Henan, China
Business Type:
Manufacturer/Factory & Trading Company
Number of Employees:
38
Year of Establishment:
2010-08-04
Management System Certification:
ISO 9001, ISO 14001
Average Lead Time:
Peak season lead time: one month
Off season lead time: within 15 workday
OEM/ODM Service

Recycling Waste Oil, Oil Distillation Plant, Distillation Plant manufacturer / supplier in China, offering 10ton Continuous Oil Distillation Plant Saving Fuel Energy, Waste Tyre Recycling to Oil Energy Continuous Pyrolsyis System, Sludge Oil Refining Gasification Continuous Pyrolysis Plant and so on.

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10ton Continuous Oil Distillation Plant Saving Fuel Energy

Get Latest Price
Min. Order / Reference FOB Price
1 Set US $45,000-65,000/ Set
Port: Lianyungang, China
Production Capacity: 25sets
Payment Terms: L/C, T/T, D/P, Western Union, Paypal, Money Gram, cash
Structure: Fixed
Usage: Oil Impurities
Type: Distillation
Mechanical Principle: Vacuum
Performance: Automatic
Plant Name: 10ton Continuous Oil Distillation Plant Saving Fue

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Basic Info

Model NO.: xhzl-10
Input: Crude Oil Sludg/Waste Oil
Output: Diesel /Gasoline
Heating Way: Direct Heating /Indirect Heating
Working Area: 500 Square Meters
Total Weight: 25 Ton
Cooling Way: by Water Cooling
Power: 15 Kw
Water Consumption: 200kgs
Trademark: XHZT
Transport Package: Reinforce Pack
Specification: XHZL-10
Origin: Shagnqiu, Henan, China
HS Code: 84198990

Product Description

10ton Continuous Oil Distillation Plant Saving Fuel Energy1. Work Flow
1) Pumping the feedstock into the sedimentation tank 1# and 2#, adding some catalyst, injecting the air by compressor into the sedimentation tanks for making the feedstock and catalyst mixed well, sedimentation quietly for 5hours.

2) After sedimentation, discharging the sediment, pumping the feedstock after sedimentation into distillation kettle.

3) Starting the high-temp circulated oil pump for distillation and the heating furnace, the feedstock will be heated during distillation kettle and furnace, when they reach the distillation cuts temp, through the rectifying tower into the oil-gas cyclone sedimentation tank for separating the ash, then into the oil-gas condenser and getting the diesel and gasoline separately stored.

4) The part of non-condensable gas into the vacuum buffering tank, vacuum pump, water seal, back fire device and into the heating furnace for supplying heat.

5) When there is "low" alarming on the liquid level, it should start to pump the feedstock (after sedimentation in tank 1# and 2#) into the distillation kettle, the whole distillation process is continuous.

6) When there is no alarming on the liquid level, but the diesel color is very dark, it shows there is much more residual oil in the distillation kettle and should discharge, then put into the residual oil tank.
1) Pumping the feedstock into the sedimentation tank 1# and 2#, adding some catalyst, injecting the air by compressor into the sedimentation tanks for making the feedstock and catalyst mixed well, sedimentation quietly for 5hours.

2) After sedimentation, discharging the sediment, pumping the feedstock after sedimentation into distillation kettle.

3) Starting the high-temp circulated oil pump for distillation and the heating furnace, the feedstock will be heated during distillation kettle and furnace, when they reach the distillation cuts temp, through the rectifying tower into the oil-gas cyclone sedimentation tank for separating the ash, then into the oil-gas condenser and getting the diesel and gasoline separately stored.

4) The part of non-condensable gas into the vacuum buffering tank, vacuum pump, water seal, back fire device and into the heating furnace for supplying heat.

5) When there is "low" alarming on the liquid level, it should start to pump the feedstock (after sedimentation in tank 1# and 2#) into the distillation kettle, the whole distillation process is continuous.

6) When there is no alarming on the liquid level, but the diesel color is very dark, it shows there is much more residual oil in the distillation kettle and should discharge, then put into the residual oil tank.

1) Pumping the feedstock into the sedimentation tank 1# and 2#, adding some catalyst, injecting the air by compressor into the sedimentation tanks for making the feedstock and catalyst mixed well, sedimentation quietly for 5hours.

