FLUID-CONDUCTING DEVICE AND METHOD FOR MIXING FLUIDS
20200222876 · 2020-07-16
Inventors
- Manfred Steinbauer (Raisting, DE)
- Hans-Joerg ZANDER (München, DE)
- Ole MUELLER-THORWART (Eichenau, DE)
- Konrad BRAUN (Lenggries, DE)
- Stefan GEWALD (München, DE)
Cpc classification
B01F25/31434
PERFORMING OPERATIONS; TRANSPORTING
F28F9/0265
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
B01F23/451
PERFORMING OPERATIONS; TRANSPORTING
F28D2021/0052
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F28F9/026
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
B01L3/502
PERFORMING OPERATIONS; TRANSPORTING
F28D21/0015
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F28D2021/0022
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F28F9/0278
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
B33Y80/00
PERFORMING OPERATIONS; TRANSPORTING
F28F9/0282
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
B01J19/24
PERFORMING OPERATIONS; TRANSPORTING
B01J19/00
PERFORMING OPERATIONS; TRANSPORTING
B01L3/00
PERFORMING OPERATIONS; TRANSPORTING
Abstract
The invention relates to a fluid-conducting device (10) having a conduit block (12), within which there are formed multiple primary conduits (14) which extend in a primary conduit direction (100) and which are designed to conduct a primary fluid. The fluid-conducting device furthermore has at least one secondary conduit (16), which extends at least partially in a secondary conduit direction (102) extending at least partially perpendicular to the primary conduit direction (100) and which is designed to conduct or to receive a secondary fluid. Here, the at least one secondary conduit (16) opens into at least one of the primary conduits (14) in order to allow the secondary fluid to flow into the at least one primary conduit (14) via the secondary conduit (16); wherein the fluid-conducting device (10) is formed at least partially by an additive manufacturing process, wherein the multiple primary conduits (14) extend parallel to one another exclusively in a primary conduit direction, wherein the fluid-conducting device (10) is configured such that it can be arranged between two tubing elements and can be fastened thereto such that a primary fluid stream through the first tubing element in the primary conduit direction passes to the fluid-conducting device (10) such that the primary fluid stream is able to penetrate into the primary conduits (14) in the conduit block (12), and such that a fluid flowing out of the fluid-conducting device in the primary conduit direction is able to flow out of the fluid-conducting device into the second tubing element. The invention also relates to a tube plate, to a tube reactor, and to a static mixer (28), which have a fluid-conducting device (10) according to the invention. The invention moreover relates to a method for mixing fluids, and to a method for producing a fluid-conducting device and/or a tube plate.
Claims
1. A fluid-conducting device (10) having: a conduit block (12), within which there are formed multiple primary conduits (14) which extend in a primary conduit direction (100) and which are designed to conduct a primary fluid; at least one secondary conduit (16), which extends at least partially in a secondary conduit direction (102) extending at least partially perpendicular to the primary conduit direction (100) and which is designed to conduct a secondary fluid; wherein the at least one secondary conduit (16) opens into at least one of the primary conduits (14) in order to allow the secondary fluid to flow into the at least one primary conduit (14) via the secondary conduit (16); and wherein the fluid-conducting device (10) is formed at least partially by an additive manufacturing process, wherein the multiple primary conduits (14) extend parallel to one another exclusively in a primary conduit direction, wherein the fluid-conducting device (10) is configured such that it can be arranged between two tubing elements and can be fastened thereto such that a primary fluid stream through the first tubing element in the primary conduit direction passes to the fluid-conducting device (10) such that the primary fluid stream is able to penetrate into the primary conduits (14) in the conduit block (12), and such that a fluid flowing out of the fluid-conducting device (10) in the primary conduit direction is able to flow out of the fluid-conducting device (10) into the second tubing element.
2. The fluid-conducting device (10) as claimed in claim 1, wherein the multiple primary conduits (14) extend substantially parallel to one another, and/or wherein the at least one secondary conduit (16) is arranged so as to extend substantially in at least one secondary conduit plane, wherein the at least one secondary conduit plane preferably extends substantially perpendicular to the primary conduit direction (100).
3. The fluid-conducting device (10) as claimed in claim 1, wherein the fluid-conducting device (10) has multiple secondary conduits (16), and/or wherein the at least one secondary conduit (16) is formed at least partially within the conduit block (12).
4. The fluid-conducting device (10) as claimed in claim 1, wherein the at least one secondary conduit (16) is formed at least partially as a secondary conduit structure (18), and wherein the secondary conduit structure (18) is formed at least partially outside the conduit block (12) and is preferably fastened to the conduit block (12).
5. The fluid-conducting device (10) as claimed in claim 4, wherein the secondary conduit structure (18) is formed integrally with the conduit block (12) and/or is preferably produced at least partially by an additive manufacturing process.
6. The fluid-conducting device (10) as claimed in claim 1, wherein the multiple primary conduits (14) each have an inlet opening, wherein the inlet openings of the multiple primary conduits (14) are arranged so as to lie in an inlet plane, and wherein the conduit block (12) preferably terminates flush with the inlet openings.
