Process for absorption of sulfur compounds from fluids using certain piperidines, piperazines, or anhydrides of monocarboxylic amino acids

Abstract: Sulfur dioxide is removed from a fluid containing SO₂ by employing as an absorbent for the SO₂ an aqueous solution of a compound represented by Formulae I, II or III: wherein each Y is independently -(CR²₂)- or -(CR²)=; each R¹, R², R⁵ or R⁶ is independently hydrogen, an alkyl group; an hydroxyalkyl group; an aldehyde group; a carboxylic acid group or salt thereof; or an alkyl group containing at least one carboxylic acid ester, a carboxylic acid or salt thereof, ether, aldehyde, ketone, or sulfoxide group; wherein at least one of R¹ and R² and at least one of R⁵ and R⁶ is a carbonyl-containing group; each R³ or R⁴ is independently hydrogen; an alkyl group; a hydroxyalkyl group; an aldehyde group; a carboxylic acid or salt group; or an alkyl, aryl, or aralkyl group containing at least one carboxylic ester, a carboxylic acid or salt, ether, aldehyde, ketones or sulfoxide group. The absorbent solution preferably can be thermally regenerated by heating to remove SO₂.

Description: This invention relates to a method for removing sulfur compounds from gaseous streams. More particularly, it relates to a method for removing sulfur compounds including sulfur dioxide (SO₂) from fluids. Removal of such sulfur compounds as sulfur dioxide, for example from fluids such as industrial and utility gas emissions, is increasingly important. Acid rain is believed to occur when sulfur dioxide in such emissions undergoes chemical changes in the atmosphere and returns to earth with precipitation. There are numerous techniques for removing sulfur compounds from gas streams containing them. One common process employs limestone scrubbing. The disadvantage of this process is the necessity of disposing of the large volume of solid waste produced. The wastes are not generally recycled. Another system, taught in US-A-4,366,134, employs potassium or sodium citrate to selectively remove SO₂ from a gas stream. While the wastes from this process can be recycled, recycle is expensive because thermally stable salts are formed and require higher heat for regeneration. More recent patents teach the use of certain piperazinone derivatives. For instance, US-A-4,112,049 teaches use of certain piperazinones and N,N'- alkyl piperazinone. In another patent, US-A-4,530,704, the removal of SO₂ from a gas stream is accomplished by contacting a gas stream containing it with an aqueous solution of a piperazinone, morpholinone or N-alkyl substituted derivatives thereof, for example N,N'-dimethyl-2-piperazinone. In US-A-4,783,327 certain hydroxyalkyl substituted piperazinones are taught for use in a similar manner. DE-A-2108282 discloses the removal of hydrogen sulfide from gases containing sulfur dioxide by reaction in the presence of a polar aprotic solvent containing certain urea or thiourea derivatives. These derivatives include 5,5-pentamethylene biuret. US-A-4217238 discloses the removal of acidic components from gaseous mixtures by contact with an aqueous solution comprising a basic salt and an activator system comprising (1) at least one sterically hindered amine and (2) an aminoacid which is a cosolvent for the sterically hindered amine. Reference is made to the removal of, inter alia, sulfur dioxide in a mixture containing at least carbon dioxide. Exemplified sterically hindered amines include 2-methylpiperazine; 2,5-dimethylpiperazine; and 2-tertbutylamino-methyl-1,4-dimethylpiperazine and exemplified amino acids include tipecolinic acid (ie 2-piperidine carboxylic acid); 2-piperidine acetic acid; 2-piperidine propionic acid; 4-methyl-2-piperidine carboxylic acid; 6-methyl-2-piperidine carboxylic acid; 6-methyl-3-piperidine carboxylic acid; 1-methyl-2-piperidine carboxylic acid; 1-methyl-3-piperidine carboxylic acid and 1-methyl-4-amino-4-piperidine carboxylic acid. There is no suggestion that those acids could be used alone. US-A-3793434 discloses the removal of acid gases from gaseous mixtures by contacting with an aqueous solution of an alkali metal salt and a piperidine derivative. The piperidine derivatives included piperidines in which a ring carbon atom is substituted by a carboxyl group although there