A plugin modular, transportable ammonia producing machine is developed that can conveniently produce ammonia from electricity, air and water. The invention includes ammonia synthesis through a plugin modular device. FIG. 5 depicts the overall process flow of the system. Water at state 1 enters the system at room temperature in the water storage tank. Next, at state 2, the water in the storage tank is sent to the circulation pump that delivers water to the air compressor. This is done for two main purposes. Firstly, the circulating water cools the compressor during operation. Secondly, as the circulating water rises in temperature while leaving the air compressor, its temperature increases. This results in an increased inlet water temperature to the proton exchange membrane (PEM) electrolyser that leads to higher water electrolysis performance.

A gas production plant includes an electrolysis arrangement for the production of gaseous hydrogen; an air separation arrangement for the production of gaseous nitrogen; a gas mixer configured to mix the gaseous hydrogen and the gaseous nitrogen in a predetermined mixing ratio; and an injector for injecting the resulting gaseous mixture into an export pipeline. A method of providing gaseous reactants for an ammonia synthesis plant is also provided.

One or more reactants are flowed into thermal contact with a heating element in a reactor for a first time period. During a first part of a heating cycle, the one or more reactants are provided with a first temperature by heating with the heating element, such that one or more thermochemical reactions is initiated. The one or more thermochemical reactions includes pyrolysis, thermolysis, synthesis, hydrogenation, dehydrogenation, hydrogenolysis, or any combination thereof. The first heating element operates by Joule heating and has a porous construction that allows gas to flow therethrough. During a second part of the heating cycle, the one or more reactants are provided with a second temperature less than the first temperature, for example, by de-energizing the heating element. A duration of the first time period is equal to or greater than a duration of the heating cycle, which is less than five seconds.

A multi-bed catalytic converter comprising: a plurality of catalytic beds which are traversed in series by a process gas, sequentially from a first catalytic bed to a last catalytic bed of said plurality, and at least one inter-bed heat exchanger (7) positioned between a first catalytic bed and a second catalytic bed of said plurality, wherein at least the last catalytic bed of said plurality is adiabatic and is made of fine catalyst with a particle size not greater than 2 mm.

Method for the control of pressure in a loop for the preparation of ammonia or methanol by means of an anti-surge control valve of a compressor and/or a compressor flow regulation valve for the recirculation of loop recirculation gas at variating flow supply of fresh synthesis gas.

A method for the control of pressure in a loop for the preparation of ammonia or methanol by using an anti-surge control valve of a compressor and/or a compressor flow regulation valve for the recirculation of loop recirculation gas at variating flow supply of fresh synthesis gas.

A catalytic bed for a chemical reactor, said catalytic bed having an annular-cylindrical geometry and comprising at least one collector made with a gas-permeable cylindrical wall, containing at least a first catalyst and a second catalyst, wherein the second catalyst has a finer particle size than the first catalyst, and wherein the first catalyst forms a layer of catalyst adjacent to and in contact with said collector.

This invention relates to system for the production of ammonia synthesis gas, comprising: one or more electrically driven air separation unit(s) configured to separate nitrogen from air; and one or more solid oxide electrolysis cell(s) configured to produce hydrogen by solid oxide electrolysis of steam in thermoneutral or endothermal mode. By configuring the electrically driven air separation unit(s) and the solid oxide electrolysis cell(s) so that heat emanating from the one or more electrically driven air separation unit(s) is transferred to the one or more solid oxide electrolysis cell(s), nitrogen production may be integrated while enabling high current density, the use of large SOEC stacks and improved reactant conversion. In addition, ammonia production plants comprising the above system as well as related methods are described.

Provided is a novel production system for a product selected from a nitrogen-containing product and a fermented and cultured product that does not involve (or can minimize) the transport of liquid ammonia. A production system for a product selected from a nitrogen-containing product and a fermented and cultured product can include: an ammonia synthesis apparatus in which an ammonia-containing gas is synthesized by reaction of a source gas containing hydrogen and nitrogen in the presence of a supported metal catalyst containing as a support one or more selected from the group consisting of: i) a conductive mayenite compound; ii) a two-dimensional electride compound or a precursor thereof; and iii) a complex formed of a support base containing at least one metal oxide selected from ZrO.sub.2, TiO.sub.2, CeO.sub.2, and MgO and a metal amide represented by a formula M(NH.sub.2).sub.x (where M represents one or more selected from Li, Na, K, Be, Mg, Ca, Sr, Ba, and Eu; and x represents a valence number of M) supported by the support base; and a production apparatus that produces a product selected from a nitrogen-containing product and a fermented and cultured product using ammonia originating from the ammonia-containing gas obtained by using the ammonia synthesis apparatus.

Provided is a novel production system that does not involve, or can minimize, the transport of liquid ammonia in the production of an organic compound or the production of a microorganism by microbial fermentation. A production system for an organic compound or a microorganism includes: an ammonia synthesis apparatus in which an ammonia-containing gas is synthesized by reaction of a source gas containing hydrogen and nitrogen in the presence of a supported ruthenium catalyst; and a culture apparatus that cultures a microorganism having organic compound productivity using ammonia originating from the ammonia-containing gas obtained by using the ammonia synthesis apparatus.