Carbon black reactor and process

Claim 2

A tubular carbon black reactor having a longitudinal axis extending from the upstream end to the downstream end thereof comprising a. an essentially cylindrical combustion section with the cylindrical axis coextensive with the longitudinal axis, said combustion section being confined by an upstream wall, a cylindrical wall, and a downstream wall, b. A reaction section in axial alignment and fluid communication operatively connected with said cylindrical combustion section at the downstream wall thereof, at least a portion of said reaction section being defined by three side walls, said portion having an essentially triangular cross-section, c. first means for generating a spirally swirling flow of hot combustion gases in said combustion zone being attached to said combustion zone, d. second means for introducing hydrocarbon feed essentially along the longitudinal axis in axial direction into the reactor, said second means being attached to an upstream confining wall of the reactor, and e. third means for withdrawing of carbon black-containing gas connected to the downstream end of said reaction section.

Claim 3

A carbon black reactor in accordance with claim 1 wherein the angles of said triangular cross-section are all within the range of 30°-100° .

Claim 4

A reactor in accordance with claim 2 wherein said cross-section is an equilateral triangle.

Claim 5

A carbon black reactor in accordance with claim 1 wherein said second means comprise a nozzle, the hydrocarbon discharge end of which is located within the combustion section axially at or downstream of the center of the combustion section.

Claim 6

A carbon black reactor in accordance with claim 1 comprising quench means for introducing quenching fluid to slow down or stop the carbon black formation reaction, which quenching means are located in the downstream section of said reaction section with triangular cross-section, and which quench means are located to discharge the quenching fluid in or near the edges of this section in which two side walls of the reaction section intersect.

Claim 7

A carbon black reactor in accordance with claim 1 wherein said essentially triangularly shaped cross-section has rounded-off corners.

Claim 8

A carbon black reactor in accordance with claim 1 wherein said reaction section is an essentially cylindrical reaction section having a choke in the upstream portion thereof, which choke has a triangular cross-section.

Claim 9

A carbon black reactor in accordance with claim 7 comprising a hydrocarbon feed nozzle extending into said choke with triangular cross-section, comprising a first tangential inlet said combustion section connected to a source of oxygen-rich hot combustion gases, and comprising a second tangential inlet into said combustion section connected to a source of fuel-rich hot combustion gases.

Claim 10

A carbon black reactor in accordance with claim 1 wherein said portion of the reaction section which has a triangular cross-section additionally is venturi-shaped and comprises an upstream portion converging in downstream direction and communicating with a downstream portion diverging in downstream direction, and converging and diverging portions having triangular cross-sections.

Claim 11

A carbon black reactor having a longitudinal axis extending from the upstream end to the downstream end of the reactor comprising a. a combustion section defined by an upstream confining wall and a downstream confining wall, both being essentially parallel to each other and perpendicular to the longitudinal axis of the reactor, and by three confining side walls, all three of these confining side walls being essentially parallel to the longitudinal axis of the reactor so that the cross-section of said combustion section is approximately triangular, b. in axial alignment and open communication with said combustion section and attached to the downstream wall thereof, a longitudinal reaction section having a smaller cross-section than said combustion section, c. first means attached to said combustion section for generating a closed loop flow of hot combustion gases along said three confining side walls in a direction perpendicular to the longitudinal axis, d. second means for introducing hydrocarbon feed along said longitudinal axis in axial direction into the carbon black reactor attached to an upstream confining wall of said reactor, and e. third means for withdrawing carbon black-containing gas connected to the downstream end of said reaction section.

Claim 12

A carbon black reactor having a longitudinal axis extending from the upstream end to the downstream end of the reactor comprising a. a combustion section defined by an upstream confining wall and a downstream confining wall, both being essentially parallel to each other and perpendicular to the longitudinal axis of the reactor, and by three confining side walls, all three of these confining side walls being essentially parallel to the longitudinal axis of the reactor so that the cross-section of said combustion section is approximately triangular, b. in axial alignment and open communication with said combustion section and attached to the downstream wall thereof, a longitudinal reaction section having a smaller cross-section than said combustion section, c. first means attached to said combustion section for generating a closed loop flow of hot combustion gases along said three confining side walls in a direction perpendicular to the longitudinal axis, d. second means for introducing hydrocarbon feed along said longitudinal axis in axial direction into the carbon black reactor attached to an upstream confining wall of said reactor, and e. third means for withdrawing carbon black-containing gas connected to the downstream end of said reaction section.

Claim 13

A carbon black reactor in accordance with claim 10 wherein said first means comprise three openings, one near each intersecting edge of two confining side walls and in one of these two confining side walls facing along the other of these two confining side walls, said three openings being in communication with a source of oxidant gas and of fuel for generating said flow of hot combustion gases along said three confining side walls.

Claim 14

A carbon black reactor in accordance with claim 10 wherein the angles of said triangular cross-section are all within the range of 30°-100°.

Claim 15

A carbon black reactor in accordance with claim 12 wherein said triangular cross-section is an equilateral triangle.

Claim 16

A carbon black reactor in accordance with claim 10 wherein said reaction section has a triangular cross-section.

Claim 17

A carbon black reactor in accordance with claim 14 wherein both the reaction section and the combustion section have an equilaterally triangular cross-section, wherein the two equilateral triangles are azimuthally turned relative to each other by 60° around the longitudinal reactor axis.

