METHOD FOR PREPARATION OF AMMONIA GAS AND CO2 FOR A UREA SYNTHESIS PROCESS

Abstract

The invention relates to a process for preparing ammonia gas and CO.sub.2 for urea synthesis. In the process of the invention, a process gas containing nitrogen, hydrogen and carbon dioxide as main components is produced from a metallurgical gas. The metallurgical gas consists of blast furnace gas, or contains blast furnace gas at least as a mixing component. The process gas is fractionated to give a gas stream containing the CO.sub.2 component and a gas mixture consisting primarily of N.sub.2 and H.sub.2. An ammonia gas suitable for the urea synthesis is produced from the gas mixture by means of ammonia synthesis. CO.sub.2 is branched off from the CO.sub.2-containing gas stream in a purity and amount suitable for the urea synthesis.

Claims

1. A process for preparing urea, where ammonium carbamate is produced from ammonia gas and CO.sub.2 using an excess of ammonia and the ammonium carbamate is converted into urea in subsequent decomposition stages at low pressure, wherein the ammonia gas required for the synthesis of urea and the CO.sub.2 which is likewise required for the synthesis of urea are produced from a metallurgical gas which contains blast furnace gas at least as mixing component or consists of blast furnace gas.

Description

BRIEF DESCRIPTION OF THE DRAWING

[0008] FIG. 1 is a schematic block diagram illustrating a process for preparing gaseous starting materials for synthesis of urea.

DETAILED DESCRIPTION

[0009] According to the invention, a metallurgical gas which contains blast furnace gas at least as a mixing component, or which consists of blast furnace gas, is used for preparing the gaseous starting materials for urea synthesis. Blast furnace gas is obtained in the production of pig iron in a blast furnace. In the blast furnace, pig iron is obtained from iron ores, additives, and coke and other reducing agents such as coal, oil or gas. As products of the reduction reactions, CO.sub.2, hydrogen and water vapor are inevitably formed. A blast furnace gas taken from the blast furnace process has, in addition to the abovementioned constituents, a high content of nitrogen. The composition of the blast furnace gas is dependent on the feedstocks and the mode of operation, and is subject to fluctuations. However, blast furnace gas usually contains from 35 to 60% by volume of N.sub.2, from 20 to 30% by volume of CO, from 20 to 30% by volume of CO.sub.2 and from 2 to 15% by volume of H.sub.2.

[0010] Furthermore, a metallurgical gas which consists of a mixed gas composed of blast furnace gas and converter gas, or of a mixed gas composed of blast furnace gas, converter gas and coke oven gas can be used for the process of the invention. Converter gas, which is created from pig iron during the steel production process, has a high content of CO, and also contains nitrogen, hydrogen and CO.sub.2. A typical converter gas composition has from 50 to 70% by volume of CO, from 10 to 20% by volume of N.sub.2, about 15% by volume of CO.sub.2 and about 2% by volume of H.sub.2. Coke oven gas is obtained in the coking of coal and has a high hydrogen content and appreciable amounts of CH.sub.4. Coke oven gas typically contains from 55 to 70% by volume of H.sub.2, from 20 to 30% by volume of CH.sub.4, from 5 to 10% by volume of N.sub.2 and from 5 to 10% by volume of CO. The coke oven gas additionally comprises CO.sub.2, NH.sub.3 and H.sub.2S.

[0011] In the process of the invention, a process gas containing nitrogen, hydrogen and carbon dioxide as main components is produced from the metallurgical gas and this process gas is subsequently fractionated to give a gas stream containing the CO.sub.2 component and a gas mixture consisting primarily of N.sub.2 and H.sub.2. An ammonia gas suitable for the urea synthesis is produced from the gas mixture by means of ammonia synthesis. CO.sub.2 is branched off from the CO.sub.2-containing gas stream in a purity and amount suitable for the urea synthesis. The conditioning of the metallurgical gas and the separation steps described can be matched to one another in such a way that ammonia and CO.sub.2 are formed in the proportions necessary for the urea synthesis and the metallurgical gas can be utilized almost completely for preparing the gaseous starting materials required for the urea synthesis.

[0012] The use of the metallurgical gas for producing process gas is advantageously preceded by a gas purification process. The gas purification process serves to separate undesirable constituents, in particular tar, sulfur and sulfur compounds, aromatic hydrocarbons (BTX) and high-boiling hydrocarbons.

[0013] The CO component of the metallurgical gas can be converted into CO.sub.2 and H.sub.2 by means of a water gas shift reaction, forming a process gas which contains nitrogen, hydrogen and carbon dioxide as main components.

