Device for measuring the flow of a gas containing particulates

Claim 2

Apparatus for continuously measuring the flow of a gas containing entrained particulates, comprising: (A) a flow channel, through which the gas flows; (B) an orifice disposed within the flow channel, including at least a first surface and a second surface; (C) means for causing the first surface and second surface independently to move in directions perpendicular to lines normal to the surfaces; (D) scraping means, for intimately contacting at least a portion of the first surface and of the second surface, at all times while the surfaces are moving, whereby particulates which adhere to the first and second surfaces are removed by the movement of the surfaces past the scraping means; (E) pressure taps, positioned so as to communicate with the flow channel upstream and downstream from the orifice, the pressure taps additionally in communication with pressure-measuring means, for measuring the pressure differential in the flow channel resulting from the passage of the gas through the orifice; and (F) thermophoretic heaters, positioned so as to heat the gas within the pressure taps, and thereby excluding particulates therefrom.

Claim 3

The apparatus for continuously measuring the flow of a gas containing entrained particulates, according to claim 1, wherein the pressure-measuring means includes a diaphragm.

Claim 4

The apparatus for continuously measuring the flow of a gas containing entrained particulates, according to claim 1 wherein the pressure-measuring means includes a piezoresistive transducer.

Claim 5

The apparatus for continuously measuring the flow of a gas containing entrained particulates, according to claim 1, wherein the thermophoretic heaters maintain the temperature of the gas within the pressure taps at least about 100° F. greater than the temperature of the gas within the flow channel.

Claim 6

The apparatus for continuously measuring the flow of a gas containing entrained particulates, according to claim 1 wherein the first and second surfaces are each, independently cylindrical.

Claim 7

The apparatus for continuously measuring the flow of a gas containing entrained particulates, according to claim 1, including means to alter the size of the orifice.

Claim 8

The apparatus for continuously measuring the flow of a gas containing entrained particulates, according to claim 1, wherein the scraping means includes polytetrafluoroethylene scrapers urged into intimate contact with the first and second surfaces by compressed springs.

Claim 9

The apparatus for continuously measuring the flow of a gas containing entrained particulates, according to claim 1, wherein the means for causing the first and second surfaces to move includes a motor drive.

Claim 10

Apparatus for continuously measuring the flow of a gas containing entrained particulates, comprising: (A) a flow channel, through which the gas flows; (B) an orifice disposed within the flow channel, including at least a first cylindrical surface and a second cylindrical surface; (C) means for causing the first cylindrical surface and second cylindrical surface, independently to rotate about the axes of the surfaces; (D) scraping means, for intimately contacting at least a portion of the first cylindrical surface and of the second cylindrical surface at all times while the surfaces are rotating, whereby particulates which adhere to the first and second cylindrical surfaces are removed by the rotation of the surfaces past the scraping means; (E) pressure taps, positioned so as to communicate with the flow channel upstream and downstream from the orifice, the pressure taps additionally in communication with pressure-measuring means, for measuring the pressure differential in the flow channel resulting from the passage of the gas through the orifice; and (F) thermophoretic heaters, positioned so as to heat the gas within the pressure taps to a temperature at least about 100° F. greater than the temperature of the flow channel, thereby excluding particulates therefrom.

Claim 11

Apparatus for continuously measuring the flow of a gas containing entrained particulates, comprising: (A) a flow channel, through which the gas flows; (B) an orifice disposed within the flow channel, including at least a first cylindrical surface and a second cylindrical surface; (C) means for causing the first cylindrical surface and second cylindrical surface, independently to rotate about the axes of the surfaces; (D) scraping means, for intimately contacting at least a portion of the first cylindrical surface and of the second cylindrical surface at all times while the surfaces are rotating, whereby particulates which adhere to the first and second cylindrical surfaces are removed by the rotation of the surfaces past the scraping means; (E) pressure taps, positioned so as to communicate with the flow channel upstream and downstream from the orifice, the pressure taps additionally in communication with pressure-measuring means, for measuring the pressure differential in the flow channel resulting from the passage of the gas through the orifice; and (F) thermophoretic heaters, positioned so as to heat the gas within the pressure taps to a temperature at least about 100° F. greater than the temperature of the flow channel, thereby excluding particulates therefrom.

