cas 929-06-6, 2-Aminoethoxyethanol | Articles data

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Supramolecular compound nano-carrier as well as preparation method and application thereof
The invention discloses a supramolecular compound nano-carrier as well as a preparation method and application thereof, and relates to the technical field of polymer chemistry and biological detection engineering. According to the supramolecular compound nano-carrier disclosed by the invention, a two-dimensional nanosheet supramolecular structure system generated by self-assembly is driven by an anion induction effect, and a supramolecular compound nano-carrier is of a single-layer nanosheet supramolecular structure constructed by a highly-oriented one-dimensional nanorod. A hydrophobic perylene group part is used as a skeleton part for constructing the highly-oriented one-dimensional nanorod, and the charge density of a single-layer nanosheet can be regulated and controlled. The surface of the water-soluble multivalent hydrophilic part can be loaded with DNAzyme deoxyribozyme for specific detection of heavy metal ions through electrostatic interaction, and the water-soluble multivalent supramolecular compound nano sensor is constructed. Based on a fluorescence change mechanism caused by specific cutting of heavy metal ions, The fluorescence detection of the heavy metal ions in food and biological tissues is realized, and the detection effect of the heavy metal ions is greatly enhanced.
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Paragraph 0068; 0084

(2021/08/14)

SYNTHESIS OF 2-(2-AMINOETHOXY) ETHANOL
A method for synthesizing 2-(2-aminoethoxy) ethanol, including the steps of producing 2-(2-phthalimidoethoxy) ethanol by reacting 5-tosyloxy-3-oxapentanol with potassium phthalate and converting the 2-(2-phthalimidoethoxy) ethanol to the 2-(2-aminoethoxy) ethanol by reacting the 2-(2-phthalimidoethoxy) ethanol with hydrazine monohydrate. Reacting the 2-(2-phthalimidoethoxy) ethanol with the hydrazine monohydrate may include forming a final mixture by adding the hydrazine monohydrate to a solution of 2-(2-phthalimidoethoxy) ethanol, refluxing the final mixture in a nitrogen atmosphere, extracting a second organic phase containing the 2-(2-aminoethoxy) ethanol from the final mixture using a second portion of chloroform, and purifying the 2-(2-aminoethoxy) ethanol from the second organic phase.
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Paragraph 0068-0071

(2021/02/12)

EXENATIDE MODIFIER AND USE THEREOF
Disclosed are an exenatide modifier for connecting the exenatide to a fatty chain with a carboxy in the terminus thereof by means of a hydrophilic connecting arm, and a use thereof in preparing drugs serving as a GLP-1 receptor agonist; a use in preparing drugs for preventing and/or treating diseases and/or symptoms associated with a low GLP-1 receptor activity; a use in preparing drugs for diseases and/or symptoms associated with glycometabolism; a use in preparing drugs for diabetes; a use in preparing drugs for fatty liver disease, and a use in preparing drugs for losing weight.
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Paragraph 0238

(2018/05/24)

mellow amination by homogeneous catalysis of the method for the production of primary amines
The invention relates to a method for producing primary amines by means of the alcohol amination of alcohols with ammonia, with water being eliminated. The method comprises the steps of: (a) a homogenously-catalysed reaction of a reaction mixture which contains at least one alcohol, ammonia, at least one non-polar solvent, and at least one catalyst containing at least one element selected from groups 8, 9 and 10 of the periodic table in the liquid phase, a product mixture (P) thus being obtained; (b) separating the phases of product mixture (P) which was obtained in step (a), if necessary after a reduction in temperature, a reduction in pressure and/or the addition of at least one polar solvent with a miscibility gap in relation to the non-polar solvent, and thus obtaining at least one polar product phase (A) and at least one non-polar phase (B) containing at least one portion of the catalyst that was introduced, with said non-polar phase (B) being separated off, (c) returning at least one portion of the non-polar phase (B) into the reaction in step (a), and (d) separating the amination product from the polar product phase (A). The non-polar solvent introduced in (a) and the catalyst introduced in step (a) are selected such that the catalyst in the non-polar phase (B) becomes enriched.
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Paragraph 0265; 0267

