Mixing apparatus with outlet nozzle and uses thereof

Claim 2

A process for the atomization of a flowable combustible material in an elongated atomization zone having an inlet and an outlet, comprising the steps of: (a) feeding in a substantially concentric and relatively independent feed relationship at least one stream of an auxiliary gas and at least one stream of said combustible material, under pressure, into said inlet of and through said elongated atomization zone and characterized by having substantially all of the pressure drop which occurs in said auxiliary gas and said combustible material in said atomization zone between said inlet and said outlet thereof, said feeding of said streams being characterized by said stream of combustible material being substantially non-atomized by said auxiliary gas stream prior to entry into said inlet of said atomization zone and said auxiliary gas and said combustible material streams being mixed substantially completely in said atomization zone; (b) expanding said auxiliary gas during its passage through said atomization zone and using the energy from the expansion thereof in said zone substantially only for directly propelling and directly atomizing said combustible material in said zone and simultaneously at spaced intervals along substantially the entire length of said zone splitting said gas and combustible material streams into partial streams and recombining said partial streams and changing the rotational direction of flow of said streams to produce an atomized combustible material at said outlet; (c) regulating the relative ratio of feed of said auxiliary gas stream and said combustible material stream into the inlet of said zone so that at the outlet of said zone there is provided a substantially continuously atomized combustible material including said auxiliary gas which occupies a substantially greater volume than that occupied by said combustible material; and (d) passing the atomized combustible material from said atomization zone through non-atomizing nozzle means located adjacent said outlet of said zone and constraining said atomized combustible material into a predetermined profile.

Claim 3

A process according to claim 1 including the step of reducing any gyratory component in said atomized combustible material as it passes through said nozzle means.

Claim 4

A process according to claim 1 including the step of constraining said atomized combustible material into a conical profile.

Claim 5

A process according to claim 1 including the step of passing said atomized combustible material from said zone through said nozzle means in a single stream.

Claim 6

A process according to claim 1 including the step of passing said atomized combustible material from said outlet through said nozzle means in a plurality of streams.

Claim 7

A process according to claim 1 including the step of directly expelling said atomized combustible material from said outlet through said nozzle means located adjacent said outlet of said zone.

Claim 8

A process according to claim 1 including the step of feeding said stream of combustible material at a pressure greater than that of said stream of auxiliary gas.

Claim 9

A process according to claim 1 including the step of passing said combustible material stream internally of said auxiliary gas stream.

Claim 10

A process according to claim 1 including the step of passing steam as said auxiliary gas into said atomization zone.

Claim 11

A process for the atomization of a flowable combustible material in an elongated atomization zone having an inlet and an outlet, comprising the steps of: (a) feeding in a substantially concentric and relatively independent feed relationship at least one stream of an auxiliary gas and at least one stream of said combustible material, under pressure, into said inlet of and through said elongated atomization zone and characterized by substantially all of the pressure drop in said streams being taken through said atomization zone, and said stream of combustible material being substantially non-atomized by said auxiliary gas stream prior to entry into the inlet of said atomization zone and said auxiliary gas and said combustible material streams being mixed substantially completely in said atomization zone; (b) expanding said auxiliary gas during its passage through said atomization zone and using the energy from the expansion thereof in said zone substantially only for directly propelling and directly atomizing said combustible material in said zone and simultaneously at spaced intervals along substantially the entire length of said zone splitting the gas and said combustible material streams into partial streams and recombining said partial streams and changing the rotational direction of flow of said streams to produce an atomized combustible product at said outlet; (c) regulating the relative ratio of feed of said auxiliary stream and said combustible material stream into the inlet of said zone so that at the outlet of said zone there is provided a substantially continuous atomized combustible product including said auxiliary gas which occupies a substantially greater volume than that occupied by said combustible material, delivering said combustible material into said atomization zone at a pressure greater than that of said auxiliary gas delivery pressure into said zone and maintaining said auxiliary gas pressure at a substantially constant level with respect to the delivery pressure of said combustible material and feeding said combustible material into said inlet of said atomization zone centrally with respect to said auxiliary gas stream, and further maintaining the temperature of said combustible material in respect to that of said auxiliary gas such that minimum condensation of said auxiliary gas occurs and (d) passing the atomized combustible material from said atomization zone through non-atomizing nozzle means located adjacent said outlet of said zone and constraining said atomized combustible material into a predetermined profile.

