silicate or dilute phosphoric acid can be used as hardening agents for the binder.

DETAILED DISCUSSION

The metal silico-phosphate useful in the practice of this invention is easily prepared by mixing a metal dihydrogen phosphate, e.g. potassium dihydrogen phosphate, with the mineral silicate, e.g. olivine and heating the mixture to above the melting point of the metal dihydrogen phosphate for about one hour. For example, potassium dihydrogen phosphate melts at about 810.degree. C. and the zinc salt melts at about 1000.degree. C. The mineral silicate should be comminuted, e.g. preferably to pass a 200 mesh sieve. The metal dihydrogen phosphate is preferably added as a dry powder, but it can also be added as an aqueous solution, e.g. a saturated solution, or as a slurry. The proportions of metal dihydrogen phosphate and mineral silicate are not critical, a range of 0.5-10:1 by weight respectively being useful. However, a proportion of about 2:1 by weight is preferred especially when the reactants are potassium dihydrogen phosphate and olivine.

During the heating process, the mixture forms a viscous polymeric melt. The metal dihydrogen phosphate is converted to metal polyphosphate which dissolves and reacts with the silicate, after which it is allowed to cool. As it cools it hardens and becomes increasingly brittle and after equilibration at room temperature and normal relative humidity. (50%) it crumbles easily. The KOP should be prepared in a heat-resistant and acid-resistant vessel. Steel is rapidly attacked by the reaction mixture at elevated temperatures.

According to the process of this invention, the aggregate is preferably, but not necessarily, first mixed with ground KOP in an amount of about 2-12% based on the aggregate. After mixing the aggregate with the KOP, there is added the hardener with additional thorough mixing. The order of mixing is not critical but it has been found that mixing the dry ingredients first and then adding the liquid ingredients tends to ensure homogeneity of the final mixture. The mixture of aggregate, binder and hardener is now delivered to the mold or core box where it is permitted to cure for 2 hours or until a compressive strength of 50 psi is obtained using the Dietert tester. The core or mold is then removed and is allowed to further harden under ambient conditions for an hour or more or overnight.

The hardener used in the practice of this invention is water, aqueous sodium silicate or preferably an aqueous solution of phosphoric acid. From about 2% to about 10% of KOP based on the weight of the aggregate is used, and similarly from about 2% to about 10% of water or dilute phosphoric acid, e.g. 50%, is used. The purpose of the acid is to retard the cure rates. Thus the higher the concentration of the acid, the slower the rate of cure, and the concentration of the acid, the more rapid the cure rate. Under foundry conditions of 70-85.degree. F. and 70-85% relative humidity the preferred binder composition was KOP-H.sub.2 O-H.sub.3 PO.sub.4 (50% black wet-process acid) in a ratio of 2:1:1 to 3:2:2.

The foundry aggregate useful in the practice of this invention can be any known aggregate such as silica sand, zircon, olivine, alumino silicate sand (zeolite), chromite sand, and the like. Olivine is a preferred aggregate. The aggregate should be of a particle size consistent with desired result.

The orthophosphoric acid used in the practice of this invention can be purified phosphoric acid, such as the 85% grade. Because of the economics, however, the preferred acid is wet process acid and can be the so-called black acid, but green acid is also useful, although it is rather dilute (about 30%) and may require longer curing time. Black acid is customarily about 54% concentration and can be used as is, or it can be further diluted, depending on curing time required.

The sodium silicate useful in the practice of this invention is not critical as to concentration. For convenience, it is preferred that it be of such concentration as to furnish the required amount of water.

Olivine sand is the preferred aggregate for use with the improved binder of this invention. It is a natural mineral consisting of a solid solution rich in magnesium orthosilicate (Fosterite) with a minor amount of ferric orthosilicate (Fayalite). Olivine is a major component of dunite rock. Typically, olivine has a composition falling within the following general ranges:

MgO--40-52% by weight SiO.sub.2 --35-45% by weight FEO--6.5-10% by weight Al.sub.2 O.sub.3, K.sub.2 O, Na.sub.2 O--Trace Any olivine falling within the above ranges is suitable for the practice of this invention.

The invention will be better understood with reference to the following examples. It is understood that these examples are intended only to illustrate the invention and it is not intended that the invention be limited thereby.

EXAMPLE 1

Potassium olivine phosphate (KOP) was prepared as follows. Olivine, comminuted to pass a 200 mesh sieve, and potassium dihydrogen phosphate were thoroughly mixed in a 1:1 dry weight ratio and the mixture was delivered to an alumina container. The mixture was then heated to over 805.degree. C. for a period of time to allow the polymeric melt to form (178 -3 hours). It was then allowed to cool, whereupon it crumbled easily. After removing the KOP from the container, it wa broken up, ground and screened to -200 mesh using a pulverizer.

Material so prepared was then used as a binder for olivine sand. KOP 150 g was first mixed with the sand 1500 g, and water 75 g was added. The mixture was quickly packed into a Dietert Tensile Core Box which produces a "dog-bone" shaped core. After one hour the compressive strength was determined using a Dietert (454B) Mold Stength Tester. After standing overnight, the tensile strength was measured. The results are given in Table 1.

