Patent Application
20140190870
The present invention relates to methods and compositions for scavenging H2S and/or mercaptans from fluids, and more particularly relates, in one non-limiting embodiment, to methods and compositions for scavenging H2S and/or mercaptans from fluids using a transition metal salt and a water-soluble aldehyde or a water-soluble aldehyde precursor.
In the drilling, downhole completion, production, transport, storage, and processing of crude oil and natural gas, including waste water associated with crude oil and gas production, and in the storage of residual fuel oil, H2S and/or mercaptans are often encountered. The presence of H2S and mercaptans is objectionable because they often react with other hydrocarbons or fuel system components. Another reason that the H2S and mercaptans are objectionable is that they are often highly corrosive. Still another reason that H2S and mercaptans are undesirable is that they have highly noxious odors. The odors resulting from H2S and mercaptans are detectable by the human nose at comparatively low concentrations and are well known. For example, mercaptans are used to odorize natural gas and used as a repellant by skunks and other animals.
The predominant H2S and mercaptan scavengers for natural gas and crude oil are water soluble monoethanolamine (MEA) triazines and monomethylamine (MMA) triazines. These compounds contain nitrogen and when used in sufficient concentration may cause problems for certain refineries. Glyoxal (C2H2O2) or acrolein (C3H4O) have been used as H2S scavengers in instances where a nitrogen-containing H2S scavenger is not desired. Glyoxal is a slow acting scavenger and may be corrosive to mild steel. Acrolein is effective scavenger but an extremely toxic substance which operators do not like to use.
Oil soluble amine formaldehyde reaction products such as the dibutylamine/formaldehyde reaction product have been used previously as hydrogen sulfide (H2S) scavengers. The generic structure of oil soluble amines is given below.
wherein R1, R2, R3 and R4 may be independently a saturated or unsaturated hydrocarbon group, e.g., alkyl, aryl , alkylaryl, alkaryl, cycloalkyl, alkenyl, aralkenyl, alkenylaryl, cycloalkenyl, and the like or heterocyclyl groups and R5 may be hydrogen or lower alkyl.
It would be desirable if a new class of H2S and mercaptan scavengers could be discovered which is very effective, but which is more efficient and increases the reaction rate as compared with prior scavengers.
There is provided in one non-limiting embodiment a composition for synergistically scavenging hydrogen sulfide and/or mercaptans from a fluid, where the composition includes at least one transition metal salt, and at least one water-soluble aldehyde or water-soluble aldehyde precursor.
There is additionally provided in one non-restrictive version, a method for scavenging hydrogen sulfide and/or mercaptans from a fluid selected from the group consisting of an aqueous phase, a gaseous phase, a hydrocarbon phase and mixtures thereof. The method involves contacting the fluid with a composition in an effective amount for synergistically scavenging hydrogen sulfide and/or mercaptans. Again, the composition includes at least one transition metal salt, and at least one water-soluble aldehyde or water-soluble aldehyde precursor.
Synergistically scavenging is defined as the amount of hydrogen sulfide and/or mercaptans scavenged is greater as compared with a composition where either the transition metal salt or the at least one water-soluble aldehyde or water-soluble aldehyde precursor is absent, used in the same total amount.
Any of these methods may optionally include corrosion inhibitors including, but not necessarily limited to phosphate esters, acetylenic alcohols, fatty acids and/or alkyl-substituted carboxylic acids and anhydrides, phosphates esters and/or polyphosphate esters, quaternary ammonium salts, imidazolines, sulfur-oxygen phosphates, and the like, and combinations thereof.
It has been surprisingly discovered that combinations of transition metal salts and water-soluble aldehydes and/or water-soluble aldehyde precursors remove hydrogen sulfide present in natural gas and in oil more completely and faster than either of the components used alone at the same total concentrations in the mixture, and is thus also expected to remove mercaptans from these fluids as well. The process by which the hydrogen sulfide is effectively removed from gas, water or oil, or combinations thereof, involves introducing a synergistic combination of transition metal salt and water-soluble aldehyde and/or water-soluble aldehyde precursor into the H2S-containing system. The synergistic scavenger combination significantly increases the reaction rate and the overall scavenging efficiency over each of the components used alone, but at the same total amount. The synergy may be seen from the data discussed below.