(2016/10/09)

METHOD FOR PRODUCING ALKANOL AMINES BY HOMOGENEOUSLY CATALYZED ALCOHOL AMINATION
PROBLEM TO BE SOLVED: To provide a method for producing alkanol amines by alcohol amination of diols using ammonia under elimination of water. SOLUTION: The invention relates to a method for producing alkanol amines which comprise a primary amino group (-NH2) and a hydroxyl group (-OH), by alcohol amination of diols comprising two hydroxyl groups (-OH) using ammonia under elimination of water. The reaction is homogeneously catalyzed in the presence of at least one complex catalyst which contains at least one element selected from groups 8, 9 and 10 of the periodic table and at least one donor ligand. SELECTED DRAWING: None COPYRIGHT: (C)2016,JPO&INPIT
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Paragraph 0088; 0099

(2016/10/27)

The preparation obtained by homogeneous catalysis mellow amination method of the primary amine
The invention relates to a method for producing primary amines comprising at least one functional group of formula (-CH2-NH2), by alcohol amination of educts which comprise at least one functional group of formula (-CH2-OH), using ammonia, and elimination of water. The homogeneously catalyzed alcohol amination is carried out in the presence of at least one complex catalyst which contains at least one element selected from the groups 8 and 9 of the periodic table and at least one phosphorus donor ligand of general formula (I).
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Paragraph 0207-0208; 0213

(2017/02/28)

· Uniform catalyst by using alcohol aminosilicone di-, tri-and a method of manufacturing a polyphenylenepolyamine
The invention relates to a method for producing primary amines, which contain at least one functional group of the formula (-CH2-NH2) and at least one further primary amino group, by the alcohol amination of reactants, which contain at least one functional group of the formula (-CH2-OH) and at least one further functional group (-X), wherein (-X) is selected from hydroxyl groups and primary amino groups, using ammonia with removal of water, wherein the reaction is carried out in a homogeneously catalyzed manner in the presence of at least one complex catalyst containing at least one element selected from groups 8, 9 and 10 of the periodic table and at least one donor ligand.
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Paragraph 0099; 0108; 0109

(2016/10/09)

Synthesis of fluorous photolabile aldehyde and carbamate and alkyl carbamate protecting groups for carbohydrate-associated amines
Two new fluorous photolabile-protecting groups (FNBC and FNB) and a new base-labile protecting group (FOC) for the masking of amines are reported. The protecting groups survive a wide range of common reaction conditions used in oligosaccharide synthesis and render the attached molecules amenable to fluorous solid-phase extraction (FSPE). A glycosyl acceptor containing the FNB group is shown to be useful in the synthesis of carbohydrates tagged with free deactivated secondary amines.
Roychoudhury, Rajarshi,Pohl, Nicola L. B.
supporting information
p. 1156 - 1159
(2014/03/21)

PROCESS FOR THE PREPARATION OF PRIMARY AMINES BY HOMOGENEOUSLY CATALYZED ALCOHOL AMINATION
Preparing a primary amine by alcohol amination of alcohol with ammonia and elimination of water includes reacting, in a homogeneously catalyzed reaction, a mixture of alcohol, ammonia, nonpolar solvent, and catalyst, in a liquid phase, to obtain a product mixture. The process then includes phase separating the product mixture into a polar product phase and a nonpolar product phase, and separating off the nonpolar product phase. At least some of the nonpolar phase returns to the homogenously catalyzed reaction. The process further includes separating off amination product from the polar product phase. At least some of the catalyst is in the nonpolar phase, and the catalyst accumulates in the nonpolar phase.
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Page/Page column 16

(2012/09/22)

