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Ultrafiltration machine instruction manual ARDLF8-40

Operation Manual – Ceramic Membrane Filter (ARDLF8-40)

CONTENT

  1. Safety precautions
  2. Components
  3. PID and 2D drawing
  4. System operation
  5. Use and maintenance
  6. Troubleshooting
  7. Appendix

Read this operating manual before performing any operation.

I: Components

1. Component List

Item No.NameSpecificationMaterialAmount
I. Filter    
1SS casingDQSH-301200-3SS304/3162 pcs
2Membrane elementCM3019041200/20nmceramics6 pcs
II. Pump (explosion-proof motor)    
1CADLF8-401.5kwSS304/3161 pc
III. Tank    
1Cleaning tank100LSS304/3161 pc
IV. Instruments    
1FlowmeterConcentrate: 1.6-16m³/h / FI01SS304/3161 pc
2FlowmeterPermeate: 40-400L/h / FI02Glass1 pc
3Pressure gauge0-1MPa / PG01,PG02SS304/3162 pcs
4Temperature meter0-150℃ / TG01SS304/3161 pc
V. Valve System    
1Filter valveV01-02SS304/3161 lot
2Cleaning valveCV01-03SS304/3161 lot
3Permeate valvePV01-04SS304/3161 lot
4Drain valveDV01-04SS304/3161 lot
5Pressure adjustment valveFV01SS304/3161 pc
6Vent valveVV01SS304/3161 pc
7Sampling valveconcentrate+permeateSS304/3162 pcs
VI. Control System    
1control PanelExplosion proof 1 pc
2Accessories  1 set
VII. Pipeline System    
1Security filterStyle YSS304/3161 pc
2Heat exchanger0.5m²SS304/3161 pc

2. Ceramic Membrane Module

2.1 3 elements/SS housing; 2 housings in series 2.2 Ceramic membrane element:

Item No.SpecificationPore size
DARQCM30-19-4*1200mmOD: 30mm ID: 4mm Channel: 19 Length: 1200mm20nm

2.3 Membrane element assembly: (see appendix 5: membrane assembly instruction)

3. Control Panel

  • 3 phase, 220V, 60HZ, Explosion proof (see appendix 1: terminal diagram for CMF3-2/M)

II: PID and 2D drawing

(see appendix 2: PID diagram/process appendix 2: 2D drawing)

III: System Operation

1. Operating Conditions

ItemDescriptionParameterItemDescriptionParameter
Membrane area0.286m2 * 6 Min. circulation volume40 L 
Working temperature5-80℃ pH0-14 
Working pressure0—4bar Work environmentinteriors 

2. System Control

  • Pressure regulation: FV01
  • System control panel: start/stop button NOTE: It is prohibited to close FV01 to 100%.

3. Pre-Start Check

3.1 Check liquid level in circulation/cleaning tank (minimum: 40L) 3.2 Check power supply and pure water supply 3.3 Check if pressure regulating valve (FV101) is fully open 3.4 Check if all other valves are closed 3.5 For first use, vent air in pump: When pump is full of liquid, start pump, loosen pump air vent bolt (in the middle of pump body) to vent air, then tighten vent bolt. But because your ethanol concentration is too high, you do not need to vent air.

4. Operation Process

4.1 System flushing 4.2 Filtration process 4.3 Cleaning process 4.4 Drainage process

NOTE:

  • Dry running of the pump is prohibited
  • Forbidden to close FV01 to 100%
  • For its ethanol filtration, VV01 can be kept closed

Before starting:

  • connect your own tank to the system (with V01,V02) as a circulation tank
  • Connect PV03 to your permeate tank
  • connect drain valve to your drain pipe

4.1 System Flush (same as 4.3 cleaning process)

For first use or long term storage (more than 72 hours), the system should be rinsed with pure water before filtering. Open Y-style safety filter and remove solids.

  • The permeate flow rate under a pressure (recommended outlet pressure/post-membrane pressure: 1 bar) should be recorded as a normal criterion for the pure water flow rate.

4.2 Filtration Process

1): Open: FV01(100% open), V02, PV02, PV03, finally open V01; all other valves keep closed.

2): Start P01, when the system works stably (5-20 minutes), adjust FV01 to suitable working pressure (1-4bar before membrane) and get a higher and stable permeate flow rate, (record this flow rate and pressure as normal criterion for source liquid flow rate). then filtration process begins.

3): When filtration stops, close all valves (except FV01).

NOTE:

  • During filtration, fresh liquids must be fed into the circulation tank to maintain the liquid concentration volume.
  • If no more fresh liquids are added, with the increase of concentration in the circulation tank, the permeate flow rate will become lower and lower. When the permeate flow rate becomes much lower than the normal criterion (recorded in 4.2), slowly open the pressure regulating valve (FV01) until fully open, then stop the pump.

