Plate reactors for chemical syntheses under high pressure in gaseous phase and with heterogeneous catalysis

Claim 2

A process for effecting chemical syntheses from reaction gases in gaseous phase and under pressure in a reaction zone (8, see FIGS. 4 and 4A) defined by an enclosure of substantially cylindrical shape and of substantially circular transverse cross-section, the process being carried out in the presence of a solid catalyst, and said process being characterized in that the reaction zone is divided into a plurality of enclosures (9) containing the catalyst therein, said enclosures being shaped as elongate parallelipipeds and located adjacent to each other, the transverse cross-sections of these enclosures being substantially included in a circle coaxial to the circle defined by the circular section of the reaction zone, the adjacent walls (1, such as 1a, 1b, 1c) of these enclosures or walls common to adjacent enclosures being tight to the gases flowing through the reaction zone, the side walls (2, such as 2a, 2b, 2c, etc . . . ) of said enclosures (9) being permeable to the gases, with the gases introduced in the reaction zone thus flowing progressively through each of the enclosures substantially perpendicularly to the axis of the reaction zone, and these gases penetrating into each enclosure (9) through a permeable wall and issuing therefrom through a permeable wall opposite to the wall wherethrough the gases are admitted, the process being further characterized in that said walls (1, such as 1a, 1b, 1c, etc . . . ) are hollow plates whose internal spaces communicate with each other, and comprising flowing a fluid heat carrier through said walls or plates under a pressure substantially equal to the pressure to which are subjected the reaction gases.

Claim 3

A process according to claim 1, wherein the fluid heat carrier flows in each of said hollow plates through a network of substantially parallel channels whose sections have a shape selected from at least one of the following shapes: square, rectangular, curvilinear, cylindrical, elliptical, circular or triangular.

Claim 4

A process according to claim 1, wherein fresh gases or a gas charge penetrate into the reaction zone (8) through two lines (7) at the vicinity of each of the two first enclosures (9) the most remote from each other, hence the most remote from the axis of the reaction zone, said two first enclosures being diametrically opposite to each other, the gases or the charge then penetrating into each of these two enclosures, through the two permeable walls (2a) of each of said enclosures, the gases or the charge flowing thereafter inside the two first enclosures (9) in the direction of the second permeable wall (2b) of each of said two fist enclosures, the gases leaving each of these two first enclosures through said so-called permeable second wall (2b) and penetrating into another enclosure (9), adjacent to the two first enclosures, through one of the two permeable walls (2c) of said other enclosure, said permable walls being those in the immediate vicinity of said permeable walls (2b) wherethrough said gases were issuing from said first enclosures, the gases thus flowing, in two separate streams, progressively through the other enclosures (9), penetrating into each enclosure (9) through one of its permeable walls and issuing through the other permeable wall, thus reaching the one or more elongate central enclosures (9), which are arranged substantially along one of the diameter of the circular section of the reaction zone, wherefrom they are subsequently withdrawn through a line (6) as reaction effluent.

Claim 5

A process according to claim 1, wherein the velocity of the gases inside said enclosures is from about 1 to 200 meters/second.

Claim 6

A process according to claim 1, wherein the reaction zone is arranged substantially vertically.

Claim 7

A process according to claim 1, wherein the reaction zone is arranged substantially horizontally.

Claim 8

A process according to claim 1, wherein the lower part of the reaction zone, into which said inclosures penetrate at least partially, is filled with a layer of solid particles havin an average diameter from one half to one thousandth the average diameter of the catalyst particles.

Claim 9

A process according to claim 1, wherein, in order to maintain substantially equal the pressure of the reaction gases and the pressure at which is subjected the fluid heat carrier, the internal spaces of the hollow plates wherethough flows said fluid heat carrier are in contact with an expansion chamber whose level varies in accordance with the instantaneous volume of liquid heat carrier in said plates, the gaseous atmosphere of the expansion chamber consisting of reaction gases reaching said chamber through an adequate by-pass in communication with the reaction space in the reaction zone.

Claim 10

A process according to claim 1, wherein nitrogen and hydrogen are passed through the catalyst-containing enclosures, thereby forming ammonia.

