The present invention is directed to a method and a system for solvent purification. Synthetic and organo-metallic chemistry for example requires very high purity solvents. More specifically, synthetic chemistry requires solvents which are nearly deplete of oxygen and moisture content. Organo-metallic chemistry requires solvents which even have a higher purity as to moisture content. In other words, the solvent needs to be “dry” before it can be used.
A traditional method for purifying or “drying out” solvents is thermal distillation. Because solvents are very volatile, thermal distillation presents a significant fire and explosion hazard. In addition, it is a very inefficient method for drying out the solvent. Typically, distillation involves use of a suitable drying agent. A typical drying agent may be Li, Na, K, CaH2, and LiAlH4. These drying agents are highly reactive and as such, are quite dangerous. Over the years, there have been many fires and explosions involving thermal distillations of solvents. Chemists characterize thermal distillation as one of the most dangerous routine procedures they perform. Moreover, the maintenance of distillation equipment and the quenching of the drying agents are very laborious.
Another purification method uses the so-called “Grubbs apparatus” which uses a very large solvent reservoir and alumina/catalyst columns to dry and de-oxygenate solvents to a desired level of purity, without using heat or water reactive drying agents. The Grubbs apparatus takes up a lot of laboratory and research space. The system uses a large storage drum holding 15-20 liters of solvent and purification columns or cylinders that are typically over 30 inches tall and have a diameter greater than 3 inches. Multiple columns are used and are connected in series. Each of the columns contains an activated filter media that removes contaminants from a solvent as it passes through the column. The solvent is passed only once through the columns to get filtered. By the time the solvent reaches the end of the last column, the solvent is sufficiently filtered.
Filling of the drum reservoir with a solvent typically occurs under a fume hood for the purpose of evacuating all hazardous solvent fumes. Solvents may be provided in 4 liter containers. Thus, multiple containers must be used to fill the drum. Solvents may also be provided in larger containers, as for example 10 or 20 liter containers. Such containers are typically heavy. Moreover, it may be difficult or impossible to empty such containers into the drum reservoir while under a fume hood.
Furthermore, after use, each of the long columns must be regenerated, i.e., the contaminants which had been filtered out from the solvent must be removed from the columns. This may be quite difficult as the cylinders are long. The problem with the Grubb system is that it is not portable and, due to its size, it is confined to the space upon where the system is housed.
Moreover, the current systems typically can not be used to purify a small volume of solvent as the small volume of solvent would be taken up by the filtering media. In other words, a substantial volume of the solvent will wet the filtering media and will not be filtered. Thus, large volumes of solvent, as for example four liters or more, are required for being filtered with current systems. This may be undesirable in cases where only a very small amount of solvent is required for the task at hand.
In an exemplary embodiment, a solvent filtering system is provided including a housing, a filtering media within the housing, an inlet for receiving a solvent, and a mechanism for moving the housing, causing the solvent to travel through the filtering media in order to filter the solvent. In one exemplary embodiment, the housing is seesawed about a pivot axis. In another exemplary embodiment, the housing is rotated about a pivot axis. In yet another exemplary embodiment, the housing defines a loop and the housing is rotated about the pivot axis, causing the solvent to travel through the filtering media. In a further exemplary embodiment, the housing defines a generally rectangular loop. In yet a further exemplary embodiment, the housing defines a generally circular loop. In another exemplary embodiment, the housing is tubular. In one exemplary embodiment, the filtering media occupies a section of the housing. In another exemplary embodiment, the filtering media includes a moisture removing media. In yet another exemplary embodiment, the filtering media includes an oxygen removing media. In a further exemplary embodiment, the system is capable of filtering 50 ml or less of solvent.
In another exemplary embodiment, a method for filtering a solvent is provided. The method includes introducing a solvent into a housing including a filtering media, and moving the housing, causing the solvent to repeatedly flow through the filtering media. In a further exemplary embodiment, moving includes rocking the housing about an axis. In yet another exemplary embodiment, moving includes rotating the housing about an axis. In yet a further exemplary embodiment, the housing is tubular. In one exemplary embodiment, the housing is generally rectangular. In yet another exemplary embodiment, the housing is generally circular. In a further exemplary embodiment, moving the housing includes moving the housing for a pre-determined amount of time for obtaining a desired level of solvent purity. In yet another exemplary embodiment, the filtering media includes a moisture removing media. In a further exemplary embodiment, the filtering media includes an oxygen removing media. In yet a further exemplary embodiment, the method also includes introducing 50 ml or less of solvent.
