Semi-soft Coking Coal<\/h2><\/div><\/div><\/div>
\n<\/span><\/span><\/div><\/p><\/div>![\"Semi-soft](\"https:\/\/www.inrl.in\/wp-content\/uploads\/2019\/03\/RB3-300x160.jpg\" "\\"Semi-soft")
i-Energy is a supplier of this main category of metallurgical- semi-soft coking coal which produces coke of lesser quality. Semi-soft coal normally have lower sales values compared to hard coking coal due to the relative availability of these products. Integrated steel mills will optimize the use of semi-soft coal in order to reduce overall costs.<\/p>\n<\/div><\/section><\/div>
\n\n\nProximate and other analysis<\/td>\n \u00a0As received<\/td>\n Air Dried<\/td>\n Dry<\/td>\n Dry ash free<\/td>\n<\/tr>\n \nTotal Moisture<\/td>\n %<\/td>\n 10<\/td>\n <\/td>\n <\/td>\n <\/td>\n<\/tr>\n \nAs Analysed Moisture<\/td>\n %<\/td>\n <\/td>\n 1<\/td>\n <\/td>\n <\/td>\n<\/tr>\n \nAsh<\/td>\n %<\/td>\n 8.6<\/td>\n 9.5<\/td>\n 9.6<\/td>\n <\/td>\n<\/tr>\n \nVolatile Matter<\/td>\n %<\/td>\n 21.4<\/td>\n 23.5<\/td>\n 23.7<\/td>\n 26.3<\/td>\n<\/tr>\n \nFixed Carbon<\/td>\n %<\/td>\n 60<\/td>\n 66<\/td>\n 66.7<\/td>\n 73.7<\/td>\n<\/tr>\n \nTotal Sulphur<\/td>\n %<\/td>\n 0.41<\/td>\n 0.45<\/td>\n 0.45<\/td>\n 0.5<\/td>\n<\/tr>\n \nPhosphorus<\/td>\n %<\/td>\n 0.05<\/td>\n 0.055<\/td>\n 0.056<\/td>\n <\/td>\n<\/tr>\n \nHardgrove Grindability Index<\/td>\n %<\/td>\n <\/td>\n 75<\/td>\n <\/td>\n <\/td>\n<\/tr>\n \nGross Calorific Value<\/td>\n kcal\/kg<\/td>\n 7065<\/td>\n 7770<\/td>\n 7850<\/td>\n 8680<\/td>\n<\/tr>\n \nCarbonisation analyses \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 As analysed<\/td>\n Ultimate analysis (%)\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 Dry ash free<\/td>\n<\/tr>\n \nCrucible Sw elling Number<\/td>\n <\/td>\n 7.5<\/td>\n Carbon<\/td>\n 88.8<\/td>\n<\/tr>\n \nGray-King Coke Type<\/td>\n <\/td>\n G5<\/td>\n Hydrogen<\/td>\n 5<\/td>\n<\/tr>\n \nRuhr Dilatometer<\/td>\n <\/td>\n <\/td>\n Nitrogen<\/td>\n 1.9<\/td>\n<\/tr>\n \n\u00a0\u00a0\u00a0\u00a0\u00a0 Initial softening temp.<\/td>\n \u02daC<\/td>\n 400<\/td>\n Oxygen<\/td>\n 3.8<\/td>\n<\/tr>\n \n\u00a0\u00a0\u00a0\u00a0\u00a0 Maximum contraction temp.<\/td>\n \u02daC<\/td>\n 445<\/td>\n Sulphur<\/td>\n 0.5<\/td>\n<\/tr>\n \n\u00a0\u00a0\u00a0\u00a0\u00a0 Maximum dilatation temp.<\/td>\n \u02daC<\/td>\n 475<\/td>\n <\/td>\n <\/td>\n<\/tr>\n \n\u00a0\u00a0\u00a0\u00a0\u00a0 Maximum contraction<\/td>\n %<\/td>\n 25<\/td>\n Ash analysis (%)\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 Dry<\/td>\n<\/tr>\n \n\u00a0\u00a0\u00a0\u00a0\u00a0 Maximum dilatation temp.<\/td>\n %<\/td>\n 105<\/td>\n SiO2<\/sub><\/td>\n59.9<\/td>\n<\/tr>\n \nGieseler Plastometer<\/td>\n <\/td>\n <\/td>\n Al2<\/sub>O3<\/sub><\/td>\n28.2<\/td>\n<\/tr>\n \n\u00a0\u00a0\u00a0\u00a0 Initial softening temp.<\/td>\n \u02daC<\/td>\n 410<\/td>\n Fe2<\/sub>O3<\/sub><\/td>\n4.1<\/td>\n<\/tr>\n \n\u00a0\u00a0\u00a0\u00a0 Maximum fluidity temp.<\/td>\n \u02daC<\/td>\n 460<\/td>\n CaO<\/td>\n 2.9<\/td>\n<\/tr>\n \n\u00a0\u00a0\u00a0\u00a0 Resolidification temp.