The present innovations relate generally to the field of producing coke from coal and more particularly to a method and apparatus for testing and evaluating the coking quality of coal in a commercial coke oven.
Coke is a key ingredient used in the manufacture of steel and other commercial applications and coke is typically produced by heating coal in a controlled atmosphere for long periods of time to drive off volatile materials and impurities from coal and convert or reduce the coal to coke. Because coal is an organic material the components of coal can vary widely and this wide variation in components results in disparate coking capabilities for coal mined from different locations. Some coal can be converted into high quality, metallurgical coke and some lack the necessary components or have too many impurities and result in a poor quality coke. Due to the wide range of coking qualities of coke, it is necessary to test the coking performance of coal and test the coking performance of various blends of coal. Unfortunately, there is an inadequate supply of testing ovens for evaluating the coking performance of coal and blends of coal and therefore, there is a need for developing some means for testing the coking performance of coal and blends of coal as part of continuously operating commercial coke oven operation. In the past, expendable, single-use containers have been used during a commercial coke oven operation in order to test the coking performance of coal samples. However, the expendable, single-use containers such as cardboard have been consumed in the extreme environment of the commercial coke oven and once the container has been consumed, or otherwise destroyed, it can be difficult to recover the sample of coal which has been at least partially converted into coke and the consumed material may leave behind ash or undesirable impurities in the converted coke.
The innovations include a method of evaluating the coking properties of coal produced in a coking oven comprising providing a certain quantity of coal to be tested and a test container intended to receive the quantity of test coal. The test container can have varying degrees of gas permeability to allow the gases and other volatiles emitted from the coal to be escape the container. The container is positioned in a coking oven along with a charge of coking coal. Ideally, the container is substantially surrounded by the coking coal, at least on the sides of the container and potentially also on the top and bottom of the container. The test coal, test container and supply of coking coal are heated in the coking oven to reduce or convert at least a portion of the test coal to coke and then the container along with the remaining supply of coking coal and coke converted therefrom are removed from the coking oven. The test container is recovered for re-use and the quantity of test coal and coke converted therefrom are recovered and removed from the test container for evaluation.
The test container is reused by positioning a second quantity of test coal in the test container and positioning the test container in a coking oven along with a charge of a second supply of coking coal. The second quantity of test coal, the testing container, and the second supply of coking coal are heated in the oven to reduce at least a portion of coal into coke. The test container and the material contained therein are removed from the oven and the second quantity of test coal is removed from the test container for evaluation. The test container can once again be repaired, if necessary, and re-used for yet another test.
The method can be modified to use a container which includes a barrier liner and/or a test container which includes thermally insulating material positioned between at least a portion of the test container and the quantity of test coal. In another modification, the supply of coking coal can be formed into a substantially solid charge before the coking operation and the test container can be positioned into a recess formed in the substantially solid charge.
Another innovation relates to the structure of a container used for evaluating the coking properties of coal in a horizontal heat recovery coking oven. This container is formed from a bottom member, a top member and at least one side member extending between the top and bottom members. The various members of the test container hold a test sample of coal which is intended to be reduced, at least in part, to coke in a coking oven. The container is designed so that it will not be consumed or destroyed during the high heat and harsh reducing environment of the coking oven and is also designed to be gas permeable so that the gases and other volatile compounds in the coal can escape during the coking operation. One of the various members of the test container is selectively moveable relative to the others so that the container can be opened and loaded with a supply of test coal and then closed to more fully contain the test coal inside the container. The various member of the container can be formed from a variety of materials including steel, ceramics, and refractory insulating materials. Various features can be integrated into the container to facilitate easy of movement of the container by machinery such as one or more loading lugs adapted for use with a crane or one or more channels adapted to receive the forks of a fork lift. While the structure of the container lends itself for use in a horizontal heat recovery coking oven, it is understood that the container can be used in any coking oven.
