Utilization of dry scrubber waste materials

Claim 2

A process for preparing a cured compacted product from dry flue gas scrubbing waste materials, said process comprising the steps of: (a) providing a substantially dry fly ash-containing powder obtained from the dry scrubbing of fly ash-containing flue gas with lime, said fly ash-containing powder comprising fly ash in intimate admixture with microparticulate crystallites of scrubber reaction materials selected from the group consisting of calcium sulfite, calcium sulfate, hydrates of calcium sulfite and calcium sulfate, calcium oxide, calcium hydroxide and mixtures thereof; (b) contacting said fly ash-containing powder with a predetermined amount of water to produce a powder/water mixture; (c) mixing said powder/water mixture in a manner and for a time sufficient to produce a uniform distribution of said water without the formation of large agglomerates or a sticky plastic mass; (d) placing said mixture in the desired configuration at the utilization site; (e) compacting the placed mixture within a predetermined time subsequent to the contacting step to a density of at least about 70% of the laboratory dry density of said mixture; and (f) curing the compacted material in place to form said cured compacted product.

Claim 3

The process of claim 1 wherein said cured compacted product is a landfill material.

Claim 4

The process of claim 1 wherein said cured compacted product is a structural landfill material.

Claim 5

The process of claim 1 wherein said cured compacted product is utilized in a roadbase composition.

Claim 6

The process of claim 1 wherein said powder/water mixture is transported to said utilization site after said mixing step.

Claim 7

The process of claim 1 wherein said water contacting and said mixing steps are performed at said utilization site.

Claim 8

The process of claim 1 wherein said predetermined amount of water is from about 60% to about 125% of the water amount which produces maximum compacted dry density.

Claim 9

The process of claim 1 wherein said predetermined amount of water is from about 90% to about 120% of the water amount which produces maximum compacted dry density.

Claim 10

The process of claim 7 wherein said water amount which produces the maximum compacted dry density is from about 20% to about 30% by weight of the dry powder.

Claim 11

The process of claim 1 wherein said amount of water is from about 12% to about 37.5% by weight based on the dry powder.

Claim 12

The process of claim 1 wherein said amount of water is from about 18% to about 36% by weight based on the dry powder.

Claim 13

The process of claim 1 additionally comprising the step of contacting said powder/water mixture with additional water at said utilization site.

Claim 14

The process of claim 12 wherein said mixture is contacted with said additional water prior to placement.

Claim 15

The process of claim 12 wherein said mixture is contacted with said additional water after placement.

Claim 16

The process of claim 1 wherein said powder/water mixture is mixed for a period of less than about 60 seconds.

Claim 17

The process of claim 1 wherein said powder/water mixture is compacted to a density of at least about 80% of the laboratory dry density of said mixture.

Claim 18

The process of claim 1 wherein said powder/water mixture is compacted to a density of at least about 90% of the laboratory dry density of said mixture.

Claim 19

The process of claim 1 wherein said powder has a NHG value of about 7 or more.

Claim 20

The process of claim 1 wherein said powder has a NHG value of from about 2 to about 6.

Claim 21

The process of claim 1 wherein said powder has a NHG value of from about 1 or less.

Claim 22

The process of claim 1 wherein said predetermined time is less than about 24 hours.

Claim 23

A process for preparing a cured compacted product from dry flue gas scrubbing waste materials, said process comprising the steps of: (a) providing a substantially dry fly ash-containing powder obtained from the dry scrubbing of fly ash-containing flue gas with lime, said fly ash-containing powder comprising fly ash in intimate admixture with microparticulate crystallites of scrubber reaction materials selected from the group consisting of calcium sulfite, calcium sulfate, hydrates of calcium sulfite and calcium sulfate, calcium oxide, calcium hydroxide and mixtures thereof, said powder having a NHG value of at least about 7; (b) contacting said fly ash-containing powder with from about 90 to about 120% of the water amount which produces maximum compacted density; (c) mixing the resulting powder/water mixture for a period of less than about 60 seconds. (d) transporting said powder/water mixture to a utilization site; (e) placing said mixture in the desired configuration at the utilization site; (f) compacting the placed mixture within about 12 hours subsequent to said contacting step to a density of at least about 70% of the laboratory dry density of said mixture; and (g) curing the compacted material in place to form said cured compacted product.

Claim 24

A process for preparing a cured compacted product from dry flue gas scrubbing waste materials, said process comprising the steps of: (a) providing a substantially dry fly ash-containing powder obtained from the dry scrubbing of fly ash-containing flue gas with lime, said fly ash-containing powder comprising fly ash in intimate admixture with microparticulate crystallites of scrubber reaction materials selected from the group consisting of calcium sulfite, calcium sulfate, hydrates of calcium sulfite and calcium sulfate, calcium oxide, calcium hydroxide and mixtures thereof, said powder having a NHG value of at least about 7; (b) contacting said fly ash-containing powder with from about 90 to about 120% of the water amount which produces maximum compacted density; (c) mixing the resulting powder/water mixture for a period of less than about 60 seconds. (d) transporting said powder/water mixture to a utilization site; (e) placing said mixture in the desired configuration at the utilization site; (f) compacting the placed mixture within about 12 hours subsequent to said contacting step to a density of at least about 70% of the laboratory dry density of said mixture; and (g) curing the compacted material in place to form said cured compacted product.

