WO2020008477A1 - A neutralizing amine formulation and process of preparation thereof - Google Patents
A neutralizing amine formulation and process of preparation thereof Download PDFInfo
- Publication number
- WO2020008477A1 WO2020008477A1 PCT/IN2019/050494 IN2019050494W WO2020008477A1 WO 2020008477 A1 WO2020008477 A1 WO 2020008477A1 IN 2019050494 W IN2019050494 W IN 2019050494W WO 2020008477 A1 WO2020008477 A1 WO 2020008477A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- amine
- formulation
- range
- present disclosure
- respect
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G7/00—Distillation of hydrocarbon oils
- C10G7/10—Inhibiting corrosion during distillation
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G75/00—Inhibiting corrosion or fouling in apparatus for treatment or conversion of hydrocarbon oils, in general
- C10G75/04—Inhibiting corrosion or fouling in apparatus for treatment or conversion of hydrocarbon oils, in general by addition of antifouling agents
Definitions
- the present disclosure generally relates to the field of inhibiting corrosion in the crude distillation units of refineries.
- the present disclosure discloses a formulation which combats the problem associated of condensing hydrocarbons which contain water and chlorides
- Refineries employ neutralizing amines to guard their crude distillation unit overhead systems from corrosion due to hydrochloric acid (HC1) or acidic sulfur species and fouling due to build-up of sublimating species.
- the amines are usually organic amines (such as di-ethanol amine, monoethanol amine, triethanolamine, morpholine, piperazine, etc.) which function by neutralizing acidic contaminants, thereby increasing the pH to an appropriate level for minimizing corrosion of the various system.
- organic amines such as di-ethanol amine, monoethanol amine, triethanolamine, morpholine, piperazine, etc.
- US 4,062,764 discloses that alkoxylated amines are useful in neutralizing the initial condensate.
- US 3,472,666 suggests that alkoxy substituted aromatic amines in which the alkoxy group contains from 1 to 10 carbon atoms are effective corrosion inhibitors in petroleum refining operations. Representative examples of these materials are aniline, anisidine and phenetidines.
- US 4,430,196 discloses the utility of hydroxylated amines.
- Representative examples of these neutralizing amines are dimethylisopropanolamine and dimethylaminoethanol.
- a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1.
- a process for preparing the formulation comprising: (a) at least one first amine; and (b) at least one second amine, the process comprising: (a) obtaining the at least one first amine; (b) obtaining the at least one second amine; (c) contacting the at least one first amine, the at least one second amine, and optionally the at least one additive to obtain the formulation, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1.
- a method of reducing fouling in a petroleum refinery comprising, adding the formulation comprising: (a) at least one first amine; and (b) at least one second amine to a water system.
- the articles“a”,“an” and“the” are used to refer to one or to more than one (i.e., to at least one) of the grammatical object of the article.
- fouling and/or corrosion problem refers to aqueous corrosion due to hydrochloric acid (HC1) or acidic sulfur species, or the build-up of sublimating species such as ammonium chloride under deposit corrosion in distillation units.
- surfactant amine refers to fatty acid amines which can be used as surfactants.
- Such surfactant amines include, by way of example Ci-io alkyl ammonium chloride, alkyldimethyl ammonium chloride.
- alkyl herein refers to a branched or unbranched chain having 1-10 carbon atoms.
- the surfactant amines in the present disclosure are those which are known to a person skilled in the art.
- ionic liquid are used to refer quaternary ammonium compounds known to a person skilled in the art.
- Ratios, concentrations, amounts, and other numerical data may be presented herein in a range format. It is to be understood that such range format is used merely for convenience and brevity and should be interpreted flexibly to include not only the numerical values explicitly recited as the limits of the range, but also to include all the individual numerical values or sub-ranges encompassed within that range as if each numerical value and sub-range is explicitly recited.
- a weight percentage of about 50 % to 90 % should be interpreted to include not only the explicitly recited limits of about 50% and 90 %, but also to include sub-ranges, such as 55-85 %, 65-75%, and so forth, as well as individual amounts, including fractional amounts, within the specified ranges, such as 90 %, 85 %, for example.
- the formulation of the present disclosure provides a neutralizing formulation/agent comprising: (a) at least one first amine; and (b) at least one second amine.
- the at least one first amine to the at least one second amine present in the formulation can have a weight ratio is in the range of 8: 1 - 10: 1.
- the neutralizing formulation effectively neutralizes the acidic species and as a result combat the primary corrosion problem encountered in crude distillation unit overhead systems.
- a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1.
- a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8.5: 1 - 9.5: 1.
- a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is 9: 1.
- a formulation as described herein wherein the at least one first amine has a weight percentage in the range of 50 to 95 % with respect to the formulation.
- a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1 and the at least one first amine has a weight percentage in the range of 50 to 95 % with respect to the formulation.
- a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8.5: 1 - 9.5: 1 and the at least one first amine has a weight percentage in the range of 50 to 95 % with respect to the formulation.
- a formulation as described herein wherein the at least one first amine has a weight percentage in the range of 60 to 95 % with respect to the formulation. In another embodiment the at least one first amine has a weight percentage in the range of 75 to 92 % with respect to the formulation. In yet another embodiment the at least one first amine has a weight percentage in the range of 80 to 90 % with respect to the formulation.
- the at least one first amine is selected from the group consisting of diethanolamine, morpholine, monoethanolamine, triethanolamine, cyclohexylamine, piperazine, diethylaminoethanol, methyldiethanolamine, ethyl ethanolamine, aminoethyl piperazine, and combinations thereof.
- a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1 and the at least one first amine is selected from the group consisting of diethanolamine, morpholine, monoethanolamine, triethanolamine, cyclohexylamine, piperazine, diethylaminoethanol, methyldiethanolamine, ethyl ethanolamine, aminoethyl piperazine, and combinations thereof.
- a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8.5: 1 - 9.5: 1 and the at least one first amine is selected from the group consisting of diethanolamine, morpholine, monoethanolamine, triethanolamine, cyclohexylamine, piperazine, diethylaminoethanol, methyldiethanolamine, ethyl ethanolamine, aminoethyl piperazine, and combinations thereof.
- the at least one first amine is selected from the group consisting of diethanolamine, morpholine, monoethanolamine, triethanolamine, cyclohexylamine, piperazine, diethylaminoethanol, and combinations thereof.
- the at least one first amine is selected from the group consisting of diethanolamine, morpholine, monoethanolamine, triethanolamine, cyclohexylamine, piperazine, and combinations thereof.
- the at least one first amine is selected from diethanolamine or morpholine.
- the at least one first amine is selected from the group consisting of diethanolamine, morpholine, diethylaminoethanol, and combinations thereof.
- the at least one second amine has a weight percentage in the range of 5 to 15 % with respect to the formulation.
- a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1 and the at least one second amine has a weight percentage in the range of 5 to 15 % with respect to the formulation.
- a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8.5: 1 - 9.5: 1 and the at least one second amine has a weight percentage in the range of 5 to 15 % with respect to the formulation.
- a formulation as described herein wherein the at least one second amine has a weight percentage in the range of 6 to 15 % with respect to the formulation. In another embodiment the at least one second amine has a weight percentage in the range of 8 to 12 % with respect to the formulation. In yet another embodiment the at least one second amine has a weight percentage of 10 % with respect to the formulation.
- a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1 and the at least one second amine is a product of epichlorohydrin and the at least one first amine and the at least one first amine.
- a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8.5: 1 - 9.5: 1 and the at least one second amine is a product of epichlorohydrin and the at least one first amine and the at least one first amine.
- a formulation as described herein wherein the at least one second amine is a product of epichlorohydrin and the at least one first amine, and has a weight percentage in the range of 5 to 15 % with respect to the formulation.
- the at least one second amine is a product of epichlorohydrin and the at least one first amine, and has a weight percentage in the range of 6 to 15 % with respect to the formulation.
