Gıda Mühendisliği Tasarımı
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Frozen French Fries and Potato Chips Factory
BEYNELMILEL FOOD CORPORATION FROZEN FRENCH FRIES ANDPOTATO CHIPS FACTORY DESIGN PROJECT PRESENTATION ORDER INTRODUCTION RECEPTION – DESTONING & WASHING – PEELING POTATO CHIPS LINE FRENCH FRIES LINE SLICING & SLICE WASHING – BLANCHING – FRYING PRECOOLING – FREEZING – COLD STORAGE CLEANING AND WASTE TREATMENT INTRODUCTION GENERAL INFORMATION NAME OF COMPANY : Beynelmilel Food Industrial Corporation DATE OF ESTABLISH : 01.01.2008 ADDRESS : BOLU Organization Zone / BOLU PHONE NUMBER : +90 374 215 98 74 WEB : www.beynelmilel.com TYPE OF PROCESS : Continuous SERVICE LIFE : 15 years ENERGY SUPPLY : Electricity…
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GMB 406 Proses Tasarımı Final Soru ve Cevapları
12.06.2008 tarihli sınav kağıdı …
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Hazelnut Oil Production
ABOUT ENTERPRISE ERBA YAĞ joint stock company Production of refined winterized hazelnut oil from inshell hazelnut Plant takes place in Düzce second industrial site Operates at 100 tons/day capacity Producing high quality edible oil for retail market and export Works 24 hours/day Operates 300 days/year Mass Balance Cleaning: 390 tons/day = 10 tons/day(foreign materials) + 380 tons/day(cleaned hazelnut) Dehulling: 380 tons/day = 190 tons/day(shell) + 190 tons/day (dehulled hazelnut) Roasting: Dry matter balance: 190x(0.88)=(0.95)x(X) X=176tons/day Pressing: Dry matter balance: 176x(0.4)=(0.85)x(X) X=83tons/day Oil balance: 176-83=93tons/day oil Toaster: 73 tons/day x (0.98)…
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Light Biscuit Factory
Food Engineering Design Light Biscuit Factory 2008/2009 IntroductIon by hürü bIndebir Contents Introduction Process Description Overall Mass Balance Mixing Drying Cooling Conveyors Sanitation Company name FLiform Capacity F 2000kg/day Operating time F 300 day/year What about our liform? More fiber Less calorie Minimum fat Much more digestible Free of sugar Capacity : 350 kg/batch Electric power : 17.2 kw Cast iron main frame covered with sheet metal of 304 CrNi Double Z- type mixing batch Automatic hydroalic pulling down unit Batch Cycle: 17-32 cycle per minute Automaticly evacuated vessel in 120º…
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Materials and Fabrication Selection
MATERIALS AND FABRICATION SELECTION ●In any engineering design; Selection of available materials of construction combined with the appropriate fabrication technique is important. ●To a new plant or ●In the improvement of an existing plant. ●Why selection of material is important ? ●Availability and cost (See Table 1 for relative cost of some metal plates) ●Because of severe operating conditions such as 1.Higher or lower temperatures 2.Corrosion 3.Flow rates 4.Pressures 5.Strong acids or strong bases Materials of Construction; 1.Metals 2.Nonmetals 1.METALS (Pure metals or alloys) 1.Iron and Steel ●Cost aspects favor…
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Mixing
Mixing usually implies the taking of two or more separate phases, such as a fluid and a powdered solid or two fluids, and causing them to be randomly distributed through one another. Agitation refers to forcing a fluid by mechanical means to flow in a circulatory or other pattern inside a vessel Blending: Agitation of two miscible liquid phase Suspension: Suspending solid particles into liquid. Dispersion: Dispersing a gas through the liquid in the form of small bubbles. Purposes for Agitating Fluids, 1. Blending of two miscible liquids, such as ethyl alcohol and water. 2. Dissolving solids…
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Pistachio Production
GLOBAL PISTACHIO Group members : Sümeyra YILDIRIM İlknur SALMAN Gülşah OKUR Ethem ÖZEN Hüseyin DEMİRCAN Şilan REYHANOĞULLARI ADVISOR : Prof. Dr. Mehmet D. Öner INTRODUCTION İLKNUR SALMAN FACTORY LOCATION NAME OF COMPANY : Global Group Co. Inc. MAIN ADRESS : Nizip Industrial Zone CAPACITY : 20000 kg raw material/day CLOSED AREA : 5 000 m2 AREA OF PLANT : 12 300 m2 OPERATION TIME : 16 hour/day NUMBER OF EMPLOYEES : 60 people WORKING CONDITION: 2 Shifts/day INTRODUCTION The pistachio, Pistacia vera in the Anacardiaceae family, is a small tree…
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Plate Heat Exchanger Calculations
PLATE HEAT EXCHANGER CALCULATIONS For T2 calculation of Regenaration Section C p,pekmez= 4.18*Xwater+ 2.5*Xsugar C p,pekmez= 4.18*0.82+ 2.5*0.18 = 3.88 kj/kg Tave = (T3 + T4)/2 = (105 +105)/2 =105 ° C table of A.2-5 and 12 from Unit operation by J. G.koplis hfg =enthalpy of saturated – enthalpy of condensate steam at 105 °C steam at 105 °C hfg = 2683.8 – 440.15 hfg = 2243 kj/kg For T7 calculation, in regeneration section; msteam*hfg= mpekmez*Cp*Δtpekmez msteam*2243 kj/kg =mpekmez*Cp*(T1-T2) 0.026*2174 kj/kg =0.436 kg/s*3.88kj/kg.°C*(90- T2) °C T2 = 55 ° C For…
