OPERATING MANUAL
UF-70 OIL/WATER FEG SYSTEM
WITH PERMEATE RECYCLE
INSTALLATION
OPERATION
MAINTENANCE
PARTS
KOCH MEMBRANE SYSTEMS, INC.
850 Main Street
Wilmington, MA 01887
(978) 657-4250
MARCH 1992
TABLE OF CONTENTS
Page
PRECAUTIONS . . . . . . . . . . . . . . . . . . . . . i
GLOSSARY . . . . . . . . . . . . . . . . . . . . . . ii
WATER QUALITY GUIDELINES . . . . . . . . . . . . . . v
1.0
INTRODUCTION . . . . . . . . . . . . . . . . .
1.1 ULTRAFILTRATION . . . . . . . . . . . . .
1.2 FEG TUBE DESCRIPTION . . . . . . . . . .
Figure 1.1 General Ultrafiltration . . .
Figure 1.2 FEG Tube Description . . . .
1.3 MODE OF OPERATION . . . . . . . . . . . .
1.3.1 Batch Operation . . . . . . . . .
1.3.2 Modified Batch Operation . . . . .
1.4 OPERATION PARAMETERS AND LIMITATIONS
FOR OIL/WATER EMULSIONS . . . . . . . . .
Figure 1.3 Batch Flow Schematic . . . .
Figure 1.4 Modified Batch Flow Schematic
1.5 PRELIMINARY SYSTEM CHECKS . . . . . . . .
1.6 FLUSHING MEMBRANE PRESERVATIVE . . . . .
1.7 SYSTEM ALARMS AND FAULTS . . . . . . . .
1.7.1 RECYCLE . . . . . . . . . . . . . . . . .
1.8 ROUTINE CHECKS AND DATA COLLECTION . . .
Figure 1.5 Performance Log
Ultrafiltration Systems . . . . . . . . .
2.0
ROUTINE OPERATING PROCEDURES . . . . . . . . .
2.1 SYSTEM DESCRIPTION . . . . . . . . . . .
2.1.1 UF-70 O/W FEG System Description .
2.1.2 UF-70 O/W FEG Component
Description . . . . . . . . . . .
Figure 2.1 Simplified Flow Schematic . .
2.2 SYSTEM START-UP . . . . . . . . . . . . .
Figure 2.2 Flow Schematic "Process Mode"
2.2.1 RECYCLE MODE. . . . . . . . . . . . . . .
2.3 PROCESS COMPLETION . . . . . . . . . . .
2.3.1 Batch Systems . . . . . . . . . .
2.4 BRIEF SHUTDOWN PROCEDURE . . . . . . . .
2.5 EXTENDED SHUTDOWN PROCEDURE . . . . . . .
2.6 PRESERVATIVE SOLUTIONS . . . . . . . . .
Table 2.1 Preservative Solutions . . . .
2.7 CLEANING PROCEDURES . . . . . . . . . . .
2.7.1 System Draining and Displacement .
Figure 2.3 Flow Schematic "Displacemet
Mode" . . . . . . . . . . . .
2.7.2 Chemical Cleaning . . . . . . . .
TABLE OF CONTENTS
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1-1
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1-1
1-2
1-3
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1-4
1-4
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1-4
1-5
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2.5A
2-6
2-6
2-6
2-7
2-7
2-7
2-8
2-8
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. 2-10
(continued)
Figure 2.4 Flow Schematic "Cleaning Mode".
2.7.3 Mechanical Cleaning
Spongeballing . . . . . . . . . . .
Table 2.2 Cleaning Formulations for
Oil Water Emulsion
Ultrafiltration Systems . . . .
Figure 2.5 Flow Schematic
"Spongeballing" . . . . . . . .
3.0
WATER FLUX DETERMINATION . . . . . . . .
3.1 STANDARD CONDITIONS AND CORRECTIONS
3.2 MEASURED FLUX EXPEDIENT . . . . . .
Table 3.1 Water Flux Temperature
Correction Factor (F) .
Page
2-11
2-14
2-15
2-17
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. . . . 3-2
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4.0
MAINTENANCE . . . . . . . . . . .
4.1 REGULAR CHECKS . . . . . . .
4.2 BYPASS OF LEAKING MEMBRANES .
Figure 4.1 Bypass of Leaking
4.3 TROUBLESHOOTING . . . . . . .
4.4 MEMBRANE TUBE REPLACEMENT . .
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Membranes
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4-1
4-1
4-1
4-1
4-2
4-2
5.0
COMPONENT SPECIFICATIONS . .
5.1 PUMP, MOTOR, COUPLINGS
5.2 VALVES . . . . . . . .
5.3 MISCELLANEOUS . . . . .
5.4 REPLACEMENT PARTS LIST.
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5-1
5-1
5-3
5-4
6.0
INSTRUMENTS AND CONTROLS . . . . . .
6.1 Pressure Gauges . . . . . . . .
6.2 Low Pressure Switch, PSI-1 . .
6.3 Temperature Indicator, TI-1 . .
6.4 Temperature Switch, TSH-1 . . .
6.5 Permeate Flowmeter, FM-1 . . .
6.6 Permeate Bypass Flowmeter, FM-2
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6-2
6-2
7.0
ELECTRICAL . . . . . . . . . . . . . . . . . . . 7-1
I
APPENDIX
CIRCULATING PUMP SPECIFICATION SHEET . . . . . . AI-1
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PRECAUTIONS
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1.
Membranes must not be allowed to dry out.
remain filled if the system is shut down.
irreversible.
The tubes must
Membrane dryout is
2.
No anti-foam agents of any kind are to be introduced into the
Koch ultrafiltration system without prior approval from Koch.
3.
No silicone-based materials (waterproofing sprays, lubricating
fluids or greases, etc.) are to be used in or around the Koch
ultrafiltration system. Using these materials in the system
in any amount will cause complete and irreversible membrane
fouling.
4.
Provisions must be made for properly venting the system during
shutdown procedures and draining. The vacuum breaker/vent
systems provided with all Koch systems must be maintained in
proper working order to keep the Koch membrane replacement
policy in force. If pressure on the permeate side of the
membrane exceeds the pressure on the process side by more than
five (5) PSI, membrane delamination may result.
5.
Minimize the time the system is under low flow conditions.
These are periods when bypass valves are open or circulating
pumps are not running.
6.
NEVER RUN THE ULTRAFILTER WITH THE PERMEATE VALVES CLOSED!
7.
