Method of continuously preparing pentamethyldiethylenetriamine and catalyst system for method

The technology of pentamethyldiethylenetriamine and diethylenetriamine is applied in the field of preparation of polyurethane catalysts, and can solve the problems of low pentamethyldiethylenetriamine yield, great environmental hazard of catalysts, easy decomposition of products, and the like, Achieve the effect of high degree of automation, low production cost, not easy to crush and lose

Active Publication Date: 2019-04-05
WANHUA CHEM GRP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantage of this invention is that the reaction time is particularly long, the yield of pentamethyldiethylenetriamine is on the low side, and the amount of catalyst is large in addition, relative to the quality of diethylenetriamine, it is 4%-8%, and the toxic nickel Catalyst, can have an impact on the environment
[0012] (1) Intermediates trimethyldiethylenetriamine and tetramethyldiethylenetriamine are easy to form formamides, which leads to low yield of pentamethyldiethylenetriamine on the one hand, and on the other hand, this recombination Partial tar can stick to reboiler coils, affecting heat transfer and causing some engineering problems
[0013] (2) The process for preparing pentamethyldiethylenetriamine adopts a batch process, the operation process is complicated, the degree of automation is low, the reaction time is long, and in the post-treatment process of the reaction solution, due to the entrainment of the catalyst, the product is prone to decomposition, which will cause the product losses and some security issues
[0014] (3) The raw materials of the reaction have high requirements on the material or the components of the catalyst are harmful to the environment

Method used

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  • Method of continuously preparing pentamethyldiethylenetriamine and catalyst system for method
  • Method of continuously preparing pentamethyldiethylenetriamine and catalyst system for method
  • Method of continuously preparing pentamethyldiethylenetriamine and catalyst system for method

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Embodiment 1

[0047] Preparation of 1# supported copper-based catalyst precursor:

[0048] Spherical γ-Al 2 o 3 (particle size 3mm, specific surface area 280m 2 / g) Calcined at 450°C for 4h. Prepare a nitrate dipping solution containing 10g copper, 0.1g hafnium and 0.5g zinc with 100ml deionized water, heat to 80°C to form a homogeneous solution, then add 89.4g γ-Al 2 o 3 Carrier, impregnated at 80°C for 12 hours, then baked in an oven at 120°C for 12 hours; finally moved to a muffle furnace, heated at 2-3°C / min to 450°C for 8 hours in an air atmosphere, and cooled naturally The 1# supported copper-based catalyst precursor was obtained. The composition of the catalyst is: copper is 10wt%, hafnium is 0.1wt%, zinc is 0.5wt%, and the rest is γ-Al 2 o 3 , calculated by the corresponding metal element in the total mass of the catalyst.

[0049] Preparation of 1# supported palladium-based catalyst precursor:

[0050] Spherical γ-Al 2 o 3 (particle size 3mm, specific surface area 280m ...

Embodiment 2

[0054] Preparation of 2# supported copper-based catalyst precursor:

[0055] Spherical γ-Al 2 o 3 (particle size 3mm, specific surface area 280m 2 / g) Calcined at 450°C for 4h. Prepare a nitrate dipping solution containing 5g copper, 0.2g hafnium and 1g zinc with 100ml deionized water, heat to 80°C to form a homogeneous solution, then add 93.8gγ-Al 2 o 3 Carrier, impregnated at 80°C for 12 hours, then baked in an oven at 120°C for 12 hours; finally moved to a muffle furnace, heated at 2-3°C / min to 400°C for 6 hours in an air atmosphere, and cooled naturally The 2# supported copper-based catalyst precursor was obtained. The composition of the catalyst is: copper is 5wt%, hafnium is 0.2wt%, zinc is 1wt%, and the rest is γ-Al 2 o 3 , calculated by the corresponding metal element in the total mass of the catalyst.

[0056] Preparation of 2# supported palladium-based catalyst precursor:

[0057] Spherical γ-Al 2 o 3 (particle size 3mm, specific surface area 280m 2 / g) Ca...

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Abstract

The invention discloses a method of continuously preparing pentamethyldiethylenetriamine and a catalyst system for the method. The method includes: subjecting diethylenetriamine, a solvent, hydrogen and formaldehyde to reaction in a two-stage fixed-bed reactor under certain reaction temperature, pressure and space velocity to obtain pentamethyldiethylenetriamine reacted liquid; the first stage ofreactor is filled with a supported copper-based catalyst, with reaction temperature controlled to 60-100 DEG C; the second stage of reactor is filled with a supported palladium-based catalyst, with reaction temperature controlled to 100-130 DEG C. The different catalysts and different reaction conditions are employed to carry out two-stage reaction; amide byproducts can be effectively decreased; the yield of pentamethyldiethylenetriamine is increased accordingly. The fixed-bed continuous process is employed herein; serial problems due to the catalysts crushed and entering a reacted liquid post-treatment system can be avoided; the method herein has the advantages of high automation level, low labor intensity, good process operational safety, low production cost and the like, and is suitablefor industrial large-scale production.

Description

technical field [0001] The present invention relates to a kind of preparation method of polyurethane catalyst, more specifically relate to a kind of method for continuously preparing pentamethyldiethylenetriamine and the catalyst system for this method. Background technique [0002] Pentamethyldiethylenetriamine is a colorless to pale yellow clear liquid, easily soluble in water. It is a highly active catalyst for polyurethane reaction. It mainly catalyzes foaming reaction and is also used to balance overall foaming and gelling reactions. It is widely used in various polyurethane rigid foams, including polyisocyanurate sheet rigid foams. Due to its strong foaming effect, it can improve the foam flow, thus improving the production process and improving the quality of the product. It is often shared with N,N-dimethylcyclohexylamine, etc. The production methods of pentamethyldiethylenetriamine include formaldehyde formic acid method and formaldehyde hydrogenation method. ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C209/68C07C211/14C07C213/00C07C215/14B01J23/656B01J23/80
CPCB01J23/6567B01J23/80C07C209/68C07C213/00C07C211/14C07C215/14
Inventor 刘振国张聪颖李鑫任树杰王丛刘志鹏唐磊
Owner WANHUA CHEM GRP CO LTD
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