Separating carbon from ash

Claim 2

In a pulverized-coal fired steam generating power plant having a furnace volume for the combustion of pulverized-coal therein generating thereby a flue-gas stream laden with flyash, a backpass volume, a horizontal pass for conducting the flyash-laden flue-gas stream from the furnace volume to the backpass volume thence therethrough, a stack, means for conducting the flyash-laden flue-gas stream from the backpass volume to the stack thence therethrough to the atmosphere, a method of separating unburned carbon as particulate matter from the flyash, said method comprising the steps of: a. effecting a separation of the flyash-laden flue-gas stream as a function of a difference in a property between a gas component of the flue-gas stream and a particle component thereof such that the gas component is more apt to flow along a first fluid flow path and the particle component is more apt to flow along a second fluid flow path, the portion of the flue-gas stream flowing along said second fluid flow path having entrained therein a quantity of flyash containing a first fraction of particles including at least unburned carbon particles and a second fraction of other particulate matter, said particles of the first fraction having a relatively higher specific gravity than the particles of the second fraction; b. as a function of the difference in the specific gravities of the first and second fractions in said quantity of flyash effecting a separation of said quantity of flyash into a first product group and an interim product group such that the ratio of the number of second fraction particles having relatively lower specific gravities in the interim product group to the number of second fraction particles having relatively lower specific gravities in the at least one of said first or second fractions is greater than the ratio of the number of first fraction particles having relatively higher specific gravities in the interim product group to the number of first fraction particles having relatively higher specific gravities in the at least one of said first or second fractions; and c. effecting a separation of the interim product group.

Claim 3

The method of separating unburned carbon as particulate matter from the flyash as set forth in claim 1 wherein the step of effecting a second separation of the flyash-laden flue-gas stream into a first product group and a second product group includes the step of providing a separator disposed along at least one of said first or second fluid flow paths operative to effect thereby the second separation.

Claim 4

The method of separating unburned carbon as particulate matter from the flyash as set forth in claim 2 wherein the step of providing a separator includes the step of providing a housing having fluid inlet means, first fluid exit means, second fluid exit means and an axis central thereto.

Claim 5

The method of separating unburned carbon as particulate matter from the flyash as set forth in claim 3 wherein the step of providing a separator includes the step of providing first separation means and second separation means disposed within the separator.

Claim 6

The method of separating unburned carbon as particulate matter from the flyash as set forth in claim 4 wherein the step of providing first separation means and second separation means includes the step of providing an inverted, truncated collector cone coaxial with the axis and disposed within the housing at the lower segment thereof above the fluid inlet means in fluid communication therewith and so as to form thereby an annular opening between the periphery of the collector cone and the housing, rotary classifier means coaxial with the axis and disposed within the housing at the upper segment thereof in fluid communication with the second fluid exit means, an expansion chamber defined by the housing and disposed therein above said collector cone and below said rotary classifier; said annular opening having a first cross sectional area and said expansion chamber having a second cross sectional area greater than the first cross sectional area.

Claim 7

The method of separating unburned carbon as particulate matter from the flyash as set forth in claim 5 wherein the step of effecting a second separation of the flyash-laden flue-gas stream into a first product group and a second product group includes the step of providing means disposed along at least one of said first or second fluid flow paths for collecting the flyash.

Claim 8

The method of separating unburned carbon as particulate matter from the flyash as set forth in claim 6 wherein the step of providing means disposed along at least one of said first or second fluid flow paths for collecting the flyash includes the step of collecting the flyash at said flyash collecting means.

Claim 9

The method of separating unburned carbon as particulate matter from the flyash as set forth in claim 7 wherein the step of collecting the flyash includes the step of entraining the collected flyash in a fluid stream.

Claim 10

The method of separating unburned carbon as particulate matter from the flyash as set forth in claim 8 wherein the step of entraining the collected flyash in the fluid stream includes the step of injecting the flyash-entrained fluid stream into the separator at the fluid inlet means.

