77-99-6Relevant articles and documents
METHOD FOR PREPARING TRIMETHYLOLPROPANE
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Paragraph 0064-0066, (2020/07/07)
A method for preparing trimethylolpropane, the method including: subjecting dimethylolbutanal (DMB) to a hydrogenation reaction in the presence of a metal catalyst and an alcohol solvent. During the hydrogenation reaction, a weight ratio of the alcohol solvent based to dimethylolbutanal is 2 to 10.
SEPARATION METHOD OF DIMETHYLOLBUTANAL AND PREPARATION METHOD OF TRIMETHYLOLPROPANE
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Paragraph 0100-0106, (2019/07/03)
The present specification relates to a separation method of dimethylolbutanal comprising: a step (A) of making n-butylaldehyde (n-BAL) react with formaldehyde (FA) under an alkylamine catalyst, thereby obtaining a dimethylolbutanal mixed product including dimethylolbutanal (DMB) and trimethylolpropane (TMP); and a step (B) of extracting 95% or more of DMB and 80% or more of TMP from the dimethylolbutanal mixed product by using a counter flow type extraction method using an organic solvent. In the step (B), the organic solvent has a flow rate of 70 to 110 g/min, the DMB mixed product has a flow rate of 40 to 70 g/min, and a weight ratio of the organic solvent to the DMB mixed product is 1.2 to 3. According to an embodiment of the present specification, the separation method can obtain DMB, at a high efficiency, which is used as a raw material for producing TMP. TMP can be obtained at a high efficiency by using the obtained DMB as a raw material for hydrogenation.COPYRIGHT KIPO 2019
Method for continuous preparation of trimethylolpropane
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Paragraph 0018-0027, (2019/04/09)
A method for continuous preparation of trimethylolpropane includes: taking a mixture of formaldehyde and butyraldehyde as a raw material, absolute ethyl alcohol as a solvent and sodium hydroxide solution as chemical agent, allowing the mixture and a catalyst to flow and mix in capillaries to form a reaction mixture therein, performing aldol condensation and disproportionated reaction on the reaction mixture in the capillaries to obtain a product comprising trimethylolpropane, wherein the temperature of the reaction mixture is controlled to be 25 to 75 DEG C, and the reaction standing time ranges from 2 to 25 minutes by prolonging the capillaries and/or increasing volume thereof or reducing flow rate of the reaction mixture. Synthesis reaction time of trimethylolpropane is shortened as compared with that of the prior art (4-6 hours), and the yield is increased to 90% from about 75%.
Method For The Combined Production of Polyols In The Presence Of An Inorganic Base
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Paragraph 0049; 0050, (2019/08/20)
The present invention relates to a process for simultaneously consecutive preparation of polyols by base-catalysed reaction of at least two different mid-chain aldehydes with formaldehyde. The simultaneous consecutive mode of operation makes it possible to achieve high conversions and high selectivities for both aldehydes, with additional achievement of a distinct reduction in the amount of unreacted formaldehyde remaining. This leads to improved process economics, since the energy costs for workup of the formaldehyde stream are distinctly reduced.
Precise Steric Control over 2D versus 3D Self-Assembly of Antimony(III) Alkoxide Cages through Strong Secondary Bonding Interactions
Moaven, Shiva,Yu, Jingze,Yasin, Jason,Unruh, Daniel K.,Cozzolino, Anthony F.
supporting information, p. 8372 - 8380 (2017/07/22)
Antimony(III) alkoxide cages were designed as building blocks for predictable supramolecular self-assembly. Supramolecular synthons featuring two Sb···O secondary bonding interactions (SBIs), each SBI stronger than 30 kJ/mol, were used to drive the formation of the supramolecular architectures. Judicious choice of pendant groups provided predictable control over the formation of self-assembled 3D columnar helices, which crystallized with hollow morphologies, or a self-assembled 2D bilayer. The Sb-O stretching frequency provides a spectroscopic signature of Sb···O SBI formation.
