Indirect determination of the waste gas rate for metallurgical process

Information

  • Patent Grant
  • 8353194
  • Patent Number
    8,353,194
  • Date Filed
    Friday, August 8, 2008
    16 years ago
  • Date Issued
    Tuesday, January 15, 2013
    11 years ago
Abstract
A method for the indirect determination of the waste gas rate in metallurgical processes. A reference gas such as helium is first added to the waste gas, specifically at a time which, with respect to flow, sufficiently precedes the taking of a sample such that a thorough mixing of the reference gas and waste gas is carried out, i.e., a virtually homogeneous distribution is achieved, and a quantitative helium analysis and nitrogen analysis of the waste gas, measured by a mass spectrometer, is carried out while taking into account the added amount of helium.
Description
PRIORITY CLAIM

This is a U.S. national stage of application No. PCT/DE2008/001336, filed on Aug. 8, 2008, which claims Priority to the German Application No.: 10 2007 044 568.9, filed: Sep. 7, 2007, the contents of both being incorporated herein by reference.


BACKGROUND OF THE INVENTION

1. Field of the Invention


The invention relates to the indirect determination of the waste gas rate or waste gas flow rate in metallurgical processes.


2. Prior Art


Information about the waste gas, its time-dependent composition and/or amount, is important for controlling metallurgical processes.


PCT/EP2005/006848 discloses a method for noncontacting waste gas measurement, particularly at a converter, wherein a segment of the waste gas volume is measured by means of an FTIR spectrometer.


In another method known from DE 28 39 316, a mass-spectrometric monitoring of a sample is carried out on the ionization currents for selected peaks relating to CO, CO2, N2 and a reference gas in the sample. The reference gas can be helium, for example.


SUMMARY OF THE INVENTION

It is an object of the invention to provide a method by which the waste gas rate in metallurgical processes can be indicated more precisely.


According to one embodiment of the invention, a reference gas such as helium is first added to the waste gas, specifically at a time which, with respect to flow, sufficiently precedes the taking of a sample such that a thorough mixing of the reference gas and waste gas is carried out, i.e., a virtually homogeneous distribution is achieved.


The indirect determination of the waste gas rate based on helium then consists in the helium analysis and nitrogen analysis of the waste gas measured by a mass spectrometer while taking into account the added amount of helium.


Combining the two affords the possibility of calculating the waste gas rate by the following formula:











Q
W

=



1
He



Q
HeB


+



He
Air

He



Q
L




,




(
1
)








where:


QW is the calculated waste gas rate Nm3/min;


QHeB is the measured helium flow rate Nm3/min;


QL is the calculated infiltrated air Nm3/min;


He is the measured helium concentration in the waste gas (−); and


HeAir is the measured concentration in the air (−), corresponding to 5.2 ppm.


The infiltrated air can be determined by the following formula:











Q
L

=





N
2

He



N

2

Air


-



N
2

He



He
Air






Q
HeB


-


1


N

2

Air


-



N
2

He



He
Air






Q

N





2

S





,




(
2
)







where






Q

N





2

S



=


Q

N





2

B


+

Q

N





2

Steel







(
3
)








and


N2, He is the measured waste gas nitrogen, helium concentration;


N2Air, HeAir is the nitrogen, helium concentration in the air corresponding in absolute values to 0.78 and 5.2 E-4;


QN2S is the source nitrogen quantity Nm3/min;


QN2B is the measured nitrogen rate (process gas) Nm3/min; and


QN2Steel is the calculated nitrogen rate as degassing product Nm3/min.


When formulas (2) and (3) are inserted into formula (1), the waste gas rate can be put into the following form:










Q
W

=



1

He
-



N
2


N

2

Air





He
Air






Q
HeB


-


1


He



N

2

Air



He
Air



-

N
2





(


Q
N2B

+

Q
N2Steel


)







(
4
)







The negative component of the formula describes the effect of the oxygen (QN2B) blown into the liquid steel in case of a special steel treatment and the nitrogen rate in the degassing (QN2Steel) of the liquid steel on the globally calculated waste gas rate.


Under normal circumstances, argon is used as stirring gas or inert gas so that only the amount of nitrogen occurring during degassing has theoretical significance for the accuracy of the waste gas flow rate calculation. Since this is very low compared to the global waste gas rate, it can be ignored.


