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MarketScreener Homepage  >  Equities  >  Toronto Stock Exchange  >  Karnalyte Resources Inc    KRN   CA4856722083

KARNALYTE RESOURCES INC

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Patent Issued for Process For Producing High Grade Hydromagnesite And Magnesium Oxide (USPTO 10,364,156): Karnalyte Resources Inc.

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08/14/2019 | 05:12pm EDT

2019 AUG 14 (NewsRx) -- By a News Reporter-Staff News Editor at NewsRx Pharma Business Daily -- From Alexandria, Virginia, NewsRx journalists report that a patent by the inventors Phinney, Robin (Okotoks, CA); Phinney, Jonathon (Martensville, CA); Ma, Siu (Edmonton, CA), filed on April 10, 2015, was published online on August 12, 2019.

The patent’s assignee for patent number 10,364,156 is Karnalyte Resources Inc. (Saskatoon, Canada).

News editors obtained the following quote from the background information supplied by the inventors: “Magnesium oxide and hydromagnesite compounds have many uses and find way into a number of products. Magnesium oxide (MgO) is commonly used in refractory, agricultural, chemical, construction, environmental, and other industrial applications. MgO is used as an insulator in industrial cables, as a basic refractory material for crucibles and as a principal fireproofing ingredient in construction materials. It is used as a reference white color in colorimetry, owing to its good diffusing and reflectivity properties. It is used extensively in heating as a component of tubular construction heating elements. The extensive use is due to its high dielectric strength and average thermal conductivity. MgO doping has been shown to effectively inhibit grain growth in ceramics and improve their fracture toughness by transforming the mechanism of crack growth at nanoscale

“In medicine, magnesium oxide is used as an antacid, magnesium supplement, and as a short-term laxative. It is also used to improve symptoms of indigestion. U.S Publication No. 20130059151 discloses use of magnesium oxide for pharmaceutical use wherein magnesium oxide when mixed with a drug that is unstable in acid, demonstrates high stabilizing effects on the drug while also demonstrating superior stability of the magnesium oxide per se.

“Hydromagnesite is used in the paper, rubber and plastics industries for various purposes such as coatings, fillers, extenders and pigments for papermaking as well as flame-retardants in electrical wires and cables but also to impart resistance to chemicals in fibers. For example, EP 0 543 262, EP 0 393 813, JP 21 50 436, JP 22 55 843, JP 51 70 984, JP 50 98 085 and KR 2003/0040953 describe flame-retardant compositions comprising hydromagnesite in admixture with other magnesium compounds such as huntite, dolomite and/or magnesium hydroxide.

“Hydromagnesite in combination with other magnesium compounds is used in the paper industries in order to impart printability, a high brightness at high opacity, also suitable smoothness and gloss to paper products such as magazines. In this respect, JP 2003/293291 describes coated paper produced by disposing an adhesive and a coating layer consisting mainly of at least one of huntite and hydromagnesite on base paper, wherein the resulting coated paper has high brightness, a high surface-masking effect and excellent printing suitability.

“For these compounds, it is important to have a high yield, high purity and superior brightness to enable use in a multitude of industries at a lower cost than existing compounds. In one particular instance, if the quality of the hydromagnesite is high enough, it can be used to replace expensive pigments like titanium oxide.

“European application 1984300 discloses a process for preparation of magnesium oxide from the reaction of magnesium salt and alkali/lime. The crude Mg(OH).sub.2 is directly calcined and then treated with water to disintegrate the mass spontaneously to yield a slurry and dissolve away the soluble salts.

“U.S. Pat. No. 4,720,375 discloses a process for preparing magnesium oxide by calcining a magnesium ore to obtain magnesium oxide and thereafter leaching at least some of the magnesium oxide with ammonium chloride solution in a recovery stage in order to obtain ammonia and magnesium chloride in solution. Thereafter, the magnesium chloride solution is treated in a precipitation stage in order to precipitate magnesium carbonate trihydrate from the solution while forming ammonium chloride for delivery to the recovery stage and the obtained magnesium carbonate trihydrate is filtered, washed, dried and calcined in order to obtain magnesium oxide of high purity.

