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Mr. M Billinghurst
Fuji Graphic Systems Canada Inc.
6425 Airport Road
Mississauga, ON L4V 1E4
Re: Metafix pH Neutralization Unit at "customer name withheld"
Dear Murray:
The testing of the Metafix pH Neutralization Unit installed on the Fuji
computer to plate processing line at "customer name withheld" is
now complete. The following
report is specific to: The Fuji Luxcel 9600 Computer to Plate installation,
processing the Fuji Digital Plate LPN3. The chemistry in this plate line
is Fuji Digital
Plate Developer, LPD3 and LPDR3.
The testing protocol undertaken by Envision was designed to determine:
- The consistency of the neutralization unit and its components
- The
acceptability of the resultant effluent for disposal in the sanitary
sewer
- The practicality of using the neutralization unit
with this equipment/plate/chemistry configuration Process comments
The Fuji Luxcel 9600 Computer to Plate processor is designed to minimize
energy and processing chemistry usage. Along with using very low
chemistry replenishment rates, the Fuji Luxcel 9600 processor minimizes
the amount
of water used for processing. When combined with the chemistry formulation,
the water minimization feature is environmentally preferable over
previous water recirculation technology.
The developer replenisher is added to the processor on a per plate
basis as well as and on a per hour basis. When the chemistry is
injected into
the processor, a corresponding amount of used chemistry overflows
into the neutralizer unit. The overflow chemistry is captured in
an internal
tank within the neutralizer unit. When a sufficient quantity is
collected it is neutralized, and then discharged to the sanitary
drain. To ensure consistent testing, it was necessary to use a
consistent sampling time frame. To do this we captured the total
amount of
wastewater flowing to the sanitary sewer from the CtP and neutralizer
for a one-minute period. The actual flow rate was measured at 20
Litres per minute.
This became
our sample period as it represented a complete batch cycle for the
CtP neutralization unit/CtP combination.
Installation of neutralization
unit:
The Metafix unit was installed on June 11. Operation of the neutralizer
was in accordance with manufacturers specifications. The unit was adjusted
to inject a sufficient amount of neutralizer into the reaction chamber
to bring the pH of the effluent within the compliance limits of the sewer
use bylaw. The initial pH test at the time of installation showed an
effluent pH of 9.7. The unit was then considered to be ready for production
and the sampling program set to begin. However, the processor/neutralizer
configuration
was not used for regular production until early July. Therefore the sampling
program was delayed until July 13.
Neutralizer unit testing:
The sampling period ran from July 13th until September 24th. During
the test period, the unit operated normally. It handled the effluent
in a manner that met the requirements of the Toronto sewer
use bylaw.
The testing period included two occurrences when the contents of the
processor tanks were transferred to the neutralization unit along with
large amounts of water, during a processor maintenance event. The neutralizer
unit continued to operate normally, and the effluent was within required
parameters during both maintenance events.
At the time each sample was taken the following items were checked
and verified:
- Correct operation of the pumps
- Ratio of the neutralizer against
the developer overflow
- Calibration of the pH probe within the Metafix
unit
- Timing of the ejet evacuation step
- pH of the effluent being discharged
- Neutralizer
unit operational consistency
Over the time of the sample program,
the staff at "customer
name withheld" was asked for
input on the operation of the neutralizer unit. All comments
indicated that
they did not have to intervene in the operation of the Metafix
unit. The unit was considered to be 100% operational during the
testing period.
pH probe calibration
At each sampling event, the accuracy of the internal pH probe was checked.
It was found to agree with calibrated test equipment within an acceptable
tolerance of +/- 0.2. The internal pH probe did not require re-calibration
during the sampling program.
Neutralizer effectiveness
The neutralization unit was operated at different neutralizer to developer
overflow ratios. During these tests, the pH results were predictable.
TABLE 1
| Date |
Total Neutralizer |
Total Litres |
pH |
Ratio |
| 12-Jun |
1 |
14 |
9.7 |
8.3 |
| 13-Jul |
7 |
72 |
8.9 |
11.1 |
| 17-Jul |
9 |
89 |
9.4 |
11.1 |
| 20-Jul |
9 |
96 |
9.4 |
11.1 |
| 24-Jul |
11 |
116 |
9.4 |
11.1 |
| 27-Jul |
12 |
124 |
9.2 |
11.1 |
| 31-Jul |
21 |
221 |
6.6* |
11.1 |
| 3-Aug |
29 |
321 |
6.1* |
11.1 |
| 9-Aug |
34 |
375 |
6.6* |
11.1 |
| 17-Aug |
40 |
443 |
9.4 |
11.1 |
| 24-Aug |
45 |
497 |
9.5 |
11.1 |
| 31-Aug |
55 |
608 |
9.6 |
11.1 |
| 24-Sep |
90 |
991 |
8.9 |
11.1 |
* These pH results are within acceptable limits for disposal to the sanitary
sewer in the City of Toronto. Please note the neutralizer unit handled
large amounts of rinse water from maintenance operations. This was inadvertently
directed to the neutralizer instead of the drain. These results are within
expectations. Although no user intervention was required, the neutralization
unit permits the user to raise or lower the pH as required by local regulations.
Table 1 Definitions:
Date - The date on which the samples of effluent were taken
Total Neutralizer - The readout of the accumulative amount of neutralizer used
to date.
Total Litres - This represents a running total of the amount of effluent processed
through the neutralizer unit
pH - The pH number represents the pH reading of the neutralized effluent
in the reaction chamber, prior to being discharged to the drain.
Ratio - This figure represents the developer tank overflow to the neutralizer
added
to the reaction chamber to make one batch. The altering of this
ratio provides the ability to raise or lower the pH of the effluent.
Analytical commentary:
Aluminum
At the time of the equipment being first used for regular production,
the aluminum content in the effluent was found to be 3 times the sewer
use compliance limits. This was the first use of the Metafix unit with
this process chemistry combination. Therefore a pump adjustment was made
to configure the Metafix equipment for this specific process chemistry/plate
combination. Subsequent analytical results confirmed the pump adjustment
had brought the aluminum levels within compliance limits.
Biological Oxygen Demand (BOD)
With the exception of the total water flow tests; all samples were taken
from the internal reaction chamber of the Metafix neutralization unit.
During the final sampling the BOD was measured at 2 times the sewer use
compliance limit. However when reaction chamber empties it combines with
the process water prior to the entry to the sanitary sewer drain. The
ratio is 1 part effluent from the reaction chamber to 10 parts process
water. The resultant BOD concentration from the combined effluent streams
will be within acceptable levels.
Summation
In our opinion, the effluent from the Fuji Luxcel 9600 CtP installed
at "customer name withheld", is operating in compliance with
the City of Toronto, sewer-use by-law #457-2000, following treatment
through the Metafix pH Neutralization
Unit. Sample analysis verified that the resultant pH following neutralization
can be predicted, and controlled using recommended operating procedures.
We also noted that the effluent from the CtP did not have a tendency
to form a gel like substance. This property reduces the possibility of
drain problems.
Envision Compliance Ltd.
T. A. Gorham
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