PROCESS FOR PREPARING ALKANOLAMINES BY HOMOGENEOUSLY CATALYZED ALCOHOL AMINATION
Process for preparing alkanolamines which have a primary amino group (—NH2) and a hydroxyl group (—OH) by alcohol amination of diols having two hydroxyl groups (—OH) by means of ammonia with elimination of water, wherein the reaction is carried out homogeneously catalyzed in the presence of at least one complex catalyst comprising at least one element selected from groups 8, 9 and 10 of the Periodic Table and also at least one donor ligand.
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Page/Page column 13-14; 16

(2012/09/22)

PROCESS FOR THE PREPARATION OF PRIMARY AMINES BY HOMOGENEOUSLY CATALYZED ALCOHOL AMINATION
Process for the preparation of primary amines which have at least one functional group of the formula (—CH2—NH2) by alcohol amination of starting materials which have at least one functional group of the formula (—CH2—OH), with ammonia, with the elimination of water, where the alcohol amination is carried out under homogeneous catalysis in the presence of at least one complex catalyst which comprises at least one element selected from groups 8 and 9 of the Periodic Table of the Elements, and also at least one phosphorus donor ligand of the general formula (I).
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Page/Page column 10; 12

(2012/09/22)

PROCESS FOR PREPARING DI-, TRI- AND POLYAMINES BY HOMOGENEOUSLY CATALYZED ALCOHOL AMINATION
Process for preparing primary amines which have at least one functional group of the formula (—CH2—NH2) and at least one further primary amino group by alcohol amination of starting materials having at least one functional group of the formula (—CH2—OH) and at least one further functional group (—X), where (—X) is selected from among hydroxyl groups and primary amino groups, by means of ammonia with elimination of water, wherein the reaction is carried out homogeneously catalyzed in the presence of at least one complex catalyst comprising at least one element selected from groups 8, 9 and 10 of the Periodic Table and also at least one donor ligand.
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Page/Page column 12; 14

(2012/09/22)

Design and synthesis of a dual linker for solid phase synthesis of oleanolic acid derivatives
A hydrophilic amino-terminated poly(ethylene glycol)-type dual linker for solid phase synthesis of oleanolic acid derivatives using trityl chloride resin was designed and synthesized for the first time. Model reactions in both liquid and solid phase were performed to show the feasibility of its selective cleavage at two different sites. The biological assay results indicated that the long and flexible alkyl ether functionality in the linker is less likely to be critical for the binding event. Following the successful solid-phase synthesis of model compounds, the potential of this dual linker in reaction monitoring and target identification is deemed worthy of further study.
Wang, Shaorong,Fang, Weishuo
experimental part
p. 4748 - 4763
(2011/08/22)

METHOD FOR PRODUCING AN AMINE
Processes for preparing an amine, which processes comprise: reacting a reactant selected from the group consisting of primary alcohols, secondary alcohols, aldehydes, ketones, and mixtures thereof, with hydrogen and a nitrogen compound selected from the group consisting of ammonia, primary amines, secondary amines and mixtures thereof, in the presence of a zirconium dioxide-, copper- and nickel-containing catalyst; wherein the catalyst comprises a catalytically active composition which comprises, before reduction with hydrogen, oxygen compounds of zirconium, copper, nickel and tin, and 0.5 to 8.0% by weight of an oxygen compound of cobalt, calculated as CoO, and wherein the catalytically active composition does not comprise any ruthenium.
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Page/Page column 11

(2011/04/14)

A PROCESS FOR THE PREPARATION OF 2-(2-AMINOETHOXY) ETHANOL (2AEE) AND MORPHOLINE WITH 2AEE: MORPHOLINE >3
The invention relates to a process for the production of 2AEE with selectivity towards 2AEE being significantly higher i.e. the ratio of 2AEE: morpholine > 3. DEG and Ammonia are reacted in a continuous mode in hydrogen atmosphere in the presence of a catalyst at temperature of 150 °C to 250 °C and pressure of 10 Bar to 20 Bar, the products being separated by distillation. The catalyst used is metal and its oxide or metal oxide on silica or alumina support. The molar ratio of ammonia: DEG is > 20 and the molar ratio of hydrogen: DEG is >1, preferably 1-30. The reactants are optionally fed in a downward flow mode. The catalyst charged into the reactor has metal and its oxide or metal oxide equivalent to a metal content of 10 % to 70 % on the support.
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Page/Page column 4