- the at least one second amine is a product of epichlorohydrin and the at least one first amine, has a weight percentage in the range of 8 to 12 % with respect to the formulation.
- the at least one second amine is a product of epichlorohydrin and the at least one first amine, and has a weight percentage of 10 % with respect to the formulation.
- the at least one second amine is a product of epichlorohydrin and the at least one first amine selected from the group consisting of diethanolamine, morpholine, monoethanolamine, triethanolamine, cyclohexylamine, piperazine, diethylaminoethanol, methyldiethanolamine, ethyl ethanolamine, aminoethyl piperazine, and combinations thereof.
- a formulation as described herein wherein the at least one second amine has a weight percentage in the range of 5 to 15 % with respect to the formulation, and is a product of epichlorohydrin and the at least one first amine selected from the group consisting of diethanolamine, morpholine, monoethanolamine, triethanolamine, cyclohexylamine, piperazine, diethylaminoethanol, methyldiethanolamine, ethyl ethanolamine, aminoethyl piperazine, and combinations thereof.
- a formulation as described herein wherein the at least one second amine has a weight percentage in the range of 5 to 15 % with respect to the formulation, and is a product of epichlorohydrin and the at least one first amine selected from the group consisting of diethanolamine, morpholine, monoethanolamine, triethanolamine, cyclohexylamine, piperazine, diethylaminoethanol, methyldiethanolamine, ethyl ethanolamine, aminoethyl piperazine, and combinations thereof and the at least one first amine has a weight percentage in the range of 50 to 95 % with respect to the formulation.
- a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1 and the at least one first amine is selected from the group consisting of diethanolamine, morpholine, monoethanolamine, triethanolamine, cyclohexylamine, piperazine, diethylaminoethanol, methyldiethanolamine, ethyl ethanolamine, aminoethyl piperazine, and combinations thereof and the at least one second amine is a product of epichlorohydrin and the at least one first amine.
- a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8.5: 1 - 9.5: 1 and the at least one first amine is selected from the group consisting of diethanolamine, morpholine, monoethanolamine, triethanolamine, cyclohexylamine, piperazine, diethylaminoethanol, methyldiethanolamine, ethyl ethanolamine, aminoethyl piperazine, and combinations thereof and the at least one second amine is a product of epichlorohydrin and the at least one first amine.
- a formulation comprising: (a) at least one first amine; (b) at least one second amine; and (c) at least one additive having a weight percentage in the range of 0 to 5 % with respect to the formulation; and is selected from the group consisting of surfactant amines, ionic liquids, and combinations thereof.
- a formulation comprising: (a) at least one first amine; (b) at least one second amine; and (c) at least one additive having a weight percentage in the range of 0 to 5 % with respect to the formulation, and is selected from the group consisting of surfactant amines, ionic liquids, and combinations thereof, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1.
- a formulation comprising: (a) at least one first amine; (b) at least one second amine; and (c) at least one additive having a weight percentage in the range of 0 to 5 % with respect to the formulation, and is selected from the group consisting of surfactant amines, ionic liquids, and combinations thereof, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8.5: 1 - 9.5: 1.
- a formulation as described herein wherein the formulation optionally comprises at least one additive having a weight percentage in the range of 0 to 5 % with respect to the formulation and selected from the group consisting of surfactant amines, ionic liquids, and combinations thereof.
- the at least one additive has a weight percentage in the range of 0.5 to 4.5 % with respect to the formulation.
- the at least one additive has a weight percentage has a weight percentage of 3 % with respect to the formulation.
- the at least one additive is surfactant amine.
- the at least one additive is ionic liquid.
- the additive is an ionic liquid, i.e. l-decyl-3- methylimidazolium chloride having a weight percentage of 2 % with respect to the formulation.
- a formulation comprising: (a) at least one first amine having a weight percentage in the range of 50 to 90 % with respect to the formulation; (b) at least one second amine having a weight percentage in the range of 5 to 10 % with respect to the formulation; and (c) at least one additive having a weight percentage in the range of 0 to 5 % with respect to the formulation.
- a formulation comprising: (a) at least one first amine having a weight percentage in the range of 50 to 90 % with respect to the formulation; (b) at least one second amine having a weight percentage in the range of 5 to 10 % with respect to the formulation; and (c) at least one additive having a weight percentage in the range of 0 to 5 % with respect to the formulation, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1.
- a formulation comprising: (a) at least one first amine having a weight percentage in the range of 50 to 90 % with respect to the formulation; (b) at least one second amine having a weight percentage in the range of 5 to 10 % with respect to the formulation; and (c) at least one additive having a weight percentage in the range of 0 to 5 % with respect to the formulation, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8.5: 1 - 9.5: 1.
- a formulation comprising: (a) at least one first amine having a weight percentage in the range of 50 to 90 % with respect to the formulation; (b) at least one second amine having a weight percentage in the range of 5 to 10 % with respect to the formulation; and (c) at least one additive having a weight percentage in the range of 0 to 5 % with respect to the formulation, wherein the at least one first amine to the at least one second amine weight ratio is 9: 1.
- a formulation comprising: (a) at least one first amine having a weight percentage in the range of 50 to 90 % with respect to the formulation; and (b) at least one second amine having a weight percentage in the range of 5 to 10 % with respect to the formulation, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1.
- a formulation comprising: (a) at least one first amine having a weight percentage in the range of 50 to 90 % with respect to the formulation; and (b) at least one second amine having a weight percentage in the range of 5 to 10 % with respect to the formulation, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8.5: 1 - 9.5: 1.
- a formulation comprising: (a) at least one first amine having a weight percentage in the range of 50 to 90 % with respect to the formulation; and (b) at least one second amine having a weight percentage in the range of 5 to 10 % with respect to the formulation, wherein the at least one first amine to the at least one second amine weight ratio is 9: 1.
- a process for preparing the formulation comprising: (a) at least one first amine; and (b) at least one second amine, the process comprising: (a) obtaining the at least one first amine; (b) obtaining the at least one second amine; and (c) contacting the at least one first amine, the at least one second amine to obtain the formulation.
- a process for preparing the formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1, the process comprising: (a) obtaining the at least one first amine; (b) obtaining the at least one second amine; and (c) contacting the at least one first amine, the at least one second amine, and optionally the at least one additive to obtain the formulation.
- a process for preparing the formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8.5: 1 - 9.5: 1, the process comprising: (a) obtaining the at least one first amine; (b) obtaining the at least one second amine; and (c) contacting the at least one first amine, the at least one second amine, and optionally the at least one additive to obtain the formulation.
- a process for preparing the formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1, the process comprising: (a) obtaining the at least one first amine; (b) obtaining at least one second amine, i.e., a reaction product obtained by contacting epichlorohydrin, and at least one first amine at a temperature in the range of 40 - 60 °C for a period in the range of 2 - 4 hours; and (c) contacting the at least one first amine, the at least one second amine, and optionally the at least one additive to obtain the formulation.
- reaction product obtained by contacting epichlorohydrin, and at least one first amine at a temperature in the range of 40 - 60 °C for a period in the range of 2 - 4 hours.
- reaction product is obtained by contacting epichlorohydrin, and at least one first amine at a temperature in the range of 42 - 58 °C for a period in the range of 2.5 - 3.5 hours.
- reaction product is obtained by contacting epichlorohydrin, and at least one first amine at a temperature in the range of 50 °C for a period in the range of 3 hours.
- contacting the at least one first amine, the at least one second amine, and optionally the at least one additive to obtain the formulation is carried out at a temperature in the range of 25 °C - 60 °C for a period in the range of 10 minutes - 120 minutes.
- contacting the at least one first amine, the at least one second amine, and optionally the at least one additive to obtain the formulation is carried out at a temperature in the range of 35 °C - 55 °C for a period in the range of 20 minutes - 100 minutes.
