Upload
lythu
View
224
Download
0
Embed Size (px)
Citation preview
• Frequent Element Change outs• Frequent Replacement of Activated Carbon due to Hydrocarbons• Refining Capacity Limited Due to Poor Quality Amine• Contactor and Regenerator Foaming• Contactor and Regenerator Flooding• Contactor and Regenerator Fouling• Contactor and Regenerator Higher Pressure Drop and therefore
Higher Energy Usage• Higher Amine Loss Causing Increased Amount of Make Up Amine• Off Spec Treated Gas• Heat Exchanger fouling• Increased Corrosion Rates• Formation of heat Stable Salts• Pump Seal Failures
THE WRONG FILTER CANCAUSE BIG PROBLEMS
BIG PROBLEMS COST BIG MONEYCost
$_________ Rich amine filtration problems limit refining capacity Foaming towers cause premature flooding along with
$_________ increased amine losses with the gas leaving the contactor$_________ increased amine make up cost$_________ increased energy usage in the regenerator $_________ reduced tower efficiency
Off spec treated gas to the fuel gas $_________ Increased burner tip maintenance$_________ Environmental repercussions$_________ Sulfur recovery catalyst damage$_________ Higher maintenance cost due to corrosion$_________ Increased waste disposal cost due to additional amine losses$_________ Increased cost for more frequent activated carbon replacement$_________ Frequent element changes cost time and money
Scan w/ FoamingScan after Proper Filtration
ClearVapor Bar
LiquidLine
100 1000
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
Tray No.2'
4'
6'
8'
10'
12'
14'
16'
18'
20'
22'
24'
26'
28'
30'
32'
34'
36'
38'
40'
42'
44'
46'
48'
50'
52'
54'
56'
58'
60'
62'
64'
66'
68'
Poor Filtration Good Filtration
DPI DPI
Photo courtesy of Tracerco NA, Pasadena, Texas
USA Patent No. 5827430 and 5893956 (International Patents Granted)
A N E W E R A I N FILTRATION PERFORMANCE & INNOVATION
CORE TECHNOLOGIES
AVIATION TECHNOLOGIES
LEADING TECHNOLOGIES
Solution for Amine Contamination
Printed in USA
Date _____________________
1. APPLICATION: Liquid Amine Filtration2. OPERATING DATA
a. Temperature (min/max/normal) ______________________________
b. Pressure (min/max/normal) psig ______________________________
c. Type of Amine (e.g. MDEA, DEA, etc.) _________________________d. Check all types of contaminant present in Amine:
___ Rigid Particulate ___ Shear Sensitive Particulate___ Deformable Semi-Solids ___ Immiscible Liquid
e. Please specify any other contaminants present
in the amine: ______________________________________________
f. Desired micron removal _____________________________________
g. Particle Size Distribution (attach analysis if available)______________
h. Type of filter currently used (e.g. depth, pleated, cotton) or
make and model ___________________________________________
i. Housing manufacturer and model ____________________________
j. Problem with current filter ___________________________________
____________________________________________________________
____________________________________________________________
____________________________________________________________
____________________________________________________________
AMINE FILTER WORK SHEET
Name _____________________________________________________________
Title _______________________________________________________________
Phone ______________________________________________________________
Email _______________________________________________________________
Company __________________________________________________________
Address ____________________________________________________________
City________________________________________________________________
State_________________________________ Zip ___________________________
Please send this completed worksheet to PECOFacet or your localPECOFacet distributor.
I am interested in: ___ Further literature ___ Visit from representative ___ Technical presentation
Other PECOFacet Elements for Amine•OPHD •Rolled or Sock •Pleated Cellulose •Carbon Cannisters •Melt Blown[
Corporate Headquarters
PO Box 640Mineral Wells, Texas 76068Ph: 800-877-7326
940-325-2575Fax: 940-325-4622E-Mail: [email protected]
www.PECOFacet.com
Locations
Almere, The Netherlands
Calgary, Canada
Cedex, France
Beijing, China
Bucharest, Romania
Houston, Texas
Kempen, Germany
Kuala Lumpur, Malaysia
La Coruna, Spain
Manama, Bahrain
Mid Glamorgan, UK
Queretaro, Mexico
Stillwell, Oklahoma
Thetford, UK
Torino, Italy
Tulsa, Oklahoma
Please refer to www.pecofacet.com for most current literature edition.
