REACTIVE FLOW STATIC MIXER WITH CROSS-FLOW OBSTRUCTIONS
20170197189 ยท 2017-07-13
Inventors
- Paul A. Gillis (Lake Jackson, TN, US)
- Joydeep Mukherjee (Missouri City, TX, US)
- John B. Cooper (West Columbia, TX, US)
- Arthur C. Flores (Alvin, TX, US)
- Daniel J. Reed (Midland, MI, US)
Cpc classification
B01F25/31425
PERFORMING OPERATIONS; TRANSPORTING
B01F25/4315
PERFORMING OPERATIONS; TRANSPORTING
B01F25/431974
PERFORMING OPERATIONS; TRANSPORTING
B01F2101/2204
PERFORMING OPERATIONS; TRANSPORTING
B01F23/451
PERFORMING OPERATIONS; TRANSPORTING
B01F25/42
PERFORMING OPERATIONS; TRANSPORTING
B01F25/431972
PERFORMING OPERATIONS; TRANSPORTING
B01F25/4316
PERFORMING OPERATIONS; TRANSPORTING
B01F25/43171
PERFORMING OPERATIONS; TRANSPORTING
B01F25/4317
PERFORMING OPERATIONS; TRANSPORTING
C07C263/10
CHEMISTRY; METALLURGY
B01F25/43172
PERFORMING OPERATIONS; TRANSPORTING
International classification
C07C263/10
CHEMISTRY; METALLURGY
Abstract
Embodiments of the present invention relate to a mixing apparatus. Particularly, embodiments of the present invention provide a mixing apparatus for mixing fluid components such as phosgene and amine during a highly reactive chemical reaction. One embodiment provides a mixing conduit comprising a cylindrical sidewall defining an inner volume, wherein one or more jets are formed through the cylindrical sidewalls and connect to the inner volume and one or more flow obstructions disposed in the inner volume, wherein each flow obstruction is positioned upstream from an associated aperture.
Claims
1-17. (canceled)
18. A mixing conduit, comprising: a cylindrical sidewall defining an inner volume, wherein in use one or more jets are formed through the cylindrical sidewall and connect to the inner volume; and one or more flow obstructions disposed in the inner volume, wherein each flow obstruction is aligned upstream from an associated aperture; wherein the cylindrical sidewall comprises a plurality of apertures formed along a circumference of the cylindrical sidewall, wherein in use said apertures form said one or more jets, and the one or more flow obstructions comprises a plurality of spokes inserted into the inner volume along the circumference of the cylindrical sidewall, and wherein each of the plurality of spokes is aligned with an associated aperture to create a flow obstruction in the first flow before the first flow reaches the associated apertures; characterized in that each spoke has a section in the shape of one of a circle, oval, triangle, diamond, non-symmetrical diamond, or tear-drop; and wherein the plurality of spokes are coupled to a disk substantially concentric to the cylindrical sidewall of the mixing conduit.
19. The mixing conduit of claim 18, wherein each spoke is tapered having a large end coupled to the cylindrical sidewall and a small end near a central axis of the mixing conduit.
20. The mixing conduit of claim 18, wherein said apertures comprise a tapered aperture having a large opening outside the mixing conduit and a small opening inside the mixing conduit.
21. The mixing conduit of claim 18, wherein an additional aperture is disposed adjacent each of the plurality of apertures downstream on a longitudinal axis of the cylindrical sidewall.
22. The mixing conduit of claim 18, comprising at least two apertures disposed concentrically.
23. The mixing conduit of claim 18, wherein said plurality of apertures comprises an aperture tilted at an angle relative to a plane perpendicular to a longitudinal axis of the mixing conduit.
24. The mixing conduit of claim 18, wherein the one or more obstructions are mounted at an angle relative to a plane perpendicular to a longitudinal axis of the mixing conduit.
25. A static mixer comprising: one or more fluid receiving conduits defining one or more outer walls of an annular chamber; and a mixing conduit of claim 18 disposed in a first conduit defining at least an inner wall of the annular chamber, wherein the annular chamber is in fluid communication with the one or more jets of the mixing conduit.
26. A method for mixing comprising: flowing a first flow along a longitude of the mixing conduit of claim 18, wherein the one or more obstructions of the mixing conduit are upstream to the one or more jets of the mixing conduit; and flowing a second flow through the one or more apertures of the mixing conduit of claim 18.
27. The method of claim 26, wherein the first flow comprises phosgene and the second flow comprises amines, preferably wherein the second flow comprises at least one of methylene diphenyl diamine, toluene diamine, and hexamethylene diamine
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0015] So that the manner in which the above recited features of the present invention can be understood in detail, a more particular description of the invention, briefly summarized above, may be had by reference to embodiments, some of which are illustrated in the appended drawings. It is to be noted, however, that the appended drawings illustrate only typical embodiments of this invention and are therefore not to be considered limiting of its scope, for the invention may admit to other equally effective embodiments.
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[0028] To facilitate understanding, identical reference numerals have been used, where possible, to designate identical elements that are common to the figures. It is contemplated that elements disclosed in one embodiment may be beneficially utilized on other embodiments without specific recitation.
DETAILED DESCRIPTION
[0029] Embodiments of the present invention relate to a static mixing apparatus for mixing components, in applications with or without chemical reactions, where mixing is rate-limiting step and may cause undesired product formation. Particularly, embodiments of the present invention provide a mixing apparatus for mixing fluid components such as phosgene and amine during a highly reactive chemical reaction.
[0030] Static mixers of the present invention are designed to provide rapid mixing in industrial reactive processes, such as the reaction of MDA with phosgene to form MDI. Embodiments of the present invention provide static mixers that enable the phosgene to engulf the amine stream and minimize secondary reactions. The energy used to mix the fluid comes from the pressure drop in a mixing device. Static mixers of the present invention improve jet mixing process which enables increased production rates while maintaining reasonable pressure drop and improving product quality.