- contacting the at least one first amine, the at least one second amine, and optionally the at least one additive to obtain the formulation is carried out at a temperature in the range of 40 °C for a period in the range of 20 minutes.
- a process for preparing the formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1, the process comprising: (a) obtaining the at least one first amine; (b) obtaining the at least one second amine; and (c) contacting the at least one first amine, the at least one second amine, and optionally the at least one additive to obtain the formulation is carried out at a temperature in the range of 25 °C - 60 °C for a period in the range of 10 minutes - 120 minutes.
- a process for preparing the formulation comprising: (a) at least one first amine; and (b) at least one second amine, the process comprising: (a) obtaining the at least one first amine; (b) obtaining the at least one second amine is carried out by contacting epichlorohydrin, and at least one first amine at a temperature in the range of 40 - 60 °C for a period in the range of 2 - 4 hours; and (c) contacting the at least one first amine, the at least one second amine carried out at a temperature in the range of 25 °C - 60 °C for a period in the range of 10 minutes - 120 minutes to obtain the formulation.
- a process for preparing the formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1, the process comprising: (a) obtaining the at least one first amine; (b) obtaining at least one second amine, i.e., a reaction product obtained by contacting epichlorohydrin, and at least one first amine at a temperature in the range of 40 - 60 °C for a period in the range of 2 - 4 hours; and (c) contacting the at least one first amine, the at least one second amine carried out at a temperature in the range of 25 °C - 60 °C for a period in the range of 10 minutes - 120 minutes to obtain the formulation.
- a process for preparing the formulation comprising: (a) at least one first amine; (b) at least one second amine; and (c) at least one additive, the process comprising: (a) obtaining the at least one first amine; (b) obtaining the at least one second amine; (c) obtaining at least one additive; and (c) contacting the at least one first amine, the at least one second amine, and the at least one additive to obtain the formulation.
- a process for preparing the formulation comprising: (a) at least one first amine; (b) at least one second amine; and (c) at least one additive, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1, the process comprising: (a) obtaining the at least one first amine; (b) obtaining at least one second amine, i.e., a reaction product obtained by contacting epichlorohydrin, and at least one first amine at a temperature in the range of 40 - 60 °C for a period in the range of 2 - 4 hours; (c) obtaining at least one additive; and (c) contacting the at least one first amine, the at least one second amine, and the at least one additive is carried out at a temperature in the range of 25 °C - 60 °C for a period in the range of 10 minutes - 120 minutes to obtain the formulation.
- a method of reducing fouling in a petroleum refinery comprising, adding the formulation comprising: (a) at least one first amine; (b) at least one second amine; and (c) at least one additive, to a water system.
- a method of reducing fouling in a petroleum refinery comprising, adding the formulation comprising: (a) at least one first amine; and (b) at least one second amine to a water system, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1.
- a method of reducing fouling in a petroleum refinery comprising, adding the formulation comprising: (a) at least one first amine; and (b) at least one second amine to a water system, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1, wherein the at least one second amine is a product of epichlorohydrin and the at least one first amine.
- a method of reducing fouling in a petroleum refinery comprising, adding the formulation comprising: (a) at least one first amine; (b) at least one second amine; and (c) at least one additive, to a water system, wherein the water system is an oil refinery overhead system.
- a method of reducing fouling in a petroleum refinery comprising, adding the formulation comprising: (a) at least one first amine; and (b) at least one second amine to a water system, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1 and the water system is an oil refinery overhead system.
- a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1, wherein the formulation can act as a film forming neutralizing amine for reducing fouling in a petroleum refinery.
- the amines (at least one amine) used in the Example 1 and Example 2 can be replaced by the following amines alone or in combination to obtain the at least one second amine of the present disclosure.
- the formulation of the present disclosure was prepared as follows: 90 % (w/w) of the first amine and 10 % (w/w) of the second amine were mixed together at a temperature in the range of 25 °C - 60 °C for a period in the range of 10 minutes - 120 minutes to obtain the formulation of the present disclosure.
- the formulation with the additive was prepared in a similar manner as described in Example 3, wherein the weight percentages of the components were kept as below: 90 % (w/w) of the first amine; 8 % (w/w) of the second amine; and 2 % (w/w) of at least one additive.
- said additive is l-decyl-3-methylimidazolium chloride (ionic liquid).
- the solution of morpholine, compound 2 and l-decyl-3-methylimidazolium chloride were heated at 40-60 °C for 20 min to obtain the neutralizing amine formulation.
- the obtained thermic fluid composition is only acceptable when certain specific base fluids are used during the preparation.
- inventive Formulations 2, 4, 6 and 7 comprising a combination of at least one first amine and at least one second amine in a weight ratio range 8: 1 to 10: 1, required lower dose to achieve the required pH range.
- the corrosion rate experiments are performed with HC1 solution.
- the HC1 was neutralized with suitable amount of amine from the Formulations of Table 2.
- the corrosion rate experiments were performed on Carbon steel coupon at 120 °C in a closed system by using high temperature and high pressure reactor. Said system simulates the water system in an oil refinery overhead system.
- Formulations 1 and 2 depicted in the Table 2 above correspond to the Formulations 1 and 2 of the Table 1.
- the numbering has hence been retained to ensure clarity.
- the Formulation 7 comprises 90 % by weight diethanol amine, 8% by weight compound 1 and 2% by weight ionic liquid (l-decyl-3-methylimidazolium chloride).
- the present disclosure provides a formulation comprising at least one first amine and at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1.
- the formulation is capable of neutralizing acidic components, i.e., the neutralizing formulation effectively neutralizes the acidic species, such as hydrochloric acid (HC1) or acidic sulfur species, and as a result combat the primary corrosion problem encountered in crude distillation unit overhead systems, thus minimizing the deposition of resulting amine salt to on overhead condensing equipment surfaces. Fouling of overhead condensing in crude distillation unit is minimized by the usage of formulation of the present disclosure, thereby reducing the productivity loss due to cleaning and/or replacing fouled equipment.
- the process of preparation of the formulation, as well as a method for reducing fouling of petroleum refinery are also disclosed herein.
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Preventing Corrosion Or Incrustation Of Metals (AREA)
Abstract
The instant disclosure provides formulation for corrosion inhibition. The formulation comprising: a) at least one first amine; and b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 – 10: 1. The instant disclosure also provides a process for preparing the formulation. Also, the instant disclosure provides a method of reducing fouling in a petroleum refinery.
Description
A NEUTRALIZING AMINE FORMULATION AND PROCESS OF
PREPARATION THEREOF
FIELD OF THE INVENTION
[001] The present disclosure generally relates to the field of inhibiting corrosion in the crude distillation units of refineries. In particular the present disclosure discloses a formulation which combats the problem associated of condensing hydrocarbons which contain water and chlorides
BACKGROUND OF THE INVENTION
[002] Refineries employ neutralizing amines to guard their crude distillation unit overhead systems from corrosion due to hydrochloric acid (HC1) or acidic sulfur species and fouling due to build-up of sublimating species. The amines are usually organic amines (such as di-ethanol amine, monoethanol amine, triethanolamine, morpholine, piperazine, etc.) which function by neutralizing acidic contaminants, thereby increasing the pH to an appropriate level for minimizing corrosion of the various system. Unfortunately, some of the best amines for refinery steam system protection are the least compatible with the crude unit processes.
[003] US 4,062,764 discloses that alkoxylated amines are useful in neutralizing the initial condensate. US 3,472,666 suggests that alkoxy substituted aromatic amines in which the alkoxy group contains from 1 to 10 carbon atoms are effective corrosion inhibitors in petroleum refining operations. Representative examples of these materials are aniline, anisidine and phenetidines.
[004] US 4,430,196 discloses the utility of hydroxylated amines. Representative examples of these neutralizing amines are dimethylisopropanolamine and dimethylaminoethanol.
[005] US 3,981,780 suggests that a mixture of the salt of a dicarboxylic acid and cyclic amines are useful corrosion inhibitors when used in conjunction with traditional neutralizing agents, such as ammonia.
