MANTARRO MILENA (IT)
QUARANTA ANDREA (IT)
| WO2001083435A1 | 2001-11-08 | |||
| WO1992001481A1 | 1992-02-06 | |||
| WO2009076420A1 | 2009-06-18 | |||
| WO2005065177A2 | 2005-07-21 | |||
| WO2009105444A2 | 2009-08-27 |
| GB2125779A | 1984-03-14 | |||
| JPH08245562A | 1996-09-24 | |||
| US5008432A | 1991-04-16 | |||
| US20080039344A1 | 2008-02-14 | |||
| US20120329930A1 | 2012-12-27 | |||
| JPH04145113A | 1992-05-19 | |||
| CN102924648A | 2013-02-13 | |||
| US4874604A | 1989-10-17 | |||
| US5554349A | 1996-09-10 | |||
| US5480860A | 1996-01-02 | |||
| US4978512A | 1990-12-18 | |||
| EP0438812A1 | 1991-07-31 | |||
| US5085842A | 1992-02-04 | |||
| US4680127A | 1987-07-14 | |||
| US5744024A | 1998-04-28 | |||
| US5354453A | 1994-10-11 | |||
| US5347004A | 1994-09-13 | |||
| EP0121377A1 | 1984-10-10 | |||
| EP0421683A1 | 1991-04-10 | |||
| US4252655A | 1981-02-24 | |||
| US5000835A | 1991-03-19 | |||
| US20080039344A1 | 2008-02-14 | |||
| US6599472B1 | 2003-07-29 |
| CLAIMS H2S scavenger in water and hydrocarbon fluids and gases present in crude oil extraction and refining processes comprising at least one compound of the following formula I wherein R is selected from the class formed by methyl, 2-(diethylamino)- ethyl, butyl, glycidyl, ethyl, benzyl, lauryl, allyl, stearyl, hydroxypropyl, isobutyl, phenyl, isobornyl, cyclohexyl, propyl, tert-butyl, sec-butyl, n-propyl and at least one amine, selected from the class formed by ethylenediamine, monoethanolamine, dimethylispropanolamine, and dimethylaminopropylamine. 2. Scavenger according to claim 1 wherein R is selected from the class formed by methyl, ethyl, propyl. 3. Scavenger according to claim 1 or 2, wherein the ratio compound of general formula I /amine varies from 5: 1 to 1 : 1 (weight/weight), preferably from 2.5:1 to 1.5: 1 , with reference to the total weight of the scavenger. 4. Scavenger according to at least one of the preceding claims further comprising metallic salts and/or organometallic compounds and/or metallic complexes with ammonia or EDTA, said metals being selected from the class formed by iron, copper, silver, sodium, potassium and zinc, wherein the weight/weight ratio between the compound of formula I and metallic salts and/or organometallic compounds and/or metallic complexes with ammonia or EDTA varies from 1 : 100 to 1 : 10. 5. Scavenger according to claim 4 wherein said metallic salts are selected from the class formed by sulphates, chlorides and/or nitrates. 6. Scavenger according to claim 4 wherein said organometallic compounds are selected from the class formed by acetates, aspirinates, gluconates and/or ascorbates. 7. Scavenger according to at least one of the preceding claims further comprising a dispersing agent. 8. Scavenger according to claim 7, wherein said dispersing agent is selected from the class formed by non-ionic and cationic surfactants, in particular quaternary ammonium salts, oxyethylated amines, alcohols and oxyethylated phenols. 9. H2S scavenger in water and hydrocarbon fluids and gases present in crude oil extraction and refining processes comprising at least one compound of the following formula I wherein R is selected from the class formed by methyl, 2-(diethylamino)- ethyl, butyl, glycidyl, ethyl, benzyl, lauryl, allyl, stearyl, hydroxypropyl, isobutyl, phenyl, isobornyl, cyclohexyl, propyl, tert-butyl, sec-butyl, n-propyl. 10. Scavenger according to claim 9, wherein R is selected from the class formed by methyl, ethyl, propyl. 1 1. H2S Scavenger in water and hydrocarbon fluids and gases present in crude oil extraction and refining processes comprising a dispersing agent and metallic salts and/or organometallic compounds and/or metallic complexes with ammonia or EDTA, said metals being selected from the class formed by iron, copper, silver, sodium, potassium and zinc. 12. Scavenger according to claim 11 , wherein said dispersing agent is selected from the class formed by non-ionic and cationic surfactants, in particular quaternary ammonium salts, oxyethylated amines, alcohols and oxyethylated phenols. 13. Scavenger according to at least one of the claims 1 1 or 12, wherein the weight/weight ratio between dispersing agent and metallic salts and/or organometallic complexes and/or metallic complexes with ammonia or EDTA varies from 2: 1 to 0.5: 1 , preferably from 1.6 : 1 to 1.2 : 1. 14. Scavenger according to at least one of the claims 1 1 to 13, wherein said metallic salts are selected from the class formed by sulphates, chlorides and/or nitrates and said organometallic compounds are selected from the class formed by acetates, aspirinates, gluconates and/or ascorbates. |
DESCRIPTION
The present invention relates to new products for H 2 S scavenging from fluids and gases, in particular water and hydrocarbon fluids and gases. These products (scavengers) are added to H 2 S-containing fluids and are able to selectively react with sulphidric acid and transform it into innocuous, nonvolatile species, which are not released even at very high temperatures (140-150°C).
