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I. 

INTRODUCTION

 

 
 

The separation of dissolved solids and water using RO membranes is a pressure driven 
temperature dependent process.  The membrane material is designed to be as permeable to water 
as possible, while maintaining the ability to reject dissolved solids. 
 
The main system design parameters require the following: 

 

 

Internal flows across the membrane surface must be high enough to prevent settling of fine 
suspended solids on the membrane surface. 

 

 

The concentration of each dissolved ionic species must not exceed the limits of solubility 
anywhere in the system. 

 

 

Pre-treatment must be sufficient to eliminate chemicals that would attack the membrane 
materials. 

 

A

.  

SPECIFICATIONS

  

 
 
 

Notes: 

 

 

Maximum production based on a feed water of 77°F, SDI < 1, 1000 ppm TDS, and pH 7. 
Individual membrane productivity may vary (± 15%). May be operated on other feed waters with reduced 
capacity.

 

 

Percent Rejection is based on membrane manufactures specifications; overall system percent rejection may 
be less.

 

 
 
 

 

R4X40-1 

R4X40-2 

R4X40-3 

Maximum Productivity 

(gallons per day) 

2200 

4400 

6600 

Quality 

(average membrane rejection) 

98 % 

Recovery 

(user adjustable) 

15 - 75 % 

25 – 75% 

32 - 75 % 

Membrane Size 

4” x 40” 

Number Of Membranes 

Prefilter 

(system ships with one 5 micron cartridge) 

20” 

Feed Water Connection 

3/4" NPTF 

Product Water Connection 

(tubing OD) 

5/8" 

Reject Water Connection 

(tubing OD) 

5/8" 

Feed Water Required 

(maximum) 

10 gpm 

12 gpm 

14 gpm 

Feed Water Pressure 

(minimum) 

10 psi 

Drain Required 

(maximum) 

10 gpm 

12 gpm 

14 gpm 

Electrical Requirement (60 Hz)

 

120 V - 15 amps  120 V - 20 amps  240 V - 12 amps 

Motor Horse Power 

 

3/4 

1 1/2 

Dimensions W x D x H 

(approximate inches) 

20 x 20 x 50 

20 x 26 x 50 

Shipping Weight 

(estimated pounds) 

120 

150 

180 

Summary of Contents for R4X40

Page 1: ...REVERSE OSMOSIS INSTALLATION AND OPERATION MANUAL Model R4X40...

Page 2: ......

Page 3: ...ty of the end user Successful long term performance of an RO system depends on proper operation and maintenance of the system This includes the initial system startup and operational startups and shut...

Page 4: ...nt II Controls Indicators and Components III Operation A Installation B Plumbing Connections C Electrical D Startup E Control Function F Operation and Maintenance Log G Troubleshooting IV Replacement...

Page 5: ...0 ppm TDS and pH 7 Individual membrane productivity may vary 15 May be operated on other feed waters with reduced capacity Percent Rejection is based on membrane manufactures specifications overall sy...

Page 6: ...suspended solids sediment from the feed water Backwashing the media removes the trapped particles Backwash can be initiated by time or differential pressure Water Softener Used to remove calcium and m...

Page 7: ...solubility Additionally the solubility is highly pH and temperature dependent Silica fouling can be prevented with chemical injection and or reduction in recovery II CONTROLS INDICATORS and COMPONENT...

Page 8: ...Figure 1...

Page 9: ...Figure 2 Controller Connections...

Page 10: ...he product water line should never be restricted Membrane and or system damage may occur if the product line is blocked 3 Connect the reject water outlet to a drain The reject outlet is located behind...

Page 11: ...rating data using the log sheet E CONTROL FUNCTION 1 When the on off switch is in the on position the inlet valve opens and the pump runs There is a five second delay between the opening of the inlet...

Page 12: ...ater TDS The meter will automatically turn it self off after a few seconds The quality meter is powered by two AAA batteries To replace the batteries lift the meter out of the bracket and remove the b...

Page 13: ...ED WATER TEMP FEED WATER HARDNESS FEED WATER CHLORINE LEVEL PRE FILTER INLET PRESSURE PRE FILTER OUTLET PRESSURE REMARKS Note Change the prefilter when the differential pressure increases by 5 10 psi...

Page 14: ...and reject Slime in pipes and vessels Shock dosage of sodium bisulfite Continuous feed of low conc bisulfite at reduced pH Peracetic acid sterilization Clean with alkaline anionic surfactant Chlorine...

Page 15: ...Low feed water temperature Adjust reject valve or replace pump Increase membrane feed pressure or heat the feed water IV REPLACEMENT PARTS LIST A list of common replacement parts is provided below Co...

Page 16: ...e the end caps The new membranes should be installed in the same orientation as the old membranes Note It is very important that the brine seal does not flip up or roll when installing the membrane br...

Page 17: ...perating at 50 recovery with a feed water SDI 1 R4X40 1 R4X40 2 R4X40 3 Product GPM 1 5 3 0 4 5 Reject GPM 1 5 3 0 4 5 Nominal flows for systems operating at 50 recovery with a feed water SDI 3 R4X40...

Page 18: ...0 68 0 86 19 66 2 0 84 18 64 4 0 81 17 62 6 0 79 16 60 8 0 77 15 59 0 74 14 57 2 0 72 13 55 4 0 70 12 53 6 0 68 11 51 8 0 66 10 50 0 64 9 48 2 0 62 8 46 4 0 61 7 44 6 0 59 6 42 8 0 57 5 41 0 55 Multip...

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