NOVEL POLYAMINES, PROCESS FOR THEIR SYNTHESIS AND THEIR USE FOR THE SELECTIVE REMOVAL OF H2S FROM A

专利摘要:
The invention relates to new polyamines of formula (I), resulting from the reaction between a polyol diglycidyl ether and piperazine: n integer between 0 and 30, R1 of different forms, R2 of formula (g5), and R2 of formula (g6) when n = 0 R6: H, alkyl radical or hydroxyalkyl C1-C6, R7: alkyl or hydroxyalkyl C1-C6, R6 and R7 can be connected to form a heterocycle at 5, 6, 7 or 8 atoms when R6 different from H, R8: H, alkyl radical or hydroxyalkyl C1-C4. The invention also relates to their method of preparation, and their use in an amine-based absorbent solution for selectively removing H2S from a gaseous effluent containing H2S and CO2.
公开号:FR3045058A1
申请号:FR1562247
申请日:2015-12-11
公开日:2017-06-16
发明作者:Bruno Delfort；Antoine Nicola；Thierry Huard；Aurelie Wender；Catherine Lefebvre；Nicolas Laloue；Karine Gaillard
申请人:IFP Energies Nouvelles IFPEN；
IPC主号:

专利说明:

Field of the invention
The present invention relates to novel nitrogen compounds belonging to the family of polyamines resulting from the reaction between a polyol diglycidyl ether and piperazine. The invention also relates to the process for synthesizing said compounds, as well as their use in a deacidification process of a gaseous effluent, such as industrial gas or natural gas.
General context
Absorption processes employing an aqueous amine solution are commonly used to remove acidic compounds, especially carbon dioxide (CO 2), hydrogen sulfide (H2S), carbon oxysulfide (COS), carbon disulfide (CS2), sulfur dioxide (SO2) and mercaptans (RSH), present in a gas. The gas is deacidified by contacting the absorbent solution in an absorption column ("absorber"), and then the absorbing solution is thermally regenerated in a regeneration column ("regenerator"). A gas depleted of acidic compounds is then produced in the absorber, and a gas rich in acidic compounds leaves the regenerator. US 6,852,144 discloses, for example, a method for removing acidic compounds from hydrocarbons. The method uses a water-N-methyldiethanolamine or water-triethanolamine absorbent solution containing a high proportion of at least one compound belonging to the following group: piperazine, methylpiperazine and morpholine.
A limitation of the absorbent solutions commonly used in deacidification applications is insufficient selectivity of H2S absorption over CO 2. In fact, in certain cases of deacidification of natural gas, selective removal of H 2 S is sought by limiting the absorption of C02 as much as possible. This constraint is particularly important for gases to be treated already containing a CO 2 content less than or equal to the desired specification. A maximum H2S absorption capacity is then sought with a maximum selectivity of H2S absorption with respect to CO 2. This selectivity makes it possible to recover an acid gas at the outlet of the regenerator having the highest possible concentration of H2S, which limits the size of the units of the sulfur chain downstream of the treatment and guarantees a better operation. In some cases, an H2S enrichment unit is needed to concentrate the acid gas in H2S. In this case, the most selective absorbing solution is also sought. The tail gas treatment units also require selective removal of H2S, which is returned upstream of the sulfur chain.
It is well known to those skilled in the art that tertiary amines or secondary amines with severe steric hindrance have a slower CO2 capture kinetics than primary amines or low-clumped secondary amines. In contrast, tertiary amines or secondary amines with severe steric hindrance have instantaneous H2S capture kinetics, which allows for selective removal of H2S based on distinct kinetic performance.
In 1950, Frazier and Kohl (Ind and Chem, 42, 2288) demonstrated that the tertiary amine N-methyldiethanolamine (MDEA) has a high degree of H2S absorption selectivity. relative to CO2, because of the distinct kinetic performance of this amine on these two gases. However, there are cases where the use of MDEA does not achieve the desired H2S absorption capacity and has insufficient selectivity. Thus, the use of MDEA for treating gases containing high partial pressures of CO 2 and H 2 S, as is the case, for example, for certain natural gases, is of limited value. The same is true when it comes to reducing the H2S contents at low partial pressures, for example in the context of refinery tail gas treatment or synthesis gas.
US Patents 4,405,581, US 4,405,582 and US 4,405,583 disclose the use of absorbent solutions based on hindered secondary amines for the selective removal of H 2 S in the presence of CO 2. US Patent 4,405,811 discloses the use of hindered tertiary aminoetheralcohols, and US 4,483,833 discloses the use of aminoalcohol and heterocyclic aminoether alcohols to remove H 2 S from a gaseous mixture comprising H 2 S and CO 2. All of these patents describe improved performances in terms of selectivity and capacity with respect to N-methyldiethanolamine. These amines have a very clear advantage over the MDEA for applications using gases with low partial pressures of acid gases. The use of these hindered amines, however, remains limited for higher acid gas pressures, as is the case in most natural gas processing applications. Absorption capacity gains can be reduced when the partial pressure of acid gas increases, especially as the temperature control in the absorber imposes a rate of acid gas load limited in the bottom of the absorber. Finally, the size of the natural gas processing units, using several hundred tons of amine, often makes the use of solvent based on these complex amines very expensive.
It is also well known to those skilled in the art that the partial neutralization of an MDEA solution by the addition of a small amount of phosphoric acid, sulfuric acid, or other acids or ammonium salts makes it possible to reduce the consumption reboiler energy for the regeneration of the amine solution, or achieves lower H2S contents in the treated gas by lowering the loading rate of acidic compounds of the regenerated amine returned to the absorber head. This type of formulation is described, for example, in patent FR 2,313,968 B1 or patent application EP 134,948 A2. EP 134 948 A2 indicates that this type of formulation makes it possible to reduce the number of trays in the absorber for a given H2S absorption specification, this reduction making it possible to limit the absorption of CO2, and therefore to improve selectivity. However, no quantification of this improvement is indicated.
On the other hand, the protonation of the amine with an acid, as for example described in EP 134,948 A2, can have a negative effect in the top of the absorber where the equilibrium approach is critical, which can in some cases to the opposite effect and lead to increase the number of trays, or increase the flow of circulating solvent (van den Brand et al, Sulfur 2002, 27-30 Oct 2002).
It is also known that the use of an organic solvent mixed with a tertiary amine or a hindered secondary amine, which may contain water, makes it possible to improve the absorption selectivity of H2S with respect to as described, for example, in patent application FR 2,485,945 or in the presentations of the Sulfinol process (Huffmaster and Nasir, Proceedings of the 74th GPA Annual Convention, Gas Treating and Sulfur Recovery, 1995, 133). The use of the organic solvent at concentrations typically between 2% and 50% (US Pat. No. 4,085,192) or between 20% and 50% (Patent Application FR 2,485,945) provides an improvement in selectivity in the case of gas pressures. high acids. This advantage is however offset by a greater co-absorption of hydrocarbons. For low acid gas pressures where the amount of organic solvent must be reduced in order to maintain a high capture level, the selectivity gain will also be reduced.
FR 2,996,464 discloses that the addition of certain organic compounds, in particular added in very small amounts, to a formulation comprising water and at least one tertiary amine or secondary hindered makes it possible to control the selectivity of the absorption during selective absorption of H2S with respect to CO2 from a gaseous effluent comprising H2S and CO2. Said organic compound, by increasing the dynamic viscosity of the aqueous solution in a controlled manner, makes it possible to improve the absorption selectivity of the H2S with respect to the CO 2. The organic compounds described are, for example, polyols, polyethers, copolymers of ethylene oxide terminated with hydrophobic units attached to the ethylene oxide groups by urethane groups, polyacrylamides partially or completely hydrolysed, polymers or copolymers comprising acrylic, methacrylic, acrylamide, acrylonitrile, N-vinylpyridine, N-vinylpyrrolidinone, N-vinylimidazole monomer units, polysaccharides. These compounds are not amines capable of reacting with the acidic compounds such as the CO 2 of the gas to be treated, as is the case with the tertiary amine or secondary amine congested with the absorbing solution.
The inventors have however discovered that the addition of organic viscosifiers has a variable effect on the absorption kinetics of CO 2 depending on the nature of the organic compound used. It thus remains difficult to predict and optimize the absorption selectivity of the H2S of a gaseous effluent containing CO 2 by an amine absorbent solution and a viscosifying organic compound solely on the basis of its viscosity.
Objectives and summary of the invention
The object of the present invention is in particular to provide compounds which can enter the amine-based absorbent solution formulations used in gas deacidification, for selective removal of H 2 S with respect to CO 2, overcoming the problems of the prior art presented above.
Novel nitrogen compounds belonging to the family of polyamines and resulting from the reaction between a polyol diglycidyl ether and piperazine can advantageously be used in the field of gas deacidification.