(2011/04/26)

CATALYST AND PROCESS FOR PREPARING AN AMINE
A process for preparing an amine by reacting a primary or secondary alcohol, aldehyde and/or ketone with hydrogen and a nitrogen compound selected from the group of ammonia and primary and secondary amines, in the presence of a supported copper-, nickel- and cobalt-containing catalyst, wherein the catalytically active material of the catalyst, before the reduction thereof with hydrogen, comprises oxygen compounds of aluminum, of copper, of nickel and of cobalt, and in the range from 0.2 to 5.0% by weight of oxygen compounds of tin, calculated as SnO, and catalysts as defined above.
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Page/Page column 12

(2011/06/24)

METHOD FOR PRODUCING ELECTRONIC GRADE 2,2'-AMINOETHOXYETHANOL
A process for preparing electronics-grade 2,2′-aminoethyoxyethanol by reacting diethylene glycol with ammonia in the presence of a catalyst in a reactor to give a reaction mixture from which a crude 2,2′-aminoethoxyethanol stream is separated off and is purified further by distillation in a pure column, wherein a sidestream comprising electronics-grade 2,2′-aminoethoxyethanol is taken off from the pure column as a result of the diethylene glycol being passed through a filter which ensures a degree of removal of at least 99% for solid particles having a maximum particle size of ≦1.5 μm before the diethylene glycol is fed into the reactor, is proposed.
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Page/Page column 2

(2010/03/02)

METHOD FOR THE CONTINUOUS SEPARATION OF MIXTURES COMPRISING MORPHOLINE (MO), MONOAMINODIGLYCOL (ADG), AMMONIA AND WATER BY MEANS OF DISTILLATION
Processes for the continuous fractional distillation of a mixture comprising morpholine (MO), monoaminodiglycol (ADG), ammonia and water from a reaction of diethylene glycol (DEG) with ammonia, the process comprising: (i) separating off ammonia from the mixture at a top of a first distillation column K10; (ii) feeding a bottom fraction from K10 to a second distillation column K20 in which water and organic products are separated off at the top at a temperature at the top in the range from 45 to 198° C. and a pressure in the range from 0.1 to 15 bar, (iii) feeding a bottom fraction from K20 to a third distillation column K30, wherein the column K30 is a dividing wall column (DWC) which preferably has a dividing wall (DW) in the longitudinal direction of the column to form an upper combined column region (1), a lower combined column region (6), an inflow part (2, 4) having an enrichment section (2) and a stripping section (4), and also an offtake part (3, 5) having an enrichment section (3) and a stripping section (5), with the bottoms from K20 being fed in in the upper or middle third of the inflow part (2, 4), based on the number of theoretical plates of the inflow part, ADG and organic products having a boiling point of >190° C. (1.013 bar) being discharged at the bottom, organic products having a boiling point of ≦128° C. (1.013 bar) being discharged at the top and MO being discharged from the middle or lower third of the offtake part (3, 5) (side offtake), based on the number of theoretical plates of the offtake part.
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Page/Page column 5-6

(2010/04/30)

METHOD FOR PRODUCING AN AMINE
Processes comprising: (i) providing a reactant selected from the group consisting of primary alcohols, secondary alcohols, aldehydes, ketones and mixtures thereof; and (ii) reacting the reactant with hydrogen and a nitrogen compound selected from the group consisting of ammonia, primary amines, secondary amines and mixtures thereof, in the presence of a catalyst comprising a zirconium dioxide- and nickel-containing catalytically active composition, to form an amine; wherein the catalytically active composition, prior to reduction with hydrogen, comprises oxygen compounds of zirconium, copper, and nickel, and one or more oxygen compounds of one or more metals selected from the group consisting of Sb, Pb, Bi, and In.
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Page/Page column 2; 10-11