Claim 12

A process for the atomization of a flowable combustible material in an elongated atomization zone having an inlet and an outlet, comprising the steps of: (a) feeding in a substantially concentric and relatively independent feed relationship at least one stream of an auxiliary gas and at least one stream of said combustible material, under pressure, into said inlet of and through said elongated atomization zone and characterized by substantially all of the pressure drop in said streams being taken through said atomization zone, and said stream of combustible material being substantially non-atomized by said auxiliary gas stream prior to entry into the inlet of said atomization zone and said auxiliary gas and said combustible material streams being mixed substantially completely in said atomization zone; (b) expanding said auxiliary gas during its passage through said atomization zone and using the energy from the expansion thereof in said zone substantially only for directly propelling and directly atomizing said combustible material in said zone and simultaneously at spaced intervals along substantially the entire length of said zone splitting the gas and said combustible material streams into partial streams and recombining said partial streams and changing the rotational direction of flow of said streams to produce an atomized combustible product at said outlet; (c) regulating the relative ratio of feed of said auxiliary stream and said combustible material stream into the inlet of said zone so that at the outlet of said zone there is provided a substantially continuous atomized combustible product including said auxiliary gas which occupies a substantially greater volume than that occupied by said combustible material, delivering said combustible material into said atomization zone at a pressure greater than that of said auxiliary gas delivery pressure into said zone and maintaining said auxiliary gas pressure at a substantially constant level with respect to the delivery pressure of said combustible material and feeding said combustible material into said inlet of said atomization zone centrally with respect to said auxiliary gas stream, and further maintaining the temperature of said combustible material in respect to that of said auxiliary gas such that minimum condensation of said auxiliary gas occurs and (d) passing the atomized combustible material from said atomization zone through non-atomizing nozzle means located adjacent said outlet of said zone and constraining said atomized combustible material into a predetermined profile.

Claim 13

The process of claim 10 wherein said auxiliary gas comprises steam and the temperature of said steam is substantially the same as that of said combustible material at their delivery into said atomization zone.

Claim 14

The process of claim 10 wherein the temperature of said combustible material is equal to or greater than that of said auxiliary gas.

Claim 15

Apparatus for use in the atomization of combustible materials, comprising in combination: (a) an atomization zone having an inlet and an outlet end, said zone being cylindrical in shape and having a uniform cross-section; (b) a chamber connected adjacent said inlet end of said atomization zone and including a cross-section greater than said cross-section of said zone; (c) a first inlet for said chamber for feeding combustible material therein and a second inlet for said chamber for feeding an auxiliary gas therein, said first and second inlets being arranged in substantially concentric relationship relative to said inlet of said atomization zone; (d) mixing means internally secured in said atomization zone for the length thereof for imparting to said combustible material and auxiliary gas flowing therethrough a multiple shearing action and change in rotational direction thereof along the length of said zone; and (e) non-atomizing nozzle means adjacent said outlet end of said atomization zone for providing a predetermined profile to the atomized combustible material which exits said atomization zone.

Claim 16

Apparatus for use in the atomization of combustible materials, comprising in combination: (a) an atomization zone having an inlet and an outlet end, said zone being cylindrical in shape and having a uniform cross-section; (b) a chamber connected adjacent said inlet end of said atomization zone and including a cross-section greater than said cross-section of said zone; (c) a first inlet for said chamber for feeding combustible material therein and a second inlet for said chamber for feeding an auxiliary gas therein, said first and second inlets being arranged in substantially concentric relationship relative to said inlet of said atomization zone; (d) mixing means internally secured in said atomization zone for the length thereof for imparting to said combustible material and auxiliary gas flowing therethrough a multiple shearing action and change in rotational direction thereof along the length of said zone; and (e) non-atomizing nozzle means adjacent said outlet end of said atomization zone for providing a predetermined profile to the atomized combustible material which exits said atomization zone.

