Design of Horizontal & Short Vertical Vessels األول :هو احنا هناخد إيه النهاردة في السكشن؟ الثاني :هناخد Vessel Design األول :يوووووووووووووووووه أمال هناخد Reactorامتى؟ الثاني :قصدك على سكشن ال non-isothermalيعني؟ أنا شفت االعالنات بتاعة السكشن امبارح على ال MBC 2وقالكComing : Soon on Decemberفقط وحصريا على شاشة ال MBC 2 الثالث :أنا مش عارف انتو ازاي فايقين ورايقين كدة وقاعدين تقولوا هناخد إيه ومش هناخد إيه ومش حاسين بالكارثة اللي أنا فيها االتنين في نفس واحد :كارثة إيه يابني؟!!! الثالث :سؤال بجد مصيري ومحيرني جدا ونفسي أالقي له إجابة األول :ياعم ما تخلص وتقول بقى وقعت قلبي الثالث :يا ترى sheetالنهاردة كام مسألة؟!!!!!!!!!!!!!!!!!!! In designing short vessels, we firstly calculate the thickness of shell and heads according to the operating pressure [i.e. internal or external]. In this case we will not do checks on the thickness as done in tall vessels so, we will design the support directly. The use of lugs is typically limited to vessels of small to medium diameter (1 to 10 ft.) and moderate height-todiameter ratios in the range of 2:1 to 5:1. And of Course Sheet5: 2 problems Sheet5 : 2 Problems After calculating fs, you should select the dimension of pipe (lug) and check on your selected dimensions [i.e. check if the lug supports will withstand the load applied on it]. Following are the steps used to select the suitable pipe dimensions: 1. From the following table, assume nominal diameter to get the inside and outside diameter of the pipe. Begin your assumption with nominal diameter = 2" [always take the Schedule number = 80]. Sheet 5: 2 Problems 2. Calculate the radius of gyration (r) from the following equation: 3. Calculate the value of h’/r. 4. Make the check on the selected pipe dimensions according to the value of h’/r . Those values are summarized in the following table: h' r The Check Relation h' 60 r fs allpipe Apipe 60 fs Apipe h' 200 r h' 200 r Fcritical 5 * f s all. pipe 1 1 all. pipe h' * r 2 2 * E ' * I min. Fcritical h' I min. I cal. 5. If the corresponding check is not correct, assume another nominal diameter [greater than 2"] and repeat the above steps. Assume: In order to check on this assumption, use the following formula: If σtension) max = - ve value: the number of bolts equal 4 used for fixation. If σtension) max = + ve value: the number of bolts calculated from the following equation: Hello?! I just want to tell u that sheet5 : 2 problems Design of Saddle Support: or Sheet5: 2 Problems In Mass Transfer?! Assume: I’ll go to the section now. I don’t know which subject but they told me that Sheet5: 2 Problems Design of Bearing Plate: Assume: Yes Design of Anchor Bolts: only 4 bolts for fixation Sheet5: 2 problems? 1. A pressurized vessel lined internally with 4 mm Nickel material is to be fabricated and installed out of doors in Mostorod area. The vessel has the following specifications: Shell inside diameter 1.5 m Shell length 4m Maximum internal pressure 20 atm.gage Operating temperature 150ºC Lug support height 2m No. of lugs 6 Corrosion allowance 1 / 16 in. Insulation thickness 2 in. Shell material C.steel Allowable tensile strength of material of construction 15000 psi Head type Dished Specify the design for: - Shell & heads. - Lug support, bearing plate & anchor bolts. - Maximum permissible vacuum applied in the vessel. 2. A process horizontal vessel is to be fabricated and installed out of doors. The vessel has the following specifications: Shell inside diameter 1.1 m Shell length 2.1 m Maximum internal pressure 10 bar Distance between two supports 1.25 m Operating temperature 150ºC Support height 1m Fluid Heavy hydrocarbon Corrosion allowance 3 mm Insulation thickness 50 mm Shell material Carbon steel Allowable tensile stength of material of construction 1000 kg/cm2 Type of heads Dished Specify the design for: - Shell & heads. - Support, bearing plate and anchor bolts.