Method and apparatus for operational monitoring of a condenser with tubes, by measurements at selected tubes

• US 5,385,202 A
• Filed: 05/06/1993
• Issued: 01/31/1995
• Est. Priority Date: 11/06/1990
• Status: Expired due to Fees

• Current Assignee: Siemens AG
• Original Assignee: Siemens AG
• Inventors: Zorner, Walter, Drosdziok, Armin
• Primary Examiner(s): Ford, John K.
• Application Number:
  US08/058,296
• Time in Patent Office: 635 Days
• Field of Search: 165/11.1, 165/95, 165/1
• US Class Current: 165/11.1
• CPC Class Codes: F28B 11/00 Controlling arrangements with features specially adapted for condensers control arrangements in general G05
• CPC Class Codes: G01K 17/12 Indicating product of flow and temperature difference directly or temperature

Abstract

A method and an apparatus are provided for the operational monitoring of a condenser including a steam chamber through which steam to be condensed flows and at least one configuration having a plurality of tubes in the steam chamber through which a coolant fluid passes from an inlet to an outlet end. The steam pressure and/or temperature is measured at least at one measuring point in the steam chamber. In addition, the inlet temperature of the coolant fluid at the inlet end, the outlet temperature of the coolant fluid at the outlet end and the coolant fluid mass throughput are measured at each selected tube. The measurements are evaluated to determine the heat transfer coefficient of each selected tube and the coefficients thus determined are assessed for diagnostic purposes. In particular, a signal is given when at least one heat transfer coefficient differs substantially from a predetermined setting.

Claims

1. A method for operational monitoring of a condenser including a steam chamber through which steam to be condensed flows, at least one configuration in the steam chamber having a multiplicity of tubes, each of the tubes conducting a flow of a coolant fluid through it from an inlet end to an outlet end, and the multiplicity of tubes having a plurality of selected tubes, which comprises:

a) obtaining an inlet temperature of the coolant fluid at the inlet end, an outlet temperature of the coolant fluid at the outlet end, an ambient temperature defined as a temperature of the steam immediately flowing around the selected tube, and a mass throughput of the coolant fluid flowing through the selected tube, for each of the selected tubes;

b) measuring at least one of the steam pressure and the steam temperature of the steam at least at one measurement point in the steam chamber;

c) calculating the temperature of the steam immediately flowing around each of the selected tubes from one of the steam pressure and the steam temperature as well as a previously ascertained form of a distribution of at least one of the pressure and the temperature in the steam chamber;

d) determining a heat transfer coefficient from a product of the mass throughput and a logarithm of a quotient of differences between the ambient temperature and the inlet temperature as well as between the ambient temperature and the outlet temperature, for each of the selected tubes; and

e) subsequently comparing the heat transfer coefficients of all of the selected tubes with a set-point value, and issuing a warning if at least one of the heat transfer coefficients deviates substantially from the set-point value.

2. The method according to claim 1, which comprises using a natural logarithm as the logarithm.

3. The method according to claim 2, which comprises:

a) determining a heat input into the coolant fluid flowing through the selected tubes from a product of the mass throughput and a difference between the outlet temperature and the inlet temperature, for each of the selected tubes;

b) determining a logarithmic temperature difference as a quotient of the difference between the outlet temperature and the inlet temperature and the logarithm, for each of the selected tubes; and

c) calculating the heat transfer coefficient from a quotient of the heat output and a mean logarithmic temperature difference.

4. The method according to claim 1, which comprises feeding the coolant flow from an inlet chamber into all of the inlet ends, and determining the inlet temperatures for all of the selected tubes in common at a measurement point in the inlet chamber.

5. The method according to claim 1, which comprises:

a) measuring an inlet pressure of the coolant fluid at the inlet end and measuring an outlet pressure of the coolant fluid at the outlet end, for each of the selected tubes; and

b) determining the mass throughput for each of the selected tubes from the difference between the inlet pressure and the outlet pressure.

6. The method of one of claims 1, which comprises:

a) conducting an electrically conductive liquid through the tubes as the coolant fluid; and

b) determining the mass throughput for each of the selected tubes with an inductive flow rate meter.

7. The method of one of claims 1, which comprises:

a) conducting water in which traces of minerals are dissolved through the tubes as the coolant fluid; and

b) determining the mass throughput for each of the selected tubes with an inductive flow rate meter.

8. In a condenser including:

a steam chamber through which steam to be condensed flows, at least one configuration in the steam chamber having a multiplicity of tubes, each of the tubes having inlet and outlet ends for conducting a flow of a coolant fluid through the tubes from the inlet ends to the outlet ends, and the multiplicity of tubes having a plurality of selected tubes,

an apparatus for operational monitoring of the condenser, comprising;

a) means disposed at least at one measuring point in the steam chamber for measuring at least one of steam pressure and steam temperature;

b) inlet temperature sensors each being disposed at the inlet end of a respective one of the selected tubes, outlet temperature sensors each being disposed at the outlet end of a respective one of the selected tubes, and means disposed at each respective selected tube for measuring mass throughput; and

c) a diagnosis device being connected to said means for measuring at least one of steam temperature and steam pressure, to said inlet temperature sensors, to said outlet temperature sensors, and to said means for measuring the mass throughput, for determining an ambient temperature defined as a temperature of the steam immediately flowing around each selected tube from one of the steam temperature and the steam pressure, as well as a previously ascertained form of a distribution of at least one of the pressure and the temperature in the steam chamber; and

for calculating a heat transfer coefficient from a product of the mass throughput and a logarithm of a quotient of differences between the ambient temperature and the inlet temperature as well as between the ambient temperature and the outlet temperature, for each of the selected tubes; and

for comparing the heat transfer coefficients of all of the selected tubes with a set-point value, and issuing a warning if at least one of the heat transfer coefficients deviates substantially from the set-point value.

9. The apparatus according to claim 8, wherein said means for measuring at least one of steam pressure and steam temperature is a steam pressure sensor.

10. The apparatus according to claim 8, wherein said means for measuring at least one of steam pressure and steam temperature is a steam temperature sensor.

11. The apparatus according to claim 8, wherein said means for measuring the mass throughput is an inductive flow rate meter.

12. The apparatus according to claim 8, wherein said means for measuring the mass throughput is a combination of an inlet pressure sensor at the inlet end and an outlet pressure sensor at the outlet end.

13. The apparatus according to claim 8, wherein the selected tubes are distributed substantially uniformly over the configuration having the multiplicity of tubes.

14. The apparatus according to claim 8, wherein the at least one measuring point is remote from the configuration having the tubes.

15. The apparatus according to claim 8, wherein the at least one measuring point is above the configuration having the tubes.