TUBE FOULING MONITOR

• US 20090188645A1
• Filed: 01/28/2009
• Published: 07/30/2009
• Est. Priority Date: 01/28/2008
• Status: Abandoned Application

• Current Assignee: Intek
• Original Assignee: Intec Incorporated (G Holdings Incorporated)
• Inventors: Harpster, Timothy J., Harpster, Joseph W.
• Application Number:
  US12/360,960
• Publication Number:
  US 20090188645A1
• Time in Patent Office: Days
• US Class Current: 165/11.100
• CPC Class Codes: F28B 1/02 using water or other liquid as the cooling medium
• CPC Class Codes: F28B 11/00 Controlling arrangements with features specially adapted for condensers control arrangements in general G05
• CPC Class Codes: F28D 7/1653 the conduit assemblies having a square or rectangular shape
• CPC Class Codes: F28F 19/00 Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
• CPC Class Codes: F28F 2200/00 Prediction; Simulation; Testing measuring quantity of heat conveyed by flowing mediums G01K17/06
• CPC Class Codes: G01K 17/06 Measuring quantity of heat conveyed by flowing media, e.g. in heating systems G01K17/02, G01K17/04 take precedencee.g. the quantity of heat in a transporting medium, delivered to or consumed in an expenditure device

Abstract

A method for measuring the effects of fouling of heat transfer tubes in heat exchangers where a cooling fluid at lower temperature is removing heat from another fluid at higher temperature includes placing a nonrestrictive mass flow rate and temperature measuring tube extension sensor on a tube outlet end; obtaining the tube inlet temperature for deriving the rise in fluid temperature; analytically computing the amount of heat transferred from the hot fluid to the cold fluid; from tube length, inside and outside tube diameter, analytically deriving the tube heat transfer coefficient; and determining tube fouling factor, the value of which is the fraction of the clean tube heat transfer coefficient available for transferring heat, by dividing the heat transfer coefficient by the known heat transfer coefficient of an unfouled tube.

Claims

1. A method for measuring the effects of fouling of heat transfer tubes in heat exchangers where a cooling fluid at lower temperature is removing heat from another fluid at higher temperature, which comprises the steps of:

(a) placing a nonrestrictive mass flow rate and temperature measuring tube extension sensor on a tube outlet end;

(b) obtaining the tube inlet temperature for deriving the rise in fluid temperature;

(c) analytically computing the amount of heat transferred from the hot fluid to the cold fluid;

(d) from tube length, inside and outside tube diameter, analytically deriving the tube heat transfer coefficient; and

(e) determining tube fouling factor, the value of which is the fraction of the clean tube heat transfer coefficient available for transferring heat, by dividing the heat transfer coefficient by the known heat transfer coefficient of an unfouled tube.

2. The method of claim 1, wherein an averaged signal is obtained from multiple location sites in a sensor and the value of said flow rate determined.

3. The method of claim 1, wherein rings of heater/temperature sensor and reference temperature sensor pairs are associated with heat transfer across the sensor wall to the flowing coolant and not caused by longitudinal temperature gradients along the length of the sensor.

4. The method of claim 1 for simulating the fouling factor of a given heat exchange tube system or additionally by employing in the sensor the same material as the heat exchanger tube coating the interior of a sensor exchange tube with a coating of the same expected fouling composition, so that measurements of the fouling factor in the tube could be determined in situ under the assumption that mass flow rate of cooling fluid remains constant.

5. The method of claim 1, wherein coatings or surface finish are applied at selected locations on an inner surface of said tube extension sensor attached to an outlet end of a heat transfer tube to inhibit fouling to improve measurements of the mass flow rate of cooling fluid passing through the sensor.

6. The method of claim 4, wherein each sensor also has a sensor tube extension coated or surface finished on an inner surface location to inhibit fouling, and at another location to promote fouling wherein at least these two measurement sites are used to determine in situ a measured fouling factor by directly measuring an effective mass flow rate ratio at the two measurement sites that have a direct and definable relationship to heat transfer coefficient ratio indicative of a fouling factor.

7. The method of claim 3, wherein the reference temperature sensor signal of the flow sensor is used as an nonrestricted means to measure the condenser tube outlet temperature to obtain the condenser tube temperature rise when combined mathematically with plant measured inlet circulating water temperature and a heated sensor temperature to measure mass flow rate to be combined to obtain a measure of the input heat of condensation on the tube due to condensation.

8. The method of claim 1, wherein which is applied to regions of fouling and regions of no fouling measure heat transfer differences between regions of fouling and in regions of no fouling to analyze the cause for difference in heat transfer coefficient.

9. The method of claim 4, wherein said coatings are evaluated for effectiveness in resisting fouling.

10. The method of claim 1, which is employed following tube cleaning for identifying cause for low heat transfer in tubed heat exchangers that may include one or more of:

(a) regions dominated by air binding,

(b) regions subjected to tube sheet fouling,

(c) regions that may be subjected to high rates of inner tube wall fouling,

(d) regions less prone to fouling of tubes internally,

(e) regions subjected to low cooling water flow rates,

(f) evaluating regions that may be analytically prone to high or low flow rates, or

(g) independently measuring h_a and h_f by appropriate placement of tube fouling meter sensors in a tube bundle.

11. The method of claim 1, which is employed to determined when ball cleaning of the heat exchange tubes is required.

12. The method of claim 1, which is employed with heat exchange tubes in air bound zones or air binding zones.

13. A sensor for monitoring and measuring in situ or by derivation the effects of fouling of heat transfer tubes in heat exchangers that are used to condense steam exhausted from turbines in electric power generating plants, which comprises:

(a) an inner tube;

(b) an adapter for mating said inner tube to an end of said heat transfer tube;

(c) a layer of insulation surrounding said inner tube;

(d) a pair of spaced apart heater/temperature sensors disposed about the outer periphery of said inner tube;

(e) an electronic signal cable in electrical connection with said heater/temperature sensor pairs.

14. The sensor of claim 13, wherein the inside of said inner tube for one of said heater/temperature sensors being treated to be resistant to fouling.

15. The sensor of claim 14, which is used for one or more of:

(a) measuring directly the effective heat transfer coefficient rate of change due to fouling that occurs within the sensor over time resulting from a flow rate signal change under conditions of constant flow rate;

(b) measuring average heat transfer coefficient of a tube by obtaining measured inlet circulating water temperature, the shell side steam temperature and tube geometry, by separate means, and combining these with the described sensors determined circulating water outlet temperature and measured circulating water mass flow rate to calculate the effective heat transfer coefficient, U_eff, of the tube;

or

(c) determining the fouling modifier of the heat transfer coefficient by measurement between two sites in the sensor one site having similar surface area for fouling as within the tube and the other site having a surface substantially immune to fouling to serve as a reference baseline flow measurement and circulating water mass flow rate measurement.

16. A method of placing the sensor of claim 13 near or at the top row of tubes in a heat exchanger to identify air pocket within the water box through loss or reduced circulating water flow rate or excessive outlet circulating water flow rate.

17. A method of attaching the flow and fouling sensor of claim 13 at the inlet end of a heat exchanger tube and a temperature sensor at the outlet end of the same tube to measure the mass flow rate of circulating water in the tube and the temperature difference across the tube, coupled with independent determination of the steam saturation temperature and tube geometry obtain a determination of the total tube fouling modifier.

18. A method of placing the sensor of claim 13 on each end of a heat exchanger tube to obtain a differential flow signal related to difference in inlet end and outlet end fouling that has a dependence on circulating water temperature such fouling as may be related to specific biological fouling or others but not limited to air binding.