4.3 Cleaning Process

(see appendix 4: cleaning instruction)

Note: The system must be cleaned when a filtration batch is completed.

1): Open: FV01(100% open), CV02, PV02, PV04, finally open CV01; all other valves keep closed.

2): Start P01, when the system works stably (5-20 minutes), adjust FV01 to suitable working pressure (1-4bar before membrane) and get a higher and stable permeate flow rate, then the cleaning process begins.

3): When cleaning stops, close all valves (except FV01).

4.4 Drainage Process

Filtration drain: 1): Open: FV01(100% open), V02, PV02, PV03, VV01(if necessary), DV01, DV02, DV03, DV04, all other valves keep closed.

2): When the drainage is finished, close all valves (except FV01).

  • Do not forget to close VV01 if it is open during drainage.

Cleaning drain: 1): Open: FV01(100% open), CV02, PV02, PV04, VV01(if necessary), DV01, DV02, DV03, DV04, all other valves keep closed.

2): When the drainage is finished, close all valves (except FV01).

  • Do not forget to close VV01 if it is open during drainage.

5. Cleaning Agent Selection

If the membrane element is seriously contaminated, depending on the nature of the feed material, the following cleaning agents can be chosen:

  • Acid Cleaner: 1~3%HNO3, 1%H3PO4, Oxalic Acid, 112°F(50°C)
  • Caustic Cleaner: 1~3%NaOH, Na3PO4, NaClO, 112°F(50°C)
  • Chelating Agent: EDTA
  • Surfactant: SDS
  • Enzymatic Agent: Amylase, Protease

Please refer to Appendix 7: Cleaning Instruction for detailed cleaning process.

When the flow of the membrane element cannot meet the production capacity demand, the membrane element must be replaced.

6. Membrane Element Assembly

(see appendix 5: membrane element assembly)

7. Membrane Element Storage

Short term (up to one week): pure water Long term: 1% w/w sodium sulfite or 1% w/w H2O2

7.1 Short-term storage shutdown

Short-term storage is applicable to cases when the shutdown is 1-7 days and the membrane elements are still installed in the system.

Storage steps are: After cleaning the system with pure water to neutral, fully ventilate the air and fill the system with pure water, store membrane elements in the system for next work.

7.2 Long-Term Storage Stoppage

Long-term storage is applicable to the case when the stoppage is more than 7 days.

The storage steps are:

  • After system cleaning, remove the membrane elements from the system, store the elements in 1% w/w sodium sulfite or 1% w/w H2O2
  • Install the elements back into the system every 1-3 months, and clean with pure water or 1~3% NaOH solution for 30min, then clean with pure water until neutral
  • Then take out elements again and store them in the freshly prepared 1% w/w sodium sulfite or 1% w/w H2O2

IV: Use and Maintenance

Please read this operation manual carefully. Any incorrect operation may damage the membrane equipment or even cause personal injury.

  1. Operation of the pump without liquid is prohibited
  2. Try to vent the air in the pump
  3. Temperature and pressure gauges in the system should be checked regularly
  4. During work, no air must enter the system.
  5. The parameters obtained from each operation, such as concentrate flow rate, permeate flow rate, membrane inlet/outlet pressure, temperature, should be recorded.
  6. The next operation step can only be performed after the pump works stably.
  7. Valves that are open during work must not be closed until the pump has stopped completely.
  8. When adjusting FV101 (pressure regulating valve), the pressure must not exceed 6 bar
  9. To avoid rapid contamination of the membrane, it is forbidden to close FV101 completely.
  10. The maximum working pressure should not exceed 6 bar, and the speed over the membrane should be controlled between 3-5 m/s
  11. If the flow rate can meet the production capacity, the working pressure should be as low as possible to reduce the contamination rate on the membrane surface.
  12. In case of any accident during work, the accident should be resolved only after draining all the fluids in the system.
  13. The system should be cleaned immediately once the drain is complete.
  14. A suitable cleaning agent must be chosen for different contaminants.
  15. After complete cleaning, if the permeate flow rate cannot be recovered well or cannot meet the production capacity, the ceramic membrane elements should be replaced.
    1. When the ambient temperature is lower than 5℃, the equipment cannot be used, and the liquid in the system must be drained to prevent the equipment from being damaged.
    2. If the equipment is not working for more than three months, it should be stored away from direct sunlight, dust, corrosive gas, combustible gas, steam, oil mist, vibration and salt environment etc, it should be cleaned regularly referring to “III 7.2 long-term shutdown storage”.
  16. V: Troubleshooting