(2010/02/17)

METHOD FOR THE PRODUCTION OF AN AMINE
Processes for preparing an amine, the processes comprising: reacting a reactant selected from the group consisting of primary alcohols, secondary alcohols, aldehydes, ketones, and mixtures thereof, with hydrogen and a nitrogen compound selected from the group consisting of ammonia, primary amines, secondary amines and mixtures thereof, in the presence of a zirconium dioxide-, copper- and nickel-containing catalyst; wherein the catalyst comprises a catalytically active composition which comprises, before reduction with hydrogen, oxygen compounds of zirconium, copper, and nickel, and 1.0 to 5.0% by weight of an oxygen compound of cobalt, calculated as CoO, and 0.2 to 5.0% by weight of a polyoxometalate.
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Page/Page column 11

(2010/12/26)

METHOD FOR PRODUCING AN AMINE
Processes for preparing an amine, which processes comprise: reacting a reactant selected from the group consisting of primary alcohols, secondary alcohols, aldehydes, ketones, and mixtures thereof, with hydrogen and a nitrogen compound selected from the group consisting of ammonia, primary amines, secondary amines and mixtures thereof, in the presence of a zirconium dioxide- and nickel-containing catalyst; wherein the catalyst comprises a catalytically active composition which comprises, before reduction with hydrogen, oxygen compounds of zirconium, nickel, and iron, and 0.2 to 5.5% by weight of at least one oxygen compound of tin, lead, bismuth, molybdenum, antimony or phosphorus, calculated as SnO, PbO, Bi2O3, MoO3, Sb2O3 and H3PO4 respectively; and wherein the catalytically active composition of the catalyst does not comprise any copper.
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Page/Page column 11

(2010/12/26)

METHOD FOR PRODUCING AN AMINE
Processes comprising: (i) providing a reactant selected from the group consisting of primary alcohols, secondary alcohols, aldehydes, ketones and mixtures thereof, and (ii) reacting the reactant with hydrogen and a nitrogen compound selected from the group consisting of ammonia, primary amines, secondary amines and mixtures thereof, in the presence of a catalyst comprising a zirconium dioxide- and nickel-containing catalytically active composition, to form an amine; wherein the catalytically active composition, prior to reduction with hydrogen, comprises oxygen compounds of zirconium, copper, nickel and cobalt, and one or more oxygen compounds of molybdenum in an amount of 5.5 to 12% by weight, calculated as MoO3.
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Page/Page column 10

(2009/12/02)

METHOD FOR PRODUCING AN AMINE
Processes comprising: (i) providing a reactant selected from the group consisting of primary alcohols, secondary alcohols, aldehydes, ketones and mixtures thereof; and (ii) reacting the reactant with hydrogen and a nitrogen compound selected from the group consisting of ammonia, primary amines, secondary amines and mixtures thereof, in the presence of a catalyst comprising a zirconium dioxide- and nickel-containing catalytically active composition, to form an amine; wherein the catalytically active composition, prior to reduction with hydrogen, comprises oxygen compounds of zirconium, copper, nickel and cobalt, and one or more oxygen compounds of one or more metals selected from the group consisting of Pb, Bi, Sn, Sb and In.
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Page/Page column 10

(2009/12/05)

METHOD FOR PRODUCING AN AMINE
Processes comprising: (i) providing a reactant selected from the group consisting of primary alcohols, secondary alcohols, aldehydes, ketones and mixtures thereof, and (ii) reacting the reactant with hydrogen and a nitrogen compound selected from the group consisting of ammonia, primary amines, secondary amines and mixtures thereof, in the presence of a catalyst comprising a zirconium dioxide- and nickel-containing catalytically active composition, to form an amine; wherein the catalytically active composition, prior to reduction with hydrogen, comprises oxygen compounds of zirconium, copper, and nickel, and one or more oxygen compounds of silver in an amount of 0.5 to 6% by weight, calculated as AgO.
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Page/Page column 10