Never start a pump without throttling the pump discharge
valve. Throttling will prevent a pressure shock wave from
damaging the membranes.
8.
The maximum pressure the membranes should be exposed to is 70
PSIG.
9.
The maximum temperature the membranes should be exposed to is
130°F.
10.
The allowable pH range for membranes (continuous) is 2.0-10.0
at 120°F (49°C).
-iGLOSSARY
Air Vent
A valve which is manually opened to allow
air to escape from the system to the
atmosphere during start-up, and opened at
shutdown to prevent a vacuum in the
system.
Cleaning System
An accessory system incorporated in the UF
unit to clean the membranes if they become
fouled. It consists of a cleaning tank,
pump, and associated piping and valves.
Concentrate
The mixture returned to the concentrate
holding tank after processing.
Deionized Water
Water from which virtually all dissolved
solids have been removed.
Demineralized Water
See "deionized water."
Emulsified Oils
A suspension of oil droplets in water made
by blending the oil with emulsifying
agents and other material. Emulsions are
also called "soluble oils," a misnomer,
but generally used in the metal working
industry.
Flux
The rate of permeation, usually expressed
as GFD (gallons per square foot of
membrane area per day).
Fouling
A condition in which the membrane flux
rate is restricted due to the accumulation
of material on the membrane surface.
Free Oil
All unemulsified oils that are present in
the process fluid.
-iiGLOSSARY
Membrane Processing
Separation of the elements of a fluid, at
the molecular level, by a membrane. The
membrane will pass through smaller
molecules while retaining larger
molecules.
Metal Fines
Very small slivers of metal generally
produced in a grinding operation.
Oil Skimmer
A device for skimming off the free oil on
the surface of the process fluid in a
tank.
Permeable
Porous to the passage or penetration by
fluids.
Permeate
The term used to describe the passage of
water through a membrane. It is also the
fluid (basically water) separated from the
process fluid in the Koch ultrafiltration
system.
Permeate Back Pressure
Pressure exerted on the permeate side of
the membrane. If this pressure exceeds 5
PSI, the membrane could be damaged.
Preservative Solution
A solution that is introduced to the
membrane tubes during the idle periods to
prevent membrane deterioration.
Process Fluid
The oil and water mixture (or other
process fluid) delivered to the UF unit
for processing.
Purge
A displacement procedure that exchanges
the process fluid in the UF system with
water from the cleaning tank.
-iiiGLOSSARY
Sludge
Deposits on the bottom of the process
tanks that are undesirable as they will
foul the membranes.
Spongeballing
A method of hydraulically forcing balls of
sponge-like material through the flow
channel of a tubular membrane.
Surfactant
Surface active agents used for cleaning
the UF system.
Tramp Oil
See " Free Oil."
U-bend
A "U" shaped tube used to connect one
membrane tube to another in the same pass
to provide a series-connected
configuration.
Ultrafilter
An arrangement of Koch tubular membranes
used in the ultrafiltration process.
Ultrafiltrate
A synonym for permeate.
Ultrafiltration
A pressure-driven permeation process used
in conjunction with semi-permeable
membranes. Flow rate through the
membranes and permeate selectivity are
governed by pore size, distribution,
membrane porosity, and the specific
process fluid itself.
-iv-
WATER QUALITY GUIDELINES
Ultrafiltration membranes are susceptible to fouling from water
that is high in mineral content or suspended material. For this
reason the water used in flushing and cleaning the membranes should
conform to the following:
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Turbidity less than 0.1 NTU
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Iron less than 0.3 ppm
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Manganese less than 0.05 ppm
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Aluminum less than 10 ppm
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Calcium less than 10 ppm
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Silica less than 10 ppm
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Free from particulate matter such as rust, scale,
flake material, sandy granular material, slurries,
scum, algae.
Softened water (less than 60 mg eq CaCO3/liter) or evaporator
condensate is generally acceptable for cleaning and flushing
ultrafiltration membranes.
-v-
1.0
INTRODUCTION
1.1 ULTRAFILTRATION
Ultrafiltration is an industrial process in which semi-permeable
membranes are used to separate water and some dissolved low
molecular weight materials from a mixture that is submitted for
processing.
The goal of the process is to effectively fractionate the original
process stream into a concentrate stream and a very low
concentration permeate stream. The concentrate is then disposed of
by the most economical means or further processed if the
concentrate contains valuable material. The permeate stream is
normally discharged to a sanitary sewer or recycled to rinse
systems since it is relatively clean.
In Koch ultrafilters, the membranes are tubular in shape and are
bonded to the inner surface of the tube support backings. The
process fluid is circulated through these membrane tubes under
pressure. The oil is retained and the water is separated from the
mixture as shown in Figure 1.1.
The pore structure of the membrane acts as a filter, passing water
and small solutes (e.g., salts), while retaining larger emulsified
and suspended matter. The pores of ultrafiltration membranes are
much smaller than the particles rejected. These particles cannot
enter the membrane structure and hence the pores cannot become
plugged.
1.2 FEG TUBE DESCRIPTION
In FEG ultrafilters, the membrane is cylindrical and bonded to the
inner surface of a protective, porous backing called a support
tube. Each membrane and backing is enclosed in a tubular housing.
The housing is threaded at both ends for connecting them in series
and to the process inlet and outlet manifolds.
1-1
SMALL
MOLECULES
LARGE
MOLECULES
MEMBRANE
FIGURE 1.1 GENERAL ULTRAFILTRATION
Boot seals, installed at each end of the membrane and the support
tube, isolate the permeate from the process stream. The boot seal
wraps around the inside and the outside of the tube ends. A
stainless steel ferrule holds the boot seal in place, the outer
portion of the boot has two formed O-rings to provide the boot-tohousing seal (see Figure 1.2). When in operation, permeate travels
through the membrane, collects in the annular space between the
membrane tube housing and the boot seals, and then flows out of the
permeate port.
Tubular membrane housing specifications are as follows:
Tubular Membrane Module Length10 Feet
Tubular Membrane Area
2.2 Square Feet
Fluid Volume per Tube
0.437 Gallons
0.054 Cubic Feet
1-3
1.3 MODE OF OPERATION
During normal operation the process fluids can be processed in
either a batch or a modified batch mode. Each of the operating
modes is described in more detail below.