[0014] The process gas is subsequently fractionated, preferably by means of pressure swing adsorption (PSA), to give a gas mixture consisting primarily of nitrogen and hydrogen and an offgas, also referred to as PSA offgas, containing the CO.sub.2 component. Pressure swing adsorption (PSA), which is known in the prior art, is used for the isolation and purification of hydrogen. In the context of the process of the invention, the pressure swing adsorption is operated in combination with a preceding gas conditioning process in such a way that a desired concentration ratio of H.sub.2 and N.sub.2 is established. One aspect of the process of the invention is therefore the coupling of a gas conditioning process, in particular a water gas shift reaction, with a pressure swing adsorption in order to produce a synthesis gas suitable for the ammonia synthesis from metallurgical gas which contains blast furnace gas at least as a mixing component, or which consists of blast furnace gas. Furthermore, secondary components which are unfavorable for the ammonia synthesis, e.g. argon, methane or carbon monoxide, can be removed or have their concentrations reduced by means of the pressure swing adsorption.

[0015] The pressure swing adsorption produces an energy-rich offgas (PSA offgas) which contains the CO.sub.2 component of the process gas and any residual proportions of CO. CO.sub.2 for the urea synthesis is obtained from the PSA offgas. In a preferred embodiment of the process of the invention, the CO.sub.2 component is separated from the pressure swing adsorption offgas (PSA offgas) and is subsequently separated into a gas containing a high concentration of CO.sub.2 for the urea synthesis and a tailgas having a lower concentration of CO.sub.2.

[0016] The invention also provides a process for preparing urea, in which ammonium carbamate is produced from ammonia gas and CO.sub.2 using an excess of ammonia and this ammonium carbamate is dissociated into water and urea. According to the invention, the ammonia gas required for the synthesis of urea and the CO.sub.2 which is likewise required for the synthesis of urea are each produced from a metallurgical gas which contains blast furnace gas at least as a mixing component, or which consists of blast furnace gas. It is essential for the process of the invention, according to an embodiment, that the gaseous starting materials for the urea synthesis are obtained entirely from the metallurgical gas. The gaseous starting materials for the urea synthesis are obtainable by the process described further above.

[0017] The invention will be illustrated below with reference to FIG. 1., which depicts merely one working example. The single figure schematically shows, in the form of a greatly simplified block diagram, a process for preparing gaseous starting materials for a urea synthesis.

[0018] A process gas 2 containing nitrogen (N.sub.2), hydrogen (H.sub.2) and carbon dioxide (CO.sub.2) as main components is produced from a metallurgical gas 1 which contains blast furnace gas at least as a mixing component and in the working example consists of blast furnace gas by means of the process depicted in the figure.

[0019] The blast furnace gas 1 has, for example, a typical composition of 50% by volume of N.sub.2, 24% by volume of CO.sub.2, 21% by volume of CO and about 4% by volume of H.sub.2. After a gas purification process 3 in which undesirable constituents, for example tar, sulfur and sulfur compounds, aromatic hydrocarbons (BTX) and high-boiling hydrocarbons are separated, the metallurgical gas 1 consisting of blast furnace gas is converted by means of a gas conditioning process 4 into the process gas 2 which consists mainly of N.sub.2, H.sub.2 and CO.sub.2. The gas conditioning process 4 includes, in particular, a CO conversion in which the CO component of the metallurgical gas 1 is converted into CO.sub.2 and H.sub.2 by means of a water gas shift reaction:

CO+H.sub.2O.fwdarw.CO.sub.2+H.sub.2.

[0020] After the conversion or the water gas shift reaction, the process gas has a composition of about 37% by volume of CO.sub.2, 21% by volume of H.sub.2 and 42% by volume of N.sub.2.

[0021] The process gas 2 is fractionated by means of pressure swing adsorption (PSA) 16 to give a gas mixture 5 consisting primarily of N.sub.2 and H.sub.2 and an offgas 6 containing the CO.sub.2 component. An ammonia gas 8 suitable for the synthesis of urea is produced from the N.sub.2- and H.sub.2-containing gas mixture by means of an ammonia synthesis 7. In the ammonia synthesis 7, the gas mixture composed of hydrogen and nitrogen can, for example, be reacted over an iron oxide mixed catalyst at pressures in the range from 150 to 200 bar and at a reaction temperature of from 350 to 550 C.

[0022] CO.sub.2 for the urea synthesis 9 is obtained from the offgas 6 from the pressure swing adsorption. According to the process scheme depicted in the figure, the CO.sub.2 component 11 is separated from the offgas 6 from the pressure swing adsorption in a first separation stage 10. Subsequently, a separation into a gas 13 containing a high concentration of carbon dioxide and a tailgas 14 having a low concentration of CO.sub.2 is carried out in a second separation stage 12. The gas 13 is, in particular, carbon dioxide in a purity necessary for the urea synthesis.

[0023] CO.sub.2 and NH.sub.3 are fed to the urea plant in the proportions required for the urea synthesis 9. In the urea plant, ammonium carbamate is produced using an excess of ammonia and this ammonium carbonate is converted into urea 15 in subsequent decomposition stages at low pressure.

[0024] The process illustrated in FIG. 1 can also be operated using a gas mixture of blast furnace gas and converter gas or using a gas mixture of blast furnace gas, converter gas and coke oven gas as metallurgical gas 1.