Your local distributor:
EL-PHD-SL-01 (LHA 4/09)
FOLD IN FLAPOUTSIDE BACK COVER OUTSIDE FRONT COVER
FOLD IN FLAPOUTSIDE BACK COVER OUTSIDE FRONT COVER
™
• Frequent Element Change outs• Frequent Replacement of Activated Carbon due to Hydrocarbons• Refining Capacity Limited Due to Poor Quality Amine• Contactor and Regenerator Foaming• Contactor and Regenerator Flooding• Contactor and Regenerator Fouling• Contactor and Regenerator Higher Pressure Drop and therefore
Higher Energy Usage• Higher Amine Loss Causing Increased Amount of Make Up Amine• Off Spec Treated Gas• Heat Exchanger fouling• Increased Corrosion Rates• Formation of heat Stable Salts• Pump Seal Failures
THE WRONG FILTER CANCAUSE BIG PROBLEMS
BIG PROBLEMS COST BIG MONEYCost
$_________ Rich amine filtration problems limit refining capacity Foaming towers cause premature flooding along with
$_________ increased amine losses with the gas leaving the contactor$_________ increased amine make up cost$_________ increased energy usage in the regenerator $_________ reduced tower efficiency
Off spec treated gas to the fuel gas $_________ Increased burner tip maintenance$_________ Environmental repercussions$_________ Sulfur recovery catalyst damage$_________ Higher maintenance cost due to corrosion$_________ Increased waste disposal cost due to additional amine losses$_________ Increased cost for more frequent activated carbon replacement$_________ Frequent element changes cost time and money
Scan w/ FoamingScan after Proper Filtration
ClearVapor Bar
LiquidLine
100 1000
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
Tray No.2'
4'
6'
8'
10'
12'
14'
16'
18'
20'
22'
24'
26'
28'
30'
32'
34'
36'
38'
40'
42'
44'
46'
48'
50'
52'
54'
56'
58'
60'
62'
64'
66'
68'
Poor Filtration Good Filtration
DPI DPI
Photo courtesy of Tracerco NA, Pasadena, Texas
USA Patent No. 5827430 and 5893956 (International Patents Granted)
A N E W E R A I N FILTRATION PERFORMANCE & INNOVATION
CORE TECHNOLOGIES
AVIATION TECHNOLOGIES
LEADING TECHNOLOGIES
Solution for Amine Contamination
Printed in USA
Date _____________________
1. APPLICATION: Liquid Amine Filtration2. OPERATING DATA
a. Temperature (min/max/normal) ______________________________
b. Pressure (min/max/normal) psig ______________________________
c. Type of Amine (e.g. MDEA, DEA, etc.) _________________________d. Check all types of contaminant present in Amine:
___ Rigid Particulate ___ Shear Sensitive Particulate___ Deformable Semi-Solids ___ Immiscible Liquid
e. Please specify any other contaminants present
in the amine: ______________________________________________
f. Desired micron removal _____________________________________
g. Particle Size Distribution (attach analysis if available)______________
h. Type of filter currently used (e.g. depth, pleated, cotton) or
make and model ___________________________________________
i. Housing manufacturer and model ____________________________
j. Problem with current filter ___________________________________
____________________________________________________________
____________________________________________________________
____________________________________________________________
____________________________________________________________
AMINE FILTER WORK SHEET
Name _____________________________________________________________
Title _______________________________________________________________
Phone ______________________________________________________________
Email _______________________________________________________________
Company __________________________________________________________
Address ____________________________________________________________
City________________________________________________________________
State_________________________________ Zip ___________________________
Please send this completed worksheet to PECOFacet or your localPECOFacet distributor.