is no exemplification of such compounds. Sulfur dioxide is included amongst the specified acid gases. There is no suggestion that the piperidine derivatives could be used alone. US-A-4783327 discloses a method of removing sulfur dioxide from a gas stream by treatment with an aqueous solution containing 4-(2-hydroxyalkyl)-2-piperazinone or a derivative thereof having one oxo substituent on a ring carbon atom. It would be advantageous to have a process for removal of sulfur compounds such as sulfur dioxide which employs an aqueous solution and uses an absorbent which has a high capacity for absorbing sulfur dioxide. The absorbent would desirably be regenerable. It is also desirable that this absorbent has adequate water compatibility at ambient or higher temperatures and its salts are water soluble to avoid inducing scaling or plugging of plant equipment. According to the present invention, there is provided a process for removing SO₂ from a fluid containing SO₂, the improvement comprising employing, as an absorbent for the SO₂, an aqueous solution containing as the only SO₂-absorbent(s) at least one compound represented by Formula A: wherein: X is -Z³- or -N(R)-; and (a) when X is -Z³-, Z¹ and Z² are both -Z³-; each Z³ independently is -(CR₂)- or -(CR)=; and each R independently is hydrogen; optionally inertly substituted alkyl; aldehyde; or carboxylic acid or salt thereof, provided that at least one R is a carbonyl-containing group; or (b) when X is -N(R)-: Z¹ and Z² are both -Z³- or both -(C=O)-; each Z³ independently is -(CR₂)-; and (1) when Z¹ and Z² are both -Z³-, each R independently is hydrogen; optionally inertly substituted alkyl; aldehyde; or carboxylic acid or salt thereof, provided that at least one R is a carbonyl-containing group; or (2) when both Z¹ and Z² are -(C=O)-, each R independently is hydrogen; optionally inertly substituted alkyl; aldehyde; carboxylic acid or salt thereof; or an aryl or aralkyl group containing at least one carboxylic ester, a carboxylic acid or salt thereof, ether, aldehyde, ketone or sulfoxide group. Thus, the present invention is a process for removing SO₂ from a fluid containing SO₂ by employing, as an absorbent for SO₂, an aqueous solution containing as the only SO₂-absorbent(s) one or more compounds compound represented by Formula I, II or III: wherein each Y is independently -(CR²₂)- or -(CR²)= and each R¹ or R² is independently hydrogen, an alkyl group; an hydroxyalkyl group; an aldehyde group; a carboxylic acid group or salt thereof; an alkyl group containing at least one carboxylic ester, a carboxylic acid or salt thereof, ether, aldehyde, ketone, or sulfoxide group; wherein the compound has at least one carbonyl group (a carbonyl-containing group), that is, at least one R¹ or R² comprises -(C=O)- for example as in an aldehyde-, ester-, carboxylic acid- (or salt), or ketone-containing group; wherein each R³ or R⁴ is independently hydrogen; an alkyl group; a hydroxyalkyl group; an aldehyde group; a carboxylic acid or salt group; or an alkyl, aryl, or aralkyl group containing at least one carboxylic ester, a carboxylic acid or salt, ether, aldehyde, ketones or sulfoxide group; wherein each R⁶ or R⁵ is independently hydrogen; an alkyl group; a hydroxyalkyl group; an aldehyde group; a carboxylic acid or salt group; an alkyl group containing at least one carboxylic ester, carboxylic acid or salt, ether, aldehyde, ketone or sulfoxide; and wherein at least one R⁵ or R⁶ is a carbonyl-containing group, such as an aldehyde group, a carboxylic acid containing group, a carboxyl ester group, or a ketone-containing group. In each of the possible R groups, each alkyl or aryl group is of a size or molecular weight suitable for use in absorbing sulfur dioxide, preferably in aqueous solutions. Preferably each alkyl or aryl, including the substituted groups such as hydroxyalkyl groups, have from 1 to 12 carbon atoms, more preferably, from 1 to 6 carbon atoms. Each alkyl group or alkyl portion of an aralkyl group is suitably cyclic, branched or unbranched and optionally is at least partially unsaturated (alkylene), for example vinyl or allyl groups or substituents. Each alkyl group is unsubstituted or inertly substituted, that is substituted with groups which do not interfere undesirably