1.3.1
BATCH OPERATION
In batch operation, process fluid is pumped from a large process
tank through the ultrafilter membrane tubes and back to the process
tank (see Figure 1.3). As water permeates from the ultrafilter,
the emulsion becomes more concentrated. When a predetermined
concentration has been reached, the batch is completed and the
remaining emulsion is disposed of in whatever manner best suits the
operator. The water that is removed from the emulsion is directed
to drain or reused depending upon the individual application. The
process tank is then refilled and processing of a new batch will
begin following a cleaning of the ultrafilter.
1.3.2
MODIFIED BATCH OPERATION
Modified batch operation differs from the batch operation mode only
in that as the level in the process tank drops due to the removal
of permeate, fresh process feed material is added to the process
tank. The advantages of the modified batch mode of operation are
that run times are extended and cleaning frequency is reduced.
1.4 OPERATIONAL PARAMETERS AND LIMITATIONS FOR OIL/WATER EMULSIONS
Maximum operating pressure at pass inlet ................. 70 PSIG
Maximum operating pressure at pass outlet ................ 20 PSIG
Minimum operating pressure at pass outlet ................ 10 PSIG
Pressure drop at 30 GPM/tube ............................. 33 PSIG
Minimum System Circulation Rate .......................... 120 GPM
Maximum Operating Temperature ............................ 130°F
Maximum back pressure at permeate outlet ................. 5 PSIG
Membrane area per 10 foot FEG tube .................... 2.2 sq. ft.
1-4
PROCESS
FEED
UF
PROCESS
TANK
RECIRCULATION LOOP
PERMEATE
RECIRCULATION PUMP
FIGURE 1.4 MODIFIED BATCH FLOW SCHEMATIC
Hold up volume per 10 foot tube ........................ 0.437 gal.
Minimum flow per series pass of tubes ..................
30 GPM
PH range for HFM membranes at 120°F (continuous)........
2.0-10.0
PH range for HFP membranes at 120°F (continuous)........
2.0-10.0
1.5
1.
PRELIMINARY SYSTEM CHECKS
Check the membrane housing U-bends and terminator nuts for
tightness. Hand tighten only. Check the permeate hose
connections on the membrane shells. Hand tighten (only) these
connections.
2.
Check the operation of the pressure and temperature switches.
3.
Open the pressure gauge isolation valves 50%.
1.6 FLUSHING MEMBRANE PRESERVATIVE
Koch ultrafiltration membranes have been impregnated with a
preservative solution prior to shipment. This must be removed from
the system prior to operation. To remove the preservative, follow
the cleaning procedure outlined in Section 2.7 using cleaning
solutions #3 or #4 as described in Table 2.2.
1.7 SYSTEM ALARMS AND FAULTS
Koch ultrafiltration systems are protected by several different
alarms. These alarms when actuated will shut the system down to
protect the membranes. All systems utilize high temperature and
low pressure alarms. Other alarms that may be included in a
system, (depending on the system size), are high concentrate, high
pressure, high pan level and low process tank level.
After an alarm fault has been corrected, the system may be
restarted as described in Section 2.2. Refer to Section 4.3 "Troubleshooting" for guidance in correcting faults.
1-7
1.8 ROUTINE CHECKS AND DATA COLLECTION
The ultrafiltration system should be checked at least twice a
shift. These checks should include a visual inspection for leaks
and a visual check of the permeate quality and flow rate. In
addition, operating data should be recorded in the Koch Membrane
Systems Operating Log Book supplied with each system. A sample
data sheet is shown on the following page.
1-8
Performance Log - Ultrafiltration Systems
SYSTEM INFORMATION
COMPANY NAME:
SPENT OIL INFORMATION
SOURCE:
LOCATION:
FREE OIL QUANTITY:
SYSTEM IDENTIFICATION:
OPERATOR:
DATE/
TIME
KOCH MEMBRANE SYSTEMS INC.
850 MAIN STREET
WILMINGTON, MA. 01887
PHONE: (800) 343-0499
SLUDGE/SOLIDS:
FEED INFORMATION
OIL pH
%
KOCH
COLOR
VOL.
ADDED
CLEANING
SYSTEM
NUMBER
PERM
VOL.
TIME
CONC.
P IN P OUT TEMP RATE
GPM REMOVED HOUR SOL'N
PSI PSI
F
FLUX
GPM
REMARKS
2.0
ROUTINE OPERATING PROCEDURES
2.1 SYSTEM DESCRIPTION
2.1.1 UF-70 O/W FEG System Description
The UF-70 system consists of up to 4 parallel passes of 8 tubes in
series. Each membrane tube is ten feet long and contains 2.2
square feet of membrane area, giving the unit an area of 70.4
square feet.
Physically the rest of the system consists of a circulating pump
rated for 120 GPM at 157 FT. HD., 50 gallon cleaning tank,
associated piping and various switches and gauges. A control panel
which contains the pump start/stop buttons, indicator lights and
alarms is mounted on the unit.
The cleaning tank is provided for flushing the membrane tubes.
This is accomplished by the proper arrangement of the valves which
allow for the circulation of the cleaning solution with the same
pump used for the process fluid. Permeate is routed to return to
the cleaning tank during this period.
2.1.2 UF-70 O/W FEG Component Description
The following component listing is to be utilized to cross
reference component descriptions used in this manual with component
numbers shown on Koch System Flow Schematic C5046-5041 which is
included with this manual. Refer to Figure 2.1, Simplified Flow
Schematic.
P-1
Circulation Pump
V-1
Process Inlet Valve
V-2
Circulation Pump Discharge Valve
V-3
Process Outlet Valve
V-4
Circulation Pump Suction Valve
(Recirculation Valve)
V-5
Cleaning Return Valve and Vent Valve
V-6
Permeate Flowmeter Bypass Valve
2-1
2-2
V-8
V-9
V-10
V-11
V-12
V-13
V-14
V-15
V-16
V-17, V-18
V-19
FI-1, FI-2
Permeate to Cleaning Tank Valve
Permeate to Drain Valve
Cleaning Tank Float Valve
System Drain Valve
Cleaning Tank Feed Valve
High Pressure Gauge Isolation Valve
Low Pressure Gauge Isolation Valve
Permeate Flowmeter Isolation Valve
Permeate Flowmeter Isolation Valve
Spongeball Insertion Isolation Valve
Spongeball Insertion Drain Valve
Permeate Flowmeter
2.2 SYSTEM START-UP (Refer to Figure 2.2)
The following procedure outlines the start-up procedure for an
oil/water mixture being processed as a BATCH operation.
1.
Turn on the main power.
2.