“Besides the natural hydromagnesite, synthetic hydromagnesite (or precipitated magnesium carbonates) can be prepared. For example, U.S. Pat. Nos. 1,361,324, 935,418, GB 548,197 and GB 544,907 generally describe the formation of aqueous solutions of magnesium bicarbonate (typically described as ‘Mg(HCO.sub.3).sub.2’), which is then transformed by the action of a base, e.g., magnesium hydroxide, to form hydromagnesite.

“U.S. Pat. No. 1,163,475 discloses a process for the preparation of basic magnesium carbonate, which comprises treating a magnesium salt solution with ammonium carbonate, while ensuring that in the precipitating medium at least 20% but not more than 85% of ammonia is neutralized by carbonic acid, and that in the reaction mixture there is always an excess of ammonia in comparison to magnesium, and not more than 63 parts by weight of carbonic acid to 24 parts by weight of magnesium. The formed carbonate is extremely voluminous containing more than 50% of water of crystallization, confirming that the formed basic magnesium carbonate is other than hydromagnesite, wherein water is about 15% of the total weight of the compound.

“U.S. Pat. No. 5,979,461 discloses a process to prepare compositions containing both, hydromagnesite and magnesium hydroxide, wherein magnesium hydroxide is mixed with water to form a suspension which is further contacted with carbon dioxide and an aqueous basic solution to form the corresponding mixture.

“U.S. Pat. No. 8,551,428 discloses a process of preparing hydromagnesite, which comprises a) providing at least one magnesium oxide source, such as magnesium oxide, magnesite, dolomite, huntite, magnesium carbonate, magnesium hydroxide, brucite and mixtures thereof; b) providing gaseous CO.sub.2 and/or carbonate-comprising anions; c) slaking of said magnesium oxide source of step a) to convert the magnesium oxide at least partially into magnesium hydroxide; d) contacting the obtained magnesium hydroxide of step c) with said gaseous CO.sub.2 and/or carbonate-comprising anions of step b) to convert the magnesium hydroxide at least partially into precipitated nesquehonite; and e) treating the obtained precipitated nesquehonite of step d) in a heat-ageing step.

“There is still a need in the art for providing alternative processes for preparing high quality hydromagnesite and magnesium oxide with high levels of purity and brightness. The greater the purity of the magnesium products, the higher the value and suitability for various industries which require very high purity chemicals, such as pharmaceutical industry.”

As a supplement to the background information on this patent, NewsRx correspondents also obtained the inventors’ summary information for this patent: “One object of the present invention is to provide an improved process and method for producing high purity hydromagnesite and/or magnesium oxide compounds.

“In accordance with an aspect of the present invention, there is provided a process for preparing hydromagnesite from a source of magnesium chloride, comprising: preparing a feedstock magnesium chloride brine solution from said source of magnesium chloride, wherein said feedstock brine solution also comprises calcium chloride, mixing a sulfate salt into said feedstock brine solution to convert said calcium chloride into a calcium sulfate precipitate; removing said calcium sulfate precipitate from said brine solution, ammoniating said brine solution obtained after removal of calcium sulfate, at a temperature range of about 20.degree. C. to about 60.degree. C. to convert magnesium chloride at least partially into magnesium hydroxide and to form ammonium chloride, and carbonating said magnesium hydroxide while maintaining the reaction temperature at about 20.degree. C. to about 120.degree. C. to form a hydromagnesite precipitate.

“In accordance with another aspect of the present invention, there is provided a process for preparing hydromagnesite from a source of magnesium chloride, comprising: preparing a magnesium chloride brine solution from said source of magnesium chloride, wherein the concentration of said brine solution is up to about 35% by weight of magnesium chloride, ammoniating said brine solution at a temperature range of about 20.degree. C. to about 60.degree. C. to convert magnesium chloride at least partially into magnesium hydroxide, carbonating said magnesium hydroxide while maintaining the reaction temperature at about 20.degree. C. to about 120.degree. C. to form a hydromagnesite precipitate.

“In accordance with another aspect of the present invention, there is provided a process for preparing a magnesium oxide product, comprising calcining the dried hydromagnesite precipitate obtained according to the process of the present invention to form the magnesium oxide product.

“In accordance with another aspect of the present invention, there is provided a hydromagnesite product formed in accordance with the process defined in the present invention.

