Classifications

• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C291/00—Compounds containing carbon and nitrogen and having functional groups not covered by groups C07C201/00 - C07C281/00
  • C07C291/02—Compounds containing carbon and nitrogen and having functional groups not covered by groups C07C201/00 - C07C281/00 containing nitrogen-oxide bonds
  • C07C291/04—Compounds containing carbon and nitrogen and having functional groups not covered by groups C07C201/00 - C07C281/00 containing nitrogen-oxide bonds containing amino-oxide bonds

Definitions

• the present invention relates to an improvement in a chemical process for preparing mono-long chain amine oxide surfactants, whereby the active content of the surfactant is greater than about 30%, by weight of the amine, and nitrite, nitrosamine and residual hydrogen peroxide levels are suppressed.
• mono-long chain amine oxide surfactants containing above 30%o active result in an unhandleable gel especially when a phase modifying solvent is not incorporated.
• some sources of mono-long chain amine oxide surfactants may be contaminated with residual amounts of nitrite materials, especially inorganic nitrites. Contamination by such nitrites may be tolerable under many circumstances. For some uses however, the presence of nitrites may be undesirable, since they can react with other ingredients which may be present in the fully formulated detergent compositions.
• U.S. Patent 5,583,258, issued December 10, 1996 to Hawkins describes an economical process for preparing concentrated (greater than 30%>) free flowing aqueous amine oxide solutions having reduced levels of nitrites and nitrosamines, and achieving said free flowing properties without the use of phase-modifying solvents.
• tertiary amine and hydrogen peroxide are reacted in the presence of up to 2.5% alkali metal bicarbonate (based on weight of the amine).
• the reaction temperature is in the range of 40-100°C and the ratio of hydrogen peroxide to amine is 95%o-125% of stoichiometric.
• the Hawkins reference is silent with respect to residual levels of hydrogen peroxide.
• the present invention relates to a process for preparing aqueous mono-long chain amine oxide surfactant compositions having an active content of 30%> or more, wherein said process comprises:
• each R* and R ⁇ are Ci -C4 alkyl or hydroxyalkyl groups; and R3 is a Cg to Cjg alkyl or alkenyl group; and
• the present invention relates to a process for preparing aqueous mono-long chain amine oxide surfactant compositions containing greater than 30% amine oxide, which comprises: A. forming an aqueous solution of bicarbonate, the amount of said bicarbonate being from about 0.3% to about 2.5% by weight of the amine used in Step B, and wherein said bicarbonate is selected from the group consisting of alkali metal bicarbonates, alkaline earth metal bicarbonates, bicarbonate precursors, and mixtures thereof,
• each R! and R ⁇ are Ci -C4 alkyl or hydroxyalkyl groups; and R3 is a Cs to C1 g alkyl or alkenyl group; and
• R 1 , R ⁇ , and R ⁇ are defined as above; wherein the reaction exotherm is allowed to reach a temperature within the range of about 60°C to about 70°C and is then maintained within that range until the hydrogen peroxide level is 50 ppm or less and wherein said process is essentially free of any phase modifying solvent.
• Mono-long chain amine oxide compositions produced by the present process contain greater than 30% amine oxide, typically 31% to 38%, preferably 32-37%. Amine
• the amines used as starting material in the present process have the following formula:
• each R! and R ⁇ are C1 -C4 alkyl or hydroxyalkyl groups, preferably methyl groups, and R- is a Cg to Cjg ; preferably a Cjo- i g, more preferably a C ⁇ -Cjg alkyl or alkenyl group.
• the oxidation step herein is conducted using hydrogen peroxide or a source of hydrogen peroxide, or hydrogen peroxide generated in situ.
• the oxidation is conducted in water.
• Hydrogen peroxide is commercially available in aqueous solutions of various strengths up to 90%, which makes it a convenient oxidizing agent for forming amine oxide solutions at the desired concentration.
• bicarbonate material is selected from the group consisting of alkali metal bicarbonates, alkaline-earth metal bicarbonates, ammonium bicarbonate, and mixtures thereof. It will also be understood that bicarbonate precursors can be used in place of bicarbonate salts, e.g., alkali metal carbonates can be used to generate bicarbonate in situ.
• bicarbonate material is ammonium bicarbonate, and more preferably, sodium bicarbonate.
• the bicarbonate material is present at a level of from about 0.3%> to
• Process The process is preferably carried out at a pH in the range of from about 7 to about 10, more preferably from about 8 to about 10.
• amine oxide surfactants herein are produced by oxidizing the desired amine with hydrogen peroxide in the form of a 5% to 70% aqueous solution.
