Removal of chlorine from pyrolysis vapors

Claim 2

In a process for the pyrolysis of solid organic wastes which includes solid organic wastes which yield hydrogen chloride upon pyrolysis, and wherein dried, comminuted solid organic waste, a solid source of heat and a carrier gas which is nondeleteriously reactive with respect to pyrolysis products are combined and passed through a pyrolysis zone maintained at a temperature from about 600° to about 2000° F. to form pyrolysis products which comprise, the solid source of heat, a carbon containing solid residue of pyrolysis, pyrolysis gases comprising a condensable pyrolytic oil and a gaseous component comprising water, hydrogen chloride, and hydrocarbons, the method of recovering a pyrolytic oil and a gaseous residue substantially free of hydrogen chloride which comprises: (a) separating the solid source of heat and the carbon containing solid residue of pyrolysis from said pyrolysis gases; (b) contacting the resulting solids free pyrolysis gases with a solid hydrogen chloride acceptor containing a calcium compound selected from the group consisting calcium carbonate, calcium oxide, calcium hydroxide, calcium bicarbonate and mixtures thereof in a hydrogen chloride removal zone maintained at a temperature above the dew point of the pyrolysis gases to form a spent hydrogen chloride acceptor, formed by reaction of the hydrogen chloride with the hydrogen chloride acceptor, having calcium chloride at the surface thereof and a pyrolysis gases residue; (c) recovering pyrolytic oil from the pyrolysis gases residue; and (d) removing said calcium chloride from said spent acceptor by washing the calcium chloride from the surface to form an aqueous solution of calcium chloride.

Claim 3

A process as claimed in claim 1 in which the hydrogen chloride removal zone is maintained at a temperature from 400° to about 1600° F.

Claim 4

In a process for the pyrolysis of solid organic wastes which includes solid organic wastes which yield hydrogen chloride upon pyrolysis wherein dried, comminuted solid organic waste, a solid source of heat and a carrier gas which is nondeleteriously reactive with respect to pyrolysis products are combined and passed through a pyrolysis zone maintained at a temperature from about 600° to about 2000° F. to form pyrolysis products which comprise the solid source of heat, a carbon containing solid residue of pyrolysis, pyrolysis gases comprising a condensable pyrolytic oil and a gaseous component which includes water, hydrogen chloride, and hydrocarbons, the method of recovering a pyrolytic oil and a gaseous residue substantially free of hydrogen chloride which comprises: (a) separating the solid source of heat and the carbon containing solid residue of pyrolysis from said pyrolysis gases; (b) contacting the resulting solids free pyrolysis gases with a solid material containing a calcium compound selected from the group consisting of calcium oxide, calcium carbonate and mixtures thereof in a hydrogen chloride removal zone maintained at a temperature above the dew point of the pyrolysis gases to convert a portion of the calcium compound to calcium chloride and yield a pyrolysis gases residue, said calcium chloride being formed on the surface of the solid material; (c) recovering pyrolytic oil from the pyrolysis gases residue; (d) treating the solid material to remove calcium chloride from the surface thereof to expose unreacted calcium compound for separation of hydrogen chloride by washing the calcium chloride from the surface to form an aqueous solution of calcium chloride; and

Claim 5

In a process for the pyrolysis of solid organic wastes which includes solid organic wastes which yield hydrogen chloride upon pyrolysis wherein dried, comminuted solid organic waste, a solid source of heat and a carrier gas which is nondeleteriously reactive with respect to pyrolysis products are combined and passed through a pyrolysis zone maintained at a temperature from about 600° to about 2000° F. to form pyrolysis products which comprise the solid source of heat, a carbon containing solid residue of pyrolysis, pyrolysis gases comprising a condensable pyrolytic oil and a gaseous component which includes water, hydrogen chloride, and hydrocarbons, the method of recovering a pyrolytic oil and a gaseous residue substantially free of hydrogen chloride which comprises: (a) separating the solid source of heat and the carbon containing solid residue of pyrolysis from said pyrolysis gases; (b) contacting the resulting solids free pyrolysis gases with a solid material containing a calcium compound selected from the group consisting of calcium oxide, calcium carbonate and mixtures thereof in a hydrogen chloride removal zone maintained at a temperature above the dew point of the pyrolysis gases to convert a portion of the calcium compound to calcium chloride and yield a pyrolysis gases residue, said calcium chloride being formed on the surface of the solid material; (c) recovering pyrolytic oil from the pyrolysis gases residue; (d) treating the solid material to remove calcium chloride from the surface thereof to expose unreacted calcium compound for separation of hydrogen chloride by washing the calcium chloride from the surface to form an aqueous solution of calcium chloride; and

Claim 6

(e) recycling said treated solid material to the hydrogen chloride removal zone.

Claim 7

(e) recycling said treated solid material to the hydrogen chloride removal zone.

Claim 8

A process as claimed in claim 3 in which the solid material containing a calcium compound is dolomite.

Claim 9

A process as claimed in claim 3 in which: (a) the aqueous solution of calcium chloride is dehydrated; (b) the calcium chloride is contacted with steam and carbon dioxide at an elevated temperature and pressure to yield calcium carbonate and hydrogen chloride; (c) the calcium carbonate is recycled to the hydrogen chloride removal zone; and (d) the hydrogen chloride is recovered as a concentrated acid.

Claim 10

A process as claimed in claim 3 in which the hydrogen chloride removal zone is maintained at a temperature from about 400° to about 1600° F.

Claim 11

The process of claim 4 wherein said dolomite is calcined.