Oxygen heat exchanger

Patent metadata

Field	Value
Publication number	US-9803860-B2
Application number	US-201213730727-A
Country	US
Kind code	B2
Filing date	Dec 28, 2012
Priority date	May 10, 2007
Publication date	Oct 31, 2017
Grant date	Oct 31, 2017

Abstract

The present invention relates to a heat exchanger for the supply of oxygen or of a gas mixture containing at least 50% oxygen, the temperature at the outlet of the exchanger not being below 300° C., it preferably being above 400° C., the oxygen or the oxygen-rich gas feeding one or more burners of a glass melting furnace, the heat of the combustion gases being used directly or indirectly to heat the oxygen or the oxygen-rich gas in the exchanger, in which the exchange power is between 20 and 300 kW, preferably between 40 and 250 kW and particularly preferably between 80 and 170 kW.

First claim

The invention claimed is:

1. A process for supplying gas to one or more burners of a glass melting furnace, comprising:
supplying combustion gases from the glass melting furnace to a first heat exchanger;
effecting a first heat exchange using the combustion gases to heat an intermediate heat transfer gas that is inert with respect to oxygen to form a heated heat transfer gas in the first heat exchanger;
supplying oxygen gas comprising oxygen or a gaseous mixture comprising at least 50% oxygen to a second heat exchanger having an outlet;
effecting a second heat exchange by heating the oxygen gas in the second heat exchanger with the heated heat transfer gas to a temperature at the outlet of the exchanger of not less than 300° C. to form heated oxygen gas;
supplying the heated oxygen gas from the outlet to one or more burners of the glass melting furnace;
generating in each burner from 1 to 6 MW in the furnace;
exchanging a power per unit area in contact with the oxygen or gas rich in oxygen in the second heat exchanger in the range of between 5 and 15 W/m 2 ,
circulating gas in the tubes carrying the oxygen gas at a rate that does not exceed 120 m/s at any point in the second heat exchanger;
exchanging power in the second heat exchanger to heat the oxygen gas in a range of between 20 and 300 kW, and
maintaining a pressure of the oxygen gas in the second heat exchanger below 3 bar,
wherein both the first and second heat exchanges are indirect heat exchanges, and
wherein surfaces of the second heat exchanger contacting the oxygen gas are polished to have a roughness that does not exceed 6 μm.

2. The process according to claim 1 , wherein each second heat exchanger supplies heated oxygen gas to at most three burners of the furnace.

3. The process according to claim 1 , further comprising:
circulating the oxygen gas in tubes in the second heat exchanger, and
contacting internal walls of the second heat exchanger with a heat transfer gas,
wherein the second heat exchanger has a tubular configuration.

4. The process according to claim 3 , in which the tubes in which the oxygen gas circulates are substantially straight and walls of the tubes have a thickness that is not more than 3 mm.

5. The process according to claim 3 , in which a chamber enclosing the tubes is formed from several elements joined by flanges, wherein tightness is assured at these flanges by composite seals, the sealing element of which is made of material that is inert with respect to oxygen.

6. The process according to claim 5 , in which the sealing element is a ring composed of compressible mineral material.

7. The process according to claim 1 , wherein a material of surfaces in contact with the oxygen gas in the second heat exchanger is made from a metal alloy of which a sample exposed to the oxygen gas does not exhibit a weight gain of more than 0.1 mg/cm 2 after 1000 cycles of exposure, wherein each cycle includes increasing the temperature of the oxygen gas to a value equal to or higher than 400° C., maintaining this phase temperature for one hour and returning to ambient temperature.

8. The process according to claim 7 , in which the alloy complies with the condition of a weight gain of less than 0.1 mg/cm 2 of exposed surface when the phase temperature is at least 500° C. in oxidising atmosphere.

9. The process according to claim 7 , in which the alloy in contact with the oxygen gas resists the spontaneous combustion test according to standard ASTM G 124 at least up to a pressure of 3 bar.

10. The process according to claim 7 , in which the alloy in contact with the oxygen gas is a ferritic steel alloy containing a percentage by weight of Cr of 12 to 30% and an Al content of 1 to 8%.