2) After sedimentation, discharging the sediment, pumping the feedstock after sedimentation into distillation kettle.

3) Starting the high-temp circulated oil pump for distillation and the heating furnace, the feedstock will be heated during distillation kettle and furnace, when they reach the distillation cuts temp, through the rectifying tower into the oil-gas cyclone sedimentation tank for separating the ash, then into the oil-gas condenser and getting the diesel and gasoline separately stored.

4) The part of non-condensable gas into the vacuum buffering tank, vacuum pump, water seal, back fire device and into the heating furnace for supplying heat.

5) When there is "low" alarming on the liquid level, it should start to pump the feedstock (after sedimentation in tank 1# and 2#) into the distillation kettle, the whole distillation process is continuous.

6) When there is no alarming on the liquid level, but the diesel color is very dark, it shows there is much more residual oil in the distillation kettle and should discharge, then put into the residual oil tank.
10ton Continuous Oil Distillation Plant Saving Fuel Energy

2.Specification
NO.NameParameter
1The raw materials:Fuel oil /waste machine oil / transformer oil/waste lube
2Out putBase oil
3Daily capacity:10ton /day
4The size of reactor(L*W*H)4000*2200*2500m
6.Reactor materialQ345R
7.Final oil out rate75-85 %
8.Feeding waycontinuous
9Slag outAuto continuous
10Working area500-600 square meters
11Cooling wayBy water
12.Heating wayDirect/indirect
13Working presureNormal/slightly negative
14Effective working temperature200-400ºC
15Power15kw
16voltage220v/380v
17Fuel to heatingCoal wood, gas oil, etc
18typePollution free
19.certificateCE.ISO

10ton Continuous Oil Distillation Plant Saving Fuel Energy
3.Major parts
a.Reactor
b.Catalyst tower
c.Heat exchanger
d.Pipe condenser
e.condenser
f. filter
g. Pipe combination cooling pool
h. Light component oil collection tank
i. Middle component oil collection tank
j. Vacuum device
k .Residue oil tank
l. Smoke dust disposal device
Include strong spray tower,draft fan,activated carbon absorption tower,recycle purify water pool
m .Filter sand filter
n .Water sealing
o .Stirring tank
p. Operation platform
q .Power distribution cabinet
r. Other attachment

10ton Continuous Oil Distillation Plant Saving Fuel Energy
4.Plant Featurs:
A. ).Continuous operating for 90 days without coking.
B) .Latest tubular heating system which can save fuel 20--30%.
c).All sealed and auto feeding and slag discharging system, available in 350degree temperature condition.
d) This model is for processing waste engine oil into diesel oil.
E).The output should be above 90%, water percent affect the data obviously.
Our distillation machine can distillate the flowing materials, turn the waste to energy.
-  Fuel oil extracted from waste plastics and scrap rubber.
-  Waste engine oil.
-  Waste raw oil.
-  Waste washing oil.
-  Waste oil, Raw oil.
-  Waste lubricating oil.
F ) .Increase oil yield 5% compared to the similar plant, oil yield rate reaches to 80%.
G). Unique condensers and vacuum device makes our pyrolysis oil distillation machine highly efficient.
H )  Advanced device and design to make sure the distillation process is proceeding in a total environmental and safe surrounding.
i) . Multiple methods to eliminate color and odor of the distilled oil which ensures the final oil is of high quality.
J). The complete set of unit produce no smoke and no smell.

10ton Continuous Oil Distillation Plant Saving Fuel Energy
5. OIL  PARAMTER AFTER DISTILLATION
ProjectDieselStandard
Oxidation stability2.2≤2.5mg/100ml
Sulfur content(%)0.3M/m ≤0.2
10% steamed residual  carbon residue (%)0.33M/m ≤0.3
Ash content (%)0.16%M/m ≤0.01
Water content (%)traces/
Mechanical impurities//
Density (G/ML)0.850.83-0.87
Solidifying point(ºC)-100
Flash point (closed )(ºC)4555
Movement viscosity3.5(20ºC ) mm2/s
3.0-8.0
Combustion value(Kcal)95008500
Colority1.2≤3.5
Cetane number4045
Acidity/Mgkoh/100ml≤7

10ton Continuous Oil Distillation Plant Saving Fuel Energy











 

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