[006] Many problems are associated with traditional neutralizing amines, i.e., formation of hydrochloride or sulfide salts of those neutralizing amines which will
condense at the water dew point on metallic surfaces. The salts appear before the dew point of water is reached and result in fouling and under-deposit corrosion.
[007] Accordingly, there is a need in the art for a neutralizing formulation/agent which can effectively neutralize the acidic species and as a result combat the primary corrosion problem encountered in crude distillation unit overhead systems.
SUMMARY OF THE INVENTION
[008] In an aspect of the present disclosure, there is provided a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1.
[009] In an aspect of the present disclosure, there is provided a process for preparing the formulation comprising: (a) at least one first amine; and (b) at least one second amine, the process comprising: (a) obtaining the at least one first amine; (b) obtaining the at least one second amine; (c) contacting the at least one first amine, the at least one second amine, and optionally the at least one additive to obtain the formulation, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1.
[0010] In an aspect of the present disclosure, there is provided a method of reducing fouling in a petroleum refinery comprising, adding the formulation comprising: (a) at least one first amine; and (b) at least one second amine to a water system.
[0011] These and other features, aspects, and advantages of the present subject matter will be better understood with reference to the following description and appended claims. This summary is provided to introduce a selection of concepts in a simplified form. This summary is not intended to identify key features or essential features of the claimed subject matter, nor is it intended to be used to limit the scope of the claimed subject matter.
DETAILED DESCRIPTION OF THE INVENTION
[0012] Those skilled in the art will be aware that the present disclosure is subject to variations and modifications other than those specifically described. It is to be understood that the present disclosure includes all such variations and modifications.
The disclosure also includes all such steps, features, compositions and compounds referred to or indicated in this specification, individually or collectively, and any and all combinations of any or more of such steps or features.
Definitions.
[0013] For convenience, before further description of the present disclosure, certain terms employed in the specification, and examples are collected here. These definitions should be read in the light of the remainder of the disclosure and understood as by a person of skill in the art. The terms used herein have the meanings recognized and known to those of skill in the art, however, for convenience and completeness, particular terms and their meanings are set forth below.
[0014] The articles“a”,“an” and“the” are used to refer to one or to more than one (i.e., to at least one) of the grammatical object of the article.
[0015] The terms“comprise” and“comprising” are used in the inclusive, open sense, meaning that additional elements may be included. It is not intended to be construed as “consists of only”.
[0016] The term fouling and/or corrosion problem refers to aqueous corrosion due to hydrochloric acid (HC1) or acidic sulfur species, or the build-up of sublimating species such as ammonium chloride under deposit corrosion in distillation units.
[0017] The term“surfactant amine” refer to fatty acid amines which can be used as surfactants. Such surfactant amines include, by way of example Ci-io alkyl ammonium chloride, alkyldimethyl ammonium chloride. The term alkyl herein refers to a branched or unbranched chain having 1-10 carbon atoms. Additionally, the surfactant amines in the present disclosure are those which are known to a person skilled in the art.
[0018] The term“ionic liquid” are used to refer quaternary ammonium compounds known to a person skilled in the art.
[0019] Throughout this specification, unless the context requires otherwise the word “comprise”, and variations such as“comprises” and“comprising”, will be understood to imply the inclusion of a stated element or step or group of element or steps but not the exclusion of any other element or steps.
[0020] The term “including” is used to mean “including but not limited to”, “including” and“including but not limited to” are used interchangeably.
[0021] Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood to one of ordinary skill in the art to which this disclosure belongs. Although methods and materials similar or equivalent to those described herein can be used in the practice or testing of the disclosure, the preferred methods, and materials are now described. All publications mentioned herein are incorporated herein by reference.
[0022] Ratios, concentrations, amounts, and other numerical data may be presented herein in a range format. It is to be understood that such range format is used merely for convenience and brevity and should be interpreted flexibly to include not only the numerical values explicitly recited as the limits of the range, but also to include all the individual numerical values or sub-ranges encompassed within that range as if each numerical value and sub-range is explicitly recited. For example, a weight percentage of about 50 % to 90 % should be interpreted to include not only the explicitly recited limits of about 50% and 90 %, but also to include sub-ranges, such as 55-85 %, 65-75%, and so forth, as well as individual amounts, including fractional amounts, within the specified ranges, such as 90 %, 85 %, for example.
[0023] The present disclosure is not to be limited in scope by the specific embodiments described herein, which are intended for the purposes of exemplification only. Functionally equivalent products, compositions, and methods are clearly within scope of the disclosure, as described herein.
[0024] As discussed in the background section, to counter the problems associated with the traditional neutralizing amines, the formulation of the present disclosure provides a neutralizing formulation/agent comprising: (a) at least one first amine; and (b) at least one second amine. The at least one first amine to the at least one second amine present in the formulation can have a weight ratio is in the range of 8: 1 - 10: 1. The neutralizing formulation effectively neutralizes the acidic species and as a result combat the primary corrosion problem encountered in crude distillation unit overhead systems.
[0025] In an embodiment of the present disclosure, there is provided a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1.
[0026] In an embodiment of the present disclosure, there is provided a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8.5: 1 - 9.5: 1.
[0027] In an embodiment of the present disclosure, there is provided a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is 9: 1.
[0028] In an embodiment of the present disclosure, there is provided a formulation as described herein, wherein the at least one first amine has a weight percentage in the range of 50 to 95 % with respect to the formulation.
[0029] In an embodiment of the present disclosure, there is provided a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1 and the at least one first amine has a weight percentage in the range of 50 to 95 % with respect to the formulation.
[0030] In an embodiment of the present disclosure, there is provided a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8.5: 1 - 9.5: 1 and the at least one first amine has a weight percentage in the range of 50 to 95 % with respect to the formulation.
[0031] In an embodiment of the present disclosure, there is provided a formulation as described herein, wherein the at least one first amine has a weight percentage in the range of 60 to 95 % with respect to the formulation. In another embodiment the at least one first amine has a weight percentage in the range of 75 to 92 % with respect to the formulation. In yet another embodiment the at least one first amine has a weight percentage in the range of 80 to 90 % with respect to the formulation.
[0032] In an embodiment of the present disclosure, there is provided a formulation as described herein, wherein the at least one first amine is selected from the group consisting of diethanolamine, morpholine, monoethanolamine, triethanolamine, cyclohexylamine, piperazine, diethylaminoethanol, methyldiethanolamine, ethyl ethanolamine, aminoethyl piperazine, and combinations thereof.
[0033] In an embodiment of the present disclosure, there is provided a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1 and the at least one first amine is selected from the group consisting of diethanolamine, morpholine, monoethanolamine, triethanolamine, cyclohexylamine, piperazine, diethylaminoethanol, methyldiethanolamine, ethyl ethanolamine, aminoethyl piperazine, and combinations thereof.
[0034] In an embodiment of the present disclosure, there is provided a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8.5: 1 - 9.5: 1 and the at least one first amine is selected from the group consisting of diethanolamine, morpholine, monoethanolamine, triethanolamine, cyclohexylamine, piperazine, diethylaminoethanol, methyldiethanolamine, ethyl ethanolamine, aminoethyl piperazine, and combinations thereof.
[0035] In an embodiment of the present disclosure, there is provided a formulation as described herein, wherein the at least one first amine is selected from the group consisting of diethanolamine, morpholine, monoethanolamine, triethanolamine, cyclohexylamine, piperazine, diethylaminoethanol, and combinations thereof. In another embodiment the at least one first amine is selected from the group consisting of diethanolamine, morpholine, monoethanolamine, triethanolamine, cyclohexylamine, piperazine, and combinations thereof. In yet another embodiment the at least one first amine is selected from diethanolamine or morpholine. In yet another embodiment the at least one first amine is selected from the group consisting of diethanolamine, morpholine, diethylaminoethanol, and combinations thereof.
