5
USA Patent No. 5827430 and 5893956 (International Patents Granted) A NEW ERA IN FILTRATION PERFORMANCE & INNOVATION CORE TECHNOLOGIES AVIATION TECHNOLOGIES LEADING TECHNOLOGIES Solution for Amine Contamination

OUTSIDE BACK COVER OUTSIDE FRONT COVER FOLD · PDF file† Refining Capacity Limited Due to Poor Quality Amine † Contactor and Regenerator Foaming † Contactor and Regenerator Flooding

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• 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

Administrator
Cross-Out
Administrator
Cross-Out
Administrator
Inserted Text
s

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