I am interested in: ___ Further literature ___ Visit from representative ___ Technical presentation
Other PECOFacet Elements for Amine•OPHD •Rolled or Sock •Pleated Cellulose •Carbon Cannisters •Melt Blown[
Corporate Headquarters
PO Box 640Mineral Wells, Texas 76068Ph: 800-877-7326
940-325-2575Fax: 940-325-4622E-Mail: [email protected]
www.PECOFacet.com
Locations
Almere, The Netherlands
Calgary, Canada
Cedex, France
Beijing, China
Bucharest, Romania
Houston, Texas
Kempen, Germany
Kuala Lumpur, Malaysia
La Coruna, Spain
Manama, Bahrain
Mid Glamorgan, UK
Queretaro, Mexico
Stillwell, Oklahoma
Thetford, UK
Torino, Italy
Tulsa, Oklahoma
Please refer to www.pecofacet.com for most current literature edition.
Your local distributor:
EL-PHD-SL-01 (LHA 4/09)
FOLD IN FLAPOUTSIDE BACK COVER OUTSIDE FRONT COVER
FOLD IN FLAPOUTSIDE BACK COVER OUTSIDE FRONT COVER
™
FOLD IN FLAP
When comparing the GOLDXtream to a radial pleatedelement at comparable flow rates, the GOLDXtream el-ement will last longer, will have a lower pressure dropover the life of the element and will more effectively re-move more types of stream impurities.
SERVICE LIFE
PRESS
URE D
RO
P[P
SID
]
25 50 75 100
PLEATED GOLDXtream
If you want cleaner amine • To reduce foaming and other problems
with towers in your amine unit• To extend the time between element
changes• To capture and retain shear sensitive
deformables and contaminants common to amine
• To extend the life of your carbon bed• To reduce the pressure drop over the life
of the elements
And your conditions meet the following:• Using a 6” X 39” element with 226 double
O ring seal • Amine temperature <180º F• Filter rating is between 1 and 100 microns
The ergonomic end caps are thermally sealed to the filter media and require no glue.
Captures and Retains Shear Sensitive and Deformable Contaminants
Reduces Pressure Drop
SH
OC
K Z
ON
E
DIR
TY
AM
INE
CLE
AN
AM
INE
8 7 6 5 4 3 2 1
1Course
Filtration Layers
ShockMicroFiltration
Layers
3
FLOW
2
Radial
Axial
Helical
Shock Zone Shock Zone
Figure 2Flow Paths
Figure 1Filtration Zones
Dirt HoldingMaximumTemperature
ChemicalCompatibility Durability
GOLDXtream
High flow synthetic pleated
High flow celluose pleated
180º F
180º F
250º F
Deg
reda
tion
Pro
duct
sLu
be/W
ater
Em
ulsi
onSi
licon
e A
ntifoa
m
Iron
Sul
fide
Rust
Iron
C
arbo
nate
Hyd
roca
rbon
Liq
uid
Lube
Oil
Immiscible Liquid
Sand
Rust
Scal
e
Car
bon
Fine
s
DeformableSemi-Solids
Shear-SensitiveParticulateRigid Particulate
GOLDXtream
High flow synthetic pleated
High flow celluose pleated
STAYING POWER
EFFICIENCY
PERFORMANCE QUALITIES
Extends CarbonBed Life
Effectively removes tough contaminants that defeat
other filters:
Amine Unit in Midwest Refinery
The pleated element used by the refiner did not effectively remove hydrocarbon contaminants. An oil sheen was left in the amine and the refiner was changing the elements more frequently than desired. When the pleated elements were removed from service, the outer netting was looseand had even separated from the end cap in at least one location. These elements were replaced with the GOLDXtream element with comparable efficiency. The PEACH® GOLDXtream element lasted about 30% longer thanthe pleated element that the refiner had been using. The GOLDXtream element also removed hydrocarbon contaminants in the first stage of the filter and eliminated the sheen in the amine.