<\/td>\n \u02daC<\/td>\n 495<\/td>\n MgO<\/td>\n 0.5<\/td>\n<\/tr>\n \n\u00a0\u00a0\u00a0\u00a0 Plastic range<\/td>\n \u02daC<\/td>\n 85<\/td>\n Mn2<\/sub>O4<\/sub><\/td>\n0.1<\/td>\n<\/tr>\n \n\u00a0\u00a0\u00a0\u00a0 Maximum fluidity<\/td>\n ddpm<\/td>\n 2000<\/td>\n Na2<\/sub>O<\/td>\n0.4<\/td>\n<\/tr>\n \nPetrographic analysis<\/td>\n As analysed<\/td>\n K2<\/sub>O<\/td>\n0.8<\/td>\n<\/tr>\n \nVitrinite Reflectance (Ro max)<\/td>\n %<\/td>\n 1.21<\/td>\n TiO2<\/sub><\/td>\n1.5<\/td>\n<\/tr>\n \nVitrinite Reflectance (Ro random)<\/td>\n %<\/td>\n 1.14<\/td>\n P2<\/sub>O5<\/sub><\/td>\n1.3<\/td>\n<\/tr>\n \nVitrinite Distribution<\/td>\n <\/td>\n <\/td>\n SO2<\/sub><\/td>\n0.3<\/td>\n<\/tr>\n \n![\"\"](\"http:\/\/i-energy.in\/wp-content\/uploads\/2017\/02\/Capture-300x110.png\")
<\/td>\nBaO<\/td>\n 0.1<\/td>\n<\/tr>\n \n<\/td>\n <\/td>\n<\/tr>\n \nSizing (mm) – % passing<\/td>\n As analysed<\/td>\n<\/tr>\n \n50<\/td>\n 100<\/td>\n<\/tr>\n \n31.5<\/td>\n 91<\/td>\n<\/tr>\n \n16<\/td>\n 79<\/td>\n<\/tr>\n \nMacerals<\/td>\n <\/td>\n <\/td>\n 8<\/td>\n 66<\/td>\n<\/tr>\n \n\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 Vitrinite<\/td>\n %<\/td>\n 58<\/td>\n 4<\/td>\n 61<\/td>\n<\/tr>\n \n\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 Liptinite<\/td>\n %<\/td>\n 0<\/td>\n 4<\/td>\n 56<\/td>\n<\/tr>\n \n\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 Semi-fusinite<\/td>\n %<\/td>\n 35<\/td>\n 2<\/td>\n 48<\/td>\n<\/tr>\n \n\u00a0\u00a0\u00a0\u00a0\u00a0 Other inertinite<\/td>\n %<\/td>\n 4<\/td>\n 1<\/td>\n 38<\/td>\n<\/tr>\n \n\u00a0\u00a0\u00a0\u00a0\u00a0 Mineral Matter<\/td>\n %<\/td>\n 3<\/td>\n 0.5<\/td>\n 28<\/td>\n<\/tr>\n \nCoke Indices (Pilot Coke Oven Tests)<\/td>\n<\/tr>\n \nJIS Drum DI 30\/15<\/td>\n <\/td>\n 95<\/td>\n ASTM Stability<\/td>\n 62<\/td>\n<\/tr>\n \nJIS Drum DI 150\/15<\/td>\n <\/td>\n 84<\/td>\n ASTM Hardness<\/td>\n 69<\/td>\n<\/tr>\n \nMicum M40<\/td>\n <\/td>\n 85<\/td>\n NSC CSR<\/td>\n 73<\/td>\n<\/tr>\n \nMicum M10<\/td>\n <\/td>\n 7<\/td>\n NSC CRI<\/td>\n 20<\/td>\n<\/tr>\n \nIRSID l20<\/td>\n <\/td>\n 80<\/td>\n <\/td>\n <\/td>\n<\/tr>\n \nIRSID l10<\/td>\n <\/td>\n 18<\/td>\n Oven w all pressure (psi)<\/td>\n < 0.5<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div><\/section><\/div><\/p>\n","protected":false},"excerpt":{"rendered":"","protected":false},"author":1,"featured_media":0,"parent":246,"menu_order":0,"comment_status":"closed","ping_status":"closed","template":"","meta":{"footnotes":""},"yoast_head":"\nSemi-soft Coking Coal - 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<\/div><\/div><\/div>
\n
\n
<\/span><\/span><\/div><\/p><\/div>\n\n
i-Energy is a supplier of this main category of metallurgical- semi-soft coking coal which produces coke of lesser quality. Semi-soft coal normally have lower sales values compared to hard coking coal due to the relative availability of these products. Integrated steel mills will optimize the use of semi-soft coal in order to reduce overall costs.<\/p>\n<\/div><\/section><\/div>
