2-(hexylamino)ethanol

Conditions: temp:0.00; pressure:0.00; stir:; See reaction.notes.procedure_details.

Procedure: In an alternate synthesis scheme for n-hexyl ethanolamine, the ethoxylation steps remained the same as above in sequence, temperature and pressure. However, the preferred weight fraction of n-hexyl amine to ethylene oxide was lowered to approximately 88 pounds n-hexyl amine to 12 pounds ethylene oxide to yield 100 pounds of reaction mass. The weight ratio of mono to di ethoxylates in the reaction mass was approximately 4.0-4.2 mono to 1.0 di. The purification section was also the same except the process was stopped after removal of n-hexyl amine overhead. The final bottoms fraction contained n-hexyl ethanolamine and some diethoxylates byproducts (less than 20% by weight). to yield 100 pounds of reaction mass after removal of n-hexyl amine overhead

Conditions: temp:0.00; pressure:0.00; stir:; See reaction.notes.procedure_details.

Procedure: This procedure outlines the steps involved in ethoxylating n-hexyl amine to n-hexyl ethanolamine and n-hexyl diethanolamine. A suitable reactor must have cooling water, a heat source of 350° F., and pressure rating of 100 psig. The material of construction may be carbon steel, stainless steel, or glass-lined steel. a heat source of 350° F., and pressure rating of 100 psig

Conditions: temp:0.00; pressure:0.00; stir:; See reaction.notes.procedure_details.

Procedure: This procedure outlines the steps involved in ethoxylating n-hexyl amine to n-hexyl ethanolamine and n-hexyl diethanolamine. A suitable reactor must have cooling water, a heat source of 350° F., and pressure rating of 100 psig. The material of construction may be carbon steel, stainless steel, or glass-lined steel. a heat source of 350° F., and pressure rating of 100 psig

Conditions: temp:0.00; pressure:0.00; stir:; See reaction.notes.procedure_details.

Procedure: In an alternate synthesis scheme for n-hexyl ethanolamine, the ethoxylation steps remained the same as above in sequence, temperature and pressure. However, the preferred weight fraction of n-hexyl amine to ethylene oxide was lowered to approximately 88 pounds n-hexyl amine to 12 pounds ethylene oxide to yield 100 pounds of reaction mass. The weight ratio of mono to di ethoxylates in the reaction mass was approximately 4.0-4.2 mono to 1.0 di. The purification section was also the same except the process was stopped after removal of n-hexyl amine overhead. The final bottoms fraction contained n-hexyl ethanolamine and some diethoxylates byproducts (less than 20% by weight). to yield 100 pounds of reaction mass after removal of n-hexyl amine overhead

Conditions: temp:0.00; pressure:0.00; stir:; See reaction.notes.procedure_details.

Procedure: This procedure outlines the steps involved in ethoxylating n-hexyl amine to n-hexyl ethanolamine and n-hexyl diethanolamine. A suitable reactor must have cooling water, a heat source of 350° F., and pressure rating of 100 psig. The material of construction may be carbon steel, stainless steel, or glass-lined steel. a heat source of 350° F., and pressure rating of 100 psig