In specific applications to remove H2S from crude oil, the hydrogen sulfide/mercaptan scavenger may be introduced in the crude oil (or other fluid) at concentrations from about 1 independently to about 100,000 ppm; in another non-limiting embodiment from about 10 independently to about 10,000 ppm; in a different embodiment from about 25 independently to about 7,500 ppm; alternatively from about 50 independently to about 5,000 ppm. The term “independently” when used in connection with a range means that any lower threshold may be combined with any upper threshold to give a valid or suitable alternative range.
It is expected that many transition metal salts may find at least some utility in the H2S/mercaptan scavenger compositions described herein. However, to give a better understanding, specific examples of suitable metal salts include, but are not necessarily limited to, zinc chloride, zinc acetate, zinc octoate, a zinc salt containing at least one hydrocarbyl group of at least 4 carbon atoms, such as zinc di-(neo-alkyl)-phosphorodithioate, zinc 2-ethylhexyl isopropyl phosphorodithioate, zinc dihydrocarbyldithiophosphates (ZDDP), zinc hydrocarbyl phosphate, zinc ethyl hexanoate (zinc 2-hexanoate), zinc naphthenates, zinc oleate, zinc carboxylate polymers (e.g. catena-2-ethylhexananto-(O,O′)-tri-μ-2-ethylhexanato(O,O′) dizinc (II)), copper salts, cobalt salts, manganese salts, iron salts such as iron chloride, iron carboxylates (e.g. iron oleate), iron neocarboxylates (e.g. iron 2-ethyl hexanoate), iron naphthenates, ferrocene, molybdenum metal salts, and combinations thereof. One specific suitable example is zinc octoate. In one non-limiting embodiment the metal salts are oil soluble, but it is expected that water soluble (aqueous soluble) metal salts will also be useful. Other transition metal salts including cobalt salts and manganese salts can also be used.
It is also expected that many water-soluble aldehydes or water-soluble aldehyde precursors will be suitable components in the H2S/mercaptan scavenger compositions described herein. But again, to give better understanding, specific examples of suitable aldehydes or water-soluble aldehyde precursors include, but are not necessarily limited to ethylene glycol hemiformal (ethylenedioxydimethanol) , glutaraldehyde, 2 [hydroxyethanol (amino)]ethanol, propylene glycol hemiformal), and combinations thereof. One specific suitable example is ethylene glycol hemiformal. In one non-limiting embodiment, there is an absence of dialdehyde, and/or an absence of glyoxal.
In one non-limiting embodiment, the amount of weight ratio of transition metal salt in the total composition with the water-soluble aldehyde or water-soluble aldehyde precursor (not accounting for any solvent) ranges from about 0.05 wt % independently to about 50 wt %, alternatively from about 5 independently to about 30 wt % transition metal salt. The water-soluble aldehyde or water-soluble aldehyde precursor comprises the balance.
The suitable solvents for the H2S/mercaptan scavenger compositions herein include, but are not necessarily limited to, Aromatic 100, ISOPAR M, kerosene, mineral oil, alcohols, glycols, and mixtures thereof.
It has been discovered that oil-soluble H2S/mercaptan scavenger compositions work well in brine solutions while water-soluble H2S/mercaptan scavenger compositions work well in non-aqueous or oil solutions. This occurs because the reaction is a heterogeneous reaction for the case of the H2S/mercaptan scavenger compositions in water. The actual concentration of the scavenger within the oil droplets in a water or brine solution is relatively high.
It has been surprisingly discovered that the amount of hydrogen sulfide and/or mercaptans scavenged is greater as compared with an otherwise identical composition with respect to transition metal salt, where the water-soluble aldehyde or water-soluble aldehyde precursor is absent and vice versa. This effect is true for the same total amount of active component.