The inventors have demonstrated that the viscosifiers used to limit the absorption of CO 2 are not equivalent in terms of performance for their use in absorbent solution formulations for an industrial process for the selective removal of H 2 S in gas-containing gases. C02.
Unexpectedly, the inventors have demonstrated that certain compounds belonging to a family of polyamines, also called coamines in the present description, resulting from the reaction between a polyol diglycidyl ether and piperazine, and added in particular in a small amount to a polyamine. solution of tertiary amine or secondary hindered, called main amine, allowed to achieve CO2 absorption rates lower than those obtained with a solution of primary amine (tertiary or secondary hindered) identical without said coamines, or with a solution of identical main amine viscosified by a non-amine organic compound according to the prior art and of viscosity equivalent to or greater than the main amine solution mixed with the coamines.
The inventors have demonstrated that the use of the polyamines according to the general formula (I) given below, resulting from the reaction between a polyol diglycidyl ether and piperazine, makes it possible to obtain good performances in terms of capacity of Absorption of acid gases and of absorption selectivity with respect to H 2 S, in particular an adsorption selectivity with respect to H 2 S which is greater than reference amines such as MDEA, in particular by adding these polyamines in small amounts to reference amine solutions. The invention thus relates, according to a first aspect, to a compound belonging to the family of polyamines, resulting from the reaction between a polyol diglycidyl ether and piperazine, and corresponding to the following general formula (I):
in which: - n is an integer between 0 and 30, - the radical R! is selected from the following groups of sub-formulas (g1 to (g4): the group of formula (g1:
where: - x is an integer between 1 and 100, preferably between 1 and 25, - the radical R3 is indifferently a hydrogen atom, an alkyl radical or a hydroxyalkyl radical, having between 1 and 4 carbon atoms, group of formula (g2):
where y is an integer from 3 to 8, the group of formula (g3):
the group of formula (g4):
where: - v and w are integers, each between 1 and 4, with the condition that the sum of v and w is equal to 2, 3, 4 or 5, - the radical R4 is indifferently a hydroxyl group, an alkyl radical or a hydroxyalkyl radical, comprising between 1 and 4 carbon atoms, and the radical R5 is indifferently a hydrogen atom or a hydroxymethyl group (-CH2OH). the radical R2 has the following formula (g5):
in which: the radical R6 is indifferently a hydrogen atom, an alkyl radical or a hydroxyalkyl radical, comprising between 1 and 6 carbon atoms, the radical R7 is indifferently an alkyl radical or a hydroxyalkyl radical, comprising 1 and 6 carbon atoms, - the radicals R6 and R7 can be linked together by a covalent bond or a heteroatom to form a heterocycle with 5, 6, 7 or 8 atoms when the radical R6 is not an atom of hydrogen, and wherein when n is 0, the radicals R6 and R7 are connected together to form a piperazine ring, the radical R2 having the formula (g6) below:
where the R8 radical is indifferently a hydrogen atom, an alkyl radical or a hydroxyalkyl radical, having between 1 and 4 carbon atoms.
Preferably, the radicals R6 and R7 are connected to one another by a covalent bond or by a heteroatom to form a 5-, 6-, 7- or 8-membered heterocycle when the radical R6 is not a hydrogen atom.
In this case, the heterocycle may be a piperazine ring.
In particular, the radical R2 may then correspond to the formula (g6). According to a second aspect, the invention relates to a process for the synthesis of a compound of the general formula (I).
According to a first implementation, the synthesis process comprises the following reactions: a first reaction of addition or polyaddition of a diglycidyl ether of a polyol of formula (IV) with piperazine of formula (V) to form an intermediate compound of formula (VI),
(Iv)
(V) R! being defined as in the general formula (I), said piperazine being in molar excess relative to said diglycidyl ether of a polyol, - a second addition reaction of said intermediate compound of formula (VI) with monoepoxide of general formula (VII)
(VII) to produce at least one nitrogen compound according to the invention.
According to a second implementation, the synthesis process comprises the following reactions: a first reaction of addition or polyaddition of a diglycidyl ether of a polyol of formula (IV) with piperazine of formula (V) to form an intermediate compound of formula (VI),
(Iv)
(V)
(VIN) R! being defined as in the general formula (I), said diglycidyl ether of a polyol being in molar excess relative to said piperazine, - a second addition reaction of said intermediate compound of formula (VIII) with an amine of general formula (IX )
(IX) the radicals R6 and R7 being defined as in the general formula (I), to produce at least one nitrogen compound according to the invention.
In particular, the first reaction and the second reaction may be conducted in two successive steps.
Alternatively, the first reaction and the second reaction can be carried out in one step.
Preferably, the diglycidyl ether of a polyol of formula (IV) of the first reaction is chosen from the list consisting of: diglycidyl ether of ethylene glycol; diglycidyl ether of diethylene glycol; diglycidyl ether of triethylene glycol; polyethylene glycol diglycidyl ether with a molar mass of between 200 and 2000 g / mol; the diglycidyl ether copolymers of ethylene glycol and propylene glycol with a molar mass of between 200 and 2000 g / mol; diglycidyl ether of 1,3-propanediol; 1,4-butanediol diglycidyl ether; diglycidyl ether of 1,5-pentanediol and 1,6-hexanediol diglycidyl ether; diglycidyl ether of 1,8-octanediol; diglycidyl ether of neopentyl glycol; 1,4-cyclohexanedimethanol diglycidyl ether; diglycidyl ether of 1,3-cyclohexanedimethanol; diglycidyl ether of 1,2-cyclohexanedimethanol; diglycidyl ethers of glycerol; diglycidyl ethers of trimethylolethane; trimethylolpropane diglycidyl ethers; diglycidyl ethers of pentaerythritol; the diglycidyl ethers of sorbitol.
Preferably, the secondary amine of formula (IX) is chosen indifferently from the group consisting of: dimethylamine; diethylamine; 2-amino-2-methyl-1-propanol; tris (hydroxymethyl) aminomethane; morpholine; N-methylpiperazine; N-hydroxyethylpiperazine; N-2-hydroxypropylpiperazine; diethanolamine; N-methylaminoethanol.
Preferably, the monoepoxide of formula (VII) is chosen indifferently from the group consisting of: - epoxy-1,2-ethane; 1,2-epoxy propane; epoxy-1,2-butane; - glycidol. According to a third aspect, the invention relates to a selective method for H2S with respect to the CO 2 of a gaseous effluent comprising H 2 S and CO 2, in which a step of absorption of the acidic compounds is carried out by placing in contact with the gaseous effluent with an absorbent solution comprising: (a) water, (b) at least one main nitrogen compound comprising at least one tertiary amine function or a secondary amine functional group comprising two secondary carbons in position a and a nitrogen atom or at least one tertiary carbon at alpha or beta of the nitrogen atom, and (c) at least one nitrogen compound attached according to the invention or obtainable by a synthetic process according to the invention.
Preferably, the absorbent solution comprises a mass fraction of water of between 3.5% and 94.5% by weight of the absorbent solution, preferably between 39.5% and 79.5% by weight, a mass fraction of main nitrogen compound of between 5% and 95% by weight of the absorbent solution, preferably between 20 and 60% by weight, - a mass fraction of the annexed nitrogen compound of between 0.5% and 25% by weight of the absorbent solution, preferably between 1% and 10% by weight, the mass fraction of the main nitrogenous compound being greater than that of the nitrogenous compound annexed.
Preferably, the main nitrogenous compound is chosen from the group consisting of: N-methyldiethanolamine; triethanolamine; diethylmonoethanolamine; dimethylmonoethanolamine; ethyldiethanolamine; the tertiary monoalkanolamines of the family of 3-alkoxypropylamines from the list consisting of N-methyl-N- (3-methoxypropyl) -2-aminoethanol, N-methyl-N- (3-methoxypropyl) -1-amino- 2-propanol, N-methyl-N- (3-methoxypropyl) -1-amino-2-butanol, N-ethyl-N- (3-methoxypropyl) -2-aminoethanol, N-ethyl-N- ( 3-methoxypropyl) -1-amino-2-propanol, N-ethyl-N- (3-methoxypropyl) -1-amino-2-butanol, N-isopropyl-N- (3-methoxypropyl) -2-aminoethanol N-isopropyl-N- (3-methoxypropyl) -1-amino-2-propanol and N-isopropyl-N- (3-methoxypropyl) -1-amino-2-butanol; the diamines in the list consisting of 1,2-bis (2-dimethylaminoethoxy) ethane, 1,2-bis (2-diethylaminoethoxy) ethane and 1,2-bis (2-pyrolidinoethoxy) ethane; 1,3-diamino-2-propanol diamines of the list consisting of 1,3-bis (dimethylamino) -2-propanol, (1-dimethylamino-3-tert-butylamino) -2- 1,3-bis (tert-butylamino) -2-propanol, 1,3-bis (diethylamino) -2-propanol, 1,3-bis (methylamino) -2-propanol, bis (ethylmethylamino) -2-propanol, 1,3 bis (n-propylamino) -2-propanol, 1,3-bis (isopropylamino) -2-propanol, 1,3 bis (n-butylamino) -2 propanol, 1,3-bis (isobutylamino) -2-propanol, 1,3-bis (piperidino) -2-propanol, and 1,3-bis (pyrrolidino) -2-propanol, the Ν, Ν Ν'-trimethyl-N'-hydroxyethyl-1,3-diamino-2-propanol; the dihydroxyalkylamines of the list consisting of N- (2'-hydroxyethyl) -2-amino-2-methyl-1-propanol, N- (2'-hydroxypropyl) -2-amino-2-methyl-1-one propanol, N- (2'-hydroxybutyl) -2-amino-2-methyl-1-propanol, (N-methyl-N-hydroxyethyl) -3-amino-2-butanol; the diamines of the family of bis (amino-3-propyl) ether or (amino-2-ethyl) - (amino-3-propyl) ethers from the list consisting of bis (dimethylamino-3-propyl) ether, bis (diethylamino-3-propyl) -ether, (dimethylamino-2-ethyl) - (dimethylamino-3-propyl) -ether, (diethylamino-2-ethyl) - (dimethylamino-3-propyl) -ether, (dimethylamino-2-ethyl) - (diethylamino-3-propyl) -ether, (diethylamino-2-ethyl) - (diethylamino-3-propyl) -ether; the