Hot Sale 500t D Edible Oil Mill with ISO Approved

Standard Information

Design No.: 100-6000t/d

Item Description
Vegetable Oil Extraction Line
Major Gadgets: extractor, desolventizer-toaster with integrated dryer-cooler, unfavorable force evaporator, horizontal stainless pipe bundle condenser, filtering method for getting rid of food foam from miscella, system for recycling solvent from exhaust fuel, circulating system for separating water from solvent, electrical control system
Applicable Raw Resources: soybeans, rapeseeds, cottonseeds, peanuts, sunflower seeds, corn germs, rice bran, palm fiber (palm food)
Generation Capacity:100-6,000t/24h raw materials
Approach Workflow

Oil Extraction Segment → DTDC CZPTlventizer Toaster Dryer Cooler → Oil Filtration Part → Evaporation and Separation Segment → Solvent Condensation and CZPTvery System → Paraffin Absorption Method → H2o Solvent Separation and CZPTvery Method → Computerized Manage System

(one) Oil Extraction Part
CZPTers can choose rotocel extractor or drag chain extractor primarily based on their needs. For diverse uncooked materials, grid trays clearance and grid trays arrangement will be correctly adjusted to guarantee that the oil residues in seed meal is bare minimum. In addition, liquids in seed meal will be completely drained off, which contributes to least solvent material. As a end result, the load imposed on desolventizing system in sequential approach will be greatly alleviated, which further lowers steam consumption.  


(2) DTDC CZPTlventizer Toaster Dryer Cooler

The device consists of pre-desolventizing layer, warmth trade layer, desolventizing layer, heat restoration layer, drying layer and cooling layer. Components ranges at each and every layer can be automatically controlled. Total utilization of secondary steam decreases steam intake. Combined steam will be utilized to heat miscella following food foam removing, which further will save vitality. The process functions complete desolventizing, light-weight yellow food, complete passivation of antinutritional variables, limited time necessary for higher temperature desolventizing and lower loss of meal NSI.


(3) Oil Filtration Part

The method is created to filter out strong impurities prior to miscella evaporation. Products employed contain substantial pressure shipping pump, centrifugal separator and filter with slagging operate. Optimum filtration effect can be reached by blend of centrifugal separation specific filtration. Considering that the filter is capable to get rid of slags automatically, no manual procedure is required.


(4) Evaporation and Separation Section

Products used in the method includes evaporator, disc stripping tower, flash separator, heat exchanger and vacuum device. Under a vacuum and negative force issue, solvent in the miscella will be evaporated and separated by increasing film evaporation and immediate stripping. After comprehensive desolvation, vivid colour leached oil will be obtained. To ensure system stability and dependability, an automated PLC management system is adopted for control of evaporating temperature and vacuum stage. Both blended steam and energy steam for vacuum pump will be adequately employed for evaporation. Heat transfer and mass transfer between great and very hot medium furthers lowers steam consumption. In addition, lipid oxidation can be prevented as properly.


(five) Solvent Condensation and CZPTvery Method
The technique primarily is made up of condenser and circulating cool h2o program. Under the vacuum situation, condensable solvent steam is condensed into liquids for cyclic utilization by way of dividing-wall warmth transfer. A number of-move construction of the condenser and correct configurations of circulation price and pace of circulating drinking water will drastically enhance effectiveness of condensation and separation and mainly lowers expenditure money and functioning price. In addition, tube plates, baffle plates and warmth exchange tubes are all produced of stainless steel, which facilities cleaning and withstands corrosion. Moreover, excellent condensation impact and long support existence can be totally ensured.


(six) Paraffin Absorption Program

The program consists of Paraffin absorption column,Paraffin desorption column,hear exchanger,storage tank, punp,Exhaust fuel blower and so on. It is capable to recycle much more than 98 per cent solvent in the exhaust gasoline, which reduces solvent reduction and safeguards atmosphere at the exact same time.
The program tends to make use of food-grade liquid paraffin to adsorb solvent fuel blended in exhaust gasoline. The solvent steam will be distilled and separated with the support of superheated steam. Then the solvent steam acquired will be recycled through condensation. To make certain stable absorption performance and system reliability, computerized manage gadgets are applied to management crucial parameters these kinds of as circulation charge, temperature and force.


(seven) H2o & Solvent Separation Segment

The program is made up of solvent-drinking water separator, boiling tank,and refreshing solvent pump. It separates water from solvent dependent on the principle that h2o repels solvent and two liquid layers will be fashioned in their mixture. To guarantee steadiness and dependability of the program, automated control products are applied to control crucial parameters this kind of as flow rate, temperature and content amount.

(eight) Automatic Management System

In our creation lines, we make use of Siemens PLC management method, which is one of mainstream automatic handle systems in today`s market. The efficient, secure and advanced DCS control technique is made up of operation station, handle station and communication community. We utilize substantial-pace and big-potential S7-400 collection PLC at the control program, big-screen Lcd at the procedure station, WINCC 7. industrial management software program as monitoring application and PROFIBUS filed bus community for communication.

   We also give the pursuing project and products:

Oilseed Pretreatment Venture
Oilseed Urgent Project
Oil Extraction Task
Oil Refining Project 
Cottonseed Miscella Refining Project
Minimal Temperature and Edible Soybean Meal Undertaking
Soy Protein Focus Venture
Soy Protein Isolate Project
Total Excess fat Soybean Powder Undertaking
ASME Strain Vessel 
ASME Warmth Exchanger 

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Hot Sale 500t D Edible Oil Mill with ISO Approved