Abstract
An arrangement having an impeller that rotates about an axis and a stationary diffuser located downstream with guide vanes. The impeller has an inlet for an axial supply flow and an outlet for a radial out-flow, wherein radially and axially extending rotor blades are arranged between a wheel disc and a cover disc of the impeller. The impeller channels are separated from one another in a circumferential direction. The diffuser extends substantially radially along a main flow direction and has an axial channel width. The diffuser has a diffuser inlet and outlet, wherein guide vanes extending axially along a blade vertical direction and radially along a through-flow direction are arranged between the wheel disc side and the cover disc side of the diffuser, which separate the guide vane channels from one another. An inlet edge angle is smaller on the cover disc side than on the wheel disc side.
Claims
1. An arrangement through which a process fluid is able to flow along a main flow direction, comprising: an impeller which is rotatable about an axis in a direction of rotation, and an upright diffuser which is situated downstream of the impeller and is equipped with guide vanes, wherein the impeller has an inlet for axial inflow and has an outlet for radial outflow, wherein radially and axially extending rotor blades are arranged between a wheel disk and a cover disk of the impeller and delimit impeller channels with respect to one another in a circumferential direction, wherein the diffuser extends radially along a main flow direction, wherein the diffuser has an axial cover disk side and an axial wheel disk side, which delimit between them an axial channel width of the diffuser, wherein the diffuser has a diffuser inlet for radial inflow and has a diffuser outlet, wherein guide vanes extending axially along a vane height direction and radially along a throughflow direction are arranged between the wheel disk side and the cover disk side of the diffuser and delimit guide vane channels with respect to one another in a circumferential direction wherein, for each axial vane height, an inlet edge angle is defined as the angle between an inlet edge tangent to a mean line at an inlet edge of the respective guide vane and a circumferential tangent through the inlet edge, wherein the inlet edge angle is smaller on the cover disk side than on the wheel disk side, and wherein the guide vanes are designed such that an angle between a tangent to the mean line in a region of the inlet edge and a tangent to the mean line in an outlet edge region is smaller on the cover disk side than on the wheel disk side.
2. The arrangement as claimed in claim 1, wherein a difference between cover disk-side and wheel disk-side inlet edge angles is at least 5°.
3. The arrangement as claimed in claim 1, wherein an angle of attack of the guide vanes is smaller on the cover disk side than on the wheel disk side.
4. The arrangement as claimed in claim 3, wherein a difference between cover disk-side and wheel disk-side angles of attack of the guide vanes is at least 5°.
5. The arrangement as claimed in claim 1, wherein the quotient of axial channel width of the diffuser equipped with vanes and maximum impeller outlet diameter is greater than 0.04.
6. The arrangement as claimed in claim 1, wherein the quotient of axial channel width of the diffuser equipped with vanes and axial channel width of the impeller at the maximum impeller outlet diameter is less than 0.95.
7. The arrangement as claimed in claim 1, wherein the guide vanes are designed such that an angle between a tangent to the mean line in an inlet edge region and a profile chord is smaller on the cover disk side than on the wheel disk side.
8. The arrangement as claimed in claim 1, wherein the guide vanes have an inclination such that, on the cover disk side, the inlet edge, in relation to a wheel disk-side inlet edge, is offset in the direction of rotation of the impeller by at least 10% of the axial channel width of the diffuser.
9. The arrangement as claimed in claim 1, wherein the guide vanes are designed such that an offset counter to the direction of rotation of the impeller at the outlet edge from the cover disk side in relation to the wheel disk side is smaller than at the inlet edge.
10. The arrangement as claimed in claim 1, wherein an axial profile of the guide vanes of the diffuser from the cover disk side to the wheel disk side is of continuously curved form.
11. The arrangement as claimed in claim 1, wherein the impeller has such a three-dimensional configuration that, at least in that third of the extent of the rotor blades along the main flow direction which is furthest downstream, an axial projection of a cover disk-side rotor blade track and a wheel disk-side rotor blade track has at least a projection, from the cover disk-side rotor blade track to the wheel disk-side rotor blade track, of at least a surface area >5% in relation to the cover disk-side rotor blade track surface.
12. The arrangement as claimed in claim 1, wherein the diffuser has such a three-dimensional configuration that, at least in that third of the extent of the guide vanes along the main flow direction which is furthest upstream, an axial projection of a cover disk-side guide vane track and a wheel disk-side guide vane track has at least a projection, from the cover disk-side guide vane track to the wheel disk-side guide vane track, of at least a surface area >5% in relation to the cover disk-side guide vane track surface.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) The invention is illustrated in more detail below on the basis of a specific exemplary embodiment with reference to the drawings, in which:
(2) FIG. 1 shows a schematic longitudinal section through an arrangement according to the invention,
(3) FIG. 2 shows a schematic longitudinal section through an arrangement according to the invention in the form of a detail II as per FIG. 1,
(4) FIG. 3 shows a schematic cross section through an arrangement according to the invention,
(5) FIG. 4 shows a schematic cross section through an arrangement according to the invention with additional geometrical details, and
(6) FIG. 5 shows a schematic cross section through a diffuser of an arrangement according to the invention in the region of a single guide vane.
