Process for producing glass microspheres

Claim 2

A process for producing hollow microspheres from particles of soda-lime-silica glass containing between about 0.01 and 0.05 weight precent sulfur in the form of sulfate compounds comprising: (a) passing the particles in a reducing atmosphere through a burner for treatment at a temperature at least about 100° C. above the normal working temperature at which said glass is manufactured but below about 1750° C.; and (b) forming hollow microspheres by reducing the sulfates to sulfur dioxide gas which is insoluble in the glass and which causes expansion of the particles.

Claim 3

A process as in claim 1, wherein the treatment temperature is at least about 1500° C.

Claim 4

A process as in claim 2, wherein the treatment temperature is about 1550°-1700° C.

Claim 5

A process as in claim 1, wherein the treatment temperature is less than about 1700° C.

Claim 6

A process for producing hollow microspheres from particles of soda-lime-silica glass containing between about 0.01 and 0.5 weight percent sulfur in the form of sulfate compounds comprising: (a) passing the particles in a reducing atmosphere through a burner for treatment at a temperature at least about 100° C. above the normal working temperature at which said glass is manufactured but below about 1750° C.; (b) maintaining said particles at the treatment temperature for less than about 0.1 second; (c) forming hollow microspheres by reducing the sulfates to sulfur dioxide gas which is insoluble in the glass and which causes expansion of the particles; and (d) solidifying the hollow microspheres by sudden cooling.

Claim 7

A process for producing hollow microspheres from particles of soda-lime-silica glass containing between about 0.01 and 0.5 weight percent sulfur in the form of sulfate compounds comprising: (a) passing the particles in a reducing atmosphere through a burner for treatment at a temperature at least about 100° C. above the normal working temperature at which said glass is manufactured but below about 1750° C.; (b) maintaining said particles at the treatment temperature for less than about 0.1 second; (c) forming hollow microspheres by reducing the sulfates to sulfur dioxide gas which is insoluble in the glass and which causes expansion of the particles; and (d) solidifying the hollow microspheres by sudden cooling.

Claim 8

A process as in claim 5, wherein said particles are cooled to below about 1000° C.

Claim 9

A process as in claim 6, wherein said particles are cooled to below about 750° C.

Claim 10

A process as in claim 5, wherein said particles are maintained at the treatment temperature for less than about 0.05 sec.

Claim 11

A process as in claim 5, wherein said particles are less than about 20 microns in size before treatment, and are maintained at the treatment temperature for less than about 0.02 sec.

Claim 12

A process as in claim 1, further comprising (a) operating the burner with a mixture of air and fuel gas fed into the burner such that the air factor (the ratio of the amount of air introduced into the burner to the amount of air necessary to produce stoichiometric combustion) is less than about 1.1.

Claim 13

A process as in claim 10, wherein the air factor is less than about 1.05.

Claim 14

A process as in claim 11, wherein the air factor is greater than about 0.75.

Claim 15

A process as in claim 12, wherein the air factor is between about 0.8 and 0.95.

Claim 16

A process as in claim 10, wherein the air factor is greater than about 0.75.

Claim 17

A process as in claim 1, further comprising (a) operating the burner with a mixture of air and fuel gas fed into the burner with an air factor (the ratio of the amount of air introduced into the burner to the amount of air necessary to produce stoichiometric combustion) selected such that the instantaneous level of hydrogen released by cracking of the fuel is less than about 4% of the gases in the burner.

Claim 18

A process as in claim 15, wherein said instantaneous level of hydrogen is less than about 3%.

Claim 19

A process for producing hollow microspheres from particles of soda-lime-silica glass containing between about 0.01 and 0.5 weight percent sulfur in the form of sulfate compounds comprising: (a) passing the particles through a burner for treatment at a temperature at least 100° C. above the normal working temperature at which said glass is manufactured but below about 1750° C.; and (b) feeding fuel gas and oxidizing gas into the path of the particles through the burner such that the particles pass first through a first zone having a reducing atmosphere and then through a second zone having a non-reducing atmosphere; wherein the reducing atmosphere causes the sulfate compounds to decompose to sulfur dioxide which is insoluble in the glass and causes expansion of the particles and formation of hollow microspheres.

Claim 20

A process for producing hollow microspheres from particles of soda-lime-silica glass containing between about 0.01 and 0.5 weight percent sulfur in the form of sulfate compounds comprising: (a) passing the particles through a burner for treatment at a temperature at least 100° C. above the normal working temperature at which said glass is manufactured but below about 1750° C.; and (b) feeding fuel gas and oxidizing gas into the path of the particles through the burner such that the particles pass first through a first zone having a reducing atmosphere and then through a second zone having a non-reducing atmosphere; wherein the reducing atmosphere causes the sulfate compounds to decompose to sulfur dioxide which is insoluble in the glass and causes expansion of the particles and formation of hollow microspheres.

Claim 21

A process as in claim 17, wherein said second zone has a neutral atmosphere.

Claim 22

A process as in claim 17, wherein said second zone has a slightly oxidizing atmosphere.

Claim 23

A process as in claim 1, wherein the average size of the particles treated is about 7-50 microns.

Claim 24

A process as in claim 20, wherein the average size of the particles treated is less than about 10 microns.

Claim 25

A process as in claim 1, wherein the sulfur content by weight in said glass is less than about 0.1%.

Claim 26

A process as in claim 22, wherein said sulfur content is greater than about 0.01%.