Claim 12

The apparatus for continuously measuring the flow of a gas containing entrained particulates, according to claim 9, wherein the pressure measuring means includes a diaphragm.

Claim 13

The apparatus for continuously measuring the flow of a gas containing entrained particulates, according to claim 9, wherein the pressure-measuring means includes a piezoresistive transducer.

Claim 14

The apparatus for continuously measuring the flow of a gas containing entrained particulates, according to claim 9, including means to alter the size of the orifice.

Claim 15

The apparatus for continuously measuring the flow of a gas containing entrained particulates, according to claim 9, wherein the scraping means includes polytetrafluoroethylene scrapers urged into intimate contact with the first and second cylindrical surfaces by compressed springs.

Claim 16

The apparatus for continuously measuring the flow of a gas containing entrained particulates, according to claim 9, wherein the means for causing the first and second cylindrical surfaces to rotate includes a motor drive.

Claim 17

Apparatus for continuously measuring the flow of a gas containing entrained particulates, comprising: (A) a flow channel, through which the gas flows; (B) an orifice disposed within the flow channel, including at least a first cylindrical surface and a second cylindrical surface; (C) means for altering the size of the orifice; (D) means for causing the first cylindrical surface and second cylindrical surface independently to rotate about the axes of the surfaces, including a motor drive; (E) scraping means, for intimately contacting at least a portion of the first cylindrical surface and of the second cylindrical surface, at all times while the surfaces are rotating, including polytetrafluoroethylene scrapers urged into intimate contact with the first and second cylindrical surfaces by compressed springs, whereby particulates which adhere to the first and second cylindrical surfaces are removed by the rotation of the cylindrical surfaces past the scraping means; (F) pressure taps, positioned so as to communicate with the flow channel upstream and downstream from the orifice, the pressure taps additionally in communication with pressure-measuring means, for measuring the Pressure differential in the flow channel resulting from the passage of the gas through the orifice; and (G) thermophoretic heaters, positioned so as to heat the gas within the pressure taps to a temperature at least about 100° F. greater than the temperature of the gas within the flow channel, thereby excluding particulates therefrom.

Claim 18

Apparatus for continuously measuring the flow of a gas containing entrained particulates, comprising: (A) a flow channel, through which the gas flows; (B) an orifice disposed within the flow channel, including at least a first cylindrical surface and a second cylindrical surface; (C) means for altering the size of the orifice; (D) means for causing the first cylindrical surface and second cylindrical surface independently to rotate about the axes of the surfaces, including a motor drive; (E) scraping means, for intimately contacting at least a portion of the first cylindrical surface and of the second cylindrical surface, at all times while the surfaces are rotating, including polytetrafluoroethylene scrapers urged into intimate contact with the first and second cylindrical surfaces by compressed springs, whereby particulates which adhere to the first and second cylindrical surfaces are removed by the rotation of the cylindrical surfaces past the scraping means; (F) pressure taps, positioned so as to communicate with the flow channel upstream and downstream from the orifice, the pressure taps additionally in communication with pressure-measuring means, for measuring the Pressure differential in the flow channel resulting from the passage of the gas through the orifice; and (G) thermophoretic heaters, positioned so as to heat the gas within the pressure taps to a temperature at least about 100° F. greater than the temperature of the gas within the flow channel, thereby excluding particulates therefrom.

Claim 19

The apparatus for continuously measuring the flow of a gas containing entrained particulates, according to claim 15, wherein the pressure-measuring means includes a diaphragm.

Claim 20

The apparatus for continuously measuring the flow of a gas containing entrained particulates, according to claim 15, wherein the pressure-measuring means includes a piezoresistive transducer.