Close the following valves:
V-2
Circulation Pump Discharge Valve
V-4
Recirculation Valve
V-5
Cleaning Return Valve
V-6
Permeate Flowmeter Bypass Valve
V-8
Permeate to Cleaning Tank Valve
V-11
System Drain Valve
V-12
Cleaning Feed Valve
V-17, V-18
Spongeball Insertion Isolation Valves
3.
Open the following valves:
V-1
V-3
System Process Inlet Valve
Process Outlet Valve
2-3
V-104
FI 100
PI
101
V-102
PI
100
TI
100
UF
70
V-101
V-101
SPONGEBALL
RETRIEVAL
BASKET
P-1
SPONGEBALL
INSERTION
V-108
PROCESS/CLEAN
TANK (100 GALS)
V-103
FIGURE 2.2 FLOW SCHEMATIC: "PROCESS MODE"
3.
Open the following valves: (continued)
V-9
Permeate to Drain Valve and any other
valves so as to provide unrestricted flow
of permeate to drain or other desired
location.
V-15, V-16
Permeate Flowmeter Isolation Valve
V-19
Spongeball Insertion Drain Valve
4.
Start the Circulation Pump, P-1.
5.
Crack open Circulation Pump Discharge Valve, V-2.
6.
Slowly fill the system. When fluid returns to the
process tank or permeate flows steadily through the
permeate flowmeter, slowly open V-2 all the way.
7.
The system should be as shown in Figure 2.2 Flow
Schematic "Process Mode."
8.
Adjust the Process Outlet Valve, V-3 to maintain a
minimum cabinet outlet pressure of 10 PSI. The inlet
pressure should not exceed 65 PSI. The difference
between the two pressures should be at minimum 33 PSI.
(Usually, V-1 will be completely open but if the inlet
pressure exceeds 65 PSI, then V-1 must be shut slightly).
Use V-4 circulation pump suction valve to adjust
pressures as well.
9.
Examine the permeate. It may have a color, but it should
remain clear. If it should remain cloudy for more than
two hours, refer to Section 4.2, Bypass of Leaking
Membranes.
2-5
2.3
PROCESS COMPLETION
Batch Systems (See Figure 2.3 Flow Schematic
Displacement Mode)
When the waste has been concentrated to the extent desired, the
batch should be terminated as follows.
1.
Slowly CLOSE the Circulation Pump Discharge Valve, V-2.
2.
STOP the Circulation Pump, P-1.
3.
PURGE the concentrate from the system to the process tank
as follows:
a.
Fill the cleaning tank with hot (120°F) water.
b.
Open the cleaning tank feed valve, V-12, leave the
process outlet valve, V-3, open.
c.
Close the process tank inlet valve, V-1.
d.
Close the circulation pump suction valve, V-4.
e.
Close the circulation pump discharge valve, V-2.
f.
Open the permeate flowmeter bypass valve, V-6.
g.
Start the circulation pump, P-1.
h.
Slowly open the circulation pump discharge valve, V2, and pump 1/2 to 3/4 of the cleaning tank contents
through the system to the process tank. The system
should now be as shown in Figure 2.3 Flow Schematic
"Displace to Process Tank."
i.
Close the circulation pump discharge valve, V-2.
j.
Stop the circulation pump, P-1.
k.
Dispose of the concentrate in the process tank in
the manner that best suits the operator.
2.3.1
2.4 BRIEF SHUTDOWN PROCEDURE
If the system is to be shutdown for 15 minutes or less, the waste
may be left in the system. This is not always the case however.
Each application is different. A trade off in flux rate loss vs.
cleaning will have to be determined by the operator(s).
2-6
Perform a short term shutdown as follows:
1.
2.
3.
2.5
Slowly close the Circulation Pump Discharge Valve, V-2
Stop the Circulation Pump, P-1.
The system may be restarted as described in Section
2.2.1.
EXTENDED SHUTDOWN PROCEDURES
1.
See Sections 2.7.1 and 2.7.2 (steps 1-17).
2.
Prepare the system for storage by filling the cleaning
tank with the appropriate solution from Table 2.1.
3.
Circulate the storage/preservation solution for 20
minutes as in a normal cleaning (Section 2.7).
4.
Slowly close the circulation pump discharge valve, V-2.
5.
Stop the circulation pump, P-1.
6.
Ensure that all the system valves are closed to lock the
preservative solution in the system.
2.6 PRESERVATIVE SOLUTIONS
If the system is to be shut down for any length of time, the
membranes must be kept wet with a preservative solution. The
following table lists the type of preservative solutions to be used
as determined by the length of the shutdown.
TABLE 2.1
PRESERVATIVE SOLUTIONS
Length of Shutdown
HFA, HFM, HFP
15 minutes to 2 days
Clean Water
2 days to 30 days
99.5% Water
99.5% Water
0.5% Sodium Benzoate 0.5% Sodium Benzoate
30 days or longer
80% Glycerine
20% Water
2-7
2.7
CLEANING PROCEDURES
HFD
Clean Water
99.5% Water
0.5% Sodium Benzoate
Cleaning is necessary when the flux rate drops to an unacceptable
level, generally 30% of the design flux. The frequency of cleaning
must be determined by operational experience and plant
requirements.
2.7.1 System Draining and Displacement (Refer to Figure 2.3 Flow
Schematic)
Prior to any cleaning procedure or extended shutdown (Section 2.4
or 2.5), the waste within the system must be removed to maximize
the efficiency of the cleaning chemicals and to minimize fouling
during extended shutdown.
If the system has no direct draining to the tank, displace the
waste with water through the process return line. Perform this
displacement according to the procedure below. Once the waste has
been displaced, perform a normal cleaning. (Section 2.7.2.)
Displacement Procedure
1.
Fill the cleaning tank with hot (120°F) water.
2.
Slowly close the Circulation Pump Discharge Valve, V-2.
3.
Stop the Circulation Pump, P-1.
4.
Close the Process Inlet Valve, V-1.
5.
Close the Circulation Pump Suction Valve, V-4.
6.
The Process Outlet Valve, V-3 should remain open.
7.
Open the cleaning tank feed valve, V-12
8.
Open the permeate flowmeter bypass valve, V-6.
9.
Start the Circulation Pump, P-1.
10. Crack open the Circulation Pump Discharge Valve, V-2.
Slowly fill the system. When fluid reaches the process
tank, slowly open V-2 100%.
11. The system should now be as described in Flow Schematic
"Displacement Mode", Figure 2.3.
12. PUMP 1/2 to 3/4 of the tank full of water through the
system.
