Patent Application
20170038149
The invention relates to a heat exchanger.
A heat exchanger generally has a pressure-bearing casing, which surrounds a casing chamber for accommodating a first fluid and which extends along a longitudinal axis The heat exchanger may include a core tube, which runs in the casing and which extends along the longitudinal axis wherein for most heat exchanger designs, the core tube extends vertically. The heat exchanger also has a tube bundle which is arranged in the casing chamber and which has multiple tubes to accommodate a second fluid (or multiple fluids). The tubes of the tube bundle are helically coiled around the longitudinal axis or the core tube) in a coil region, extending from a lower coil end to an upper coil end.
The heat exchangers of this type known from the prior art, include tubes and tube flows that are coiled over the entire bundle length, i.e. along the entire coil region. This results in tube flows for all of the tubes in the bundle that have approximately the same temperature at the beginning of the bundle and also at the end of the bundle.
Therefore, if it is desired that one or more tube flows have a temperature at the inlet or outlet which lies between the bundle inlet temperature and the bundle outlet temperature, then the bundle must be divided into at least two bundles. The separation of the bundles is realized at planes where the desired temperature prevails. When a tube bundle is divided or separated in this way, two separate, relatively short bundles are created. The portion of the second fluid which has not yet reached its predefined final temperature is conducted from one bundle to the other separate bundle, for example by a connecting tube line. The portion of the second fluid which has reached its defined final temperature at the separation point is extracted from the heat exchanger at the separation point. Alternatively, the individual bundles may be installed in separate heat exchangers.
The present invention provides a new design for a heat exchanger where it is desired to produce fluids at more than one temperature. The present invention provides a relatively simple design.
The heat exchanger of the invention has at least one tube which is coiled around the longitudinal axis (or the core tube when in place) in only a section of the coil region. Below this section, the at least one tube runs as a straight tube to the lower coil end. Alternatively, above this section, the at least one tube runs as a straight tube to the upper coil end. In another alternative, the at least one tube runs as a straight tube both above and below the coiled section to the respective lower coil end and upper coil end.
The tubes of the tube bundle of the helically coiled heat exchanger of the invention may be coiled around the core tube so that the core tube bears the load of the tubes of the tube bundle. The tubes of the tube bundle may be coiled in multiple layers around the core tube, with spacers provided between the individual layers.
The tube bundle may also have multiple tube groups, wherein the tubes of a tube group have a common inlet and outlet, such that the tubes of a tube group can be supplied with a fluid flow which is distributed among the individual tubes of the tube group.
By having the at least one tube, helically coiled for only a section of the longitudinal axis (or core tube) as noted above, the heat exchange occurs substantially only in that section. Below and above the section, where the tube runs as a straight tube there is very little heat exchange as compared to the coiled portion. The coiled and straight tube sections may be formed integrally or may be connected in some other way.
According to the invention, the tube bundles of the heat exchanger do not have to be divided. Rather, the at least one tube is coiled only in the stated section where the desired temperature prevails. Before and after the coiled section, the at least one tube extends as a straight tube to the respective coil end and does not significantly participate in the exchange of heat The heat exchange that occurs in the straight tube portions is negligible as compared to the coiled portion.
A straight profile of a tube or tube section is generally defined to mean a linear profile of the tube or tube section. However, the invention also includes tubes or tube sections that have some curvature but wherein that tube section participates to a significantly lesser extent in the exchange of heat as compared to the coiled section. For example, a profile for the tube section according to the invention is realized if the respective tube section extends along or parallel to the longitudinal axis or is coiled around the core tube extending around the longitudinal axis of the heat exchanger by less than 180°.
According to the invention, the coiled section of the tube is selected and positioned along the longitudinal axis (or core tube), such that during operation of the heat exchanger, the desired intermediate temperature prevails in the coiled section. This desired temperature is lower than the temperature prevailing at the lower coil end and higher than a temperature prevailing at the upper coil end.
The heat exchanger of the invention may include multiple tubes which are coiled only around a section of the longitudinal axis or the core tube, and then extend as straight tubes below the coiled portion to the lower coil end, or above the coiled portion to the upper coil end, or both below and above the coiled portion. The multiple tubes may be coiled in multiple layers around the core tube.
In addition, multiple tubes of a tube bundle may be coiled in multiple layers around the longitudinal axis or around the core tube.
The heat exchanger according to the invention may be used for realizing an indirect exchange of heat between a refrigerant flow, as the first fluid, and a hydrocarbon-containing flow, as the second fluid, wherein, the hydrocarbon-containing flow may be natural gas. The heat exchanger according to the invention may be used for all types of fluid flows.
Further details and advantages of the invention will be discussed with reference to the drawing figures.
The tube sections 200a, 200b may be formed integrally with the coiled portion in section A or may be connected in to the coiled section in some other way.
The heat exchanger shown in
The heat exchanger 1 is designed for the indirect exchange of heat between a first fluid and a second fluid. The heat exchanger 1 has a casing 10 which surrounds a casing chamber M for accommodating the first fluid. The first fluid can be introduced into the casing chamber M via an inlet connector 101 on the casing 10 and can be extracted from the casing chamber M via an outlet connector 102 on the casing 10,
The casing 10 extends along the longitudinal axis L in a vertical direction. The tube bundle 2 is also arranged in the casing chamber M, the tube bundle 2 having a multiplicity of tubes 20 for accommodating the second fluid. The tubes 20, in a coil region W which extends along the longitudinal axis L from a lower coil end E to an upper coil end E′, may be helically coiled in multiple layers 22 around a core tube 21. The core tube 21 also extends along the longitudinal axis L and is arranged concentrically in the casing chamber M. Multiple tubes 20 of the tube bundle 2 may each form a tube group (three such tube groups are shown in
As shown in
The tube bundle 2, and the associated fluid flow, has an input temperature TE, at the lower coil end E and has an output temperature TE′ at the upper coil end E′.
Below the section A or above the section A or both below and above the section A, the at least one tube 200 has tube sections 200a and 200b which run in substantially straight or linear fashion to the lower coil end E and the upper coil end E′ respectively and then to an associated inlet connector 103 or outlet connector 105 respectively.
The desired temperature TA prevails at the lower transition from the tube section 200a to the section A and the desired temperature TA′ prevails at the upper transition from the section A to the tube section 200b. Since the tube sections 200a and 200b do not significantly participate in the exchange of heat, a temperature similar to the temperature TA prevails at the end of the tube section 200a or the coil end E, and a temperature similar to temperature TA′ prevails at the end of the tube section 200b or the coil end E′.
The casing 10 and the core tube 21 may be of cylindrical form at least in sections, such that the longitudinal axis L forms a cylinder axis of the casing 10 and of the core tube 21 which runs concentrically therein. In the casing chamber M a barrel 3 may be arranged which surrounds the tube bundle 2 or at least one tube 200, such that, between the tube bundle 2 and the barrel 3, there is formed an intermediate chamber 4 which surrounds the tube bundle 2 or tube 200. The barrel 3 serves to prevent the first fluid in the casing chamber M from bypassing the tube bundle 2 and tube 200. The first fluid is thus guided in the casing chamber M especially in the region of the casing chamber M which is surrounded by the barrel 3.
The individual tube layers 22 may (in particular in the case of horizontal mounting of the tube bundle 2) be supported on one another or on the core tube 21 using spacer elements 6 that extend along the longitudinal axis L. Multiple spacer elements 6 may be arranged one above the other in a radial direction R of the tube bundle 2.
| Number | Date | Country | Kind |
|---|---|---|---|
| 15002356.2 | Aug 2015 | EP | regional |
