Patent Application
20150060334
The technical field generally relates to methods and apparatuses for processing hydrocarbon streams containing organic nitrogen species, and more particularly relates to methods and apparatuses for removing organic nitrogen species from hydrocarbon streams.
When extracted, crude oil may contain a number of undesired compounds or contaminants, such as sulfur compounds. Reduction in the amount of sulfur compounds in automotive fuels and other refined hydrocarbons is typically required in order to meet environmental concerns and governmental regulations. Further, sulfur compounds often adversely impact refinery operations, e.g., by poisoning catalysts. In many hydrocarbon processing schemes, sulfur is removed from the hydrocarbon feedstock by catalytic hydrodesulfurization in hydrotreating process units.
Crude oils also may contain various organic nitrogen species in quantities that impact the refinery processing of the crude oils fractions. Specifically, the presence of organic nitrogen species in the hydrocarbon feedstock may suppress the hydrodesulfurization function of hydrotreating catalysts and require relatively higher operating pressure. This suppression is particularly troublesome for older hydrotreating process units that have relatively lower limits on operating pressure. As a result, older hydrotreating process units cannot process hydrocarbon streams having relatively high organic nitrogen species content, such as cracked feedstocks.
Hydrodesulfurization suppression is also problematic for selective hydrotreating processes that are inherently constrained by low operating pressure. For example, processes for forming high octane product streams require relative lower operating pressures during hydrotreating. Therefore, hydrocarbon streams with a relatively high organic nitrogen species content cannot be processed into high octane products without a reduction in organic nitrogen species content.
Accordingly, it is desirable to provide methods and apparatuses for processing hydrocarbon streams containing organic nitrogen species. Further, it is desirable to provide methods and apparatuses that continuously contact hydrocarbon streams with aqueous acidic solutions to react with and remove organic nitrogen species from the hydrocarbon streams. Furthermore, other desirable features and characteristics will become apparent from the subsequent detailed description and the appended claims, taken in conjunction with the accompanying drawings and the foregoing technical field and background.
Methods and apparatuses for processing hydrocarbon streams containing organic nitrogen species are provided. In one exemplary embodiment, a method for processing a hydrocarbon stream containing organic nitrogen species includes adding an aqueous acidic solution to a hydrocarbon feed stream to form a reaction stream. The method further includes contacting the reaction stream with a reaction surface and reacting the aqueous acidic solution and the organic nitrogen species to form an ammonium sulfate rich stream and a lean nitrogen naphtha stream. Also, the method includes separating an ammonium sulfate rich aqueous phase and an oil phase from the ammonium sulfate rich stream.
In another embodiment, method for processing a hydrocarbon stream including organic nitrogen species includes feeding the hydrocarbon stream to a mixer vessel and continuously injecting an aqueous acidic solution into the mixer vessel. The method further includes mixing the hydrocarbon stream and the aqueous acidic solution to form a reaction stream. The organic nitrogen species and the aqueous acidic solution are reacted in a chamber to form aqueous ammonium sulfates. The method includes withdrawing a lean nitrogen naphtha stream from the chamber.
In another embodiment, an apparatus for processing a hydrocarbon stream containing organic nitrogen species is provided. The apparatus includes a mixer vessel configured to receive and mix the hydrocarbon stream and an aqueous acidic solution to form a reaction stream. Further, the apparatus includes a chamber configured to receive the reaction stream and containing a reactive surface configured to contact the reaction stream and to facilitate a reaction between the organic nitrogen species and the aqueous acidic solution to form an ammonium sulfate rich stream and a lean nitrogen naphtha stream. The apparatus also includes a separation unit configured to separate an ammonium sulfate rich aqueous phase and an oil phase from the ammonium sulfate rich stream.
Embodiments of methods and apparatuses for processing hydrocarbon streams containing organic nitrogen species will hereinafter be described in conjunction with the following drawing figures, wherein like numerals denote like elements, and wherein:
The following detailed description is merely exemplary in nature and is not intended to limit the methods and apparatuses for processing hydrocarbon streams containing organic nitrogen species. Furthermore, there is no intention to be bound by any theory presented in the preceding background or the following detailed description.
Methods and apparatuses for processing hydrocarbon streams containing organic nitrogen species are provided herein. The methods and apparatuses provide for reacting the organic nitrogen species with an aqueous acidic solution. In an exemplary embodiment, an aqueous acidic solution is continuously injected and mixed into a hydrocarbon feed stream. Reaction between the aqueous acidic solution and the organic nitrogen species in the hydrocarbon stream results in the formation of aqueous ammonium sulfates. The reaction rate between the aqueous acidic solution and the organic nitrogen species may be enhanced by contacting the hydrocarbon stream with a reactive surface. The reaction forming the aqueous ammonium sulfates results in a nitrogen lean hydrocarbon stream that may undergo further processing, such as hydrotreating to reduce sulfur content. The aqueous ammonium sulfates may be separated for use as a solid byproduct. Further, exemplary methods and apparatuses provide for control of the flow rates of the hydrocarbon feed stream, the aqueous acidic solution, and the nitrogen lean hydrocarbon stream to maintain continuous injection of the aqueous acidic solution and a minimum level of acidity in the stream during reaction.
