Method of drying salt and similar materials through the use of heat engine waste heat
The present invention provides a method and system for generating electricity using a drive for the electrical generator that is powered by an engine (e.g., turbine). The method and system uses high pressure hot gases produced by combustion of a fuel and an oxygen-bearing gas, using at least a portion of the electricity generated to power manufacturing plant equipment. Additionally, hot waste gases from the heat engine are transported to a process dryer (e.g., rotary kiln dryers) to dry minerals, salt, pigments, sands, and clay.
1. A method of drying a material in a manufacturing plant, said method comprising:
generating electricity with an electrical generator;
providing a hot waste gas stream having a temperature of about 100° C. to about 600° C., wherein said hot waste gas stream is withdrawn from an exhaust gas outlet of a gas turbine coupled to said electrical generator;
introducing said hot waste gas stream into a dryer;
while said hot waste gas is being introduced into said dryer, introducing the material to be dried into said dryer, said material to be dried:
having an initial moisture content upon being introduced into said dryer; and
being selected from the group consisting of sodium chloride, potassium chloride, magnesium chloride, and potassium sulfate, said hot waste gas causing dried material to exit said dryer at a final moisture content that is lower than said initial moisture content; and
transmitting at least a portion of said electricity generated by said electrical generator to at least one piece of equipment in said manufacturing plant to provide electrical power to said piece of equipment, said piece of equipment being used in manufacturing said material to be dried.
2. The method of claim 1 , wherein said dryer is selected from the group consisting of rotary kiln dryers, fluidized bed dryers, and dispersion dryers.
3. The method of claim 1 , wherein said material to be dried has an initial moisture content of from about 5% to about 50% by weight, based upon the total weight of the material to be dried as it is introduced into the dryer taken as 100% by weight.
4. The method of claim 1 , wherein said dried material has a final moisture content of from about 1% to about 15% by weight, based upon the total weight of the material as it exits the dryer taken as 100% by weight.
5. The method of claim 1 , wherein said final moisture content is less than about 40% of said initial moisture content.
6. The method of claim 1 , wherein said hot waste gas has a temperature of about 200° C. to about 600° C. as it is being introduced into the dryer.
7. The method of claim 1 , further comprising contacting said material to be dried with said hot waste gas in said dryer, wherein at least a portion of the heat from said hot waste gas evaporates at least a portion of the moisture on said material to be dried to provide the dried material.
8. A method of drying a material in a manufacturing plant, said method comprising:
generating electricity with an electrical generator;
providing a hot waste gas stream having a temperature of about-100° C. to about 600° C. wherein said hot waste gas stream is withdrawn from an exhaust gas outlet of a gas turbine coupled to said electrical generator;
introducing said hot waste gas stream into a dryer;
while said hot waste gas is being introduced into said dryer, introducing the material to be dried into said dryer, said material to be dried:
having an initial moisture content upon being introduced into said dryer, and
being selected from the group consisting of sodium chloride, potassium sulfate, magnesium chloride, and potassium chloride, said hot waste gas causing dried material to exit said dryer at a final moisture content that is less than about 50% of said initial moisture content; and
transmitting at least a portion of said electricity generated by said electrical generator to at least one piece of equipment in said manufacturing plant to provide electrical power to said piece of equipment, said piece of equipment being used in manufacturing said material to be dried.
9. The method of claim 8 , wherein said dryer is selected from the group consisting of rotary kiln dryers, fluidized bed dryers, and dispersion dryers.
10. The method of claim 9 , wherein said dryer is a rotary kiln dryer.
11. The method of claim 8 , wherein said hot waste gas has a temperature of about 200° C. to about 600° C.
12. The method of claim 8 , further comprising contacting said material to be dried with said hot waste gas in said dryer, wherein at least a portion of the heat from said hot waste gas evaporates at least a portion of the moisture on said material to be dried to provide the dried material.