(2009/12/27)

Method for Preparing Aminodiglycol (Adg) and Morpholine
Processes comprising: providing a starting material comprising diethylene glycol; and reacting the starting material with ammonia in the presence of a heterogeneous transition metal catalyst to form a reaction product comprising aminodiglycol and morpholine; wherein the catalyst comprises a catalytically active composition, which prior to treatment with hydrogen, comprises a mixture of oxygen-containing compounds of copper, nickel, cobalt and at least one of aluminum and zirconium; and wherein the catalyst is present as one or more shaped catalyst particles selected from spheres, extrudates, pellets and other geometries, wherein the sphere or extradate has a diameter of s2/mmp3), as defined by a ′ = A p V p where Ap is the external surface area of the catalyst particle (mms2) and Vp is the volume of the catalyst particle (mmp3).
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Page/Page column 4

(2008/12/04)

Thermodynamics and equilibrium solubility of carbon dioxide in diglycolamine/morpholine/water
Carbon dioxide solubility was studied in 3.5 m (23.5 wt %) morpholine (MOR), 17.7 m (65 wt %) 2-aminoethoxyethanol (diglycolamine or DGA), and 3.6 m MOR + 14.7 m DCA (11 wt % MOR + 53 wt % DGA). CO2 solubility was determined by dynamic measurements with a wetted wall contactor. Carbamate and bicarbonate concentrations were determined by 13C NMR in solutions loaded with 13CO2. The data are represented by the electrolyte NRTL model. At a given CO2 loading (mol/mol amine), the CO2 vapor pressure over 3.5 m MOR is 10 to 1000 times greater than 17.7 m DGA. In 3.6 m MOR + 14.7 m DGA, the CO2 vapor pressure is 5 to 7 times greater than in 17.7 m DGA at high CO2 loading, but the same below 0.2 loading. MOR carbamate is less stable than DGA carbamate by a factor of 7 to 10 from (300 to 333) K. The model predicts that MOR vapor pressure is 100 times greater than DGA over 3.6 m MOR + 14.7 m DGA from (313 to 333) K. The heat of CO2 absorption in the blend is equivalent to 17.7 m DGA up to 0.35 loading but is 40 % lower at 0.5 loading. The working capacity of the blend is 17 % less than 17.7 m DGA.
Al-Juaied, Mohammed,Rochelle, Gary T.
p. 708 - 717
(2007/10/03)

Production of catalyst
Disclosed are catalysts, the catalytically active mass of which contains 22 to 40 percent by weight of oxygen-containing compounds of zirconium, calculated as ZrO2, 1 to 30 percent by weight of oxygen-containing compounds of copper, calculated as CuO, 15 to 50 percent by weight of oxygen-containing compounds of nickel, calculated as NiO, the molar ratio between nickel and copper being greater than 1, 15 to 50 percent by weight of oxygen-containing compounds of cobalt, calculated as CoO, and less than 1 percent by weight of an alkali metal, calculated as alkali metal oxide, prior to being treated with hydrogen. Also disclosed is a method for the production of amines by reacting primary and secondary alcohols, aldehydes, or ketones with hydrogen and nitrogen compounds selected from the group ammonia, primary and secondary amines, in the presence of said catalysts at an elevated temperature and an elevated pressure.
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Page/Page column 20

(2008/06/13)