DETAILED DESCRIPTION OF INVENTION
(7) FIGS. 1 and 2 show, in a schematic illustration, longitudinal sections through an arrangement ARG according to the invention, wherein FIG. 2 shows a detail in FIG. 1 that is denoted by II. An arrangement ARG according to the invention is flowed through by a process fluid PFF from an inlet INL to an outlet EXT along a main flow direction MFD. The arrangement ARG comprises an impeller IMP which is rotatable about an axis X in the direction of rotation RTD. An upright diffuser DFF equipped with guide vanes VNE is situated downstream of the impeller IMP. The impeller IMP has an inlet INI for a substantially axial inflow and has an outlet EXI for a substantially radial outflow. The suitability for the substantially axial inflow and the substantially radial outflow of the impeller is characterized by the profile of the flow channel extending through the impeller and of the impeller channels ICH. Radially and axially extending rotor blades BLD are situated between a wheel disk HWI and a cover disk SWI of the impeller IMP. The rotor blade channels ICH are delimited with respect to one another in a circumferential direction CDR by said rotor blades BLD, as can be seen in FIGS. 3 and 4. The diffuser DFF extends with diffuser flow channels along a main flow direction MFD, which extends substantially radially. The diffuser DFF has an axial cover disk side SWS and an axial wheel disk side HWS. This nomenclature is based on the arrangement of the cover disk SWI and the wheel disk HWI of the impeller IMP. The axial cover disk side SWS and the axial wheel disk side HWS of the diffuser DFF delimit between them an axial channel width SAC of the diffuser DFF. The diffuser DFF has a diffuser inlet IND for a substantially radial inflow and has a diffuser outlet EXD.
(8) In FIG. 2, the diffuser is subdivided into three portions, into a first diffuser third TS1, a second diffuser third TS2 and a third diffuser third TS3, which extend along the main flow direction MFD. Guide vanes VNE extending axially along a vane height direction and radially along a throughflow direction extend between the wheel disk side HWS and the cover disk side SWS. The guide vanes VNE delimit individual guide vane channels HCN with respect to one another in a circumferential direction CDR.
(9) In FIGS. 3, 4 and 5, a cross section of the arrangement ARG according to the invention or of a detail thereof is shown in each case, so that it is also possible to see how the guide vane channels HCN are delimited with respect to one another in a circumferential direction CDR by means of the guide vanes VNE. Since the guide vanes VNE naturally do not have a completely straight profile along the main flow direction MFD, the delimitation of this type is also to be understood accordingly. The individual guide vanes VNE can be defined as a stack of vane profiles PRL (for example vane profile PRL as illustrated in FIG. 5) along the vane height. The vane height extends, as shown in FIGS. 1 and 2, parallel to the axis X, that is to say axially. The vane profiles PRL themselves are two-dimensional geometries which define the vane outer contour at a particular vane height position. The actual outer contour of the vanes on the respective suction side SCS and pressure side PRS is obtained as a surface interpolation between the linear delimitation contours of the vane profiles PRL, which each indicate a linear specification at the respective vane height position (also axial position in this case).
(10) FIG. 3 shows, in detail schematically in cross section, the arrangement ARG according to the invention having an impeller IMP and a diffuser DFF which adjoins downstream and which is designed as a stator STA. A radial clearance RCL of a radial gap is present between the impeller IMP and the diffuser DFF. In the illustration, the impeller IMP rotates counter to a circumferential direction CDR. The individual guide vanes VNE of the diffuser DFF are shown merely as schematic mean lines BWL. In this case, a mean line BWL describes a profile section or a profile of a vane at a particular height position in that the mean line BWL, also sometimes referred to as line of curvature, is a line defined by the center points of inscribed circles or circles tangent to the suction side and the pressure side of the profile. FIG. 5 shows in detail, on the basis of two circles CLC, by way of example, how the pressure side PRF and suction side SCS of a guide vane VNE define the mean line BWL by means of the inscribed circles CLC.
(11) In this case, FIG. 5 shows merely an axial section through the diffuser DFF in the region of a guide vane VNS, wherein the illustration applies both to the cover disk side SWS and to the wheel disk side HWS.
