DEVICE AND METHOD FOR HEATING A FLUID IN A PIPELINE WITH SINGLE-PHASE ALTERNATING CURRENT
20230098601 · 2023-03-30
Inventors
- Andrey Shustov (Ludwigshafen am Rhein, DE)
- Sric JENNE (Ludwigshafen an Rhein, DE)
- Kiara Aenne KOCHENDOERFER (Ludwigshafen an Rhein, DE)
Cpc classification
H05B2203/005
ELECTRICITY
H05B2203/022
ELECTRICITY
International classification
Abstract
An apparatus (100) for heating a fluid is proposed. The apparatus comprises at least one electrically conductive pipeline (112) and/or at least one electrically conductive pipeline segment (114) for receiving the fluid, and at least one single-phase AC power source and/or at least one single-phase AC voltage source (126), each pipeline (112) and/or each pipeline segment (114) being assigned a sin-gle-phase AC power source and/or a single-phase AC voltage source (126) which is connected to the respective pipeline (112) and/or to the respective pipeline segment (114), the respective single-phase AC power source and/or single-phase AC voltage source (126) being designed to generate an electrical current in the respective pipeline (112) and/or in the respective pipeline segment (114), which warms up the respective pipeline (112) and/or the respective pipeline segment (114) by Joulean heat, which is produced when the electrical current passes through conducting pipe material, for heating the fluid, the single-phase AC power source and/or the single-phase AC voltage source (126) being connected to the pipeline (112) and/or the pipeline segment (114) in an electrically conducting manner in such a way that the alternating current generated flows into the pipeline (112) and/or the pipeline segment (114) via a forward conductor (128) and flows back to the AC power source and/or AC voltage source (126) via a return conductor (130).
Claims
1.-14. (canceled)
15. An apparatus (110) for heating a fluid comprising at least one electrically conductive pipeline (112) and/or at least one electrically conductive pipeline segment (114) for receiving the fluid, and at least one single-phase AC power source and/or at least one single-phase AC voltage source (126), each pipeline (112) and/or each pipeline segment (114) being assigned a single-phase AC power source and/or a single-phase AC voltage source (126) which is connected to the respective pipeline (112) and/or to the respective pipeline segment (114), the respective single-phase AC power source and/or single-phase AC voltage source (126) being designed to generate an electrical current in the respective pipeline (112) and/or in the respective pipeline segment (114), which warms up the respective pipeline (112) and/or the respective pipeline segment (114) by Joulean heat, which is produced when the electrical current passes through conducting pipe material, for heating the fluid, the single-phase AC power source and/or the single-phase AC voltage source (126) being connected to the pipeline (112) and/or the pipeline segment (114) in an electrically conducting manner in such a way that the alternating current generated flows into the pipeline (112) and/or the pipeline segment (114) via a forward conductor (128) and flows back to the AC power source and/or AC voltage source (126) via a return conductor (130), the apparatus (110) comprising a plurality of pipelines (112) and/or pipeline segments (114), the pipelines (112) and/or pipeline segments (114) being through-connected and thus forming a pipe system for receiving the fluid, the pipelines (112) and/or pipeline segments (114) and correspondingly incoming and outgoing pipelines being connected to one another in a fluid-conducting manner, the pipelines (112) and/or pipe segments (114) and the incoming and outgoing pipelines (112) being galvanically separated from one another.
16. The apparatus (110) according to claim 15, wherein the apparatus (110) comprises L pipelines (112) and/or pipeline segments (114), where L is a natural number greater than or equal to two, the pipelines (112) and/or pipeline segments (114) comprising symmetrical or asymmetrical pipes and/or a combination thereof.
17. The apparatus (110) according to claim 15, wherein the apparatus (110) comprises isolators (124) which are designed for galvanic separation between the respective pipelines (112) and/or pipeline segments (114) and the incoming and outgoing pipelines, the isolators (124) being designed to ensure a free through-flow of the fluid.
18. The apparatus (110) according to claim 15, wherein a number or all of the pipelines (112) and/or pipeline segments (112) are configured in series and/or in parallel.
19. The apparatus (110) according to claim 15, wherein the apparatus (110) comprises a plurality of single-phase AC power or single-phase AC voltage sources (126), the single-phase AC power and/or single-phase AC voltage sources (126) being configured with or without the possibility of controlling at least one electrical output variable.
20. The apparatus (110) according to claim 19, wherein, to connect the single-phase AC power or single-phase AC voltage sources (126) and the respective pipelines (112) and/or with the respective pipeline segments (114), the apparatus (110) comprises 2 to N forward conductors (128) and 2 to N return conductors (130), where N is a natural number greater than or equal to three.