It has been found that oil-soluble formulations of these compounds act as hydrogen sulfide and/or mercaptan scavengers when the hydrogen sulfide and/or mercaptan is present in the aqueous phase, the gaseous phase and a hydrocarbon phase. These methods and compositions may be used to remove hydrogen sulfide and/or mercaptans present in natural gas produced from natural gas wells. They may also be used to remove hydrogen sulfide and/or mercaptans from crude oil. Additionally they may be used to remove hydrogen sulfide and/or mercaptans from brines and other aqueous solutions containing them. Stated another way, the scavenging composition is expected to remove hydrogen sulfide and/or mercaptans in hydrocarbon gas streams, hydrocarbon liquid streams, produced water liquid stream and/or mixed production streams that contain all three phases.
More specifically, the H2S/mercaptan scavengers are expected to be useful in a wide variety of applications, particularly “upstream” and “downstream” applications (upstream and downstream of a refinery) including, but not necessarily limited to, residual fuel oil, jet fuel, bunker fuel, asphalt, recovered aqueous streams, as well as mixed production streams, for instance downhole or downstream of wellhead, including, but not limited to scavenging H2S and mercaptans from production fluids. Another suitable application may be to remove hydrogen sulfide from a hydrogen stream, and the like. In one non-limiting embodiment the method is practiced in a refinery. The primary applications within a refinery involve hydrocarbon liquid phases and hydrocarbon gaseous phases.
When the method scavenges H2S and/or mercaptans from a gaseous phase, the method may be practiced by contacting the gaseous phase with droplets of the composition, and/or passing the gaseous phase through the composition, such as by bubbling through a tower.
The scavenging compositions described herein may also include corrosion inhibitors including, but not necessarily limited to, phosphate esters, acetylenic alcohols, fatty acids and/or alkyl-substituted carboxylic acids and anhydrides, phosphates esters and/or polyphosphate esters, quaternary ammonium salts, imidazolines, sulfur-oxygen phosphates, and the like and combinations thereof.
The invention will now be illustrated with respect to certain examples which are not intended to limit the invention in any way but simply to further illustrate it in certain specific embodiments.
A continuous gas flow apparatus was used to evaluate H2S scavenger performance. This apparatus involved the sparging of a given composition of gas containing hydrogen sulfide in a vessel containing a liquid hydrocarbon. In the tests described here the liquid was heated at 75° C. and the pressure was 1 atm (0.1 MPa). Gas containing 3000 ppm H2S and 2% carbon dioxide was sparged continuously through a vessel containing liquid hydrocarbon. The initial concentration of H2S in the vapor space in equilibrium with liquid hydrocarbon was measured at 3,000 ppm. The concentration of H2S gas exiting the vessel was measured. The experiments were performed using following solutions:
A: (solution of 100% ethylene glycol hemiformal)
B: (solution of 16% by weight of zinc as zinc octoate in a hydrocarbon solvent)
The drop of H2S concentration is recorded in ISOPAR M as a function of time for 200 ppm of A, 200 ppm A+B (80% A and 20% B), and 200 ppm of solution B is shown in
The results can be described in terms of maximum H2S scavenged and H2S scavenging rate for various ratios of component A and component B as shown in
It may be seen clearly that the combinations of A and B show synergistic behavior for the maximum drop in H2S concentration and speed of reaction when compared with pure A or B.
In addition to the rate of H2S scavenging, the combination of A and B was also synergistic with respect to the overall scavenging efficiency.
