NASA Technical Reports Server (NTRS) 19860018819: Reverse osmosis water purification system

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TDA Progress Report 42-85 


N86-28291 t 

January- March 1986 


I 


Reverse Osmosis Water Purification System 


H. G. Ahlstrom, P. S. Hames, and F. J. Menninger 


Ground Antenna and Facilities Engineering Section 



! A new reverse osmosis water purification system , which uses a programmable con- 
troller (PC) as the control system , was designed and built to maintain the cleanliness and 
level of water for various systems of a 64-m antenna . The installation operates with other 
equipment of the antenna at the Goldstone Deep Space Communication Complex. The 
reverse osmosis system was designed to be fully automatic; with the PC many complex 
sequential and timed logic networks were easily implemented and are modifiable. The PC 
monitors water levels , pressures , flows , control panel requests ; and set points on analog 
I meters ; with this information various processes are initiated , monitored , modified , halted , 

I or eliminated as required by the equipment being supplied pure water. 


J 


I. Introduction 

A reverse osmosis water purification system was designed 
and installed for the Goldstone Deep Space Communication 
Complex, California. This article describes the water treatment 
requirements, control philosophy, and hardware and software 
specifications. 

The moving part of the 64-m antenna shown in Fig. 1, a 
complex structure weighing over 3.2 XI 0 6 kg (7 X 10 6 lb), 
rotates horizontally on a film of oil 0.2 mm (0.008 in.) thick 
beneath three large pads. The risk of losing a spacecraft track 
is high if the hydrostatic bearing fails due to insufficient 
cooling. 

There are three requirements for pure water for systems 
that support the antenna operation. The first is cooling water 
for the hydraulic system that maintains the critical film of 
oil beneath each pad. The second requirement is for pure 
coolant water for the high-power transmitter. The third pure 
water use is for make-up water for the boilers and chilled- 


water loop of the air conditioning system. Water supplied to 
the station is pumped from nearby underground wells. The 
chemical composition and quality are not adequate for direct 
use; therefore, a purification system is necessary to meet the 
specifications. 


II. Functional Requirements 

The performance and functional requirements for the pure 
water system can be summarized as follows: 

The two principal design criteria for the water purification 
system are reliability and flexibility - reliability is derived 
from the mission requirements and flexibility from the need 
for versatility in monitoring and control, to permit unattended 
operation. This versatility must meet constantly changing 
process requirements, which include such events as placing an 
operation on “hold” to perform another process, and sensing 
the proper conditions for returning to the original operation. 


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Without automatic controls, such variations would require 
labor-intensive attention to the equipment. 

Several water purification systems were considered, includ- 
ing gas/oil fired water distillation, solar stills, reverse osmosis, 
and purchasing purified water from a commercial water sup- 
plier. The stringent cleanliness standards for the product of 
this system, as well as the reliability required, led to the selec- 
tion of reverse osmosis as the type of purification preferred. 
The need for reliability and flexibility resulted also in the 
selection of a programmable controller to manage the opera- 
tion. The reverse osmosis system is shown in Fig. 2. 

It was required that the plant be nearly maintenance free. 
The new design should have process error checking and fully 
automated operation, should automatically perform routine 
“housekeeping” functions, and should be capable of remotely 
controlled operation. 


III. Reverse Osmosis Principles of Operation 

Osmosis is the spontaneous passage of a liquid from a dilute 
to a more concentrated solution through a semipermeable 
membrane, which allows passage of the liquid but not of 
dissolved solids. Reverse osmosis (R.O.) is the forced reversal 
of this natural phenomenon, usually accomplished by apply- 
ing enough pressure to the concentrated solution to overcome 
the natural pressure (osmotic pressure) of the less concen- 
trated solution. 

This property of some membrane materials makes them 
ideal for water purification. In general application, the mem- 
brane unit is made up of either a bundle of fibers approxi- 
mately the diameter of a human hair, or a spiral-wound 
membranous material, within an epoxy tube. In either case, 
the membrane surrounds a central core, within which the 
clean, or “product” water flows after permeating through the 
membrane to the core. 

The reject water, or “concentrate,” emerges from the out- 
side membrane material on the same side where the raw water 
entered. No chemical reactions or phase transitions are involved. 
One of the principal advantages of semipermeable membranes 
over other methods of separating water from its contaminants 
is that, with proper care, the membranes can be expected to 
last from three to five years. 