• the amount of hydrogen peroxide is typically from 100% to 1 15% of stoichoimetric to the amount of amine.
• the hydrogen peroxide is used at about a 1% to 10% excess of the stoichoimetric amount.
• the reaction can occur at temperatures of 40°C to 100°C.
• the initial reaction exotherm is controlled by application of cooling (and/or heat) until the reaction reaches 60° to 70°C, and then heat is provided, as needed, to maintain a 60° to 70°C temperature throughout the remainder of the reaction.
• the hydrogen peroxide level is monitored and the reaction is considered complete when the hydrogen peroxide level reaches 50 ppm or less.
• the conversion of amine to amine oxide will be from about 95% to about 99.5%, with any residual hydrogen peroxide being decomposed to a resulting level of 50 ppm or less, preferably 40 ppm or less, more preferably 15 ppm or less by virtue of maintaining the above-specified reaction temperature.
• Reaction temperatures above about 70°C can result in undesired byproducts.
• Temperatures below about 60°C will result in longer reaction times or the need to add reducing agents such as sodium sulfite to achieve the specified hydrogen peroxide level. Longer reaction times are economically undesirable.
• aqueous amine oxide compositions are free of said residues. Reaction times for the present process will typically be between 5 and 7 hours. Conduct of the reaction in the present manner makes possible the production of high active (30% to 38%) aqueous amine oxide compositions with excellent flowability characteristics as well as minimal levels of hydrogen peroxide, and the low nitrite and nitrososamine levels described in the Hawkins '258 Patent described above. Typically the amine oxide compositions produced by the present process will have a nitrite content below about 3 ppm and a nitrosamine content below about 500 ppb.
• the present invention may be characterized as an improvement over the process of the Hawkins '258 patent wherein the improvement is the production of amine oxides having less than 50ppm residual hydrogen peroxide and wherein said improvement is achieved by conduct of the process at a maintained temperature of 60°-70°C.
• the oxidation of the amine is carried out using otherwise conventional procedures, and can be conducted in a batch or multi-stage continuous manner.
• Monitoring of hydrogen peroxide level is done by standard sodium thiosulfate titration analysis.
• the batch size is 1000 grams.
• the reactor is a 3000 milliliter glass vessel stirred with a Teflon blade at the end of a mixing shaft.
• the reactor is supported from above so that a cold water bath or electric heating mantle can be placed up around the bottom and sides of the reactor as needed to control temperature.
• the temperature is monitored by a thermometer immersed in the reaction materials.
• the water and sodium bicarbonate are added and mixed, the amine is weighed into the reactor and continuous agitation is begun. The temperature is adjusted as indicated for individual batches and the hydrogen peroxide is added. Reaction time is recorded from the addition of hydrogen peroxide.
• Run B was conducted in the same manner, except that when the temperature reached 60- 70°C it was maintained there throughout the entire reaction time, which was 6:00 hours. The experiment is summarized as follows:
• the product was a free flowing aqueous solutions at room temperature, containing approximately 37%o amine oxide.
• EXAMPLE II The following are examples of hand dishwashing compositions utilizing amine oxide of the present invention.
• Polymer is (N,N-dimethylamino)ethyl methacrylate homopolymer.

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• Chemical & Material Sciences (AREA)
• Organic Chemistry (AREA)
• Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
• Detergent Compositions (AREA)
• Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
• Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)

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• 1998
  • 1998-11-24 US US09/200,391 patent/US6294514B1/en not_active Expired - Lifetime
• 1999
  • 1999-11-18 ES ES99960454T patent/ES2228140T3/es not_active Expired - Lifetime
  • 1999-11-18 WO PCT/US1999/027315 patent/WO2000031026A1/en not_active Ceased
  • 1999-11-18 JP JP2000583854A patent/JP4334772B2/ja not_active Expired - Lifetime
  • 1999-11-18 DE DE69921352T patent/DE69921352T2/de not_active Expired - Lifetime
  • 1999-11-18 CA CA002348920A patent/CA2348920C/en not_active Expired - Lifetime
  • 1999-11-18 EP EP99960454A patent/EP1133469B1/en not_active Expired - Lifetime
  • 1999-11-18 CN CNB998136719A patent/CN1183105C/zh not_active Expired - Lifetime
  • 1999-11-18 AT AT99960454T patent/ATE280150T1/de not_active IP Right Cessation

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