tertiary beta-hydroxylated diamines of the list consisting of 1-dimethylamino-3- (2-dimethylaminoethoxy) -2-propanol, 1,1'-oxybis [3- (dimethylamino) -2-propanol], Ν , Ν, Ν ', Ν' - (tetramethyl) -1,6-diamino-2,5-hexanediol, N, N, N ', N' - (tetramethyl) -1,7-diamino-2,6- heptanediol, N, N, N ', N' - (tetramethyl) -1,8-diamino-2,7-octanediol, N, N, N ', N' - (tetramethyl) -1,9-diamino- 2,8-nonanediol, N, N, N ', N' - (tetramethyl) -1,10-diamino-2,9-decanediol; di- (2-hydroxyalkyl) -monoamines from the list consisting of 1 - [(2-hydroxyethyl) methylamino] -2-methyl-2-propanol, 1,1 '- (methylimino) -bis- [2] 2-methyl-2-propanol], 2 - [(2-hydroxy-2-methylpropyl) amino] -2-methyl-1-propanol, 2 - [(2-hydroxy-2-methylpropyl) amino] -1- butanol, bis (2-hydroxy-2-methylpropyl) amine; the congested tertiary 4- (aminoethyl) -morpholines of the list consisting of 1- (4-morpholino) -2- (methylisopropylamino) -ethane, 1- (4-morpholino) -2- (methyltertiobutylamino) -ethane, 1- (4-morpholino) -2- (diisopropylamino) ethane, 1- (4-morpholino) -2- (1-piperidinyl) ethane; the diamines in the list consisting of (N-morpholinoethyl) isopropylamine, (N-piperidinoethyl) isopropylamine, (N-morpholinoethyl) tert-butylamine; the amines of the family of N-alkyl-3-hydroxypiperidines and N-alkyl-4-hydroxypiperidines of the list consisting of N-methyl-4-hydroxy-piperidine, N-ethyl-3-hydroxypiperidine, N-methyl-3-hydroxypiperidines; methyl-3-hydroxy-piperidine; the alkylaminopiperazines which are 1-methyl-4- (3-dimethylaminopropyl) -piperazine, 1-ethyl-4- (diethylaminoethyl) -piperazine.
The absorbent solution may further comprise a physical solvent selected from the group consisting of methanol, ethanol, 2-ethoxyethanol, benzyl alcohol, triethyleneglycoldimethylether, tetraethyleneglycoldimethylether, pentaethyleneglycoldimethylether, hexaethyleneglycoldimethylether, Γheptaethyleneglycoldimethylether, octaethyleneglycoldimethylether, diethylene glycol butoxyacetate, glycerol triacetate, sulfolane, N-methylpyrrolidone, N-methylmorpholin-3-one, Ν, Ν-dimethylformamide, N-formyl-morpholine, N, N-dimethyl imidazolidin-2-one, N-methylimidazole, ethylene glycol, diethylene glycol, triethylene glycol, thiodiglycol, and tributyl phosphate, propylene carbonate. The gaseous effluent may be chosen from natural gas, synthesis gases, refinery gases, acid gases from an amine unit, gases from a Claus tail reduction unit, gases of biomass fermentation. Other objects and advantages of the invention will appear on reading the following description of examples of particular embodiments of the invention, given by way of non-limiting examples, the description also making reference to the appended FIG. -after.
Brief description of the figure
FIG. 1 represents a schematic diagram of the implementation of an acid gas treatment process.
FIG. 2 illustrates a process for synthesizing a compound according to the invention according to a first implementation.
FIG. 3 illustrates a process for synthesizing a compound according to the invention according to a second implementation.
In the figures illustrating the preparation of the nitrogen compounds according to the invention, the arrows represent reaction stages. These are reaction schemes. The illustrations of the synthesis method according to the invention do not include all the components necessary for its implementation. Only the elements necessary for the understanding of the invention are represented therein, those skilled in the art being able to complete this representation to implement the invention.
Detailed description of the invention
The novel nitrogen compounds according to the invention are polyamines resulting from the reaction between a polyol diglycidyl ether and piperazine, and correspond to the following general formula (I): in which: n is an integer between 0 and 30, the radical R! is selected from the following groups of sub-formulas (g1 to (g4): • the group of formula (g1:
where: x is an integer between 1 and 100, preferably between 1 and 25, and the radical R3 is chosen indifferently from a hydrogen atom, an alkyl radical containing between 1 and 4 carbon atoms, and a hydroxyalkyl radical comprising between 1 and 4 carbon atoms. The group of formula (g2):
, where y is an integer between 3 and 8 • the group of formula (g3):
• the group of formula (g4):
where: v and w are integers, each in the range of 1 to 4, with the proviso that the sum of v and w is 2, 3, 4 or 5, the radical R4 is selected indifferently from a hydroxyl group, an alkyl radical containing between 1 and 4 carbon atoms, and a hydroxyalkyl radical containing between 1 and 4 carbon atoms, and the radical R5 is chosen indifferently from a hydrogen atom and a hydroxymethyl group (-CH2OH). the radical R2 has the following formula (g5): in which:
the radical R 6 is chosen indifferently from a hydrogen atom, an alkyl radical comprising between 1 and 6 carbon atoms, and a hydroxyalkyl radical containing between 1 and 6 carbon atoms, the radical R 7 is chosen indifferently from an alkyl radical containing between 1 and 6 carbon atoms, and a hydroxyalkyl radical having between 1 and 6 carbon atoms, and the radicals R6 and R7 can be linked together by a covalent bond or a heteroatom to form a heterocycle with 5, 6, 7 or 8 atoms when the radical R6 is not a hydrogen atom.
When the heterocycle is a piperazine ring, the radical R2 may be of formula (g6) below:
with the radical R8 chosen indifferently from a hydrogen atom, an alkyl radical containing between 1 and 4 carbon atoms, and a hydroxyalkyl radical containing between 1 and 4 carbon atoms.
In the general formula (I), when n is 0, the radicals R6 and R7 are connected together to form a piperazine ring. In this case, the radical R2 has the formula (g6) above.
According to the form taken by the radical R2, the general formula (I) can be written more precisely according to one of the formulas (II) and (III) below: in which the radical R2 corresponds to the formula (g6) above. wherein R2 is of formula (g5) above.
Synthesis of a compound according to the invention
The nitrogen compounds according to the general formula (I) can be synthesized according to any route permitted by organic chemistry.
Advantageously, the synthesis of the compounds of the invention is based on a first addition or polyaddition reaction between a diglycidyl ether of a polyol of formula (IV) below:
(iv), and piperazine of formula (V) below:
(V)
This reaction leads to the following pattern (-X-):
(-X-)
According to the relative amounts of piperazine and the polyol diglycidyl ether used, two main modes of synthesis allow the preparation of the compounds according to the general formula (I).
The polyol diglycidyl ether may be chosen from the list of compounds consisting of: diglycidyl ether of ethylene glycol; diglycidyl ether of diethylene glycol; diglycidyl ether of triethylene glycol; polyethylene glycol diglycidyl ether with a molar mass of between 200 and 2000 g / mol; the diglycidyl ether copolymers of ethylene glycol and propylene glycol with a molar mass of between 200 and 2000 g / mol; diglycidyl ether of 1,3-propanediol; 1,4-butanediol diglycidyl ether; diglycidyl ether of 1,5-pentanediol and 1,6-hexanediol diglycidyl ether; diglycidyl ether of 1,8-octanediol; diglycidyl ether of neopentyl glycol; 1,4-cyclohexanedimethanol diglycidyl ether; diglycidyl ether of 1,3-cyclohexanedimethanol; diglycidyl ether of 1,2-cyclohexanedimethanol; diglycidyl ethers of glycerol; diglycidyl ethers of trimethylolethane; trimethylolpropane diglycidyl ethers; diglycidyl ethers of pentaerythritol; the diglycidyl ethers of sorbitol.
Synthesis of a compound according to the invention according to a first mode: synthesis routes A1 and A2 (FIG. 2)
FIG. 2 illustrates a first mode of synthesis of the compounds according to the invention, in which a molar excess of piperazine with respect to the diglycidylether of polyol is implemented.
According to this embodiment, a first reaction is carried out which is an addition or polyaddition reaction of the diglycidyl ether of a polyol of formula (IV) with a molar excess of piperazine. In this case, the unit (-X-) may be flanked by piperazine chain ends, which leads to the following general formula (VI):
(VI)
Ri and n are defined as above in relation to the general formula (I).
By molar excess of piperazine with respect to the polyol diglycidyl ether is meant the excess which makes it possible to guarantee the obtaining of the structure (VI). a second reaction which is an addition reaction between the compound of formula (VI) and a monoepoxide of general formula (VII) below makes it possible to obtain a compound according to the invention corresponding to general formula (I).
In formula (VII), the radical R8 is defined as above in relation to the general formula (g6).
This monoepoxide may be chosen for example, without being limiting, from epoxy-1,2-ethane, epoxy-1,2-propane, epoxy-1,2-butane or glycidol.
(VII ·)
According to this first mode, the synthesis can be carried out in two steps (synthetic route A1 in FIG. 2) or in one step (synthetic route A2 in FIG. 2). According to the A2 route, a single step is carried out in which the polyol diglycidyl ether, the piperazine and the monoaddition product of the monoepoxide of formula (VII) are reacted simultaneously with piperazine, which has the formula (VII) below, to lead to the nitrogen compound according to the general formula (I).
Synthesis of a compound according to the invention according to a second mode: synthesis routes B1 and B2 (FIG. 3):
FIG. 3 illustrates a second mode of synthesis of the compounds according to the invention, in which a molar excess of polyol diglycidyl ether relative to piperazine is used.
According to this embodiment, a first reaction is carried out which is an addition or polyaddition reaction of piperazine with a molar excess of a diglycidyl ether of a polyol of formula (IV). In this case, the (-X-) motif can be flanked by glycidyl chain ends, which leads to the following general formula (VIN):
(WINE)
Ri and n are defined as above in relation to the general formula (I).