This article focuses on the application of a programmable 
controller (PC) to control the R.O. process. It is therefore 
necessary to be aware of the constraints on the operation of 
the system and the process variations to take advantage of the 
flexibility the programmable controller provides. 


IV. The Reverse Osmosis Process 

The water purification process at the Goldstone antenna is 
divided into three stages: pretreatment, reverse osmosis, and 
post-treatment. The process is controlled by a programmable 
controller. The controller’s actions are determined by the 
status of switches on the control panel and various sensors on 
the process equipment. An instrumentation panel monitors 
various analog signals and reports out-of-bounds conditions to 
the PC. 

Figure 3 is a simplified flow diagram of the R.O. system. 
Many essential controls are omitted for simplification; the 
diagram is not intended as a complete representation but only 
as an aid to the discussion. 

A. Pretreatment Stage 

The reverse osmosis unit processes raw water from either 
the local water supply (demand tank fill) or the cooling tower 
sump water (tower recycle). The water cannot be run directly 
into the R.O. membranes; it must first go through preliminary 
processing so as not to damage the membranes. This pretreat- 
ment involves flowing the water through a sand filter (to 
remove large dirt particles) and a carbon filter (to remove 
chlorine, which would oxidize the membranes), injecting 
acid to control pH level to a slightly acidic condition (excess 
alkalinity can foul membranes), and flowing the water through 
a 10-micron prefilter and then past sensors that check for 
pH level and the presence of chlorine. (Raw water typically 
has a pH of 8.5 to 11.5; the R.O. membranes require the pH to 
be approximately 6.0.) Now the water contains very few 
nondissolved solids, but is still high in dissolved solids. It is 
now ready for the reverse osmosis treatment. 

B. Reverse Osmosis Treatment Stage 

The reverse osmosis treatment section consists of pressure 
switches, flow controls, conductivity ratio sensors, flow 
meters, R.O. membranes, pressure gauges, and a main pump. 
Each of these is critical to the production of purified water. 

The inlet pressure to the pump must remain above 10 psi 
to avoid cavitation in the pump. The inlet pressure to the 
membranes must stay below 400 psi; otherwise the membranes 
will be damaged. Pressure switches monitor these critical 
items. 

The flow controls are adjusted to maintain a ratio of 50 
percent product water and 50 percent reject water, with a 
production flow of 15 gallons per minute. The reject water 
contains all the impurities removed from the product water 
and drains into the sewer. 


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The conductivity ratio sensors are part of the membrane 
efficiency meter, shown in Fig. 4, measuring the amount of 
dissolved solids in the water. The total dissolved solids in 
feedwater are typically 500 to 600 parts per million (ppm). 
Product water typically contains less than 45 ppm. The meter 
determines what percentage of dissolved solids is being rejected 
by the membranes; when it drops below 90 percent, the 
PRODUCT WATER LOW REJECT RATIO error signal is 
generated. 

C. Post-Treatment Stage 

Product water flows through an ultraviolet sterilizer, and 
then to either the demand tank by way of a degassifier, or 
to the cooling tower for sump recycle. The ultraviolet steri- 
lizer kills bacteria in the water. The degassifier is a tall cham- 
ber above the demand tank, filled with saddle packing; water 
flows down over these saddles as air is simultaneously blown 
up over them removing dissolved gasses. 

From the degassifier, product water flows into the demand 
tank until it reaches a preset level, monitored by a level switch. 
The demand tank can then drain to either the shutdown flush 
pump, or the demand pump. The shutdown flush pump 
supplies product water to the main pump for a cleaning flush 
of the membranes after every operation. The demand pump 
supplies water to the additional PC-controlled functions. 


V. Additional Control Functions of the PC 

In addition to processing water through the R.O. unit, the 
PC manages the water level of the cooling tower, a transmitter 
coolant storage tank, and an air conditioning chilled water 
storage tank. In addition, it manages the cleanliness of the 
cooling tower. The demand pump pumps water to three 
places, as selected by solenoid valves: the heating and air 
conditioning system (make-up water), the cooling tower sump, 
or the transmitter coolant system storage tank through a 
deionizer. 