In a further exemplary embodiment, a solvent filtering system is provided including a housing, a filtering media within the housing, an inlet for receiving a solvent, and a mechanism for moving the filtering media relative to the housing, causing the solvent to travel through the filtering media in order to filter the solvent. In yet a further exemplary embodiment, the filtering media includes a moisture removing media. In another exemplary embodiment, the filtering media includes an oxygen removing media. In yet another exemplary embodiment, the system is capable of filtering 50 ml or less of solvent.
In one exemplary embodiment, a method for filtering a solvent is provided including introducing a solvent into a housing including a filtering media, and moving the filtering media within the housing, causing the solvent to repeatedly flow through the filtering media. In another exemplary embodiment, moving the filtering media includes moving the filtering media for a pre-determined amount of time in order to obtain a desired level of solvent purity. In yet another exemplary embodiment, the filtering media includes a moisture removing media. In a further exemplary embodiment, the filtering media includes an oxygen removing media. In yet a further exemplary embodiment, the method includes introducing 50 ml or less of solvent.
Each of the aforementioned embodiment systems and methods can filter the solvent without incorporating a pump for pumping the solvent, causing it to travel through the filtering medium. In another exemplary embodiment, a method for filtering solvent is provided. The method includes introducing a solvent into a housing including a filtering media, and repeatedly moving the solvent relative to a filtering media without pumping the solvent through the filtering media.
The system of the present invention may be made small enough for filtering four or less liters of solvent. In one exemplary embodiment, the system includes a filter housing, referred to herein as a “capsule” for convenience, which is small enough to filter less than one liter of solvent. For example, the capsule may be made small enough to filter 20 to 30 milliliters of solvent. Such a small volume of solvent can not be filtered with the conventional systems as the small volume of solvent would be just enough to wet the filtering media such that only a small or no amount of solvent will pass through the filtering media.
In one exemplary embodiment, as shown in
In another exemplary embodiment, the capsule may be continuously rotated (instead of seesawing back and forth) about the pivot axis 16. Rotation of the capsule is maintained for an amount of time to obtain a desired level of solvent purity.
In another exemplary embodiment, as shown in
In yet another exemplary embodiment as shown in
In each of the above-identified embodiments, the filtering media may be placed in a single location within the capsule, or in more than one locations, as for example shown in
In another exemplary embodiment as shown in
In one exemplary embodiment, the filtering media is a media that removes moisture from the solvent. An exemplary media is Molecular Sieve. An exemplary Molecular Sieve is marketed under the trademark MOLSIV® which is registered to UOP, A Honeywell Company.
The movement of the capsules or filtering media is caused by a mechanism which is not shown. The mechanism may include a motor for moving the capsule. In another exemplary embodiment, the mechanism may be manually operated. Furthermore, the capsules may be made very small, as for example to only handle about 50 milliliters or less of solvent. In other exemplary embodiments, the system may have a sufficient size for filtering up to four liters of solvent or even more than four liters of solvent. These systems provide an advantage in that multiple systems may be placed in a fume hood and moved or rotated for a desired amount of time to obtain a desired level of solvent purity. As can be seen with these embodiments, a pump is not required to pump the solvent through the filtering media. Rather, the fluid is moved through the media by movement of the filter capsule or housing itself or by movement of the filtering media relative to the housing.
The exemplary embodiment system may be made small enough for incorporation into a fume hood. For example, with the embodiment shown in
With the exemplary systems, the solvent may be filtered to a desired level of moisture by circulating the filter capsules, or by seesawing the filter capsules, or by moving the filtering media relative to the capsule for a period of time or for an amount of revolutions or strokes to obtain the desired purity. The desired purity may be measured by removing the solvent by using well known methods or techniques and measuring its purity. For given solvents of a given volume and using a given filtering media, the amount of time or circulation may be predetermined. In addition, an oxygen removing filtering media may also be incorporated into the capsules for removing oxygen from the solvent. Moreover, in other exemplary embodiments, the inventive system may be used to filter solvents that are used in fields other than organo-metallic chemistry. In yet a further exemplary embodiment, the filtering media may be any filtering media for removing any undesired component from the solvent. In other exemplary embodiments, different types of filtering media for removing the same or different types of components from the solvent may be placed at different locations in the capsule or at the same location in the capsule or may be mixed together prior to placing in the capsule.
Although the present invention has been described and illustrated with respect to exemplary embodiments, it is to be understood that it is not to be so limited, since changes and modifications may be made therein which are within the full intended scope of this invention as hereinafter claimed.
This application is based upon and claims priority on U.S. Provisional Patent Application Ser. No. 61/437,465, filed on Jan. 28, 2011, the contents of which are fully incorporated herein by reference.
Number | Date | Country | |
---|---|---|---|
61437465 | Jan 2011 | US |