State of the Art
H 2 S removal from water and hydrocarbon fluids has been the subject of numerous patents: various physical and chemico-physical means are claimed, but in particular the chemical compounds proposed as scavengers of the sulphidric acid are very many. An H 2 S scavenger selectively reacts with H 2 S forming a different compound (either a salt or an organic tiocompound) which retains the H 2 S in the starting fluid, preventing its development in the atmosphere and therefore preventing risks to the health of operators in charge of manipulating H 2 S-rich fluids.
In particular, in the petroleum industry H 2 S presence is a problem long highlighted, which may derive both from the same composition of the crude oil, rich in sulphides and H 2 S, and from the presence of bacteria that, under certain conditions, produce H 2 S, thereby increasing the content of this toxic gas in production fluids. Moreover, even during crude oil refining, H 2 S can result as cracking product of sulphured compounds present in the crude oil load, and therefore even crude oils initially without this problem, can produce refining residues with variable contents of sulphidric acid, from a few ppm to hundreds of ppm.
Currently triazines, and in particular hexahydrotriazines (US5554349-US5480860 - WO92/01481-US4978512) and glyoxal (EP0438812 - US5085842 - US4680127) are widely used as scavengers. However, both these substances are more soluble in water than in hydrocarbons and therefore disperse poorly in crude oil and refinery plant residues, greatly slowing down reaction kinetics.
Actually, triazines, though being the H 2 S scavengers most used on the world market, do not exhibit a favorable reaction ratio as they are molecules of rather high molecular weight - 250/300 Daltons - and even though theoretically a triazine molecule might react with several H 2 S molecules, in reality, by being scarcely soluble in a hydrocarbon fluid they practically react with a 1 : 1 molar ratio; therefore, the weight ratio is clearly unfavorable. Triazines which react very quickly in a water environment; in hydrocarbons, in which are scarcely soluble, they have to be strongly overdosed to try to increase the reaction kinetics. However, even when heavily overdosing them and, in the presence of dispersing agents such as quaternary ammonium salts and oxyethylated amines, the reaction rate in heavy fluids such as fuel oils is very limited. Other drawbacks in triazine use are:
- They cannot be used on bitumens, as their thermal stability is at the limit at the temperatures at which bitumens are manipulated (150 - 200°C), and also the adduct formed from the reaction between triazines and H 2 S tends to decompose at those temperatures, re-forming the starting H 2 S
- According to the latest EC rules, many triazines are classified as extremely toxic substances, lethal when inhaled.
They cannot be used on H 2 S-containing naphthas and kerosenes, since triazine synthesis envisages formation of a certain amount of water and therefore are marketed in concentrated water solutions. When water addition is strictly forbidden (gasolines, naphthas, kerosenes), triazine use is impossible.
A solution to triazines' scarce compatibility with hydrocarbon fluids has been surmised in various patents, and attempts at obviating this problem were made by combining triazine with a dispersing agent (ammonium salts or oxyethylated amines - US5744024) or modifying the lipophilicity of triazine itself, by inserting in the molecule substituents having a rather long hydrocarbon chain (US5354453 - US5347004).