A. Cooling Tower Functions 

A front panel switch, as shown in Fig. 5, tells the PC 
whether to refill the sump with raw water, purified water from 
the R.O., or nothing. The cleanliness of the tower water is 
monitored by a conductivity meter on the instrument panel. 
When a preset high limit in the conductivity meter is reached, 
the PC starts a cleanup process as determined by another 
front panel switch, which tells the PC whether to recycle the 
sump water through the R.O. or to pump it to the drain 
(blow down). Blow down is the operation of removing water 
from the sump and replacing it with fresh water. The con- 
troller blows down the sump by pumping water to drain and 


replacing the lost water with either raw or R.O. water, as 
selected. (If neither recycle nor blow down is selected, an 
alarm is generated.) When conductivity reaches the low limit, 
the PC ends the cleanup process. 

In recycle mode, the R.O. returns only 50 percent of the 
water it removes from the tower. If the refill switch is on 
R.O., then the other 50 percent is furnished from the demand 
tank. Since the R.O. must be flushed after each water produc- 
ing cycle, there must be enough water in the demand tank to 
flush the R.O. membranes. Therefore, when the demand tank 
is below this middle level switch the PC will first fill the demand 
tank before proceeding with the recycle request. 

B. Transmitter Tank Fill Function 

The front panel switch selects between MANUAL-OFF- 
AUTOMATIC refill of the transmitter coolant tank. In auto- 
matic, a level switch indicates to the PC the need for water. 
(In manual, the level switch is overridden.) If the demand tank 
is not empty and the tower is not being refilled, the demand 
pump is turned on and a valve opens to send water to the 
transmitter coolant tank through a deionizer. The deionizer 
further purifies the water to a resistivity of at least 2 megohms/ 
centimeter. (With a fresh deionizer, the output can be as high 
as 16 megohms/centimeter.) The water is monitored by a 
resistivity meter that has a preset low-level trip point, at which 
the XMTR WATER LOW RESISTIVITY error signal is gener- 
ated when the water is top conductive. To prevent excess 
water from being pumped to the transmitter, this function can 
be active for only ten hours. Then the system must be reset 
before more water will be pumped to the transmitter. 

C. Air Conditioning System Fill Function 

In normal operation, a manual valve is opened and water is 
allowed to flow down to a chilled-water storage tank at the 
control building for the air conditioning system and to the 
humidifiers. (There is an elevation difference of approximately 
30 feet.) If a large quantity of water is required, the demand 
pump may be turned on and the line to the storage tank pres- 
surized (G-86 PRESSURIZE front panel indicator on). This 
function has the lowest priority, and is interruptible by the 
tower-refill-with-R.O.-water process or the transmitter-tank -fill 
process. To prevent excess water from being pumped to the 
storage tank, this function is active for only 10 hours. Then 
the system must be reset before more water may be pumped. 


VI. Housekeeping Functions 

At the end of each water-producing operation, the system 
automatically goes into a “shutdown flush” cycle. The flush 
pump pumps product water from the demand tank to the 


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main pump ahd then to the reverse osmosis unit. The product 
water from this operation returns to the demand tank or 
sump, depending on the production cycle that was just fin* 
ished. The purpose of this flush is to feed very pure water 
into the membranes so as to flush out any contaminants. 

A high-flow flush is performed once each day. (This is 
different from a shutdown flush and is performed even if no 
water production cycles have taken place that day.) A sole- 
noid valve is opened to bypass the reject flow control valve; 
the reduced backpressure causes 90 percent of the water to 
go out the reject ports, thus flushing any solids from the sur- 
face of the membranes. The high-flow flush of the membranes 
lasts for fifteen minutes. In addition, once a week the sand 
filter and the carbon filter are backflushed, one at a time. 
Each of these filters is also backflushed when a high pressure 
drop exists across the filter. 

All of these operations are part of programmed mainte- 
nance activities, independent of any other actions, and are 
initiated by the programmable controller’s software clock. 
They are, however, subject to the same monitoring and alarm 
controls that accompany all other operations. The timing is 
part of the PC program; no additional hardware is required. 

