Stannous oxide powder and method for producing same
US-2020231461-A1 · Jul 23, 2020 · US
US11525187B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11525187-B2 |
| Application number | US-202017433909-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 21, 2020 |
| Priority date | Feb 28, 2019 |
| Publication date | Dec 13, 2022 |
| Grant date | Dec 13, 2022 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
The present invention provides a high-concentration tin sulfonate aqueous solution, in which a divalent tin ion (Sn 2+ ) concentration is 360 g/L to 420 g/L, a tetravalent tin ion (Sn 4+ ) concentration is 10 g/L or less, a free methanesulfonic acid concentration is 40 g/L or less, a Hazen unit color number (APHA) is 240 or less, and a turbidity is 25 FTU or less. This aqueous solution is produced such that stannous oxide powder whose temperature is adjusted to a temperature of 10° C. or lower is added to an aqueous methanesulfonic acid solution having a concentration of 60% by mass to 90% by mass when the aqueous solution circulates in a state of being maintained at the temperature of 10° C. or lower, and the stannous oxide powder is dissolved.
Opening claim text (preview).
What is claimed is: 1. A method for producing a high-concentration tin sulfonate aqueous solution the method comprising: a step of diluting methanesulfonic acid with pure water to obtain an aqueous methanesulfonic acid solution having a concentration of 60% by mass to 90% by mass; a step of causing the aqueous methanesulfonic acid solution to circulate in a state of being maintained at a temperature of 10° C. or lower; a step of subjecting the aqueous methanesulfonic acid solution and a first stannous oxide powder to a neutralization reaction by adding the first stannous oxide powder whose temperature is adjusted to a temperature of 10° C. or lower to the circulating aqueous methanesulfonic acid solution and dissolving the first stannous oxide powder; and a step of adding a second stannous oxide powder and pure water to adjust a concentration of Sn 2+ in a range of 360 g/L to 420 g/L. 2. The method for producing a high-concentration tin sulfonate aqueous solution according to claim 1 , wherein the circulating aqueous methanesulfonic acid solution is bubbled with nitrogen gas and/or degassed with a hollow fiber membrane degassing module. 3. The method for producing a high-concentration tin sulfonate aqueous solution according to claim 1 , wherein the stannous oxide powder contains impurities of a plurality of metals, and a total content of the plurality of kinds of metals is 30 mg/L or less in terms of metal. 4. The method for producing a high-concentration tin sulfonate aqueous solution according to claim 3 , wherein the plurality of metals includes sodium, potassium, lead, iron, nickel, copper, zinc, arsenic, antimony, aluminum, silver, bismuth, magnesium, calcium, titanium, chromium, manganese, cobalt, indium, tungsten, thallium, and cadmium. 5. The method for producing a high-concentration tin sulfonate aqueous solution according to claim 3 , wherein a content of each of the plurality of metals is 10 mg/L or less in terms of metal. 6. The method for producing a high-concentration tin sulfonate aqueous solution according to claim 1 , wherein the first stannous oxide powder contains chloride ions, and a content of the chloride ions is 10 mg/L or less. 7. The method for producing a high-concentration tin sulfonate aqueous solution according to claim 1 , wherein the high-concentration tin sulfonate aqueous solution contains: a divalent tin ion (Sn 2+ ) concentration is 360 g/L to 420 g/L, a tetravalent tin ion (Sn 4+ ) concentration is 10 g/L or less, a free methanesulfonic acid concentration is 40 g/L or less, a Hazen unit color number (APHA) is 240 or less, and a turbidity is 25 FTU or less.
Related publications grouped by family.
Answers are generated from the same data shown on this page.