Desain vapour space i. Volume Vapour Space Desain liquidcrystal space i.

vapour space liquidcrystal space liquidcrystal channel Gambar LC.1 Bagian Utama Kristalisator

a. Desain vapour space i. Volume Vapour Space

H H c H n D D n θ Sudut apex, θ = 30 o Laju massa air, F = 708,025 kgjam Densitas uap jenuh air, ρ = 1000 kgm 3 40 o C; 1 atm Space time uap air dalam vapour space, t = 0,25 jam Volume uap, V f = ρ t F = 1000 25 , 025 , 708 × = 0,177 m 3 Faktor kelonggaran = 20 Volume tangki, Vt = 1,2 x Vf = 1,2 x 0,177 = 0,212 m 3 ii. Dimensi Vapour Space Universitas Sumatera Utara Diameter Silinder : Tinggi Silinder D : H = 1 : 1 Tutup dan alas tangki berbentuk ellipsoidal dengan ellipsoidal dengan rasio axis major terhadap minor 2 : 1, sehingga tinggi tutup Hc = 16 D Brownell Young,1959 Volume tutup V c ellipsoidal = π 4 D 2 H h = π 4 D 2 1 6 D = π 24 D 3 Vt = Vs + Vc Vt = π 4 D 3 + π 24 D 3 Vt = 7 π 24 D 3 Diameter Tangki D = � 24V t 7 π 3 = � 24 × 0,212 7 π 3 = 0,614 m Tinggi silinder H = D = 0,614 m Tinggi tutup ellipsoidal H c = 16 x D = 0,102 m Diameter tutup = D = 0,614 m Diameter liquidcrystal channel, D n = 0,15 D = 0,15 ×0,614 = 0,092 m Tinggi conical section, H n = ½ D – D n tan θ = ½ ×0,614-0,092×tan30 o = 0,151 m

b. Desain liquidcrystal space i.

Volume liquidcrystal space Universitas Sumatera Utara D D l H H s H s θ Sudut elevasi, θ = 30 o Laju massa liquidcrystal, F = 4182,491 kgjam Densitas liquidcrystal = 2005,586 kgm 3 Space time dalam liquidcrystal space, t = 1 jam Volume liquidcrystal, V f = ρ t F = 586 , 2005 1 491 , 4182 × = 2,085 m 3 Faktor kelonggaran = 20 Volume tangki, V t = 1 + 0,2 × 2,085 = 2,503 m 3 ii. Dimensi vapour space Diameter Silinder : Tinggi Silinder D : H = 1 : 1 Tutup dan alas tangki berbentuk ellipsoidal dengan ellipsoidal dengan rasio axis major terhadap minor 2 : 1, sehingga tinggi tutup Hc = 16 D Brownell Young,1959 Volume tutup V c ellipsoidal = π 4 D 2 H h = π 4 D 2 1 6 D = π 24 D 3 Vt = Vs + Vc Universitas Sumatera Utara Vt = π 4 D 3 + π 24 D 3 Vt = 7 π 24 D 3 Diameter Tangki D = � 24V t 7 π 3 = � 24 × 2,503 7 π 3 = 1,398 m Tinggi silinder H = D = 1,398 m = 55,030 in Tinggi tutup ellipsoidal H c = 16 x D = 0,233 m Diameter tutup = D = 1,398 m Diameter sambungan, D l = 2,5 D n = 2,5 ×0,092 = 0,230 m Tinggi conical section, H n = ½ D – D l tan90- θ = ½ ×1,398-0,230×tan60 o = 1,011 m iii. Panjang liquidcrystal channel Panjang liquidcrystal channel, L = 0,7 × H = 0,7 ×1,011 = 0,978 m iv. Tekanan Desain Tinggi level cairan, Hf = H H V V c t f + = 233 , 389 , 1 503 , 2 085 , 2 + = 1,359 m Phidrostatik = ρ x g x Hf = 2005,586 x 9,8 x 1,359 = 26709,448 Pa = 26,709 kPa Po = Tekanan Operasi = 1 atm = 101,325 kPa Faktor kelonggaran = 20 Pdesign = 1+0,2 x Phidrosatik + Po = 1,2 x 26,709 + 101,325 = 153,641 kPa = 21,992 psia

v. Tebal Dinding Silinder