Absorbs Hydrocarbons Without BlindingWhy did the GOLDXtream last longer and improve the filtration?
The GOLDXtream is a depth style cartridge with gradient density layers custom designed for amine service. This means larger contaminants are re-tained by outer layers while smaller contaminants are blocked at the inner layers. This construction allows hydrocarbons and other deformable contaminants to migrate through the element media and be trapped within one of the three Filtration Zones without premature plugging. Therefore optimal contaminant loading is achieved.
FIE
LD
AP
PLIC
ATIO
N
Fewer Element Changes
Gels, Agglomerations, Iron Sulfides, Heat Degradation Products, Emulsionsand more!�
Extreme
Good Fair Poor
Radial
Axial
Shock ZoneShock Zone
Helical
GOLDXtream utilizes PEACH® GOLD Technology
developed for EXTREME applications such as filtering
amine and glycol. This unique product contains three
complex filter zones (figure 1). Zone 1 contains as many
as four engineered filter media that are interlaid in a
conical helix stucture creating radial, axial, and helical
flow patterns (figure 2) trapping large particles and
absorbing immiscible hydrocarbon. Zone 2 (The Shock
Zone) is the anular pocket between Zone 1 and 2. This
area creates a dynamic shock that kinetically challenges
contaminants and rectifies the fluid flow as it enters the
final zone of EXTREME filtration. Zone 3 is constructed
of as many as four engineered filter media with smaller
fibers designed to trap the smallest and most elusive of
the targeted contaminants.
GOLDXtream truly takes amine filtration to its
EXTREME. By exploiting the effective surface areas
of up to eight different media and millions of
carefully selected fibers, all filtration mechanisms
are at work including sieving, impaction, and
diffusion. The unique structure created with PEACH®
GOLD Technology adds dimensions to filtration such as
simultaneous axial, radial, and helical flow patterns and
shock zones. This extraordinary product challenges the
most EXTREME contaminants and is engineered to
provide longer on-stream life with low or differential
pressure and greater contaminant removal
capabilities than similar products.
The
Cartridge is the Solution
Try GOLDXtream in Your
Amine System Today. Expect
EXTREME PERFORMANCE!
INSIDE FRONT COVER INSIDE BACK COVER
INSIDE FRONT COVER INSIDE BACK COVERFOLD IN FLAP
™
FOLD IN FLAP
When comparing the GOLDXtream to a radial pleatedelement at comparable flow rates, the GOLDXtream el-ement will last longer, will have a lower pressure dropover the life of the element and will more effectively re-move more types of stream impurities.
SERVICE LIFE
PRESS
URE D
RO
P[P
SID
]
25 50 75 100
PLEATED GOLDXtream
If you want cleaner amine • To reduce foaming and other problems
with towers in your amine unit• To extend the time between element
changes• To capture and retain shear sensitive
deformables and contaminants common to amine
• To extend the life of your carbon bed• To reduce the pressure drop over the life
of the elements
And your conditions meet the following:• Using a 6” X 39” element with 226 double
O ring seal • Amine temperature <180º F• Filter rating is between 1 and 100 microns
The ergonomic end caps are thermally sealed to the filter media and require no glue.