When triazines cannot be used, the use of organometallic compounds such as zinc octoate is quite well-established. Besides these typologies of organic compounds, above all to treat strong hydrocarbon environments such as fuel oils and bitumens, a long series of organometallic compounds were considered in H 2 S scavenging. At the forefront, zinc and iron compounds, above all organic ones such as octoate (EP0121377 - EP421683 - US4252655 - US5000835); moreover, dispersions of powdered oxide, above all zinc oxides, and inorganic salts (WO2009/076420 - US2008/0039344 - US6599472 - WO2005/065177 - WO 2009 - 105444) have been proposed. Furthermore, copper, cadmium, mercury, silver, nickel and magnesium and compounds thereof were used. Also this class of compounds, though affording a partial solution to the problem of solubility in hydrocarbons (with consequent improved mixability with fuel oils and bitumens) entails drawbacks: containing a metal, they cannot be used in gasolines, naphthas, kerosenes. the stoichiometric ratio with H 2 S is markedly penalizing for this class of scavengers (very high molecular weight (MW); therefore, they have to be used in a very high weight ratio relative to the H 2 S present (1 : 15 / 1 :20 H 2 S relative to Zn octoate).
- When in a concentrated solution, metallic salts are markedly viscous and therefore scarcely manipulable/dispersible in cold climates; when diluted to be better manipulated/dispersed the use ratio grows even more, making them highly penalized economically.
Hence, the need to overcome these drawbacks was felt in the state of the art.
Therefore, object of the present invention is to provide scavengers not entailing such drawbacks. Therefore, object of the present invention are the scavengers of claim 1. Further objects are specified in the dependent claims.
Brief description of the figure
A figure (1) showing an operation diagram of the Seta H 2 S Analyzer is enclosed to the present description
Description of the Invention
The H 2 S scavengers according to the present invention are employed in water and hydrocarbon fluids and gases present in crude oil extraction and refining processes, particularly before and after the refining processes.
According to the invention, such scavengers comprise
at least one compound of the following formula I
and one amine. In the compound of formula I, radical R is selected from the class formed by methyl, 2-(diethylamino)-ethyl, butyl, glycidyl, ethyl, benzyl, lauryl, allyl, stearyl, hydroxypropyl, isobutyl, phenyl, isobornyl, cyclohexyl, propyl, tert-butyl, sec- butyl, n-propyl. Advantageously, R represents methyl, ethyl, propyl.
As amines according to the present invention, amines selected from the class formed by ethylenediamine, monoethanolamine, dimethylispropanolamine, and dimethylaminopropylamine can be employed. The ratio between the compounds of general formula I and the amine varies from 5:1 to 1 : 1 (weight/weight), preferably from 2.5: 1 to 1.5: 1 with reference to the total weight of the scavenger. Without being bound to particular reaction mechanisms, it can be assumed that amine presence strongly catalyzes the reaction between MMA and H 2 S: laboratory data confirm that scavenging efficacy is multiplied in the presence of amines: even though efficacy is not a factor that can be accurately quantitated, it being dependent on reaction conditions, temperature, contact times, etc., it can however be stated that it increases 2- to 10-fold. Thus, reaction kinetics is sped up, enabling H 2 S clearing at very low ratios.
A further object of the present invention is a scavenger comprising, besides at least one compound of formula I and at least one amine, metallic salts and/or organometallic compounds and/or metallic complexes with ammonia or EDTA. The metals employed belong to the class formed by iron, copper, silver, sodium, potassium and zinc. Advantageously, the weight/weight ratio between the compound of formula I and metallic salts and/or organometallic compounds and/or metallic complexes with ammonia or EDTA varies from 1 : 100 to 1 :10 with reference to the total weight of the scavenger. Preferred metallic salts are sulphates, chlorides and/or nitrates, whereas the organometallic compounds are selected from the class formed by acetates, aspirinates, gluconates and/or ascorbates.
A further object of the present invention is a scavenger that, besides at least one compound of formula I, at least one amine and metallic salts and/or organometallic compounds and/or metallic complexes with ammonia or EDTA, further comprises a dispersing agent. Advantageously said dispersing agent belongs to the class formed by non-ionic and cationic surfactants, in particular quaternary ammonium salts, oxyethylated amines, alcohols and oxyethylated phenols.