[0036] In an embodiment of the present disclosure, there is provided a formulation as described herein, wherein the at least one second amine has a weight percentage in the range of 5 to 15 % with respect to the formulation.
[0037] In an embodiment of the present disclosure, there is provided a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1 and the at least one second amine has a weight percentage in the range of 5 to 15 % with respect to the formulation.
[0038] In an embodiment of the present disclosure, there is provided a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8.5: 1 - 9.5: 1 and the at least one second amine has a weight percentage in the range of 5 to 15 % with respect to the formulation.
[0039] In an embodiment of the present disclosure, there is provided a formulation as described herein, wherein the at least one second amine has a weight percentage in the range of 6 to 15 % with respect to the formulation. In another embodiment the at least one second amine has a weight percentage in the range of 8 to 12 % with respect to the formulation. In yet another embodiment the at least one second amine has a weight percentage of 10 % with respect to the formulation.
[0040] In an embodiment of the present disclosure, there is provided a formulation as described herein, wherein the at least one second amine is a product of epichlorohydrin and the at least one first amine.
[0041] In an embodiment of the present disclosure, there is provided a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1 and the at least one second amine is a product of epichlorohydrin and the at least one first amine and the at least one first amine.
[0042] In an embodiment of the present disclosure, there is provided a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of
8.5: 1 - 9.5: 1 and the at least one second amine is a product of epichlorohydrin and the at least one first amine and the at least one first amine.
[0043] In an embodiment of the present disclosure, there is provided a formulation as described herein, wherein the at least one second amine is a product of epichlorohydrin and the at least one first amine, and has a weight percentage in the range of 5 to 15 % with respect to the formulation. In another embodiment the at least one second amine is a product of epichlorohydrin and the at least one first amine, and has a weight percentage in the range of 6 to 15 % with respect to the formulation. In one another embodiment the at least one second amine is a product of epichlorohydrin and the at least one first amine, has a weight percentage in the range of 8 to 12 % with respect to the formulation. In yet another embodiment the at least one second amine is a product of epichlorohydrin and the at least one first amine, and has a weight percentage of 10 % with respect to the formulation.
[0044] In an embodiment of the present disclosure, there is provided a formulation as described herein, wherein the at least one second amine is a product of epichlorohydrin and the at least one first amine selected from the group consisting of diethanolamine, morpholine, monoethanolamine, triethanolamine, cyclohexylamine, piperazine, diethylaminoethanol, methyldiethanolamine, ethyl ethanolamine, aminoethyl piperazine, and combinations thereof.
[0045] In an embodiment of the present disclosure, there is provided a formulation as described herein, wherein the at least one second amine has a weight percentage in the range of 5 to 15 % with respect to the formulation, and is a product of epichlorohydrin and the at least one first amine selected from the group consisting of diethanolamine, morpholine, monoethanolamine, triethanolamine, cyclohexylamine, piperazine, diethylaminoethanol, methyldiethanolamine, ethyl ethanolamine, aminoethyl piperazine, and combinations thereof.
[0046] In an embodiment of the present disclosure, there is provided a formulation as described herein, wherein the at least one second amine has a weight percentage in the range of 5 to 15 % with respect to the formulation, and is a product of epichlorohydrin and the at least one first amine selected from the group consisting of diethanolamine,
morpholine, monoethanolamine, triethanolamine, cyclohexylamine, piperazine, diethylaminoethanol, methyldiethanolamine, ethyl ethanolamine, aminoethyl piperazine, and combinations thereof and the at least one first amine has a weight percentage in the range of 50 to 95 % with respect to the formulation.
[0047] In an embodiment of the present disclosure, there is provided a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1 and the at least one first amine is selected from the group consisting of diethanolamine, morpholine, monoethanolamine, triethanolamine, cyclohexylamine, piperazine, diethylaminoethanol, methyldiethanolamine, ethyl ethanolamine, aminoethyl piperazine, and combinations thereof and the at least one second amine is a product of epichlorohydrin and the at least one first amine.
[0048] In an embodiment of the present disclosure, there is provided a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8.5: 1 - 9.5: 1 and the at least one first amine is selected from the group consisting of diethanolamine, morpholine, monoethanolamine, triethanolamine, cyclohexylamine, piperazine, diethylaminoethanol, methyldiethanolamine, ethyl ethanolamine, aminoethyl piperazine, and combinations thereof and the at least one second amine is a product of epichlorohydrin and the at least one first amine.
[0049] In an embodiment of the present disclosure, there is provided a formulation comprising: (a) at least one first amine; (b) at least one second amine; and (c) at least one additive having a weight percentage in the range of 0 to 5 % with respect to the formulation; and is selected from the group consisting of surfactant amines, ionic liquids, and combinations thereof.
[0050] In an embodiment of the present disclosure, there is provided a formulation comprising: (a) at least one first amine; (b) at least one second amine; and (c) at least one additive having a weight percentage in the range of 0 to 5 % with respect to the formulation, and is selected from the group consisting of surfactant amines, ionic
liquids, and combinations thereof, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1.
[0051] In an embodiment of the present disclosure, there is provided a formulation comprising: (a) at least one first amine; (b) at least one second amine; and (c) at least one additive having a weight percentage in the range of 0 to 5 % with respect to the formulation, and is selected from the group consisting of surfactant amines, ionic liquids, and combinations thereof, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8.5: 1 - 9.5: 1.
[0052] In an embodiment of the present disclosure, there is provided a formulation as described herein, wherein the formulation optionally comprises at least one additive having a weight percentage in the range of 0 to 5 % with respect to the formulation and selected from the group consisting of surfactant amines, ionic liquids, and combinations thereof. In another embodiment the at least one additive has a weight percentage in the range of 0.5 to 4.5 % with respect to the formulation. In one another embodiment the at least one additive has a weight percentage has a weight percentage of 3 % with respect to the formulation. In yet another embodiment the at least one additive is surfactant amine. In another embodiment the at least one additive is ionic liquid. In another embodiment of the present disclosure, the additive is an ionic liquid, i.e. l-decyl-3- methylimidazolium chloride having a weight percentage of 2 % with respect to the formulation.
[0053] In an embodiment of the present disclosure, there is provided a formulation comprising: (a) at least one first amine having a weight percentage in the range of 50 to 90 % with respect to the formulation; (b) at least one second amine having a weight percentage in the range of 5 to 10 % with respect to the formulation; and (c) at least one additive having a weight percentage in the range of 0 to 5 % with respect to the formulation.
[0054] In an embodiment of the present disclosure, there is provided a formulation comprising: (a) at least one first amine having a weight percentage in the range of 50 to 90 % with respect to the formulation; (b) at least one second amine having a weight percentage in the range of 5 to 10 % with respect to the formulation; and (c) at least one
additive having a weight percentage in the range of 0 to 5 % with respect to the formulation, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1.
[0055] In an embodiment of the present disclosure, there is provided a formulation comprising: (a) at least one first amine having a weight percentage in the range of 50 to 90 % with respect to the formulation; (b) at least one second amine having a weight percentage in the range of 5 to 10 % with respect to the formulation; and (c) at least one additive having a weight percentage in the range of 0 to 5 % with respect to the formulation, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8.5: 1 - 9.5: 1.
[0056] In an embodiment of the present disclosure, there is provided a formulation comprising: (a) at least one first amine having a weight percentage in the range of 50 to 90 % with respect to the formulation; (b) at least one second amine having a weight percentage in the range of 5 to 10 % with respect to the formulation; and (c) at least one additive having a weight percentage in the range of 0 to 5 % with respect to the formulation, wherein the at least one first amine to the at least one second amine weight ratio is 9: 1.
[0057] In an embodiment of the present disclosure, there is provided a formulation comprising: (a) at least one first amine having a weight percentage in the range of 50 to 90 % with respect to the formulation; and (b) at least one second amine having a weight percentage in the range of 5 to 10 % with respect to the formulation, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1.
