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Full Auto Sludge Dryer Vedio 230813

10 month ago
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Product details

Continuous Heat Pump Drying Machine for Petroleum Sludge

Innovative Technology of Loren LCPD Series Low Temperature Continuous Dryer

-Solve Technical Bottlenecks Between Frosting And Poor High Temperature Performance

-Dehumidification Performance Ratio: (SMER) 3kgs.HO2/KW.H

-Patent for Intermediate Heat Exchange Cooling Dehumidification

-Patent for Temperature Echelon Utilization Technology

-Patent for Double-effect, Triple-Effect Dehumidification Technology

-Larger Dryer Temperature range:From 15-80with Intake Temp. 95to meet Cool Air Drying, Heat Air Drying and Alternative Cool and Hot Air Dehumidification

-Adopts Advanced Refrigerant Recovery Technology Improve Compressor Cooling Efficiency to Save Running Cost by way of Energy Saving Machine to exchange the Low Pressure Air with High Pressure Air to heat the low pressure air and cool the refrigerant liquid

-Module Design to fit for upgrading and maintenance

-PLC Intelligent Control of single or multiple sets together with Remote Control

-Widely Applicant Field of industrial, ETP, food and Pharmacy etc.

Definition of Batch Hot Pump Dehumidification Machine for Research Center

It Is a Device That Uses The Refrigeration System To Cool And Humidify

The Hot And Humid Air While Recovering The Air Moisture By The Heat

Pump Principle To Condense The Latent Heat.
Dehumidification Heat Pump = Dehumidification Drying+ Heat Pump (Energy Recovery) Combined

A. Dehumidification

The Moisture Contained In The Air Is Different Under Different Working Conditions. When The Air Cools Down, The Water Vapor In The Air Gradually Condenses And Reaches a Saturated State. When The Dew Point Of The Air Continues To Decrease, The Water Vapor In The Air Becomes Condensed Water And Precipitates, So That The Absolute Water Content In The Air Is Reduced. Air Achieves The Dehumidification Process

B. Condensation

It Is The Gas That Turns Into a Liquid When It Is Cold, Such As Water Vapor Turns Into Water Condensation Heat - The Latent Heat Of Phase Change Refers To The Heat Absorbed Or Released From One Phase To Another By a Unit Mass Of Material Under Isothermal Isostatic Conditions. Solid, Liquid-Melting Heat (Or Solidification Heat), Liquid, Gas-Vaporization Heat (Or Condensation Heat), Solid, Gas-Sublimation Heat (Or Condensation Heat)

2424KJ/kg at -30; 2355KJ/kg at 60and 2258KJ/kg at 100

The Final Applicant of Dyed Sludge Particles Can Be Used As

-Fertilizer

-Fuel

-Incineration

-Building Materials

-Bio Fuel

-Landfill Covering Soil

-Land Utilization Etc.

Feature of Loren Heat Pump Sludge Dehumidifier For Semiconductor Processing

-Closed Loop Drying Design Save 50% Energy with No Exhausted Gas or Heat Loss

-Our Heat Recovery Cycle Patented Technology Fit For High Temp. & Low Humidity Drying Process.

-The higher The Temperature, The Higher The Dehumidification Performance SMER (kg.H20/kw.h) Ratio;

-Continuous Mesh Belt Drying Mode, Suitable For Various Types Of Sludge Drying Systems (Including Sludge With Large Sand Content) To Have  Long Service Life

-Sludge Slitting And Crushing Patented Technology by Using Different Paving Modes As per The Solid Content Of Sludge

-Low Temperature (40-75) Fully Enclosed Drying Process, No Tail Gas Discharge, No Need For Odor Treatment System; Low Temperature Drying Can Fully Avoid The Volatilization Of Different Types Of Organic Compounds In The Sludge And Avoid The Volatilization Of Odorous Gases (Chain Alkanes The Volatilization Temperature Of Aromatic Hydrocarbons Is 100-300, The Volatilization Temperature Of Cycloalkanes Is Mainly 250-300, The Volatilization Temperature Of Nitrogen-Containing Compounds, Amines, Oximes Is Mainly 200-300, Alcohols, Ethers The Volatilization Temperature Of Aldehydes, Aliphatic Ketones, Amides And Nitriles Are All Above 300. In Addition, The Volatilization Temperature Of Aldehydes And Anilines Is Mainly At 150, And That Of Lipids Is At 150-250);

