Oil Industry Term

Knife Mixer 4.6.12 Crushing 2.5.5
Pour gas 3.2.20 Heat conducting oil 4.8.10
Thermal oil furnace 4.8.11 Road furnace 4.8.9
Drain gas 4.8.8 Low temperature condensation method 3.5.15
Low temperature desolvation 3.4.15 Dripping dry section 3.2.18.14
Iodine-hydrogen ratio 7.16 Iodine value 6.1.6
Gasket 2.3.11 Power consumption 7.11
E
Secondary press 2.1.4
F
Wind Pick 1.1.2 Wind Pick 1.1.10
Re-refining 4.6.20 Negative catalyst 5.1.6
Rich 3.5.24 Exhaust 3.5.25
Waste water cooking tank 3.5.11 Water separator 3.5.10
Dissolution 5.4 Molecular distillation 5.4.7
Powder degree 1.6.4 closed augers 3.2.18.1
G
Dry cake (ç²•) residual oil rate 7.4 Dry type catcher 3.4.14
Dry Brown Kernel Shell Separator 2.5.26 Drying Test 6.2.18
Glycerin 4.2.3 High-grade layer steaming offline 3.4.10
High moisture steam 1.7.7 Bow leacher 3.2.23
Solid Adsorption 3.5.17 Solid Impurity 4.2.16
Solid Grease Index 6.2.8 Scraper Oil Tank 4.3.2
Scraper Slurry Separator 2.5.24 Tubular Centrifuge 4.4.5
Tube stripper 3.3.12 Roller crusher 1.4.2
Filter 4.3.4 Filter Filament 4.1.7
Peroxide value 6.1.10
H
Nuclear residue separation 2.5.10 Nuclear residue separator 2.5.11
Nuclear residue separation screen 2.5.12 Constant position tank 3.3.9
Post-processing 5.1.12 After opening the door 3.2.18.11
Chemical refining 4.1.3 Ring extractor 3.2.25
Mixed Condensers 3.5.3 Mixed Condensers 3.5.7
Mixer 4.6.8 Mixed Leaching 3.2.5
Mixed Oil 3.3.1 Mixed Oil Treatment 3.3
Mixed Oil Tank 3.3.3 Hybrid Oil Filter 3.3.4
Hybrid Oil Refining 4.1.5 Mixed Oil Concentration 3.3.2
Mixing oil stripping 3.3.11 Mixing oil circulation pump 3.2.27
Mixing oil preheating 3.3.6 Mixing oil evaporation 3.3.6
Mixed steam 3.5.1
J
Mechanical refining 4.1.1 Mechanical vacuum pump 4.8.13
Extremely Hydrogenated 5.1.14 Oil Collector 3.2.18.7
Heating Test 6.1.14 Heat Dehydration 4.4.7
Heating coloring test 6.2.17 Pressurized hydrolysis method 5.3.2
False bottom 3.2.18.5 Batch alkali refining 4.6.3
Batch leaching 3.2.8 Batch hydrogenation 5.1.3
Intermittent hydration 4.4.2 Batch deodorization 4.8.2
Intermittent Press 2.1.1 Alkali 4.6.1
Pulp-plate mixers 6.4.10 Colloidal impurities 4.2.18
Arbor-type Shell Kernel Screen 1.3.14 Combined with Oil 3.2.15
Crystallization 5.4.1 Crystallizer 4.9.2
Desorption Tower 3.5.22 Feed Section 3.2.18.12
Leaching 3 Leaching Section 3.2.18.13
Leaching tank 3.2.18.4 Leaching tank 3.2.26
Leacher 3.2.17 Leacher shell 3.2.18.2
Leaching time 3.2.11 Leaching temperature 3.2.10
Immersion leaching 3.2.4 Refining 4
Refining rate 7.6 Refined oil 4.1.8
Standing sediment 4.4.6
K
Antioxidants 4.2.13 Shell Kernel Separation 1.3.10
Shell kernel separation screen 1.3.11 Shell containing kernel ratio 1.3.18
Mineral oil absorption device 3.5.20
L
Wax 4.2.9 Lipid 4.2.4
Refrigerated Recovery Unit 3.5.18 Refrigerated Testing 6.2.12
Centrifugal Sheller 1.3.8 Centrifugal Oil 2.5.8
Centrifugal Mixer 4.6.9 Theoretical Alkaline 4.6.4
Vertical Rolling Mill 1.6.1.1 Vertical Cooking Wok 1.7.2
Vertical steam drying machine 3.4.6 Continuous alkali refining 4.6.2
Continuous Leaching 3.2.9 Continuous Shell Kernel Water Separator 2.5.25
