Methods and systems for controlling condensate when reducing oxygen content in biogas
US-2024001297-A1 · Jan 4, 2024 · US
US2016158696A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016158696-A1 |
| Application number | US-201414901548-A |
| Country | US |
| Kind code | A1 |
| Filing date | May 26, 2014 |
| Priority date | Jun 27, 2013 |
| Publication date | Jun 9, 2016 |
| Grant date | — |
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.
A treatment process of PF 5 including an absorption step for inducing absorption of PF 5 by an acidic solution containing an acid to obtain a solution containing PF 5 A − , an adjustment step to adjust concentration of HCl in the solution, and a thermolysis step for heating the solution containing PF 5 A − ions obtained in the absorption step or the adjustment step to decompose the solution to an acidic mixture containing H 3 PO 4 and HF.
Opening claim text (preview).
1 . A treatment process of PF 5 comprising: an absorption step for inducing absorption of PF 5 by an acidic solution containing at least one acid selected from hydrogen fluoride (HF), hydrogen chloride (HCl), hydrogen bromide (HBr), hydrogen iodide (HI), phosphoric acid (H 3 PO 4 ), and fluorophosphoric acid compound (H 2 PO 3 F or HPO 2 F 2 ) to obtain a solution containing PF 5 A − which is an ion composed of an acid-based anion A − selected from F, Cl − , Br − , I − , H 2 PO 4 − , HPO 3 F − , and PO 2 F 2 − combined with PF 5 ; and a thermolysis step for heating the solution obtained in the absorption step to 35° C. or higher and 75° C. or lower for 2 to 96 hours to decompose PF 5 A − in the solution to form an acidic mixture containing at least one of F and PO 4 3− . 2 . A treatment process of PF 5 comprising: an absorption step for inducing absorption of PF 5 by an acidic solution containing at least one acid selected from hydrogen fluoride (HF), hydrogen chloride (HCl), hydrogen bromide (HBr), hydrogen iodide (HI), phosphoric acid (H 3 PO 4 ), and fluorophosphoric acid compound (H 2 PO 3 F or HPO 2 F 2 ) to obtain a solution containing PF 5 A − which is an ion composed of an acid-based anion A − selected from F − , Cl − , Br − , I − , H 2 PO 4 − , HPO 3 F − , and PO 2 F 2 − combined with PF 5 ; an adjustment step for blowing in a gas containing 1 to 100 vol % of hydrogen chloride (HCl), or adding hydrochloric acid of a concentration of 1 to 36 wt % to the solution obtained in the absorption step to adjust concentration of HCl in the solution to 1 to 36 wt %; and a thermolysis step for heating the solution obtained in the adjustment step to 35° C. or higher and 75° C. or lower to decompose the solution. 3 . The treatment process according to claim 1 , wherein a concentration of PF 5 to be absorbed in the acidic solution in the absorption step is 0.00001 vol % (0.1 ppm) or higher and lower than 20 vol % (200,000 ppm). 4 . The treatment process according to claim 1 , wherein the acidic solution to be used in the absorption step contains 1 molar equivalent or higher of acid against an amount of PF 5 to be absorbed. 5 . (canceled) 6 . The process according to claim 2 , wherein the thermolysis step comprises heating the solution obtained in the adjustment step for 2 to 96 hours to decompose PF 5 A − in the solution to form an acidic mixture containing at least one of F and PO 4 3− . 7 . The treatment process according to claim 2 , wherein a concentration of PF 5 to be absorbed in the acidic solution in the absorption step is 0.00001 vol % (0.1 ppm) or higher and lower than 20 vol % (200,000 ppm). 8 . The treatment process according to claim 2 , wherein the acidic solution to be used in the absorption step contains 1 molar equivalent or higher of acid against an amount of PF 5 to be absorbed.
Fluorine or fluorine-containing compounds · CPC title
Halogens or halogen compounds · CPC title
by neutralisation; pH adjustment (for degassing C02F1/20; using ion-exchange C02F1/42; for flocculation or precipitation of suspended impurities C02F1/52; for removing dissolved compounds C02F1/58) · CPC title
by reduction {(C02F1/4676 takes precedence)} · CPC title
Thermal hydrolysis · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.