Referring to
The coke oven operation 12 typically includes dozens and dozens of individual coke ovens 14 processing tons of coal each day to generate coke for use in commercial operations such as steelmaking. The coke oven operation 12 typically runs continuously, immediately loading a new charge of coking coal 16 as soon as the coke oven 14 has been cleared following a coking cycle. Continuous operation of the ovens 14 allows the efficiency of using the latent heat in the coke oven 14 from one coking operation in the next cycle. Because of the relative size of the coke ovens 14, the large capital investment in such structures and the high heat required for each coking cycle, it is critically important that each coke oven 14 be run substantially continuously with minimal downtime.
Coal, the raw material used to create coke, is an organic material which can vary greatly in its properties from coal mine to coal mine. In view of these variabilities inherent in the raw material and the significant capital investment in the coke oven operations, an operator must have some means for effectively and efficiently testing the coking performance of particular coals or coal blends before committing an entire coke oven 14 or battery of ovens to converting the coal. As seen in
In order to provide for ease of transportation and movement of the test container 30, a plurality of lugs 46 can be provided on the side walls 34 or other suitable locations so that the container can be lifted by a crane or other piece of machinery. Although lugs 46 are shown, it is understood that a variety of different structures can be integrated into the test container 30 to allow securing the test container for movement such as pad-eyes, points, hooks, apertures, or the like. Channels 48 may also be mounted to the side walls 34 and/or bottom member 32 and the channels 48 can be sized to receive the forks of a conventional forklift to permit easy transportation of the test container 30. Still another design element of the test container 30 are one or more gussets 50 attached to the side walls 34 to give added strength and rigidity to the container 30 for enduring the tortuous coking operation. Similarly, skis 54 or other abrasion resistant members can be welded to the bottom member 32 to assist in the sliding movement of the test container. For example, when the test container 30 is loaded into the coke oven 14, it will likely be necessary to slide the container 30 along the bottom wall of the oven and the skis 54 can assist in this sliding action.
During the coking operation, the high heat inside the coke oven 14 drives off from the test coal impurities and other volatile materials in the form of gases and therefore, the container should provide some means for the gaseous material to escape. As seen in
By following the process outlined above, the coking oven receives substantially a full charge of conventional coking coal and therefore, the coking cycle of the oven continues to operate at substantially full commercial capacity while still allowing for the testing of the coking quality of coal blends and coal samples in a commercial environment. In order to evaluate any adverse effects of coking two different coal blends during the same coking cycle (one coal blend inside the test container 30 and a second, different coal blend loaded into the coking oven around the container) testing has shown no different coking performance resulting from this process. First, coal blend A was converted inside a test container with a different coal blend B in the coking oven and second, coal blend A was converted in the same oven under the same operating conditions and no appreciable coking properties were realized between coal blend A used in the test container as compared to coal blend A which was coked by the conventional process.
One key benefit of the test container as described herein is the fact that the container is designed and intended to be reused in at least two coal to coke conversions. Through the use of suitable materials such as the steel and ceramic materials described above along with the specific design, the container can be used for multiple coking cycles with little or no repair. This ability to reuse the test container reduces costs and waste from the testing operation.
The structure of the test container can be altered in various ways to alter the performance of the container during the coking operation.
When steel or some other metal is used to construct the test container, there can be undesirable heat transfer from the structural members of the container to the test coal. One solution to this is to provide thermally insulating materials intermediate the some or all of the members of the test container and the test coal. As seen in
The coking process depicted in
The testing method described in
As seen in
Converted coal to coke in a stamp charging operation can require slight modifications to the structure of the test container. In stamp charging operations, coals having lower quality coking performance can be mixed with higher quality coals to create a suitable blend. However, this mixing can result in a coal blend which will expand during the heating/reduction process. As seen in
Another option integrated into the test container 430 seen in
As utilized herein, the terms “approximately,” “about,” “substantially,” and similar terms are intended to have a broad meaning in harmony with the common and accepted usage by those of ordinary skill in the art to which the subject matter of this disclosure pertains. It should be understood by those of skill in the art who review this disclosure that these terms are intended to allow a description of certain features described and claimed without restricting the scope of these features to the precise numerical ranges provided. Accordingly, these terms should be interpreted as indicating that insubstantial or inconsequential modifications or alterations of the subject matter described and are considered to be within the scope of the disclosure.
