Liquid purification or separation – Particulate material type separator – e.g. – ion exchange or... – Spaced beds
Reexamination Certificate
1999-03-22
2001-04-10
Langel, Wayne (Department: 1754)
Liquid purification or separation
Particulate material type separator, e.g., ion exchange or...
Spaced beds
Reexamination Certificate
active
06214225
ABSTRACT:
BACKGROUND OF THE INVENTION
1. Field of the Invention
This invention relates to a process for the preparation of an ultra pure hydrogren peroxide solution, and to a plant for the implementation of the process.
2. Description of the Related Art
The use of hydrogen peroxide for advanced technology applications or applications in the food industry, in hygiene or health requires increasingly pure products which must meet a growing number of increasingly tight specifications. In particular, the demands of users are turning towards hydrogen peroxide solutions in which the content of each metal impurity is less than one part per billion (ppb) and preferably less than 100 parts per trillion (ppt). In the following account, such solutions will be known as ultrapure hydrogen peroxide solutions.
It is well known, according to the prior art, that it is possible to remove certain impurities by passing the solution through a bed of ion-exchange adsorbents. Mention may be made, for example, of functionalized polymers of polystyrene/divinylbenzene type, silicas or aluminosilicates, in particular the varieties containing controlled micropores, such as zeolites, or active charcoals; these solids carry functional groups capable of complexing either cations or anions. Mention may be made, as examples of functional groups capable of complexing cations, of the carboxylic, sulphonic, phosphonic, hydroxide, amine oxide or phosphine oxide groups or alternatively of cyclic or open polyoxaalkyls, such as, for example, ethylene oxide polymers. Mention may be made, as examples of functional groups capable of complexing anions, of the quaternary ammonium or quaternary phosphonium groups. These adsorbents can also be obtained by polymerization of a monomer carrying a functional group, for example poly(methacrylic acid)s, poly(vinylphosphonic acid)s, polyvinylpyridines, polyvinylpyrrolidones, poly(vinyl alcohol)s, saponified polylactones and copolymers containing these units. The adsorbents which are the most often described are polystyrene gels or crosslinked polystyrenes possessing sulphonic —SO
3
H or trimethylammonium (CH
3
)
3
N
+
— functional groups.
Many combinations have been provided, such as, for example, anionic resin followed by cationic resin or cationic resin followed by anionic resin or alternatively anionic resin followed cationic resin followed by cationic+anionic “mixed bed”. Additions to the inter-stage phases are also described, such as, for example, the addition of acid in order to modify the pH or the addition of chelating agents, such as aminomethylenecarboxylic or aminomethylenephosphonic derivatives.
It is well known to the person skilled in the art that the use of anion-exchange adsorbents presents great difficulties when employed for the purification of hydrogen peroxide. In particular, the hydroxide form, under which these products are generally available industrially, cannot be used directly because of its excessively high basicity, resulting in significant decomposition of hydrogen peroxide. Many publications describe the use of adsorbents exchanged by carbonate or bicarbonate ions, which are less basic, in order to limit the decomposition of hydrogen peroxide, without, however, eliminating it completely.
It is essential to be able to control this phenomenon of decomposition of hydrogen peroxide on adsorbent beds because, as this decomposition with release of gaseous oxygen is exothermic, the rate is accelerated according to the well known Arhenius law. The formation of a gas pocket can further aggravate the phenomenon since, by separating the liquid from the decomposition point, the heat released can no longer be removed by evaporation of the water and the cooling effect of the liquid is lost. Such a process is characteristic of a divergent reaction which can result in an extremely violent autoaccelerated decomposition reaction, which is all the more dangerous since it is highly exothermic and produces gaseous oxygen, thus with a considerable expansion force which can cause explosions.
SUMMARY OF THE INVENTION
The present invention relates to a process for the purification of an ultrapure hydrogen peroxide solution, characterized in that it comprises at least one sequence which includes successively passing the said solution through at least four beds of cation-exchange adsorbents (CEA) and of anion-exchange adsorbents (AEA) according to the sequence:
AEA→CEA→AEA→CEA.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS OF THE INVENTION
The hydrogen peroxide solution to be purified according to the present invention, originating from a technical solution, has a concentration of 1 to 70% by weight and preferably of 5 to 50% by weight. The adsorbents are chosen from those which are described above.
The beds of adsorbents exhibit a height/diameter ratio of between 0.5 and 100, in particular between 1 and 50. In a first preferred alternative form, the subject of the present invention is the process as defined above in which the beds of adsorbents each exhibit a height to diameter ratio of greater than 3 and in particular of between 5 and 10 and, more particularly, of approximately 6.
The anion-exchange adsorbents are preferably fed in an upward mode, whereas the cation-exchange adsorbents are preferably fed in a downward mode. However, it is also possible to operate in a completely gravitational mode in which all the beds operate in an upward mode.
The hydrogen peroxide solution throughputs, expressed as volume of solution/hour passed per volume of bed of adsorbent, generally vary between 0.5 and 100, preferably from 1 to 50 and more particularly from 10 to 30.
It is possible to define the geometries of the beds so that the true space velocities and/or throughputs in each adsorbent are optimized. In a specific configuration, a high space velocity is applied during the passage of the solution in the first sub-sequence AEA→CEA and a low space velocity during the passage in the second sub-sequence AEA→CEA.
It is also possible to operate under pressure; a working pressure of less than 5 atm above atmospheric pressure will preferably be chosen.
The temperature of the solution to be purified according to the process as described above is less than or equal to 30° C. and preferably between −10° C. and +10° C.
In an alternative form of the process as defined above, it comprises, upstream or downstream of sequences for passing the solution to be purified through the beds of ion-exchange adsorbents, one or more purification stages, such as, for example, distillation, liquid extraction, crystallization, absorption, filtration, ultrafiltration, nanofiltration or reverse osmosis. If appropriate, the starting solution is brought beforehand to the desired assay and then purified.
Depending on the degree of purity and of dilution of the hydrogen peroxide solution to be purified, one or more of these additional stages is/are employed.
In a second preferred variant of the present invention, the technical hydrogen peroxide solution to be purified, which is at a concentration of 30% to 70% by weight, is distilled and brought to the desired assay beforehand and then purified according to the sequence which is the subject of the present invention.
According to a third alternative form of the purification process which is the subject of the present invention, a hydrogen peroxide solution of technical quality or of so-called “food” quality, having a concentration of approximately 50 to 70% by weight, is subjected to the following pretreatment: a first distillation/concentration stage, in order to obtain a condensate having a concentration of greater than 80%, plus a first purification by low-temperature crystallization and the removal of the supernatant. The crystals collected are washed, superficially dried and then melted and the solution obtained is diluted to 30 or 35% with deionized water of ultrapure electronic quality. After the said pretreatment, the resulting solution is purified using the sequence which is the subject of the present invention.
Another
Carre Martine
Demay Didier
Devos Christine
Jeanin Serge
Ledon Henry
Burns Doane Swecker & Mathis L.L.P.
L'Air Liquide, Societe Anonyme pour l'Etude et l'
Langel Wayne
LandOfFree
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