Continuous deodorization 4.8.4 Continuous deodorization equipment 4.8.6
Continuous Hydration 4.4.1 Continuous Press 2.1.2
Smelting 7.8 Burning acid price ratio 7.7
Tube condenser 3.5.5 Phosphate degumming 4.5.3
Phospholipid 4.2.8 Thiocyanate 6.1.7
Sulfuric acid degumming 4.5.1 Fluid bed dryer 1.2.5
Hexagonal sieve 1.1.6 Track leacher 3.2.21
Screw discharge decanter centrifuge 4.3.3 Spiral oil press 2.3
Screw shaft 2.3.4
M
Hair oil 4.1.6 Early oils 4.3
Coal consumption 7.10 gossypol 4.2.11
Disc 1.3.2 Grinding 1.3.3
Grinding seeds 2.4.4
N
Heat resistance test 6.1.15 Slurry water separator 2.5.23
Countercurrent leaching 3.2.13 Freezing point 6.2.7
Concentration difference 3.2.2
P
Disc mixer 4.6.11 Spray leaching 3.2.3
Spray Condenser 3.5.6 Spray Installation 3.2.18.6
Poor oil 3.5.23 Plate dryer 1.2.4
Flat bottom wok 1.7.5 Balance tank 8.5.9
Rotary leacher 3.2.18 Broken 1.4
Broken particle size 1.4.3 ç²• 3.4.1
ç²• processing 3.4 ç²• cooler 3.4.11
Separation at the end of the last 3.4.12 steam drying machine 3.4.4
Thickness 1.6.2
Q
Odor and taste 6.2.4 Steam consumption 7.12
Gas-liquid separator 3.3.10 Front door open type 3.2.18.10
Hydrogenation reactor tank 5.1.4 Hydrogenated oil 5.1.1
Clean up 1.1 Total oxidation number 6.1.19
Hydroxyl value 6.1.9
R
Burning point 6.2.15 kernel shell rate 1.3.17
Melting point 6.2.6 Solvent 3.1
Solvent ratio 3.2.1 Solvent residue 7.17
Solvent fractionation 5.4.2 Solvent recovery 3.5
Solvent loss 7.14 Solvent preheater 3.2.28
Solvent steam 3.5.4 Solvent turnover tank 3.2.29
Solubility Test 6.2.16 Emulsification Fractionation 5.4.3
Emulsification phenomenon 4.4.10 into the squeeze (immersion) conditions 2.1.5
Soft bean box 1.5.1 softens 1.5
Softening pan 1.5.2 Resau-Mesh and Pollensk value 6.1.12
Wet steaming 1.7.6
S
Pigment 4.2.14 Color 6.2.3
Bacterial can 2.5.2 Screening 1.1.1
Flash point 6.2.14 Flash evaporation system 3.4.16
Upper steam 3.2.26.2 Penetration 3.2.12
Embryo 1.6.3 Wet separation 2.5.22
Wet ç²• 3.4.2 Wet ç²• æº¶ 3.4.3
Wet trapper 3.4.13 Edible hydrogenated oil 5.1.2
The actual compression ratio 2.3.17 by the rolling embryo 2.1.6
Mature embryo 1.7.1 Two-stage spiral oil press 2.3.2
Water method to take oil 2.4 water seal pool 3.5.26
Water consumption 7.13 Hydration 4.4
Hydration Tank 4.4.3 Water Jet Vacuum Pump 4.8.15
Washing 4.6.13 Washing machine 1.1.12
Mixing and stirring the oil 2.4.5 Water selection 1.1.4
Acid hydrolysis 5.2.3 Acid refining tank 4.5.2
Sourcing Mixer 4.5.4 Acidic Degumming 4.5
Acid value 6.1.1 Random ester-ester interchange 5.2.5
T
Sugar 4.2.7 Twicher Act 5.3.1
Packing absorber 3.5.21 Transparency 6.2.2
Dewaxing 4.9 Deodorizing 4.8
Deodorization tank 4.8.3 Detoxification 2.5.3
Decolorization 4.7 Decolorization tank 4.7.3
Decolorization Tower 4.7.4 Deacidification 4.6
Spring Rolling Mill 1.6.1.4 Cake Turning Device 2.3.14
Adjust steamer 1.7.3 Carbonyl value 6.1.13
W
Wesson loss 7.9 Vitamin E 4.2.12
Exhaust 3.5.13 Exhaust gas recovery 3.5.14
Tail gas condenser 3.5.19 Stability test 6.1.1
Horizontal Filter 4.3.9 Horizontal Cooking Wok 1.7.4
Horizontal steam drying machine 3.4.5 Physical and chemical refining 4.1.4
Physical refining 4.1.2
X
Aspirator 4.8.5 Suction Screen 1.1.9
