Sulfide scavenger

Information

  • Patent Grant
  • 8562820
  • Patent Number
    8,562,820
  • Date Filed
    Tuesday, May 1, 2007
    17 years ago
  • Date Issued
    Tuesday, October 22, 2013
    11 years ago
Abstract
1,3,5-(2H2,4H2,6H2)tripropanediamine N,N,N′,N′,N″,N″ hexamethyl is used to scavenge sulfur compounds from hydrocarbons. A novel method of making the triazine comprises autocondensing (CH3)2NCH2CH2CH2N═CH2.
Description
BACKGROUND OF THE INVENTION

1. Field of the Invention


This invention relates to the treatment of hydrocarbons and other compositions to remove sulfides therefrom. Compositions and methods are disclosed for the treatment of newly recovered crude oil, natural gas and the like to ameliorate the odors and other problems caused by the presence of sulfides such as hydrogen sulfide. The compositions can also be used to treat sulfides in sewage, pulp and paper manufacturing systems, and similar industrial fluids and suspensions.


2. Description of the Related Art


Various compositions have been proposed and used for the treatment of hydrocarbons to remove or otherwise treat hydrogen sulfide and/or other sulfides present in them. See, for example, Gatlin's U.S. Pat. Nos. 5,128,049, 5,486,605, 5,488,103, and 5,498,707, U.S. Pat. No. 4,978,512 in the name of Dillon, and Stanchem's Canadian Patent 2,269,476.


The treating agents for the removal of sulfides are often referred to as scavengers in the patent literature. Frequently the compositions are reaction products of aldehydes and amine compounds, and may or may not contain one or more triazines or derivatives thereof. See the descriptions in columns 5-8 of Trauffler et al. U.S. Pat. No. 5,698,171, Sullivan III et al. U.S. Pat. Nos. 5,674,377, 5,674,377 and 5,744,024, Rivers et al. U.S. Pat. No. 5,554,591, Weers et al. U.S. Pat. Nos. 5,074,991, 5,169,411, 5,223,127, 5,266,185, 6,024,866 and 5,284,576, Pounds et al. U.S. Pat. Nos. 5,462,721 and 5,688,478, Bhatia et al. Canadian patents 2,125,513 and 2,148,849, and Callaway U.S. Pat. No. 5,958,352. They may be contacted with the hydrocarbons in various ways as mentioned in these patents and others such as Galloway U.S. Pat. No. 5,405,591 and Fisher U.S. Pat. No. 6,136,282. Note that Callaway's ('352) trimer has the structure:




embedded image


Sexton's GB patent 2,245,588 (p. 14) suggests the use of a reaction product of dimethylaminopropylamine and paraformaldehyde to treat fuel oils to prevent color and sediment formation. See also the triazines said to be useful for removing H2S in petroleum liquid, in Bhatia's U.S. Pat. No. 5,354,453. All of the patents identified in this paragraph and the preceding one are incorporated entirely by reference, as my invention may include the use of any of the sulfide scavengers recited or identified in them, particularly those containing at least one nitrogen, as a complement to the invention described herein.


The above cited references do not utilize the triazine compound described below to remove sulfides from hydrocarbons.


Many of the scavengers mentioned in the above cited patents remain, in one form or another, in the hydrocarbons they are used to treat. That is, they may be effective at suppressing the evolution of hydrogen sulfide, for example, but the sulfur is left in the hydrocarbon. There is a need for a method of treating hydrocarbons which does not merely neutralize the sulfur compounds, but enables the ready removal of them from the hydrocarbons.


SUMMARY OF THE INVENTION

My invention employs a triazine of the structural formula:




embedded image



for the treatment of hydrocarbons to remove sulfides and other sulfur compounds. This triazine is sometimes described herein as 1,3,5-(2H2,4H2,6H2) tripropanediamine N,N,N′,N′,N″,N″ hexamethyl, and may sometimes be known as S-triazine, 1,3,5-tris[(3-dimethylamine)propyl]hexahydro. The compound may be referred to herein as “TPDAHM triazine” for tripropyldiaminehexamethyl. Unlike the tertiary butyl triazines used by Sullivan et al. in U.S. Pat. No. 5,674,377, this triazine may be described as hydrophilic. It not only attracts the target sulfur compounds in the hydrocarbons, but also can be separated from the hydrocarbon after associating with the sulfur compounds, by contact with water, thereby facilitating the permanent removal of the sulfur compound from the hydrocarbon. This effect may be compared with the use of Sullivan et al.'s hydroxyalkyl hexahydro triazines (prepared by the reaction of an alkanol amine and formaldehyde—U.S. Pat. No. 5,744,024 at col. 5, lines 29-30). Sullivan's material is also apparently hydrophilic but Sullivan et al. demonstrate it is ineffective without the concurrent use of an accompanying ammonium compound.