    ClassificationDescriptionCauseSolution
    System failureSystem cannot bootPower phase is not correctsingle phase
      Power is not connectedConnect the power
      The voltage is not suitableCheck the power supply
      Defective circuit or poor contactCheck circuit or contacts
     DrainLoose clamp or flangeReset
      Damaged sealsReplace seals
    Pump failureAbnormal sound, abnormal vibration, pump pressure gauge pointer fluctuates; Pressure does not riseLoss of power phaseCheck energy
      Stamps are worn outReplace seals
      Air in pump not ventedVent air into the pump
      Pipe leaks, air sucked inCheck suction pipe
      Loose baseTighten the base bolts
      Pump works in opposite directionAdjust power supply
    System failurePermeate flow rate lower or fallsSystem pressure is too lowAdjust regulating valve to increase system pressure
      Feed temperature is too lowRaise the temperature
      Feed concentration is very highDecrease concentration
      Contaminated elementChemical cleaning
     Permeate is cloudyMembrane element is damagedReplace membrane element
      Leaking sealsReassemble or replace seals
      BubblesNo need to treat

    VI: Appendix

    1. terminal diagram
    2. PID/process diagram
    3. 2D drawing
    4. DQCM cleaning instruction
    5. membrane element assembly
    6. experimental record sheet
 

Appendix 1: Terminal Diagram for ARDLF8-40

Technical Specifications

  • Project Name: ARDLF8-40
  • Voltage: AC220V 60HZ+N+PE
  • Drawing Number: DCC

Terminal Connection Table (XT)

TerminalInternal CableExternal CablePageFunction
XT1-Q1:2TO/2.0:HPower AC220V 60HZ
XT2-Q1:4B/2.1:H 
XT3-Q1:6C/2.1:H 
XT4-P.MN/2.1:H 
XT5PEPE/2.1:H 
XT6-FR1:2-M1:U1/2.2:HFeed Pump 1.5KW
XT7-FR1:4-M1:V1/2.3:H 
XT8-FR1:6-M1:W1/2.3:H 
XT9PE-M1:PE/2.3:H 

Important Notes on the Electrical System:

  1. The system includes a main power supply circuit
  2. Low voltage power distribution
  3. Connections for 1.5KW feed pump
  4. Control system with integrated protections
  5. All connections must be made following the specified color and numbering code.

The feed pump features:

  • Explosion proof motor
  • Overload protection
  • Start/stop control system
  • Operation and stop indicators

Appendix 2: PID / Process Diagram

Appendix 3: 2d Drawing

 

Connection Specifications Table

Item No.SpecificationDescription
P1NPT2.5″Draining the cleaning tank
P2NPT2.5″Draining the system
P3NPT1″Permeate drainage
P4NPT1″Permeate/to permeate tank
P5NPT3/4″Heat exchanger inlet/outlet
P6NPT3/4″Air ventilation
P7NPT2.5″Liquid inlet/from feed tank
P8NPT2″Retentate return/return to circulation tank

Main Dimensions

  • Overall height: 1902 mm
  • Width: 787 mm
  • Base length: 1514 mm
  • Base details:
    • 278mm + 269mm + 297mm = 1514mm (total length)
    • 210mm + 350mm (side dimensions)
    • Height from ground: 40 mm

The drawing shows three different views of the system:

  1. Front left view
  2. Front view with dimensions
  3. Front right view
  4. Isometric view (3D perspective)
  5. Side view

This technical plan is essential for:

  • Installing the equipment
  • Space planning
  • Identifying connections
  • System maintenance
 
 

Appendix 5: Membrane Assembly Instructions with Conical Seals

Necessary Materials

  • Inner hex key
  • Conical seals
  • Housing gasket

Step by Step Procedure

Preparation Phase

  1. Preparation of Materials
    • Gather inner hex key
    • Conical seals
    • Housing gasket
  2. Surface Preparation
    • Place the case on a flat wooden board or soft cloth

Element Installation Phase

  1. Installing the First Element
    • Seal one end of the membrane element with the conical seals
    • Insert the element into the hole in the housing
    • Ensure that both ends of the element protrude the same length on both sides of the housing
  2. Full Installation
    • Insert all membrane elements into the housing one by one

Sealing Phase

  1. First End Sealing
    • Cover the end of the housing with the plate
    • Secure with inner hexagon bolt
  2. Second End Sealing
    • Flip the case over
    • Insert the conical seals
    • Fix the plate

Final Phase

  1. Installation of the Board
    • Place the housing gasket into the gasket groove
  2. Final Assembly
    • Fix the reducer at both ends of the housing with the clamp

Important Notes

  • Ensure all connections are tight
  • Check that the conical seals are properly seated
  • Check that the elements are aligned evenly
  • Perform a final visual inspection of all joints and connections
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