with use of the compounds to absorb sulfur dioxide, with solubility of the compounds in water or with regeneration of an aqueous solution of the compound after sulfur dioxide is absorbed. The groups preferably also exhibit chemical and thermal stability because the compounds often undergo repeated absorption/regeneration cycles. Exemplary of such inert substituents are hydroxyl groups; carbonyl groups including those in aldehydes, esters, acids, carboxylates and ketones; and sulfoxides. Preferred substituents, R, are those which enhance solubility in water, preferably without decreasing the capacity for absorbing SO₂, the regenerability of the compound after absorption, or the chemical and heat stability under conditions of use. Preferred substituents are generally hydrogen, formyl groups, alkyl groups and groups having at least one hydroxyl, or carboxylic acid or salt group; more preferably hydrogen, alkyl or hydroxyalkyl. When the R substituent includes a salt, the salt suitably has any counterion which allows water solubility, preferably such a metal cation, more preferably an alkali metal counterion, or mixtures thereof. Compounds of Formula I include piperidines having at least one carbonyl-containing substituent on the ring nitrogen and/or on at least one ring carbon atom; compounds wherein R¹ is other than hydrogen, more preferably a carbonyl-containing group, most preferably a formyl or carboxylate group. Formyl groups on nitrogen generally enhance regenerability, while carboxylic acids and salts generally enhance absorption of SO₂. Exemplary of compounds of Formula I are 1-formyl piperidine; ethyl piperidine-2-carboxylate; ethyl 1-piperidine propionate; 1-piperidine propionic acid; 1-piperidine carboxaldehyde; and 4-piperidine carboxaldehyde. Preferred compounds include 1-formyl piperidine and 1-piperidine propionic acid. Piperidines having carbonyl-containing substituents on the ring nitrogen are commercially available, and are prepared by methods within the skill in the art, for instance by procedures such as those taught by Jones et al. in J. Chem. Soc. , (1952), pp. 3261-3264, teaching the reaction of carbon dioxide and a pyridine to produce formyl piperidines; Hess, et al. in Chem. 50 , 385-9 (1917) teaching synthesis of 2-piperidene carboxylate by oxidation of picoline with formaldehyde; Treibs, et al. in Chem. Ber. , 89 , 51-57 (1956) teaching preparation of such compounds as 3-piperidine-propionate and methyl-2-piperidinopropionate by reaction of nitrite and bromo-substituted dicarboxylic acids via oximino and dioximino dicarboxylic acids; Drake, et al. in J. Amer. Chem. Soc. , 56 , 697-700 (1934) teaching preparation of alkyl-1-piperidinopropionate, for example by reaction of certain bromo substituted acrylic esters and piperidine; or Sternberg, et al. in J. Amer. Chem. Soc. , 75 , 3148-3152 (1953) teaching preparation of N-formyl piperidine by reacting dicobalt octacarbonyl with piperidine in the presence of a Lewis base. Piperidines having carbonyl-containing substitution on a ring carbon are commercially available and are known in the art. They are prepared by methods within the skill in the art, for instance by procedures such as those taught in US-A-2,680,116 (Trick, et al.) which teaches treatment of such compounds as dioxodialkyl-piperidines or derivatives thereof with formic acid esters followed by reduction to produce piperidine-diones; GB-A-742,733 (Roche Products, Ltd.) which teaches reaction of certain dioxodialkyltetrahydropyridines with formaldehyde and reduction to produce certain alkyltetrahydropyridinediones and alkylpiperidinediones; Shechter, et al. in J. Amer. Chem. Soc. , 73 , 3087-3091 (1951) teach preparation of certain 2-piperidones by reacting cyclopentanones with hydrazoic acid sulfuric acids. Other methods of preparing 2-piperidones are taught by Langley et al. in J. Amer. Chem. Soc , 74 ,, 2012-15 (1952) and by Horning, et al.; Ibid , pp. 2680-2681. Preferred compounds among compounds of Formula II include anhydrides produced from amine-containing acids, such as glycine anhydride, and 1,4-dimethyl-2,5-piperazinedione. Exemplary of preferred anhydrides are 2,5-piperazinedione (glycine anhydride); 1-methyl-2,5-piperazinedione; 1,4-dimethyl-2,5-piperazinedione; 