It should be noted that the term “exemplary” as used herein to describe various embodiments is intended to indicate that such embodiments are possible examples, representations, and/or illustrations of possible embodiments (and such term is not intended to connote that such embodiments are necessarily extraordinary or superlative examples).
It should be noted that the orientation of various elements may differ according to other exemplary embodiments, and that such variations are intended to be encompassed by the present disclosure.
It is also important to note that the constructions and arrangements of the test container and processes described in the various exemplary embodiments are illustrative only. Although only a few embodiments have been described in detail in this disclosure, those skilled in the art who review this disclosure will readily appreciate that many modifications are possible (e.g., variations in sizes, dimensions, structures, shapes and proportions of the various elements, values of parameters, mounting arrangements, use of materials, orientations, etc.) without materially departing from the novel teachings and advantages of the subject matter recited in the claims. For example, elements shown as integrally formed may be constructed of multiple parts or elements, the position of elements may be reversed or otherwise varied, and the nature or number of discrete elements or positions may be altered or varied. The order or sequence of any process or method steps may be varied or re-sequenced according to alternative embodiments. Other substitutions, modifications, changes and omissions may also be made in the design, operating conditions and arrangement of the various exemplary embodiments without departing from the scope of the present disclosure.
Number | Name | Date | Kind |
---|---|---|---|
469868 | Osbourn | Mar 1892 | A |
1424777 | Schondeling | Aug 1922 | A |
1430027 | Plantinga | Sep 1922 | A |
1486401 | Van Ackeren | Mar 1924 | A |
1572391 | Klaiber | Feb 1926 | A |
1721813 | Geipert | Jul 1929 | A |
1818370 | Wine | Aug 1931 | A |
1848818 | Becker | Mar 1932 | A |
1955962 | Jones | Apr 1934 | A |
2394173 | Harris et al. | Feb 1946 | A |
2424012 | Bangham et al. | Jul 1947 | A |
2902991 | Whitman | Sep 1959 | A |
3462345 | Kernan | Aug 1969 | A |
3545470 | Paton | Dec 1970 | A |
3616408 | Hickam | Oct 1971 | A |
3630852 | Nashan et al. | Dec 1971 | A |
3652403 | Knappstein et al. | Mar 1972 | A |
3676305 | Cremer | Jul 1972 | A |
3709794 | Kinzler et al. | Jan 1973 | A |
3746626 | Morrison, Jr. | Jul 1973 | A |
3748235 | Pries | Jul 1973 | A |
3784034 | Thompson | Jan 1974 | A |
3806032 | Pries | Apr 1974 | A |
3836161 | Buhl | Sep 1974 | A |
3839156 | Jakobi et al. | Oct 1974 | A |
3844900 | Schulte | Oct 1974 | A |
3857758 | Mole | Dec 1974 | A |
3875016 | Schmidt-Balve et al. | Apr 1975 | A |
3876506 | Dix et al. | Apr 1975 | A |
3878053 | Hyde | Apr 1975 | A |