7. The fluid-conducting device (10) as claimed in claim 1, wherein the fluid-conducting device (10) is formed integrally.
8. The fluid-conducting device (10) as claimed in claim 1, wherein the at least one secondary conduit (16) opens into a plurality of primary conduits (14) of the multiple primary conduits (14).
9. A tube plate for a heat exchanger, wherein the tube plate has a fluid-conducting device (10) as claimed in claim 1, and wherein the tube plate is designed such that tubings (24) are connectable to the primary conduits (14).
10. A tube reactor having a fluid-conducting device (10) as claimed in claim 1, wherein at least one reactor tube is connected to the primary conduits (14) so as to extend in the primary conduit direction (100).
11. A static mixer (26) having a fluid-conducting device (10) as claimed in claim 1, wherein at least one tubing element (28) is connected to the primary conduits (14) so as to extend in the primary conduit direction (100).
12. A method for mixing a secondary fluid into a primary fluid, comprising the steps of: providing a fluid-conducting device (10) produced at least partially by an additive manufacturing process and having: a conduit block (12), within which there are formed multiple primary conduits (14) which extend in a primary conduit direction (100) and which are designed to conduct a primary fluid; at least one secondary conduit (16), which extends at least partially in a secondary conduit direction (102) extending at least partially perpendicular to the primary conduit direction (100) and which is designed to conduct a secondary fluid; wherein the at least one secondary conduit (16) opens into at least one of the primary conduits (14) in order to allow the secondary fluid to flow into the at least one primary conduit (14) via the secondary conduit (16); and wherein the multiple primary conduits (14) extend parallel to one another exclusively in a primary conduit direction, wherein the fluid-conducting device (10) is configured such that it can be arranged between two tubing elements and can be fastened thereto such that a primary fluid stream through the first tubing element in the primary conduit direction passes to the fluid-conducting device (10) such that the primary fluid stream is able to penetrate into the primary conduits (14) in the conduit block (12), and such that a fluid flowing out of the fluid-conducting device (10) in the primary conduit direction is able to flow out of the fluid-conducting device (10) into the second tubing element; feeding the primary fluid into the primary conduits (14) such that the primary fluid flows through the primary conduits (14); feeding the secondary fluid into the primary conduits (14) via the at least one secondary conduit (16) such that mixing of the secondary fluid with the primary fluid is realized in the primary conduits (14).
13. The method for mixing as claimed in claim 12, wherein the fluid-conducting device (10) has multiple secondary conduits (16), and wherein the feeding-in of the secondary fluid is realized via one or more secondary conduits (16) of the multiple secondary conduits (16) independently of the other secondary conduits (16) of the multiple secondary conduits (16).
14. A method for producing a fluid-conducting device (10) as claimed in claim 1, comprising producing the fluid-conducting device (10) at least partially by an additive manufacturing process.
15. A method for producing a tube plate as claimed in claim 9 for a heat exchanger, comprising producing the tube plate at least partially by an additive manufacturing process.
Description
DESCRIPTION OF THE FIGURES
[0039]
[0040]
[0041]
[0042]
[0043]
[0044]
DETAILED DESCRIPTION OF THE DRAWINGS
[0045]
[0046] Multiple secondary conduits 16 extend in a plane perpendicular to the primary conduit direction 100 and open into the primary conduits 14. It is possible via the secondary conduits 16 for the secondary fluid to be injected into the primary conduits 14 in the secondary conduit direction 102 via the feed conduits 16a. Alternatively, and not constituting part of the invention, or additionally, it is possible via the secondary conduits 16 for one or more sensor elements 22 (see
[0047] Here, the flow direction of the secondary fluid in the secondary conduits 16 is intended to be applicable to the secondary conduit direction 102, although, in mathematical terms, said flow direction does not strictly extend in a direction.
[0048] According to the shown preferred embodiment of the fluid-conducting device 10, one secondary conduit 16 opens into each primary conduit 14, while each secondary conduit 16 opens into a plurality of primary conduits 14. Here, the secondary fluid can be fed in via one feed conduit 16a, or from both sides in temporal succession, or simultaneously, via both feed conduits 16a. The simultaneous feeding-in via both feed conduits 16a preferably ensures a relatively uniform feeding of the secondary fluid into each primary conduit, since all the flow paths of the secondary fluid thereby have similar lengths and thus similar pressure losses. It also offers the advantage that the secondary fluid can be fed in quicker, or with a higher flow rate, than if the secondary fluid is fed in only via one of the feed conduits 16a.
[0049] For example, the fluid-conducting device 10 may be formed in a tube plate and/or as a tube plate for a heat exchanger. Alternatively, the fluid-conducting device 10 may be used in a tube reactor, for example in a tube bundle reactor (not shown). A tube reactor can have multiple tubes, which preferably extend in a parallel manner and through which a process medium flows. For example, the process medium may be present as the primary fluid and conducted into the individual tubes of the tube reactor by means of the fluid-conducting device 10 or the primary conduits 14. The desired chemical conversions can then take place in the tubes. Heat emissions are often associated with chemical reactions. In order to operate the tube reactor in a reliable temperature range, the heat released in exothermic reactions must in some cases be removed and/or the heat to be absorbed in endothermic reactions must be provided. This may be realized for example by means of an exchange of heat via the tube walls. Furthermore, the tubes may frequently be filled with a catalyst bed. However, there are also non-catalytic reactions able to be carried out for which the tubes may be filled with inert beds and/or may remain empty.