A continuous gas flow apparatus was used to evaluate H2S scavenger performance. This apparatus involved the sparging of a given composition of gas containing hydrogen sulfide in a vessel containing a liquid hydrocarbon. In the tests described here the liquid was heated at 75° C. and the pressure was 1 atm (0.1 MPa). Gas containing 3000 ppm H2S and 2% carbon dioxide was sparged continuously through a vessel containing liquid hydrocarbon. The initial concentration of H2S in the vapor space in equilibrium with liquid hydrocarbon was measured at 3,000 ppm. The concentration of H2S gas exiting the vessel was measured. The experiments were performed using following solutions:
A: (solution of 100% ethylene glycol hemiformal)
B: (solution of 16% by weight of zinc as zinc octoate) in a hydrocarbon solvent)
C: (solution of 50% A and 17% B) with 33% solvent
D: (solution of 50% A and 27.5% B) with 22.5% solvent
E: (solution of 65% A and 13.75% B with 5% tertiary amine) with 16.25% solvent
In Table I the specific consumption of the four solutions to scavenge one kilogram of hydrogen sulfide is compared with each other.
The table demonstrates that a reduction in the specific consumption of different solutions for a fixed mass of hydrogen sulfide occurs with mixtures of ethylene glycol hemiformal and zinc octoate occurs. The best reduction in specific consumption of the hydrogen sulfide scavenging solution occurs when glycol hemiformal is used with zinc octoate and a tertiary amine (Solution E).
In the foregoing specification, the invention has been described with reference to specific embodiments thereof, and has been demonstrated as effective in providing methods and compositions for scavenging H2S and/or mercaptans from aqueous fluids, hydrocarbon fluids, gaseous phases and/or combinations thereof. However, it will be evident that various modifications and changes can be made thereto without departing from the broader spirit or scope of the invention as set forth in the appended claims. Accordingly, the specification is to be regarded in an illustrative rather than a restrictive sense. For example, specific transition metal salts, water-soluble aldehydes, water-soluble aldehyde precursors, and solvents falling within the claimed parameters, but not specifically identified or tried in a particular composition or method or proportion, are expected to be within the scope of this invention.
The words “comprising” and “comprises” as used throughout the claims is interpreted as “including but not limited to”.
The present invention may suitably comprise, consist or consist essentially of the elements disclosed and may be practiced in the absence of an element not disclosed. For instance, in a method for scavenging hydrogen sulfide and/or mercaptans from a fluid selected from the group consisting of an aqueous phase, a gaseous phase, a hydrocarbon phase and mixtures thereof, the method may consist of or consist essentially of contacting the fluid with a composition in an effective amount for synergistically scavenging hydrogen sulfide and/or mercaptans, where the composition consists of or consists essentially of at least one transition metal salt and at least one water-soluble aldehyde or water-soluble aldehyde precursor, where synergistically scavenging is defined as the amount of hydrogen sulfide and/or mercaptans scavenged is greater as compared with a composition where either the transition metal salt or the water-soluble aldehyde or water-soluble aldehyde precursor is absent, used in the same total amount.
Alternatively, in a composition for scavenging hydrogen sulfide and/or mercaptans from a fluid, the composition may consist of, or consist essentially of, at least one transition metal salt and at least one water-soluble aldehyde or water-soluble aldehyde precursor.
There may be further provided in a non-limiting embodiment, a fluid treated to scavenge hydrogen sulfide and/or mercaptans therefrom, where the fluid consists essentially of or consists of a fluid selected from the group consisting of an aqueous phase, a gaseous phase, a hydrocarbon phase and mixtures thereof, a composition present in an effective amount for synergistically scavenging hydrogen sulfide and/or mercaptans from the fluid, where the composition consists essentially of or consists of at least one transition metal salt, and at least one water-soluble aldehyde or water-soluble aldehyde precursor; where synergistically scavenging is defined as the amount of hydrogen sulfide and/or mercaptans scavenged is greater as compared with a composition where either the transition metal salt or the at least one water-soluble aldehyde or water-soluble aldehyde precursor is absent, used in the same total amount.
This application claims the benefit of U.S. Provisional Patent Application No. 61/750,973 filed Jan. 10, 2013, incorporated herein by reference in its entirety.
| Number | Date | Country | |
|---|---|---|---|
| 61750973 | Jan 2013 | US |