Captures and Retains Shear Sensitive and Deformable Contaminants
Reduces Pressure Drop
SH
OC
K Z
ON
E
DIR
TY
AM
INE
CLE
AN
AM
INE
8 7 6 5 4 3 2 1
1Course
Filtration Layers
ShockMicroFiltration
Layers
3
FLOW
2
Radial
Axial
Helical
Shock Zone Shock Zone
Figure 2Flow Paths
Figure 1Filtration Zones
Dirt HoldingMaximumTemperature
ChemicalCompatibility Durability
GOLDXtream
High flow synthetic pleated
High flow celluose pleated
180º F
180º F
250º F
Deg
reda
tion
Pro
duct
sLu
be/W
ater
Em
ulsi
onSi
licon
e A
ntifoa
m
Iron
Sul
fide
Rust
Iron
C
arbo
nate
Hyd
roca
rbon
Liq
uid
Lube
Oil
Immiscible Liquid
Sand
Rust
Scal
e
Car
bon
Fine
s
DeformableSemi-Solids
Shear-SensitiveParticulateRigid Particulate
GOLDXtream
High flow synthetic pleated
High flow celluose pleated
STAYING POWER
EFFICIENCY
PERFORMANCE QUALITIES
Extends CarbonBed Life
Effectively removes tough contaminants that defeat
other filters:
Amine Unit in Midwest Refinery
The pleated element used by the refiner did not effectively remove hydrocarbon contaminants. An oil sheen was left in the amine and the refiner was changing the elements more frequently than desired. When the pleated elements were removed from service, the outer netting was looseand had even separated from the end cap in at least one location. These elements were replaced with the GOLDXtream element with comparable efficiency. The PEACH® GOLDXtream element lasted about 30% longer thanthe pleated element that the refiner had been using. The GOLDXtream element also removed hydrocarbon contaminants in the first stage of the filter and eliminated the sheen in the amine.
Absorbs Hydrocarbons Without BlindingWhy did the GOLDXtream last longer and improve the filtration?
The GOLDXtream is a depth style cartridge with gradient density layers custom designed for amine service. This means larger contaminants are re-tained by outer layers while smaller contaminants are blocked at the inner layers. This construction allows hydrocarbons and other deformable contaminants to migrate through the element media and be trapped within one of the three Filtration Zones without premature plugging. Therefore optimal contaminant loading is achieved.
FIE
LD
AP
PLIC
ATIO
N
Fewer Element Changes
Gels, Agglomerations, Iron Sulfides, Heat Degradation Products, Emulsionsand more!�
Extreme
Good Fair Poor
Radial
Axial
Shock ZoneShock Zone
Helical
GOLDXtream utilizes PEACH® GOLD Technology
developed for EXTREME applications such as filtering
amine and glycol. This unique product contains three
complex filter zones (figure 1). Zone 1 contains as many
as four engineered filter media that are interlaid in a
conical helix stucture creating radial, axial, and helical
flow patterns (figure 2) trapping large particles and
absorbing immiscible hydrocarbon. Zone 2 (The Shock
Zone) is the anular pocket between Zone 1 and 2. This
area creates a dynamic shock that kinetically challenges
contaminants and rectifies the fluid flow as it enters the
final zone of EXTREME filtration. Zone 3 is constructed
of as many as four engineered filter media with smaller
fibers designed to trap the smallest and most elusive of
the targeted contaminants.
GOLDXtream truly takes amine filtration to its
EXTREME. By exploiting the effective surface areas
of up to eight different media and millions of
carefully selected fibers, all filtration mechanisms
are at work including sieving, impaction, and
diffusion. The unique structure created with PEACH®
GOLD Technology adds dimensions to filtration such as
simultaneous axial, radial, and helical flow patterns and
shock zones. This extraordinary product challenges the
most EXTREME contaminants and is engineered to
provide longer on-stream life with low or differential
pressure and greater contaminant removal
capabilities than similar products.
The
Cartridge is the Solution
Try GOLDXtream in Your
Amine System Today. Expect
EXTREME PERFORMANCE!