[0058] In an embodiment of the present disclosure, there is provided a formulation comprising: (a) at least one first amine having a weight percentage in the range of 50 to 90 % with respect to the formulation; and (b) at least one second amine having a weight percentage in the range of 5 to 10 % with respect to the formulation, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8.5: 1 - 9.5: 1.
[0059] In an embodiment of the present disclosure, there is provided a formulation comprising: (a) at least one first amine having a weight percentage in the range of 50 to 90 % with respect to the formulation; and (b) at least one second amine having a weight percentage in the range of 5 to 10 % with respect to the formulation, wherein the at least one first amine to the at least one second amine weight ratio is 9: 1.
[0060] In an embodiment of the present disclosure there is provided a process for preparing the formulation comprising: (a) at least one first amine; and (b) at least one second amine, the process comprising: (a) obtaining the at least one first amine; (b) obtaining the at least one second amine; and (c) contacting the at least one first amine, the at least one second amine to obtain the formulation.
[0061] In an embodiment of the present disclosure there is provided a process for preparing the formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1, the process comprising: (a) obtaining the at least one first amine; (b) obtaining the at least one second amine; and (c) contacting the at least one first amine, the at least one second amine, and optionally the at least one additive to obtain the formulation.
[0062] In an embodiment of the present disclosure there is provided a process for preparing the formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8.5: 1 - 9.5: 1, the process comprising: (a) obtaining the at least one first amine; (b) obtaining the at least one second amine; and (c) contacting the at least one first amine, the at least one second amine, and optionally the at least one additive to obtain the formulation.
[0063] In an embodiment of the present disclosure there is provided a process for preparing the formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1, the process comprising: (a) obtaining the at least one first amine; (b) obtaining at least one second amine, i.e., a reaction product obtained by contacting epichlorohydrin, and at least one first amine at a temperature in the range of
40 - 60 °C for a period in the range of 2 - 4 hours; and (c) contacting the at least one first amine, the at least one second amine, and optionally the at least one additive to obtain the formulation.
[0064] In an embodiment of the present disclosure there is provided a process for preparing the formulation as described herein, wherein at least one second amine is a reaction product obtained by contacting epichlorohydrin, and at least one first amine at a temperature in the range of 40 - 60 °C for a period in the range of 2 - 4 hours. In another embodiment reaction product is obtained by contacting epichlorohydrin, and at least one first amine at a temperature in the range of 42 - 58 °C for a period in the range of 2.5 - 3.5 hours. In one another embodiment reaction product is obtained by contacting epichlorohydrin, and at least one first amine at a temperature in the range of 50 °C for a period in the range of 3 hours.
[0065] In an embodiment of the present disclosure there is provided a process as described herein, wherein contacting the at least one first amine, the at least one second amine, and optionally the at least one additive to obtain the formulation is carried out at a temperature in the range of 25 °C - 60 °C for a period in the range of 10 minutes - 120 minutes. In another embodiment contacting the at least one first amine, the at least one second amine, and optionally the at least one additive to obtain the formulation is carried out at a temperature in the range of 35 °C - 55 °C for a period in the range of 20 minutes - 100 minutes. In another embodiment contacting the at least one first amine, the at least one second amine, and optionally the at least one additive to obtain the formulation is carried out at a temperature in the range of 40 °C for a period in the range of 20 minutes.
[0066] In an embodiment of the present disclosure there is provided a process for preparing the formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1, the process comprising: (a) obtaining the at least one first amine; (b) obtaining the at least one second amine; and (c) contacting the at least one first amine, the at least one second amine, and optionally the at least one additive to obtain the formulation is carried out at a temperature in the range of 25 °C - 60 °C for a period in the range of 10 minutes - 120 minutes.
[0067] In an embodiment of the present disclosure there is provided a process for preparing the formulation comprising: (a) at least one first amine; and (b) at least one second amine, the process comprising: (a) obtaining the at least one first amine; (b) obtaining the at least one second amine is carried out by contacting epichlorohydrin, and at least one first amine at a temperature in the range of 40 - 60 °C for a period in the range of 2 - 4 hours; and (c) contacting the at least one first amine, the at least one second amine carried out at a temperature in the range of 25 °C - 60 °C for a period in the range of 10 minutes - 120 minutes to obtain the formulation.
[0068] In an embodiment of the present disclosure there is provided a process for preparing the formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1, the process comprising: (a) obtaining the at least one first amine; (b) obtaining at least one second amine, i.e., a reaction product obtained by contacting epichlorohydrin, and at least one first amine at a temperature in the range of 40 - 60 °C for a period in the range of 2 - 4 hours; and (c) contacting the at least one first amine, the at least one second amine carried out at a temperature in the range of 25 °C - 60 °C for a period in the range of 10 minutes - 120 minutes to obtain the formulation.
[0069] In an embodiment of the present disclosure there is provided a process for preparing the formulation comprising: (a) at least one first amine; (b) at least one second amine; and (c) at least one additive, the process comprising: (a) obtaining the at least one first amine; (b) obtaining the at least one second amine; (c) obtaining at least one additive; and (c) contacting the at least one first amine, the at least one second amine, and the at least one additive to obtain the formulation.
[0070] In an embodiment of the present disclosure there is provided a process for preparing the formulation comprising: (a) at least one first amine; (b) at least one second amine; and (c) at least one additive, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1, the process comprising: (a) obtaining the at least one first amine; (b) obtaining at least one second amine, i.e., a reaction product obtained by contacting epichlorohydrin, and at least one first amine at
a temperature in the range of 40 - 60 °C for a period in the range of 2 - 4 hours; (c) obtaining at least one additive; and (c) contacting the at least one first amine, the at least one second amine, and the at least one additive is carried out at a temperature in the range of 25 °C - 60 °C for a period in the range of 10 minutes - 120 minutes to obtain the formulation.
[0071] In an embodiment of the present disclosure there is provided a method of reducing fouling in a petroleum refinery comprising, adding the formulation comprising: (a) at least one first amine; (b) at least one second amine; and (c) at least one additive, to a water system.
[0072] In an embodiment of the present disclosure there is provided a method of reducing fouling in a petroleum refinery comprising, adding the formulation comprising: (a) at least one first amine; and (b) at least one second amine to a water system, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1.
[0073] In an embodiment of the present disclosure there is provided a method of reducing fouling in a petroleum refinery comprising, adding the formulation comprising: (a) at least one first amine; and (b) at least one second amine to a water system, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1, wherein the at least one second amine is a product of epichlorohydrin and the at least one first amine.
[0074] In an embodiment of the present disclosure there is provided a method of reducing fouling in a petroleum refinery comprising, adding the formulation comprising: (a) at least one first amine; (b) at least one second amine; and (c) at least one additive, to a water system, wherein the water system is an oil refinery overhead system.
[0075] In an embodiment of the present disclosure there is provided a method of reducing fouling in a petroleum refinery as described herein, wherein the water system is in an oil refinery overhead system.
[0076] In an embodiment of the present disclosure there is provided a method of reducing fouling in a petroleum refinery comprising, adding the formulation comprising: (a) at least one first amine; and (b) at least one second amine to a water system, wherein
the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1 and the water system is an oil refinery overhead system.
[0077] In an embodiment of the present disclosure there is provided a formulation comprising: (a) at least one first amine; and (b) at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1, wherein the formulation can act as a film forming neutralizing amine for reducing fouling in a petroleum refinery.
[0078] Although the subject matter has been described in considerable detail with reference to certain preferred embodiments thereof, other embodiments are possible.
EXAMPLES
[0079] The disclosure will now be illustrated with working examples, which is intended to illustrate the working of disclosure and not intended to take restrictively to imply any limitations on the scope of the present disclosure. Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood to one of ordinary skill in the art to which this disclosure belongs. Although methods and materials similar or equivalent to those described herein can be used in the practice of the disclosed methods and compositions, the exemplary methods, devices and materials are described herein. It is to be understood that this disclosure is not limited to particular methods, and experimental conditions described, as such methods and conditions may apply.