EXAMPLE 2

The experiment of Example 1 was repeated in all essential details except that a 50% solution of aqueous phosphoric acid was substituted for water to retard the cure rate. The results are given in Table 1.

EXAMPLE 3

The experiment of Example 1 was repeated in all essential details except that sodium silicate solution was substituted for the water. The sodium silicate used was No. 22 obtained from E. I. duPont de Nemours Company. It had a ratio of SiO.sub.2 to Na.sub.2 O of 1.90. The SiO.sub.2 content was 28.5% and the Na.sub.2 O content was 15.0%.

EXAMPLE 4

The experiment of Example 1 was repeated in all essential details except that the KOP was prepared from a 2:1 mixture of dihydrogen potassium phosphate and olivine. The results are given in Table 1.

EXAMPLE 5

The experiment of Example 1 was repeated in all essential details except that the KOP was prepared from a 3:1 mixture of potassium dihydrogen phosphate and olivine. The results are given in Table 1.

EXAMPLE 6

The experiment of Example 5 was repeated in all essential details except that 8% of KOP based on sand, and 4% water were used. The results are given in Table 1.

EXAMPLE 7

The experiment of Example 1 was repeated in all essential details except that the KOP was prepared from 6:1 mixture of KH.sub.2 PO.sub.4 and olivine. The results are given in Table 1

TABLE 1______________________________________Example Compressive TensileNumber Strength at 1 Hr Strength______________________________________1 26 psi 20 psi2 13 703 35 554 36 105 45 106 50+ 87 16 20______________________________________

EXAMPLE 8

The experiment of Example 5 was repeated in all essential details except that the binder consisted of KOP, water and phosphoric acid in a 2:1:1 ratio by weight and the amount added to the sand was sufficient to provide 6% KOP based on the weight of the sand. The temperature was 75.degree. F. and the relative humidity 65%. The results are given in Table 2.

EXAMPLE 9

The experiment of Example 1 was repeated in all essential details except that the binder consisted of KOP, water and phosphoric acid in a 2:1:1 ratio by weight and the amount added to sand was sufficient to provide 6% KOP. The results are given in Table 2.

EXAMPLE 10

The experiment of Example 9 was repeated in all essential details except that the amount of binder added to the sand was sufficient to provide 3% KOP. The results are given in Table 2.

EXAMPLE 11

The experiment of Example 9 was repeated in all essential details except that the KOP was prepared by heating a 1:1:1 by weight ratio of potassium dihydrogen phosphate olivine and water at 850.degree. C. for three hours. The mold was allows to stand overnight and the tensile strength was measured. It was then heated at 900.degree. C. for two hours and allowed to cool to room temperature at which time the tensile strength was again measured. The results are given in Table 2.

TABLE 2______________________________________ CompressiveExample 50% Strength at Tensile StrengthNumber KOP H.sub.3 PO.sub.4 2 Hrs Pre* Post**______________________________________ 8 6% 6% 40 psi 160 psi 65 psi 9 6 5 40 170 6010 3 3 25 105 1011 6 6 10 130 5012 3 3 10 70 30______________________________________ *Before heating. **After heating.

EXAMPLE 12

The experiment of Example 1 is repeated in all essential details except that a zeolite is substituted for olivine in the reaction with potassium dihydrogen phosphate. The mold thereby obtained has good compressive strength.

EXAMPLE 13

The experiment of Example 1 is repeated in all essential details except that nepheline syenite is substituted for olivine in the reaction with potassium dihydrogen phosphate. The mold thereby obtained has good compressive strength.

Claims

1. An improved process for preparing foundry cores and molds from a foundry aggregate and an inorganic cement binder therefor, comprising the steps of (a) mixing the aggregate with potassium olivine phosphate and as a hardener therefor water, aqueous sodium silicate, or aqueous phosphoric acid, (b) delivering the resulting mixture into a core box or mold box and (c) allowing to stand for a length of time sufficient for the binder to cure and form the core or mold.

2. The process of claim 6 wherein the aggregate is olivine, silica, zircon, zeolite or chromite sand.

3. The process of claim 6 wherein the hardener is water.

4. The process of claim 1 wherein the hardener is aqueous phosphoric acid.

5. The process of claim 1 wherein the hardener is aqueous sodium silicate.

6. An improved process for preparing foundry cores and molds from a foundry aggregate and an inorganic cement binder therefor, comprising the steps of (a) mixing the aggregate with zinc olivine phosphate and as a hardener therefor water, aqueous sodium silicate, or aqueous phosphoric acid, (b) delivering the resulting mixture into a core box or mold box and (c) allowing to stand for a length of time sufficient for the binder to cure and form the core or mold.

7. The process of claim 1 wherein the hardener is water.

8. The process of claim 1 wherein the hardener is aqueous phosphoric acid.

9. The process of claim 1 wherein the hardener is aqueous sodium silicate.