Coal fired power plant with pollution control and useful byproducts

Claim 2

A coal fired power plant comprising: (a) coal gasification means for heating coal in the presence of an oxidant-lean atmosphere under partial coal-gasifying conditions to produce a carbonaceous char and a crude gas stream; (b) means for separating sulfur-containing compounds from the crude gas stream to produce a combustible gas stream and a sulfur compound-containing stream; (c) means for converting the sulfur compound containing stream into elemental sulfur; (d) energy-conversion means for burning a portion of the combustible gas stream and a portion of the carbonaceous char to produce electricity and SO 2 -containing flue gas; (e) flue gas desulfurization means for contacting the SO 2 -containing flue gas with lime and limestone to convert sulfur compounds in the flue gas to gypsum; (f) gypsum desulfurization means for heating the gypsum and the remaining portion of carbonaceous char under reducing conditions utilizing burning of the remaining portion of the combustible gas stream to provide energy to produce a SO 2 -containing gas stream and a sintered usable aggregate; and (g) means for recycling the SO 2 -containing gas stream from step (f) to the coal gasification means.

Claim 3

The coal fired power plant of claim 1, wherein said coal gasification means heats particulate coal in the presence of an oxidant-lean atmosphere which contains up to about 20% by volume of steam, wherein there are controlling means for controlling the oxidant content and the feed rate of the oxidant-lean atmosphere to maintain a temperature of from about 700° C. to about 1100° C.

Claim 4

The coal fired power plant of claim 1, wherein the feed controlling means controls feed rate of the oxidantlean atmosphere to maintain a temperature of from about 750° C. to about 1000° C.

Claim 5

The coal fired power plant of claim 1, wherein the partial coal-gasifying conditions include a pressure from about 1.5 to about 20 atmospheres.

Claim 6

The coal fired power plant of claim 1, wherein there are means to control the partial coal-gasifying conditions to produce a carbonaceous char which contains from about 40 to 80% weight carbon.

Claim 7

The coal fired power plant of claim 1, wherein at least a portion of the combustible gas stream is used for producing steam and the steam is directed to the oxidantlean atmosphere in the coal gasification means.

Claim 8

The coal fired power plant of claim 1, wherein the gypsum desulfurization means for the heating of the gypsum and the carbonaceous char passes a mixture of air and the combustible gas through the gypsum and the carbonaceous char, wherein there are means for controlling the flow ratios of the air and the combustible gas to maintain a temperature sufficiently high to cause thermal decomposition and reduction of the gypsum, and to maintain reducing conditions within the gypsum and the carbonaceous char.

Claim 9

The coal fired power plant of claim 7, wherein the flow means for controlling the flow rates of the air and the combustible gas stream maintain a temperature of the gypsum and the carbonaceous char of from about 1100° C. to about 1500° C.

Claim 10

The coal fired power plant of claim 8, wherein the flow rates of the air and the combustible gas stream are controlled to maintain a temperature of from about 1200° C. to about 1300° C.

Claim 11

The coal fired power plant of claim 1, wherein the gypsum desulfurization means is a rotary kiln, a fluid bed reactor or a travelling grate reactor.

Claim 12

The coal fired power plant of claim 1, wherein the gypsum desulfurization means is a travelling grate reactor.

Claim 13

The coal fired power plant of claim 11 wherein step (f) includes means for moving the travelling grate carrying a charge of pelletized feed mixture successively through firing and post-firing zones, and means for retaining charge in the post-firing zone for a period of from about 10 to about 30 minutes.

Claim 14

The coal fired power plant of claim 1, wherein the coal is lignite, subbituminous or bituminous.

Claim 15

The coal fired power plant of claim 13, wherein the coal is high sulfur coal.

Claim 16

A process for converting coal into electrical energy and usable byproducts, comprising the steps of: (a) heating coal in a coal gasification zone in the presence of an oxidant-lean atmosphere under partial coal-gasifying conditions to produce a carbonaceous char and a crude gas stream; (b) separating substantial portions of sulfurcontaining compounds from the crude gas stream to produce a combustible gas stream and a sulfur compound containing stream; (c) converting the sulfur-containing compounds into elemental sulfur; (d) burning a portion of the combustible gas stream and a portion of the carbonaceous char to power energy-conversion means to produce electricity and SO 2 -containing flue gas; (e) feeding the remaining portions of the carbonaceous char product and the combustible gas stream into a gypsum desulfurization zone; (f) feeding the SO 2 -containing flue gas from the energy-conversion means into a flue gas desulfurization zone; (g) contacting the SO 2 -containing flue gas with lime and limestone in the flue gas desulfurization zone to convert sulfur compounds in the flue gas to gypsum; (h) feeding the gypsum into the gypsum desulfurization zone; (i) heating the gypsum and the remaining portion of the carbonaceous char in the gypsum desulfurization zone under reducing conditions utilizing burning of the remaining portion of the combustible gas stream to provide energy to produce a SO 2 -containing gas stream and a sintered usable aggregate, and (j) recycling the SO 2 -containing gas stream from step (i) to the coal gasification zone to provide at least a portion of the oxidant-learn atmosphere.