The sand filter and carbon filter backflush and the high- 
flow flush may be activated manually by using the power of 
the PC. This capability was accomplished without the use of 
an additional front panel switch. When all process selector 
switches are turned to OFF, and the ALARM ACKNOWLEDGE 
button is pushed twice, all three flushes are enabled. The sand 
filter is flushed first, followed by the carbon filter, and then 
the high-flow flush. At any time, each flush can be canceled by 
pushing the ALARM ACKNOWLEDGE button twice. This 
action establishes a form of reset, in which the first push 
holds everything, preventing the machine from running; the 
second push resets all sequences. 


VII. Process Alarms 

If any of eleven parameters is out of limits, an alarm 
sequence is initiated. Once a process is started, each instru- 
ment can generate an error signal, after a time delay has been 
satisfied to allow for transient water conditions. Once an error 
signal is generated, it will create an error routine that shuts off 
the applicable process. The eight processes of the R.O. system 
for purposes of alarm shutdown are demand tank fill, tower 
refill, tower recycle, tower blowdown, transmitter tank refill, 
air conditioning system pressurize, high-flow flush, and shut- 
down flush. After a five-minute delay, the controller will 
attempt to restart the interrupted process. This allows for the 
air bubbles that can get into the water supply. The delay 


can be manually overridden by pushing the ALARM ACK- 
NOWLEDGE button twice. If, after two restart attempts, 
the error still exists, the interrupted process will be shut off 
until it is manually reset by operator action (pressing the 
ALARM ACKNOWLEDGE button twice). The error is now a 
fatal error. When a fatal error occurs, an alarm is sent by the 
controller to a console at the communications center of the 
complex. 

When an operator acknowledges an alarm, the system is 
placed in a “hold” condition with a 30-minute allowance for 
maintenance. If someone should forget to reactivate the sys- 
tem, the hold condition is canceled; if no reset has been input 
by this time, the system goes into SYSTEM SHUTDOWN 
mode and transmits an alarm. 

VIII. Process History 

The PC has been programmed to restart the system and 
continue, if an error does not reappear. This feature makes it 
difficult for maintenance personnel to determine whether 
there have been any errors since the last time the system was 
checked. Maintenance personnel may not check on the system 
for up to a week or two at a time. Repetition of a certain 
error can be a telltale signal that a certain section is becoming 
marginal and should be checked closely before it shuts the 
system down. As a maintenance feature, each error increments 
its own counter inside the PC when it shuts the system down. 

There are also counters assigned to each process. Some 
count the number of times a process has occurred, and others 
count the number of five -minute increments each is on. 
These are useful in analyzing how the machinery has been 
used since the last time it was checked. The number of five- 
minute increments a process has been on can be multiplied 
by a constant to give an accounting of how much water was 
sent for each use; this number is within ten percent of the 
actual number and does not require costly totalizing flow 
meters to report back to the PC. There are two totalizing flow 
meters, one for the product water and one for the reject water, 
but they do not report back to the PC. 


IX. The Programmable Controller Rationale 

The large number of control and monitoring actions required 
in a system such as this makes the programmable controller an 
ideal choice for control methods. The necessity to effect the 
control actions, make the control change decisions, and pro- 
vide the requisite isolation of sensor inputs from control 
outputs could suggest a completely computer-controlled 
system. But the sophistication of expensive computer hard- 
ware would constitute control “overkill” in this case, and the 


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cost would be compounded by the environmental protection 
necessary for most computer installations. The programmable 
controller modules are rugged and provide the ideal compro- 
mise, with cost savings on both ends. 

For example, during pre-treatment, the water is monitored 
for excessive pressure drop at three stages, as well as for high 
or low pH or the presence of chlorine. If any sensor detects 
an out-of-limits condition, an error routine is generated and 
the condition is displayed on the appropriate analog meter. 
At the same time, corrective action is started by the PC. If 
another process was in progress at the time, it might continue, 
or be placed on “hold,” depending on the relative importance 
of the two actions. Note that the relative importance can 
change; the first priority of the system is to keep the cooling 
tower sump filled; if the sump is not low, and another process, 
for instance the production of pure water, is ongoing and a 
high pressure drop occurs, the process would be suspended 
until the excessive pressure drop is corrected by a backflush 
of the offending tank. If, however, the cooling tower water 
level is low, refilling to a specified level would take priority 
and the backwash itself would be put on “hold.” 

