Page 245 - Facility Piping Systems Handbook for Industrial, Commercial, and Healthcare Facilities
P. 245

HEAT TRANSFER, INSULATION, AND FREEZE PROTECTION

                                    HEAT TRANSFER, INSULATION, AND FREEZE PROTECTION   5.29

                        T  =  ambient temperature at a distance from pipe that would not be affected by the heat of
                         2
                           the pipe (This would be either the ground temperature for buried pipe or the design
                           temperature of the air.)
                        A =  area, in square feet, normal to the direction of heat flow of a 1-ft long section of pipe
                           (Where there is insulation, the cylinder of insulation should be used to calculate the
                           arithmetic mean of the area between the pipe wall and the outside of the insulation.
                           Refer to Table 5.6.)
                        X =  distance, in inches, from the outside of the pipe wall where T  is measured to where
                                                                        1
                           T  is taken
                            2
                        TABLE 5.10  Heat Loss from Typical Steel Tank on Grade

                                                 Tank capacities—in thousands of gallons
                          °F   °C   100    150    200    300    400    500    750    1,000

                        35     2      85    114    135    175    206    238    312    380
                        30    –1     121    162    193    248    294    340    445    543
                        25    –4     161    216    257    330    393    453    594    722
                        20    –7     202    271    323    414    493    568    745    907
                        15    –10    245    329    391    502    537    689    904  1,099
                        10    –13    290    389    463    595    707    816   1,071  1,302
                         5    –15    337    452    539    691    822    949   1,244  1,514
                         0    –18    388    521    620    796    947   1,093  1,434  1,744
                        –5    –20    441    592    705    905  1,076   1,241  1,628  1,981
                        –10   –23    498    669    797  1,023  1,216   1,403  1,841  2,239
                        –15   –26    557    748    891  1,143  1,360   1,569  2,058  2,503
                        –20   –29    619    830    989  1,270  1,510   1,742  2,286  2,781
                        –25   –33    685    920  1,096  1,406  1,673   1,930  2,532  3,080
                        –30   –34    752  1,010  1,203  1,545  1,837   2,119  2,781  3,383
                        –35   –37    825  1,108  1,320  1,694  2,015   2,325  3,050  3,710
                        –40   –40    898  1,206  1,437  1,844  2,193   2,531  3,320  4,039
                        –50   –45   1,059  1,422  1,694  2,175  2,586  2,984  3,915  4,762
                        –60   –51   1,229  1,651  1,966  2,524  3,002  3,463  4,544  5,528


                                    TABLE 5.11  Heat Loss in Riser of Elevated Storage Tanks
                                    Btuloss per hour through 4-ft-diameter (3.3-m) riser per foot-length
                                    Atmospheric
                                    temperature, °F       °C            Btu/h
                                     35                     2             69
                                     30                    –1            192
                                     25                    –4            340
                                     20                    –7            506
                                     15                   –10            692
                                     10                   –13            893
                                     5                    –15           1,092
                                     0                    –18           1,309
                                     –5                   –20           1,536
                                     –10                  –23           1,771
                                    –15                   –26           2,020
                                    –20                   –29           2,291
                                    –25                   –33           2,568



                     Downloaded from Digital Engineering Library @ McGraw-Hill (www.accessengineeringlibrary.com)
                                Copyright © 2009 The McGraw-Hill Companies. All rights reserved.
                                  Any use is subject to the Terms of Use as given at the website.
   240   241   242   243   244   245   246   247   248   249   250