Claim 17

Apparatus according to claim 13 wherein said nozzle means comprises a nozzle having a single cylindrical passageway whose diameter is between 0.5 and 0.9 of the diameter of said zone.

Claim 18

An apparatus according to claim 13 wherein said nozzle means comprises a nozzle having at least two passageways angularly disposed to form a divergent cone with respect to the axis of said zone.

Claim 19

Apparatus according to claim 13 wherein said nozzle means comprises a nozzle at said outlet end of said zone for retaining said mixing means in said zone.

Claim 20

A process for the atomization of a flowable combustible material comprising the steps of: (a) feeding at least one stream of an auxiliary gas and at least one stream of said combustible material independently of said at least one stream of auxiliary gas, under pressure, into and through an elongated atomization zone having an inlet and an outlet and characterized by substantially all of the pressure drop in said streams being taken through said atomization zone and said stream of combustible material being substantially non-atomized by said auxiliary gas stream prior to entry into the inlet of said atomization zone; (b) expanding said auxiliary gas simultaneously at spaced intervals along substantially the entire length of said zone splitting the gas and said combustible material streams into partial streams and recombining said partial streams and changing the rotational direction of flow of said streams to produce an atomized combustible product at said outlet; (c) regulating the relative ratio of feed of said auxiliary stream and said combustible material stream into the inlet of said zone so that at the outlet of said zone there is provided a substantially continuous atomized combustible product including said auxiliary gas which occupies a substantially greater volume than that occupied by said combustible material, delivering said combustible material into said atomization zone at a pressure greater than that of said auxiliary gas delivery pressure into said zone and maintaining said auxiliary gas pressure at a substantially constant level with respect to the delivery pressure of said combustible material and feeding said combustible material into said inlet of said atomization zone centrally with respect to said auxiliary gas stream, and further maintaining the temperature of said combustible material in respect to that of said auxiliary gas such that minimum condensation of said auxiliary gas occurs and increasing the delivery rate of said combustible material whereby there is a corresponding decrease in the consumption of said auxiliary gas, while the pressure of said auxiliary gas is maintained substantially constant.

Claim 21

A process for the atomization of a flowable combustible material comprising the steps of: (a) feeding at least one stream of an auxiliary gas and at least one stream of said combustible material independently of said at least one stream of auxiliary gas, under pressure, into and through an elongated atomization zone having an inlet and an outlet and characterized by substantially all of the pressure drop in said streams being taken through said atomization zone and said stream of combustible material being substantially non-atomized by said auxiliary gas stream prior to entry into the inlet of said atomization zone; (b) expanding said auxiliary gas simultaneously at spaced intervals along substantially the entire length of said zone splitting the gas and said combustible material streams into partial streams and recombining said partial streams and changing the rotational direction of flow of said streams to produce an atomized combustible product at said outlet; (c) regulating the relative ratio of feed of said auxiliary stream and said combustible material stream into the inlet of said zone so that at the outlet of said zone there is provided a substantially continuous atomized combustible product including said auxiliary gas which occupies a substantially greater volume than that occupied by said combustible material, delivering said combustible material into said atomization zone at a pressure greater than that of said auxiliary gas delivery pressure into said zone and maintaining said auxiliary gas pressure at a substantially constant level with respect to the delivery pressure of said combustible material and feeding said combustible material into said inlet of said atomization zone centrally with respect to said auxiliary gas stream, and further maintaining the temperature of said combustible material in respect to that of said auxiliary gas such that minimum condensation of said auxiliary gas occurs and increasing the delivery rate of said combustible material whereby there is a corresponding decrease in the consumption of said auxiliary gas, while the pressure of said auxiliary gas is maintained substantially constant.

Claim 22

A process for the atomization of a flowable combustible material comprising the steps of: (a) feeding at least one stream of an auxiliary gas and at least one stream of said combustible material independently of said at least one stream of auxiliary gas, under pressure, into and through an elongated atomization zone having an inlet and an outlet and characterized by substantially all of the pressure drop in said streams being taken through said atomization zone and said stream of combustible material being substantially non-atomized by said auxiliary gas stream prior to entry into the inlet of said atomization zone; (b) expanding said auxiliary gas simultaneously at spaced intervals along substantially the entire length of said zone splitting the gas and said combustible material streams into partial streams and recombining said partial streams and changing the rotational direction of flow of said streams to produce an atomized combustible product at said outlet; (c) regarding the relative ratio of feed of said auxiliary stream and said combustible material stream into the inlet of said zone so that at the outlet of said zone there is provided a substantially continuous atomized combustible product including said auxiliary gas which occupies a substantially greater volume than that occupied by said combustible material, delivering said combustible material into said atomization zone at a pressure greater than that of said auxiliary gas delivery pressure into said zone and maintaining said auxiliary gas pressure at a substantially constant level with respect to the delivery pressure of said combustible material and feeding said combustible material into said inlet of said atomization zone centrally with respect to said auxiliary gas stream, and further maintaining the temperature of said combustible material in respect to that of said auxiliary gas such that minimum condensation of said auxiliary gas occurs and maintaining the flow rate of said combustible material proportional to the square root of the pressure differential between said combustible material and said auxiliary gas.

Claim 23

A process for the atomization of a flowable combustible material comprising the steps of: (a) feeding at least one stream of an auxiliary gas and at least one stream of said combustible material independently of said at least one stream of auxiliary gas, under pressure, into and through an elongated atomization zone having an inlet and an outlet and characterized by substantially all of the pressure drop in said streams being taken through said atomization zone and said stream of combustible material being substantially non-atomized by said auxiliary gas stream prior to entry into the inlet of said atomization zone; (b) expanding said auxiliary gas simultaneously at spaced intervals along substantially the entire length of said zone splitting the gas and said combustible material streams into partial streams and recombining said partial streams and changing the rotational direction of flow of said streams to produce an atomized combustible product at said outlet; (c) regarding the relative ratio of feed of said auxiliary stream and said combustible material stream into the inlet of said zone so that at the outlet of said zone there is provided a substantially continuous atomized combustible product including said auxiliary gas which occupies a substantially greater volume than that occupied by said combustible material, delivering said combustible material into said atomization zone at a pressure greater than that of said auxiliary gas delivery pressure into said zone and maintaining said auxiliary gas pressure at a substantially constant level with respect to the delivery pressure of said combustible material and feeding said combustible material into said inlet of said atomization zone centrally with respect to said auxiliary gas stream, and further maintaining the temperature of said combustible material in respect to that of said auxiliary gas such that minimum condensation of said auxiliary gas occurs and maintaining the flow rate of said combustible material proportional to the square root of the pressure differential between said combustible material and said auxiliary gas.

Claim 24

A process for the atomization of a flowable combustible material comprising the steps of: (a) feeding at least one stream of an auxiliary gas and at least one stream of said combustible material independently of said at least one stream of auxiliary gas, under pressure, into and through an elongated atomization zone having an inlet and an outlet and characterized by substantially all of the pressure drop in said streams being taken through said atomization zone and said stream of combustible material being substantially non-atomized by said auxiliary gas stream prior to entry into the inlet of said atomization zone; (b) expanding said auxiliary gas simultaneously at spaced intervals along substantially the entire length of said zone splitting the gas and said combustible material streams into partial streams and recombining said partial streams and changing the rotational direction of flow of said streams to produce an atomized combustible product at said outlet; (c) regulating the relative ratio of feed of said auxiliary stream and said combustible material stream into the inlet of said zone so that at the outlet of said zone there is provided a substantially continuous atomized combustible product including said auxiliary gas which occupies a substantially greater volume than that occupied by said combustible material, delivery said combustible material into said atomization zone at a pressure greater than that of said auxiliary gas delivery pressure into said zone and maintaining said auxiliary gas pressure at a substantially constant level in the range between substantially 8.5 to substantially 10 bars, with respect to the delivery pressure of said combustible material and feeding said combustible material into said inlet of said atomization zone centrally with respect to said auxiliary gas stream, and further maintaining the temperature of said combustible material in respect to that of said auxiliary gas such that minimum condensation of said auxiliary gas occurs.