My invention includes a novel method of making TPDAHM triazine by the autocondensation of the compound (CH2)2N CH2 CH2 CH2 N═CH2.







DETAILED DESCRIPTION

My scavenger may be made by reacting dimethylaminopropylamine with formaldehyde (preferably paraformaldehyde):




embedded image


The formaldehyde may be used in excess; in the above formula, for example, the expression 3HCHO may read 3-6HCHO—that is, the formaldehyde may be used in a molar ratio to the amine of 1:1 to 2:1, 3:1 or more, i.e., as much as a 10:1 ratio of formaldehyde to amine may be appropriate. See pages 13 and 14 of GB 2,245,588A for a description of a preferred synthesis. One mole of the dimethylaminopropylamine (DMAPA) is dissolved in toluene and stirred. One mole of paraformaldehyde is added. The reaction mixture is heated, preferably to reflux, and the evolved water may be collected. After water evolution is completed, the solvent is removed by heating under vacuum.


In a preferred method, the DMAPA is charged to a clean, dry reactor equipped with a vent line, along with a desired amount of a hydrophobic solvent, for example an aliphatic solvent; as a particular example, isoparaffin, and the paraformaldehyde is charged in increments of 20% of the desired amount, every 15 minutes or 20 minutes, with mixing as needed to control the exotherm. Close the reactor and vent, and continue to mix, maintaining a temperature between 180° F.-200° F. for 14 hours to 16 hours. Distill off the water; increase temperature slowly, bearing in mind the DMAPA boils at 275° F., to 310° F.-320° F. to continue to remove water. The product is effective to remove sulfur compounds by contact from oil and gas.


In any of the methods mentioned above, the formaldehyde may be in the form of an inhibited or an uninhibited solution, and may include up to 60% or more methanol. Commercial forms of formaldehyde, such as Methyl FORMCEL (55% formaldehyde in methanol or water) or Butyl FORMCEL (40% formaldehyde in butanol), both Trademarks of Celanese Corporation, may be used.


A preferred method of making my 1,3,5 (2H2, 4H2, 6H2) tripropanediamine N,N,N′,N′,N″,N″ hexamethyl is to autocondense the compound (CH3)2N CH2 CH2 CH2 N═CH2. This may be done in the presence of paraformaldehyde, which, it is believed, acts as a catalyst. In this reaction, no water is coproduced:




embedded image


Following are examples of the use of 1,3,5 (2H2, 4H2, 6H2) tripropanediamine N,N,N′,N′,N″,N″ hexamethyl to remove sulfur compounds from hydrocarbons:


The triazine can be added directly to a hydrocarbon stream, gas, compressed liquid such as butane or propane, or to liquids such as crude oil or fuel oil; also gasoline, Diesel oil, kerosene or bunker oil to scavenge hydrogensulfide and other sulfur compounds without water being present. The triazine may be added to oil based drilling muds where only emulsified water is present and oil is the continuous phase.


Thus it is seen that my invention is a method of treating a hydrocarbon to remove sulfur compounds from the hydrocarbon comprising adding 1,3,5 (2H2, 4H2, 6H2) tripropanediamine N,N,N′,N′,N″,N″ hexamethyl to the hydrocarbon in the presence of water. While the triazine itself is oil soluble, a reaction product of the triazine and the sulfur compound is drawn into the water, thereby separating the hydrocarbon from the water containing the reaction product. The sulfur compound may be a sulfide (for example, hydrogen sulfide), a mercaptan, or a dialkyl disulfide such as dimethyl disulfide. The hydrocarbon may be a liquid such as crude petroleum, for example, or a gas such as natural gas or a gas which emanates from an aerobic sewage plant, a landfill, coal gas recovery systems, digester effluents, or a compost pile, and may contain from 1 ppm to 10% by weight sulfide compound. It may be used in a tower or a tank. The triazine may be added to the hydrocarbon in an amount from 1 part per million to 10% by weight; the water may preferably be present in an amount from 10% to 200% of the weight of the triazine. The water containing the sulfur compound may be separated from the hydrocarbon by any known method—for example, decanting, or centrifuging.


