Abstract: A glove remover apparatus is provided. The glove remover apparatus is especially suitable for the removing of a used medical glove in a sterile manner; however the glove remover apparatus is not limited to removing only medical gloves. The glove remover apparatus may have an extended long handle having a trigger spring at the distal end wherein the trigger spring grasps a glove on the user's hand. Once grasped by the apparatus, the used glove may be safely removed without a user needing to actually touch the glove.

Abstract: A glove remover apparatus is provided. The glove remover apparatus is especially suitable for the removing of a used medical glove in a sterile manner; however the glove remover apparatus is not limited to removing only medical gloves. The glove remover apparatus may have an extended long handle having a trigger spring at the distal end wherein the trigger spring grasps a glove on the user's hand. Once grasped by the apparatus, the used glove may be safely removed without a user needing to actually touch the glove.

Abstract: A reactor for contacting a fluid with a granular solid, the reactor including: a reactor housing including a reaction zone in which the fluid and the granular solid are contacted together; a granular solids inlet adapted to deliver a bed of granular solids into the reaction zone wherein the height and/or width dimension of the bed of the granular solids is substantially less than the length of the bed; a plurality of fluid inlets for delivering the fluid into the reaction zone, whereby the delivery of the fluid into the reaction zone at least partially fluidises the bed of granular solids; a granular solids outlet for receiving the bed of granular solids after having passed through the reaction zone; and, a fluid outlet for receiving the fluid, and any entrained particles, after the fluid has passed through the reaction zone.

Abstract: A process for producing syngas from a carbonaceous substance and/or treating a carbonaceous substance, the process including the following steps: a) reducing the surface moisture of the carbonaceous substance; b) reducing the inherent moisture of the carbonaceous substance; and, c) gasifying the carbonaceous substance to produce syngas, wherein at step a) the carbonaceous substance is directly contacted with a hot gas at a temperature of between 50° C. to 250° C., and/or the carbonaceous substance is indirectly contacted with saturated steam at a temperature of between 105° C. and 250° C.

Abstract: A reactor for contacting a fluid with a granular solid, the reactor including: a reactor housing including a reaction zone in which the fluid and the granular solid are contacted together; a granular solids inlet adapted to deliver a bed of granular solids into the reaction zone wherein the height and/or width dimension of the bed of the granular solids is substantially less than the length of the bed; a plurality of fluid inlets for delivering the fluid into the reaction zone, whereby the delivery of the fluid into the reaction zone at least partially fluidises the bed of granular solids; a granular solids outlet for receiving the bed of granular solids after having passed through the reaction zone; and, a fluid outlet for receiving the fluid, and any entrained particles, after the fluid has passed through the reaction zone.

Abstract: A process, system and apparatus is provided for passivating carbonaceous material against spontaneous combustion. The process involves drying the carbonaceous material in a low oxygen environment and pre-conditioning the carbonaceous material by contacting it with volatile matter contained in a countercurrent gas stream. The volatile matter coats the particles of dried carbonaceous material and plugs the micropores of the dried carbonaceous material, thereby passivating it against adsorption of water and oxygen, and thus spontaneous combustion. The pre-conditioned dried material then undergoes devolatilisation at temperatures at which volatile matter is evolved. The evolved volatile matter mixes with the countercurrent gas stream and is used to pre-condition dried carbonaceous material located upstream.