Synthesis and Hydrolytic Lability of α-Phenoxyacetamides Containing Hydroxy Groups in the N-alkyl Residue
Secondary and tertiary amides of 3,5-biscarbonyl>phenoxyacetic acid bearing hydroxy groups in positions β (β-OH) and γ (γ-OH) relative to the acetamide nitrogen atom have been synthesized.Such amides easily undergo cleavage of the acetamide bond in water at neutral pH.Hydrolysis rate constant for a series of such amides and protonation constants for the corresponding leaving amines were determined.No simple correlation between the two parameters could be found.A study of the dependence of these parameters on the structural features of the substrates, such as the presence of an N-methyl group and number of β-OH and γ-OH groups, was carried out.All these features lead to enhancement of the amide hydrolysis rate and a synergistic effect is operative when both N-methyl and β-OH groups are contained in the substrate.Presence of a methyl group increases the basicity of amines whereas β-OH and γ-OH groups have the opposite effect.Mechanistic speculations seem to indicate that the abnormal lability of the acetamide bond is due to protic-like catalysis by an intramolecular OH...N hydrogen bond.
Anelli, Pier Lucio,Brocchetta, Marino,Canipari, Sonia,Losi, Pietro,Manfredi, Giuseppe,et al.
p. 135 - 142
(2007/10/03)

Heterocyclic hydrazines and hydrazones
N-carbamoyl-2-carboxyaryl-heterocyclic and hydrazinecarboximidamide-hydrazone derivatives, intermediates and processes for their preparation, agricultural compositions containing them and their use as agricultural chemicals, in particular herbicides.
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(2008/06/13)

Synthesis of New Phospholipids Linked to Steroid-Hormone Derivatives Designed for Two-Dimensional Crystallization of Proteins
The synthesis of phospholipids 1n-3n, rationally designed for two-dimensional crystallization of progesterone and estradiol receptors, is reported.The structure of theses lipids provides them with essential properties such as fluidity and stability when spread into monolayers at the air/H2O interface, affinity for the protein to be crystallized, and accessibility of the ligand under the lipid monolayer.
Lebeau, Luc,Oudet, Pierre,Mioskowski, Charles
p. 1697 - 1706
(2007/10/02)

Determination des parametres thermodynamiques de l'equilibre de formation de carbamates d'amino-alcools en solution aqueuse par resonance magnetique nucleaire du carbone-13
The formation of alkanolamine carbamates is demonstrated in aqueous solutions of monoethanolamine, diglycolamine or diisopropanolamine and of sodium bicarbonate by carbon-13 nuclear magnetic resonance spectroscopy.A quantitative study of the ratio -> + 2->/ as a function of the temperature allows us to determine the thermodynamic parameters of the following equilibrium R2NH (or RNH2) + CO2 = R2NCO2- (or RNHCO2-) + H+ (KR).The values of KR, ΔHoR, ΔGoR and ΔSoR at 25 deg C are discussed.
Barth, Danielle,Rubini, Patrice,Delpuech, Jean-Jacques
p. 227 - 230
(2007/10/02)

Amine bisulfites
This invention relates to the amine bisulfites which are useful as a combination corrosion inhibitor/oxygen scavenger. This is illustrated by heterocyclic amine bisulfites such as pyridine bisulfites.
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(2008/06/13)

Macrocyclic compounds having oxa and aza linkages in the ring and containing spirooxetane groups
Compound having the formula EQU1 WHEREIN Y is --XCH2 CH2 --X--, --X(CH2 CH2 X)2 or EQU2 p is 1 to 4, and each X is O or NH, N-alkanoyl, N-benzoyl wherein the benzene ring is optionally substituted with --NO2, --NH2, or --CH3, N-alkyl or N-β-hydroxyalkyl each of up to 8 carbons and wherein the total number of N is 1 to 3 are disclosed. The compounds can be polymerized by opening of the oxetane ring in the presence of electrophilic agents, or the oxetane ring can be hydrolyzed to a dihydroxy group and reacted with diacid halides to form polyesters or with diisocyanates to form polyurethanes. Both monomers and polymers complex metal ions and can be used to separate such ions from solutions.
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(2008/06/13)