While the foregoing is directed to embodiments of the present invention, other and further embodiments of the invention may be devised without departing from the basic scope thereof, and the scope thereof is determined by the claims that follow.

Claims
  • 1. A method for treating a liquid hydrocarbon to remove a sulfur compound therefrom, comprising: combining 1,3,5-(2H2,4H2,6H2) tripropanediamine N,N,N′,N′,N″,N″ hexamethyl triazine and the liquid hydrocarbon comprising the sulfur compound to form a reaction product of the triazine and the sulfur compound; thencombining water with the liquid hydrocarbon and the reaction product;drawing the reaction product into the water; andseparating the liquid hydrocarbon from the water comprising the reaction product.
  • 2. The method of claim 1, wherein the liquid hydrocarbon comprises a liquid substance selected from the group consisting of crude oil, crude petroleum, petroleum, fuel oil, gasoline, diesel oil, kerosene oil, bunker oil, compressed liquid propane, and compressed liquid butane.
  • 3. The method of claim 1, wherein the triazine is combined with the liquid hydrocarbon at an amount within a range from about 1 ppm to about 10% by weight of the liquid hydrocarbon.
  • 4. The method of claim 3, wherein the water is combined with the liquid hydrocarbon and the triazine at an amount within a range from about 10% to about 200% by weight of the triazine.
  • 5. The method of claim 1, the liquid hydrocarbon comprises the sulfur compound at a concentration within a range from about 1 ppm to about 10% by weight of the liquid hydrocarbon.
  • 6. The method of claim 5, wherein the sulfur compound comprises a compound selected from the group consisting of hydrogen sulfide, mercaptan, dialkyl disulfide, dimethyl disulfide, and derivatives thereof.
  • 7. The method of claim 1, wherein the water containing the reaction product is separated from the liquid hydrocarbon by a decanting process.
  • 8. The method of claim 1, wherein the water containing the reaction product is separated from the liquid hydrocarbon by a centrifuging process.
  • 9. The method of claim 1, wherein combining the triazine and the liquid hydrocarbon comprises adding the triazine to a hydrocarbon stream containing the liquid hydrocarbon without the presence of water.
  • 10. A method for treating a liquid hydrocarbon to remove a sulfur compound therefrom, comprising: combining at least 1,3,5-(2H2,4H2,6H2) tripropanediamine N,N,N′,N′,N″,N″ hexamethyl triazine and the liquid hydrocarbon comprising the sulfur compound to form a reaction product of the triazine and the sulfur compound, wherein the triazine is combined with the liquid hydrocarbon at an amount within a range from about 1 ppm to about 10% by weight of the liquid hydrocarbon;combining water with the liquid hydrocarbon and the reaction product;drawing the reaction product into the water; andseparating the liquid hydrocarbon from the water comprising the reaction product.
  • 11. The method of claim 10, wherein the water is combined with the liquid hydrocarbon and the triazine at an amount within a range from about 10% to about 200% by weight of the triazine.
  • 12. The method of claim 10, the liquid hydrocarbon comprises the sulfur compound at a concentration within a range from about 1 ppm to about 10% by weight of the liquid hydrocarbon.
  • 13. The method of claim 12, wherein the sulfur compound comprises a compound selected from the group consisting of hydrogen sulfide, mercaptan, dialkyl disulfide, dimethyl disulfide, and derivatives thereof.
  • 14. The method of claim 10, wherein the liquid hydrocarbon comprises a liquid substance selected from the group consisting of crude oil, crude petroleum, petroleum, fuel oil, gasoline, diesel oil, kerosene oil, bunker oil, compressed liquid propane, and compressed liquid butane.
  • 15. The method of claim 10, wherein the water containing the reaction product is separated from the liquid hydrocarbon by a decanting process.
  • 16. The method of claim 10, wherein the water containing the reaction product is separated from the liquid hydrocarbon by a centrifuging process.
  • 17. The method of claim 10, wherein combining the triazine and the liquid hydrocarbon comprises adding the triazine to a hydrocarbon stream containing the liquid hydrocarbon without the presence of water.
  • 18. A method for treating a liquid hydrocarbon to remove a sulfur compound therefrom, comprising: combining at least 1,3,5-(2H2,4H2,6H2) tripropanediamine N,N,N′,N′,N″,N″ hexamethyl triazine, water, and the liquid hydrocarbon comprising the sulfur compound to form a reaction product of the triazine and the sulfur compound, wherein the liquid hydrocarbon comprises a liquid substance selected from the group consisting of crude oil, crude petroleum, petroleum, fuel oil, gasoline, diesel oil, kerosene oil, bunker oil, compressed liquid propane, and compressed liquid butane, the sulfur compound at a concentration within a range from about 1 ppm to about 10% by weight of the liquid hydrocarbon, and the sulfur compound comprises a compound selected from the group consisting of hydrogen sulfide, mercaptan, dialkyl disulfide, dimethyl disulfide, and derivatives thereof;drawing the reaction product into the water; andseparating the liquid hydrocarbon from the water comprising the reaction product.
  • 19. The method of claim 18, wherein the water is combined with the liquid hydrocarbon and the triazine at an amount within a range from about 10% to about 200% by weight of the triazine.
  • 20. The method of claim 18, wherein the triazine is combined with the liquid hydrocarbon and the water at an amount within a range from about 1 ppm to about 10% by weight of the liquid hydrocarbon.
CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a continuation of U.S. Ser. No. 10/291,461, filed Nov. 8, 2002, now U.S. Pat. No. 7,211,665, which claims benefit of U.S. Ser. No. 60/345,847, filed Nov. 9, 2001, which are herein incorporated in their entirety by reference.