Claim 25

The process of claim 22 wherein said utilization site comprises a landfill site and said mixture is placed as a landfill material.

Claim 26

The process of claim 22 wherein said fly ash-containing powder is contacted with from about 25 to about 35% by weight of water based on the dry powder.

Claim 27

The process of claim 1 wherein said fly ash-containing powder has a NHG value of less than 7 and further comprising the step of adding from about 2 to about 15% by weight of an additional cementitious material based on the dry weight of said powder.

Claim 28

The process of claim 25 wherein said cementitious material is selected from the group consisting of lime, Portland cement, calcium sulfate hemihydrate, water glass, and synthetic resins or latices.

Claim 29

A cured compacted product made from material which comprises a fly ash-containing powder, said powder comprising fly ash in intimate admixture with microparticulate crystallites of scrubber reaction materials selected from the group consisting of calcium sulfite, calcium sulfate, hydrates of calcium sulfite and calcium sulfate, calcium oxide, calcium hydroxide and mixtures thereof, said product exhibiting a compressive strength of at least about 25 psi, a compacted dry density of from about 55 to about 95 pounds per cubic foot, and a permeability of less than about 1×10 -5 cm/sec.

Claim 30

A cured compacted product made from material which comprises a fly ash-containing powder, said powder comprising fly ash in intimate admixture with microparticulate crystallites of scrubber reaction materials selected from the group consisting of calcium sulfite, calcium sulfate, hydrates of calcium sulfite and calcium sulfate, calcium oxide, calcium hydroxide and mixtures thereof, said product exhibiting a compressive strength of at least about 25 psi, a compacted dry density of from about 55 to about 95 pounds per cubic foot, and a permeability of less than about 1×10 -5 cm/sec.

Claim 31

The product of claim 27 in the form of a compacted landfill material.

Claim 32

The product of claim 27 in the form of a compacted structural landfill material.

Claim 33

A roadbase composition comprising the product of claim 27.

Claim 34

The product of claim 30 additionally comprising aggregate materials.

Claim 35

The product of claim 27 wherein said compressive strength is from about 25 to about 100 psi.

Claim 36

The product of claim 27 wherein said compressive strength is from about 100 to about 800 psi.

Claim 37

The product of claim 27 wherein said compressive strength is above about 800 psi.

Claim 38

The product of claim 29 wherein said density is from about 65 to about 95 pounds per cubic foot.

Claim 39

The product of claim 30 wherein said density is from about 70 to about 95 pounds per cubic foot.

Claim 40

A cured compacted product made from a material which comprises a fly ash-containing powder having a NHG value of 7 or more, said powder comprising fly ash in intimate admixture with microparticulate crystallites of scrubber reaction materials selected from the group consisting of calcium sulfite, calcium sulfate, calcium oxide, calcium hydroxide and mixtures thereof, said product exhibiting a compressive strength of at least about 800 psi, a compacted dry density of from about 55 to about 95 per cubic foot, and a permeability of less than about 1×10 -5 cm/sec.

Claim 41

A cured compacted product made from a material which comprises a fly ash-containing powder having a NHG value of 7 or more, said powder comprising fly ash in intimate admixture with microparticulate crystallites of scrubber reaction materials selected from the group consisting of calcium sulfite, calcium sulfate, calcium oxide, calcium hydroxide and mixtures thereof, said product exhibiting a compressive strength of at least about 800 psi, a compacted dry density of from about 55 to about 95 per cubic foot, and a permeability of less than about 1×10 -5 cm/sec.

Claim 42

A cured compacted product made from a material which comprises a fly ash-containing powder having a NHG value of less than 7, said powder comprising fly ash in intimate admixture with microparticulate crystallites of scrubber reaction materials selected from the group consisting of calcium sulfite, calcium sulfate, hydrates of calcium sulfite, and calcium sulfate, calcium oxide, calcium hydroxide and mixtures thereof, and an additional cementitious material selected from the group consisting of lime, Portland cement, calcium sulfate hemihydrate, water glass, and synthetic resins or latices, said product exhibiting a compressive strength of at least about 25 psi, a compacted dry density of from about 55 to about 95 pounds per cubic foot, and a permeability of less than about 1×10 -5 cm/sec.

Claim 43

A cured compacted product made from a material which comprises a fly ash-containing powder having a NHG value of less than 7, said powder comprising fly ash in intimate admixture with microparticulate crystallites of scrubber reaction materials selected from the group consisting of calcium sulfite, calcium sulfate, hydrates of calcium sulfite, and calcium sulfate, calcium oxide, calcium hydroxide and mixtures thereof, and an additional cementitious material selected from the group consisting of lime, Portland cement, calcium sulfate hemihydrate, water glass, and synthetic resins or latices, said product exhibiting a compressive strength of at least about 25 psi, a compacted dry density of from about 55 to about 95 pounds per cubic foot, and a permeability of less than about 1×10 -5 cm/sec.