3897312 | Armour et al. | Jul 1975 | A |
3906992 | Leach | Sep 1975 | A |
3912091 | Thompson | Oct 1975 | A |
3917458 | Polak | Nov 1975 | A |
3930961 | Sustarsic et al. | Jan 1976 | A |
3957591 | Riecker | May 1976 | A |
3959084 | Price | May 1976 | A |
3963582 | Helm et al. | Jun 1976 | A |
3984289 | Sustarsic et al. | Oct 1976 | A |
4004702 | Szendroi | Jan 1977 | A |
4004983 | Pries | Jan 1977 | A |
4040910 | Knappstein et al. | Aug 1977 | A |
4059885 | Oldengott | Nov 1977 | A |
4067462 | Thompson | Jan 1978 | A |
4083753 | Rogers et al. | Apr 1978 | A |
4086231 | Ikio | Apr 1978 | A |
4100033 | Holter | Jul 1978 | A |
4111757 | Ciarimboli | Sep 1978 | A |
4124450 | MacDonald | Nov 1978 | A |
4141796 | Clark et al. | Feb 1979 | A |
4145195 | Knappstein et al. | Mar 1979 | A |
4147230 | Ormond et al. | Apr 1979 | A |
4189272 | Gregor et al. | Feb 1980 | A |
4194951 | Pries | Mar 1980 | A |
4196053 | Grohmann | Apr 1980 | A |
4211608 | Kwasnoski et al. | Jul 1980 | A |
4213489 | Cain | Jul 1980 | A |
4213828 | Calderon | Jul 1980 | A |
4222748 | Argo et al. | Sep 1980 | A |
4225393 | Gregor et al. | Sep 1980 | A |
4235830 | Bennett et al. | Nov 1980 | A |
4248671 | Belding | Feb 1981 | A |
4249997 | Schmitz | Feb 1981 | A |
4263099 | Porter | Apr 1981 | A |
4285772 | Kress | Aug 1981 | A |
4287024 | Thompson | Sep 1981 | A |
4289584 | Chuss et al. | Sep 1981 | A |
4289585 | Wagener et al. | Sep 1981 | A |
4303615 | Jarmell et al. | Dec 1981 | A |
4307673 | Caughey | Dec 1981 | A |
4314787 | Kwasnik et al. | Feb 1982 | A |
4330372 | Cairns et al. | May 1982 | A |
4334963 | Stog | Jun 1982 | A |
4336843 | Petty | Jun 1982 | A |
4340445 | Kucher et al. | Jul 1982 | A |
4342195 | Lo | Aug 1982 | A |
4344820 | Thompson | Aug 1982 | A |
4366029 | Bixby et al. | Dec 1982 | A |
4373244 | Mertens et al. | Feb 1983 | A |
4375388 | Hara et al. | Mar 1983 | A |
4392824 | Struck et al. | Jul 1983 | A |
4395269 | Schuler | Jul 1983 | A |
4396394 | Li et al. | Aug 1983 | A |
4396461 | Neubaum et al. | Aug 1983 | A |
4431484 | Weber et al. | Feb 1984 | A |
4439277 | Dix | Mar 1984 | A |
4445977 | Husher | May 1984 | A |
4446018 | Cerwick | May 1984 | A |
4448541 | Wirtschafter | May 1984 | A |
4452749 | Kolvek et al. | Jun 1984 | A |
4459103 | Gieskieng | Jul 1984 | A |
4469446 | Goodboy | Sep 1984 | A |
4508539 | Nakai | Apr 1985 | A |
4527488 | Lindgren | Jul 1985 | A |
4568426 | Orlando | Feb 1986 | A |
4570670 | Johnson | Feb 1986 | A |
4614567 | Stahlherm et al. | Sep 1986 | A |
4645513 | Kubota et al. | Feb 1987 | A |
4655193 | Blacket | Apr 1987 | A |
4655804 | Kercheval et al. | Apr 1987 | A |
4680167 | Orlando | Jul 1987 | A |
4704195 | Janicka et al. | Nov 1987 | A |
4720262 | Durr et al. | Jan 1988 | A |
4726465 | Kwasnik et al. | Feb 1988 | A |
4929179 | Breidenbach et al. | May 1990 | A |
4941824 | Holter et al. | Jul 1990 | A |
5052922 | Stokman et al. | Oct 1991 | A |
5062925 | Durselen et al. | Nov 1991 | A |