Claim 11

The method of separating unburned carbon as particulate matter from the flyash as set forth in claim 9 wherein the step of injecting the flyash-entrained fluid stream into the separator at the fluid inlet means includes the step of directing the flyash-entrained fluid stream through the separator whereby the flyash-entrained fluid stream flows through the housing from the fluid inlet means around the collector cone and through the annular opening into the expansion chamber wherein relatively heavy unburned carbon particles and other relatively heavy flyash fall out of the flyash-entrained fluid stream into the collector cone to form a second product group discharged from the separator at the first fluid exit means, thence while yet still containing those unburned carbon particles and other flyash not so heavy as to fall out of the flyash-entrained fluid stream upward from the expansion chamber to the rotary classifier means whereat those unburned carbon particles and other flyash possessing sufficient velocity pass through the rotary classifier means to form a first product group discharged from the separator at the second fluid exit means and whereat those unburned carbon particles and other flyash not possessing sufficient velocity fall into the collector cone to join the second product group discharged from the separator at the first fluid exit means.

Claim 12

The method of separating unburned carbon as particulate matter from the flyash as set forth in claim 10 wherein the step of directing the flyash-entrained fluid stream through the separator includes the step of effecting control over the mass flow rate of the flyash-entrained fluid stream over a continuous range of mass flow rates.

Claim 13

The method of separating unburned carbon as particulate matter from the flyash as set forth in claim 11 wherein the step of directing the flyash-entrained fluid stream through the separator includes the step of effecting control over the rotational velocity of the rotary classifier means over a continuous range of rotational velocities.

Claim 14

The method of separating unburned carbon as particulate matter from the flyash as set forth in claim 12 wherein the step of effecting a second separation of the flyash-entrained flue-gas stream into a first product group and a second product group includes the step of simultaneously establishing a first mass flow rate of the flyash-entrained fluid stream and a first rotational velocity of the rotary classifier means.

Claim 15

The method of separating unburned carbon as particulate matter from the flyash as set forth in claim 13 wherein the step of simultaneously establishing a first mass flow rate of the flyash-entrained fluid stream and a first rotational velocity of the rotary classifier means includes the step of establishing a first mass flow rate and a first rotational velocity such that the distribution between the coarse product group and the fine product group of the weight percentage of unburned carbon after the second separation as a function of the mass flow rate of the flyash-entrained fluid stream is characterized by an approximately linear functional relationship according to the equation y=mx+b wherein m is approximately equal to -1.07×10 -3 and b is approximately equal to 9.5.

Claim 16

The method of separating unburned carbon as particulate matter from the flyash as set forth in claim 5 wherein the step of effecting a second separation of the flyash-laden flue-gas stream into a first product group and a second product group includes the step of injecting the flyash-laden flue-gas stream of at least one of the first or second fluid flow paths into the separator at the fluid inlet means.

Claim 17

The method of separating unburned carbon as particulate matter from the flyash as set forth in claim 15 wherein the step of injecting the flyash-laden flue-gas stream of at least one of the first or second fluid flow paths into the separator at the fluid inlet means includes the step of directing the flyash-laden flue-gas stream of at least one of the first or second fluid flow paths through the separator whereby the flyash-laden flue-gas stream of at least one of the first or second fluid flow paths flows through the housing from the fluid inlet means around the collector cone and through the annular opening into the expansion chamber wherein relatively heavy unburned carbon particles and other relatively heavy flyash fall out of the flyash-laden flue-gas stream of at least one of the first or second fluid flow paths into the collector cone to form a second product group discharged from the separator at the first fluid exit means, thence while yet still containing those unburned carbon particles and other flyash not so heavy as to fall out of the flyash-laden flue-gas stream of at least one of the first or second fluid flow paths upward from the expansion chamber to the rotary classifier means whereat those unburned carbon particles and other flyash possessing sufficient velocity pass through the rotary classifier means to form a first product group discharged from the separator at the second fluid exit means and whereat those unburned carbon particles and other flyash not possessing sufficient velocity fall into the collector cone to join the second product group discharged from the separator at the first fluid exit means.

Claim 18

The method of separating unburned carbon as particulate matter from the flyash as set forth in claim 16 wherein the step of directing the flyash-laden flue-gas stream of at least one of the first or second fluid flow paths through the separator includes the step of effecting control over the mass flow rate of the flyash-laden flue-gas stream of at least one of the first or second fluid flow paths over a continuous range of mass flow rates.