Waste gas rate determined by a measuring unit (mass spectrometer) in Nm3/min: Simplified formula:










Q
W

=


1

He
-


He
Air




N
2


N

2

Air








Q
HeB






(
5
)







Estimation of the necessary minimum helium concentration in the waste gas at which a carbon balance can be achieved with an accuracy of +/−(0.005-0.007%):

    • Approximately 100×HeAir





BRIEF DESCRIPTION OF THE DRAWINGS


FIG. 1 is a schematic representation of a system for the indirect determination of waste gas rate according to one embodiment of the present invention.





DETAILED DESCRIPTION OF THE DRAWINGS


FIG. 1 is the measurement system described above applied in the control of a metallurgical process, specifically by way of the example of a Vacuum Oxygen Decarburization (VOD) process. Only the parts necessary for understanding the invention are shown in the drawing.


Helium from another source is injected into the waste gas flow. The amount is adjusted corresponding to the waste gas pressure. The helium source, the waste gas pressure gauge, and the helium flow regulator are preferably arranged and shown in FIG. 1.


The corresponding value for the added amount of helium is acquired by the measuring unit and is used for the calculation.


A sample is then removed from the waste gas flow and supplied to the measurement station.


The waste gas flow rate QW is then determined according to the formula described above from the flow rate QHeB, the gas concentration X %, the quantity of N2 process gas QN2B, and taking into account the quantity of N2 reaction gas QN2steel if required for measuring accuracy.


Thus, while there have shown and described and pointed out fundamental novel features of the invention as applied to a preferred embodiment thereof, it will be understood that various omissions and substitutions and changes in the form and details of the devices illustrated, and in their operation, may be made by those skilled in the art without departing from the spirit of the invention. For example, it is expressly intended that all combinations of those elements and/or method steps which perform substantially the same function in substantially the same way to achieve the same results are within the scope of the invention. Moreover, it should be recognized that structures and/or elements and/or method steps shown and/or described in connection with any disclosed form or embodiment of the invention may be incorporated in any other disclosed or described or suggested form or embodiment as a general matter of design choice. It is the intention, therefore, to be limited only as indicated by the scope of the claims appended hereto.

Claims
  • 1. A method for the indirect determination of a waste gas rate of a waste gas in a metallurgical process, comprising: adding helium as a reference gas to the waste gas;measuring a helium flow rate;mixing the reference gas and the waste gas such that a substantially homogeneous distribution is achieved;taking a sample of the mixed reference gas and waste gas; andanalyzing the sample by a mass spectrometer to perform a reference gas analysis and nitrogen analysis of the waste gas, while taking into account the added amount of the reference gas, wherein the waste gas rate is determined by the formula:
  • 2. The method according to claim 1, wherein adding the reference gas further comprises regulating a flow rate of the helium at a helium gas source.
  • 3. The method according to claim 1, further comprising determining concentrations of O2, CO, CO2, Ar, and H2 in the sample gas by mass spectrometry.
Priority Claims (1)
Number Date Country Kind
10 2007 044 568 Sep 2007 DE national
PCT Information
Filing Document Filing Date Country Kind 371c Date
PCT/DE2008/001336 8/8/2008 WO 00 3/2/2010
Publishing Document Publishing Date Country Kind
WO2009/030192 3/12/2009 WO A
US Referenced Citations (11)
Number Name Date Kind
3188180 Holler Jun 1965 A
3400585 Kraus et al. Sep 1968 A
3520657 Frumerman Jul 1970 A
3522035 Putman Jul 1970 A
3934470 Amati et al. Jan 1976 A
4040789 Voss et al. Aug 1977 A
4251269 Hoshi et al. Feb 1981 A
4251270 Hoshi et al. Feb 1981 A
4273312 Phillips et al. Jun 1981 A
4305906 Mikasa et al. Dec 1981 A
5518931 Plessers May 1996 A
Foreign Referenced Citations (2)
Number Date Country
28 39 316 Mar 1979 DE
EP2005006848 Feb 2006 WO
Related Publications (1)
Number Date Country
20100192672 A1 Aug 2010 US