1-(2-hydroxyethyl)-2,5-piperazinedione: 1,4-bis(2-hydroxyethyl)-2,5-piperazinedione; 1-(2-hydroxyethyl)-4-methyl-2,5-piperazinedione; 4-(2-hydroxyethyl)-2,5-piperazinedione; 1-aminoethyl-2,5-piperazinedione; 1-formyl-2,5-piperazinedione; 1-acetyl-2,5-piperazinedione; 1-(carboxymethyl)-2,5-piperazinedione; 1-carbethoxy-2,5-piperazinedione; 3-(2-hydroxyethyl)-2,5-piperazinedione; 3,6-bis(2-hydroxyethyl)-2,5-piperazinedione; 1-(2-hydroxyethyl)-3-methyl-2,5-piperazinedione; 3-methyl-2,5-piperazinedione; 3-formyl-2,5-piperazinedione; 1,3,4,6-tetramethyl-2,5- piperazinedione; 1-(2-hydroxyethyl)-3,3-dimethyl-2,5-piperazinedione; 1,4-bis(2-hydroxyethyl)-3,3-dimethyl-2,5-piperazinedione; 1,4-bis(2-hydroxyethyl)-3,3,6,6-tetramethyl-2,5-piperazinedione; 1-butyl-2,5-piperazinedione; 1,4-dibutyl-2,5-piperazinedione; and 3,3'-dibutyl-2,5-piperazinedione. Preferred compounds include 2,5-piperazinedione and 1,4-dimethyl-2,5-piperazinedione. Such anhydrides are commercially available and are known in the art. They are prepared by methods within the skill in the art, for instance by processes taught in Synthetic Methods of Organic Chemistry , W. Theilheimer, Vol. 13, p. 224 (1959). Preferred compounds among compounds of Formula III include piperazines having at least one carbonyl-containing substituent on the ring nitrogen and/or on at least one ring carbon atom; compounds wherein R⁵ is other than hydrogen, more preferably a carbonyl-containing group, most preferably a formyl or carboxylate group; compounds in which at least one carbonyl group is on a carbon atom within 1, more preferably adjacent to the nitrogen; compounds having more than one oxygen atom, more preferably more than one carbonyl oxygen. Formyl groups on nitrogen generally enhance regenerability, while carboxylic acids and salts generally enhance absorption of SO₂. Exemplary of the compounds of Formula III are piperazines such as ethyl-1-piperazine carboxylate; 1,4-piperazine-dicarboxylic acid; 1-succinylpiperazine; 1-formyl piperazine, 4-formylpiperazine; 1,4-diformylpiperazine; 1-formyl-2-methylpiperazine; 1-formyl-2,5-dimethylpiperazine; 1-(2-hydroxyethyl)-4-sulfoxyl piperazine; and 1-piperazine carboxylic acid. Preferred compounds include ethyl-1-piperazine carboxylate; 1,4-diformylpiperazine; and 1-succinylpiperazine. Such piperazines are commercially available and are known in the art. They are prepared by methods within the skill in the art, for instance by processes taught in Kirk-Othmer Encyclopedia of Chemical Technology , vol. 2, pp 295-299 (1978). Among compounds of Formula I, II, and III absorbent compounds having high boiling points relative to water are desirable to prevent overhead loss of the absorbent during a thermal regeneration step. The subject compounds possess a much higher boiling point than the trimethyl phosphate employed for that purpose in US-A-4,320,101. Among compounds of Formula I, II, and III preferred compounds are those which have a capacity for absorbing SO₂ which, in combination with the water solubility, is suitable for use in aqueous solutions for absorbing SO₂. The capacity for absorbing SO₂ is determined by saturating a solution of a known concentration of the absorbent in water with SO₂, for example by sparging SO₂ (preferably in a mixture simulating that found in for example smokestacks) into the solution. Sparging is continued until the solution has absorbed a maximum amount of SO₂ (saturation). Then the concentration of bisulfite (including sulfite that may be present) and bisulfate (including sulfate) ions are determined, for example using a standardized commercially available ion chromatograph unit. Such determinations are within the skill in the art and are exemplified in the Examples of this invention. Capacity is calculated as the mole ratio of absorbed SO₂ (as measured by the sum of the moles of bisulfite and bisulfate) to absorbent compound. The capacity for absorbing SO₂ is considered in combination with the water solubility of the compound because the absorbing capacity of a solution is the capacity of the absorbent multiplied by the amount of absorbent present. An arbitrary parameter CS defined as: CS = [Capacity in (moles SO₂/moles absorbent)]X(Solubility in moles absorbent/liter at 23°C) is determined for a potential absorbent. Absorbents