Claim 27

A process for producing hollow microspheres from particles of soda-lime-silica glass containing between about 0.01 and 0.5 weight percent sulfur in the form of sulfate compounds, comprising: (a) passing the particles through a burner for treatment at a temperature at least about 100° C. above the normal working temperature at which said glass is manufactured but below about 1750° C.; (b) operating the burner with a mixture of air and fuel gas fed into the burner such that the air factor is less than about 1.1; (c) maintaining said particles at the treatment temperature for less than about 0.1 second; (d) forming micropheres by reducing the sulfates to sulfur dioxide gas which is insoluble in the glass and which causes expansion of the particles; and (e) solidifying the hollow microspheres by sudden cooling to a temperature of between about 750° and 1000° C.

Claim 28

A process for producing hollow microspheres from particles of soda-lime-silica glass containing between about 0.01 and 0.5 weight percent sulfur in the form of sulfate compounds, comprising: (a) passing the particles through a burner for treatment at a temperature at least about 100° C. above the normal working temperature at which said glass is manufactured but below about 1750° C.; (b) operating the burner with a mixture of air and fuel gas fed into the burner such that the air factor is less than about 1.1; (c) maintaining said particles at the treatment temperature for less than about 0.1 second; (d) forming micropheres by reducing the sulfates to sulfur dioxide gas which is insoluble in the glass and which causes expansion of the particles; and (e) solidifying the hollow microspheres by sudden cooling to a temperature of between about 750° and 1000° C.

Claim 29

A process as in claim 24, further comprising (a) feeding fuel gas and oxidizing gas into the path of the particles through the burner such that the particles pass first through a first zone with a reducing atmosphere and then through a second zone with a non-reducing atmosphere.

Claim 30

A process as in claim 24 or claim 25, wherein the treatment temperature is about 1550°-1700° C., and the burner is operated with an air factor of about 0.8-0.95.

Claim 31

A process as in claim 26, wherein the particles are maintained at the treatment temperature for less than about 0.05 second, and the particles are solidified by sudden cooling to below about 750° C.

Claim 32

A process for producing hollow microspheres from particles of soda-lime-silica glass containing between about 0.01 and 0.5 weight percent sulfur in the form of sulfate compounds comprising: (a) passing the particles through a burner for treatment at a temperature of at least about 100° C. above the normal working temperature at which said glass is manufactured and above at least about 1500° C. but below about 1700° C.; (b) operating the burner with a mixture of air and fuel gas fed into the burner such that the air factor is between about 0.75 and 1.1 and such that the instantaneous level of hydrogen released by cracking of the fuel is less than about 4% of the gases in the burner; (c) feeding fuel gas and oxidizing gas into the path of the particles through the burner such that the particles pass first through a first zone having a reducing atmosphere and then through a second zone having a non-reducing atmosphere; (d) maintaining said particles at the treatment temperature for less than about 0.1 second; (e) forming micropheres by reducing the sulfates to sulfur dioxide gas which is insoluble in the glass and which causes expansion of the particles; and (f) solidifying the particles by sudden cooling to a temperature of about 750° to 1000° C.

Claim 33

A process for producing hollow microspheres from particles of soda-lime-silica glass containing between about 0.01 and 0.5 weight percent sulfur in the form of sulfate compounds comprising: (a) passing the particles through a burner for treatment at a temperature of at least about 100° C. above the normal working temperature at which said glass is manufactured and above at least about 1500° C. but below about 1700° C.; (b) operating the burner with a mixture of air and fuel gas fed into the burner such that the air factor is between about 0.75 and 1.1 and such that the instantaneous level of hydrogen released by cracking of the fuel is less than about 4% of the gases in the burner; (c) feeding fuel gas and oxidizing gas into the path of the particles through the burner such that the particles pass first through a first zone having a reducing atmosphere and then through a second zone having a non-reducing atmosphere; (d) maintaining said particles at the treatment temperature for less than about 0.1 second; (e) forming micropheres by reducing the sulfates to sulfur dioxide gas which is insoluble in the glass and which causes expansion of the particles; and (f) solidifying the particles by sudden cooling to a temperature of about 750° to 1000° C.

Claim 34

A process for producing hollow microspheres from parties of soda-line-silica glass containing between 0.01 and 0.5 weight percent sulfur in the form of sulfate compounds which comprises: heating the particles in a reducing atmosphere by passing the particles through a burner at a sufficient temperature and for a sufficient time to decompose the sulfate compounds to sulfur dioxide and cause formation of hollow microspheres; and rapidly cooling the microspheres to retain their shape.

Claim 35

A process for producing hollow microspheres from parties of soda-line-silica glass containing between 0.01 and 0.5 weight percent sulfur in the form of sulfate compounds which comprises: heating the particles in a reducing atmosphere by passing the particles through a burner at a sufficient temperature and for a sufficient time to decompose the sulfate compounds to sulfur dioxide and cause formation of hollow microspheres; and rapidly cooling the microspheres to retain their shape.

Claim 36

The method of claim 29 wherein the particles are heated at a temperature range of at least about 100° C. above the normal working temperature at which said glass is manufactured but below about 1750° C.

Claim 37

The method of claim 29 wherein the particles are heated for less than 0.01 second.

Claim 38

The method of claim 29 wherein the microspheres are rapidly cooled to a temperature of between 750° and 1000° C.

Claim 39

The method of claim 29 wherein the particles pass through a zone of a neutral or oxidizing atmosphere before being rapidly cooled.

Claim 40

The method of claim 29 wherein the burner is operated with an air factor of between 0.75 and 1.1.