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A Rankine cycle apparatus includes a pump, an evaporator, an expander, and a condenser. The evaporator has a plurality of heat transfer tubes arranged in rows in a flow direction of a high-temperature fluid to be heat-exchanged with a working fluid. The heat transfer tube located in a most upstream

A Rankine cycle apparatus includes a pump, an evaporator, an expander, and a condenser. The evaporator has a plurality of heat transfer tubes arranged in rows in a flow direction of a high-temperature fluid to be heat-exchanged with a working fluid. The heat transfer tube located in a most upstream row in the flow direction of the high-temperature fluid is defined as a most upstream heat transfer tube. For example, the most upstream heat transfer tube forms an inlet of the evaporator so that the working fluid flows into the evaporator through the inlet and first passes through the most upstream heat transfer tube.

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1. A Rankine cycle apparatus comprising: a pump that pressurizes a working fluid;an evaporator that heats the working fluid discharged from the pump;an expander that expands the working fluid heated in the evaporator; anda condenser that cools the working fluid discharged from the expander, whereint

1. A Rankine cycle apparatus comprising: a pump that pressurizes a working fluid;an evaporator that heats the working fluid discharged from the pump;an expander that expands the working fluid heated in the evaporator; anda condenser that cools the working fluid discharged from the expander, whereinthe evaporator comprises a plurality of heat transfer tubes arranged in rows in a flow direction of a high-temperature fluid to be heat-exchanged with the working fluid,when the heat transfer tube located in a most upstream row in the flow direction of the high-temperature fluid is defined as a most upstream heat transfer tube, the following requirement (A), or (B) is satisfied:(A) the rows comprise a first section and a second section, the first section including the most upstream heat transfer tube, and the second section including the heat transfer tubes other than the most upstream heat transfer tube so that the second section accepts the working fluid having passed through the first section and allows the working fluid to exchange heat with the high-temperature fluid in a counter-flow manner; and(B) the rows comprise a first section and a second section, the first section being composed of rows adjacent to each other and including the most upstream heat transfer tube in one of the rows and the heat transfer tube forming an inlet of the evaporator in a row other than the row of the most upstream heat transfer tube, and the second section being located downstream of the first section in the flow direction of the high-temperature fluid and accepting the working fluid having passed through the first section,the working fluid has a thermal decomposition temperature lower than a temperature of the high-temperature fluid flowing on an outer peripheral surface of the most upstream heat transfer tube and is in a liquid phase or in a gas-liquid two phase when flowing in the most upstream heat transfer tubethe evaporator is a fin tube heat exchanger comprising a fin and further comprises a heat insulating structure that prevents heat transfer between the first section and the second section,the first section and the second section share the fin, andthe heat insulating structure comprises a through hole formed in the fin at a boundary between the first section and the second section. 2. The Rankine cycle apparatus according to claim 1, wherein the requirement (B) is satisfied, andat least a portion of the first section is configured to allow the working fluid and the high-temperature fluid to exchange heat with each other in a counter-flow manner. 3. The Rankine cycle apparatus according to claim 2, wherein the second section is composed of rows adjacent to each other and is configured to allow the working fluid and the high-temperature fluid to exchange heat with each other in a parallel-flow manner in the heat transfer tubes located in at least two of the adjacent rows. 4. The Rankine cycle apparatus according to claim 2, wherein the second section is composed of rows adjacent to each other and is configured to allow the working fluid and the high-temperature fluid to exchange heat with each other in a counter-flow manner in the heat transfer tubes located in at least two of the adjacent rows. 5. The Rankine cycle apparatus according to claim 1, wherein the requirement (A) is satisfied. 6. The Rankine cycle apparatus according to claim 5, wherein the most upstream heat transfer tube forms an inlet of the evaporator so that the working fluid flows into the evaporator through the inlet and first passes through the most upstream heat transfer tube. 7. The Rankine cycle apparatus according to claim 1, wherein a member constituting the first section is spaced from a member constituting the second section. 8. The Rankine cycle apparatus according to claim 1, wherein the first section includes nothing but the heat transfer tube or the heat transfer tubes, andthe second section has a structure of a fin tube heat exchanger. 9. The Rankine cycle apparatus according to claim 1, wherein the number of rows in the second section is larger than the number of rows in the first section. 10. The Rankine cycle apparatus according to claim 1, wherein an outer diameter of the heat transfer tube included in the first section is larger than an outer diameter of the heat transfer tube included in the second section. 11. The Rankine cycle apparatus according to claim 1, wherein the most upstream heat transfer tube is an internally smooth tube. 12. The Rankine cycle apparatus according to claim 1, wherein the evaporator is a fin tube heat exchanger comprising a fin, andthe fin is a flat fin without a cut-and-raised portion. 13. The Rankine cycle apparatus according to claim 1, wherein the most upstream heat transfer tube is offset in the flow direction of the high-temperature fluid. 14. A combined heat and power system comprising: the Rankin cycle apparatus according to claim 1; anda heat medium circuit in which a heat medium flows, the heat medium serving as a low-temperature heat source for cooling the working fluid in the condenser of the Rankine cycle apparatus. 15. The Rankine cycle apparatus according to claim 1, wherein the first section includes only the most upstream heat transfer tube,the most upstream heat transfer tube is an internally smooth tube, andeach of the heat transfer tubes in the second section is an internally grooved tube. 16. An evaporator for use in a Rankine cycle, comprising a plurality of heat transfer tubes arranged in rows in a flow direction of a high-temperature fluid to be heat-exchanged with a working fluid in the Rankine cycle, wherein when the heat transfer tube located in a most upstream row in the flow direction of the high-temperature fluid is defined as a most upstream heat transfer tube, the following requirement (A), or (B) is satisfied:(A) the rows comprise a first section and a second section, the first section including the most upstream heat transfer tube, and the second section including the heat transfer tubes other than the most upstream heat transfer tube so that the second section accepts the working fluid having passed through the first section and allows the working fluid to exchange heat with the high-temperature fluid in a counter-flow manner; and(B) the rows comprise a first section and a second section, the first section being composed of rows adjacent to each other and including the most upstream heat transfer tube in one of the rows and the heat transfer tube forming an inlet of the evaporator in a row other than the row of the most upstream heat transfer tube, and the second section being located downstream of the first section in the flow direction of the high-temperature fluid and accepting the working fluid having passed through the first section,the working fluid has a thermal decomposition temperature lower than a temperature of the high-temperature fluid flowing on an outer peripheral surface of the most upstream heat transfer tube and is in a liquid phase or in a gas-liquid two phase when flowing in the most upstream heat transfer tubethe evaporator is a fin tube heat exchanger comprising a fin and further comprises a heat insulating structure that prevents heat transfer between the first section and the second section,the first section and the second section share the fin, andthe heat insulating structure comprises a through hole formed in the fin at a boundary between the first section and the second section. 17. The evaporator for use in a Rankine cycle according to claim 16, wherein the requirement (A) is satisfied, andthe most upstream heat transfer tube forms an inlet of the evaporator so that the working fluid flows into the evaporator through the inlet and first passes through the most upstream heat transfer tube. 18. The evaporator for use in a Rankine cycle according to claim 16, wherein the first section includes only the most upstream heat transfer tube,the most upstream heat transfer tube is an internally smooth tube, andeach of the heat transfer tubes in the second section is an internally grooved tube.