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30TPD rice bran oil machine
Fatty acid |
Percentage |
Myristic acid |
0.6% |
Palmitic acid |
21.5% |
Stearic acid |
2.9% |
Oleic acid |
38.4% |
Linoleic acid |
34.4% |
α- Linolenic acid |
2.2% |
1. Rice Bran Pretreatment Workshop
Rice bran→Magnetic separation→Cleaning
→Extrusion Puffing →Countercurrent drying
2. Rice Bran Solvent Extraction Workshop
Material embryos→Extraction→Wet meal→Evaporation→Cooling→Product meal packing-
Mixed oil→Filter→Negative pressure evaporation → Crude oil -Solvent recovery
3. Crude Rice Bran Oil Refining Workshop
crude oil---1.phosphoric acid degumming ,washing,drying---2.dewaxing---3.first time decolorization---4.AB twin towers physical deacidification--- 5.alkali refining---6.second time decolorization---7.eacidification,deodorization---8.derosination ---finished product(8section).
Producing grade-1 and grade-2 oil use physical-chemistry 1-8 sections.The grade-3 and grade-4 oil only need full-physical 1--4 section.
4.Refined Rice Bran Oil Dewaxing Workshop.
Technical parameters
Expansion workshop main parameters
1,Designed processing capacity rice bran :100T/D(ton/day)
2,rice bran quality
a moisture 11-13% b impurity≤2% c oil 15-20% d bulk density 320 kg/m3
3,Economic and technical index
a power consumption:24.5kwh/T b steam consumption:180kg/T c water consumption:80Kg/T
Extraction workshop main parameters
1,Designed processing capacity
a,rice bran expansion material 100T/D
b,extracting moisture for the expansion material : 7—9%
c,material temperature: 55—65℃
2,Technical performance index
a residual solvent in meal: ≤500ppm(qualified detonate test)
b moisture in meal: ≤12-13% c residual oil in meal: ≤1%
d residual solvent in crude oil: ≤300 ppm e total volatile of crude oil: ≤0.2%
3,technological and economic index
a solvent consumption: ≤2kg/T b power consumption : 28.5kw.h/T
c steam consumption : 400kg/T d water consumption : 250KG/T
e circulating water : 45m3/T
Refining workshop main parameter
1,Designed processing capacity crude oil:20T/D
2,Crude oil under 20 acid value adopt a method that combines firstly physical process then chemical process to produce first grad oil.Crude oil of 20-30 acid value will be used to produce two grad oil.Above 30 acid value adopt full physical refining to produce three and four grad oil.
3,technological and economic index
a acid value≤15.0-60.0mgKOH/g b Moisture and volatile≤0.5%
c impurity:≤0.5% d wax:≤5%
4,techno-economic index
a steam consumption ≤680kg/T oil b power consumption ≤75watt/T oil
c water consumption 200Kg/T oil(soft water) d Phosphate dosage 2-3 Kg /T oil
e citric acid dosage 1 Kg / T oil f Alkali dosage acid value×1 Kg/T oil
g Clay dosage 40~60 Kg / T oil h Circulating cooling water dosage about200M3/h
5,refining loss index:
a Degumming loss= gel content %×1.4
b Acid stripping consumption for chemical refining=FFA%×1.5,
Acid stripping consumption for physical refining=FFA%×1.2
c decolorizationconsumption =Clay dosage×30%
d Deodorization consumption ≤0.5%
e Dewaxing consumption: Wax paste oil concentration 50%
f Refining rate: 1refining loss %
Welcome to
-- Henan Huatai Cereals & Oils Machinery Co., Ltd.
-- Covers100,000.00 square meters and have more than 580 staffs
-- Located in the Industry cluster of Huaxian, Henan Province
-- Specialized in researching, designing, manufacturing, installation
-- 22 items national patents, 6 international prizes, etc.
-- Our equipments have got ISO9001, SGS, CE, IAF and CNAS certifications.
-- Oversea customers include Bolivia, Sudan, Kazakhstan, Russia, Tajikistan,
Malaysia, Indonesia, Bangladesh, Egypt, Vietnam, Thailand, Burma, etc.
Factory Base
1. Ensure to timely provide complete sets of equipment and accessories.
2. Ensure that one-time installation debugging acceptance.
3. To provide high quality material with preferential price.
4. Priority to provide customer our new craft works and products.
5.In the installation process, we will appoint a installation supervision staff on the spot.
6. On-line debugging and Feeding trial operation.
Customer Visiting
The followings are the equipments of our company:
Main Projects Scope:
-----30-5000T/D oilseeds pretreatment project
-----30-5000T/D oilseeds extraction project
-----10-500T/D crude oil refining project
-----10-500T/D crude oil fractionation project
-----Oil interesterification project
-----Oilseeds protein, phospholipid project
-----Natural pigment extraction project
-----Grain deep processing project
Typical Project:
----30-1000T/D rice bran pretreatment, expanding, extraction project
----30-600T/D rice bran oil refining project
----150-1000T/D cottonseed dephenolizing protein
----10-1000T/D palm fruit oil pressing project
----10-500T/D Non acid method biodiesel production project
----10-2000T/D corn deep processing project
Newest Technology:
---Energy saving oil vacuum deodorization technology
---Concentrated protein extraction technology
---Mixed oil extraction technology
---Mixed oil refining technology
---Molecular distillation technology
---Broken rice desaccharification technology
---Continuous lignite extraction technology
Please feel free to contact with me!
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