Claim 11

A process according to claim 1, wherein hydrogen and at least one carbon oxide are passed through the catalyst-containing zones, thereby synthesizing methanol or higher homologue alcohols thereof.

Claim 12

A process for effecting chemical synthesis reactions from reaction gases in gaseous phase and under pressure in a reaction zone (8, see FIGS. 4 and 4A) defined as an enclosure of substantially cylindrical shape and of substantially circular transverse cross-section, the process being carried out in the presence of a solid catalyst, said process comprising circulating said reaction gases into the reaction zone (8) divided into a plurality of enclosures (9) containing the catalyst, said enclosures, being defined by adjacent walls (1, axial side walls such as 1a, 1b, 1c . . . ) parallel to one another and by side walls (2, axial end walls such as 2a, 2b, 2c . . . ) parallel to one another, said enclosures (9) being shaped as elongate parallelipipeds, substantially parallel to the axis of the reactor cylinder, and being adjacent to each other, the transverse cross-sections of the enclosures being substantially included in a circle coaxial to the circle defined by the circular section of the reaction zone, the adjacent walls (1) of these enclosures, or the common walls of the adjacent enclosures, being tight to the gases flowing through the reaction zone and forming a deflected path wherethrough the gas is compelled to flow, said side walls (2, axial end walls such as 2a, 2b, 3c . . . ) of said enclosures (9) being permeable to the gases, with these gases penetrating into each enclosure (9) through a permeable wall and issuing therefrom through a permeable wall opposite to the wall wherethrough the gases are admitted, flowing as a result progressively through each of the enclosures substantially perpendicular to the axis of the reaction zone, and said process comprising circulating a fluid heat carrier through said walls (1) which are hollow plates whose internal spaces communicate with each other, under a pressure substantially equal to the pressure to which are subjected the reaction gases.

Claim 13

A process for effecting chemical synthesis reactions from reaction gases in gaseous phase and under pressure in a reaction zone (8, see FIGS. 4 and 4A) defined as an enclosure of substantially cylindrical shape and of substantially circular transverse cross-section, the process being carried out in the presence of a solid catalyst, said process comprising circulating said reaction gases into the reaction zone (8) divided into a plurality of enclosures (9) containing the catalyst, said enclosures, being defined by adjacent walls (1, axial side walls such as 1a, 1b, 1c . . . ) parallel to one another and by side walls (2, axial end walls such as 2a, 2b, 2c . . . ) parallel to one another, said enclosures (9) being shaped as elongate parallelipipeds, substantially parallel to the axis of the reactor cylinder, and being adjacent to each other, the transverse cross-sections of the enclosures being substantially included in a circle coaxial to the circle defined by the circular section of the reaction zone, the adjacent walls (1) of these enclosures, or the common walls of the adjacent enclosures, being tight to the gases flowing through the reaction zone and forming a deflected path wherethrough the gas is compelled to flow, said side walls (2, axial end walls such as 2a, 2b, 3c . . . ) of said enclosures (9) being permeable to the gases, with these gases penetrating into each enclosure (9) through a permeable wall and issuing therefrom through a permeable wall opposite to the wall wherethrough the gases are admitted, flowing as a result progressively through each of the enclosures substantially perpendicular to the axis of the reaction zone, and said process comprising circulating a fluid heat carrier through said walls (1) which are hollow plates whose internal spaces communicate with each other, under a pressure substantially equal to the pressure to which are subjected the reaction gases.

Claim 14

A process according to claim 11, wherein the fluid heat carrier flows in each of said hollow plates through a network of substantially parallel channels whose sections have a shape selected from at least one of the following shapes: square, rectangular, curvilinear, cylindrical, elliptical, circular or triangular.

Claim 15

A process according to claim 11, wherein nitrogen and hydrogen are passed through the catalyst-containing enclosures, thereby forming ammonia.

Claim 16

A process according to claim 11, wherein hydrogen and at least one carbon oxide are passed through the catalyst-containing zones, thereby synthesizing methanol or higher homologue alcohols thereof.

Claim 17

A process according to claim 11, wherein the reaction zone is arranged substantially vertically.

Claim 18

A process according to claim 11, wherein the reaction zone is arranged substantially horizontally.