Claim 17

A process for converting coal into electrical energy and usable byproducts, comprising the steps of: (a) heating coal in a coal gasification zone in the presence of an oxidant-lean atmosphere under partial coal-gasifying conditions to produce a carbonaceous char and a crude gas stream; (b) separating substantial portions of sulfurcontaining compounds from the crude gas stream to produce a combustible gas stream and a sulfur compound containing stream; (c) converting the sulfur-containing compounds into elemental sulfur; (d) burning a portion of the combustible gas stream and a portion of the carbonaceous char to power energy-conversion means to produce electricity and SO 2 -containing flue gas; (e) feeding the remaining portions of the carbonaceous char product and the combustible gas stream into a gypsum desulfurization zone; (f) feeding the SO 2 -containing flue gas from the energy-conversion means into a flue gas desulfurization zone; (g) contacting the SO 2 -containing flue gas with lime and limestone in the flue gas desulfurization zone to convert sulfur compounds in the flue gas to gypsum; (h) feeding the gypsum into the gypsum desulfurization zone; (i) heating the gypsum and the remaining portion of the carbonaceous char in the gypsum desulfurization zone under reducing conditions utilizing burning of the remaining portion of the combustible gas stream to provide energy to produce a SO 2 -containing gas stream and a sintered usable aggregate, and (j) recycling the SO 2 -containing gas stream from step (i) to the coal gasification zone to provide at least a portion of the oxidant-learn atmosphere.

Claim 18

The process of claim 15, wherein step (a) comprises heating particulate coal in the presence of an oxidant-lean atmosphere which contains up to about 20% by volume of steam, wherein the oxidant content and the feed rate of the oxidant-lean atmosphere are controlled to maintain a temperature of from about 700° C. to about 1100° C.

Claim 19

The process of claim 16, wherein the feed rate of the oxidant-lean atmosphere is controlled to maintain a temperature of from about 750° C. to about 1000° C.

Claim 20

The process of claim 17, wherein the partial coalgasifying conditions include a pressure from about 1.5 to about 20 atmospheres.

Claim 21

The process of claim 15, wherein the partial coalgasifying conditions of step (a) are controlled to produce a carbonaceous char which contains from about 40 to about 80% weight carbon.

Claim 22

The process of claim 15, wherein at least a portion of the combustible gas stream is used for producing steam and the steam is directed to the oxidant-lean atmosphere of step (a).

Claim 23

The process of claim 15, wherein the heating of the gypsum and the carbonaceous char in step (i) is achieved by passing a mixture of air and the remaining portion of the combustible gas through the gypsum and the carbonaceous char, wherein the flow ratios of the air and the combustible gas are controlled to maintain a temperature sufficiently high to cause thermal decomposition and reduction of the gypsum, and to maintain reducing conditions within the gypsum and the carbonaceous char.

Claim 24

The process of claim 21, wherein the flow rates of the air and the combustible gas stream are controlled to maintain a temperature of the gypsum and the carbonaceous char of from about 1100° C. to about 1500° C.

Claim 25

The process of claim 22, wherein the flow rates of the air and the combustible gas stream are controlled to maintain a temperature of from about 1200° C. to about 1300° C.

Claim 26

The process of claim 15, wherein step (i) is conducted in a rotary kiln, fluid bed reactor or a travelling grate reactor.

Claim 27

The process of claim 15, wherein the heating of step (i) is conducted in a travelling grate reactor.

Claim 28

The process of claim 25 wherein step (i) includes moving the travelling grate carrying a charge of pelletized feed mixture successively through firing and post-firing zones, and the charge is retained in the post-firing zone for a period of from about 10 to about 30 minutes.

Claim 29

The process of claim 15, wherein the coal is lignite, subbituminous for bituminous.

Claim 30

The process of claim 27, wherein the coal is high sulfur coal.