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Precautions 

 

1. Precautions for system design

                                 

 

Warning 

1. Confirm the specifications. 

- Give careful consideration to operating conditions such as the application, fluid and environment, 

and use the product within the operating ranges specified in this catalog.

 

- The product is provided for physical, chemical and industrial equipment.

 

2. Fluids 

- For the compatibility between the materials composing the product and the fluids, check the 

compatibility check list. Since the compatibility of the fluid used may vary depending on its type, 
additives, concentration, temperature, etc., give sufficient consideration when selecting the 
material. 

- For fluids other than those listed on the check list, please consult us. Also, use them within the 

range of the operating fluid temperatures. 

- If foreign matters are mixed in the fluid, these may cause abrasion of the inside of the pump 

resulting in a problem. Use an appropriate filter (strainer) to remove them. In general, 80 to 100 
mesh (150 to 180 μm) filters are recommended. 

- When transferring a coagulable liquid, take measures to prevent it from coagulating in the pump. 
- Precautions to observe when transferring slurry 

Basically, it is not recommended to transfer slurry because this will result in seating failure and 
wearing of the check valve and accumulation of particles. However, if you intend to increase the 
number of maintenance cycles even though this promotes wear and accumulation of particles, 
use a suction lift of no more than 1 m and also a slurry containing solid particles of the following 
diameter. 
If the specific gravity of the slurry is less than 3, use particles that have a diameter of no more 
than ø0.25 mm and have been passed through a #60 or finer mesh (e.g. aluminum powder). 
If the specific gravity of the slurry is 3 or more, use particles that have a diameter of no more 
than ø0.15 mm and have been passed through a #100 or finer mesh (e.g. iron powder) 

- Take countermeasures to prevent the operating fluid from getting onto the body of the process 

pump. 

3. Water hammer 

If a valve is operated abruptly etc., a high pressure may be applied due to water hammer. Take 
measures to prevent pressures higher than specified from being applied. 

<Examples of measures> 
- Use a water hammer resistant valve to reduce the valve closing speed. 

- Use an elastic piping material such as rubber hose or an accumulator to absorb the impact 

pressure. 

4. Liquid seals   

To ensure that fluid does not become sealed inside the process pump, when 
stopping the pump, relieve the discharge pressure inside it. As shown in the 
figure at right, make a circuit which has a relief valve installed on the 
system. 

5. Fluid pressure supplied to the process pump 

Feeding the fluid from the suction side into the pump under pressure, or   
drawing it using a negative pressure, will reduce the life of the pump. 

6. Ensure space for maintenance. 

Secure the space required for maintenance and inspection. Take into consideration also leakage 
from the product. When transferring a flammable liquid or a liquid that may affect the human body 
or environment, take measures including fire ban and keeping the area off limits. 

7. Use a design which prevents reverse pressure and reverse flow. 

If reverse pressure or reverse flow occurs on the discharge side of the process pump, the 
equipment is liable to become damaged or malfunction. Take safety measures in designing the 
circuit. 

8. Measures against static electricity 

Take measures against static electricity as static electricity may occur depending on the fluid. 
Particularly, when circulating flammable fluid through the pump, be sure to take measures to 
prevent the occurrence of static electricity. 

 
 
 

Summary of Contents for PA3310 Series

Page 1: ...Doc no PAB OM E001 F PRODUCT NAME Process Pump MODEL Series Product Number PA P 3310 Series...

Page 2: ...ons P 2 to 3 Names and functions of parts P 4 Precautions P 5 to 9 Applicable Fluids P 10 Specifications P 11 Performance Curve P 12 to 13 Working Principle P 14 Maintenance Parts P 14 Piping and Oper...

Page 3: ...nt failure when configuring the equipment 2 Only personnel with appropriate training should operate machinery and equipment The product specified here may become unsafe if handled incorrectly The asse...

Page 4: ...ts 2 Vacuum pads are excluded from this 1 year warranty A vacuum pad is a consumable part so it is warranted for a year after it is delivered Also even within the warranty period the wear of a product...

Page 5: ...scharge piping Pilot air supply port AIR SUP Supplies air of set pressure Connect the air piping Pilot air exhaust port AIR EXH Exhausts pilot air Reset button Air operated reset port Resets the pump...

Page 6: ...wder If the specific gravity of the slurry is 3 or more use particles that have a diameter of no more than 0 15 mm and have been passed through a 100 or finer mesh e g iron powder Take countermeasures...

Page 7: ...type of some models adopts an air spring for the built in air control circuit and the pump may malfunction and stop when the pilot air pressure fluctuation exceeds 50 kPa 3 Reverse flow The check val...

Page 8: ...P2 to 3 of Best Pneumatics 6 Use of humid air may cause condensation inside the body Use air which has been treated by a refrigerated air dryer such as IDF series when condensation occurs When dew for...

Page 9: ...afety of the system before performing work Caution 1 Caution when transferring a highly penetrating liquid When transferring a liquid that is highly penetrating through fluoropolymer components of the...

Page 10: ...be sure to continue lubricating the pump Warning 1 Test before using with the actual equipment Test the pump before using it with the actual equipment Even if there is no problem in a short term test...

Page 11: ...applicability may vary depending on your operating conditions be sure to check it by means of experimentation 6 Compatibility is indicated for fluid temperatures specified for the respective products...

Page 12: ...areas New PFA Diaphragm PTFE Check valve PTFE New PFA Discharge rate 1 to 13L min Note Average discharge pressure 0 to 0 4MPa Pilot air pressure 0 2 to 0 5MPa Air consumption 140 L min ANR or less Suc...

Page 13: ...marked point In this case the point is between the discharge curves solid lines for SUP 0 4 MPa and SUP 0 5 MPa and based on the proportional relationship to these lines the pilot air pressure for th...

Page 14: ...e required specification example the viscosity is 100 mPa s and the discharge rate is 2 7 L min Since this is equivalent to 45 of the discharge rate for fresh water 2 7 L min 0 45 6 L min indicating t...

Page 15: ...opposite direction the fluid in pump chamber A is forced out and fluid is sucked into pump chamber B 3 Continuous suction and discharge is performed by the reciprocal motion of the diaphragm Maintenan...

Page 16: ...IR EXH 3 To stop the pump exhaust the air pressure being supplied to the pump by the 3 port solenoid valve of the air supply port AIR SUP The pump will also stop if the throttle on the discharge side...

Page 17: ...16 Dimensions Integrated fitting type With nut Tube extension...

Page 18: ...4 14 1 Sotokanda Chiyoda ku Tokyo 101 0021 JAPAN Tel 81 3 5207 8249 Fax 81 3 5298 5362 URL https www smcworld com Note Specifications are subject to change without prior notice and any obligation on...

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