Process for producing solid, liquid and gaseous fuels from organic starting material

Claim 2

A process for producing a petroleum-type liquid fuel comprising de-watering an organic starting material selected from the group consisting of fresh sludge, sewage sludge, fermentation sludge from waste water purifying plants, and organic components of private or industrial garbage to obtain a dry, solid bulk material of powdery or granular consistency, subjecting said dry material to heating under the exclusion of air under such conditions that no substantial cleavage of carbon-carbon bonds takes place, said heating being carried out at a rate of 5° C. to 30° C. per minute up to a conversion temperature until the development of gases and vapors has substantially ceased, isolating the gases and vapors from the remaining solid residues and separating the liquid contained in the isolated gases and vapors whereby a petroleum-type fuel is produced.

Claim 3

The process of claim 1 wherein said isolated gases and vapors are subjected to condensation whereby said petroleum-type fuel is produced.

Claim 4

The process of claim 1 wherein said conversion temperature is a maximum of about 400° C.

Claim 5

The process of claim 3 wherein said conversion temperature is at least 200° C.

Claim 6

A process according to claim 1 wherein a conversion catalyst is admixed to the organic starting material before heating.

Claim 7

A process according to claim 1 wherein a catalyst selected from the group consisting of aluminum oxide, and aluminum salt, phosphoric acid, a phosphate, a borate, silica gel, a silicate, an aluminum silicate and an oxide of a transition metal and a mixture of these catalysts is used.

Claim 8

A process according to claim 6 wherein an oxide of a transition metal selected from the group consisting of Ti, V, Cr, Mn, Fe, Co, Ni, Cu and Zn or a mixture of these oxides or a mixture of at least one of these oxides together with at least one of the other compounds mentioned in claim 6 is used.

Claim 9

A process according to claim 6 wherein a catalyst selected from the group consisting of Al 2 O 3 , montmorillonite, Al 2 O 3 *CuO, Al 2 O 3 *V 2 O 5 or Al 2 O 3 *NiO is used.

Claim 10

A process according to claim 1 wherein a conversion temperature of 250° to 350° C. is applied.

Claim 11

A process according to claim 9 wherein a conversion temperature of 280° to 330° C. is applied.

Claim 12

A process according to claim 10 wherein a conversion temperature of about 300° C. is applied.

Claim 13

A process according to claim 1 wherein the heating rate is 10° C. to 20° C. per minute.

Claim 14

A process according to claim 1 wherein the organic starting material is sewer sludge or fermentation sludge obtained from biological waste water purifying plants.

Claim 15

A process according to claim 13 wherein the organic starting material is sewer sludge.

Claim 16

A process according to claim 1 wherein the yield of petroleum-type fuel produced is at least 20% by weight of the dewatered starting material.

Claim 17

A process for producing a petroleum-type liquid fuel consisting essentially of de-watering an organic starting material selected from the group consisting of fresh sludge, sewage sludge, fermentation sludge from waste water purifying plants, and organic components of private or industrial garbage to obtain a dry, solid bulk material of powdery or granular consistency, subjecting said dry material to heating under the exclusion of air under such conditions that no substantial cleavage of carbon-carbon bonds takes place, said heating being carried out at a rate of 5° C. to 30° C. per minute up to a conversion temperature until the development of gases and vapors has substantially ceased, isolating the gases and vapors from the remaining solid residues and separating the liquid contained in the isolated gases and vapors whereby a petroleum-type fuel is produced.

Claim 18

A process for producing a petroleum-type liquid fuel consisting essentially of de-watering an organic starting material selected from the group consisting of fresh sludge, sewage sludge, fermentation sludge from waste water purifying plants, and organic components of private or industrial garbage to obtain a dry, solid bulk material of powdery or granular consistency, subjecting said dry material to heating under the exclusion of air under such conditions that no substantial cleavage of carbon-carbon bonds takes place, said heating being carried out at a rate of 5° C. to 30° C. per minute up to a conversion temperature until the development of gases and vapors has substantially ceased, isolating the gases and vapors from the remaining solid residues and separating the liquid contained in the isolated gases and vapors whereby a petroleum-type fuel is produced.