Abstract: The present invention relates to a method for the manufacture of ethyleneamine from a mixture comprising water (H2O), ethylenediamine (EDA) and N-methylethylendiamine (NMEDA), comprising the steps of: (i) providing a feed stream comprising EDA, NMEDA and water; (ii) separating the feed stream provided in step (i) in the one or more distillation columns into a. a fraction A comprising water and NMED A wherein the weight ratio of water to NMEDA in fraction A is more than 100:1; b. a fraction B comprising water, NMEDA and EDA wherein the weight ratio of water to NMEDA is in the range of 1:100 to 100:1; and c. a fraction C comprising water and EDA wherein the weight ratio of EDA to water is more than 5:1.

Abstract: A process for producing EDA from a mixture comprising water (H2O), ethylenediamine (EDA) and N-methylethylenediamine (NMEDA) by feeding the mixture into a rectification column, wherein the rectification column is operated at the top pressure in the range of 5.0 to 7.5 bar.

Abstract: A process for the manufacture of alkanolamines and/or a process for the conversion of alkanolamines wherein the process is performed in one or equipment items, wherein one or more steel parts of the one or more equipment items, which have one or more surfaces in contact with an alkanolamine, are made of duplex steel and Use of duplex stainless steel as a construction material for parts of an equipment item used in an alkanolamine and/or alkyleneamine manufacturing process or separation process, which have one or more surfaces in contact with alkyleneamines and/or alkanolamines and the use of duplex steel as a construction material for steel parts of a equipment items used in an alkanolamine manufacturing or conversion process.

Abstract: A process for producing EDA from a mixture comprising water (H2O), ethylenediamine (EDA) and N-methylethylenediamine (NMEDA) by feeding the mixture into a rectification column, wherein the rectification column is operated at the top pressure in the range of 5.0 to 7.5 bar.

Abstract: The present invention relates to a process for purifying ethoxyquin by distillation, to high-purity ethoxyquin obtainable by means of distillative purification and to the use thereof, particularly as additive in foodstuffs and feedstuffs.

Abstract: The present invention relates to a process for purifying ethoxyquin by distillation, to high-purity ethoxyquin obtainable by means of distillative purification and to the use thereof, particularly as additive in foodstuffs and feedstuffs.

Abstract: In one of many possible embodiments, a system is provided for modeling telecommunication switch investments. The exemplary system includes a telecommunication switch modeling application configured to determine equipment quantities having capacity to satisfy switch design parameters descriptive of at least one model telecommunication switch, and calculate model investments associated with the equipment quantities. The exemplary system also includes a telecommunication switch investment modeling application configured to weight the model investments in accordance with at least one of a network parameter descriptive of an actual telecommunication switch and a “what-if” input descriptive of a hypothetical telecommunication switch configuration to form weighted investments that are specific to at least one of the actual telecommunication switch and the hypothetical telecommunication switch configuration.

Abstract: In one of many possible embodiments, a system is provided for modeling telecommunication switch investments. The exemplary system includes a telecommunication switch modeling application configured to determine equipment quantities having capacity to satisfy switch design parameters descriptive of at least one model telecommunication switch, and calculate model investments associated with the equipment quantities. The exemplary system also includes a telecommunication switch investment modeling application configured to weight the model investments in accordance with at least one of a network parameter descriptive of an actual telecommunication switch and a “what-if” input descriptive of a hypothetical telecommunication switch configuration to form weighted investments that are specific to at least one of the actual telecommunication switch and the hypothetical telecommunication switch configuration.

Abstract: In one of many possible embodiments, a system is provided for modeling telecommunication switch investments. The exemplary system includes a telecommunication switch modeling application configured to determine equipment quantities having capacity to satisfy switch design parameters descriptive of at least one model telecommunication switch, and calculate model investments associated with the equipment quantities. The exemplary system also includes a telecommunication switch investment modeling application configured to weight the model investments in accordance with at least one of a network parameter descriptive of an actual telecommunication switch and a “what-if” input descriptive of a hypothetical telecommunication switch configuration to form weighted investments that are specific to at least one of the actual telecommunication switch and the hypothetical telecommunication switch configuration.

Abstract: The invention relates to a process for continuously, distillatively removing piperazine from an ethylenediamine-piperazine mixture under pressure at elevated temperature, by discharging the ethylenediamine at the top and the piperazine at the bottom of a distillation column. For the purpose of improving the quality of the piperazine, especially its color and color stability, the piperazine is subjected directly to circulation conveying it through an evaporator unit operated at a temperature of from about 160° C. to about 170° C. and returning it into the distillation column. After a residence time of from about 30 min to about 60 min in the circulation system, the piperazine is discharged in vapor form from a side draw in the lower section of the distillation column.