5078822 | Hodges et al. | Jan 1992 | A |
5114542 | Childress et al. | May 1992 | A |
5227106 | Kolvek | Jul 1993 | A |
5228955 | Westbrook, III | Jul 1993 | A |
5318671 | Pruitt | Jun 1994 | A |
5670025 | Baird | Sep 1997 | A |
5928476 | Daniels | Jul 1999 | A |
5968320 | Sprague | Oct 1999 | A |
6017214 | Sturgulewski | Jan 2000 | A |
6059932 | Sturgulewski | May 2000 | A |
6139692 | Tamura et al. | Oct 2000 | A |
6152668 | Knoch | Nov 2000 | A |
6187148 | Sturgulewski | Feb 2001 | B1 |
6189819 | Racine | Feb 2001 | B1 |
6290494 | Barkdoll | Sep 2001 | B1 |
6596128 | Westbrook | Jul 2003 | B2 |
6626984 | Taylor | Sep 2003 | B1 |
6699035 | Brooker | Mar 2004 | B2 |
6758875 | Reid et al. | Jul 2004 | B2 |
6907895 | Johnson et al. | Jun 2005 | B2 |
6946011 | Snyder | Sep 2005 | B2 |
7056390 | Fratello et al. | Jun 2006 | B2 |
7077892 | Lee | Jul 2006 | B2 |
7314060 | Chen et al. | Jan 2008 | B2 |
7331298 | Barkdoll et al. | Feb 2008 | B2 |
7497930 | Barkdoll et al. | Mar 2009 | B2 |
7611609 | Valia et al. | Nov 2009 | B1 |
7644711 | Creel | Jan 2010 | B2 |
7727307 | Winkler | Jun 2010 | B2 |
7803627 | Hodges | Sep 2010 | B2 |
7827689 | Crane et al. | Nov 2010 | B2 |
7998316 | Barkdoll | Aug 2011 | B2 |
8071060 | Ukai et al. | Dec 2011 | B2 |
8079751 | Kapila et al. | Dec 2011 | B2 |
8236142 | Westbrook | Aug 2012 | B2 |
8266853 | Bloom et al. | Sep 2012 | B2 |
8398935 | Howell, Jr. et al. | Mar 2013 | B2 |
20060102420 | Huber et al. | May 2006 | A1 |
20070205091 | Barkdoll et al. | Sep 2007 | A1 |
20080169578 | Crane et al. | Jul 2008 | A1 |
20080179165 | Chen et al. | Jul 2008 | A1 |
20080271985 | Yamasaki | Nov 2008 | A1 |
20090217576 | Kim et al. | Sep 2009 | A1 |
20090283395 | Hippe | Nov 2009 | A1 |
20100095521 | Bertini et al. | Apr 2010 | A1 |
20100115912 | Worley | May 2010 | A1 |
20100236914 | Bardkoll | Sep 2010 | A1 |
20100287871 | Bloom et al. | Nov 2010 | A1 |
20110223088 | Chang et al. | Sep 2011 | A1 |
20110253521 | Kim | Oct 2011 | A1 |
20120024688 | Barkdoll | Feb 2012 | A1 |
20120030998 | Barkdoll et al. | Feb 2012 | A1 |
20120152720 | Reichelt et al. | Jun 2012 | A1 |
20120228115 | Westbrook | Sep 2012 | A1 |
20130216717 | Rago et al. | Aug 2013 | A1 |
20140033917 | Rodgers et al. | Feb 2014 | A1 |
20140048402 | Quanci et al. | Feb 2014 | A1 |
20140048404 | Quanci et al. | Feb 2014 | A1 |
20140048405 | Quanci et al. | Feb 2014 | A1 |
20140083836 | Quanci et al. | Mar 2014 | A1 |
20140182195 | Quanci et al. | Jul 2014 | A1 |
20140182683 | Quanci et al. | Jul 2014 | A1 |
20140183023 | Quanci et al. | Jul 2014 | A1 |
20140183024 | Chun et al. | Jul 2014 | A1 |
20140183026 | Quanci et al. | Jul 2014 | A1 |
20140262139 | Choi et al. | Sep 2014 | A1 |
20140262726 | West et al. | Sep 2014 | A1 |
Number | Date | Country |
---|---|---|
2775992 | May 2011 | CA |
2064363 | Oct 1990 | CN |
1092457 | Sep 1994 | CN |
1255528 | Jun 2000 | CN |
2528771 | Feb 2002 | CN |