Claim 25

A process for the atomization of a flowable combustible material comprising the steps of: (a) feeding at least one stream of an auxiliary gas and at least one stream of said combustible material independently of said at least one stream of auxiliary gas, under pressure, into and through an elongated atomization zone having an inlet and an outlet and characterized by substantially all of the pressure drop in said streams being taken through said atomization zone and said stream of combustible material being substantially non-atomized by said auxiliary gas stream prior to entry into the inlet of said atomization zone; (b) expanding said auxiliary gas simultaneously at spaced intervals along substantially the entire length of said zone splitting the gas and said combustible material streams into partial streams and recombining said partial streams and changing the rotational direction of flow of said streams to produce an atomized combustible product at said outlet; (c) regulating the relative ratio of feed of said auxiliary stream and said combustible material stream into the inlet of said zone so that at the outlet of said zone there is provided a substantially continuous atomized combustible product including said auxiliary gas which occupies a substantially greater volume than that occupied by said combustible material, delivery said combustible material into said atomization zone at a pressure greater than that of said auxiliary gas delivery pressure into said zone and maintaining said auxiliary gas pressure at a substantially constant level in the range between substantially 8.5 to substantially 10 bars, with respect to the delivery pressure of said combustible material and feeding said combustible material into said inlet of said atomization zone centrally with respect to said auxiliary gas stream, and further maintaining the temperature of said combustible material in respect to that of said auxiliary gas such that minimum condensation of said auxiliary gas occurs.

Claim 26

Apparatus for use in the atomization of combustible materials, comprising in combination: (a) an atomization zone having an inlet and an outlet end, said zone being cylindrical in shape and having a uniform cross-section; (b) a chamber connected adjacent said inlet end of said atomization zone and including a cross-section greater than said cross-section of said zone; (c) a first inlet for said chamber for feeding combustible material therein and a second inlet for said chamber for feeding an auxiliary gas therein, said first and second inlets being arranged in substantially concentric relationship relative to said inlet of said atomization zone; (d) mixing means comprising a plurality of vanes internally secured in said atomization zone for the length thereof for imparting to said combustible material and auxiliary gas flowing therethrough a multiple shearing action and change in rotational direction thereof along the length of said zone; and (e) non-atomizing nozzle means comprising a nozzle located externally of and directly adjacent said outlet end of said atomization zone for providing a predetermined profile to the atomized combustible material which exits said atomization zone and said nozzle being disposed in abutting relation with respect to the adjacent one of said vanes for retaining said vanes in said zone.

Claim 27

Apparatus for use in the atomization of combustible materials, comprising in combination: (a) an atomization zone having an inlet and an outlet end, said zone being cylindrical in shape and having a uniform cross-section; (b) a chamber connected adjacent said inlet end of said atomization zone and including a cross-section greater than said cross-section of said zone; (c) a first inlet for said chamber for feeding combustible material therein and a second inlet for said chamber for feeding an auxiliary gas therein, said first and second inlets being arranged in substantially concentric relationship relative to said inlet of said atomization zone; (d) mixing means comprising a plurality of vanes internally secured in said atomization zone for the length thereof for imparting to said combustible material and auxiliary gas flowing therethrough a multiple shearing action and change in rotational direction thereof along the length of said zone; and (e) non-atomizing nozzle means comprising a nozzle located externally of and directly adjacent said outlet end of said atomization zone for providing a predetermined profile to the atomized combustible material which exits said atomization zone and said nozzle being disposed in abutting relation with respect to the adjacent one of said vanes for retaining said vanes in said zone.

Claim 28

Apparatus according to claim 20 wherein said nozzle includes an inwardly projecting portion toward said atomization zone.