Process for inhibiting particulate emission during friction of heat-treated iron ore pellets and use of an alcohol by-product to inhibit particulate emission
A process for the inhibition of particulate emission during friction of heat-treated iron ore pellets includes the following steps: a) removal of heat-treated iron ore pellets at a temperature of 200° C.; and b) spraying of an alcohol by-product on pellets. The use of an alcohol by-product as an inhibitor of particulate emission is further described, with the alcohol by-product being sprayed on heat-treated iron ore pellets, which can partially or completely replace water during the handling, stacking, loading, and unloading of materials such as pellets, granules, fines, and other products from iron ore and other minerals. This process significantly reduces the emission of particulates in the an operational area.
1. A process of inhibiting particulate emission caused by friction of heat-treated iron ore pellets consisting of:
providing iron ore pellets in an oven;
subjecting the iron ore pellets to a heat treatment in an oven at a temperature above 250° C. and below 1350° C.;
removing the heat-treated iron ore pellets from the oven and cooling to a temperature between 200° C. and 250° C.; and
spraying glycerin on the heat-treated iron ore pellets immediately after the cooling, wherein the glycerin is a particulate emission inhibitor that does not evaporate when in contact with the heat-treated iron ore pellets,
wherein particulate emission of the heat treated iron ore pellets is reduced from about 500 mg/m 3 prior to spraying glycerin to about 100 mg/m 3 after spraying glycerin, wherein the particulate emission is measured under the following conditions: the heat treated iron ore pellets with and without spraying glycerin are separately submitted to tumbling using an abrasion drum under International Standard: ISO3271:1995 for 1 minute, the drum door is immediately opened and an emission of particulate in suspension inside the drum is measured.
2. The process of claim 1 , wherein the glycerin is in a proportion of 500g per ton of the heat-treated iron ore pellets.
3. The process of claim 1 , wherein the friction of the heat treated iron ore pellets occurs during stacking, loading, or unloading of the iron ore pellets.
4. The process of claim 1 , wherein the glycerin is derived from biodiesel production.
5. A process of inhibiting particulate emission caused by friction of heat-treated iron ore pellets comprising:
providing iron ore pellets in an oven;
subjecting the iron ore pellets to a heat treatment in an oven at a temperature above 250° C. and below 1350° C.;
removing the heat-treated iron ore pellets from the oven and cooling to a temperature between 200° C. and 250° C.; and
spraying glycerin on the heat-treated iron ore pellets immediately after the cooling, wherein the glycerin is a particulate emission inhibitor that does not evaporate when in contact with the heat-treated iron ore pellets,
wherein particulate emission of the heat treated iron ore pellets is reduced from about 500 mg/m 3 prior to spraying glycerin to about 100 mg/m 3 after spraying glycerin, wherein the particulate emission is measured under the following conditions: the heat treated iron ore pellets with and without spraying glycerin are separately submitted to tumbling using an abrasion drum under International Standard: ISO3271:1995 for 1 minute, the drum door is immediately opened and an emission of particulate in suspension inside the drum is measured.
6. The process of claim 5 , wherein the glycerin is in a proportion of 500g per ton of the heat-treated iron ore pellets.
7. The process of claim 5 , wherein the glycerin is derived from biodiesel production.
8. The process of claim 5 , wherein the friction of the heat treated iron ore pellets occurs during stacking, loading, or unloading of the iron ore pellets.
9. A process of inhibiting particulate emission caused by friction of heat-treated iron ore pellets comprising:
providing iron ore pellets in an oven;
subjecting the iron ore pellets to a heat treatment in an oven at a temperature above 250° C. and below 1350° C.;
removing the heat-treated faw iron ore pellets from the oven and cooling to a temperature between 200° C. and 250° C.; and
spraying glycerin on the heat-treated iron ore pellets immediately after the cooling, wherein the glycerin is in a proportion of 500g per ton of the heat-treated iron ore pellets, and wherein the glycerin is a particulate emission inhibitor that does not evaporate when in contact with the heat-treated iron ore pellets,
wherein particulate emission of the heat treated iron ore pellets is reduced from about 500 mg/m 3 prior to spraying glycerin to about 100 mg/m 3 after spraying glycerin, wherein the particulate emission is measured under the following conditions: the heat treated iron ore pellets with and without spraying glycerin are separately submitted to tumbling using an abrasion drum under International Standard: ISO3271:1995 for 1 minute, the drum door is immediately opened and an emission of particulate in suspension inside the drum is measured.