2-8
2-9
Displacement Procedure (continued)
12. CLOSE the Circulation Pump Discharge Valve, V-2.
13. STOP the Circulation Pump, P-1.
14. CLOSE the Process Return Valve, V-3.
15. Drain the system by performing the following steps:
a.
OPEN the following valves:
V-11
System Drain Valve
V-2
Circulation Pump Discharge Valve
V-4
Circulation Pump Suction Valve
V-5
Cleaning Return Valve
b.
CLOSE the following valves:
V-12
Cleaning Tank Feed Valve
16. Fill the cleaning tank with hot (120°F) water.
2.7.2 Chemical Cleaning (Refer to Figure 2.4 Flow Schematic
"Cleaning Mode.")
The normal cleaning solution is a mixture of 1.0% by volume of Koch
Liquid Detergent (KLD) pH adjusted to 10-10.5 with caustic in hot
(120°F) water. Other cleaning solutions are listed in Table 2.2.
If a cleaning is not successfully accomplished with a hot detergent
wash (as determined by a water flux test), you should contact the
Koch Technical Service Group for assistance.
The following procedure should be followed when performing a
chemical cleaning:
1.
Remove the waste oil from the system by following the
displacement procedure outlined in Section 2.7.1.
2.
Fill the cleaning tank with the appropriate cleaning
solution from Table 2.2.
3.
Close the following valves:
V-1
Process Inlet Valve
V-2
Circulation Pump Discharge Valve
2-10
V-104
FI 100
PI
V-102
101
PI
100
TI
100
UF
70
V-101
SPONGEBALL
RETRIEVAL
BASKET
P-1
SPONGEBALL
INSERTION
V-105
PROCESS/CLEAN
TANK (100 GALS)
V-103
FIGURE 2.4 FLOW SCHEMATIC: "CLEANING MODE"
3.
Close the following valves: (continued)
V-3
Process Outlet Valve
V-4
Circulation Pump Suction Valve
V-9
Permeate to Drain Valve
V-11
System Drain Valve
4.
Open the following valves:
V-5
Cleaning Return/Vent Valve
V-6
Permeate Flowmeter Bypass Valve
V-8
Permeate to Cleaning Tank Valve
V-12
Cleaning Feed Valve
V-15
Permeate Flowmeter Isolation Valve
V-16
Permeate Flowmeter Isolation Valve
5.
Start the Circulation Pump.
6.
Slowly open the Circulation Pump Discharge Valve, V-2.
The system should now be as shown in Figure 2.4 Flow
Schematic "Cleaning Mode."
7.
Adjust the Circulation Pump Discharge Valve, V-2 and the
Circulation Pump Suction Valve, V-4 to obtain a membrane
inlet pressure of 50-55 PSIG and a membrane outlet
pressure of 18-20 PSIG. Maintain a minimum differential
of 33 PSIG between the inlet and outlet pressures.
8.
Circulate the cleaning solution for approximately two
hours or until the permeate rate stops increasing.
Unusually long or repeated cleanings may be required for
severely fouled membranes. DO NOT ALLOW the system
temperature to exceed 125°F.
9.
If a chemical cleaning does not restore adequate flux
rate to the system, mechanically clean the membranes as
described in Section 2.7.3. If in doubt as to whether or
2-12
not this mechanical cleaning is necessary, measure the
water flux of the system (see Section 3.0). If the
measured water flux is less than that listed in Table
3.1, a mechanical cleaning should be performed. The
water flux is measured by circulating clean warm water
(70-100°F) through the system in the same manner used
during the cleaning of the system.
10.
On the completion of a cleaning, shut the system down by
closing the Circulation Pump Discharge Valve, V-2 and
stopping the Circulation Pump, P-1.
11.
Transfer the contents of the cleaning tank to the process
tank by the following series of steps:
12.
OPEN the following valves:
V-3
Process Outlet Valve
V-5
Cleaning Return and Vent Valve
V-6
Permeate Flowmeter Bypass Valve
V-8
Permeate to Cleaning Tank Valve
V-12
Cleaning Tank Feed Valve
13.
CLOSE the following valves:
V-1
Process Tank Feed Valve
V-2
Circulation Pump Discharge Valve
V-4
Circulation Pump Suction Valve
V-9
Permeate to Drain Valve
V-11
System Drain Valve
14.
Start the Circulation Pump, P-1.
15.
Slowly open the Circulation Pump Discharge Valve, V-2.
16.
When the system is vented, close the Cleaning Return and
Vent Valve, V-5.
2-13
17.
When the cleaning tank is empty, close the Circulation
Pump Discharge Valve, V-2 and stop the circulation pump.
18.
The system can now be started on a process fluid as
described in Section 2.2.
Mechanical Cleaning Spongeballing (See Figure 2.5 Flow
Schematic "Spongeballing")
If after a chemical cleaning, the corrected water flux of the
system is less than normal (see Section 3.0), mechanically cleaning
the system may be necessary. Mechanically cleaning the membranes
is performed by hydraulically forcing spherical sponges through the
membrane tubes. It is normally done during chemical cleaning.
2.7.3
Spongeballs are available from Koch or they may be cut from finecelled soft sponge (approximately 1-1/4 inches in diameter).
Spongeballing a system is performed by following the procedure
described below:
1.
The system should be in the cleaning mode (see Section
2.7).
2.
Ensure that the spongeball insertion valves, V-17 and V18 are closed, the spongeball insertion drain valve V-19
is open, and the spongeball retrieval basket is
positioned under the cleaning return line.
3.
Remove the victaulic clamp and cover from the spongeball
insertion rig.
4.
Moisten and insert approximately ten (10) spongeballs.
2-14
TABLE 2.2 CLEANING FORMULATIONS FOR
OIL/WATER EMULSION ULTRAFILTRATION SYSTEMS
Solution #
Components
% Concentrate
1
Ultraclean A
2
Ultraclean A
KOCHKLEEN 221
3
Koch Liquid
KLD III
1.0%
May be more
effective than UC-A.
Excellent for
complexing metals.
4
Koch Liquid
KLD III
KOCHKLEEN 221
1.0%
More effective than
KLD alone with some
process streams.
5
Note:
KOCHKLEEN 120
KOCHKLEEN 221
.5%
Comments
0.5%
Add until pH
is 10.0-10.5
Add until pH
is 10.0-10.5
2.0%
Add until pH
is 3.0 - 3.5
KLD III is a liquid and is
1% solution requires 1 gal
Ultraclean A and KOCHKLEEN
and 2% require 4.2 lbs and
respectively.