The molar excess of the polyol diglycidyl ether relative to piperazine means the excess which makes it possible to guarantee the obtaining of the structure (VIII). a second reaction which is an addition reaction between the compound of formula (VIII) and an amine of general formula (IX) below makes it possible to obtain a compound according to the invention corresponding to general formula (I).
(IX)
In the formula (IX), the radicals R6 and R7 are defined as above in relation to the general formula (I).
This amine may be chosen for example, without being limiting, from dimethylamine, diethylamine, 2-amino-2-methyl-1-propanol, tris (hydroxymethyl) aminomethane, morpholine, N-methylpiperazine, N-methylpiperazine, hydroxyethylpiperazine, N-2-hydroxypropylpiperazine, diethanolamine, N-methylaminoethanol.
According to this second embodiment, the synthesis can be carried out in two steps (synthetic route B1 in FIG. 3) or in one step (synthetic route B2 in FIG. 3). According to the route B2, a single step is carried out in which the polyol diglycidyl ether, the piperazine and the amine of general formula (IX) are simultaneously reacted to yield the nitrogen compound according to the general formula (I).
The steps of the various modes of synthesis are carried out under suitable conditions allowing the described reactions, that is to say the conditions allowing the realization of said chemical reaction, generally comprising a given reaction medium and given operating conditions (reaction time For example, the reaction between the polyol diglycidyl ether of formula (IV) and piperazine is preferably carried out at a temperature between 0 ° C and 140 ° C, for example between room temperature. and 140 ° C, for example at 100 ° C. Other steps aimed for example at eliminating certain undesired compounds, such as filtration or distillation steps, may also be carried out in the various synthesis routes described without departing from the scope of the present invention.
Use of the compounds according to the invention in the treatment of gaseous effluents
The compounds according to the invention can be used in various fields of chemistry, and can be advantageously used in the field of the treatment of industrial gas and natural gas.
The present invention proposes to carry out a selective removal of the H2S with respect to the CO2 of a gaseous effluent comprising H2S and CO2, by implementing an aqueous solution comprising a main amine and at least one nitrogen compound according to the general formula (I). The solution is contacted with the gaseous effluent to selectively remove the H2S it contains. The use of the polyamines according to the invention makes it possible, in combination with a tertiary tertiary or hindered secondary amine, to obtain good performances in terms of selectivity of H2S absorption relative to CO 2, in particular greater selectivity than with aqueous solutions of reference amines such as N-methyldiethanolamine (MDEA), for a cyclic capacity for absorption of acid gases, in particular H 2 S, which is equivalent or greater.
The method comprises a step of absorbing the acidic compounds by contacting the gaseous effluent with an absorbent solution comprising: (a) water, (b) at least one main nitrogen compound comprising at least one tertiary amine function or a secondary amine function comprising two secondary carbons in position a and a 'of the nitrogen atom or at least one tertiary carbon in alpha or beta of the nitrogen atom, and (c) at least one nitrogen compound annex according to general formula (I).
Reference will also be made to the expression "secondary hindered amine function" to designate a secondary amine function of a nitrogen compound, comprising two secondary carbons in position a and a 'of the nitrogen atom or at least one tertiary carbon in alpha or beta of the nitrogen atom.
A tertiary carbon will be defined as a carbon atom bonded to three carbon atoms, and a secondary carbon as a carbon atom bonded to two carbon atoms.
The main nitrogenous compound, or main amine, is understood to mean the nitrogenous compound, comprising at least one tertiary amine function or a hindered secondary amine function and not satisfying the general formula (I). The mass concentration of the main compound in the absorbent solution is greater than that of the nitrogen compound according to the general formula (I). It is understood that in the case where there are several nitrogen compounds, main and / or annexes, it is the total mass concentration of said main nitrogen compounds which is greater than the mass concentration (total) of nitrogen compound (s). (s) annex (s).
The term "nitrogen-containing compound" is understood to mean the polyamine corresponding to the general formula (I), obtained by reaction between a polyol diglycidyl ether and piperazine as described above. The nitrogen compound annexed according to general formula (I) is also called coamine in the present description. The annexed nitrogen compound has a total mass concentration lower than that of the main nitrogen compound, and has a viscosifying effect, that is to say that it has the effect of increasing the dynamic viscosity of the absorbent solution compared with the same one. solution without said nitrogen compound annexed. The addition of coamines, in particular in small amounts, in an aqueous absorbing solution of a main amine as defined above, makes it possible to limit the absorption of CO 2, more precisely the rate of absorption of CO 2, during bringing it into contact with the gas to be deacidified, and thus improving the selective removal of H2S with respect to CO2.
Composition of the absorbent solution
The absorbent solution preferably comprises: - a mass fraction of coamine of general formula (I) of between 0.5% and 25% by weight of the absorbent solution, preferably between 1% and 10% by weight, - a mass fraction of main amine of between 5% and 95% by weight of the absorbent solution, preferably between 20 and 60% by weight, - a mass fraction of water of between 3.5% and 94.5% by weight of the absorbent solution, preferably between 39.5% and 79.5% by weight, the mass fraction of the main amine being greater than that of the polyamines of general formula (I).
If the absorbing solution comprises several main amines, and / or several coamines, the concentration ranges given refer to the total concentration of primary amines and the total concentration of coamines.
The concentration ranges given are included limits.
Unless otherwise indicated, the concentrations of the various compounds are expressed as percentages by weight of the absorbent solution in the present description.
The sum of the mass fractions expressed in% by weight of the various compounds of the absorbent solution is equal to 100% by weight of the absorbent solution.
Preferably, the main nitrogenous compound is chosen from the group consisting of: N-methyldiethanolamine; triethanolamine; diethylmonoethanolamine; dimethylmonoethanolamine; ethyldiethanolamine; the tertiary monoalkanolamines of the family of 3-alkoxypropylamines from the list consisting of N-methyl-N- (3-methoxypropyl) -2-aminoethanol, N-methyl-N- (3-methoxypropyl) -1-amino- 2-propanol, N-methyl-N- (3-methoxypropyl) -1-amino-2-butanol, N-ethyl-N- (3-methoxypropyl) -2-aminoethanol, N-ethyl-N- ( 3-methoxypropyl) -1-amino-2-propanol, N-ethyl-N- (3-methoxypropyl) -1-amino-2-butanol, N-isopropyl-N- (3-methoxypropyl) -2-aminoethanol N-isopropyl-N- (3-methoxypropyl) -1-amino-2-propanol and N-isopropyl-N- (3-methoxypropyl) -1-amino-2-butanol; the diamines in the list consisting of 1,2-bis (2-dimethylaminoethoxy) ethane, 1,2-bis (2-diethylaminoethoxy) ethane and 1,2-bis (2-pyrolidinoethoxy) ethane; 1,3-diamino-2-propanol diamines of the list consisting of 1,3-bis (dimethylamino) -2-propanol, (1-dimethylamino-3-tert-butylamino) -2- 1,3-bis (tert-butylamino) -2-propanol, 1,3-bis (diethylamino) -2-propanol, 1,3-bis (methylamino) -2-propanol, bis (ethylmethylamino) -2-propanol, 1,3 bis (n-propylamino) -2-propanol, 1,3-bis (isopropylamino) -2-propanol, 1,3 bis (n-butylamino) -2 propanol, 1,3-bis (isobutylamino) -2-propanol, 1,3-bis (piperidino) -2-propanol, and 1,3-bis (pyrrolidino) -2-propanol, the Ν, Ν Ν'-trimethyl-N'-hydroxyethyl-1,3-diamino-2-propanol; the dihydroxyalkylamines of the list consisting of N- (2'-hydroxyethyl) -2-amino-2-methyl-1-propanol, N- (2'-hydroxypropyl) -2-amino-2-methyl-1-one propanol, N- (2'-hydroxybutyl) -2-amino-2-methyl-1-propanol, (N-methyl-N-hydroxyethyl) -3-amino-2-butanol; the diamines of the family of bis (amino-3-propyl) ether or (amino-2-ethyl) - (amino-3-propyl) ethers from the list consisting of bis (dimethylamino-3-propyl) ether, bis (diethylamino-3-propyl) -ether, (dimethylamino-2-ethyl) - (dimethylamino-3-propyl) -ether, (diethylamino-2-ethyl) - (dimethylamino-3-propyl) -ether, (dimethylamino-2-ethyl) - (diethylamino-3-propyl) -ether, (diethylamino-2-ethyl) - (diethylamino-3-propyl) -ether; the tertiary beta-hydroxylated diamines of the list consisting of 1-dimethylamino-3- (2-dimethylaminoethoxy) -2-propanol, 1,1'-oxybis [3- (dimethylamino) -2-propanol], Ν , Ν, Ν ', Ν' - (tetramethyl) -1,6-diamino-2,5-hexanediol, N, N, N ', N' - (tetramethyl) -1,7-diamino-2,6- heptanediol, N, N, N ', N' - (tetramethyl) -1,8-diamino-2,7-octanediol, N, N, N ', N' - (tetramethyl) -1,9-diamino- 2,8-nonanediol, N, N, N ', N' - (tetramethyl) -1,10-diamino-2,9-decanediol; di- (2-hydroxyalkyl) -monoamines from the list consisting of 1 - [(2-hydroxyethyl) methylamino] -2-methyl-2-propanol, 1,1 '- (methylimino) -bis- [2 2-methyl-2-propanol], 2 - [(2-hydroxy-2-methylpropyl) amino] -2-methyl-1-propanol, 2 - [(2-hydroxy-2-methylpropyl) amino] -1- butanol, bis (2-hydroxy-2-methylpropyl) amine; the congested tertiary 4- (aminoethyl) -morpholines of the list consisting of 1- (4-morpholino) -2- (methylisopropylamino) -ethane, 1- (4-morpholino) -2- (methyltertiobutylamino) -ethane, 1- (4-morpholino) -2- (diisopropylamino) ethane, 1- (4-morpholino) -2- (1-piperidinyl) ethane; the diamines in the list consisting of (N-morpholinoethyl) isopropylamine, (N-piperidinoethyl) isopropylamine, (N-morpholinoethyl) tert-butylamine; the amines of the family of N-alkyl-3-hydroxypiperidines and N-alkyl-4-hydroxypiperidines of the list consisting of N-methyl-4-hydroxy-piperidine, N-ethyl-3-hydroxypiperidine, N-methyl-3-hydroxypiperidines; methyl-3-hydroxy-piperidine; the alkylaminopiperazines which are 1-methyl-4- (3-dimethylaminopropyl) -piperazine, 1-ethyl-4- (diethylaminoethyl) -piperazine.
