Abstract: A gutter diverter is disclosed may include providing a base having a generally triangular shaped planar section having a first leg, a second leg, and a third leg positioned at a periphery of the generally triangular shaped planar section. In addition, the gutter diverter may include forming a first attachment tab positioned on the first leg of the base and projecting orthogonally downwardly from the base. The gutter diverter may include forming a second attachment tab positioned on the second leg of the base and projecting orthogonally downwardly from the base. Moreover, the gutter diverter may include forming a diverter plate positioned on the third leg of the base and projecting orthogonally upwardly from the base.

Abstract: A gutter diverter is disclosed may include providing a base having a generally triangular shaped planar section having a first leg, a second leg, and a third leg positioned at a periphery of the generally triangular shaped planar section. In addition, the gutter diverter may include forming a first attachment tab positioned on the first leg of the base and projecting orthogonally downwardly from the base. The gutter diverter may include forming a second attachment tab positioned on the second leg of the base and projecting orthogonally downwardly from the base. Moreover, the gutter diverter may include forming a diverter plate positioned on the third leg of the base and projecting orthogonally upwardly from the base.

Abstract: Aluminum scrap containing a carbon-containing coating is cleaned with about 212.degree. F. hot water, and then decarbonized with about 1000.degree. F. superheated steam which produces a carbon-containing volatile from the carbon-containing coating and a decarbonized aluminum scrap. A spent steam and carbon-containing volatile gaseous mixture at about 212.degree. F. is contacted with a warm water filtrate at a nominal temperature of about 132.degree. F., recovered from the process which causes the spent steam to condensed. The condensate at about 212.degree. F. is separated from the carbon-containing volatile and the latter combusted. The combustion products can be used to preheat indirectly other stream in the process or to dry the decarbonized aluminum scrap at a temperature low enough not to cause oxidation of the aluminum scrap.