_RP_10B-1997_scan.pdf

Addendum 2 November 2000 Recommended Practice for Testing Well Cements API RECOMMENDED PRACTICE 10B TWENTY-SECOND EDITION,DECEMBER 1997 American Petroleum Institute Helping You Get The Job Done Right?Copyright American Petroleum Institute Provided by IHS under license with APINot for ResaleNo reproduction or networking permitted without license from IHS-,-,-Copyright American Petroleum Institute Provided by IHS under license with APINot for ResaleNo reproduction or networking permitted without license from IHS-,-,-Addendum 2 to API RP IOB,Testing Well Cements(Contains Addendum 1 to API RP 1 O B -October 1999)Note:Vertical lines indicate items not contained in Addendum 1 Page 13,Section 7.6.2 The reference to Section 11 should be Section 9.Page 16,Table 2,Schedule lOSg,Elapsed Time 120 min,column 7,for temperature gradient of 2.7”C/100 m Replace“(1520”with“(152)”.Page 18,Section 9.2,metric value for Specific Heat Replace“2.1-2.4kJ/9kg x K)”with“2.1-2.4 kJ/(kg x K)”.Page 19,Section 9.2,4th paragraph,first sentence Replace“rotated as a speed”with“rotated at a speed”.Page 20,Section 9.4.4:Replace with the following:During the test period,the temperature and pressure of the cement slurry in the slurry con-tainer should be increased in accordance with the appropriate well-simulation test schedule(see 9.5).Schedules may be calculated or taken from the tables.Temperature of the cement slurry shall be determined by use of an ASTM classification“special”Type J thermocouple(see Appendix B)located in the center of the sample container.The tip of the thermocouple shall be vertically positioned,within the paddle shaft,in the slurry cup in such a way that it is between 1.75 in.(4.45 cm)and 3.50 in.(8.89 cm)above the inside of the base of the sam-ple container.As there are many models of consistometers having different dimensions,care must be taken to ensure that the thermocouple used is compatible with the consistometer and the position of the tip of the thermocouple is in the correct location specified above.Page 22,Equation(8b)The constant should be 9.776.Page 87,Section 10.6.2.10 The reference to 10.6 should be“10.8”.Page 87,Section 10.7.1.11 The reference to 10.6 should be“10.8”.Page 89,Section 11.2.1.1,first sentence The inside dimensions given for the bottom,1.102 in.,27.99 mm,and top,1.154 in.,29.3 1 mm are reversed.The inside dimension for the bottom should be 1.154 in.(29.3 1 mm)and the inside dimension for the top should be 1.102 in.(27.99 mm)as shown in Figure 9.Page 95,Equation(17b)Replace“4”with“2”.1 Copyright American Petroleum Institute Provided by IHS under license with APINot for ResaleNo reproduction or networking permitted without license from IHS-,-,-2 API RECOMMENDED PRACTICE 10B-ADDENDUM 2 Page 96,Section 12.4.2(begins on page 95)“cylinder”.Remove the words“which is also transmitted to the”and add the word“or”following Page 96,Equation(19b)Replace“32.55”with“16.28”.Page 98,Section 12.8.1.1 First paragraph:The reference to Curve A should be Curve D.Second paragraph:The reference to Curve B should be Curve A.Page 98,Section 12.8.1.2 First paragraph:The reference to Figure 1 1,Curve C,should be Figure 11,Curves B and C.Second paragraph,second sentence:The reference to Figure 11,Curve C should be Figures 11 and 12,Curve B.Second paragraph,fourth sentence:The reference to Figure 11,Curve D should be Figures 11 and 12,Curve C.Second paragraph,sixth sentence:The reference to Figure 1 1,Curve B should be Figures 11 and 12,Curve A.Page 101,Figure 12 The scale for the Shear-rate axis(x-axis)should begin with 1,not O.Page 104,Section 13.2,first sentence Replace“m”with p”and“r”with“p”.Page 105,Section 13.3,first sentence Replace Y with“p”.Page 105,Equations(62),(63),and(64)The term KRepL should be in the denominator rather than the numerator.Page 106,Section 13.4,third paragraph Replace“mi with“y”and Y with“p.”Page 106,Equation(72)The title should read“Annular Flow:Pipe”.Page 106,Equation(73)The title should read“Annular Flow:Slot”.Copyright American Petroleum Institute Provided by IHS under license with APINot for ResaleNo reproduction or networking permitted without license from IHS-,-,-TESTING WELL CEMENTS 3 Page 106,Equation(75)The title should read“Annular Flow:Pipe”.Page 106,Equation(76)The title should read“Annular Flow:Slot”.Page 106,Section 13.4,right-hand column,first paragraph The introductory sentence and table should read as follows:Depending on the value of the Reynolds number the flow regime is classified as follows:I Flow Regime I Pipe Flow I Annular Flow I I Laminar I a I a I Transitional I Re,Re,Rep2 I R B P ReBP2 I I I Turbulent I Re,t Re,I Re,t Re,I Page 106,Equation(78)The title should read“Annular Flow:Pipe”.Page 106,Equation(79)The title should read“Annular Flow:Slot”.Page 107,Equation(88)The title should read“Annular Flow:Pipe”.Page 107,Equation(89)The title should read“Annular Flow:Slot”.Page 107,Equations(90),(91),(92),and(93)The term in the denominator of each of these equations,6ReBpz