US3190745A - Method of improving blast furnace performance using raw petroleum coke - Google Patents
Method of improving blast furnace performance using raw petroleum coke Download PDFInfo
- Publication number
- US3190745A US3190745A US224232A US22423262A US3190745A US 3190745 A US3190745 A US 3190745A US 224232 A US224232 A US 224232A US 22423262 A US22423262 A US 22423262A US 3190745 A US3190745 A US 3190745A
- Authority
- US
- United States
- Prior art keywords
- furnace
- petroleum coke
- coke
- raw petroleum
- blast furnace
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000002006 petroleum coke Substances 0.000 title claims description 17
- 238000000034 method Methods 0.000 title claims description 6
- 239000000571 coke Substances 0.000 description 13
- 239000002893 slag Substances 0.000 description 9
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 239000007789 gas Substances 0.000 description 6
- 239000002184 metal Substances 0.000 description 6
- 229910052751 metal Inorganic materials 0.000 description 6
- 239000002245 particle Substances 0.000 description 5
- 235000019738 Limestone Nutrition 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 239000006028 limestone Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000011800 void material Substances 0.000 description 2
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- 206010039509 Scab Diseases 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000005422 blasting Methods 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 238000001000 micrograph Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 230000000306 recurrent effect Effects 0.000 description 1
- 238000011946 reduction process Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 235000002639 sodium chloride Nutrition 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 239000004449 solid propellant Substances 0.000 description 1
- 239000011345 viscous material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B5/00—Making pig-iron in the blast furnace
- C21B5/007—Conditions of the cokes or characterised by the cokes used
Definitions
- blast furnaces may be considered as having five parts: (1) the bottom, (2) the hearth, (3) the bosh, (4) the stack, and (5) the furnace top.
- Raw materials including the burden are charged through the top of the furnace.
- the burden or ore to be reduced may consist of raw screened and'blended ores,
- the coke is consumed or gasified by means of a preheated blast of air which is forced into the furnace under pressure through tuyeres at the top of the hearth.
- This gasification of carbon supplies the necessary reducing gases and heat to promote the chemical reactions of reduction and also melt the iron and slag formed.
- the preheated hot blast may range in temperatures from about 1000" to over 1800 F. subject to limitations of heating capacity and refractory linings used.
- the blast may be modified or enriched with oxygen; steam; and gaseous, liquid, or solid fuels.
- this hanging is characterized by rapidly increasing blast pressures and lack of movement of the burden in the upper reaches of the stock column. Initially this hanging may be caused by several conditions, either singly or in combination, such as:
- Fused slag may resolidify
- Coke and burden fines may plug the void space and cause both arching of the solid material and resistance to flow of the gases;
- Redeposited carbon from the reaction may fill the voids between particles of ore and thus impervious masses.
- the quantity of blast has been reduced in order to lower its buoyant effect, with the result that the weight of the material above the scaffolding incrustation is sometimes able to break the incrustation.
- This is referred to as a bosh slip.
- the incrustation can be removed'by the use of quartzSi0 addition which acts on the deposits like rocksalt on ice. 'Sometimes extra metallurgical or foundry coke over the amount normally used has been, added and found to be helpful. In extreme cases a number of holes may be drilled at various levels of the furnace to blast or dynamite out the incrustation or bridges, etc.
- An additional complicating factor in blast furnace operation is that the blast furnace operator must think about 8 to 10 hours ahead of the furnace because any burden or charge change will require that time to travel through the furnace and reach the hearth where its effect will be mainly manifested.
- raw petroleum coke has low ash content (typically about 0.3% as compared to 7-14% ash, for normal furnace coke), upon burning, it contrib utes very little if any to slag build-up as does normal furnace coke upon burning. Further it permits a limestone burden adjustment which forms a more nearly finished slag in the bosh or primary melting zone.
- EXAMPLE 1 A blast furnace having a hearth 23 feet in diameter and a working volume of 28,000 cubic feet was sick" or cold for months, had an in-wall temperature fifteen feet above the bosh of 900-l000 F., and was producing only about 150 tons of hot metal per day. Thirty-two tons of raw petroleum coke, having a volatile content of 12.5% and a particle size of 100% 4 inch mesh and approximately 50% inch mesh, was charged through the top of said furnace and added to the normal furnace charge already therein. Within 48 hours the in-wall temperatures 15 feet above the bosh had increased by about 100-400 F. to 1000-1300 F., 1100 F. average. After this 48 hours, thirty-two more tons of the same raw petroleum coke were charged into the furnace in the same manner.