According to one embodiment, the absorbent solution may contain organic compounds that are non-reactive with respect to acidic compounds (commonly called "physical solvents"), which make it possible to increase the solubility of at least one or more acidic compounds of the gaseous effluent. For example, the absorbent solution may comprise between 5% and 50% by weight of physical solvent such as alcohols, ethers, ether alcohols, glycol ethers and polyethylene glycol ethers, glycol thioethers, glycol esters and alkoxy esters, and the like. polyethylene glycol, glycerol esters, lactones, lactams, N-alkylated pyrrolidones, morpholine derivatives, morpholin-3-one, imidazoles and imidazolidinones, N-alkylated piperidones, cyclotetramethylenesulfones, N-alkylated alkylformamides, N-alkylacetamides, ether ketones of alkyl carbonates or alkyl phosphates and their derivatives. By way of example and without limitation, it may be methanol, ethanol, 2-ethoxyethanol, benzyl alcohol, triethyleneglycoldimethylether, tetraethyleneglycoldimethylether, pentaethyleneglycoldimethylether, hexaethyleneglycoldimethylether, Heptaethyleneglycoldimethylether, octaethyleneglycoldimethylether, diethylene glycol butoxyacetate, glycerol triacetate, sulfolane, N-methylpyrrolidone, N-methylmorpholin-3-one, N, N-dimethylformamide, N-formyl morpholine, N, N-dimethyl-imidazolidin-2-one, N-methylimidazole, ethylene glycol, diethylene glycol, triethylene glycol, thiodiglycol, propylene carbonate, tributyl phosphate.
Nature of gaseous effluents
Absorbent solutions comprising at least one nitrogen compound according to the invention can be used to deacidify the following gaseous effluents: natural gas, synthesis gases, refinery gases, acid gases from an amine unit, gases from a tail reduction unit of the Claus process, the biomass fermentation gases. These gaseous effluents contain one or more of the following acidic compounds: CO2, H2S, mercaptans (for example methyl mercaptan (CH3SH), ethyl mercaptan (CH3CH2SH), propyl mercaptan (CH3CH2CH2SH)), COS, CS2, the S02.
The deacidification process using the compounds according to the invention may for example be used to deacidify a synthesis gas. The synthesis gas contains carbon monoxide CO, hydrogen H 2 (generally in a H 2 / CO ratio equal to 2), water vapor (generally at saturation at the temperature at which washing is performed) and C02 (of the order of ten percent). The pressure is generally between 20 and 30 bar, but can reach up to 70 bar. It may contain, in addition, sulfur impurities (H2S, COS, etc.), nitrogen (NH3, HCN) and halogenated impurities.
The deacidification process using the compounds according to the invention can also be used to deacidify a natural gas. Natural gas consists mainly of gaseous hydrocarbons, but can contain several of the following acidic compounds: CO2, H2S, mercaptans, COS, CS2. The content of these acidic compounds is very variable and can be up to 70% by volume for CO2 and up to 40% by volume for H2S. The temperature of the natural gas can be between 20 ° C and 100 ° C. The pressure of the natural gas to be treated may be between 10 and 200 bar. The invention can be implemented to achieve specifications generally imposed on the deacidified gas, which are less than 2% of CO2, less than 4 ppm of H2S, and less than 50 ppm, or even less than 10 ppm, volume of total sulfur.
Process for removing acidic compounds in a gaseous effluent
The method for selectively removing H2S from a gaseous effluent containing CO 2 comprises a step of absorbing the acidic compounds H 2 S and CO 2 by contacting the gaseous effluent with an absorbent solution according to the invention. 'invention.
With reference to FIG. 1, the absorption step consists of bringing the gaseous effluent 1 into contact with the absorbent solution 4. The gaseous effluent 1 is introduced at the bottom of the absorption column C1, the absorbing solution is introduced at the head of column C1. Column C1 is provided with gas-liquid contacting means, for example loose packing, structured packing or distillation trays. During contact, the amine functions of the molecules of the absorbent solution react with the acidic compounds contained in the effluent, so as to obtain a gaseous effluent depleted in acidic compounds 2, in particular depleted in H2S and CO2, and discharged at the top of the C1 column, and an absorbent solution enriched in these same acidic compounds 3 discharged at the bottom of column C1, to be preferably regenerated. The selective absorption step of the H 2 S can be carried out at a pressure in the absorption column C1 of between 1 bar and 200 bar, preferably between 20 bar and 100 bar for the treatment of a natural gas, and at a temperature in the absorption column C1 of between 20 ° C. and 100 ° C., preferably between 30 ° C. and 90 ° C., or even between 30 ° C. and 60 ° C. The use of a nitrogen compound according to general formula (I), added to the aqueous solution comprising the tertiary amines or secondary hindered according to the invention makes it possible to obtain a selectivity of absorption of H2S vis-a-vis CO2 greater than that reached with solutions comprising the same amines without the nitrogen compound according to the general formula (I). The increase in the dynamic viscosity generated by the addition of the compound according to the invention has the effect of reducing the absorption of CO 2 relative to that of H2S, much more efficiently than by adding a compound viscosifier according to the prior art. The absorption step may be followed by a regeneration step of the acid-enriched absorbent solution, for example as shown diagrammatically in FIG. 1. The regeneration step notably consists in heating and, optionally, relaxing, the absorbent solution enriched in acidic compounds to release the acidic compounds in gaseous form. The absorbent solution enriched in acidic compounds 3 is introduced into the heat exchanger E1, where it is heated by the stream 6 from the regeneration column C2. The heated solution at the outlet of the exchanger E1 is introduced into the regeneration column C2.
The regeneration column C2 is equipped with internal contacting between gas and liquid, for example trays, loose or structured packings. The bottom of column C2 is equipped with a reboiler R1 which provides the heat necessary for regeneration by vaporizing a fraction of the absorbent solution. In the column C2, under the effect of contacting the absorbent solution 5 with the vapor produced by the reboiler, the acid compounds are released in gaseous form and discharged at the top of the column C2 via the line 7. The solution regenerated absorbent 6, that is to say depleted in acidic compounds, is cooled in the exchanger E1. The cooled solution 4 is then recycled to the absorption column C1. The regeneration step of the process according to the invention can be carried out by thermal regeneration, optionally supplemented by one or more expansion steps. For example, the absorbent solution enriched in acidic compounds 3 can be sent to a first expansion tank (not shown) before it passes through the heat exchanger E1. In the case of a natural gas, the expansion makes it possible to obtain a gas evacuated at the top of the flask containing most of the aliphatic hydrocarbons co-absorbed by the absorbing solution. This gas may optionally be washed with a fraction of the regenerated absorbent solution and the gas thus obtained may be used as a fuel gas. The expansion flask preferably operates at a pressure lower than that of the absorption column C1 and greater than that of the regeneration column C2. This pressure is generally set by the conditions of use of the fuel gas, and is typically of the order of 5 to 15 bar. The expansion flask operates at a temperature substantially identical to that of the absorbent solution obtained at the bottom of the absorption column C1.
The regeneration can be carried out at a pressure in the column C2 of between 1 bar and 5 bar, or even up to 10 bar and at a temperature in the column C2 of between 100 ° C. and 180 ° C., preferably between 110 ° C. C and 170 ° C, more preferably between 110 ° C and 140 ° C. Preferably, the regeneration temperature in the regeneration column C2 is between 155 ° C. and 180 ° C. in the case where it is desired to reinject the acid gases. Preferably, the regeneration temperature in the regeneration column C2 is between 115 ° C. and 130 ° C. in the cases where the acidic Ga is sent to the atmosphere or in a downstream treatment process, such as a Claus process or a tail gas treatment process.
Advantageously, the process according to the invention makes it possible to reduce the energy requirements for the regeneration of the absorbing solution, insofar as the improvement of the selectivity decreases the amount of CO 2 captured, the heat of absorption of CO 2 being generally between 50 and 80 kJ / mole.
Examples
In the following examples, the term "product according to the invention" refers to any compound or mixture of compounds according to the invention.
The examples below illustrate, in a non-limiting manner, the synthesis of the compounds according to the invention (Examples 1 to 5), as well as some of the performances of these compounds when they are used in aqueous solution for the selective elimination of H2S with respect to CO2 contained in a gaseous effluent by contacting the gaseous effluent with the solution.
