摘要:
Process and plant for the synthesis of ammonia from a hydrocarbon feedstock, comprising: primary reforming with steam and air-fired secondary reforming wherein primary reforming is performed at a temperature and pressure of at least 790 °C and 50 bar, and secondary reforming is carried out substantially in absence of excess air, the so obtained make-up synthesis gas having a H 2 to N 2 molar ratio in the range 2.5 to 3.
摘要:
A process for selective removal of at least a gaseous reaction product (P) from a gaseous system, the molecule of said reaction product having a non-zero electric dipole moment and the other gaseous components of said gaseous system having molecules with electric dipole moment which is null or negligible compared to the electric dipole moment of molecule of said reaction product; a non-uniform electric field (4) being generated between at least a positive electrode (2) and a negative electrode (1), said positive electrode and negative electrode being located at opposite sides of at least one permeation membrane (3), the selective passage of said reaction product through said membrane being enhanced by said electric field.
摘要:
A heat-exchanger type reactor (1) which has a plurality of tubes (6) holding a catalyst, a shell section through which a heat-transfer medium is passed to carry out heat-transfer with a reaction fluid in said tubes (6), and upper (4) and lower (5) tube sheets, the upper ends of said tubes (6) being joined to said upper tube sheet (4) by way of first expansion joints (2) fixed to the upper side of said upper tube sheet (4), the lower ends of said tubes (6) being fixed directly to the floatable lower tube sheet (5), a floatable room (8) being formed which is partitioned by said lower tube sheet (5) and an inner end plate (inner head)(7) joined to the lower side thereof and has an opening (17) in the lower part, and said opening (17) being joined by way of a second expansion joint (3) to a tube-side outlet (12) to the outside of the reactor (1).
摘要:
A process for producing ammonia synthesis gas from the reforming of hydrocarbons with steam in a primary reformer (1) equipped with a plurality of externally heated catalytic tubes and then together with air in a secondary reformer (2) is characterized in that the reaction of said hydrocarbons with said steam in said primary reformer (1) is performed at an operating pressure of more than 35 bar in the catalytic tubes, in that air is added to said secondary reformer in excess over the nitrogen amount required for ammonia synthesis and in that the excess of nitrogen is removed downstream the secondary reformer preferably by cryogenic separation or by molecular sieves of the TAS or PSA type. This process allows to obtain high synthesis gas production capacities and lower investment and energy costs.
摘要:
A process for selective removal of at least a gaseous reaction product (P) from a gaseous system, the molecule of said reaction product having a non-zero electric dipole moment and the other gaseous components of said gaseous system having molecules with electric dipole moment which is null or negligible compared to the electric dipole moment of molecule of said reaction product; a non-uniform electric field (4) being generated between at least a positive electrode (2) and a negative electrode (1), said positive electrode and negative electrode being located at opposite sides of at least one permeation membrane (3), the selective passage of said reaction product through said membrane being enhanced by said electric field.
摘要:
An ammonia converter system and method are disclosed. The reactor can alter the conversion of ammonia by controlling the reaction temperature of the exothermic reaction along the length of the reactor to parallel the equilibrium 5curve for the desired product. The reactor 100 can comprise a shell 101 and internal catalyst tubes 109. The feed gas stream enters the reactor, flows through the shell 101, and is heated by indirect heat exchange with the catalyst tubes 109. The catalyst tubes 109 comprise reactive zones 122 having catalyst and reaction limited zones 124 that can comprise inert devices that function to both separate 10the reactive zones, increase heat transfer area, and reduce the temperature of the reaction mixture as the effluent passes through the catalyst tube 109.
摘要:
Process for the preparation of ammonia comprising steps of contacting an ammonia synthesis gas with an ammonia synthesis catalyst arranged as reaction zone in one or more catalyst tubes; cooling the reaction zone by heat conducting relationship with a cooling agent; and withdrawing an ammonia rich effluent stream from the reaction zone. The converter comprises at least one catalyst tube adapted to receive ammonia synthesis gas and to hold a reaction zone of ammonia synthesis catalyst and a cooling agent at the shell side of the catalyst tubes.
摘要:
A process for selective removal of at least a gaseous reaction product (P) from a gaseous system, the molecule of said reaction product having a non-zero electric dipole moment and the other gaseous components of said gaseous system having molecules with electric dipole moment which is null or negligible compared to the electric dipole moment of molecule of said reaction product; a non-uniform electric field (4) being generated between at least a positive electrode (2) and a negative electrode (1), said positive electrode and negative electrode being located at opposite sides of at least one permeation membrane (3), the selective passage of said reaction product through said membrane being enhanced by said electric field.