“In accordance with another aspect of the present invention, there is provided a magnesium oxide product formed in accordance with the process defined in the present invention.

“It has been found that by observing certain temperatures together with stirring and settling times that high quality products can be synthesized.”

The claims supplied by the inventors are:

“We claim:

“1. A method of preparing hydromagnesite from a source of magnesium chloride, comprising: a) preparing a first brine solution from said source of magnesium chloride, wherein said first brine solution comprises magnesium chloride and calcium chloride; b) mixing a sulfate salt into said first brine solution capable of converting said calcium chloride into a calcium sulfate precipitate thereby forming said calcium sulfate precipitate and a second brine solution comprising magnesium chloride; c) removing said calcium sulfate precipitate from said second brine solution; d) ammoniating said second brine solution, after step c), at a temperature range of about 20.degree. C. to about 60.degree. C. to convert magnesium chloride at least partially into magnesium hydroxide and to form ammonium chloride; and e) carbonating said magnesium hydroxide while maintaining the reaction temperature at about 20.degree. C. to about 120.degree. C. to form a hydromagnesite precipitate, f) wherein said first brine solution contains from about 25% to about 35% by weight magnesium chloride in water, g) wherein said mixing of said sulfate salt is carried out at a temperature of about 60.degree. C. to about 90.degree. C.

“2. The method of claim 1, wherein said first brine solution has a specific gravity from about 1.2 to about 1.35.

“3. The method of claim 1, further comprising adjusting a magnesium chloride concentration of said second brine solution to be in a range of about 10% to about 20% by weight magnesium chloride in water, after removing calcium sulfate.

“4. The method of claim 1, wherein said carbonation is carried out in multiple steps.

“5. The method of claim 1, wherein said sulfate salt is magnesium sulfate or sodium sulfate, wherein said salt is provided as a solid or solution in water.

“6. The method of claim 1, wherein said step of mixing said sulfate salt is carried out at a temperature of about 80.degree. C.

“7. The method of claim 1, wherein carbon dioxide for said step of carbonating is obtained from calcination of limestone, wherein CaO is produced along with said carbon dioxide.

“8. The method of claim 7, further comprising treating said CaO with said ammonium chloride to form ammonia gas and recycling said ammonia gas to the step of ammoniating.

“9. The method of claim 1, wherein said second brine solution further comprises water soluble impurities, said method further comprising the step of washing said hydromagnesite precipitate to remove said water soluble impurities.

“10. The method of claim 9, wherein said water soluble impurities comprise at least one of sodium chloride or potassium chloride.

“11. The method of claim 9, wherein said step of washing includes the step re-slurring said hydromagnesite precipitate to form an about 50% slurry in water.

“12. The method of claim 11, wherein said step of re-slurring is conducted at a temperature of between about 50.degree. C. and about 100.degree. C.

“13. The method of claim 9, further comprising the step of drying said hydromagnesite precipitate after washing to produce a dried hydromagnesite precipitate.

“14. The method of claim 13, wherein said step of drying is carried out at a temperature of about 100.degree. C. to about 150.degree. C.

“15. The method of claim 14, wherein said hydromagnesite precipitate has a purity of at least about 99%.

“16. The method of claim 1, wherein said hydromagnesite precipitate comprises particles having an average particle size from about 20 microns to about 50 microns.

“17. The method of claim 1, wherein said first brine solution contains from about 27% to about 35% by weight magnesium chloride in water.”

For additional information on this patent, see: Phinney, Robin; Phinney, Jonathon; Ma, Siu. Process For Producing High Grade Hydromagnesite And Magnesium Oxide. U.S. Patent Number 10,364,156, filed April 10, 2015, and published online on August 12, 2019. Patent URL: http://patft.uspto.gov/netacgi/nph-Parser?Sect1=PTO1&Sect2=HITOFF&d=PALL&p=1&u=%2Fnetahtml%2FPTO%2Fsrchnum.htm&r=1&f=G&l=50&s1=10,364,156.PN.&OS=PN/10,364,156RS=PN/10,364,156

(Our reports deliver fact-based news of research and discoveries from around the world.)

Copyright © 2019 NewsRx LLC, NewsRx Pharma Business Daily, source Health Newsletters

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