Claim 18

A carbon black reactor in accordance with claim 10 wherein said reaction section has a cylindrical cross-section.

Claim 19

A carbon black reactor in accordance with claim 10 wherein said reaction section is venturi-shaped.

Claim 20

A carbon black reactor in accordance with claim 10 wherein said reaction section is venturi-shaped and has a triangular cross-section both in the converging and the diverging portions of the venturi-shaped section.

Claim 21

A tubular carbon black reactor having a longitudinal axis extending from its upstream to its downstream end comprising a. a combustion section having a circular cross-section, b. in axial alignment and open communication operatively connected with said combustion section, a reaction section constituting the narrowest of the two sections, being defined by three or four sidewalls and having essentially triangular or, respectively, rectangular cross-section, c. first means attached to said combustion section for generating a closed loop spirally swirling flow of hot combustion gases in said combustion section,

Claim 22

A tubular carbon black reactor having a longitudinal axis extending from its upstream to its downstream end comprising a. a combustion section having a circular cross-section, b. in axial alignment and open communication operatively connected with said combustion section, a reaction section constituting the narrowest of the two sections, being defined by three or four sidewalls and having essentially triangular or, respectively, rectangular cross-section, c. first means attached to said combustion section for generating a closed loop spirally swirling flow of hot combustion gases in said combustion section,

Claim 23

d. second means attached to said reaction section for introducing hydrocarbon feed radially into said reaction section at approximately the center between two side edges, each one of these side edges being the intersection between two of the three or four sidewalls, and

Claim 24

d. second means attached to said reaction section for introducing hydrocarbon feed radially into said reaction section at approximately the center between two side edges, each one of these side edges being the intersection between two of the three or four sidewalls, and

Claim 25

e. third means attached to the downstream end of the reaction section for withdrawing carbon black-containing smoke.

Claim 26

e. third means attached to the downstream end of the reaction section for withdrawing carbon black-containing smoke.

Claim 27

A carbon black reactor in accordance with claim 19 wherein said first means comprise tangential oxidant feed means for introducing oxidant essentially tangentially in contact with the walls confining the combustion section, and radial fuel feed means for introducing fuel from approximately the longitudinal axis in radially outward direction, such as to produce swirling hot combustion gases in said combustion chamber.

Claim 28

A carbon black reactor in accordance with claim 19 wherein said combustion section is confined by an essentially plain upstream confining wall perpendicular to the longitudinal axis and by a frustoconically shaped confining wall having the longitudinal axis as its axis, and converging in downstream direction from said upstream confining wall into said reaction section.

Claim 29

A carbon black reactor in accordance with claim 19 wherein said combustion section is confined by an essentially plain upstream confining wall and by an essentially plain downstream confining wall, said plain walls being parallel to each other and perpendicular to the longitudinal axis of the reactor, and by a cylindrical wall connecting the two plain walls.

Claim 30

A carbon black reactor in accordance with claim 19 wherein every angle of the triangular cross-section of said reaction section is in the range of 30°-100° .

Claim 31

A carbon black reactor in accordance with claim 23 wherein all the angles are 60° .

Claim 32

A carbon black reactor in accordance with claim 19 wherein the cross-section of said reaction section is a square.

Claim 33

A carbon black reactor in accordance with claim 19 wherein said reaction section, having triangularly shaped cross-section, is connected with the downstream end thereof to a widened quench section.

Claim 34

A process for the production of carbon black comprising

Claim 35

A process for the production of carbon black comprising

Claim 36

a. generating a spiraling flow of hot combustion gases in a combustion section of a longitudinally disposed reactor having a longitudinal axis extending from the upstream end to the downstream end thereof,

Claim 37

a. generating a spiraling flow of hot combustion gases in a combustion section of a longitudinally disposed reactor having a longitudinal axis extending from the upstream end to the downstream end thereof,

Claim 38

b. introducing hydrocarbon feed liquid under normal conditions in axial direction along the longitudinal axis into said combustion section to produce a mixture of said hot combustion gases and said hydrocarbon feed,

Claim 39

b. introducing hydrocarbon feed liquid under normal conditions in axial direction along the longitudinal axis into said combustion section to produce a mixture of said hot combustion gases and said hydrocarbon feed,

Claim 40

c. moving said mixture of hot combustion gases and hydrocarbon feed into and through a reaction section being in axial alignment and open communication operatively connected with said combustion section, at least a portion of said reaction section having essentially triangularly shaped cross-section, and

Claim 41

c. moving said mixture of hot combustion gases and hydrocarbon feed into and through a reaction section being in axial alignment and open communication operatively connected with said combustion section, at least a portion of said reaction section having essentially triangularly shaped cross-section, and

Claim 42

d. withdrawing carbon black-containing smoke from the downstream end of the reaction section.

Claim 43

d. withdrawing carbon black-containing smoke from the downstream end of the reaction section.

Claim 44

A process in accordance with claim 27 wherein said hydrocarbon feed is discharged into the combustion section axially at or beyond the midpoint of the combustion section into admixture with the hot combustion gases.

Claim 45

A process in accordance with claim 28 wherein said hot combustion gases are generated by at least two burners discharging fuel and oxidant tangentially into a wide cylindrically shaped precombustion section, the equivalent weight ratio of oxidant to fuel being not more than 1.2 times the equivalent weight ratio for a stoichiometric combustion of the fuel in the oxidant.