EXAMPLE 1 Synthesis of Product A According to the Invention 40.0 g of a polyethylene glycol diglycidyl ether of average molar mass of 400 g / mol are reacted with 11.0 g of piperazine at 100 ° C. for 5 hours, then at 50 ° C., the medium is diluted with 50.0 g of ethanol. After returning to ambient temperature, 7.6 g of epoxy-1,2-propane are introduced, and the reaction is then continued with stirring for 2 hours at room temperature. After evaporation under reduced pressure of the excess of epoxy-1,2-propane and ethanol, 54.0 g of a very viscous product are obtained, the product A, whose concentration in amine functions is estimated at 4.7 mol / kg of product A. The amine concentration is estimated on the basis of the material balance.
EXAMPLE 2 Synthesis of Product B According to the Invention To 40.0 g of a polyethylene glycol diglycidyl ether with an average molar mass of 400 g / mol, 9.65 g of piperazine are reacted at 100 ° C. for 5 hours, then at 50 ° C., the medium is diluted with 50.0 g of ethanol. After returning to ambient temperature, 5.8 g of epoxy-1,2-propane are introduced and the reaction is continued with stirring for 2 hours at room temperature. After evaporation under reduced pressure of the excess of epoxy-1,2-propane and ethanol, 52.0 g of a very viscous product are obtained, the product B, the concentration of which in function amines is estimated at 4.3 moles / kg of product B. The amine concentration is estimated on the basis of the material balance.
EXAMPLE 3 Synthesis of Product C According to the Invention To 40.0 g of a polyethylene glycol diglycidyl ether having an average molar mass of 400 g / mol, 8.0 g of piperazine are reacted at 100 ° C. for 5 hours, then at 50 ° C., the medium is diluted with 50.0 g of ethanol. After returning to ambient temperature, 5.0 g of epoxy-1,2-propane is introduced and the reaction is continued with stirring for 2 hours at room temperature. After evaporation under reduced pressure of the excess of epoxy-1,2-propane and ethanol, 49.3 g of a highly viscous product are obtained, the product C, whose concentration in amines function is estimated at 3.8 moles / kg of product C. The amine concentration is estimated on the basis of the material balance.
EXAMPLE 4 Synthesis of Product D According to the Invention To 35.6 g of a polyethylene glycol diglycidyl ether having an average molar mass of 400 g / mole, 7.5 g of piperazine are reacted at 100 ° C. for 5 hours, then at 50 ° C., the medium is diluted with 50.0 g of ethanol. After returning to ambient temperature, 3.2 g of epoxy-1,2-propane are introduced and the reaction is continued with stirring for 2 hours at room temperature. After evaporation under reduced pressure of the excess of epoxy-1,2-propane and ethanol, 48.2 g of a very viscous product are obtained, the product D, whose concentration in amines function is estimated at 3.6 moles / kg of product D. The amine concentration is estimated on the basis of the material balance.
EXAMPLE 5 Synthesis of Product E According to the Invention 40.0 g of a 1,4-butanediol diglycidyl ether whose epoxide number is between 120 and 130 g / epoxide equivalent are reacted with 14.4. g of piperazine at 100 ° C. for 5 hours, then at 50 ° C. the medium is diluted with 50.0 g of etharol. After returning to ambient temperature, 5.5 g of epoxy-1,2-propane are then introduced and the reaction is continued with stirring for 2 hours at room temperature. After evaporation under reduced pressure of the excess of epoxy-1,2-propane and ethanol, 53.5 g of a highly viscous product are obtained, the product E, the concentration of which in function amines is estimated at 6.3 moles / kg of product E. The amine concentration is estimated on the basis of the material balance.
Example 6: rate of absorption of CO an amine formulation for a selective absorption process
Comparative CO 2 absorption tests are carried out by different absorbent solutions: an aqueous solution of 45.75% by weight of N-methyldiethanolamine (MDEA) MDEA, which constitutes a reference absorbent solution for a selective elimination in gas treatment ; an aqueous solution of MDEA at 45.75% by weight containing 5% by weight of polyethylene glycol (PEG) with a molecular weight of 35 000 g / mol, which is a viscosifying compound described in document FR 2 996 464. an aqueous solution of MDEA at 45.degree. , 00% weight containing 10% by weight of the product B according to the invention. an aqueous solution of MDEA at 45.75% by weight containing 5% by weight of the product C according to the invention.
For each test, the CO 2 absorption flux is measured by the aqueous absorbent solution in a closed reactor, of the Lewis cell type. 200 g of solution are introduced into the closed reactor, regulated at a temperature of 45 ° C. Four successive injections of CO 2 of 100 to 200 mbar are carried out in the vapor phase of the reactor having a volume of 200 cm 3. The gas phase and the liquid phase are respectively agitated at 100 revolutions / minute and at 120 revolutions / minute, and are entirely characterized from the hydrodynamic point of view. For each injection, the rate of absorption of CO 2 is measured by variation of pressure in the gas phase. An overall transfer coefficient Kg is thus determined by an average of the results obtained on the four injections.
The results obtained are shown in Table 1 below in relative absorption rate relative to the reference aqueous absorbent solution comprising 45.75% by weight of MDEA. The relative absorption rate is defined by the ratio of the overall transfer coefficient of the absorbent solution tested to the overall transfer coefficient of the reference absorbent solution (with MDEA).
The dynamic viscosity of the various amine solutions at 45 ° C. is obtained using an automatic viscometer of the LOVIS 2000M type from Anton Paar, operating according to the principle of the Hoepler viscometer. The viscosity is deduced from the measurement of the falling time of a steel ball in a 1.59 mm diameter capillary (main range from 1 to 20 mPa.s, extended range from 0.3 to 90 mPa.s) inclined at various angles according to DIN 53015 and ISO 12058, as well as the density measurement of amine solutions obtained on an Anton Paar DMA 4100 densimeter at 45 ° C.
Table 1 The examination of the results shows for the formulation according to the invention a rate of absorption of CO 2 slower than the reference formulation.
It is also noted that the addition of product B or product C respectively to a solution of MDEA, respectively at 45.0% by weight and 45.75% by weight of MDEA, decreases the CO2 absorption kinetics by 42%, respectively 31%, compared to 27% with the addition of 35,000 PEG at 5% weight according to the teaching of the prior art. This result is all the more surprising that in the case of the formulation according to the prior art, the viscosity is higher and the concentration of amine functions is lower than in the formulation according to the invention.
It therefore appears that the products B and C exemplified according to the invention are surprisingly of particular interest and improved in the case of a selective deacidification of a gaseous effluent in which it is sought to limit the absorption kinetics of CO 2.
Example 7 Absorption Capacity of LLS of MDEA Formulations and Product C for an Acid Gas Process.
The performance of the absorption capacity of the H2S at 40 ° C. of an aqueous solution of MDEA and of product A according to the invention, containing 45.75% by weight of MDEA and 5% by weight of product C, is compared with those of an aqueous solution of MDEA containing 50% by weight of MDEA which constitutes a reference absorbent solution for the deacidification of gas containing H2S.
An absorption test at 40 ° C is carried out on aqueous amine solutions in a thermostatic equilibrium cell. This test consists in injecting into the equilibrium cell, previously filled with degassed aqueous amine solution, a known quantity of acid gas, of the H 2 S in this example, and then waiting for the establishment of the equilibrium state. . The quantities of acid gas absorbed in the aqueous amine solution are then deducted from the temperature and pressure measurements by means of material and volume balances. The solubilities are conventionally represented in the form of H 2 S partial pressures (in bar) as a function of the H 2 S feed rate (in moles of H 2 S / kg of absorbing solution and in moles of H 2 S / mol of MDEA).
In the case of deacidification in natural gas treatment, the partial H 2 S pressures encountered in the acid gases are typically between 0.1 and 1 bar at a temperature of 40 ° C. By way of example, in this industrial range, the rates of H2S feedstock obtained at 40 ° C. for various partial H 2 S pressures between the absorbent solution of MDEA at 50% by weight and the absorbent solution according to the invention.
Table 2 At 40 ° C., for partial LbS pressures of less than or equal to 1 bar, the absorption capacity of the aqueous solution of MDEA and of product A according to the invention is equivalent to or greater than that of the MDEA solution. reference.
It can therefore be seen that the absorbent solution according to the invention has an H2S absorption capacity that is equivalent to or greater than the reference aqueous MDEA solution, in the partial H2S pressure range of between 0.1 and 1 bar. , corresponding to a range of partial pressure representative of the usual industrial conditions.
As illustrated in the preceding example, the absorption of CO 2 is slower in the aqueous solution according to the invention than in a reference aqueous solution of MDEA. In addition, the H2S absorption capacity of the absorbent solutions according to the invention compared to the reference MDEA solutions is equivalent or greater for an H 2 S partial pressure of 0.1 - 1 bar, as illustrated in the present example. It therefore appears that the exemplified product according to the invention is particularly advantageous for improving the absorption selectivity of H2S with respect to CO 2 and for reducing the flow rates of absorbent solution to be used on applications of selective deacidification (H2S with respect to CO 2), i.e., absorb a given flow rate of H2S while reducing the co-absorbed CO 2 flow rate relative to the reference MDEA absorbent solution.