used in the practice of the invention preferably have a CS of at least 0.05, more preferably at least 0.5, most preferably at least 0.7 moles SO₂/liter at 23°C. The compounds used in the present invention are employed in aqueous solution usually at a concentration of from 0.1 weight percent in water up to their saturation concentration in water at the temperature at which the absorber is operated. The absorbent solution, after use, is preferably thermally regenerated, for example by passing steam through the solution, and recycled to the absorption step. The absorber usually is operated at a temperature of from 0° to 120°C, but is preferably operated at a temperature of from 5° to 75°C, most preferably at from 5° to 60°C. Pressures of from atmospheric to 10 atmospheres (0 to 900 kPag) usually are employed, but 0 to 10 psig (0 to 70 kPag) is preferably and conveniently employed. Higher temperatures and pressures are not deleterious so long as they are below the decomposition conditions of the absorbent, but equipment design modifications may be required to allow for pressure and temperature resistance. Fluids being treated in the practice of this invention suitably contain any amount of SO₂ for example from one ppm (parts per million) (by volume) up to 100 volume percent, preferably from 100 ppm to 3000 ppm (by volume). The fluids are suitably in any form suitable for sufficient contact, direct or indirect, with the aqueous solution to permit absorption of SO₂. Gas, liquid, suspension and other fluid forms are suitable, but gas form is preferred. The absorbent compounds are suitably employed using any process within the skill in the art, preferably by contact (direct or indirect) with the fluid containing SO₂. Direct contact particularly contact such as flowing the fluid (preferably gas) through the aqueous solution is preferred. Other means of direct contact include contact of the aqueous solution with SO₂-containing liquid (for example under pressure), optionally with release of pressure after absorption. Indirect contact, such as through a membrane, is also suitable. Thermal regeneration of the absorbent suitably takes place at any temperature below the thermal decomposition temperature of the absorbent compound, preferably at a temperature of from 75°C to 150°C, most preferably from 90°C to 120°C, at atmospheric pressure. Reduced pressure or pressures above atmospheric are suitable, but 0 to 10 psig (0 to 70 kPag) is convenient. Regeneration at 100°C at atmospheric pressure is particularly convenient because water in the aqueous solution boils and can be refluxed while the SO₂ is released. Regenerability of an absorbent is a measure of the ability of the absorbent to release SO₂ (so that the absorbent may be reused). Regenerability is determined by measuring the bisulfate and bisulfite concentrations in a solution of known concentration of absorbent which has been saturated with SO₂ as in the determination of SO₂ absorption capacity. This solution is referred to herein as the enriched solution. Then a portion of the enriched solution is heated to strip SO₂ as a gas. For purposes of the measurement, stripping is done at the boiling point of the solution, 100°C with N₂ sparge at 0.5 SCFH (Standard cubic feet per hour) (equivalent to 4 x10⁻⁶ m³/s at 16°C) for 4 hours. During the stripping, additional water is frequently added to make up the water loss due to evaporation. A sample of this stripped solution is analyzed for bisulfite and bisulfate concentration by the same method used to analyze the concentration of the original enriched solution. The difference in combined bisulfite and bisulfate concentrations between the stripped and enriched SO₂ solution is used to calculate the percent regenerability of each solution using the equation: Percent regenerability of absorbents used in the practice of the invention is preferably at least 30, more preferably at least 50, most preferably at least 60 percent. The following examples illustrate the use of the absorbent compounds in the process of the invention. All parts, ratios and percentages are by weight unless otherwise indicated. Examples 1 - 4 For each of the absorbent compounds listed in Table 1, the amount of compound indicated in the Table was placed into a