21. The apparatus (110) according to claim 19, wherein the respective single-phase AC power or single-phase AC voltage sources (126) are configured identically or differently.
22. The apparatus (110) according to claim 21, wherein the apparatus (110) comprises 2 to M different single-phase AC power and/or single-phase AC voltage sources (126), where M is a natural number greater than or equal to three, the single-phase AC power and/or single-phase AC voltage sources (126) being electrically controllable independently of one another.
23. An installation comprising at least one apparatus (110) according to claim 15.
24. The installation according to claim 23, wherein the installation is selected from the group consisting of: a steam cracker, a steam reformer, a device for alkane dehydrogenation, a device for dry reforming.
25. A method for heating a fluid by using an apparatus (110) according to claim 15 relating to an apparatus, the method comprising the following steps: providing at least one electrically conductive pipeline (112) and/or at least one electrically conductive pipeline segment (114) for receiving the fluid; receiving the fluid in the pipeline (112) and/or the pipeline segment (114); providing at least one single-phase AC power source and/or at least one single-phase AC voltage source (126), each pipeline (112) and/or each pipeline segment (114) being assigned a single-phase AC power source and/or a single-phase AC voltage source (126) which is connected to the respective pipeline (112) and/or to the respective pipeline segment (114), generating by the respective single-phase AC power source and/or single-phase AC voltage source (126) an electrical current in the respective pipeline (112) and/or in the respective pipeline segment (114), which warms up the respective pipeline (112) and/or the respective pipeline segment (114) by Joulean heat, which is produced when the electrical current passes through conducting pipe material, for heating the fluid, the single-phase AC power source and/or the single-phase AC voltage source (126) being connected to the pipeline (112) and/or the pipeline segment (114) in an electrically conducting manner in such a way that the alternating current generated flows into the pipeline (112) and/or the pipeline segment (114) via a forward conductor (128) and flows back to the AC power source and/or AC voltage source (126) via a return conductor (130).
26. The method according to claim 25, wherein, as the fluid, a hydrocarbon to be thermally cracked, is heated.
27. The method according to claim 15 relating to a method, wherein, as the fluid, water or steam is heated, with said water or said steam being heated in particular to a temperature in the range of 550° C. to 700° C., and the fluid additionally comprising a hydrocarbon to be thermally cracked, in particular a mixture of hydrocarbons to be thermally cracked, the fluid to be heated being a preheated mixture of hydrocarbons to be thermally cracked and steam.
28. The method according to claim 15 relating to a method, wherein, as the fluid, combustion air of a reformer furnace is preheated, for example to a temperature in the range of 200° C. to 800° C., preferably 400° C. to 700° C.
Description
BRIEF DESCRIPTION OF THE FIGURES
[0078] Further details and features of the invention may be found in the following description of preferred examples, in particular in conjunction with the subclaims. The respective features may be implemented separately, or several of them may be implemented in combination with one another. The invention is not restricted to the examples. The examples are diagrammat-ically represented in the figures. References which are the same in the individual figures de-note elements which are the same or have the same function, i.e. they correspond to one another in respect of their functions.
[0079] Specifically:
[0080]
[0081]
[0082]
[0083]
[0084]
[0085]
[0086]
[0087]
EXAMPLES
[0088]
[0089] For example, the apparatus 110 may be part of an installation. For example, the installation may be selected from the group consisting of: a steam cracker, a steam reformer, a device for alkane dehydrogenation, a device for dry reforming. For example, the apparatus 110 may be designed for carrying out at least one process selected from the group consisting of steam cracking, steam reforming, alkane dehydrogenation, dry reforming. The apparatus 110 may for example be part of a steam cracker. The steam cracker may be designed for warming up the fluid to a temperature in the range of 550° C. to 1100° C. For example, the apparatus 110 may be part of a reformer furnace. For example, the fluid may be a combustion air of a reformer furnace which is prewarmed or heated up, for example to a temperature in the range of 200° C. to 800° C., preferably of 400° C. to 700° C. For example, the apparatus 110 may be part of a device for alkane dehydrogenation. The device for alkane dehydrogenation may be designed to warm up the fluid to a temperature in the range of 400° C. to 700° C. However, other temperatures and temperature ranges are also conceivable.