INSIDE FRONT COVER INSIDE BACK COVER
INSIDE FRONT COVER INSIDE BACK COVERFOLD IN FLAP
™
• Frequent Element Change outs• Frequent Replacement of Activated Carbon due to Hydrocarbons• Refining Capacity Limited Due to Poor Quality Amine• Contactor and Regenerator Foaming• Contactor and Regenerator Flooding• Contactor and Regenerator Fouling• Contactor and Regenerator Higher Pressure Drop and therefore
Higher Energy Usage• Higher Amine Loss Causing Increased Amount of Make Up Amine• Off Spec Treated Gas• Heat Exchanger fouling• Increased Corrosion Rates• Formation of heat Stable Salts• Pump Seal Failures
THE WRONG FILTER CANCAUSE BIG PROBLEMS
BIG PROBLEMS COST BIG MONEYCost
$_________ Rich amine filtration problems limit refining capacity Foaming towers cause premature flooding along with
$_________ increased amine losses with the gas leaving the contactor$_________ increased amine make up cost$_________ increased energy usage in the regenerator $_________ reduced tower efficiency
Off spec treated gas to the fuel gas $_________ Increased burner tip maintenance$_________ Environmental repercussions$_________ Sulfur recovery catalyst damage$_________ Higher maintenance cost due to corrosion$_________ Increased waste disposal cost due to additional amine losses$_________ Increased cost for more frequent activated carbon replacement$_________ Frequent element changes cost time and money
Scan w/ FoamingScan after Proper Filtration
ClearVapor Bar
LiquidLine
100 1000
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
Tray No.2'
4'
6'
8'
10'
12'
14'
16'
18'
20'
22'
24'
26'
28'
30'
32'
34'
36'
38'
40'
42'
44'
46'
48'
50'
52'
54'
56'
58'
60'
62'
64'
66'
68'
Poor Filtration Good Filtration
DPI DPI
Photo courtesy of Tracerco NA, Pasadena, Texas
USA Patent No. 5827430 and 5893956 (International Patents Granted)
A N E W E R A I N FILTRATION PERFORMANCE & INNOVATION
CORE TECHNOLOGIES
AVIATION TECHNOLOGIES
LEADING TECHNOLOGIES
Solution for Amine Contamination
Printed in USA
Date _____________________
1. APPLICATION: Liquid Amine Filtration2. OPERATING DATA
a. Temperature (min/max/normal) ______________________________
b. Pressure (min/max/normal) psig ______________________________
c. Type of Amine (e.g. MDEA, DEA, etc.) _________________________d. Check all types of contaminant present in Amine:
___ Rigid Particulate ___ Shear Sensitive Particulate___ Deformable Semi-Solids ___ Immiscible Liquid
e. Please specify any other contaminants present
in the amine: ______________________________________________
f. Desired micron removal _____________________________________
g. Particle Size Distribution (attach analysis if available)______________
h. Type of filter currently used (e.g. depth, pleated, cotton) or
make and model ___________________________________________
i. Housing manufacturer and model ____________________________
j. Problem with current filter ___________________________________
____________________________________________________________
____________________________________________________________
____________________________________________________________
____________________________________________________________
AMINE FILTER WORK SHEET
Name _____________________________________________________________
Title _______________________________________________________________
Phone ______________________________________________________________
Email _______________________________________________________________
Company __________________________________________________________
Address ____________________________________________________________
City________________________________________________________________
State_________________________________ Zip ___________________________
Please send this completed worksheet to PECOFacet or your localPECOFacet distributor.
I am interested in: ___ Further literature ___ Visit from representative ___ Technical presentation
Other PECOFacet Elements for Amine•OPHD •Rolled or Sock •Pleated Cellulose •Carbon Cannisters •Melt Blown[
Corporate Headquarters
PO Box 640Mineral Wells, Texas 76068Ph: 800-877-7326
940-325-2575Fax: 940-325-4622E-Mail: [email protected]
www.PECOFacet.com
Locations
Almere, The Netherlands
Calgary, Canada
Cedex, France
Beijing, China
Bucharest, Romania
Houston, Texas
Kempen, Germany
Kuala Lumpur, Malaysia
La Coruna, Spain
Manama, Bahrain
Mid Glamorgan, UK
Queretaro, Mexico
Stillwell, Oklahoma
Thetford, UK
Torino, Italy
Tulsa, Oklahoma
Please refer to www.pecofacet.com for most current literature edition.
Your local distributor:
EL-PHD-SL-01 (LHA 4/09)
FOLD IN FLAPOUTSIDE BACK COVER OUTSIDE FRONT COVER
FOLD IN FLAPOUTSIDE BACK COVER OUTSIDE FRONT COVER
™