[0031] Embodiments of the present invention create a velocity profile in a first flow, typically a main cross-flow, as the first flow passes through a conduit and intersects with a second flow injected into the conduit by one or more jets formed through the conduit. In one embodiment, the velocity profile in the first flow is made by one or more flow obstructions placed upstream in the conduit. The one or more flow obstructions direct the first flow, such as phosgene, around the second flow, such as amine. The flow obstructions minimize the phosgene-deficient regions close to the amine jets and let the phosgene better engulf the amine stream.
[0032] One embodiment of the present invention provides a static mixer having a conduit with at least one aperture formed through a circumference of the conduit, and at least one obstruction disposed in the conduit upstream to the at least one aperture. During mixing, a first flow component flows through the conduit passing the at least one obstruction then encounters a second flow entering the conduit through the associated at least one aperture.
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[0034] The mixing conduit 100 comprises a cylindrical sidewall 101 defining an inner volume 107. A first flow 105 is configured to enter the inner volume 107 from an inlet end 108 of the mixing conduit 100. The mixing conduit 100 has a central axis 106.
[0035] A plurality of apertures 102 are formed through the cylindrical sidewall 101 around a circumference of the mixing conduit 100. The plurality of apertures 102 are configured to inject a second flow 104 to the inner volume 107 of the mixing conduit 100. In one embodiment, the plurality of apertures 102 are evenly distributed around the circumference of the mixing conduit 100.
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[0037] The mixing conduit 100 further comprises a plurality of spokes 103 disposed between the plurality of apertures 102 and the inlet end 108 of the mixing conduit 100. Each of the plurality of spokes 103 is aligned with an associated aperture 102 to create a flow obstruction in the first flow 105 before the first flow reaches the associated apertures 102.
[0038] In one embodiment, the plurality of spokes 103 are inserted into the mixing conduit 100 through the cylindrical sidewall 101. Each spoke 103 may have an inner end 103.sub.1 and an outer end 103.sub.2. The inner end 103.sub.1 is smaller than the outer end 103.sub.2 so that after the inner end 103a enters the mixing conduit 100 by penetrating the cylindrical sidewall 101, the outer end 103.sub.2 plugs the opening to seal the mixing conduit 100. Because each spoke 103 is directly aligned with an associated aperture 102, the spoke 103 creates a first flow velocity decrease upstream of the entrance of the second flow 104 from each aperture 102, therefore, allowing the second flow 104 to penetrate deeper inside the inner volume 107 and improving mixing.
[0039] Various factors may be adjusted to improve mixing according to the processing condition. For example, the distance 109 between the apertures 102 and the spokes 103, the size of each spoke 103, mounting angle of the spokes 103, the length of each spoke 103, the shape of the spoke 103, the design of the associated aperture 102, can be adjusted.
[0040] During mixing, the first flow 105 enters the mixing conduit 100 from the inlet end 108 and encounters the plurality of spokes 103. The plurality of spokes 103 mask the second flow 104 downstream from the cross-flow of the first flow 105 and increase the velocity of the first flow 105 in the spaces between the second flow from the apertures 102.
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[0042] The mixing conduit 100 isolates the first-flow conduits 153 from the second-flow conduit 155 so that the second flow 104 can only mix with the second flow 105 via the plurality of apertures 102 in the mixing conduit 100. The first flow 105 enters the mixing conduit 100 from the inlet end 152 of the first-flow conduit 153, passes the plurality of spokes 103, then mixes with the second flow 104 entering the mixing conduit 100 from the second conduit 155 through the plurality of apertures 102. The mixed flow 157 exits the mixing conduit 100 through the outlet end 158. In one embodiment the flow area within first-flow conduit 153 maybe varying to impart, for example a reducing and expanding flow profile.
[0043] It should be noted that the mixing conduit 100 may be used with other mixing devices. Various mixing conduits may be used with a static mixer of the present invention.
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[0054] Embodiments of spokes described above may be used in combination of various aperture designs.
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[0059] Detailed description of other jets that may be combined with obstructions described herein may be found in U.S. patent application Ser. No. 12/725,266 filed on Mar. 16, 2010, by at least a partial common inventorship, which is herein incorporated by reference.
EXAMPLE
[0060] Embodiments of the present inventions are used in mixing phosgene as the first flow with amine as the second flow as in MDI production process. The static mixer's performance is determined by the level of undesirable by-products, such as uretoneimines, and the pressure losses in the static mixer. In one embodiment, the second flow comprises at least one of methylene diphenyl diamine, toluene diamine, and hexamethylene diamine. Mixing conduits with flow obstructions according to embodiments of the present invention modifies velocity profiles in the first flow such that an amount of ureas, carbodiimides, and uretonimines formed are less than in a method where no obstructions are disposed in the inner volume. A comparison of performance of several mixers is given in Table 1.
[0061] For the mixers showing in Table 1, the number, size and shape of the amine jets were held constant. Option 1 represents the prior art with no upstream flow obstruction, as shown in
TABLE-US-00001 TABLE 1 Relative Comparison of Selectivity and Pressure Drop Option 1 Option 2 Option 4 Option 5 No Disc with Option 3 Tapered Spokes Obstruction Spokes Spokes Spokes Annulus Relative 1 0.89 0.96 0.88 0.80 uretonimine Amine 1 1.02 1.00 1.01 1.00 pressure drop Phosgene 1 1.10 1.04 1.08 1.23 pressure drop
[0062] While the foregoing is directed to embodiments of the invention, other and further embodiments of the invention may be devised without departing from the basic scope thereof.