[0090] The pipeline 112 and/or the pipeline segment 114 may be designed to receive and transport the fluid. The pipeline 112 and/or the pipeline segment 114 may comprise at least one leg or a turn. The pipeline 112 may comprise at least one symmetrical pipe and/or at least one asymmetrical pipe.
[0091]
[0092] The pipelines 112 and/or pipeline segments 114 and correspondingly incoming and outgoing pipelines may be connected to one another in a fluid-conducting manner, while the pipelines 112 and/or pipeline segments 114 and the incoming and outgoing pipelines may be galvanically separated from one another. The apparatus 110 may comprise at least one galvanic separation, in particular at least one isolator 124, in particular a plurality of isolators 124. The galvanic separation between the respective pipelines 112 and/or pipeline segments 114 and the incoming and outgoing pipelines can be ensured by the isolators 124. The isolators 124 can ensure a free flow of the fluid.
[0093] The apparatus 110 has at least one single-phase AC power source and/or at least one single-phase AC voltage source 126. For example, the alternating current may be a sinusoidal alternating current. The single-phase AC power source and/or at least one single-phase AC voltage source 126 may be designed to provide an electrical current with a single phase.
[0094] The apparatus 110 has a forward conductor 128. The forward conductor 128 may be designed to conduct the alternating current generated to the pipeline 112 and/or the pipeline segment 114. The forward conductor 128 may be designed to apply the alternating current to the pipeline 112 and/or the pipeline segment 114 and/or to provide the alternating current for the pipeline 112 and/or for the pipeline segment 114. The forward conductor 128 may be designed to conduct the alternating current generated to the pipeline 112 and/or the pipeline segment 114 in such a way that the alternating current generated flows into the pipeline 112 and/or the pipeline segment 114 via the forward conductor 128. The forward conductor 128 may be a feeder.
[0095] The AC power source and/or the AC voltage source 126 are designed to generate an alternating current in the respective pipeline 112 and/or the respective pipeline segment 114. The alternating current generated can warm up the respective pipeline 112 and/or the respective pipeline segment 114 by Joulean heat, which is produced when the electrical current passes through conducting pipe material, for heating the fluid. Warming up the pipeline 112 and/or the pipeline segment 114 may comprise a change in a temperature of the pipeline 112 and/or the pipeline segment 114, in particular a rise in the temperature of the pipeline 112 and/or the pipeline segment 114.
[0096] The AC power source and/or AC voltage source 126 is connected to the pipeline 112 and/or the pipeline segment 114 in an electrically conducting manner in such a way that the alternating current generated flows into the pipeline 112 and/or the pipeline segment 114 via the forward conductor 128 and flows back to the AC power source and/or AC voltage source 126 via a return conductor 130. The return conductor 130 may be designed to carry away the alternating current after it has flowed through the pipeline 112 and/or the pipeline segment 114, in particular to the AC power source and/or AC voltage source 126.
[0097] The apparatus may comprise a plurality of single-phase AC power or single-phase AC voltage sources 126, for example three, as shown by way of example in
[0098] Each of the pipelines 112 and/or for each pipeline segment 114 can be assigned an AC power source and/or AC voltage source 126, which is connected to the respective pipeline 112 and/or to the respective pipeline segment 114, in particular electrically via at least one electrical connection.
[0099] To connect the single-phase AC or single-phase AC voltage sources 126 and the respective pipelines 112 and/or to the respective pipeline segments 114, the apparatus 110 can have two to N forward conductors 128 and two to N return conductors 130, where N is a natural number greater than or equal to three. The respective single-phase AC power source and/or AC voltage source 126 may be designed to generate an electrical current in the respective pipeline 112 and/or in the respective pipeline segment 114.
[0100] The AC power and/or AC voltage sources 126 may be either controlled or uncontrolled. The AC power and/or AC voltage sources 126 may be configured with or without the possibility of controlling at least one electrical output variable. For example, the apparatus may comprise at least one controller 127. The controller may be for example an external controller, that is to say a controller 127 arranged outside the reaction space. The apparatus 110 may comprise 2 to M different AC power and/or AC voltage sources 126, where M is a natural number greater than or equal to three. The AC power and/or AC voltage sources 126 may be electrically controllable independently of one another. For example, a different current may be generated in the respective pipelines 112 and/or in the respective pipeline segments 114 and different temperatures reached in the pipelines 112 and/or pipeline segments 114.