In this application, several different conditions enable 
various processes. There are 32 inputs, 64 outputs, 114 
internal logic relays, and 77 storage registers. Only 44 of the 
77 storage registers are used for time delays and time-outs. 
To implement this design in discrete components would 
require a relay panel that was cost prohibitive, not to mention 
labor intensive. Moreover, should a slight change in process 
requirements occur, the task of rewiring would be time con- 
suming and costly. 

From an extensive survey of commercial programmable 
controllers available for this application, the Square D SY/ 
MAX-20 (Fig. 6) was selected. Following are two of the 
features that determined the selection. 

A. Dual Memory 

The dual memory fits the reliability philosophy of this 
subsystem, which must support a very critical and probably 
unrepeatable mission. The application memory combines the 
advantages of random access memory (RAM) and electrically 
alterable read-only memory (EAROM) to ensure both the 
program flexibility offered by the RAM and the memory- 
saving characteristic of the EAROM. Program information 
stored in the EAROM is retained in the event of power failure, 
and even if the memory module is removed from the processor. 
The memory can be reprogrammed as often as desired, the 
change being as small as one contact or as large as the entire 
program . 


These memory modules had several features unlike those of 
other manufacturers, at the time of purchase. The memory 
was programmed, when installed in the PC, with a command 
from the program to transfer the contents of the RAM to the 
EAROM. The memory was encased in a steel box with a 
rugged connector on the back. The connector configuration 
prevented the memory module from being inserted incorrectly 
into the PC. 

B. Computer Interface Module 

Another important feature is the computer interface mod- 
ule, which permits remote control and monitoring, as well as 
communication with the programmer. In this application all 
inputs, outputs, internal relays, and storage registers are 
accessible to a computer at a remote location. A modem in the 
PC cabinet is used to transmit this data to the computer 
terminal 14 miles from the pure water system installation. The 
computer can request any data that is stored in the PC at any 
time; and the PC can be called up as desired. This allows a 
historical record of how the system has been performing, and 
can indicate the development of trends in the process, such as 
gradually decreasing time between carbon filter backwashes, 
indicating the approach of the need to replace the carbon. 

The computer interface allows access to information in the 
PC through a non-proprietary serial port. Any computer with 
a serial port could be programmed to communicate with the 
Square D processor. 

X. Summary 

The reverse osmosis water purification system for the 
NASA/JPL 64-meter antenna has been designed and installed. 
Utilization of a programmable controller made it possible to 
meet stringent performance requirements. The system has 
operated successfully since July 1982, with little or no pre- 
ventive maintenance. Due to this increased reliability perfor- 
mance, the cooling system of the antenna has been much more 
reliable and has required significantly less maintenance. 

One advantage of the programmable controller was the 
ability to make small program changes quickly during system 
startup: RAM could be modified and tested operationally 
before it was transferred to EAROM. 

The successful experience gained by this PC installation 
led to the selection of PCs for control of other facilities at 
the Deep Space Communications Complex. Examples are 
as follows: 

(1) A 15 -foot diameter mobile antenna used in the Orion 
earthquake research program: The SY/MAX-20 PC 


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controls antenna deployment, storage, and leveling 
of the trailer and antenna, making it possible to assem- 
ble and disassemble the system in 20 to 30 minutes. 

(2) The electrical power generating station at the Echo 
Station (DSS 12): This installation, with five 500-kW 
diesel generators, is also controlled by a SY/MAX-20. 

(3) Air conditioning for three buildings at DSS 12, build- 
ings G26 (control room), G34 (hydromechanical build- 
ing), and G35 (antenna): This complex system, designed 


to meet the varying needs of three very different 
structures, utilizes a Square D Model 500 program- 
mable controller, which simplifies' control of a highly 
automated and energy efficient system. 

The reverse osmosis water purification system, under pro- 
grammable controller management, has met all of its principal 
design objectives: a cost-effective, high reliability, maintenance- 
free plant that incorporates fully automated operation, process 
error checking, automatic performance of routine housekeep- 
ing functions, and capability of remotely controlled operation. 


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ORIGINAL 'PAGE iZ 

OF POOR QUALITY 



Fig. 1. The 64-m antenna at Goldstone, California 



Fig. 2. Reverse osmosis water purification system 


TRANSMITTER 



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Fig. 3. Simplified flow diagram of the R.O. system 



























ORIGINAL PAGE 13 
OF POOR QUALITY 



Fig. 4. R.O. instrument panel 



Fig. 5. R.O. control panel 


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