Higher concentration
may be required for
severely fouled
membranes.
More effective than
UC-A alone. Do not
use with HFA
membranes.
This cleaner is used
to clean metalfouled membranes. It
is preceeded and
followed by 1 of the
above cleaners.
used on a volume basis. That is a
of KLD III per 100 gal of water.
120 are solids so solutions of .5%
16.7 lbs per 100 gal of water,
2-15
5.
Replace the cover and victaulic clamp. Close the
spongeball insertion drain valve, V-19.
6.
Close V-4 to force spongeballs to the spongeball
retrieval basket.
7.
Open the spongeball insertion valves, V-17 and V-18.
8.
Throttle V-2, to force spongeballs to the inlet manifold.
9.
When all the balls have been caught in the basket in the
cleaning tank, open V-2 and close the spongeball
insertion valves, V-17 and V-18. It should require 2-3
minutes for all the balls to pass through the system.
10.
Repeat steps 1-8 four times. If the flux has not been
restored to an acceptable level, different chemical
cleaning solutions should be used and the chemical wash
repeated.
2-16
V-106
FI 100
PI
101
V-102
PI
100
TI
100
UF
70
V-101
SPONGEBALL
RETRIEVAL
BASKET
P-1
SPONGEBALL
INSERTION
V-105
PROCESS/CLEAN
TANK ( 100 GALS)
V-103
FIGURE 2.5 FLOW SCHEMATICS: "SPONGEBALLING MODE"
KOCHKLEEN®
10/30/01
UF CLEANING PROGRAM - OILY WASTE WATER
Step 1.
Rinse the system
Step 2.
Caustic Cycle
pH 10.0-10.5
125-130 F
90-120 min.
1% KOCHKLEEN KLD III v/v
Adjust pH with KOCHKLEEN 221 if needed
Step 3.
Rinse the system well
Step 4.
Acid Cycle
pH 3.0-4.0
125-130 F
30 min.
2 % KOCHKLEEN 120 w/w
Adjust pH down with KOCHKLEEN 221 if needed
Step 5.
Rinse the system well
Step 6.
Caustic Cycle
pH 10.0-10.5
125-130 F
45 min.
1% KOCHKLEEN KLD III v/v
Adjust pH with KOCHKLEEN 221 if needed
Step 7.
Rinse the system well
Step 8.
Water Flux Readings (GFD)
"Spongeball is recommended during each wash cycle"
Cleaning Precautions:
• Care should be taken not to chill shock the membranes when proceeding from
one step to the next.
• All chemicals should be measured accurately.
• Over-dosage of chemicals will cause shorter membrane life.
Contact KOCH Membrane Systems if you have any questions concerning
the above cleaning procedure.
3.0
WATER FLUX DETERMINATION
Water flux is the rate of permeation measured while circulating
water through the ultrafilters. Determining this rate will give an
indication of the cleanliness of the membrane surface.
3.1 STANDARD CONDITIONS AND CORRECTIONS
Standard conditions for measuring flux set at an average pressure
of 50 PSIG and a temperature of 77°F. Because these conditions are
not always attainable, the measured flux can be corrected for
temperature and pressure. Water flux should, however, be taken at
an average pressure of 20 PSIG or more.
The units for water flux are gallons of permeate per square foot of
membrane surface per day (GFD). Because the permeate rate is
generally measured in gallons per minute, the rate will have to be
converted as follows:
Jm (GFD) = (Permeate rate in GPM) (1440 min/day)
Total membrane area in ft. sq.
The measured flux, Jm, can be corrected to standard conditions by
using the following equation:
Jcorr = (Jm) (100) (F)
Pin + Pout
Where Pin is the inlet pressure
Pout is the outlet pressure
F is the temperature correction factor (see Table 3.1).
3-1
The normal fluxes for clean membranes at standard conditions are
listed below:
Membrane Type
HFM
HFP
Water Flux (GFD) @ 50 PSIG, 25°C
100 - 150
100 - 150
3.2 MEASURED FLUX EXPEDIENT
A convenient method of determining measured flux (GFD) is to divide
the quantity of permeate (in milliliters) collected in 10 seconds
from a series pass of tubes by the number of 10 ft. membrane tubes
in that pass. The resultant number will be measured by flux rate
in GFD for that particular pass.
For example:
tubes.
1600 ml in 10 seconds from a series pass of 8 10 ft.
Jm = 1600 = 200 GFD
8
The measured flux is then corrected for temperature and pressure.
3-2
TABLE 3.1
T(°F)
126
124
122
120
118
117
115
113
112
109
108
106
104
102
100
99
97
95
93
91
90
88
86
84
WATER FLUX TEMPERATURE CORRECTION FACTOR (F)
T(°C)
53
51
50
49
48
47
46
45
44
43
42
41
40
39
38
37
36
35
34
33
32
31
30
29
F
0.595
0.605
0.615
0.625
0.636
0.647
0.658
0.670
0.682
0.694
0.707
0.720
0.734
0.748
0.762
0.777
0.793
0.808
0.825
0.842
0.859
0.877
0.896
0.915
T(°F)
82
81
79
77
75
73
72
70
68
66
64
63
61
59
57
55
54
52
50
48
46
45
43
41
3-3
T(°C)
28
27
26
25
24
23
22
21
20
19
18
17
16
15
14
13
12
11
10
9
8
7
6
5
F
0.935
0.956
0.978
1.000
1.023
1.047
1.072
1.098
1.125
1.152
1.181
1.212
1.243
1.276
1.310
1.346
1.383
1.422
1.463
1.506
1.551
1.598
1.648
1.699
4.0
MAINTENANCE
4.1 REGULAR CHECKS
The following items should be checked and corrected on a regular
basis:
Pump:
-
Bearing lubrication (every two weeks)
Seal leakage (daily)
Secure to bedplate (daily)
Motor:
-
Alignment to pump (excessive current
draw, vibration, heat, etc.) (every
two days)
Secure bedplate (daily)
-
Vacuum Breakers
and Vent Valves:
-
Coupling deterioration (whenever
shutdown)
-
Disassemble, inspect and clean
monthly
4.2 BYPASS OF LEAKING MEMBRANES
A defective (leaking) membrane will cause turbid permeate. This
problem can be overcome without shutting the system down for tube
replacement. The permeate in the defective tube is prevented from
entering the permeate handling lines by plugging the permeate port
(1/4" NPT) of the defective tube and capping the permeate fitting
that is connected to the defective tube. (See Figure 4.1.)
