Patent Application
20130287655
This invention relates to an apparatus and method for removing mercury or mercury containing compounds from fluids, e.g., liquids, gases and gaseous condensates. More particularly, it relates to the use of porous membranes and scrubbing solutions which, when used in tandem, remove mercury from the aforementioned fluids.
Mercury (Hg), is a contaminant of many natural products, including hydrocarbon fuels. It exists in many forms such as elemental mercury. Organic and inorganic compounds also contain it. In the case of the hydrocarbon fuels mentioned herein, mercury is believed to have originated from geologic deposits from which the fuels, such as natural gas, have been obtained.
The toxicity of mercury containing compounds, even in extremely small quantities, is very well known. Also of importance is the fact that when elemental mercury is present in industrial materials or natural gas streams, it compromises the safety and integrity of the equipment and piping handling these streams, due to issues of metallurgical chemistry. See, e.g., U.S. Pat. No. 4,880,527 to Audeh, incorporated by reference in its entirety.
Given the dangers and the ubiquity of mercury in industrial production, there is a vast literature on ways to remove the substance from materials containing it. In this regard see, e.g., U.S. Pat. No. 7,476,365 to Al-Faqeer, incorporated by reference. Additional references teaching removal of mercury from materials include U.S. Pat. No. 7,306,774 to DeBerry; U.S. Pat. No. 7,727,307 to Winkler, et al.; U.S. Pat. No. 6,197,269 to Jansen, et al.; U.S. Pat. No. 4,474,896 to Chao, et al.; U.S. Pat. No. 7,381,388 to Cooper, et al.; U.S. Pat. No. 6,872,370 to Cooper, et al.; U.S. Pat. No. 6,491,822 to Alper; U.S. Pat. No. 6,355,092 to Jansen, et al.; WO 2008/116864 to DenBoestert, et al.; and U.S. 2006/0116287 to Durante, et al. All are incorporated by reference herein.
For the most part, these references teach adsorption of contaminants, such as elemental mercury, onto a solid material. None suggests the apparatus or method which constitute features of the invention described herein.
The invention involves a process and apparatus for removal of mercury from a liquid or gaseous stream, such as a feedstream or process stream (the “first stream” hereafter) by passing the substance on one side of a porous membrane, while passing a second stream, e.g., a “scrubbing stream”, which is capable of removing the mercury from the sample, first stream, feedstream, or process stream, on the other side of the membrane. The scrubbing may occur via solubilizing the mercury into the second stream, reacting it with a reactive component in the “scrubbing,” or “second” stream, or both.
Transfer of mercury occurs, essentially, through the pores of the porous membranes. The size of the pores is not critical. Membranes associated with nano-, ultra-, and micro-filtration are all within the ambit of the invention; however, pore size and number (surface porosity) provide a means to control the rate of transfer of mercury across the streams, and the interfacial stability between the first and second stream.
The scrubbing solution, also referred to as “absorbent liquid,” can be any solution capable of solubilizing or reacting with mercury, or performing both tasks. Exemplary of materials which can be included in the solution are alkali metal sulfides, ammonium bisulfide salts, disulfide salts, polysulfide salts (salts which contain Sx, where x>2), hydrogen peroxide, perchlorate, and other materials known to the skilled artisan.
The scrubbing solution may be treated, e.g., to remove solid precipitate, and/or to have relevant chemicals added to replenish the solution, and then be recirculated. Of course, the skilled artisan will recognize that a completely new solution may be used as well.
The invention as described herein provides non-dispersive contact between the two streams, which is a distinct advantage over the conventional, dispersed phase systems now employed, including liquid/liquid extraction, and gas/liquid scrubbing and absorption.
Problems encountered by the art, including solvent holdup, formation of emulsions, foaming, unloading and flooding, are all avoided.
Further, the invention allows for very high packing densities of the membranes, and as a result the units employed are much smaller than the units now seen in industrial practice.
Also, as compared to the state of the art, the membranes are functional in both horizontal and vertical placement, as compared to vertical only, which is an advantage in terms of deployment in standard systems.
Features of the invention will be seen in the disclosure which follows.
The fluids may flow in counter directions, as in this example, or in co-directions.
Mercury transfers from the mercury rich stream to the scrubbing solution stream that is in direct contact with it within the pores of the membrane contactor module 102. Thus, stream “105” will be leaner in mercury, while stream “106” will be richer in mercury.
A second embodiment of the invention is depicted in
The “scrubbing solution treatment zone” 113, may contain additional materials and equipment such as one or more storage tanks for fresh scrubbing solution, scrubbing solution which has been used, and treated to remove the mercury, or used scrubbing solution which is to be either treated, or disposed of Storage tanks may also be provided for each of these. The zone may also include, e.g., means for treating solutions such as mercury containing scrubbing streams so as to filter solids, be these mercury compounds or other solids, sedimentation or segregation units, as well as means for replenishing and/or adjusting the scrubbing solution.
A system as shown in
A hollow fiber membrane module type was built by bundling seven hollow, porous polypropylene fibers and cementing them, with epoxy, into polyethylene tubes and PVC-Y fittings, to form a shell, and inlet/exit ports. Relevant properties of the fibers included an OD of ˜2500 μm, and pore sizes from 2 to 20 μm.
The spiked condensate was then circulated from a condensate reservoir and then back to it, through the lumen side of the hollow fibers. Simultaneously, a polysulfide solution composed of 15.6 wt % of NaOH, 6.3 wt % S8, and 78.1 wt % H2O was circulated from its own reservoir, through the hollow fiber module outside the bores, that is, on the shell side.
Circulation of both liquids was facilitated via calibrated, internally lined gear pumps, with plastic tubing.
Samples were analyzed over time, using standard Cold Vapor Atomic Fluorescence (“CVAF”). As the spiked condensate and polysulfide solutions circulated in the system, they were sampled to track the mercury content in the condensate. The results are presented below, as an average of the multiple analyses for each sample with standard deviation of the analysis.
The following table shows the results for the mass transfer of mercury through the pores of different ultrafiltration membranes obtained from Millipore Company, again using the embodiment of
Other features of the invention will be clear to the skilled artisan and need not be reiterated here.
The terms and expression which have been employed are used as terms of description and not of limitation, and there is no intention in the use of such terms and expression of excluding any equivalents of the features shown and described or portions thereof, it being recognized that various modifications are possible within the scope of the invention.
This application claims priority from U.S. Provisional Application No. 61/614,209 filed Mar. 22, 2012, incorporated by reference in its entirety.
| Number | Date | Country | |
|---|---|---|---|
| 61614209 | Mar 2012 | US |
