Heterogeneous reactor

• US 4,744,958 A
• Filed: 03/28/1986
• Issued: 05/17/1988
• Est. Priority Date: 05/12/1972
• Status: Expired due to Fees

• Current Assignee: Pircon Dolores R
• Original Assignee: Pircon Dolores R Executor To The Estate of Piron Ladislav Dec'D
• Inventors: Pircon, Ladislav J.
• Primary Examiner(s): Nozick, Bernard
• Application Number:
  US06/845,614
• Time in Patent Office: 781 Days
• Field of Search: 55/84-91, 55/240, 55/241, 55/465, 55/257 NP, 261/116, 261/DIG. 54, 422/193
• US Class Current: 422/606
• CPC Class Codes: B01D 2221/02 Small separation devices for domestic application, e.g. for canteens, industrial kitchen, washing machines
• CPC Class Codes: B01D 45/08 by impingement against baffle separators
• CPC Class Codes: B01D 47/06 Spray cleaning
• CPC Class Codes: B01D 47/10 Venturi scrubbers
• CPC Class Codes: B01J 19/22 in the form of endless belts
• CPC Class Codes: B01J 19/26 Nozzle-type reactors, i.e. the distribution of the initial reactants within the reactor is effected by their introduction or injection through nozzles
• CPC Class Codes: B01J 2219/00051 Controlling the temperature
• CPC Class Codes: B01J 2219/00121 by direct heating or cooling
• CPC Class Codes: B01J 2219/00128 by evaporation of reactants
• CPC Class Codes: B01J 2219/00162 controlling the pressure
• CPC Class Codes: B01J 2219/00164 controlling the flow
• CPC Class Codes: B01J 8/22 gas being introduced into the liquid

Abstract

An apparatus for promoting heterogeneous chemical and physical reactions in a gas stream using a casing which is substantially liquid and gas tight having a gas inlet in one end and a gas outlet in the other end; nozzle means within the casing having an entry toward said one end in communication with the gas inlet and an outlet toward said other end, said nozzle means having an effective cross-sectional area of about 2 to about 64 times the effective cross-sectional area of the outlet and the mean angle of convergence of the nozzle being about 6° to about 20°; means in the casing for introduction of reactant liquids and solids into the gas stream before said nozzle means; means for removing liquid and particulate matter from said other end of the casing following desired reaction; and means for separately removing the gas from said other end of the casing. The apparatus and process of this invention is especially useful in providing a self-cleaning, non-clogging system for inducing high reaction kinetics without the normally required high turbulence and concurrent pressure drop of a scrubber; or packing to provide surface area such as used in conventional absorber.

Claims

1. 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 comprising:

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°

to 20°

, 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 said variable 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 liquids or solids as variable sized non-compressible liquids 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.

2. The apparatus of claim 1 wherein a spray means introduces solid particles of differing sizes between about 40 to about 1500 microns in diameter to the gas stream prior to said nozzle.

3. The apparatus of claim 1 wherein 2 to about 6 single nozzle stages are in series within said casing.

4. The apparatus of claim 1 having 2 to about 6 multiple nozzle stages each said nozzle stage having 2 to about 6 nozzles.

5. The apparatus of claim 1 wherein the pressure drop is 3.5 inches of water and less across each nozzle stage.

6. The apparatus of claim 1 wherein said mean angle of convergence is about 8°

to 18°

.

7. The apparatus of claim 1 wherein said entry of the nozzle has an effective cross-sectional area about 2 to about 36 times the cross-sectional area of the nozzle outlet.

8. The apparatus of claim 1 wherein said mean angle of convergence is about 12°

to about 16° and

said entry of the nozzle has an effective cross-sectional area about 2 to about 4 times the effective cross-sectional area of the nozzle outlet.

9. The apparatus of claim 1 additionally having impingement means beyond said nozzle outlet 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.

10. The apparatus of claim 1 wherein said mean angle of convergence is about 12°

to about 16°

.

11. The apparatus of claim 1 wherein a spray means introduces liquid in droplet form to the gas stream prior to said nozzle entry.

12. The apparatus of claim 11 wherein said spray means introduces droplets about 40 to about 1500 microns in diameter and in an amount of about 0.8 gallons liquid per 1000 cubic feet of said gas.

13. 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°

to 20°

, 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.

14. The apparatus of claim 13 wherein a spray means introduces solid particles of differing sizes between about 40 to about 1500 microns in diameter to the gas stream prior to said nozzle entry.

15. The apparatus of claim 13 wherein the pressure drop is 3.5 inches of water and less across each stage.

16. The apparatus of claim 13 wherein said mean angle of convergence is about 8°

to 18°

.

17. The apparatus of claim 13 wherein said entry of the nozzle has an effective cross-sectional area about 2 to about 36 times the cross-sectional area of the nozzle outlet.

18. The apparatus of claim 13 wherein said mean angle of convergence is about 12°

to about 16° and

said entry of the nozzle has an effective cross-sectional area about 2 to about 4 times the effective cross-sectional area of the nozzle outlet.

19. The apparatus of claim 13 wherein said mean angle of convergence is about 12°

to about 16°

.

20. The apparatus of claim 13 wherein a spray means introduces liquid in droplet form to the gas stream prior to said nozzle.

21. The apparatus of claim 20 wherein said spray means introduces droplets of differing sizes between about 40 to about 1500 microns in diameter and in an amount of about 0.9 gallons liquid per 1000 cubic feet of said gas.

22. 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°

to 20°

, 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.

23. 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°

to 20°

, 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.