Adsorbent 4.7.2 Adsorption and Decoloration 4.7.1
Washing-drying tank 4.6.17 Pressing down 3.2.26.1
Fiber residue 2.5.13 Box filter press 4.3.7
Unloading ç²• 3.2.26.3 Accumulator 2.2.4
Hydrocyclones 3.3.5 Selective hydrogenation 5.1.13
Y
Cake Press 2.2.3 Filter Press 4.3.5
Compression ratio 2.3.15 Press 2
Press method oil 2.1 Smoke point 6.2.13
Salting 4.4.11 Smoke 2.4.2
Oxidation acid value 6.1.17 Crystal tank 4.9.3
Liquid-liquid extraction 5.4.4 Liquid absorption 3.5.16
Hydraulic press method 2.2 Hydraulic rolling mill 1.6.1.3
Hydraulic Oil Press 2.2.1 One Press 2.1.3
Acetyl value 6.1.8 Total oil loss 7.5
Alkali ratio ratio 4.6.7 Oil foot 4.2.21
Oil shelling 1.3 Oil drying 1.2.2
Oil moisture regulation 1.2 Oil peeling 1.3.15
Oil Humidification 1.2.1 Oil Humidifier 1.2.3
Oil Road 2.1.7 oil to oil ratio 7.15
Oil shielding pump 4.8.12 oil to oil ratio 5.1.10
Hydrogen separation 5.1.11 Oil residue 4.2.20
Fat 4.2.1 Fat Accompanying 4.2.5
Chemical properties of greases 6.1 Physicochemical properties of greases 6
Physical properties of grease 6.2 Grease upgrading 5.2.7
Grease & Grease Accompaniers 4.2 Grease Processing 5
Grease Leaching 3.2 Grease Refinery 4.1
Oil Hydrogenation 5.1 Oil Hydrolysis 5.3
Oil palm fruit smashing can 2.5.6 Oil palm processing 2.5
Oil Palm Bacteria 2.5.1 Free Fat 3.2.14
Free fatty acid 4.2.19 Free fatty acid content 6.1.2
Pretreatment 1 Pre-pressed cake 3.2.16
Pre-press leaching 3.2.7 Pre-pressed screw press 2.3.3
Disc Sheller 1.3.1 Disc Filter 4.3.8
Cylindrical sieve 1.1.8
Z
Saponification value 6.1.4 Soap 4.2.22
Soap foot tank 4.6.18 Total compression ratio 2.3.16
Flame arrester 3.5.27 Ester-ester interchange 5.2.4
Esterification 5.2 Transesterification 5.2.1
Ester value 6.1.5 Zenis refining method 4.6.19
Embryo 1.6 Chromating Machine 1.6.1
Roller 1.6.1.5 Rolling distance adjusting mechanism 1.6.1.6
Pressing cage 2.3.8 Pressing screw 2.3.6
2.3.10 pressing circle 2.3.13
Squeegee knife 2.3.12 Press bar 2.3.9
Pressing shaft 2.3.5 tent filter 3.2.18.9
Refractive index 6.2.5 Vacuum drying 4.6.14
Vacuum Dryer 4.6.15 Vacuum Rotary Filter 4.9.4
Penetration 6.2.9 Shake oil 2.4.6
Steamed 1.7 Distillation 5.4.5
Steam distillation deodorization 4.8.1 Steam jet vacuum pump 4.8.14
Whole kernel rate 1.3.19 Fatty acid 4.2.2
Fatty Acid Distillation 5.4.6 Fat-Soluble Impurities 4.2.17
Fatty Acid Freeze Point 6.2.10 Direct Leaching 3.2.6
Neutralization tank 4.6.16 Neutralization value 6.1.3
Neutral oil recovery 4.4.9 Co-catalyst 5.1.7
Filter aids 4.7.5 Rotor 3.2.18.3
Cloud point 6.2.11 Seed shell separation 1.3.12
Seed shell separator 1.3.13 Automatic material gate 3.4.9
Free Gas 3.5.12 Palm Fruit Remover 2.5.4
Brown Core 2.5.17 Brown Core Shelling 2.5.19
Brown core shell, grade and separation of kernels 2.5.20 Brown core shell grade grading sieve 2.5.21
Brown kernel 2.5.18 Brown kernel oil 2.5.27
Preparation of palm kernel oil 2.5.16 Palm oil centrifuge 2.5.9
Palm oil 2.5.7 total alkali production 4.6.6
DTDC steam drying machine 3.4.8 DT steam drying machine 3.4.7
P-anisidine value 6.1.18 U-shaped extractor 3.2.22
Y-shaped leacher 3.2.24

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