The application discloses a design method of a shell-
boiling tube-condensing wound tube
heat exchanger, according to the inlet and outlet temperatures of the tube and the shell, the
dew point and
bubble point of the working medium of the tube and the shell, the whole
heat exchanger is divided into three parts, i.e. a tube-condensing shell-liquid section, a tube-condensing shell-boiling section and a tube-condensing shell-gas section, and the heat exchange capacity, the
surface heat exchange coefficient of the tube and the shell, the comprehensive heat
exchange coefficient, the pressure drop of the tube and the shell, the heat exchange area and the axial effective heat exchange length of the three parts of the wound tube
heat exchanger are respectively designed and calculated; the tube is always in a gas-liquid
mixed phase state of condensation
phase change, the
surface heat exchange coefficients of the tube and the shell are related to the
dryness, therefore, the three parts of the wound tube heat exchanger are designed and calculated by using the finite volume method. The design method of the shell-
boiling tube-condensing wound tube heat exchanger has the characteristics of high calculation precision, complete design method and high calculation efficiency, and has high commercial value and market promotion value.