| Proximate and other analysis<\/td>\n | \u00a0As received<\/td>\n | Air Dried<\/td>\n | Dry<\/td>\n | Dry ash free<\/td>\n<\/tr>\n | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| Total Moisture<\/td>\n | %<\/td>\n | 10<\/td>\n | <\/td>\n | <\/td>\n | <\/td>\n<\/tr>\n | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| As Analysed Moisture<\/td>\n | %<\/td>\n | <\/td>\n | 1<\/td>\n | <\/td>\n | <\/td>\n<\/tr>\n | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| Ash<\/td>\n | %<\/td>\n | 8.6<\/td>\n | 9.5<\/td>\n | 9.6<\/td>\n | <\/td>\n<\/tr>\n | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| Volatile Matter<\/td>\n | %<\/td>\n | 21.4<\/td>\n | 23.5<\/td>\n | 23.7<\/td>\n | 26.3<\/td>\n<\/tr>\n | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| Fixed Carbon<\/td>\n | %<\/td>\n | 60<\/td>\n | 66<\/td>\n | 66.7<\/td>\n | 73.7<\/td>\n<\/tr>\n | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| Total Sulphur<\/td>\n | %<\/td>\n | 0.41<\/td>\n | 0.45<\/td>\n | 0.45<\/td>\n | 0.5<\/td>\n<\/tr>\n | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| Phosphorus<\/td>\n | %<\/td>\n | 0.05<\/td>\n | 0.055<\/td>\n | 0.056<\/td>\n | <\/td>\n<\/tr>\n | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| Hardgrove Grindability Index<\/td>\n | %<\/td>\n | <\/td>\n | 75<\/td>\n | <\/td>\n | <\/td>\n<\/tr>\n | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| Gross Calorific Value<\/td>\n | kcal\/kg<\/td>\n | 7065<\/td>\n | 7770<\/td>\n | 7850<\/td>\n | 8680<\/td>\n<\/tr>\n | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| Carbonisation analyses \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 \u00a0 As analysed<\/td>\n | Ultimate analysis (%)\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 Dry ash free<\/td>\n<\/tr>\n | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| Crucible Sw elling Number<\/td>\n | <\/td>\n | 7.5<\/td>\n | Carbon<\/td>\n | 88.8<\/td>\n<\/tr>\n | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| Gray-King Coke Type<\/td>\n | <\/td>\n | G5<\/td>\n | Hydrogen<\/td>\n | 5<\/td>\n<\/tr>\n | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| Ruhr Dilatometer<\/td>\n | <\/td>\n | <\/td>\n | Nitrogen<\/td>\n | 1.9<\/td>\n<\/tr>\n | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| \u00a0\u00a0\u00a0\u00a0\u00a0 Initial softening temp.<\/td>\n | \u02daC<\/td>\n | 400<\/td>\n | Oxygen<\/td>\n | 3.8<\/td>\n<\/tr>\n | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| \u00a0\u00a0\u00a0\u00a0\u00a0 Maximum contraction temp.<\/td>\n | \u02daC<\/td>\n | 445<\/td>\n | Sulphur<\/td>\n | 0.5<\/td>\n<\/tr>\n | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| \u00a0\u00a0\u00a0\u00a0\u00a0 Maximum dilatation temp.<\/td>\n | \u02daC<\/td>\n | 475<\/td>\n | <\/td>\n | <\/td>\n<\/tr>\n | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| \u00a0\u00a0\u00a0\u00a0\u00a0 Maximum contraction<\/td>\n | %<\/td>\n | 25<\/td>\n | Ash analysis (%)\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 Dry<\/td>\n<\/tr>\n | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| \u00a0\u00a0\u00a0\u00a0\u00a0 Maximum dilatation temp.