Heterogeneous reactor

A low pressure drop apparatus, having pressure drop of less than that characteristic of a high turbulence reactor, for promoting heterogeneous chemical and physical reactions in a gas stream by cocurrent movement of said gas stream and reactant liquids or solids comprising:

• a vertical casing which is substantially liquid and gas tight having a gas inlet in the upper end and a gas outlet in the lower end and means capable of introducing said gas stream through said inlet at a velocity of about 380 to about 2100 feet per minute;
• two to six straight sided continually converging nozzle means having a common axis and each said nozzle symmetrical with respect to said axis within said casing having an entry at the upper end in communication with said gas inlet and an outlet at the lower end, said entry being unrestricted allowing entry of all said reactant liquids or solids and being in substantially closed relation to said casing to avoid substantial bypass of said nozzle and having an effective cross-sectional area of about 2 to about 64 times the effective cross-sectional area of said outlet and the mean angle of convergence of said nozzle being about 6.degree. to 20.degree., said outlet being formed by the end of straight continually converging sides of said nozzle means and being unrestricted allowing passage of all said reactant liquids or solids, said nozzle having unrestricted flow of said gas stream and said reactant liquids or solids therethrough creating substantially only along the axis of said nozzle means differential velocities and differential accelerations and decelerations between various sized non-compressible liquids or solids and the compressible gas passing through said nozzle maintaining plug flow of said gas stream and creating pressure drops of less than about 11.2 inches of water promoting said reactions;
• spray means in said casing for introduction of said reactant liquids or solids as variable sized non-compressible liquids or solids to said gas stream prior to each said nozzle entry;
• solid plate impingement means beyond at least one of said nozzle outlets at a distance from said outlet of about 1.3 to about 2.5 times the diameter of said outlet to retain said plug flow of said gas stream prior to said impingement means and sized to insure impingement thereon of substantially all liquid and particulate matter entrained in the gas stream passing from said nozzle outlet;
• means for removing liquid and particulate matter from said lower end of said casing following desired reaction;
• and
• means for removing the gas separately from the liquid and particulate matter from said lower end of said casing, said gas being removed without passage through any liquid pool.

A low pressure drop apparatus, having pressure drop of less than that characteristic of high turbulence reactors, for promoting heterogeneous chemical and physical reactions in a gas stream by cocurrent movement of said gas stream and reactant liquids or solids consisting of:

• a casing which is substantially liquid and gas tight having a gas inlet in one end and a gas outlet in the other end and means capable of introducing said gas stream through said inlet at a velocity of about 380 to about 2100 feet per minute;
• two to six straight sided continually converging nozzle means having a common axis and each said nozzle symmetrical with respect to its axis within said casing having an entry at one end in communication with said gas inlet and an outlet at the other end, said entry being unrestricted allowing entry of all said reactant liquids or solids and being in substantially closed relation to said casing to avoid substantial bypass of said nozzle and having an effective cross-sectional area of about 2 to about 64 times the effective cross-sectional area of said outlet and the mean angle of convergence of said nozzle being about 6.degree. to 20.degree., said outlet being formed by the end of straight continually converging sides of said nozzle means and being unrestricted allowing passage of all said reactant liquids or solids, said nozzle means having unrestricted flow of said gas stream and said reactant liquids or solids therethrough creating substantially only along the axis of said nozzle means differential velocities and differential accelerations and decelerations between the various sized non-compressible liquids or solids and the compressible gas passing through said nozzle maintaining plug flow of said gas stream and creating pressure drops less than about 11.2 inches of water promoting said reactions;
• reactant introduction means in said one end of said casing prior to said entry to said converging nozzle means for introduction of said reactant liquid or solids;
• means for removing liquid and particulate matter from said casing following desired reaction;
• and
• means for removing the gas separately from the liquid and particulate matter from said other end of said casing, said gas being removed without passage through any liquid pool.

A low pressure drop apparatus, having pressure drop of less than that characteristic of a high turbulence reactor, for promoting heterogeneous chemical and physical reactions in a gas stream by cocurrent movement of said gas stream and reactant liquids or solids consisting of:

• a vertical casing which is substantially liquid and gas tight having a gas inlet in the upper end and a gas outlet in the lower end and means capable of introducing said gas stream through said inlet at a velocity of about 380 to about 2100 feet per minute;
• two to six straight sided continually converging nozzle means having a common axis and each said nozzle symmetrical with respect to said axis within said casing having an entry at the upper end in communication with said gas inlet and an outlet at the lower end, said entry being unrestricted allowing entry of all said reactant liquids or solids and being in substantially closed relation to said casing to avoid substantial bypass of said nozzle and having an effective cross-sectional area of about 2 to about 64 times the effective cross-sectional area of said outlet and the mean angle of convergence of said nozzle being about 6.degree. to 20.degree., said outlet being formed by the end of straight continually converging sides of said nozzle means and being unrestricted allowing passage of all said reactant liquids or solids, said nozzle having unrestricted flow of said gas stream and said reactant liquids or solids therethrough creating substantially only along the axis of said nozzle means differential velocities and differential accelerations and decelerations between various sized non-compressible liquids or solids and the compressible gas passing through said nozzle maintaining plug flow of said gas stream and creating pressure drops of less than about 11.2 inches of water promoting said reactions;
• spray means in said casing for introduction of said reactant liquids or solids to said gas stream prior to each said nozzle entry;
• solid plate impingement means beyond at least one of said nozzle outlets at a distance from said outlet of about 1.3 to about 2.5 times the diameter of said outlet to retain said plug flow of said gas stream prior to said impingement means and sized to insure impingement thereon of substantially all liquid and particulate matter entrained in the gas stream passing from said nozzle outlet;
• means for removing liquid and particulate matter from said lower end of said casing following desired reaction;
• and
• means for removing the gas separately from the liquid and particulate matter from said lower end of said casing, said gas being removed without passage through any liquid pool.