FIGURE 4.1
BYPASS OF LEAKING MEMBRANE
4-1
4.3 TROUBLESHOOTING
The following table is intended to serve as a guide for locating
problems which may occur with the system:
Problem
Low Flux
Probable Cause
Fouled membranes
Corrective Action
Clean or replace
membranes
Improper operating
pressure
Adjust system inlet
and outlet pressure
High feed
concentration
Remove feed from
system
Low temperature
Increase temperature
(but do NOT exceed
125°F)
Batch overconcentrated
Add process fluid to
tank or empty tank and
refill with fresh
process fluid
Empty feed tank
Add feed material
Ruptured membrane tube
Replace tube
Faulty pump
Repair or replace pump
Low pressure switch
activates at more
than 10 PSI
Adjust pressure switch
High temperature
High fluid temperature
Shut down system and
allow to cool
Permeate with
High Turbidity
Leaking membrane
Plug or replace tube
Low Pressure
4.4 MEMBRANE TUBE REPLACEMENT
Generally, the best time to replace a defective membrane tube is
during a shutdown for cleaning. In the meantime, the defective
tube should be isolated to prevent leakage of concentrate into the
permeate (see Section 4.2, "Bypass of Leaking Membrane").
4-2
All new membrane tubes must be prepared before installing as
replacements. Refer to the following sections for the proper
procedure:
A.
Preparing Individual Membrane Tubes
Prepare membrane tubes as follows:
1.
Remove endcaps and permeate plug from the membrane tube.
2.
Hose out the membrane tube with D.I. water.
3.
Drain the membrane tube.
4.
Reinstall the endcaps to protect threads.
B.
Installing Membrane Tubes
After the membrane tube has been prepared by the above procedure,
install it as follows:
1.
Disconnect the permeate hose fittings attached to the
defective membrane tube.
2.
Disconnect the membrane tube to be replaced from the PVC
U-bends or manifold to which it is attached.
3.
Remove the defective membrane tube from the unit.
4.
Install the new membrane tube.
5.
Remove the two protective endcaps from the membrane tube.
6.
Ensure that both the PVC spacers and rubber washers are
installed at both ends of the membrane tube (PVC spacer
goes in first.)
7.
Reconnect the U-bends or manifold connection. Carefully
orient the permeate port into the proper position.
Reconnect permeate tubing.
Start the system as outlined in Section 2.2 "System Startup." If a
process fluid leak appears at the replacement tube U-bend or
manifold coupling, tighten the leaking connection by hand until the
4-3
leak stops. If this does not stop the leak, shut down the unit,
flush the process fluid from the membrane tubes and drain the unit.
Then disconnect the leaking U-bend or manifold coupling and add
another membrane washer to the connection. This should be done
only as a last resort.
C.
Installation of Recycle Option
1.
Plant air supply is connected to the air line located on
the electrical cabinet for operation of recycle valve V21.
2.
An air line must also be connected from the electrical
panel to V-21, to operate the valve.
3.
Recycle valve V-21 is installed so that the "common" port
connects to the UF permeate line. The normally open port
is connected to the permeate "out" or drain line. The
normally closed port is connected to the process tank
line.
4-4
5.0
COMPONENT SPECIFICATIONS
5.1
PUMP, MOTOR, COUPLINGS
1.
Circulating Pump P-1
Horizontal End Suction Centrifugal pump, frame-mounted, all
iron construction, semi-open impeller, mechanical seal.
Capacity:
Pump:
120 GPM @ 157 Ft. HD.
Carver Model 1 1/2" x 2" x 7 LA with 6 1/2 dia.
impeller.
P/N 0121566
IMPORTANT NOTE:CARE MUST BE TAKEN TO INSURE PUMP INSTALLED HAS
PROPER DIAMETER IMPELLER. THIS IS A CRITICAL
POINT.
Motor:
Coupling:
5.2
10 HP at 3500 RPM, 230/460 volt, 3 pH, 60 HZ,
TEFC 215T Frame.
P/N 0110235
Woods Sureflex #6S. 1 3/8" x 1 1/4" standard
keyway.
1 1/4 flange
P/N 0125062
1 3/8 flange
P/N 0125063
sleeve
P/N 0125516
VALVES
Gear Operated Butterfly Valves
a.
Pump Discharge Valve, V-2
2" Butterfly Valve with Gear operator, cast iron body 316
stainless steel disc and shaft. BUNA-N seat and seal.
P/N 0131073
b.
Outlet Valve, V-3, Return to Suction V-4
Same as "a" (above).
P/N 0131073
5-1
Lever Operated Butterfly Valves
a.
Inlet Valve, V-1
3" Butterfly Valve with lever operator, cast iron body.
316 stainless steel disc and shaft. BUNA-N seat and
seal.
P/N 0131082
Cleaning Tank Return Line/Air Vent Valve V-5,
and Drain Valve, V-11
1" SOC true union ball valve, PVC construction, teflon seats
and seals.
GF + Type 342
P/N 0130140
Cleaning Tank Float Valve, V-10
3/4" NPT float valve, brass construction.
P/N 0139105
Permeate Valves, V-15, and V-16
Similar to V-5 and V-11 except 1/2" SOC.
P/N 0130085
Permeate Valves V-6, V-8, V-9
1" IPS true union ball valve, PVC construction, teflon seats
and seals, socket ends.
+ GF + Type 342.
P/N 0130170
Clean Tank To Pump Suction V-12
2" SOC true union ball valve, PVC construction, teflon seat,
Viton seal.
+ GF + Type 342
P/N 0130220
5-2
Pressure Gauge Isolation Valves V-13, V-14
1/2" NPT Ball Valve, steel construction, Endurion coated,
teflon seats and seals. Tee handle.
P/N 0130320
Vacuum Breaker VB-1
1 1/4" NPT x 1" NPT bushing check valve. Carbon steel
construction, stainless steel spring. Crack pressure 1/8 psi.
P/N 0136135
Sponge-Ball Insertion Valves, V-17, V-18
1 1/2" NPT ball valve, steel construction, full port, teflon
seats and seals.
P/N 0130420
Sponge-Ball Drain Valve, V-19
1/2 NPT ball valve, steel construction, teflon seats and
seals.
P/N 0130320
5.3
MISCELLANEOUS
Strainer ST-1
3~ flanged "Y" strainer with hinged steel cover, cast iron
body, stainless steel screen with 5/32 diameter perforation.
P/N 0061390
Cleaning Tank
This tank to be fabricated in 304 stainless steel to Abcor
Drawing No. C5388-3051.