11. The process according to claim 7 , in which the alloy in contact with the oxygen gas, for an oxygen temperature not exceeding 500° C., is an alloy containing a percentage by weight of chromium in the range of between 10 and 20% by weight.

12. The process according to claim 7 , in which the alloy has a Ni content higher than 25% and a Cr content from 10 to 30%.

13. The process according to claim 12 , in which the alloy is one of those commercially available under the names “Inconel 600 H”, “600L”, “601”, “617”, “625”, “Incoloy 800H” or “800HT”.

14. The process according to claim 13 , further comprising bringing elements in the heat exchanger in contact with the oxygen gas to a temperature in the range of between 300° and 900° C.

15. The process according to claim 7 , in which the alloy complies with the condition of a weight gain of less than 0.1 mg/cm 2 of exposed surface when the phase temperature reaches at least 600° C. and the oxidising atmosphere exceeds 80% oxygen.

16. The process according to claim 7 , in which the alloy complies with the condition of a weight gain of less than 0.1 mg/cm 2 of exposed surface when the phase temperature is at least 650° C. in oxidising atmosphere.

17. The process according to claim 3 , further comprising:
placing an oxygen detector in contact with the heat transfer gas, and
connecting the oxygen detector to an alarm when the oxygen content is more than 1% higher than that of the heat transfer gas.

18. The process according to claim 1 , wherein a power exchanged in the second heat exchanger to heat the oxygen gas is in a range of between 40 and 250 kW.

19. The process according to claim 1 , wherein a power exchanged in the second heat exchanger to heat the oxygen gas is in a range of between 80 and 170 kW.

20. The process according to claim 1 , further comprising maintaining a pressure of the oxygen gas in the second heat exchanger below 2 bar.

21. The process according to claim 1 , where the heated oxygen gas at the outlet is at a temperature of not less than 400° C.

22. The process according to claim 1 , further comprising and each burner consuming heated oxygen at a rate of between 200 to 1200 Nm 3 per hour.

23. The process according to claim 1 , further comprising heating the heat transfer gas to between 450° C. and 1000° C.

24. A process for supplying gas to one or more burners of a glass melting furnace, comprising:
effecting a first heat exchange with combustion gas from the melting furnace with an intermediate heat transfer gas to form a heated heat transfer gas, wherein the heat transfer gas is formed by a gas that is inert with respect to oxygen;
passing the heated heat transfer gas to a heat exchanger having an outlet,
supplying oxygen gas comprising oxygen or a gaseous mixture comprising at least 50% oxygen to the heat exchanger;
effecting a second heat exchange by heating the oxygen gas in the heat exchanger via the heat transfer gas to a temperature at the outlet of the heat exchanger of not less than 300° C. to form heated oxygen gas;
supplying the heated oxygen gas from the outlet to one or more burners of the glass melting furnace;
each burner generating from 1 to 6 MW in the furnace,
exchanging a power per unit area in contact with the oxygen or gas rich in oxygen in the second heat exchanger in the range of between 5 and 15 W/m 2 ,
circulating gas in the tubes carrying the oxygen gas at a rate that does not exceed 120 m/s at any point in the second heat exchanger;
exchanging power in the second heat exchanger to heat the oxygen gas in a range of between 20 and 300 kW, and
maintaining a pressure of the oxygen gas in the second heat exchanger below 3 bar,
wherein both the first and second heat

Assignees

• Agc Glass Europe
• Air Liquide

Inventors

• Douxchamps Olivier
• Baudelet Eric
• Leroux Bertrand
• Constantin Gabriel
• Tsiava Remi
• Symoens Bruno

Classifications

• F28F19/00

  Preventing the formation of deposits or corrosion, e.g. by using filters {or scrapers} · CPC title

• F28F21/08

  of metal · CPC title

• F28D7/16

  the conduits being arranged in parallel spaced relation ({F28D7/0008 - F28D7/0058 take precedence}; F28D7/02 - F28D7/10 take precedence) · CPC title

• C03B5/2353 Primary

  by combustion with pure oxygen or oxygen-enriched air, e.g. using oxy-fuel burners or oxygen lances · CPC title

• F23L15/04 Primary

  Arrangements of recuperators · CPC title