[0080] It is well recognized that corrosion will occur on the internal surfaces of refinery equipment when amine salts condense above the temperature of the water dewpoint. The neutralization formulation of the present disclosure neutralizes the acidic components at the point of initial condensation and minimizes/ eliminates deposits of salts on metal surfaces of distillation columns and thereby avoids formation of fouling and under deposit corrosion.
Example 1
Process for preparing second amine (Compound 1):
[0081] The general outline of the process disclosed in the present disclosure has been depicted as Scheme- 1 in the following section. Epichlorohydin (1 mole) was mixed with
2 moles of diethanolamine (at least one amine) at a temperature of 50 °C. The mixture was stirred for a period of 3 hours to obtain the Compound 1. LC-MS peak at 267 confirmed the formation of compound.
[0082]
Compound-211 «;
Scheme 1
Example 2
Process for preparing second amine (Compound 2):
[0083] Epichlorohydin ( 1 mole) was mixed with 2 moles of morpholine at a temperature of 50 °C stirred for a period of 3 hours to obtain the Compound 2. LC-MS peak at 231 confirmed the formation of compound.
[0084] The amines (at least one amine) used in the Example 1 and Example 2 can be replaced by the following amines alone or in combination to obtain the at least one second amine of the present disclosure.
(a) monoethanolamine, (b) triethanolamine, (c) cyclohexylamine, (d) piperazine, (e) diethylaminoethanol, (f) methyldiethanolamine, (g) ethyl ethanolamine, (h) aminoethyl piperazine.
A person skilled in the art would be able to modify the provided process to obtain alternate combinations. For instance, the Compound 3 (refer Table 1) was prepared in a manner similar to the process employed to obtain Compound 1, by conveniently replacing diethanolamine with monoethanol amine.
Example 3
Process of preparing the Formulation of the present disclosure:
[0085] The formulation of the present disclosure was prepared as follows: 90 % (w/w) of the first amine and 10 % (w/w) of the second amine were mixed together at a temperature in the range of 25 °C - 60 °C for a period in the range of 10 minutes - 120 minutes to obtain the formulation of the present disclosure.
Example 4
Process of preparing the Formulation with the additive:
[0086] The formulation with the additive was prepared in a similar manner as described in Example 3, wherein the weight percentages of the components were kept as below: 90 % (w/w) of the first amine; 8 % (w/w) of the second amine; and 2 % (w/w) of at least one additive. For instance, said additive is l-decyl-3-methylimidazolium chloride (ionic liquid). The solution of morpholine, compound 2 and l-decyl-3-methylimidazolium chloride were heated at 40-60 °C for 20 min to obtain the neutralizing amine formulation.
Example 5
Neutralizing capacity of the Formulation of the present disclosure:
[0087] The studies were performed by using high temperature (70 °C) pH measurements in a closed system. The inhibitory efficiency was calculated based on amine required to obtain the pH in the range of 8 to 9. From the data given in Table 1 below it is clear that the Formulations 2, 4 and 6 comprising 10 % concentration of Compound 1, Compound 2, and Compound 3, respectively, significantly improved the neutralizing activity in a synergetic manner in comparison with the base amine. Similarly, the Formulation 7 comprising 8% of compound 1 and 2% of l-decyl-3-methylimidazolium chloride (IF). The lower dosage to achieve said pH range was considered particularly useful.
Table 1
[0088] Thus, it can be summarized that the obtained thermic fluid composition is only acceptable when certain specific base fluids are used during the preparation. In other words, the inventive Formulations 2, 4, 6 and 7 comprising a combination of at least one first amine and at least one second amine in a weight ratio range 8: 1 to 10: 1, required lower dose to achieve the required pH range.
Example 6
Corrosion inhibition by the Formulation of the present disclosure:
[0089] The corrosion rate experiments are performed with HC1 solution. The HC1 was neutralized with suitable amount of amine from the Formulations of Table 2. The corrosion rate experiments were performed on Carbon steel coupon at 120 °C in a closed system by using high temperature and high pressure reactor. Said system simulates the water system in an oil refinery overhead system.
[0090] The summary of the corrosion rates is given below in Table 2. As can be seen, the amine blend (formulation) has superior activity in comparison with pure amine. Table 2
CS- carbon steel
[0091] The Formulations 1 and 2 depicted in the Table 2 above, correspond to the Formulations 1 and 2 of the Table 1. The numbering has hence been retained to ensure
clarity. Further, the Formulation 7 comprises 90 % by weight diethanol amine, 8% by weight compound 1 and 2% by weight ionic liquid (l-decyl-3-methylimidazolium chloride).
[0092] The results depicted in the Table 2 indicate the surprising enhancement in corrosion inhibition observable upon involvement of Formulation of the instant Application (refer Formulations 2 and 7). In particular, the inventive Formulation 2 was found to slow down the corrosion rate in carbon steel dramatically (a reduction in rate by 18%), whereas the inventive Formulation 7 revealed a reduction in rate by -24% in comparison to the base amine (diethanolamine). Thus, the enhancement suggested by Formulation 7, clearly indicates the beneficial role of the ionic liquid additive.
[0093] Although the subject matter has been described in considerable detail with reference to certain examples and implementations thereof, other implementations are possible.
Advantages of the present disclosure:
[0094] The present disclosure provides a formulation comprising at least one first amine and at least one second amine, wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1. The formulation is capable of neutralizing acidic components, i.e., the neutralizing formulation effectively neutralizes the acidic species, such as hydrochloric acid (HC1) or acidic sulfur species, and as a result combat the primary corrosion problem encountered in crude distillation unit overhead systems, thus minimizing the deposition of resulting amine salt to on overhead condensing equipment surfaces. Fouling of overhead condensing in crude distillation unit is minimized by the usage of formulation of the present disclosure, thereby reducing the productivity loss due to cleaning and/or replacing fouled equipment. The process of preparation of the formulation, as well as a method for reducing fouling of petroleum refinery are also disclosed herein.
Claims
1. A formulation comprising:
a) at least one first amine; and
b) at least one second amine,
wherein the at least one first amine to the at least one second amine weight ratio is in the range of 8: 1 - 10: 1.
2. The formulation as claimed in claim 1 , wherein the at least one first amine to the at least one second amine weight ratio is 9: 1.
3. The formulation as claimed in claim 1, wherein the at least one first amine has a weight percentage in the range of 50 to 95 % with respect to the formulation.
4. The formulation as claimed in claim 1, wherein the at least one first amine is selected from the group consisting of diethanolamine, morpholine, monoethanolamine, diethylaminoethanol, triethanolamine, cyclohexylamine, piperazine, methyldiethanolamine, ethyl ethanolamine, aminoethyl piperazine, and combinations thereof.
5. The formulation as claimed in claim 1, wherein the at least one second amine has a weight percentage in the range of 5 to 15 % with respect to the formulation.
6. The formulation as claimed in claim 1, wherein the at least one second amine is a product of epichlorohydrin and the at least one first amine.
7. The formulation as claimed in claim 1, wherein the formulation optionally comprises at least one additive having a weight percentage in the range of 0 to 5 % with respect to the formulation and selected from the group consisting of surfactant amines, ionic liquids, and combinations thereof.
8. A process for preparing the formulation as claimed in any one of the claims 1 - 7, the process comprising:
a. obtaining the at least one first amine;
b. obtaining the at least one second amine;
c. contacting the at least one first amine, the at least one second amine, and optionally the at least one additive to obtain the formulation.
9. The process as claimed in claim 8, wherein the at least one second amine is a reaction product obtained by contacting epichlorohydrin, and at least one first amine at a temperature in the range of 40 - 60 °C for a period in the range of 2 - 4 hours.
