Vessel and method for solid-liquid separation
Devices, systems, and methods for separating solids from liquids are disclosed. A vessel includes an inlet, a carrier liquid outlet, a product outlet, a purifying section, and a heater. The inlet directs a slurry into the purifying section. The slurry comprises particles of a solid and a carrier liquid. The purifying section preferentially drives the particles of the solid towards a heating zone of the purifying section versus the carrier liquid. This displaces a first portion of the carrier liquid away from the heating zone of the purifying section. The heater heats the slurry. The carrier liquid outlet drives a majority of the carrier liquid out of the vessel. The product outlet is adjacent to the heating zone of the purifying section.
1. A method for separating solid carbon dioxide particles from a carrier liquid and producing a substantially pure liquid carbon dioxide stream from the separated solid dioxide particles, the method comprising the steps of:
a. introducing a slurry stream ( 150 ) comprising a carrier liquid and solid carbon dioxide particles into an inlet section ( 140 ) of a vertical column vessel ( 102 ) under pressure;
b. allowing the solid carbon dioxide particles to settle by gravity into the lower end of the vertical column vessel ( 102 ) which defines a heating section ( 142 ), while displacing the less dense carrier liquid up, towards the upper end of the vertical column vessel ( 102 );
c. heating the heating section ( 142 ) of the vertical column vessel ( 102 ) to melt the solid carbon dioxide particles to form a product liquid stream ( 151 ) of substantially pure carbon dioxide;
d. driving a majority carrier liquid stream ( 154 ) out of the vertical column vessel ( 102 ) through a carrier liquid stream outlet extending through the top of the vertical column vessel ( 102 ); and
e. driving the product liquid stream ( 151 ) of substantially pure carbon dioxide out of the vertical column vessel ( 102 ) through a product outlet at the lower end of the vertical column vessel ( 102 ) that is separate and distinct from the carrier liquid outlet.
2. The method of claim 1 , wherein heating of the heating section is accomplished by:
f. passing a portion of the product liquid stream ( 151 ) of substantially pure carbon dioxide exiting through the product outlet, through a heat exchanger ( 110 ) external of the vertical column vessel ( 102 ), thereby increasing the temperature of the portion of the product liquid stream ( 151 ) of substantially pure carbon dioxide; and
g. recirculating the portion of the product liquid stream ( 151 ) of substantially pure carbon dioxide of increased temperature into the heating section ( 142 ) of the vertical column vessel ( 102 ).
3. The method of claim 1 , wherein the carrier liquid is isopentane.