Claim 19

The method of separating unburned carbon as particulate matter from the flyash as set forth in claim 17 wherein the step of directing the flyash-laden flue-gas stream of at least one of the first or second fluid flow paths through the separator includes the step of effecting control over the rotational velocity of the rotary classifier means over a continuous range of rotational velocities.

Claim 20

The method of separating unburned carbon as particulate matter from the flyash as set forth in claim 18 wherein the step of simultaneously establishing a first mass flow rate of the flyash-laden flue-gas stream of at least one of the first or second fluid flow paths and a first rotational velocity of the rotary classifier means includes the step of establishing a first mass flow rate and a first rotational velocity such that the distribution between the second product group and the first product group of the weight percentage of unburned carbon after the second separation as a function of the mass flow rate of the flyash-laden flue-gas stream of at least one of the first or second fluid flow paths is characterized by an approximately linear functional relationship according to the equation y=mx+b wherein m is approximately equal to -1.07×10 -3 and b is approximately equal to 9.5.

Claim 21

In a pulverized-coal fired steam generating power plant having a furnace volume for the combustion of pulverized-coal therein generating thereby a flue-gas stream laden with flyash, a backpass volume, a horizontal pass for conducting the flyash-laden flue-gas stream from the furnace volume to the backpass volume thence therethrough, a stack, means for conducting the flyash-laden flue-gas stream from the backpass volume to the stack thence therethrough to the atmosphere, a system for separating the unburned carbon as particulate matter from the flyash, said system comprising: a. means for effecting a separation of the flyash-laden flue-gas stream as a function of a difference in a property between a gas component of the flue-gas stream and a particle component thereof such that the gas component is more apt to flow along a first fluid flow path and the particle component is more apt to flow along a second fluid flow path, the portion of the flue-gas stream flowing along said second fluid flow path having entrained therein a quantity of flyash containing a first fraction of particles including at least unburned carbon particles and a second fraction of other particulate matter, said particles of the first fraction having a relatively higher specific gravity than the particles of the second fraction; b. means for effecting a separation of said quantity of flyash into a first product group and an interim product group as a function of the difference in the specific gravities of the first and second fractions in said quantity of flyash such that the ratio of the number of second fraction particles having relatively lower specific gravities in the interim product group to the number of second fraction particles having relatively lower specific gravities in the at least one of said first or second fractions is greater than the ratio of the number of first fraction particles having relatively higher specific gravities in the interim product group to the number of first fraction particles having relatively higher specific gravities in the at least one of said first or second fractions; and c. means for effecting a separation of the interim product group.

Claim 22

In a pulverized-coal fired steam generating power plant having a furnace volume for the combustion of pulverized-coal therein generating thereby a flue-gas stream laden with flyash, a backpass volume, a horizontal pass for conducting the flyash-laden flue-gas stream from the furnace volume to the backpass volume thence therethrough, a stack, means for conducting the flyash-laden flue-gas stream from the backpass volume to the stack thence therethrough to the atmosphere, a system for separating the unburned carbon as particulate matter from the flyash, said system comprising: a. means for effecting a separation of the flyash-laden flue-gas stream as a function of a difference in a property between a gas component of the flue-gas stream and a particle component thereof such that the gas component is more apt to flow along a first fluid flow path and the particle component is more apt to flow along a second fluid flow path, the portion of the flue-gas stream flowing along said second fluid flow path having entrained therein a quantity of flyash containing a first fraction of particles including at least unburned carbon particles and a second fraction of other particulate matter, said particles of the first fraction having a relatively higher specific gravity than the particles of the second fraction; b. means for effecting a separation of said quantity of flyash into a first product group and an interim product group as a function of the difference in the specific gravities of the first and second fractions in said quantity of flyash such that the ratio of the number of second fraction particles having relatively lower specific gravities in the interim product group to the number of second fraction particles having relatively lower specific gravities in the at least one of said first or second fractions is greater than the ratio of the number of first fraction particles having relatively higher specific gravities in the interim product group to the number of first fraction particles having relatively higher specific gravities in the at least one of said first or second fractions; and c. means for effecting a separation of the interim product group.