graduate cylinder and deionized water was added to bring the total volume to 70 ml (milliliters) at room temperature (23°C) to form a solution. A 5/95 volume percent mixture of SO₂ and N₂ (respectively) gases was sparged through a coarse (100-150 µm) gas dispersion tube into the solution at 2.0 standard cubic feet per hour, meaning cubic feet at 60°F(16°C) at atmospheric pressure passed per hour (SCFH) (equivalent to 1.6x10⁻⁵ m³/s at 16°C) for 4 hours to form a SO₂ enriched solution. A small sample of the SO₂ enriched solution was analyzed for bisulfite [HSO₃⁻] and bisulfate [HSO₄⁻] concentration using a standardized ion chromatograph commercially available from Dionex Corporation under the trade designation Dionex™ IC Series 4000, having a column packed with AG4/AS4 resin also commercially available from Dionex Corporation, a conductivity detector commercially available from Wescant, Corp. and a Dionex anion micro membrane suppressor commercially available from Dionex Corp. under the trade designation 8080. The sum of the bisulfite and bisulfate concentrations was used to calculate the SO₂ capacity (mole ratio of SO₂/absorbent compound) as indicated in the Table. The reported concentrations were corrected for the absorption of water in the absence of absorbent. Then, the remaining SO₂ enriched solution was transferred into a flask and heated to boil on a hot plate at 100°C with N₂ sparge (0.5 SCFH) ( 4 x10⁻⁶ m³/s at 16°C) for 4 hours to strip SO₂ as a gas. During the stripping, additional water was frequently added to make up the water loss due to evaporation. A sample of this stripped solution was analyzed for bisulfite and bisulfate concentration by the same method used to analyze the concentration of the original enriched solution. The difference in combined bisulfite and bisulfate concentration between the stripped and original (enriched) SO₂ solution was used to calculate the SO₂ percent regenerability of each solution using the equation: The CS, calculated by multiplying the capacity times the solubility in moles/l, is included in Table 1. The compounds used in Examples 1, 2 and 4 were used in concentrations less that saturation; therefore the CS reported in the table was based on concentration in place of solubility. The data in Table 1 show that absorbents preferred for use in the practice of this invention had CS values within the preferred range. Examples 5-9 The process of Example 1 was repeated except using the compounds and amounts shown in Table 2 with the results shown therein. The compounds used in Examples 5-7 are used in concentrations less than saturation; therefore, the CS reported is based on those concentrations and is less than the true CS.

Claims: A process for removing SO₂ from a fluid containing SO₂, the improvement comprising employing, as an absorbent for the SO₂, an aqueous solution containing as the only SO₂-absorbent(s) at least one compound represented by Formula A: wherein: X is -Z³- or -N(R)-; and (a) when X is -Z³-: Z¹ and Z² are both -Z³-; each Z³ independently is - (CR₂)- or -(CR)=; and each R independently is hydrogen; optionally inertly substituted alkyl; aldehyde; or carboxylic acid or salt thereof, provided that at least one R is a carbonyl-containing group; or (b) when X is -N(R)-: Z¹ and Z² are both -Z³- or both -(C=O)-; each Z³ independently is -(CR₂)-; and (1) when Z¹ and Z² are both -Z³-, each R independently is hydrogen; optionally inertly substituted alkyl; aldehyde; or carboxylic acid or salt thereof, provided that at least one R is a carbonyl-containing group; or (2) when both Z¹ and Z² are -(C=O)-, each R independently is hydrogen; optionally inertly substituted alkyl; aldehyde; carboxylic acid or salt thereof; or an aryl or aralkyl group containing at least one carboxylic ester, a carboxylic acid or salt thereof, ether, aldehyde, ketone or sulfoxide group. A process of Claim 1, wherein at least one compound of Formula A is represented by Formula I: wherein each Y is independently -(CR²₂)- or -(CR²)= and each R¹ or R² is independently hydrogen, an alkyl group; an hydroxyalkyl group; an aldehyde group; a carboxylic acid group or salt thereof; an alkyl group containing at least one carboxylic ester, a carboxylic acid or salt thereof, ether, aldehyde, ketone, or sulfoxide