[0101]
[0102]
[0103]
[0104] In the examples of
[0105]
[0106] The apparatus 110 can have symmetrical and/or asymmetrical pipes and/or combinations thereof. In a purely symmetrical configuration, the apparatus 110 can have pipelines 112 and/or pipeline segments 114 of an identical type of pipe. The apparatus 110 can have any combination of types of pipe, which may for example also be connected as desired in parallel or in series. The type of pipe may be characterized at least by one feature selected from the group consisting of: a horizontal configuration of the pipeline 112 and/or the pipeline segment 114; a vertical configuration of the pipeline 112 and/or the pipeline segment 114; a length in the inlet (L1) and/or outlet (L2) and/or transition (L3); a diameter in the inlet (d1) and outlet (d2) and/or transition (d3); the number n of passes; the length per pass; the diameter per pass; the geometry; the surface; and the material. Alternatively or additionally, the type of pipe may be selected from at least one pipeline 112 and/or at least one pipeline segment 114 with or without galvanic separation and/or grounding 125. The galvanic separation may for example be configured using an isolator 124. For example, a galvanic separation may be provided at the inlet 120 of the pipeline 112 and/or the pipe segment 114 and a galvanic separation may be provided at the outlet 122 of the pipeline 112 and/or the pipe segment 114. For example, a galvanic separation may be provided at the inlet 120 of the pipeline 112 and/or the pipe segment 114 and a grounding 125 may be provided at the outlet 122 of the pipeline 112 and/or the pipe segment 114. For example, a galvanic separation may only be provided at the inlet 120 of the pipeline 112 and/or of the pipe segment 114. For example, a grounding 125 may only be provided at the inlet 120 of the pipeline 112 and/or of the pipe segment 114. For example, the pipeline 112 and/or the pipe segment 114 may be provided without grounding 125 at inlet 120 and outlet 122 and/or without galvanic separation at inlet 120 and outlet 122. Alternatively or additionally, the type of pipe may be characterized by a direction of flow of the fluid. The fluid can in principle flow in two directions of flow, referred to as the first and second directions of flow. The first and second directions of flow can be opposite.
[0107] Alternatively or additionally, the type of pipe may be characterized by the application of alternating current to the pipeline 112 and/or the pipeline segment 114. For example, a forward conductor 128 may be connected midway along the pipeline 112 and/or the pipe segment 114. The return conductors 130 may be connected to the beginnings or ends of the pipeline 112 and/or the pipe segment 114. For example, the forward conductor 128 may be connected at the beginning of the pipeline 112 and/or the pipe segment 114 and the return conductor 130 at the end of the pipeline 112 and/or the pipe segment 114.
[0108] Any combination of the types of pipe is possible.
[0109]
[0116] In
[0117] In FIG. 7Aiv, type of pipe A1D4F2, the apparatus 110 has in comparison with FIG. 7Aiii only a grounding 125 instead of the isolator. Embodiments without isolators 124 or groundings 125 are also possible, as shown in
[0118] In
[0119]
[0120] The apparatus 110 may comprise a combination of at least two different types of pipe which are connected in parallel and/or in series. For example, the apparatus 110 may comprise pipelines 112 and/or pipeline segments 114 of different lengths in the inlet (L1) and/or outlet (L2) and/or transition (L3). For example, the apparatus may comprise pipelines and/or pipeline segments with an asymmetry of the diameters in the inlet (d1) and/or outlet (d2) and/or transition (d3). For example, the apparatus 110 may comprise pipelines 112 and/or pipeline segments 114 with a different number of passes. For example, the apparatus 110 may comprise pipelines 112 and/or pipeline segments 114 with passes with different lengths per pass and/or different diameters per pass.
[0121] In principle, any combinations of all types of pipe in parallel and/or in series are possible. Pipelines 112 and/or pipeline segments 114 can be present in various types of pipe in the form of a construction kit 138 and may be selected and combined as desired, dependent on an intended use.
[0122]
[0123] By using pipelines 112 and/or pipeline segments 114 of different types of pipe, more accurate temperature control and/or an adaptation of the reaction when there is a fluctuating feed and/or a selective yield of the reaction and/or an optimized process technology can be made possible.
LIST OF REFERENCE SIGNS
[0124] 110 Apparatus [0125] 111 Reactive space [0126] 112 Pipeline [0127] 114 Pipeline segment [0128] 118 Pipe system [0129] 120 Inlet [0130] 122 Outlet [0131] 124 Isolator [0132] 125 Grounding [0133] 126 Single-phase AC power source and/or AC voltage source [0134] 127 Controller [0135] 128 Forward conductor [0136] 130 Return conductor [0137] 132 Heating wire [0138] 134 First pipeline [0139] 136 Second pipeline [0140] 138 Construction kit