US Referenced Citations (38)
Number Name Date Kind
2149380 Yabroff et al. Mar 1939 A
2783205 Brooks Feb 1957 A
3053757 Bloembergen Sep 1962 A
4266054 Au May 1981 A
4430196 Niu Feb 1984 A
4440649 Loftin et al. Apr 1984 A
4675169 Hass Jun 1987 A
4978366 Weers Dec 1990 A
4978512 Dillon Dec 1990 A
5074991 Weers Dec 1991 A
5082987 Olbrich et al. Jan 1992 A
5128059 Storey et al. Jul 1992 A
5169411 Weers Dec 1992 A
5223127 Weers et al. Jun 1993 A
5266185 Weers et al. Nov 1993 A
5284576 Weers et al. Feb 1994 A
5347004 Rivers et al. Sep 1994 A
5354453 Bhatia Oct 1994 A
5405591 Galloway Apr 1995 A
5415785 Braden et al. May 1995 A
5462721 Pounds et al. Oct 1995 A
5486605 Gatlin Jan 1996 A
5488103 Gatlin Jan 1996 A
5498707 Gatlin Mar 1996 A
5554349 Rivers et al. Sep 1996 A
5567213 Gentry et al. Oct 1996 A
5674377 Sullivan, III et al. Oct 1997 A
5688478 Pounds et al. Nov 1997 A
5697443 Brezinski et al. Dec 1997 A
5698171 Trauffer et al. Dec 1997 A
5744024 Sullivan et al. Apr 1998 A
5958352 Callaway et al. Sep 1999 A
6024866 Weers et al. Feb 2000 A
6063346 Luna May 2000 A
6117310 Rivers Sep 2000 A
6136282 Fisher Oct 2000 A
7211665 Gatlin May 2007 B2
20020157989 Gatlin et al. Oct 2002 A1
Foreign Referenced Citations (10)
Number Date Country
2125513 Jan 1995 CA
2005946 Feb 1995 CA
2148849 Dec 1995 CA
2404511 Aug 1975 DE
4027300 Mar 1992 DE
40 27 300 May 1992 DE
1 456 732 Nov 1976 GB
2 245 588 Jan 1992 GB
WO 9201481 Feb 1992 WO
WO 9201481 Feb 1992 WO
Non-Patent Literature Citations (3)
Entry
W. J. Kauffman, Observations on the Synthesis and Characterization of N, N′, N″ Tris-(dimethylaminopropyl) hexahydro-s-triazine and isolable intermediates, J Heterocyclic Chemistry, p. 409-411, (Apr. 1, 1975).
Ulf Fuchslueger, Gunther Socher, Hans-Jorg Grether, and Manfred Grasserbauer, Capillary Supercritical Fluid Chromatography/Mass Spectrometry of Phenolic Mannich Bases With Dimethyl Ether Modified Ethane as the Mobile Phase, Analytical Chemistry, American Chemical Society, vol. 7 (No. 13), p. 2324-2333, (Jul. 1, 1999).
GB Examination Report, Application No. GB0328368.6, dated Nov. 14, 2005.
Related Publications (1)
Number Date Country
20070284288 A1 Dec 2007 US
Provisional Applications (1)
Number Date Country
60345847 Nov 2001 US
Continuations (1)
Number Date Country
Parent 10291461 Nov 2002 US
Child 11743054 US