Each of
As shown, the treated stream 30 exits the mixer vessel 20 and enters a reaction chamber 32. The exemplary reaction chamber 30 includes a reactive material 34. The reactive material 34 may have small, low-volume pores that provide an increased surface area of the reactive material 34. For example, the reactive material 34 may be a bed of activated carbon or other suitable material providing an increased surface area. Contact of the treated solution 30 with the reactive material 34 increases the rate of reaction between the organic nitrogen species from the hydrocarbon stream 12 and the acid from the aqueous acidic solution 28. During the reaction, sulfuric acid combines with organic nitrogen species to produce ammonium sulfates. As a result, coalesced ammonium sulfates 38 accumulate at the bottom of the reaction chamber 32.
Due to removal of coalesced ammonium sulfates 38 from the treated stream 30, a lean nitrogen hydrocarbon stream 40, i.e., a stream having a lower organic nitrogen content than the hydrocarbon stream 12, is formed and is removed from the reaction chamber 32. In an exemplary embodiment, the organic nitrogen content of the lean nitrogen hydrocarbon stream 40 is less than 30% of the organic nitrogen content of the hydrocarbon stream 12, such as less than 15% of the organic nitrogen content of the hydrocarbon stream 12, for example less than 5% of the organic nitrogen content of the hydrocarbon stream 12. In certain embodiments, the lean nitrogen hydrocarbon stream 40 may be substantially free of organic nitrogen species, such has having fewer than 10 parts per million (ppm). In
After settling, the coalesced ammonium sulfates may be rejected from the reaction chamber 32 in an aqueous phase. Specifically, a bottom stream 44 is removed from the reaction chamber 32 and includes the aqueous phase of dissolved ammonium sulfates and an oil phase. The bottom stream 44 is delivered to a separation unit 50. An exemplary separation unit 50 is a drain pot. As shown, an aqueous ammonium sulfate stream 52 and a recycle oil stream 54 are separated in and removed from the separation unit 50. The recycle oil stream 54 is fed back into the reaction chamber 32. The aqueous ammonium sulfate stream 52 may be processed further at unit 60 to form a solid ammonium sulfate byproduct 62.
As shown in
Referring to
A reactor effluent 110 is formed and is fed to an acid settler 112. The reactor effluent 110 is separated into hydrocarbon phase 114 and an acid phase 116 in the acid settler 112. The hydrocarbon phase 114 is delivered to a caustic scrubber 118 where it is hot-water washed with caustic for pH control. It is then delivered to a deisobutanizer 122 and is successively depropanized, deisobutanized, and debutanized. The alkylate product 102 obtained from the deisobutanizer 112 can then go directly to motor-fuel blending or be rerun to produce aviation-grade blending stock. The isobutane 124 is recycled to the feed.
As shown, a portion of the acid phase 116, containing aqueous sulfuric acid, may be recycled for re-introduction to the reactor 106. Alternatively or additionally, the acid phase 116 may be utilized in the nitrogen removal zone 200 as aqueous acidic solution 28. As a result of the nitrogen removal process utilizing the aqueous acidic solution 28 outlined in reference to
In
After hydrodesulfurization occurs in the reactor 304, a reactor effluent 308 including hydrogen sulfide may be cooled through heat exchange with the incoming feed (not shown) and decompressed such that the reactor effluent 308 includes a mixture of liquid and gas. The reactor effluent 308 enters a gas separator vessel 310 which separates the reactor effluent 308 into a gas stream 312 and a liquid stream 314. The gas stream 312 passes through an amine contactor 316 where hydrogen sulfide is removed in stream 318. The hydrogen sulfide free gas then forms recycle gas 302 which is combined with the incoming lean nitrogen hydrocarbon stream 40.
The liquid stream 314 from the gas separator vessel 310 is routed through a stripper distillation tower 320. The bottoms product 322 from the stripper distillation tower 320 forms a desulfurized liquid product. The overhead sour gas 324 formed by the stripper distillation tower 320 typically contains hydrogen, methane, ethane, hydrogen sulfide, propane, and, perhaps, some butane and heavier components. That sour gas may be processed for removal of hydrogen sulfide and for recovery of propane, butane and pentane or heavier components. The residual hydrogen, methane, ethane, and some propane may be used as refinery fuel gas. The hydrogen sulfide removed and recovered by amine gas treating unit may be subsequently converted to elemental sulfur in a Claus process unit or to sulfuric acid in a wet sulfuric acid process or in the conventional Contact Process.
As described herein, a method and apparatus for processing a hydrocarbon stream containing organic nitrogen species have been provided. In exemplary embodiments, an aqueous acidic solution is continuously injected into the hydrocarbon stream and reacted with the organic nitrogen species therein to form ammonium sulfates. The ammonium sulfates are removed from the lean nitrogen hydrocarbon stream as an aqueous stream. The method and apparatus described above are particularly well-suited for use in upstream processing before hydrodesulfurization.
While at least one exemplary embodiment has been presented in the foregoing detailed description, it should be appreciated that a vast number of variations exist. It should also be appreciated that the exemplary embodiment or exemplary embodiments are only examples, and are not intended to limit the scope, applicability, or configuration of the claimed subject matter in any way. Rather, the foregoing detailed description will provide those skilled in the art with a convenient road map for implementing an exemplary embodiment or embodiments. It being understood that various changes may be made in the function and arrangement of elements described in an exemplary embodiment without departing from the scope set forth in the appended claims.
