Oil Extraction Plant for Burma Cusotmer

Oil Extraction Plant for Burma Cusotmer

Standard Info

Model No.: 100-6000t/d

Item Description
Vegetable Oil Extraction Line
Significant Products: extractor, desolventizer-toaster with built-in dryer-cooler, unfavorable force evaporator, horizontal stainless pipe bundle condenser, filtering system for getting rid of food foam from miscella, technique for recycling solvent from exhaust gasoline, circulating technique for separating h2o from solvent, electrical handle system
Applicable Raw Supplies: soybeans, rapeseeds, cottonseeds, peanuts, sunflower seeds, corn germs, rice bran, palm fiber (palm food)
Creation Capability:100-six,000t/24h raw resources
Approach Workflow

Oil Extraction Area → DTDC CZPTlventizer Toaster Dryer Cooler → Oil Filtration Area → Evaporation and Separation Area → Solvent Condensation and CZPTvery Program → Paraffin Absorption Program → Drinking water Solvent Separation and CZPTvery System → Computerized Manage Method

(one) Oil Extraction Area
CZPTers can select rotocel extractor or drag chain extractor based on their needs. For different uncooked components, grid trays clearance and grid trays arrangement will be appropriately modified to ensure that the oil residues in seed food is bare minimum. In addition, liquids in seed food will be totally drained off, which contributes to minimum solvent material. As a consequence, the burden imposed on desolventizing unit in sequential process will be tremendously alleviated, which additional minimizes steam intake.  

 

(two) DTDC CZPTlventizer Toaster Dryer Cooler

The equipment is composed of pre-desolventizing layer, heat trade layer, desolventizing layer, warmth recovery layer, drying layer and cooling layer. Materials levels at every single layer can be routinely managed. Full utilization of secondary steam lowers steam consumption. Combined steam will be employed to heat miscella following food foam removing, which additional saves strength. The approach features comprehensive desolventizing, light-weight yellow meal, total passivation of antinutritional aspects, limited time needed for high temperature desolventizing and low reduction of food NSI.

  

(3) Oil Filtration Part

The approach is developed to filter out sound impurities prior to miscella evaporation. Units utilized consist of high stress supply pump, centrifugal separator and filter with slagging function. The best possible filtration impact can be achieved by mixture of centrifugal separation precise filtration. Because the filter is capable to remove slags routinely, no guide operation is needed.

 

(four) Evaporation and Separation Segment

Devices utilised in the procedure is made up of evaporator, disc stripping tower, flash separator, warmth exchanger and vacuum device. Below a vacuum and adverse force condition, solvent in the miscella will be evaporated and separated by climbing film evaporation and immediate stripping. Following extensive desolvation, vivid colour leached oil will be acquired. To guarantee program balance and trustworthiness, an computerized PLC handle system is adopted for handle of evaporating temperature and vacuum stage. Equally mixed steam and energy steam for vacuum pump will be sufficiently employed for evaporation. Warmth transfer and mass transfer in between amazing and hot medium furthers minimizes steam usage. In addition, lipid oxidation can be prevented as effectively.

 

(5) Solvent Condensation and CZPTvery Technique
The method primarily is composed of condenser and circulating cool h2o system. Underneath the vacuum problem, condensable solvent steam is condensed into liquids for cyclic utilization via dividing-wall warmth transfer. Several-pass structure of the condenser and appropriate settings of flow charge and pace of circulating water will greatly enhance efficiency of condensation and separation and largely lowers expenditure cash and working price. In addition, tube plates, baffle plates and warmth exchange tubes are all made of stainless metal, which amenities cleansing and withstands corrosion. In addition, excellent condensation influence and lengthy services lifestyle can be completely ensured.

 

(6) Paraffin Absorption Program

The method consists of Paraffin absorption column,Paraffin desorption column,listen to exchanger,storage tank, punp,Exhaust fuel blower and so on. It is capable to recycle more than 98 percent solvent in the exhaust gas, which reduces solvent decline and shields setting at the very same time.
The program tends to make use of foodstuff-grade liquid paraffin to adsorb solvent gas combined in exhaust gas. The solvent steam will be distilled and separated with the help of superheated steam. Then the solvent steam attained will be recycled through condensation. To ensure stable absorption performance and program dependability, automated handle units are used to handle essential parameters this sort of as stream charge, temperature and stress.

 

(seven) H2o & Solvent Separation Area

The technique is made up of solvent-water separator, boiling tank,and new solvent pump. It separates drinking water from solvent based on the basic principle that drinking water repels solvent and two liquid levels will be formed in their combination. To make sure steadiness and reliability of the system, automatic management devices are applied to control critical parameters this sort of as flow rate, temperature and substance degree.

(8) Computerized Handle Method

In our production lines, we make use of Siemens PLC management program, which is a single of mainstream computerized handle programs in today`s sector. The effective, secure and superior DCS handle system is composed of procedure station, handle station and interaction community. We employ high-pace and large-potential S7-400 collection PLC at the control method, big-display screen Lcd at the operation station, WINCC seven. industrial manage application as monitoring software and PROFIBUS filed bus network for communication.

   We also give the subsequent undertaking and gear:

Oilseed Pretreatment Project
Oilseed Pressing Task
Oil Extraction Task
Oil Refining Project 
Cottonseed Miscella Refining Project
Minimal Temperature and Edible Soybean Meal Project
Soy Protein Concentrate Undertaking
Soy Protein Isolate Undertaking
Entire Fat Soybean Powder Venture
ASME Force Vessel 
ASME Heat Exchanger 

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Oil Extraction Plant for Burma Cusotmer