- the raw petroleum coke employed in this invention is typically of the type produced from a delayed coker system and generally will have a volatile matter content between about 8 and about 15% with about 12 to 14% being typical. It is preferable also that a substantial proportion of the raw petroleum coke employed be not too large nor too fine. Raw petroleum coke particles which are retained on a inch screen and which pass through a inch screen are typical of preferred particle sizes, but this should not be interpreted as precluding the use of minor percentages of raw petroleum coke coarser than 5 inches or finer than inch. The ash content of the raw petroleum coke is preferably no higher than about one percent.
- the invention although most applicable to blast furnaces, can be applied to any shaft furnace, such as hot blast basic cupolas, in which incrustation or build-up of viscous material along the in-walls is a problem.
- a method of assisting in restoring a shaft furnace to normal operating temperature after the temperature of said furnace has been reduced below said normal operating'temperature because of scaffolding which comprises adding to the shaft furnace as extra coke, raw petroleum coke, having a volatile matter content between about 8% and about 15% and an ash content less than about 1%, in an amount sufficient to increase said reduced operating temperature toward said normal operating temperature.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture Of Iron (AREA)
- Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
- Vertical, Hearth, Or Arc Furnaces (AREA)
Priority Applications (8)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| NL297825D NL297825A (oth) | 1962-09-17 | ||
| NL129094D NL129094C (oth) | 1962-09-17 | ||
| US224232A US3190745A (en) | 1962-09-17 | 1962-09-17 | Method of improving blast furnace performance using raw petroleum coke |
| GB31866/63A GB999351A (en) | 1962-09-17 | 1963-08-13 | Method of improving blast or cupola furnace performance |
| DEG38470A DE1212567B (de) | 1962-09-17 | 1963-08-14 | Verfahren zur Normalisierung des Ofenganges eines Schachtofens |
| FR945573A FR1367299A (fr) | 1962-09-17 | 1963-08-23 | Procédé pour améliorer le rendement des hauts fourneaux |
| LU44327D LU44327A1 (oth) | 1962-09-17 | 1963-08-26 | |
| JP38045276A JPS5010801B1 (oth) | 1962-09-17 | 1963-08-28 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US224232A US3190745A (en) | 1962-09-17 | 1962-09-17 | Method of improving blast furnace performance using raw petroleum coke |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3190745A true US3190745A (en) | 1965-06-22 |
Family
ID=22839798
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US224232A Expired - Lifetime US3190745A (en) | 1962-09-17 | 1962-09-17 | Method of improving blast furnace performance using raw petroleum coke |
Country Status (3)
| Country | Link |
|---|---|
| US (1) | US3190745A (oth) |
| JP (1) | JPS5010801B1 (oth) |
| GB (1) | GB999351A (oth) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3770418A (en) * | 1968-03-04 | 1973-11-06 | T Wilde | Method of melting iron with lumps of carbon coke |
| US4144053A (en) * | 1976-11-03 | 1979-03-13 | Republic Steel Corporation | Processes for blast furnace operations |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2184318A (en) * | 1934-11-15 | 1939-12-26 | Ruzicka Stevan | Process for simultaneous production of alumina cement and pig iron in blast furnaces |
| US3058821A (en) * | 1960-02-18 | 1962-10-16 | Great Lakes Carbon Corp | Manufacture of coke |
-
1962
- 1962-09-17 US US224232A patent/US3190745A/en not_active Expired - Lifetime
-
1963
- 1963-08-13 GB GB31866/63A patent/GB999351A/en not_active Expired
- 1963-08-28 JP JP38045276A patent/JPS5010801B1/ja active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2184318A (en) * | 1934-11-15 | 1939-12-26 | Ruzicka Stevan | Process for simultaneous production of alumina cement and pig iron in blast furnaces |
| US3058821A (en) * | 1960-02-18 | 1962-10-16 | Great Lakes Carbon Corp | Manufacture of coke |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3770418A (en) * | 1968-03-04 | 1973-11-06 | T Wilde | Method of melting iron with lumps of carbon coke |
| US4144053A (en) * | 1976-11-03 | 1979-03-13 | Republic Steel Corporation | Processes for blast furnace operations |
Also Published As
| Publication number | Publication date |
|---|---|
| GB999351A (en) | 1965-07-21 |
| JPS5010801B1 (oth) | 1975-04-24 |
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