COAL GASIFICATION

Coal gasification is reviewed here to provide a foundation for more detailed discussion of biomass gasification.

A. Brief History

Coal gasification to produce gas for a variety of applications such as fuels, chemicals, and chemical intermediates has been known for many years. The largest application of coal gasification by far has been for manufactured fuel gas production by pyrolytic and partial oxidation processes in which the primary fuel components in the product gas are hydrogen, carbon monoxide, and methane. The first manufactured gas (town gas) plant was built in England in 1812 by London and Westminster Chartered Gas, Light and Coke Company, although the first record of experimental manufactured gas production from coal dates back to seventeenth-century England (cj. Environmental Research and Technology and Koppers Co., 1984; Srivastava, 1993). North America’s first manufactured gas plants were built in Baltimore in 1816, in Boston in 1822, and in New York in 1825 (Rhodes, 1974). The early processes involved the carbonization or destructive distillation of bituminous coal at temperatures of 600 to 800°C in small cast-iron retorts to yield “coal gas” (Villaume, 1984). It has been estimated that more than 1500 manufactured gas plants were in operation in the United States during the nineteenth century and the first half

Temperature

Enthalpy

Process

Stoichiometry

(kj)

Pyrolysis

C6H10O5

— 5CO + 5H2 + C

300

180

1000

209

c6H10o5

-* 5CO + CH4 + 3H2

300

105

1000

120

c6H10o5

4CO + CH4 + C + 2H2 + H20

300

-26

1000

-16

c6H10o5

-ч> 3CO + C02 + 2CH4 + H2

300

-142

1000

-140

c6H10o5

3CO + CH4 + 2C + H2 + 2H20

300

-158

1000

-152

C6H10O5

2CO + C02 + 2CH4 + C + H20

300

-274

1000

-276

Partial oxidation

QH10O, + 0.5O2 -> 6CO + 5H2

300

71

1000

96

c6h10o5

+ 02 ^ 6CO + 4H2 + H20

300

-172

1000

-142

c6HI0o5

+ 02 5CO + C02 + 5H2

300

-213

1000

-180

QH10o5

+ 1.502 -> 6CO + 3H2 + 2H20

300

-414

1000

-389

c6h10o5

+ 1.502 -> 4CO + 2C02 + 3H2

300

-498

1000

-464

СбН[оОд

+ 202 3CO 4- 3C02 + 5H2

300

-778

1000

-745

Steam gasification

C6Hl0O5

+ H20 -> 6CO + 6H2

300

310

1000

322

c6H10o5

+ 2H20 5CO + C02 + 7H2

300

272

1000

310

C6H10O5

+ 3H20 ^ 4CO + 2C02 + 8H2

300

230

1000

276

c6H10o5

+ 7H20 -> 6C02 + 12H2

300

64

1000

137

c6H10o5

+ H20 4CO + C02 + CH4 + 4H2

300

64

1000

85

c6Hi0o5

+ H20 2CO + 2C02 + 2CH4 + 2H2

300

-184

1000

-175

“The standard enthalpies of formation used for the calculations are from Stull, Westrum, and Sinke (1987) and Daubert and Danner (1989). The standard enthalpy of formation of cellulose was calculated from its heat of combustion. The monomeric unit of cellulose is C6H10O5. The enthalpies are listed in kj/g-mol of monomeric unit gasified.

TABLE 9.2 Higher Heating Values of Combustibles Commonly Formed in Gasification Processes

Higher heating value

Combustible

MJ/m5 (n)

Btu/SCF

Methane

39.73

1012

Ethane

69.18

1762

Propane

98.51

2509

Ethylene

64.43

1641

Propylene

92.42

2354

Benzene

146.1

3722

Carbon monoxide

12.67

322.6

Hydrogen

12.74

324.5

of the twentieth century. The gasification processes used in these plants af­forded water gas, producer gas, oil gas, coke oven gas, and blast furnace gas (Liebs, 1985; Remediation Technologies, Inc., 1990).

Natural gas displaced most manufactured gas for municipal distribution in industrialized countries after World War II. In the 1960s and 1970s, interest in developing advanced coal gasification processes was rekindled when it was believed that natural gas reserves would become insufficient in a few years to meet demand. This activity has since declined, but several coal gasification processes developed during this period have been commercialized and are used for production of fuel and synthesis gas.