
Introduction
The APV Paramine solution is an answer to the sealing difficulties experienced by sour gas processors. Amines including Sulfinols are employed to carry high concentrations of hydrogen sulfide and carbon dioxide in the rich stream which recovers heat from the hotter lean stream.
The Challenge
Our customers naturally employ high efficiency plate heat exchangers because of their natural advantages over shell and tubes
However, some of these customers have had frustrations with their plate heat exchangers – unavoidable until now. Here are the issues plate heat exchanger customers in the gas-processing sector have had to battle with.
The Initial Investigation
The diagonal bridge gasket in contact with hot rich amine is in fact maintained close to the temperature of the lean stream via conduction. In other words, it runs much hotter than the rich stream bulk temperature. The bridge gasket was almost invariably the area of failure. However, examination of the failed rubbers did indicate lesser but significant degradation of other areas as shown.
It was decided to test various established and development rubber compounds and some of the results are presented below for laboratory testing in 135°C rich Sulfinol for a fixed period.
Label |
Initial Hardness |
Final Hardness Shore A |
Volumetric Swell |
Weight Gain |
|
| EPDM | A |
77 |
62 |
14.6 |
47.1 |
| EPDM | B |
76 |
59 |
14.9 |
44.5 |
| Hydrogenated Nitrile | A |
89 |
71 |
24.6 |
86.5 |
B |
82 |
76 |
26.7 |
96.2 |
|
C |
79 |
71 |
29.4 |
101.0 |
|
D |
76 |
62 |
27.7 |
96.8 |
|
| Paramine | A |
84 |
63 |
7.5 |
15.8 |
B |
95 |
84 |
1.9 |
12.7 |
|
C |
91 |
69 |
7.3 |
16.0 |
|
D |
88 |
66 |
7.5 |
14.9 |
|
E |
82 |
59 |
9.7 |
22.6 |
|
| Nitrile | A |
82 |
90 |
19.9 |
71.0 |
The EPDM labeled A was the control gasket compound exhibiting field failures.
We could make some basic conclusions from the numbers above as well as inspection of the samples:
The basic nitrile was quickly hardening where a seal could not be maintained. The hydrogenated nitrile suffered very high volumetric and mass gains and other test parameters not mentioned above ruled it out. Except for softening, clearly the Paramine compound performed best.
Other possibilities had to be considered.
a) What would happen if the gasket volume was adjusted to partially account for expected swelling
b) What would happen if the key gasket areas were lined with Paramine?
c) Will there be advantages of detail in switching from the existing SR14 model to the B model?
d) Will there be an advantage in using BL welded pairs?
These questions would be answered in a comparative field trial stage.
Comparison of Various Solutions
The results after 3 months are summarised below:
Option |
Description |
Remarks |
1 |
SR14 with EPDM, A, all around: |
As expected, deterioration. |
2 |
SR14 with EPDM, A, modified gasket design |
Less damage than 1. Not a viable option. |
3 |
SR14 with EPDM, A, bridge lined with Paramine |
Intended protection but embrittlement evident. Not a viable option. |
| 4 |
SR14 with Paramine all around |
Extrusion effect in bridge. |
5 |
SR14 with Paramine all around but modified gasket design |
Less extrusion in bridge. |
6 |
B plate with Paramine all around |
Some extrusion evident. |
7 |
BL welded pair with Paramine rich amine ports |
Rich side Paramine gasket performed very well. The EPDM in contact with lean shows unacceptable aging. |
After the 21-month service for option 7, it was concluded that the Paramine gaskets in BL welded pairs had not aged with time but that the lean amine boundary gaskets in EPDM had aged significantly. |
||
The Final Solution
APV agreed that BL welded pairs with complete Paramine gaskets will provide the 5 year plus life required for these exchangers. These alterations made to the design are proprietary and made specifically to suit this service. Up to July 2004, the first installation has completed 70 months of service without incident. 4 units run on MDEA and 4 on Sulfinol.
Qualitative Comparisons with Alternatives
Here are some pros and cons with alternative technologies:
Conventional |
APV |
Fully |
|
| Seal life | Can be very short, e.g. ½ year at 135°C | Expect 5 years at 140°C | Not an issue except corrosion or fatigue cracking of welds which can cause total replacement needs |
| Flexibility to re-arrange/expand | Fully flexible | Fully flexible | None |
| Ability to inspect for sulfide fouling, lean stream, and clean manually or in chemicals | Open & inspect | Open & inspect | Usually no ability to inspect |
| Ability to inspect for rich fouling | Open & inspect | Not available | Usually no ability to inspect |
| Resistance to thermal stresses | Excellent | Excellent | Inherent weakness |
| Repairable? | Individual plates & gaskets can be replaced | Individual pairs and gaskets can be replaced. | Usually impossible Conventional |
| Conventional PHE | APV Paramine | Fully Welded | |
| Compact | Yes | Yes | Usually not |
| Liquid hold up | Low | Low | Usually high |
| Fouling Usually good experience although fouling must be allowed for and controlled via high shear | Excellent experience so far with 3mm gap. | Infrequent in-place cleaning employed. | Non-compact-higher fouling. Compact – plugging risks. |
| Capital cost guide for large applications with high recovery | Lowest | Higher | Very high |
| Medium term ownership costs for high temperature sour applications | High | Low | Higher |
Conclusion
Bearing in mind its flexibility, heat transfer performance, ability to achieve close temperature approaches, resistance to thermal gradient stresses and long term field testing in amine service, the APV Paramine System is the system of choice for large sour gas amine interchanges. It also follows that other amine service devoid of sour gas will also benefit greatly if the APV Paramine System is employed.