XT-80 soap making machine for 20-60g small soaps

XT—80 Toilet soap strip output machine is designed to make grinded soap flakes into strips in the process of manufacturing small size toilet soaps before they are pressed the shapes required.It is simple in structure and of endurance; units in soap production are made of high- quality stainless steel Major Technical References Production     Capacity  80Kg /h  Outside Diameter of screw

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Hydraulic system of edible edible oil press machine

Hydraulic system is the main power force of hydraulic oil press machine, it includes transmission shaft, turbine, worm gear, gear pump, high pressure pump, overflow valve; super high pressure safety valve; hand-operated valve; seamless steel tube; pipeline connect and other spare parts. This machine adopts the advanced power pack of the world, and compared with

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Main engine of edible oil press machine

Main engine includes base, upright, top plate, oil drip pan nut and so on , it is one of the main parts. Firstly the oil material is put into the assembly of the press boring ,then it being droved up by the oil cylinder piston ,oil will outflow from the gap of press boring ,and

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How does an edible oil press work?

The seed is placed into the feeder either by labor or by conveyor. Then through the huge pressure or violent motion in the closed press, the original structure of oil seeds are broken and a series of changes happened inside. Finally the oil is expressed out of the the oil seeds. Cold pressing is temperature

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Brief introduction of rapeseed oil press machine

When operating, the good processed oil material into the pressing chamber from hopper, and the screw rotate to push-in the material for squeezing. For the material is conducted in the motion state, under high pressure of chamber, the material, screw, and chamber have a great friction resistance, which resulting in relative motion. On the other

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Edible oil solvent condensation & recovery process

Solvent condensation system combines with evaporation system closely, and evaporative condenser and steam stripping condenser all work under negative pressure. Non-condensable gas enters the energy saver from the shell of the first evaporator. In energy saver, noncondensable gas exchanges heat with condensate from the evaporative condenser. Finally, the condensate temperature discharged from energy saver is

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Main economic and technical parameters of towline extractor

Main Economic and Technical Parameters of Towline Extractor (take 500T/D as an example) Steam consumption ≤ 280kg/t (soybean) Power consumption installed capacity 320KW Solvent consumption ≤ 4kg/t (No.6 solvent) Residual oil in meal ≤ 1.0% Moisture in meal 12~13% (adjustable) Solvent in meal ≤ 500ppm Urase activity 0.05-0.25 (soybean meal) Total volatile matter ≤ 0.3% Residual solvent ≤ 300ppm Mechanical impurities ≤ 0.2%

Main economic and technical parameters of edible oil solvent extraction

Main economic and technical parameters( take 300t soybean as an example): Capacity 30-500T/D Residual oil in meal ≤ 1% Solvent consumption ≤ 2Kg/T (No.6 solvent oil) Crude oil moisture and volatile matter ≤ 0.30% Power consumption ≤ 15KWh/T Steam consumption ≤ 280KG/T (0.8MPa) Finished meal moisture ≤ 13% (adjustable) Residual solvent in finished meal ≤300PPM

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The introduction of cooking oil refinery equipment

1. The neutralizing tank is used for acid for acid,alkali refining or rinse 2. The decoloring tank is for bleaching grease 3. The deodorizing tank is sued for deodotization tank 4. The conducting oil furnance provide the heating for production 5. The vacuum pump provide vacuum for bleaching , deodorization which is can reach 755mmkg

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Rice bran oil processing plant — refining introduction

Main Processes Introduction a.Hydration Degumming & Alkali Refining Deacidification Process b.Continuous Refining Decoloring Process 1. The oil fully contacting with the decolorant can improve the decolorization efficiency and reduce the usage of decolorant; 2. The continuous and uniform material flows will balance the decoloring time and avoid the recovery of grease oxidation and acid value.

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