A further object of the present invention is an H 2 S scavenger in water and hydrocarbon fluids and gases present in crude oil extraction and refining processes comprising at least one compound of the following formula I
wherein R is selected from the class formed by methyl, 2-(diethylamino)-ethyl, butyl, glycidyl, ethyl, benzyl, lauryl, allyl, stearyl, hydroxypropyl, isobutyl, phenyl, isobornyl, cyclohexyl, propyl, tert-butyl, sec-butyl, n-propyl. Advantageously, R is selected from the class formed by methyl, ethyl, butyl.
A further object of the present invention is an H 2 S scavenger in water and hydrocarbon fluids and gases present in crude oil extraction and refining processes comprising a dispersing agent and metallic salts and/or organometallic compounds and/or metallic complexes with ammonia or EDTA. Advantageously, the metals are selected from the class formed by iron, copper, silver, sodium, potassium and zinc. The dispersing agent used is selected from the class formed by non-ionic and cationic surfactants, in particular quaternary ammonium salts, oxyethylated amines, alcohols and oxyethylated phenols. The weight/weight ratio between dispersing agent and metallic salts and/or organometallic compounds and/or metallic complexes with ammonia or EDTA, varies from 2: 1 to 0.5: 1 , preferably from 1.6 : 1 to 1.2 : 1. The metallic salts are selected from the class formed by sulphates, chlorides and/or nitrates, and said organometallic compounds are selected from the class formed by acetates, aspirinates, gluconates and/or ascorbates. H 2 S-containing fluids treatable with the scavenger according to the present invention can be from crude oil to all petroleum cuts such as gasoline, Kerosene, diesel oil, the heavy residues, coming both from atmospheric and vacuum distillation plants, and from thermal and catalytic cracking plants (FCC slurry, visbreaking residue, LC Finer/H-Oil). Moreover, said technology can be applied on heavy refinery end products, such as bitumen and fuel oils.
The use of scavengers containing compounds of formula I wherein R is methyl ensures the following advantages:
It is a substance not particularly dangerous for manipulation
Usable on H 2 S-containing naphthas and kerosenes, as not containing water and not being particularly soluble in water
Does not contain metals.
It is very reactive toward H 2 S, and the stoichiometric ratio with H 2 S is favorable (very low MW); therefore, it can be dosed in a very low weight ratio (1 :5 / 1 :8 H 2 S relative to MMA).
- It is perfectly fluid even without heating. Amines particularly effective for this purpose are ethylenediamine, monoethanolamine, dimethylispropanolamine, dimethylaminopropylamine, dicyclohexylamine, dimethylcyclohexylamine, tributylamine, tetraethylenepentamine (TEPA).
Scavenger efficacy tests were conducted by following the IP 570 method (ASTM D 7621); specifically, the Seta H 2 S Analyzer was used, which follows the abovecited method. This instrument enables direct analysis of crude oil over short times (15 minutes). Hereinafter, a brief description: oil is additivated at a given dosage ratio and left under incubation at 35°C and at rest. At the time of interest, a known volume of sample is collected, which is dissolved into the analysis diluent, and the whole is heated at 60°C. With an air flow of 30L/min, H 2 S is stripped from the solution and carried to the electrochemical sensor. After 15' scrubbing, H 2 S content is calculated on the basis of sensor-detected mV and analyzed sample amount. Another method (UOP 163-80) can be used for the same purpose: a sample of the liquid hydrocarbon to be analyzed is placed in a potentiometric cell in ammonia-isopropyl alcohol, titrating with silver nitrate in alcoholic solution. As reference electrode a glass electrode is used, whereas the measurement electrode is a silver/silver sulphide one.
By this method it is possible to measure the amount of mercaptans and H 2 S present, directly from the titration curve. The analysis can be performed manually by an operator or automatically, using an automatic titrator.
Seven examples of embodiment of the invention are enclosed to the present description.
Example 1 :
A model solution (80% isopar L and 20% Solvesso 150) was doped with about 150 ppm of H 2 S. With said solution, efficiency measurements were performed for various chemicals, both oil-soluble and water-soluble ones. Additivations were carried out at ambient temperature and at an active dosage ratio of 1 : 1 relative to the H 2 S titer. Additivated products were kept at 40°C and under bland stirring over different times.