[0050] If it is expected that the reaction will start immediately after the reaction partners are brought together, for example after the primary fluid is brought together with the secondary fluid, this may necessitate further safety measures. If, for example, the reaction occurs prior to the entry of the primary fluid into the reactor tube, no heat removal would be possible first of all, with the result that the reaction could overheat and/or progress in an uncontrolled manner. Also, undesirable secondary reactions as a result of non-catalytic reaction could be a problem here. These difficulties are avoided through the use of a tube reactor having a fluid-conducting device 10 according to the preferred embodiment, since the reaction partners are mixed at the latest possible time, specifically are not mixed until they are in the primary conduits 14 or in the conduit block 12. In this way, a tube reactor according to the invention according to the preferred embodiment permits very late mixing of the reaction partners, that is to say of the primary fluid with the secondary fluid, directly upon entry into the into the primary conduits 14 or into the reactor tubes.
[0051]
[0052]
[0053] Within the secondary conduit, the secondary fluid can flow in the secondary conduit direction 102, wherein a mouth of the secondary conduit 16 into the primary conduit 14 is formed such that the secondary conduit structure 18 has, at corresponding positions, outlet openings 20 from which the secondary fluid can exit the secondary conduit structure 18 in order to flow into the corresponding primary conduit 14. The flow of the secondary fluid from the outlet openings 20 into the respective primary conduits 14 may in this case be supported by a flow or a stream of the primary fluid in the primary conduit direction 14. In other words, a stream of the primary fluid in the primary conduit direction can help the secondary fluid exiting the outlet openings 20 of the secondary structure 18 to be drawn along into the primary conduits or entrained. For example, the secondary conduit structure 18 may have two opposite outlet openings 20 at the same height or at the same position along the secondary conduit direction 102, in order for example to feed secondary fluid into two adjacent primary conduits 14 (merely one primary conduit 14 being illustrated). It is alternatively possible for provision to be made of a branch from the secondary conduit 16, which branch directs the secondary fluid in the desired direction to the mouth of the primary conduit 14. The fluid-conducting device 10 may be used for example as a tube plate and/or in a tube plate for a heat exchanger.
[0054]
[0055] Furthermore, in the embodiment shown of the fluid-conducting device 10, connecting elements 12a are illustrated at the conduit block 12, by means of which it is possible for example for conduit tubes to be connected to the primary conduits 14. For example, it is possible via the connecting elements 12a for tubings 24, for example of a heat exchanger, to be connected to the conduit block 12 if the fluid-conducting device is used in a or as a tube plate for a heat exchanger. The connecting elements 12a may in this case also be formed integrally with the fluid-conducting device 10 or with the conduit block 12 and produced for example by means of an additive manufacturing process or 3D printing.
[0056]
[0057]
[0058] The static mixer 26 thus serves for mixing the primary fluid with the secondary fluid, wherein preferably the mixing is brought about solely by the flow movement of the primary fluid stream 110 and the secondary fluid stream 112. As a result of the primary conduits 14, the primary fluid stream 110 is divided, mixed with the secondary fluid stream 112 and then combined again into a mixed fluid stream 114.
[0059] The use of the fluid-conducting device 10 makes it possible in this way for very good mixing of the primary fluid with secondary fluid to be achieved, since the combining of the primary fluid stream 110 and the secondary fluid stream 112 is realized via a multiplicity of mouths or outlet openings 20 in the primary conduits 14, which are preferably distributed uniformly over the entire cross section of the flow tube 28. Moreover, according to the embodiment shown, preferably by way of the narrowing of the flow cross section from the tubing 28 to the primary conduits 14, an increased speed and/or turbulence of the primary fluid stream 110 is obtained, which contributes to the mixing. Furthermore, as a result of such a static mixer 26, preferably with the exiting of the mixed fluid stream 114 from the primary conduits 14 into the tubing 28 in the primary conduit direction 100, considerable swirling is obtained, which in turn has a positive effect on the mixing.
[0060] Furthermore, a static mixer 26 according to the preferred embodiment offers the advantage that at least the primary conduits 14 are able to be cleaned mechanically, and are thus also able to be used for fluids with a high fouling value without the risk of permanent attachment of impurities and/or blockage of the primary conduits 14.
REFERENCE SIGNS
[0061] 10 Fluid-conducting device [0062] 12 Conduit block [0063] 12a Connecting element [0064] 14 Primary conduit [0065] 16 Secondary conduit [0066] 16a Feed conduit [0067] 18 Secondary conduit structure [0068] 20 Outlet opening [0069] 22 Sensor element [0070] 22a Sensor head [0071] 24 Tubing [0072] 26 Static mixer [0073] 28 Tubing element [0074] 100 Primary conduit direction [0075] 102 Secondary conduit direction [0076] 110 Primary fluid stream [0077] 112 Secondary fluid stream [0078] 114 Mixed fluid stream