Desorption of volatile compounds dissolved in a liquid phase
First Claim
1. A method of desorption of volatile compounds from an aqueous liquid containing ammonia, by means of a stripping column, comprising the steps of supplying the aqueous liquid to the upper part of the column, blowing a gaseous mixture including free oxygen into the lower part of the column, supplying at least one of sodium hydroxide and calcium hydroxide to an intermediate part of the column at a plurality of levels, withdrawing a gaseous mixture including ammonia from the top of the column, measuring the pH and the temperature of the aqueous liquid at a plurality of levels in the column, controlling the flow rate of the aqueous liquid and the flow rate and temperature of the gaseous mixture blown in and of the hydroxide so that the pH of the aqueous liquid, at least in a predetermined zone in the column, is at least 11 and, subsequently reacting the ammonia content and oxygen content of the withdrawn gaseous mixture, the amount of oxygen in the gaseous mixture blown in being controlled so that substantially only water and nitrogen are produced.
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Abstract
Volatile compounds are desorbed from an aqueous liquid containing ammonia, by means of a stripping column. The aqueous liquid is supplied to the upper part of the column and a gaseous mixture including free oxygen is blown into the lower part of the column. Sodium hydroxide and/or calcium hydroxide is supplied to an intermediate part of the column at a plurality of levels. A gaseous mixture including ammonia is withdrawn from the top of the column. The pH and the temperature of the aqueous liquid are measured at a plurality of levels in the column. The flow rate of the aqueous liquid and the flow rate and temperature of the gaseous mixture blown in and of the hydroxide are controlled so that the pH of the aqueous liquid, at least in a predetermined zone of the column, is at least 11.
7 Citations
6 Claims
- 1. A method of desorption of volatile compounds from an aqueous liquid containing ammonia, by means of a stripping column, comprising the steps of supplying the aqueous liquid to the upper part of the column, blowing a gaseous mixture including free oxygen into the lower part of the column, supplying at least one of sodium hydroxide and calcium hydroxide to an intermediate part of the column at a plurality of levels, withdrawing a gaseous mixture including ammonia from the top of the column, measuring the pH and the temperature of the aqueous liquid at a plurality of levels in the column, controlling the flow rate of the aqueous liquid and the flow rate and temperature of the gaseous mixture blown in and of the hydroxide so that the pH of the aqueous liquid, at least in a predetermined zone in the column, is at least 11 and, subsequently reacting the ammonia content and oxygen content of the withdrawn gaseous mixture, the amount of oxygen in the gaseous mixture blown in being controlled so that substantially only water and nitrogen are produced.
Specification
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- Resources
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Current AssigneeCentre de Recherches Metallurgiques- Centrum VOOR Research In The Metallurgie ASBL
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Original AssigneeCentre de Recherches Metallurgiques- Centrum VOOR Research In The Metallurgie ASBL
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InventorsJosis, Christian Rubens
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Primary Examiner(s)Spear, Jr., Frank A.
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Assistant Examiner(s)Burks, Richard W.
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Application NumberUS05/696,175Time in Patent Office777 DaysField of Search55/46, 55/19, 55/20, 55/52, 55/53, 55/70, 55/160, 55/196, 55/202, 423/356US Class Current95/9CPC Class CodesB01D 19/00 Degasification of liquidsB01D 19/0005 with one or more auxiliary ...B01D 3/18 with horizontal bubble platesB01D 3/32 Other features of fractiona...B01D 3/34 with one or more auxiliary ...B01D 53/14 by absorptionB01D 53/18 Absorbing units; Liquid dis...C02F 1/20 by degassing, i.e. liberati...C02F 1/586 by removing ammoniacal nitr...C02F 2101/16 Nitrogen compounds, e.g. am...C10K 1/08 by washing with liquids; Re...C10K 1/12 alkaline-reacting including...