Abatement % Abatement %
Product 3 hours 24 hours
Triazine (reference) 29.7 81.2
Glyoxal (reference) 43.7 75.5
MMA 12.6 64.7 MMA + DMAPA (amine) 89.4 93.5
MMA + DMAPA + Potassium
aspirinate 98.2 99
MMA + DMAPA +
Potassium aspirinate+ Dispersing
agent 99.2 99.8
The innovative products according to this patent application were tested relative to two reference additives (Triazine and Glyoxal).
Tests were repeated in the presence of MMA coupled to other Potassium compounds (sulphate, nitrate, acetate, aspirinate, gluconate and ascorbate), obtaining abatement percentages similar to those reported.
Example 2:
A Fuel Oil sample was fluxed with 25% xylene and doped with about 73 ppm of H 2 S. Tests were performed at 60°C. Additivations were performed at ambient temperature and at variable dosage ratios ( 1 :6— 1 :3— 1 :1) relative to the H 2 S titer.
Tests were repeated by replacing the indicated Potassium and Copper compounds with other derivatives of the same metals (complexes with ammonia and EDTA, sulphates, chlorides, nitrates, acetates, aspirinates, gluconates and/or ascorbates) obtaining abatement percentages similar to those reported. Example 3:
A real sample of Iran Light Crude Oil containing about 60 ppm of H 2 S was used. Tests and additivations were carried out at 35°C, and additivated samples were left in an hermetically sealed vessel for 3 hours in the absence of stirring.
Example 4:
A set of samples of modified road Bitumen having a high H 2 S content were additivated with 500 ppm of product. Samples were left in sealed containers for 4 hours and then for 24 hours, without any stirring. A certain loss of H 2 S concentration was found also in blanks, probably due to a less than perfect seal of the containers: in any case, it was possible to assess the efficacy as H 2 S scavengers of the various products tested.
Additive Dosage Initial H 2 S H 2 S - 4h H 2 S - 24h ppm ppm ppm ppm
Blank - 113.6 86 68
Zinc octoate (reference) 500 - 18 15.7
Potassium aspirinate +
Dispersing agent 500 38.7 27.5
Copper EDTA +
Dispersing agent 500 13.1 8
Iron gluconate+
Dispersing agent 500 26.8 23.2
Blank - 127 96 83 Zinc octoate (reference) 700 - 26.9 13.7
Potassium aspirinate +
Dispersing agent 700 51.8 33.4
Copper EDTA +
Dispersing agent 700 18.4 3
Iron gluconate +
Dispersing agent 700 43 32.2
Tests were repeated by replacing the indicated Potassium, Iron and Copper compounds with other derivatives of the same metals (complexes with ammonia and EDTA, sulphates, chlorides, nitrates, acetates, aspirinates, gluconates and/or ascorbates) obtaining abatement percentages similar to those reported.
Example 5:
A battery of tests were performed on H 2 S-containing light Naphtha. The products were tested at various dosage ratios; it is important to note that Naphtha specifications rule out water presence in even a minimal amount, therefore water- containing products are absolutely to be avoided.
Sample MMA H 2 S MMA + MEA H 2 S ppm ppm ppm ppm
Blank 3 - 34 - 34
5: 1 ratio 170 28 170 <1
10: 1 ratio 340 6 340 <1 Example 6:
Some samples of H 2 S-containing Fuel Oil were additivated. Samples were left in sealed containers, without any stirring: some were analyzed immediately after additivation (10 min.), others after 3 hours. H 2 S residue was tested by an internal method (air insufflation to drag away H 2 S and assessment of gas output from the vessel with a calibrated Draeger vial, specific for H 2 S determination).
Tests were repeated by replacing the Copper (EDTA) compound with the Copper - ammonia compound, with Copper sulphate, chloride, nitrate, acetate, aspirinate, gluconate and ascorbate, obtaining abatement percentages similar to those reported.
Example 7:
A set of samples of H 2 S-containing Fuel Oil were additivated. Samples were left in sealed containers, at 60°C, without any stirring: some were analyzed at +1 hour from additivation, others at +3 hours. H 2 S residue was tested by IP 570 method (Seta analyzer).
Tests were repeated by replacing the Copper (EDTA) compound with the Copper - ammonia compound, with Copper sulphate, chloride, nitrate, acetate, aspirinate, gluconate and ascorbate, obtaining abatement percentages similar to those reported.