Incineration of lime-conditioned sewage sludge with high sulfur fuel

Claim 2

An economical, non-polluting process for the disposal of a sewage waste stream in which the waste stream is dewatered and the combustible sludge formed thereby is incinerated, comprising the steps of: a. Adding a quantity of lime and a quantity of fine crushed coal to the sewage waste stream sufficient to function as filtering aids, b. Dewatering the sewage waste stream by filtering to form sludge filter cake containing a relatively large amount of lime and a quantity of fine coal therein, c. Incinerating the sludge filter cake to burn the combustible sludge and the fine coal therein using a high-sulfur fuel as auxiliary fuel at a temperature at which the sulfur present in the fuel and in the sludge filter cake reacts with the lime in the sludge filter cake and with oxygen to produce CaSO 4 , and d. Removing the CaSO 4 with the solids produced by the incineration operation for disposal.

Claim 3

The process of claim 1 wherein the quantity of lime added to said sewage waste stream is at least 10 pounds per 100 pounds of dry solids in said filter cake.

Claim 4

The process of claim 1 wherein the quantity of lime present in said filter cake is 50% in excess of the theoretical requirement for reaction with the sulfur present during incineration.

Claim 5

The process of claim 1 wherein the auxiliary fuel is a high-sulfur oil containing 1/2%, by weight, or more of sulfur.

Claim 6

The process of claim 1 wherein the auxiliary fuel is a high-sulfur coal containing 1/2%, by weight, or more of sulfur.

Claim 7

The process of claim 5 wherein the fine crushed coal serving as a filtering aid is a high-sulfur coal.

Claim 8

The process of claim 1 wherein the incineration is conducted as a fluidized bed reaction.

Claim 9

The process of claim 7 wherein the incineration is carried out in the temperature range from about 1200° F. to about 1600° F.

Claim 10

The process of claim 1 wherein the dewatering step is a filter press operation.

Claim 11

An economical, non-polluting process for the disposal of a sewage waste stream in which the waste stream is dewatered and the sludge produced thereby is incinerated, comprising the steps of: a. Adding lime to said sewage waste stream as a filtering aid in the amount of at least 10 pounds per 100 pounds of dry solids in the filter cake produced in the dewatering step hereafter, b. Introducing fine crushed coal of high-sulfur content into said sewage waste stream as a further filtering aid, c. Dewatering the sewage waste stream in a filter press to form sludge filter cake containing lime in an amount at least 50% in excess of that required for reaction with the sulfur present in the incineration step hereafter, d. Incinerating the sludge filter cake in a fluidized bed reactor at a temperature from about 1200° F. up to about 1600° F. using a high-sulfur auxiliary fuel whereby the sulfur present during incineration reacts with the lime in the filter cake and with oxygen to produce CaSO 4 , and e. Removing the CaSO 4 with the other solids, including ash, produced during incineration.

Claim 12

An economical, non-polluting process for the disposal of a sewage waste stream in which the waste stream is dewatered and the sludge produced thereby is incinerated, comprising the steps of: a. Adding lime to said sewage waste stream as a filtering aid in the amount of at least 10 pounds per 100 pounds of dry solids in the filter cake produced in the dewatering step hereafter, b. Introducing fine crushed coal of high-sulfur content into said sewage waste stream as a further filtering aid, c. Dewatering the sewage waste stream in a filter press to form sludge filter cake containing lime in an amount at least 50% in excess of that required for reaction with the sulfur present in the incineration step hereafter, d. Incinerating the sludge filter cake in a fluidized bed reactor at a temperature from about 1200° F. up to about 1600° F. using a high-sulfur auxiliary fuel whereby the sulfur present during incineration reacts with the lime in the filter cake and with oxygen to produce CaSO 4 , and e. Removing the CaSO 4 with the other solids, including ash, produced during incineration.