(12) FIG. 4 shows similar relationships in a combined view with the impeller IMP. There, the impeller IMP is divided into three portions of thirds which follow one another along the main flow direction MFD, more or less from a rotor blade inlet edge ILE to a rotor blade outlet edge ITE. In this case, the rotor blade inlet edge ILE and the rotor blade outlet edge ITE are not necessarily identical to the inlet INI of the impeller and the outlet XEI of the impeller, respectively. The main flow direction MFD extends axially in the impeller IMP too—that is to say also into the plane of the drawing in FIG. 4. The information about the axial extent is naturally lost in the axial projection of the rotor blades BLD in FIG. 4. The impeller has a first impeller portion IS1, a second impeller portion IS2 and a third impeller portion IS3. By contrast to FIG. 5, FIG. 4 shows, with dashed lines in each case, the cover disk side SWS and the wheel disk side HWS both for a rotor blade BLD and for a guide vane VNE.
(13) It can be seen in particular in FIG. 5 that, for each axial vane, an inlet edge angle LEA is defined as the angle between an inlet edge tangent TLV of the respective guide vane VNE and a circumferential tangent CTG through the inlet edge DLE. In this case, the inlet edge angle LEA is measured in the mathematically positive sense from the circumferential tangent CTG to the inlet edge tangent TLV. The circumferential tangent CTG is a tangent in the circumferential direction at the respective indicated position, at the position of the inlet edge DLE in this case. Said circumferential tangent CTG can also be defined as being perpendicular to a radial RAD and the reference point, comprising the inlet edge DLE in this case.
(14) FIGS. 4 and 5 also each show the profile chord VCH of the profile of the guide vane VNE in the respective section, said profile chord extending as a straight line from an inlet edge DLE to an outlet edge DTE. In a manner similar to that for the inlet edge angle LEA, based on the profile chord VCH, the angle of attack AOA is also defined as a mathematically positively measured angle from the circumferential tangent CTG to the profile chord VCH.
(15) FIG. 4 shows these relationships for the cover disk side SWS and the wheel disk side HWS of the diffuser DFF. The arrangement ARG provides that, for the diffuser DFF, the inlet edge angle LEA is smaller on the cover disk side than on the wheel disk side. Advantageously, the difference between the cover disk-side and wheel disk-side inlet edge angles LEA is at least 5 degrees.
(16) As also illustrated in FIG. 2, the quotient of axial channel width SAC of the diffuser DFF equipped with vanes and maximum impeller outlet diameter is greater than 0.04. It can likewise be seen in FIG. 2 that the quotient of axial channel width SAC of the diffuser equipped with vanes and axial channel width IAC of the impeller IMP at the maximum impeller outlet diameter DIE is less than 0.95. Particularly, as also illustrated in FIG. 5, the guide vane VNE is designed such that an angle, referred to as profile angle of curvature VBA in this case, between a tangent TLV to the mean line BWL in the inlet edge region and a tangent TTV to the mean line BWL in the outlet edge region TEA is smaller on the cover disk side than on the wheel disk side. The angle of curvature VBA is in this case also again measured in the mathematically positive sense, proceeding from the tangent TLV to the mean line BWL in the inlet edge region.
(17) Also illustrated in FIG. 5 is an advantageous configuration of the invention such that an angle between the tangent TLV to the mean line BWL in the inlet edge region and the profile chord VCH is smaller on the cover disk side than on the wheel disk side, wherein the angle is referred to here as the inlet angle of attack VTC. It should be noted that FIG. 5 shows the relationships on the wheel disk side HWS or cover disk side SWS in a fundamentally schematic manner and accordingly represents both sides.
(18) The illustration with superimposed profile sections in FIG. 4 becomes unclear when all of these geometrical relationships are marked.
(19) An inlet edge DLE of the guide vanes VNE may advantageously, as illustrated in FIG. 4, be slightly radially offset downstream in relation to the inlet of the diffuser DFF, wherein this radial offset is indicated as CBS in FIG. 4.
(20) FIG. 4 schematically shows the relationship whereby the guide vanes VNE have an inclination such that, on the cover disk side, the inlet edge VLE, in relation to the wheel disk-side inlet edge VLE, is offset counter to the direction of rotation RTD of the impeller IMP by at least 10% of the axial channel width SAC of the diffuser DFF. In this context, it is also expedient, as illustrated in FIG. 4, for the guide vanes VNE to be designed such that an offset counter to the direction of rotation RTD of the impeller IMP at the outlet edge DTE from the cover disk side SWS in relation to the wheel disk side HWS is smaller than at the inlet edge VLE. The axial profile of the guide vanes of the diffuser DFF from the cover disk side SWS to the wheel disk side HWS is of continuously curved form.