P/N0211636
5-3
5.4
REPLACEMENT PARTS LIST
Item
Quantity
Membrane Washer
U Bend
PVC Holding Nut
Retaining Ring Truarce #5108-131
Manifold Nipple Cap
Push On Permeate Plug
PVC Shoulder Spacer
Permeate Pass Kit
Membrane Tubes
10' HFM-251FNO
10' HFD-251FNO
10' HFA-251FNO
10' HFP-276FNO
Koch Part Number
8
7
2
4
8
4
0020378
0020390
0020280
0020310
0160235
0211805
0020290
0211786
2
2
2
2
0711532
0711212
0711124
0711622
3
7
If you are located in a remote region where industrial parts may be
difficult to obtain, the following list of replacement parts is
recommended:
Item
Quantity
Fuse
Fuse
Pump Seal
Coupling
Coupling
Coupling
Pressure Switch
Temp Switch
U-Bend
Permeate Pass Kit
Motor
Membrane Washer
PVC Holding Nut
Retaining Ring Truarce #5108-131
Manifold Nipple Cap
Push On Permeate Plug
PVC Shoulder Spacer
Membrane Tubes
10' HFM-251FNO
10' HFD-251FNO
10' HFA-251FNO
10' HFP-276FNO
4
2
2
2
2
2
Koch Part Number
7
2
4
8
0101614
0101670
0126058
0125062
0125063
0125516
0211440
0211463
0020390
0211786
0110235
0020378
0020280
0020310
0160235
0211805
0020290
8
8
8
8
0711532
0711212
0711124
0711622
1
1
7
8
1
8
7
5-4
6.0
INSTRUMENTS AND CONTROLS
6.1
Pressure Gauges
Standard Abcor pressure gauge, 1/2" NPT connection, diaphragm
isolated, range.
PI-1
0-100 PSI
P/N 0140010
PI-2
0-60 PSI
P/N 0140009
6.2
Low Pressure Switch, PSL-1
Snap action pressure switch, 1/4" NPT lower female connection,
adjustable range to 60 PSI, proof pressure 450 PSI, set by
Abcor at 20 PSI decreasing pressure.
P/N 0211440
6.3
Temperature Indicator, TI-1
3" Dial, 4" stem, Bi-Metallic Thermometer
Range 0-200°F, 1/2 NPT lower male connection.
Ashcroft Dial Thermometer 30AI60L
Ashcroft Dial Thermowell 75W0250ST260S
U" Dimension 2 1/2", 316 Stainless Steel.
3/4" NPTM x 1/2", NPTF connection.
6.4
P/N 0140160
P/N 0140152
Temperature Switch, TSH-1
ASCO Tri-point temperature switch with fixed deadband and
adjustable set point, switch rating 5 amps at 120 VAC. Unit
to consist of:
a.)
Watertight Switch assembly with a Dual Range 10-71°C
(50°-160°F)
P/N 0211463
6-1
b.)
Direct Temperature Probe Transducer Unit
P/N 0211465
c.)
316 S/S - 2 1/2" Thermowell with internal and external
threads
P/N 0140155
6.5
Permeate Flowmeter, FM-1
Direct reading in GPM 1/2" NPT 316 stainless steel end
fittings. Buna-N "O" rings. Range 0 - 2.5 GPM
P/N 0200020
6.6
Permeate Bypass Flowmeter, FM-2
Direct reading in GPM water. 1" NPT 316 stainless steel end
fittings. Buna-N "O" rings. Range 0-10 GPM.
P/N 0200030
6-2
7.0
ELECTRICAL
All wiring will be as per the latest edition of the national
electrical code (NEC) JIC standards (EGP).
All electrical components will be to NEMA standards and UL and CSA
approved where applicable. Refer to electrical schematic for
standard components.
7-1
APPENDIX I
CIRCULATION PUMP SPECIFICATION SHEET
KMS Part No.
0121566
Specification Control Sheet Ref.
A5388-8004
Duty
Circulation Pump P-1
Project No.
1.
2.
REQUIREMENTS
1.1
Liquid/Temperature
1.2
Total Generated Head ft.
1.3
Capacity GPM
1.4
Suction Conditions
1.5
Sp. Gravity
1.6
Viscosity C. Stokes
PUMP DATA P/N 0121566
2.1
Pump Mfg/Serial No.
2.2
Number of pump stages
2.3
Shaft arrangement
2.4
Model and size
2.5
Delivery branch bore
2.6
Suction branch bore
2.7
Table of flange
2.8
Capacity
2.9
Total generated head
2.10 Imp dia. - rating
2.11 Imp dia. min/max
2.12 Pump speed - RPM
2.13 Recommended drive - BHP rating/max
2.14 Type of drive
2.15 Maximum suction lift
2.16 Performance curve
2.17 Discharge position/rotation
2.18
2.19
Efficiency %
Bedplate reqd yes/no
AI-1
APPENDIX I
Oil Water/125°F
157 ft.
120 GPM
Flooded
1.0
Carver
One
Horiz. End Suction
1 1/2"x 2"x 7" LA
1 1/2"
2"
120 GPM
157 ft.
6 1/2" Semi open
4 1/2"/7"
3500 RPM
7.7/10
Direct
3699/7-10-70
Vertical/C.W. from
Motor End
62%
CIRCULATION PUMP SPECIFICATION SHEET
(Continued)
3.
4.
5.
MATERIALS OF CONSTRUCTION
3.1
Casing/covers/chamber
3.2
Impeller
3.3
Neck Rings
3.4
Shaft
3.5
Shaft/impeller/sleeves
3.6
Gland
3.7
Gland packing
3.8
Lantern ring
3.9
Bearing type
3.10 Mechanical seal type
3.11
Lubrication
MOTOR
4.1
4.2
4.3
4.4
4.5
4.6
4.7
P/N 0110235
Type
Enclosure
Frame Size
Rating - HP
Speed - RPM
Specification
Electricity supply
4.8
4.9
4.10
Class of insulation
Terminal box position
F.L. current
Ball
Crane Single Type
21-BPICI
Grease
Tri-Voltage
TEFC
215 T
10 HP
3500 RPM
208/230/460V, 3 PH,
60 HZ
B
F-1
24.4/12.2 AMPS
APPROX. SHIPPING SPEC.
5.1
5.2
5.3
CI
CI
STL
STL
STL/CI/416 S/S
C.I.
Net Weight
Gross Weight
Capacity
AI-2