10. The process as claimed in claim 8, wherein contacting the at least one first amine, the at least one second amine, and optionally the at least one additive to obtain the formulation is carried out at a temperature in the range of 25 °C - 60 °C for a period in the range of 10 minutes - 120 minutes.
11. A method of reducing fouling in a petroleum refinery comprising, adding the formulation as claimed in claim 1 to a water system.
12. The method as claimed in claim 11, wherein the water system is in an oil refinery overhead system.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
IN201841025004 | 2018-07-04 | ||
IN201841025004 | 2018-07-04 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2020008477A1 true WO2020008477A1 (en) | 2020-01-09 |
Family
ID=67544291
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/IN2019/050494 WO2020008477A1 (en) | 2018-07-04 | 2019-07-02 | A neutralizing amine formulation and process of preparation thereof |
Country Status (1)
Country | Link |
---|---|
WO (1) | WO2020008477A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2022172279A1 (en) * | 2021-02-15 | 2022-08-18 | Hindustan Petroleum Corporation Limited | A corrosion inhibiting dioleyl compound, and a corrosion inhibiting film forming amine formulation thereof |
Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3472666A (en) | 1966-10-19 | 1969-10-14 | Exxon Research Engineering Co | Corrosion inhibitor |
US3779905A (en) * | 1971-09-20 | 1973-12-18 | Universal Oil Prod Co | Adding corrosion inhibitor to top of crude oil still |
US3930810A (en) * | 1974-07-31 | 1976-01-06 | Universal Oil Products Company | Additives for petroleum distillates |
US3981780A (en) | 1973-04-20 | 1976-09-21 | Compagnie Francaise De Raffinage | Compositions for inhibiting the corrosion of metals |
US4062764A (en) | 1976-07-28 | 1977-12-13 | Nalco Chemical Company | Method for neutralizing acidic components in petroleum refining units using an alkoxyalkylamine |
US4430196A (en) | 1983-03-28 | 1984-02-07 | Betz Laboratories, Inc. | Method and composition for neutralizing acidic components in petroleum refining units |
US5176847A (en) * | 1989-01-06 | 1993-01-05 | Baker Hughes Incorporated | Demulsifying composition |
WO2000001785A1 (en) * | 1998-07-01 | 2000-01-13 | Betzdearborn Inc. | Methods and compositions for inhibiting corrosion |
US20050183325A1 (en) * | 2004-02-24 | 2005-08-25 | Sutkowski Andrew C. | Conductivity improving additive for fuel oil compositions |
US20110147275A1 (en) * | 2009-12-18 | 2011-06-23 | Exxonmobil Research And Engineering Company | Polyalkylene epoxy polyamine additives for fouling mitigation in hydrocarbon refining processes |
EP3031885A1 (en) * | 2014-12-09 | 2016-06-15 | Afton Chemical Corporation | Composition for surface voltage reduction in distillate fuel |
EP3246380A1 (en) * | 2016-05-18 | 2017-11-22 | Bharat Petroleum Corporation Ltd. | Crude unit overhead corrosion control using multi amine blends |
-
2019
- 2019-07-02 WO PCT/IN2019/050494 patent/WO2020008477A1/en active Application Filing
Patent Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3472666A (en) | 1966-10-19 | 1969-10-14 | Exxon Research Engineering Co | Corrosion inhibitor |
US3779905A (en) * | 1971-09-20 | 1973-12-18 | Universal Oil Prod Co | Adding corrosion inhibitor to top of crude oil still |
US3981780A (en) | 1973-04-20 | 1976-09-21 | Compagnie Francaise De Raffinage | Compositions for inhibiting the corrosion of metals |
US3930810A (en) * | 1974-07-31 | 1976-01-06 | Universal Oil Products Company | Additives for petroleum distillates |
US4062764A (en) | 1976-07-28 | 1977-12-13 | Nalco Chemical Company | Method for neutralizing acidic components in petroleum refining units using an alkoxyalkylamine |
US4430196A (en) | 1983-03-28 | 1984-02-07 | Betz Laboratories, Inc. | Method and composition for neutralizing acidic components in petroleum refining units |
US5176847A (en) * | 1989-01-06 | 1993-01-05 | Baker Hughes Incorporated | Demulsifying composition |
WO2000001785A1 (en) * | 1998-07-01 | 2000-01-13 | Betzdearborn Inc. | Methods and compositions for inhibiting corrosion |
US20050183325A1 (en) * | 2004-02-24 | 2005-08-25 | Sutkowski Andrew C. | Conductivity improving additive for fuel oil compositions |
US20110147275A1 (en) * | 2009-12-18 | 2011-06-23 | Exxonmobil Research And Engineering Company | Polyalkylene epoxy polyamine additives for fouling mitigation in hydrocarbon refining processes |
EP3031885A1 (en) * | 2014-12-09 | 2016-06-15 | Afton Chemical Corporation | Composition for surface voltage reduction in distillate fuel |
EP3246380A1 (en) * | 2016-05-18 | 2017-11-22 | Bharat Petroleum Corporation Ltd. | Crude unit overhead corrosion control using multi amine blends |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2022172279A1 (en) * | 2021-02-15 | 2022-08-18 | Hindustan Petroleum Corporation Limited | A corrosion inhibiting dioleyl compound, and a corrosion inhibiting film forming amine formulation thereof |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4992210A (en) | Crude oil desalting process | |
US5114566A (en) | Crude oil desalting process | |
JP3962919B2 (en) | Metal anticorrosive, metal anticorrosion method, hydrogen chloride generation inhibitor and method for preventing hydrogen chloride generation in crude oil atmospheric distillation equipment | |
US7989403B2 (en) | Corrosion inhibitors containing amide surfactants for a fluid | |
AU2004243559B2 (en) | Use of quaternary ammonium carbonates and bicarbonates as anticorrosive agents, method for inhibiting corrosion and anticorrosive coatings using these agents | |
US4430196A (en) | Method and composition for neutralizing acidic components in petroleum refining units | |
CN102953067B (en) | Mannich base decalcification corrosion inhibitor, preparation and application thereof | |
CN110777382A (en) | Neutralizing film-forming corrosion and scale inhibitor and preparation method thereof | |
US20170051194A1 (en) | Fluoro-inorganics for acidification or neutralization of water systems | |
RU2334689C2 (en) | Composition for corrosion and salt deposition prevention | |
CA2812001C (en) | Quaternized dithiazines and method of using same in treatment of wells | |
US4490275A (en) | Method and composition for neutralizing acidic components in petroleum refining units | |
WO2020008477A1 (en) | A neutralizing amine formulation and process of preparation thereof | |
EP3110905A2 (en) | Quaternary fatty acid esters as corrosion inhibitors | |
US8404181B2 (en) | Corrosion inhibition | |
KR101226307B1 (en) | Inhibition of corrosion in fluid systems | |
CA2867413A1 (en) | Corrosion-protection system for treating metal surfaces | |
AU2014235194B2 (en) | Method to control corrosion of a metal surface using alkyl sulfamic acids or salts thereof | |
CN107190264B (en) | A kind of oil-soluble composite corrosion inhibitor | |
US20050012077A1 (en) | Quaternary ammonium carbonates and bicarbonates as anticorrosive agents | |
CN112695328A (en) | Water-soluble neutralization corrosion inhibitor and preparation method thereof | |
US20190119580A1 (en) | Process for controlling corrosion in petroleum refining units | |
MXPA03011659A (en) | Composition for inhibiting corrosion based on bisimidazoline 2-oleic-2'-naphthenic. | |
CN106995923B (en) | Corrosion inhibitor for air cooling device, preparation method and application thereof | |
RU2564329C1 (en) | Composition for preventing inorganic deposits |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 19749806 Country of ref document: EP Kind code of ref document: A1 |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
122 | Ep: pct application non-entry in european phase |
Ref document number: 19749806 Country of ref document: EP Kind code of ref document: A1 |