Patent Number: 051715180
Section: claims

1. A method of determining differences in the rate of heat transfer through first and second tube walls, comprising: (a) obtaining a tubing segment having a first wall, the first wall including an inner surface defining an inner side of the tubing segment and a radially spaced outer surface defining an outer side of the tubing segment,  (b) supporting a quantity of thermally conductive material on one of the inner side and the outer side of the tubing segment having a first wall, the thermally conductive material being in thermal contact with the first wall,  (c) placing one of a heating medium and a cooling medium having an initial temperature T.sub.a on the other of the inner side and the outer side of the tubing segment in thermal contact with the first wall, and determining the time required for the temperature of a portion of the thermally conductive material in thermal contact with the first wall to change from a first temperature T.sub.1 to a second temperature T.sub.2, T.sub.1 and T.sub.2 being outside the melting range and vaporization range of the thermally conductive material,  (d) obtaining a tubing segment having a second wall, the second wall including an inner surface defining an inner side of the tubing segment and a radially spaced outer surface defining an outer side of the tubing segment,  (e) supporting a quantity of thermally conductive material on one of the inner side and outer side of the tubing segment having a second wall, the thermally conductive material being in thermal contact with the second wall,  (f) placing one of a heating medium and a cooling medium having an initial temperature T.sub.b on the other of the inner side and outer side of the tubing segment in thermal contact with the second wall, and determining the time required for the temperature of a predetermined portion of the thermally conductive material in thermal contact with the second wall to change from a third temperature T.sub.3 to a fourth temperature T.sub.4, T.sub.3 and T.sub.4 being outside the melting range and vaporization range of the thermally conductive material, T.sub.3 being greater than T.sub.4 when T.sub.1 &gt;T.sub.2 and T.sub.3 being less than T.sub.4 when T.sub.1 &lt;T.sub.2, and  (g) comparing the times obtained in steps (b) and (f).  (h) after step (c), removing the medium having an initial temperature T.sub.a from thermal contact with the first wall, placing one of a heating medium and a cooling medium having an initial temperature T.sub.c on the other of the inner side and the outer side of the tubing segment in thermal contact with the first wall, and determining the time required for the temperature of the portion of the thermally conductive material in thermal contact with the first wall to change from a fifth temperature T.sub.5 to a sixth temperature T.sub.6, T.sub.5 being greater than T.sub.6 when T.sub.1 &lt;T.sub.2 and T.sub.5 being less than T.sub.6 when T.sub.1 &gt;T.sub.2,  (i) after step (f), removing the medium having an initial temperature T.sub.b from thermal contact with the second wall, placing one of a heating medium and a cooling medium having an initial temperature T.sub.d on the other of the inner side and the outer side of the tubing segment in contact with the second wall, and determining the time required for the temperature of the portion of the thermally conductive material in thermal contact with the second wall to change from a seventh temperature T.sub.7 to an eighth temperature T.sub.8, T.sub.7 being greater than T.sub.8 when T.sub.3 &lt;T.sub.4, and T.sub.7 being less than T.sub.8 when T.sub.3 &gt;T.sub.4, and  (j) comparing the times obtained in steps (h) and (i).  (a) removing a segment of fouled tubing from a heat exchanger, the tubing segment having a first wall including an inner surface and a radially spaced outer surface,  (b) supporting a quantity of a thermally conductive material in contact with one of the inner surface and the outer surface of the first wall,  (c) placing one of a heating medium and a cooling medium having a constant temperature T.sub.a in contact with the other of the inner surface and the outer surface of the first wall, and subsequently determining the time required for the temperature of a predetermined portion of the thermally conductive material to change from a first temperature T.sub.1 to a second temperature T.sub.2, T.sub.1 and T.sub.2 being outside the melting range and vaporization range of the thermally conductive material,  (d) obtaining a substantially clean segment of heat exchanger tubing having a second wall including an inner surface and an outer surface,  (e) supporting a quantity of the thermally conductive material in contact with one of the inner surface and the outer surface of the second wall,  (f) placing the medium used in step (c) in contact with the other of the inner wall and the outer wall of the tubing segment and determining the time required for the temperature of the thermally conductive material to change from T.sub.1 to T.sub.2, and  (g) comparing the times obtained in steps (c) and (f). 2. The method of claim 1, wherein the tubing segment having a second wall is obtained by altering the physical characteristics of the tubing segment having a first wall. 3. The method of claim 2, wherein altering the physical characteristics of the tubing segment having a first wall includes cleaning at least one of the inner surface and outer surface of the tubing segment having a first wall. 4. The method of claim 1, wherein the tubing segment having a first wall is obtained from a heat exchanger after use. 5. The method of claim 1, wherein T.sub.1 =T.sub.3 and T.sub.2 =T.sub.4. 6. The method of claim 1, wherein T.sub.a =T.sub.b. 7. The method of claim 1, wherein the medium having a temperature T.sub.a and the medium having a temperature T.sub.b are kept at constant temperatures when time measurements are made. 8. The method of claim 7, wherein T.sub.1 =T.sub.3, T.sub.2 =T.sub.4 and T.sub.a =T.sub.b. 9. The method of claim 1, wherein the mediums having temperatures T.sub.a and T.sub.b are baths containing water. 10. The method of claim 1, wherein steps (c) and (f) are conducted repeatedly and average values of time are calculated for each step. 11. The method of claim 1, wherein the quantity of thermally conductive material in thermal contact with the first wall has the same conductivity and composition as the quantity of thermally conductive material in contact with the second wall. 12. The method of claim 11, wherein the thermally conductive material has a higher thermal conductivity than the first and second walls. 13. The method of claim Il, wherein the thermally conductive material is an alloy comprising lead and bismuth. 14. A method according to claim 1, wherein at least one of the inner surface and outer surface of the tubing segment having a first wall is radioactive. 15. A method according to claim 1, further comprising the step of determining the percent difference in the rate of heat transfer through the tubing segment having a first wall and the tubing segment having a second wall, taking into account any differences between T.sub.1 and T.sub.3, T.sub.2 and T.sub.4, and the mediums having the temperatures T.sub.a and T.sub.b, and taking into account any changes in T.sub.a and T.sub.b during the measurement process. 16. The method of claim 1, further comprising: 17. The method of claim 16, wherein T.sub.a =T.sub.b, T.sub.c =T.sub.d, T.sub.1 =T.sub.3, T.sub.2 =T.sub.4, T.sub.5 =T.sub.7 and T.sub.6 =T.sub.8 18. The method of claim 16, wherein steps (c), (f), (h) and (i) are conducted repeatedly and average values of time are calculated. 19. A method of determining a change in the rate of heat transfer through the wall of a heat exchanger tube due to fouling of the surface of the tube, comprising the steps of: