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Liquid CO2 Generation Plant, Liquid CO2 Generator for Food Use,
| Price | $75000.00 |
|---|---|
| Min Order | 1 Piece |
| Availability | In Stock |
| Shipping From | Guangdong, China |
| Popularity | 278 people viewed |
Model NO.:
MK-EP2888
Application Fields:
Food, Food
Certification:
RoHS, ISO, CE
Condition:
New
Noise Level:
Low
Parts:
Gas Tank
Purpose:
Gas Manufacturing
Usage:
Hydrogen, Nitrogen, Oxygen, Ozone, CO2
Machine Size:
Large
Trademark:
Markevina or OEM
Transport Package:
Standard Export Carton Packing
Specification:
Customized
Origin:
China
Product Description
Liquid Air Separation Equipment,
Liquid Air generation system,
Air Generation Plant for Liquid CO2
Conditions
1.1 Design points of atmospheric conditions
Atmospheric pressure 100kPa (A)
Ambient temperature 32ºC
Relative humidity 80 %
Altitude 100m
Atmospheric oxygen content 20.95% O2
1.2 Atmospheric temperature
The annual average temperature 19.3ºC
Extreme maximum temperature 43ºC
Extreme minimum temperature -5ºC
1.3 Earthquake intensity
1.4 Impurity conditions of raw material air
CO2 ≤400 ppm
CH4 ≤5 ppm
C2H2 ≤0.5 ppm
CnHm £8 ppm
Mechanical impurities £30 mg/m3
1.5 Utility conditions
1.5.1 circulating water
The inlet temperature 32 ºC
The return water temperature
Inlet pressure 0.4MPa (G)
Outlet pressure 0.25MPa (G)
PH (pH) 7~8
Suspended matter content ≤20mg/L
Total hardness tendency 3.2 L
The fouling coefficient 1.72~3.44×10-4 m2.K /W
Cl ≤300 mg/L
Ca+ 30~200 mg/L
Petroleum ≤5 mg/L
1.5.2 Power supply conditions
High-voltage power 10KV±5%, AC three-phase
Low voltage power 380V/220V, AC three-phase four-wire system,the center point is directly grounded,frequency 60±0.5 Hz.
1.5.3 User's backup instrument air (for startup)
Pressure 0.5 Mpa (G)
Temperature £30 ºC
Dew point <35 ºC
Flow 300 m3 / h
Requirements without oil.
Annex II. Main Technical Performance of Air Separation Device
Note: 1. The data of liquid product is converted into gas state. Nm /h refers to 0ºC,760mmHg. (the same below)
Operation cycle (two large heating interval) ≥2 years
The heating thawing time of the device ~ 36 hours
The start-up time of the device (from the start of the expander until the oxygen product reaches the purity index) ~ 36 hours
2. The power consumption of the above products is as follows :(for reference, the order data shall prevail)
Liquid Air generation system,
Air Generation Plant for Liquid CO2
Conditions
1.1 Design points of atmospheric conditions
Atmospheric pressure 100kPa (A)
Ambient temperature 32ºC
Relative humidity 80 %
Altitude 100m
Atmospheric oxygen content 20.95% O2
1.2 Atmospheric temperature
The annual average temperature 19.3ºC
Extreme maximum temperature 43ºC
Extreme minimum temperature -5ºC
1.3 Earthquake intensity
1.4 Impurity conditions of raw material air
CO2 ≤400 ppm
CH4 ≤5 ppm
C2H2 ≤0.5 ppm
CnHm £8 ppm
Mechanical impurities £30 mg/m3
1.5 Utility conditions
1.5.1 circulating water
The inlet temperature 32 ºC
The return water temperature
Inlet pressure 0.4MPa (G)
Outlet pressure 0.25MPa (G)
PH (pH) 7~8
Suspended matter content ≤20mg/L
Total hardness tendency 3.2 L
The fouling coefficient 1.72~3.44×10-4 m2.K /W
Cl ≤300 mg/L
Ca+ 30~200 mg/L
Petroleum ≤5 mg/L
1.5.2 Power supply conditions
High-voltage power 10KV±5%, AC three-phase
Low voltage power 380V/220V, AC three-phase four-wire system,the center point is directly grounded,frequency 60±0.5 Hz.
1.5.3 User's backup instrument air (for startup)
Pressure 0.5 Mpa (G)
Temperature £30 ºC
Dew point <35 ºC
Flow 300 m3 / h
Requirements without oil.
Annex II. Main Technical Performance of Air Separation Device
- Yield and purity (out of bounds)
| Product Name | Output Nm/h | Purity (V/V) | Outlet pressure MPa(G) | Remarks |
| Liquid oxygen | 1500 | ≥99.6% O2 | Intake tank | continuation |
| Liquid nitrogen | 300 | ≤3ppm O2 | Intake tank | continuation |
| Liquid argon | 40 | ≤1.5ppm O2,≤4ppm N2 | Intake tank | continuation |
Operation cycle (two large heating interval) ≥2 years
The heating thawing time of the device ~ 36 hours
The start-up time of the device (from the start of the expander until the oxygen product reaches the purity index) ~ 36 hours
2. The power consumption of the above products is as follows :(for reference, the order data shall prevail)
| Serial NO. | Equipment | Motor power (rated power) | Shaft power under normal working conditions kW | Voltage grade | Remarks |
| Raw material air compressor | 850 | 784 | 10kV | ||
| Circulating air compressor | 1470 | 1330 | 10kV | ||
| Pre-cooling group | 55 | 41.9 | 380V | ||
| Low temperature Pre-cooling group | 75.4 | 75.4 | 380V | ||
| Molecular sieve purification system | |||||
| Electric heater | 126 | :45 | 380V | One use and one standby, discontinuous operation | |
| Expansion group | |||||
| Electric heater | 3 | 220V | discontinuous operation | ||
| oil pump | 2.2×2 | 1 | 380V | One use and one standby | |
| Average power consumption of air separation system (in axis power):2277.3 kW | |||||
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