1358822 | Jul 2002 | CN |
1468364 | Jan 2004 | CN |
2668641 | Jan 2005 | CN |
2509188 | Nov 2011 | CN |
202226816 | May 2012 | CN |
212176 | Jul 1909 | DE |
3329367 | Feb 1921 | DE |
19545736 | Jun 1997 | DE |
19803455 | Aug 1999 | DE |
10154785 | May 2003 | DE |
2339664 | Aug 1977 | FR |
441784 | Jan 1936 | GB |
606340 | Aug 1948 | GB |
611524 | Nov 1948 | GB |
725865 | Mar 1955 | GB |
54054101 | Apr 1979 | JP |
57051786 | Mar 1982 | JP |
57051787 | Mar 1982 | JP |
57083585 | May 1982 | JP |
57090092 | Jun 1982 | JP |
58091788 | May 1983 | JP |
59051978 | Mar 1984 | JP |
59053589 | Mar 1984 | JP |
59071388 | Apr 1984 | JP |
59108083 | Jun 1984 | JP |
59145281 | Aug 1984 | JP |
60004588 | Jan 1985 | JP |
61106690 | May 1986 | JP |
62011794 | Jan 1987 | JP |
62285980 | Dec 1987 | JP |
01103694 | Apr 1989 | JP |
01249886 | Oct 1989 | JP |
H0319127 | Mar 1991 | JP |
07188668 | Jul 1995 | JP |
07216357 | Aug 1995 | JP |
08127778 | May 1996 | JP |
2001200258 | Jul 2001 | JP |
03197588 | Aug 2001 | JP |
2002106941 | Apr 2002 | JP |
2003041258 | Feb 2003 | JP |
2003071313 | Mar 2003 | JP |
04159392 | Oct 2008 | JP |
2009144121 | Jul 2009 | JP |
2012102302 | May 2012 | JP |
1019960008754 | Oct 1996 | KR |
1019990054426 | Jul 1999 | KR |
10-0797852 | Jan 2008 | KR |
1020110010452 | Feb 2011 | KR |
10-0296700 | Oct 2011 | KR |
101318388 | Oct 2013 | KR |
WO-9012074 | Oct 1990 | WO |
WO-9945083 | Sep 1999 | WO |
WO-2007103649 | Sep 2007 | WO |
WO 2008034424 | Mar 2008 | WO |
WO-2010107513 | Sep 2010 | WO |
WO 2012029979 | Mar 2012 | WO |
Entry |
---|
ASTM D5341-99(2010)e1, Standard Test Method for Measuring Coke Reactivity Index (CRI) and Coke Strength After Reaction (CSR), ASTM International, West Conshohocken, PA, 2010. |
Crelling et al., “Effects of Weathered Coal on Coking Properties and Coke Quality”, Fuel, 1979, vol. 58, Issue 7, pp. 542-546. |
Diez, et al., “Coal for Metallurgical Coke Production: Predictions of Coke Quality and Future Requirements for Cokemaking”, International Journal of Col Geology, 2002, vol. 50, Issue 1-4, pp. 389-412. |
International Search Report and Written Opinion for PCT/US2013/054737 mailed on Nov. 18, 2013, 10 pages. |
Rose, Harold J., “The Selection of Coals for the Manufacture of Coke”, American Institute of Mining and Metallurgical Engineers, Feb. 1926, 8 pages. |
Clean coke process: process development studies by USS Engineers and Consultants, Inc., Wisconsin Tech Search, request date Oct. 5, 2011, 17 pages. |
Database WPI, Week 199115, Thomson Scientific, Lond, GB; AN 1991-107552. |
JP 03-197588, Inoqu Keizo et al., Method and Equipment for Boring Degassing Hole in Coal Charge in Coke Oven, Japanese Patent (Abstract Only) Aug. 28, 1991. |
JP 04-159392, Inoue Keizo et al., Method and Equipment for Opening Hole for Degassing of Coal Charge in Coke Oven, Japanese Patent (Abstract Only) Jun. 2, 1992. |
Number | Date | Country | |
---|---|---|---|
20140061018 A1 | Mar 2014 | US |