Method for regenerating an aqueous solution of MEG containing salts with purge treatment
The present invention relates to a process for regenerating a rich MEG aqueous solution ( 100 ), recovering a maximum amount of MEG while at the same time removing the carboxylic acid salts, including: a) vacuum evaporation of the solution ( 100 ) in a unit ( 1000 ); b) optional precipitation in a tank ( 1002 ) of the inorganic salts of a portion ( 105 ) of the liquid residue enriched in MEG and in salts ( 104 ) obtained from a); c) removal of the precipitated inorganic salts in a solid/liquid separation unit ( 1003 ); d) sending all or part ( 114 ) of the liquid effluent ( 112 ) obtained from c) into a separation unit ( 1004 ) different from the unit ( 1000 ) to form, notably, an MEG stream depleted in carboxylic acid salts or in carboxylic acids ( 115 ); e) recycling of said stream ( 115 ) into step a).
1. Process for regenerating a solution of monoethylene glycol (MEG) containing water and dissolved salts, including the following steps:
a) evaporating said solution ( 100 ) under vacuum in a first evaporation unit ( 1000 ) to produce a gaseous effluent including MEG and water ( 101 ), and a liquid residue enriched in MEG and in salts ( 104 ), and recycling a first portion ( 106 ) of said liquid residue enriched in MEG and in salts ( 104 ) into said first vacuum evaporation unit ( 1000 );
c) sending a second portion ( 105 ) of said liquid residue enriched in MEG and in salts ( 104 ) obtained from step a) into a solid/liquid separation zone ( 1003 ) to separate a stream containing precipitated salts including inorganic salts ( 111 ) and a liquid effluent including dissolved salts, among which are carboxylic acid salts ( 112 );
d) sending a portion ( 114 ) or all of said liquid effluent ( 112 ) obtained in step c) into a second evaporation unit ( 1004 ) different from the first vacuum evaporation unit ( 1000 ) to perform a separation between the MEG and at least a portion of the carboxylic acid salts and evaporating said portion ( 114 ) or all of said liquid effluent ( 112 ) obtained in step c) under vacuum to form a vapor enriched in MEG and depleted in carboxylic acid salts ( 115 ) and a residual liquid effluent enriched in carboxylic acid salts ( 116 );
e) recycling said vapor enriched in MEG and depleted in carboxylic acid salts ( 115 ) into step a), or mixing said vapor enriched in MEG and depleted in carboxylic acid salts ( 115 ) with the gaseous effluent including MEG and water ( 101 ) obtained from step a), and using said gaseous effluent including MEG and water ( 101 ) obtained from step a) or said mixture to produce the regenerated MEG solution.
2. Process according to claim 1 , in which, in step e), the vapor enriched in MEG and depleted in carboxylic acid salts ( 115 ) obtained from step d) is recycled into step a).
3. Process according to claim 2 , in which a step f) of purifying the gaseous effluent ( 101 ) obtained from step a) is also performed in a purification unit ( 1001 ) to form a stream of water ( 103 ) and the regenerated MEG solution ( 102 ).
4. Process according to claim 3 , in which the purification step f) is a vacuum distillation.
5. Process according to claim 1 , in which, prior to step a), evaporation at atmospheric pressure of the MEG solution containing water and dissolved salts ( 100 ) to be regenerated is performed in an initial evaporation unit, to produce a water-enriched gaseous effluent and a liquid residue enriched in MEG and in salts, all of which is sent into step a).
6. Process according to claim 1 , in which step a) is performed at a temperature of between 120° C. and 155° C., and at a pressure of between 0.01 MPa and 0.07 MPa.
7. Process according to claim 1 , in which step c) is performed at a temperature of between 50° C. and 90° C., and at atmospheric pressure.
8. Process according to claim 1 , in which the portion ( 114 ) or all of said liquid effluent ( 112 ) obtained in step c) is sent intermittently into the separation unit ( 1004 ) of step d).
9. Process according to claim 1 , in which an additional liquid or gaseous stream ( 117 ) is sent into said second evaporation unit to increase the amount of MEG recovered in the stream ( 115 ) during step d), said stream being chosen from water, steam or an inert gas.
10. Process according to claim 1 , in which step d) is performed at a temperature of between 120° C. and 155° C., and at a pressure of between 0.01 MPa and 0.07 MPa.
11. Process according to claim 1 , further comprising the following step b) preceding step c):
b) sending the second portion ( 105 ) of said liquid residue enriched in MEG and in salts into a tank ( 1002 ) in which the temperature of said second portion ( 105 ) of said salt-enriched liquid residue is lowered so as to precipitate inorganic salts to form a stream enriched in precipitated salts ( 108 ), recycling a first fraction ( 109 ) of said stream enriched in precipitated salts ( 108 ) into the tank ( 1002 ), and recycling a stream depleted in precipitated salts ( 107 ) into the vacuum evaporation unit ( 1000 ) in step a).
12. Process according to claim 11 , in which, in step c), a second fraction ( 110 ) of said stream enriched in precipitated salts ( 108 ) obtained from the tank ( 1002 ) is sent into the solid/liquid separation unit ( 1003 ).
13. Process according to claim 12 , in which, the second fraction ( 110 ) of said stream enriched in precipitated salts ( 108 ) obtained from the tank ( 1002 ) is sent into the solid/liquid separation unit ( 1003 ) intermittently.
14. Process according to claim 12 , in which, in which, the second fraction ( 110 ) of said stream enriched in precipitated salts ( 108 ) obtained from the tank ( 1002 ) is sent into the solid/liquid separation unit ( 1003 ) intermittently if the concentration of inorganic salts of said stream enriched in precipitated salts ( 108 ) is between 10% by weight and 50% by weight.