PROCESS FOR PRODUCTION OF DITRIMETHYLOLPROPANE
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Paragraph 0102, (2014/05/20)
Provided is a method for producing di-TMP by reacting n-butyl aldehyde (NBD), formaldehyde and a base, said method including a first step of reacting the NBD, formaldehyde (1) and a base (I) to obtain a reaction mixture solution containing trimethylolpropane (TMP), di-TMP and 2-ethyl-2-propenal (ECR); a second step of distilling the reaction mixture solution to recover the ECR therefrom; and a third step of sequentially adding the ECR recovered by distillation, and adding at least one of a base (II) and formaldehyde (2), to the reaction mixture solution from which the ECR has been recovered by distillation, and thereby allowing a reaction for production of the di-TMP to proceed gradually, in which TMP is added in any one of the first to third steps or in plural steps of the first to third steps.
METHOD FOR PRODUCING DITRIMETHYLOLPROPANE
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Paragraph 0146; 0147; 0148; 0149; 0150, (2013/07/25)
The present invention provides a method for producing ditrimethylolpropane which is characterized by the following (1) and (2): (1) a distillation still residue separated from purified trimethylolpropane is subjected to re-distillation under specific conditions to obtain a ditrimethylolpropane-containing solution having given contents of bis-TMP and tri-TMP; and (2) when subjecting the ditrimethylolpropane-containing solution to crystallization with an organic solvent, the crystallization is initiated under pressure at a temperature exceeding a boiling point of the organic solvent as measured under normal pressures, and the resulting crystallization product solution is cooled at a temperature drop rate of 2° C./min or less. According to the above method, it is possible to produce a high-purity ditrimethylolpropane from a distillation still residue obtained upon production of trimethylolpropane in a simple, industrially useful manner.
Method for improving the color number of trimethylolpropane
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Page/Page column 3-4, (2012/07/27)
The present invention relates to a method for producing trimethylolpropane having a low color number by processing a raw reaction solution obtained according to the inorganic Cannizarro process while adhering to precisely defined pH values.
PROCESS FOR PRODUCTION OF DITRIMETHYLOLPROPANE
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Page/Page column 9, (2010/07/10)
The present invention provides a method for producing ditrimethylolpropane including reacting n-butyraldehyde with formaldehyde in the presence of a base catalyst to thereby produce trimethylolpropane and ditrimethylolpropane, wherein the method includes (I) a step of reacting n-butyraldehyde with formaldehyde (1) in the presence of a base catalyst (1), to thereby produce a reaction mixture containing trimethylolpropane, ditrimethylolpropane, and 2-ethyl-2-propenal; (II) a step of recovering 2-ethyl-2-propenal through distillation of the produced reaction mixture; and (III) a step of adding, to a distillation residue obtained through recovery of 2-ethyl-2-propenal, the recovered 2-ethyl-2-propenal and formaldehyde (2), and optionally a base catalyst (2), to thereby allow reaction for production of ditrimethylolpropane to proceed, wherein the amounts of formaldehyde (I) and the base catalyst (1) supplied in step I and formaldehyde (2) and the base catalyst (2) supplied in step II are controlled to specific amounts, to thereby effectively produce ditrimethylolpropane. According to the present invention, the yield of di-TMP is considerably increased, and the amount of bis-TMP by-produced can be considerably reduced with respect to the amount of di-TMP (i.e., a product of interest) produced; that is, di-TMP can be effectively produced in an industrially advantageous manner.
PROCESS FOR HYDROGENATING METHYLOLALKANALS
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Page/Page column 3-4, (2009/04/24)
A process for catalytically hydrogenating methylolalkanals of the general formula in which R1 and R2 are each independently a further methylol group or an alkyl group having from 1 to 22 carbon atoms or an aryl or aralkyl group having from 6 to 33 carbon atoms, in the liquid phase over a hydrogenation catalyst, which comprises setting a pH of from 7.0 to 9.0 in the hydrogenation effluent by adding at least one tertiary amine, an inorganic base or an inorganic or organic acid to the hydrogenation feed.