权利要求:
Claims (16)
[1" id="c-fr-0001]
Nitrogen compound belonging to the family of polyamines, resulting from the reaction between a polyol diglycidyl ether and piperazine, and corresponding to the following general formula (I):

in which: - n is an integer between 0 and 30, - the radical R! is selected from the following groups of sub-formulas (g1 to (g4): • the group of formula (g1:

x is an integer between 1 and 100, preferably between 1 and 25, the radical R 3 is indifferently a hydrogen atom, an alkyl radical or a hydroxyalkyl radical, comprising between 1 and 4 carbon atoms, the group of formula (g2):

where y is an integer between 3 and 8, • the group of formula (g3):

• the group of formula (g4):

where: - v and w are integers, each between 1 and 4, with the condition that the sum of v and w is equal to 2, 3, 4 or 5, - the radical R4 is indifferently a hydroxyl group, a alkyl radical or a hydroxyalkyl radical, having between 1 and 4 carbon atoms, and - the radical R5 is indifferently a hydrogen atom or a hydroxymethyl group (-CH2OH). the radical R2 has the following formula (g5): in which:

the radical R6 is indifferently a hydrogen atom, an alkyl radical or a hydroxyalkyl radical, comprising between 1 and 6 carbon atoms; the radical R7 is indifferently an alkyl radical or a hydroxyalkyl radical, comprising between 1 and 6; carbon atoms, the radicals R6 and R7 may be connected to one another by a covalent bond or by a heteroatom to form a 5-, 6-, 7- or 8-membered heterocycle when the radical R6 is not a hydrogen atom , and wherein when n is 0, the radicals R6 and R7 are connected together to form a piperazine ring, the radical R2 having the formula (g6) below:

where the R8 radical is indifferently a hydrogen atom, an alkyl radical or a hydroxyalkyl radical, having between 1 and 4 carbon atoms.
[2" id="c-fr-0002]
2. Compound according to claim 1, in which the radicals R6 and R7 are connected to one another by a covalent bond or by a heteroatom to form a 5-, 6-, 7- or 8-membered heterocycle when the radical R6 is not an atom. hydrogen.
[3" id="c-fr-0003]
The compound of claim 2 wherein the heterocycle is a piperazine ring.
[4" id="c-fr-0004]
4. Compound according to claim 3, in which the radical R2 corresponds to the formula (ge)
[5" id="c-fr-0005]
5. Process for the synthesis of a nitrogen compound according to one of claims 1 to 4, comprising the following reactions: a first reaction of addition or polyaddition of a diglycidyl ether of a polyol of formula (IV) with piperazine of formula (V) to form an intermediate compound of formula (VI),

(VI) being defined as in the general formula (I), said piperazine being in molar excess relative to said diglycidyl ether of a polyol, - a second addition reaction of said intermediate compound of formula (VI) with a monoepoxide of general formula ( VII)

(VII) for producing at least one nitrogen compound according to one of claims 1 to 4.
[6" id="c-fr-0006]
6. Process for the synthesis of a nitrogen compound according to one of claims 1 to 4, comprising the following reactions: a first reaction of addition or polyaddition of a diglycidyl ether of a polyol of formula (IV) with piperazine of formula (V) to form an intermediate compound of formula (VI),

(Iv)

(V)

