Process for treating diamine absorbent streams
An absorbent, water flow technology used in the field of operating ion exchange processes
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Embodiment 1
[0092] Example 1 - Renewable SO from diamine 2 Sodium removal from absorbents
[0093] This example illustrates the use of cation exchange resins to remove sodium from diamine absorbents. The absorbent supplied to the test bed was sodium contaminated Cansolv Absorbent DS. The components are shown in Table 1.
[0094] Table 1: Components of sodium-contaminated diamine absorbents
[0095] Amine Concentration (wt%) 24.2 Sodium concentration (wt%) 2 Sulfate concentration (wt%) 12 HSAS: (eq. SO 4 2- / mole amine) 1.1 Water (wt%) 61.8
[0096] The test was carried out in a 3 cm diameter insulated column with Lewatitt K-2629 strong acid ion exchange resin. The resin bed had a height of 35 cm and a bed volume (BV) of 200 ml. All fluids introduced into the column were at 50°C. Prior to designing this experiment, the resin was processed through several cycles of loading and regeneration.
[0097] Sodium removal experiments were carried ou...
Embodiment 2
[0108] The effect of amine heat stable salt level on sodium removal performance was tested. Again, the sodium-contaminated Cansolv Absorbent DS was used in this experiment. The experimental conditions are shown in Table 3.
[0109] Table 3: Composition of spent absorbent
[0110]
[0111] The same procedure as Example 1 was used, but following the fluid conditions in Table 4.
[0112] Table 4: Fluid Conditions for Example 2
[0113]
[0114] The regeneration effluent was analyzed for amines and the results are shown in Figure 6 . A summary of sodium removal efficiency and amine loss is shown in Table 5. It is clear that low amounts of thermostable salts favor higher sodium removal and lower amine losses.
[0115] Table 5: Amine loss at various thermostable salt concentrations
[0116]
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