<\/td>\n | %<\/td>\n | 105<\/td>\n | SiO2<\/sub><\/td>\n| 59.9<\/td>\n<\/tr>\n | Gieseler Plastometer<\/td>\n | <\/td>\n | <\/td>\n | Al2<\/sub>O3<\/sub><\/td>\n | 28.2<\/td>\n<\/tr>\n | \u00a0\u00a0\u00a0\u00a0 Initial softening temp.<\/td>\n | \u02daC<\/td>\n | 410<\/td>\n | Fe2<\/sub>O3<\/sub><\/td>\n | 4.1<\/td>\n<\/tr>\n | \u00a0\u00a0\u00a0\u00a0 Maximum fluidity temp.<\/td>\n | \u02daC<\/td>\n | 460<\/td>\n | CaO<\/td>\n | 2.9<\/td>\n<\/tr>\n | \u00a0\u00a0\u00a0\u00a0 Resolidification temp.<\/td>\n | \u02daC<\/td>\n | 495<\/td>\n | MgO<\/td>\n | 0.5<\/td>\n<\/tr>\n | \u00a0\u00a0\u00a0\u00a0 Plastic range<\/td>\n | \u02daC<\/td>\n | 85<\/td>\n | Mn2<\/sub>O4<\/sub><\/td>\n | 0.1<\/td>\n<\/tr>\n | \u00a0\u00a0\u00a0\u00a0 Maximum fluidity<\/td>\n | ddpm<\/td>\n | 2000<\/td>\n | Na2<\/sub>O<\/td>\n | 0.4<\/td>\n<\/tr>\n | Petrographic analysis<\/td>\n | As analysed<\/td>\n | K2<\/sub>O<\/td>\n | 0.8<\/td>\n<\/tr>\n | Vitrinite Reflectance (Ro max)<\/td>\n | %<\/td>\n | 1.21<\/td>\n | TiO2<\/sub><\/td>\n | 1.5<\/td>\n<\/tr>\n | Vitrinite Reflectance (Ro random)<\/td>\n | %<\/td>\n | 1.14<\/td>\n | P2<\/sub>O5<\/sub><\/td>\n | 1.3<\/td>\n<\/tr>\n | Vitrinite Distribution<\/td>\n | <\/td>\n | <\/td>\n | SO2<\/sub><\/td>\n | 0.3<\/td>\n<\/tr>\n | <\/td>\nBaO<\/td>\n | 0.1<\/td>\n<\/tr>\n | <\/td>\n | <\/td>\n<\/tr>\n | Sizing (mm) – % passing<\/td>\n | As analysed<\/td>\n<\/tr>\n | 50<\/td>\n | 100<\/td>\n<\/tr>\n | 31.5<\/td>\n | 91<\/td>\n<\/tr>\n | 16<\/td>\n | 79<\/td>\n<\/tr>\n | Macerals<\/td>\n | <\/td>\n | <\/td>\n | 8<\/td>\n | 66<\/td>\n<\/tr>\n | \u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 Vitrinite<\/td>\n | %<\/td>\n | 58<\/td>\n | 4<\/td>\n | 61<\/td>\n<\/tr>\n | \u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 Liptinite<\/td>\n | %<\/td>\n | 0<\/td>\n | 4<\/td>\n | 56<\/td>\n<\/tr>\n | \u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 Semi-fusinite<\/td>\n | %<\/td>\n | 35<\/td>\n | 2<\/td>\n | 48<\/td>\n<\/tr>\n | \u00a0\u00a0\u00a0\u00a0\u00a0 Other inertinite<\/td>\n | %<\/td>\n | 4<\/td>\n | 1<\/td>\n | 38<\/td>\n<\/tr>\n | \u00a0\u00a0\u00a0\u00a0\u00a0 Mineral Matter<\/td>\n | %<\/td>\n | 3<\/td>\n | 0.5<\/td>\n | 28<\/td>\n<\/tr>\n | Coke Indices (Pilot Coke Oven Tests)<\/td>\n<\/tr>\n | JIS Drum DI 30\/15<\/td>\n | <\/td>\n | 95<\/td>\n | ASTM Stability<\/td>\n | 62<\/td>\n<\/tr>\n | JIS Drum DI 150\/15<\/td>\n | <\/td>\n | 84<\/td>\n | ASTM Hardness<\/td>\n | 69<\/td>\n<\/tr>\n | Micum M40<\/td>\n | <\/td>\n | 85<\/td>\n | NSC CSR<\/td>\n | 73<\/td>\n<\/tr>\n | Micum M10<\/td>\n | <\/td>\n | 7<\/td>\n | NSC CRI<\/td>\n | 20<\/td>\n<\/tr>\n | IRSID l20<\/td>\n | <\/td>\n | 80<\/td>\n | <\/td>\n | <\/td>\n<\/tr>\n | IRSID l10<\/td>\n | <\/td>\n | 18<\/td>\n | Oven w all pressure (psi)<\/td>\n | < 0.5<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div><\/section><\/div><\/p>\n","protected":false},"excerpt":{"rendered":"","protected":false},"author":1,"featured_media":0,"parent":246,"menu_order":0,"comment_status":"closed","ping_status":"closed","template":"","meta":{"footnotes":""},"yoast_head":"\n | |