-The System Is Safe To Operate, Has No Hidden Danger Of Explosion, And Does Not Need Nitrogen Flushing Operation; The Oxygen Content Of The Sludge Drying Process Is <12%, The Dust Concentration Is <60g/m3, The Particle Temperature Is <110°c, And The Whole Drying Process Is Dust-Free (Air Velocity < 2 m/s);

-The Mesh Belt Transmission Speed Is Controlled By Frequency Conversion, And The Moisture Content Of The Sludge Discharge Is Adjustable (10-30%)

-Small Footprint: 3.5 Square Meters Per Ton Water Evaporation

--Removal Water 3 kg per 1 degree Electricity Consumption

- No Pollutant Discharged Out

-No Noise Contamination

-Globally No Influenced By Outside Temperature and Circumstance Change

-Moderate and Low Temperature Drying Yield Out Better Quality Dry Sludge

-The Sanitation Condition of Drying Process is Excellent

-Fit for Inert Environment Changes,

-Fit For Inflammable & Explosive, Volatile And Toxic Materials Occasions

-Ventilation Temperature Can Reach 95

- PLC Touch Screen Control

-Lower Investment and Lower Maintenance Charge 

Working Principle

Utilizing The Dehumidification Principle Of The Low-Temperature Heat Pump, The Sludge Is Dried By Convective Hot Air, So That The Moisture In The Material Absorbs Heat And Evaporates Into The Air To Achieve The Purpose Of Reducing The Moisture Content. It Use The Refrigeration System To Cool The Hot And Humid Air Below The Dew Point To Precipitate Moisture, And Then Heat The Air Through Multiple Heat Recovery Technologies To Keep The Moisture In The Sludge Evaporating,

Evaporation-Dehumidification-Heating-Evaporation-Re-Dehumidification,

In Fact It Is Equal To The Organic Combination Of Dehumidification Heat Pump + Heat Recovery Technology + Material Delivery System.

Applicant

-Municipal Sewage Treatment Plant

-ETP , STP

-Chemical Factory

-Pharmaceutical Factory

-Paper Making Factory

-Dyeing and Printing

-Leather Processing

-Electric Plating Plant

-Food Processing

-Landfill

-Dangerous or Harmful Sludge


Model Selection & Specification Table   

 Low Temperature Continuous  Heat Pump Sludge Drying Machine

Model

Daily Water Removal Volume

(Ton)

Hour Water Removal Volume

(M3)

Overall Dimension L*W*H

(M)

Total Drive Power

(kw)

Inlet Sludge Moisture %)

Output Sludge Moisture %)

LCPD-1.5

1.5

1.00

5.0*3.6*3.4

17

70-85

10-50

LCPD-2.0

2.0

1.34

5.5*3.8*3.4

23

70-85

10-50

LCPD-3.0

3.0

2.00

6.5*3.8*3.4

34

70-85

10-50

LCPD-4.0

4.0

2.67

7.0*4.0*3.4

45

70-85

10-50

LCPD-5.0

5.0

3.33

8.5*4.0*3.4

56

70-85

10-50

LCPD-6.0

6.0

4.00

8.5*4.2*3.4

67

70-85

10-50

LCPD-8.0

8.0

5.33

10.5*4.2*3.4

89

70-85

10-50

LCPD-10

10

6.67

13*4.2*3.4

112

70-85

10-50

LCPD-12

12

8.00

15*4.2*3.4

134

70-85

10-50

LCPD-16

16

10.67

20*4.0*3.4

178

70-85

10-50

LCPD-20

20

13.33

20*4.06*3.4

223

70-85

10-50


Different Dry Sludge Quantity Table Under Different Moisture

Sludge Moisture(%)

Sludge Volume Per Ton ( M3)

Sludge Moisture(%)

Sludge Volume Per Ton ( M3)

99.9

200

60

0.5

98

10

50

0.4

90

2

40

0.33

85

1.33

30

0.29

802

1.0

20

0.25

70

0.67

10

0.22

60

0.5

5

0.21



 

 

 

 

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