Abstract: A process for producing a hydrocarbon stream with reduced CS2 content, comprising contacting a hydrocarbon stream containing CS2 with a solid reactive CS2-scavenger which contains primary and/or secondary amino group-bearing hydrocarbon residues attached to a solid support, at a temperature in the range of from 0 to 300° C., and separating the obtained reaction product of CS2 and reactive CS2-scavenger from the hydrocarbon stream.

Abstract: A conveyor cleaning system includes a treating region, a processing region, and a conveyor belt traveling from the treating region to the processing region. A distributor positioned across the treating region deposits a film of ozonated water on the conveyor belt. In the processing region, the conveyor belt is exposed to soiling agents such as grease and other animal matter. A high-pressure rinser may be positioned over the treating section such that the distributor is positioned between the high-pressure rinser and the processing region. Ozonated water may be generated by a system including first and second tanks. The first tank is filled with ozone gas and water. After a predetermined time, undissolved ozone gas is released. The contents of the first tank are then transferred to a second tank along with more ozone gas. After waiting a predetermined time period, undissolved ozone gas is released from the second tank.

Abstract: A conveyor cleaning system includes a treating region, a processing region, and a conveyor belt traveling from the treating region to the processing region. A distributor positioned across the treating region deposits a film of ozonated water on the conveyor belt. In the processing region, the conveyor belt is exposed to soiling agents such as grease and other animal matter. A high-pressure rinser may be positioned over the treating section such that the distributor is positioned between the high-pressure rinser and the processing region. Ozonated water may be generated by a system including first and second tanks. The first tank is filled with ozone gas and water. After a predetermined time, undissolved ozone gas is released. The contents of the first tank are then transferred to a second tank along with more ozone gas. After waiting a predetermined time period, undissolved ozone gas is released from the second tank.

Abstract: A conveyor cleaning system includes a treating region, a processing region, and a conveyor belt traveling from the treating region to the processing region. A distributor positioned across the treating region deposits a film of ozonated water on the conveyor belt. In the processing region, the conveyor belt is exposed to soiling agents such as grease and other animal matter. A high-pressure rinser may be positioned over the treating section such that the distributor is positioned between the high-pressure rinser and the processing region. Ozonated water may be generated by a system including first and second tanks. The first tank is filled with ozone gas and water. After a predetermined time, undissolved ozone gas is released. The contents of the first tank are then transferred to a second tank along with more ozone gas. After waiting a predetermined time period, undissolved ozone gas is released from the second tank.

Abstract: The present invention relates to a process for separating at least one metal compound and/or a component thereof from a mixture, said process comprising contacting the said mixture with a heteropoly acid or heteropoly acid anion, thereby producing a precipitate comprising the heteropoly acid or heteropoly acid anion and the metal compound and/or a component thereof. The present invention further relates to a process for the purification of a mixture containing at least one metal compound, said process comprising contacting the said mixture with a heteropoly acid or heteropoly acid anion, thereby producing a precipitate that is substantially insoluble in the said reaction mixture and recovering the reaction mixture.