group; wherein the compound has at least one carbonyl group. A process of Claim 1, wherein at least one compound of Formula A is represented by Formula II: wherein each R³ or R⁴ is independently hydrogen; an alkyl group; a hydroxyalkyl group; an aldehyde group; a carboxylic acid or salt thereof; or an alkyl, aryl, or aralkyl group containing at least one carboxylic ester, a carboxylic acid or salt thereof, ether, aldehyde, ketone or sulfoxide group. A process of Claim 1, wherein at lest one compound of Formula A is represented by Formula III: wherein each R⁶ or R⁵ is independently hydrogen; an alkyl group; a hydroxyalkyl group; an aldehyde group; a carboxylic acid or salt thereof; an alkyl group containing at least one carboxylic ester, carboxylic acid or salt thereof, ether, aldehyde, ketone or sulfoxide; and wherein at least one R⁶ or R⁵ is a carbonyl-containing group. A process of any one of the preceding claims, wherein the R substituents individually are selected from hydrogen, alkyl, formyl and groups having at least one hydroxyl or carboxylic acid or salt thereof. A process of any one of the preceding claims, wherein each alkyl group or moiety has from 1 to 6 carbon atoms. A process of any one of the preceding claims, wherein said compound is a piperidine or piperazine having at least one carbonyl-containing group on the ring nitrogen. A process of Claim 7, wherein at least one R¹ or R⁵ is formyl or carboxylic acid or a salt thereof. A process of any one of the preceding claims, wherein said compound is a piperidine or piperazine having carbonyl-containing substitution on a ring carbon atom. A process of Claim 2, wherein said compound is selected from ethyl piperidine-2-carboxylate; ethyl 1-piperidine propionate; 1-piperidine propionic acid; 1-piperidine carboxaldehyde; 4-piperidine carboxaldehyde; and 1-formyl-piperidine. A process of Claim 4, wherein said compound is selected from: ethyl-1-piperazine carboxylate, 1,4-diformylpiperazine, 1-succinylpiperazine, 1-(2-hydroxyethyl)-4-sulfoxylpiperazine, 1-formylpiperazine, 1-piperazinecarboxylic acid, 1,4-piperazinedicarboxylic acid, 1-formyl-2-methylpiperazine, and 1-formyl-2,5-dimethylpiperazine. A process of Claim 3, wherein said compound is selected from: glycine anhydride, 1-methyl-2,5-piperazinedione, 1,4-dimethyl-2,5-piperazinedione, 1-(2-hydroxyethyl)-2,5-piperazinedione, 1-aminoethyl-2,5-piperazinedione, 1,4-bis(2-hydroxyethyl)-2,5-piperazinedione, 1-formyl-2,5-piperazinedione, 1,4-bis(2-hydroxyethyl)-3,3-dimethyl-2,5-piperazinedione, 1-acetyl-2,5-piperazinedione, 1-carbethoxy-2,5-piperazinedione, 1-(carboxymethyl)-2,5-piperazinedione, 3-hydroxyethyl-2,5-piperazinedione, 3,6-bis(2-hydroxyethyl)-2,5-piperazinedione, 3-methyl-2,5-piperazinedione, 3-formyl-2,5-piperazinedione, 4-(2-hydroxyethyl)-2,5-piperazinedione, 1-(2-hydroxyethyl)-3-methyl-2,5-piperazinedione, 1,3,4,6-tetramethyl-2,5-piperazinedione, 1-(2-hydroxyethyl)-3,3-dimethyl-2,5-piperazinedione, 1,4-bis(2-hydroxyethyl)-3,3,6,6-tetramethyl-2,5-piperazinedione, 1-butyl-2,5-piperazinedione, 1,4-dibutyl-2,5-piperazinedione, and 3,3'-dibutyl-2,5-piperazinedione. A process of any one of the preceding claims, wherein the aqueous solution contains a concentration of the absorbent compound of at least 0.1 weight percent; and wherein absorption of the SO₂ from the fluid is conducted at a temperature of from 0°C to 120°C. A process of any one of the preceding claims, wherein after absorption of SO₂ by the aqueous solution, SO₂ is removed from the aqueous solution by heating the solution. A process of Claim 14, wherein said solution is heated to a temperature of from 75°C to 150°C. A process of any one of the preceding claims, wherein the absorbent has a percent regenerability of at least 30 percent. A process of any one of the preceding claims, wherein the absorbent has a CS of at least 0.05. The use of an aqueous solution of a compound as defined in Claim 1 to absorb SO₂. A use as claimed in Claim 18, wherein the compound is as defined in any one of Claims 2 to 17.

Inventors: CHANG DANE, CHRISTIANSEN STEVEN H, CRUMP DRUCE K, CHANG, DANE, CHRISTIANSEN, STEVEN H., CRUMP, DRUCE K.
Applicants: DOW CHEMICAL CO, THE DOW CHEMICAL COMPANY
Application year: 1991
Main classification: B01D53
IPC codes: B01D53, C10K1