(VIN) R! being defined as in the general formula (I), said diglycidyl ether of a polyol being in molar excess relative to said piperazine, - a second addition reaction of said intermediate compound of formula (VIII) with an amine of general formula (IX ) the radicals R6 and R7 being defined as in the general formula (I), to produce at least one nitrogen compound according to one of claims 1 to 4.
[7" id="c-fr-0007]
7. Synthesis process according to any one of claims 5 or 6, wherein the first reaction and the second reaction are conducted in two successive steps.
[8" id="c-fr-0008]
8. Synthesis process according to any one of claims 5 or 6, wherein the first reaction and the second reaction are carried out in one step.
[9" id="c-fr-0009]
9. Synthesis process according to one of claims 5 to 8, wherein the diglycidyl ether of a polyol of formula (IV) of the first reaction is selected from the list consisting of: - the diglycidyl ether of ethylene glycol; diglycidyl ether of diethylene glycol; diglycidyl ether of triethylene glycol; polyethylene glycol diglycidyl ether with a molar mass of between 200 and 2000 g / mol; the diglycidyl ether of copolymers of ethylene glycol and of propylene glycol with a molar mass of between 200 and 2000 g / mol; diglycidyl ether of 1,3-propanediol; 1,4-butanediol diglycidyl ether; diglycidyl ether of 1,5-pentanediol; diglycidyl ether of 1,6-hexanediol; the diglycidyl ether of 1,8-octanediol; diglycidyl ether of neopentyl glycol; 1,4-cyclohexanedimethanol diglycidyl ether; diglycidyl ether of 1,3-cyclohexanedimethanol; diglycidyl ether of 1,2-cyclohexanedimethanol; diglycidyl ethers of glycerol; diglycidyl ethers of trimethylolethane; diglycidyl ethers of trimethylolpropane; diglycidyl ethers of pentaerythritol; diglycidyl ethers of sorbitol.
[10" id="c-fr-0010]
10. Synthesis process according to one of claims 6 to 9, wherein the secondary amine of formula (IX) is chosen indifferently from the group consisting of: - dimethylamine; diethylamine; 2-amino-2-methyl-1-propanol; tris (hydroxymethyl) aminomethane; morpholine; N-methylpiperazine; N-hydroxyethylpiperazine; N-2-hydroxypropylpiperazine; diethanolamine; N-methylaminoethanol.
[11" id="c-fr-0011]
11. Synthesis process according to one of claims 5 or 7 to 9, wherein the monoepoxide of formula (VII) is chosen indifferently from the group consisting of: - epoxy-1,2-ethane; 1,2-epoxy propane; epoxy-1,2-butane; - glycidol.
[12" id="c-fr-0012]
12. Process for selectively removing H2S with respect to CO 2 from a gaseous effluent comprising H 2 S and CO 2, in which an absorption step of the acidic compounds is carried out by contacting the gaseous effluent. with an absorbent solution comprising: (a) water, (b) at least one main nitrogen compound comprising at least one tertiary amine function or a secondary amine function comprising two secondary carbons at position a and a 'of the atom of nitrogen or at least one tertiary carbon alpha or beta of the nitrogen atom, and (c) at least one nitrogen compound according to any one of claims 1 to 4, or obtainable by a process synthesis device according to one of claims 5 to 11.
[13" id="c-fr-0013]
13. The method of claim 12, wherein the absorbent solution comprises: a mass fraction of water of between 3.5% and 94.5% by weight of the absorbent solution, preferably between 39.5% and 79.5%; % by weight, - a mass fraction of the main nitrogen compound of between 5% and 95% by weight of the absorbent solution, preferably between 20 and 60% by weight, - a mass fraction of the annexed nitrogen compound of between 0.5% and 25% by weight. % by weight of the absorbent solution, preferably between 1% and 10% by weight, the mass fraction of the main nitrogenous compound being greater than that of the annexed nitrogen compound.
[14" id="c-fr-0014]
14. Process according to one of Claims 12 and 13, in which the main nitrogenous compound is chosen from the group consisting of: N-methyldiethanolamine; triethanolamine; diethylmonoethanolamine; dimethylmonoethanolamine; ethyldiethanolamine; the tertiary monoalkanolamines of the family of 3-alkoxypropylamines from the list consisting of N-methyl-N- (3-methoxypropyl) -2-aminoethanol, N-methyl-N- (3-methoxypropyl) -1-amino- 2-propanol, N-methyl-N- (3-methoxypropyl) -1-amino-2-butanol, N-ethyl-N- (3-methoxypropyl) -2-aminoethanol, N-ethyl-N- ( 3-methoxypropyl) -1-amino-2-propanol, N-ethyl-N- (3-methoxypropyl) -1-amino-2-butanol, N-isopropyl-N- (3-methoxypropyl) -2-aminoethanol N-isopropyl-N- (3-methoxypropyl) -1-amino-2-propanol and N-isopropyl-N- (3-methoxypropyl) -1-amino-2-butanol; the diamines in the list consisting of 1,2-bis (2-dimethylaminoethoxy) ethane, 1,2-bis (2-diethylaminoethoxy) ethane and 1,2-bis (2-pyrolidinoethoxy) ethane; 1,3-diamino-2-propanol diamines of the list consisting of 1,3-bis (dimethylamino) -2-propanol, (1-dimethylamino-3-tert-butylamino) -2- 1,3-bis (tert-butylamino) -2-propanol, 1,3-bis (diethylamino) -2-propanol, 1,3-bis (methylamino) -2-propanol, bis (ethylmethylamino) -2-propanol, 1,3 bis (n-propylamino) -2-propanol, 1,3-bis (isopropylamino) -2-propanol, 1,3 bis (n-butylamino) -2 propanol, 1,3-bis (isobutylamino) -2-propanol, 1,3-bis (piperidino) -2-propanol, and 1,3-bis (pyrrolidino) -2-propanol, the Ν, Ν Ν'-trimethyl-N'-hydroxyethyl-1,3-diamino-2-propanol; the dihydroxyalkylamines of the list consisting of N- (2'-hydroxyethyl) -2-amino-2-methyl-1-propanol, N- (2'-hydroxypropyl) -2-amino-2-methyl-1-one propanol, N- (2'-hydroxybutyl) -2-amino-2-methyl-1-propanol, (N-methyl-N-hydroxyethyl) -3-amino-2-butanol; the diamines of the family of bis (amino-3-propyl) ether or (amino-2-ethyl) - (amino-3-propyl) ethers from the list consisting of bis (dimethylamino-3-propyl) ether, bis (diethylamino-3-propyl) -ether, (dimethylamino-2-ethyl) - (dimethylamino-3-propyl) -ether, (diethylamino-2-ethyl) - (dimethylamino-3-propyl) -ether, (dimethylamino-2-ethyl) - (diethylamino-3-propyl) -ether, (diethylamino-2-ethyl) - (diethylamino-3-propyl) -ether; the tertiary beta-hydroxylated diamines of the list consisting of 1-dimethylamino-3- (2-dimethylaminoethoxy) -2-propanol, 1,1'-oxybis [3- (dimethylamino) -2-propanol], Ν , Ν, Ν ', Ν' - (tetramethyl) -1,6-diamino-2,5-hexanediol, N, N, N ', N' - (tetramethyl) -1,7-diamino-2,6- heptanediol, N, N, N ', N' - (tetramethyl) -1,8-diamino-2,7-octanediol, N, N, N ', N' - (tetramethyl) -1,9-diamino- 2,8-nonanediol, N, N, N ', N' - (tetramethyl) -1,10-diamino-2,9-decanediol; di- (2-hydroxyalkyl) -monoamines from the list consisting of 1 - [(2-hydroxyethyl) methylamino] -2-methyl-2-propanol, 1,1 '- (methylimino) -bis- [2- 2-methyl-2-propanol), 2 - [(2-hydroxy-2-methylpropyl) amino] -2-methyl-1-propanol, 2 - [(2-hydroxy-2-methylpropyl) amino] -1-butanol Bis (2-hydroxy-2-methylpropyl) amine; the congested tertiary 4- (aminoethyl) -morpholines of the list consisting of 1- (4-morpholino) -2- (methylisopropylamino) -ethane, 1- (4-morpholino) -2- (methyltertiobutylamino) -ethane, 1- (4-morpholino) -2- (diisopropylamino) ethane, 1- (4-morpholino) -2- (1-piperidinyl) ethane; the diamines in the list consisting of (N-morpholinoethyl) isopropylamine, (N-piperidinoethyl) isopropylamine, (N-morpholinoethyl) tert-butylamine; the amines of the family of N-alkyl-3-hydroxypiperidines and N-alkyl-4-hydroxypiperidines of the list consisting of N-methyl-4-hydroxy-piperidine, N-ethyl-3-hydroxypiperidine, N-methyl-3-hydroxypiperidines; methyl-3-hydroxy-piperidine; the alkylaminopiperazines which are 1-methyl-4- (3-dimethylaminopropyl) -piperazine, 1-ethyl-4- (diethylaminoethyl) -piperazine.
[15" id="c-fr-0015]
15. Method according to one of claims 12 to 14, wherein the absorbent solution further comprises a physical solvent selected from the group consisting of methanol, ethanol, 2-ethoxyethanol, benzyl alcohol, triethylene glycol dimethyl ether, tetraethyleneglycoldimethylether, pentaethyleneglycoldimethylether, hexaethyleneglycoldimethylether, Γheptaethyleneglycoldimethylether, octaethyleneglycoldimethylether, diethyleneglycol butoxyacetate, glycerol triacetate, sulfolane, N-methylpyrrolidone, N-methylmorpholin-3-one, Ν, Ν-dimethylformamide N-formyl morpholine, N, N-dimethylimidazolidin-2-one, N-methylimidazole, ethyleneglycol, diethyleneglycol, triethyleneglycol, thiodiglycol, and tributylphosphate, propylene carbonate.
[16" id="c-fr-0016]
16. Method according to one of claims 12 to 15, wherein the gaseous effluent chosen is from natural gas, synthesis gas, refinery gas, acid gas from an amine unit, gases from of a reduction unit at the bottom of the Claus process, the biomass fermentation gases.

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2017-06-16| PLSC| Publication of the preliminary search report|Effective date: 20170616 |

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2019-12-23| PLFP| Fee payment|Year of fee payment: 5 |

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优先权:

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申请号 | 申请日 | 专利标题

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FR1562247A|FR3045058B1|2015-12-11|2015-12-11|NOVEL POLYAMINES, PROCESS FOR THEIR SYNTHESIS AND THEIR USE FOR THE SELECTIVE REMOVAL OF H2S FROM A GASEOUS EFFLUENT COMPRISING CO2|FR1562247A| FR3045058B1|2015-12-11|2015-12-11|NOVEL POLYAMINES, PROCESS FOR THEIR SYNTHESIS AND THEIR USE FOR THE SELECTIVE REMOVAL OF H2S FROM A GASEOUS EFFLUENT COMPRISING CO2|

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US16/060,819| US10710021B2|2015-12-11|2016-12-05|Polyamines, synthesis process thereof and use of same for the selective elimination of H2S from a gaseous effluent comprising CO2|

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JP2018529246A| JP6924758B2|2015-12-11|2016-12-05|The novel polyamines, their synthetic methods and their use for the selective removal of H2S from gaseous effluents containing CO2.|

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PCT/EP2016/079779| WO2017097716A1|2015-12-11|2016-12-05|Novel polyamines, synthesis process thereof and use of same for the selective elimination of h2s from a gaseous effluent comprising co2|

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EP16809695.6A| EP3397671B1|2015-12-11|2016-12-05|Novel polyamines, synthesis process thereof and use of same for the selective eliminationof h2s from a gaseous effluent comprising co2|

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CA3007264A| CA3007264A1|2015-12-11|2016-12-05|Novel polyamines, synthesis process thereof and use of same for the selective elimination of h2s from a gaseous effluent comprising co2|

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RU2018123584A| RU2732132C2|2015-12-11|2016-12-05|Novel polyamines, a method for synthesis thereof and use thereof for selectively removing h2s from a gas stream containing co2|

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CN201680081568.8A| CN108602952B|2015-12-11|2016-12-05|Novel polyamines, method for their synthesis and their use for the removal of CO from a gas containing atmosphere2Selective removal of H from the gaseous effluent of2Use of S|

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SA518391751A| SA518391751B1|2015-12-11|2018-06-07|Novel polyamines, synthesis process thereof and use of same for the selective elimination of h2s from a gaseous effluent comprising co2|