ANNEXURES · 2018-09-30 · [3] Sl. No. Generatio Phase-1 Phase-2 Total Capacity Plant Facilities...

ANNEXURES

[1]

DETAILS OF PLANT FACILITIES AND CAPACITY

Sl. No.

Phase-1 Phase-2 Total Capacity Plant Facilities Production Unit

Description Annual Production/

Generation Production Unit


Generation Total Annual Production/ Generation

No of

Units Unit Unit

Capacity Unit Annual

Capacity No of Units

Unit Unit Capacity

Unit Annual Capacity

C1 C2 C3 C4 C5 C6 C7 C13 C14 C15 C16 C17 C18=C7+C12+C17 1 Sponge Iron Plant 1.001 0.546 1.547

DR Kilns 2 TPD 500 MTPA 0.455 0.455

2 TPD 600 MTPA 0.546 2 TPD 600 MTPA 0.55 1.092

2 Pelletisation Plant 1 MTPA 1.2 MTPA 1.47 1 MTPA 1.2 MTPA 1.47 2.948

3 Beneficiation Plant (Based on input)

1 MTPA 2.69 MTPA 2.7 1 MTPA 2.69 MTPA 2.7 5.4

4 Coal Washery (Based on input ROM Coal)

1 TPH 400 MTPA 2.616 1 TPH 235 MTPA 1.524 4.141

5 Mini Blast Furnace 1 CUM 600 MTPA 0.567 1 CUM 1050 MTPA 0.992 1.559

6 Sinter Plant 1 SQM 64 MTPA 0.612 1 SQM 110 MTPA 1.051 1.663

7 Coke Oven Plant 6 TPA 70000 MTPA 0.420 10 TPA 70000 MTPA 0.70 1.12

8 Steel Melting Shop MTPA 1.232 MTPA 1.232 2.464

8.1 Steel Melting Via IF-Route

MTPA 0.539 0.539

a Induction Furnace 7 Ton 20 MTPA 0.539 0.539

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Sl. No.






No of

Units Unit Unit



Unit Unit Capacity


C1 C2 C3 C4 C5 C6 C7 C13 C14 C15 C16 C17 C18=C7+C12+C17 b Laddle Furnace 4 Ton 20 0

8.2 Steel Melting via EAF-VD-AOF Route

MTPA 0.693 MTPA 1.232 1.925

a Electric Arc Furnace

1 Ton 90 MTPA 0.693 1 Ton 160 MTPA 1.232 1.925

b Laddle Furnace 1 Ton 90 1 Ton 160 0

8.3 Continuous Casting Machine

MTPA 1.207 MTPA 1.207 2.415

a Billets/ Bloom Caster/Slab Caster

2 Strands 3 MTPA 1.207 1 Strands 3 MTPA 1.207 2.415

9 Finished Product Facilities

MTPA 1.450 MTPA 1.400 2.850

9.1 Rolling Mill (TMT/ Flat/ Round/ Wire Rod/ Structural Mill/ others)

MTPA 0.800 0.800 1.600

a Rolling Mill-1 4 TPA 200000 MTPA 0.800 2 TPA 300,000.00 MTPA 0.600 1.400

b Rolling Mill-2 1 TPA 200,000.00 MTPA 0.200 0.200

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[3]

Sl. No.






No of

Units Unit Unit



Unit Unit Capacity


C1 C2 C3 C4 C5 C6 C7 C13 C14 C15 C16 C17 C18=C7+C12+C17 9.2 Strip

Mill/Sheet/Coil/ Wire & Bar Mill/Wire Rope

1 TPA 450000 MTPA 0.450 1 TPA 400,000.00 MTPA 0.400 0.8500

9.3 Ductile Pipe Plant 1 TPA 200000 MTPA 0.200 1 TPA 200,000.00 MTPA 0.200 0.400

10 Producer Gas Plant Nm3/Annum 240000000 Nm3/Annum 240000000 480000000

Producer Gas Plant 10 Nm3/Hr 3000 Nm3/Annum 240000000 10 Nm3/Hr 3000 Nm3/Annum 240000000 480000000

11 Oxygen Plant MTPA 0.0350 MTPA 0.0630 0.0980

Oxygen Plant 1 TPD 100 Nm3/Annum 24500000 1 TPD 180.00 Nm3/Annum 44100000 68600000

12 Lime Plant MTPA 0.105 MTPA 0.1995 0.3045

Lime Plant 1 TPD 300 TPA 105000 1 TPD 570 TPA 199500 304500

13 Cement Plant MTPA 0.884 MTPA 0.802 1.686

Cement Plant alongwith Clinker Plant

1 TPD 2600 TPA 884000 1 TPD 2300 TPD 801596 1685596

14 Captive Power Plant

MW 217.00 MW 168.00 385.00

14.1 WHRB Based CPP MW 67.00 MW 68.00 135.00

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[4]

Sl. No.






No of

Units Unit Unit



Unit Unit Capacity


C1 C2 C3 C4 C5 C6 C7 C13 C14 C15 C16 C17 C18=C7+C12+C17 a WHRB (500 TPD

DR Kiln) 2 TPH 50 MW 20.00 20.00

b WHRB (600 TPD DR Kiln)

2 TPH 60 MW 24.00 2 TPH 60 MW 24.00 48.00

c WHRB (MBF) 1 TPH 50 MW 11.00 1 TPH 90 MW 20.00 31.00

d WHRB (Coke Oven)

1 TPH 60 MW 12.00 1 TPH 100 MW 24.00 36.00

14.2 AFBC/CFBC based CPP

MW 150.00 MW 100.00 250.00

a AFBC/CFBC 2 TPH 125 MW 50.00 50.00

b AFBC/CFBC 2 TPH 250 MW 100.00 2 TPH 250 MW 100.00 200.00

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Mahesh

Text Box

Mahesh

Text Box

ANNEXURE : III

[1/6]

LIST OF PLOTS Pvt. Land Acquired in Village Jharbandha : Khata No. 719 Plot No. 3013, 3082, 3120, 3005, 3332, 3138, 3016, 3608, 3410, 3506/3932, 3076, 3077, 3110, 3331, 3398, 3400, 3512, 3537, 3542, 2828, 3277, 2963, 2965, 2969, 3029, 2733/4901, 2744, 2794, 2799, 2802, 2971, 3024, 3334, 2804, 2731, 3178, 3025, 3027, 3032, 3033, 2891, 2966, 3052, 3285, 3280, 3282, 3504, 3605, 3174/4279, 3505, 2982, 3322, 3324, 3326, 3328, 3501, 3527, 3528, 3532, 3553, 3556, 2975/4013, 3572, 2735/4358, 2967, 2962, 2972, 3166, 3084, 3103, 2826, 2837, 3437, 3443, 3559, 2785, 2833, 2835, 2840, 2842, 2850, 2875, 2873, 3336, 3373, 3375, 3383, 3388, 3419, 3490, 3491/4066, 3423, 3444, 2907/4012, 3319, 3316, 3500, 3526/4010, 3525/4011, 3329/4006, 3555/4007, 3299, 3303, 3062, 3074, 3088, 3093, 3095, 3114, 3600/4327, 3604, 2830, 3547, 3548, 3549, 3093/4333, 2784, 2787, 2977, 3297, 3302, 3305, 3309, 3311, 3571/4032, 2778, 2782, 3158, 3004, 3008, 3106, 3109, 3121, 3137, 3140, 3142, 3145, 3589, 3607, 3406/3885, 3110/4061, 3110/4062, 3078/4055, 3134, 3078, 3118, 3133, 3076/4053, 3078/4058, 3085, 3086, 3089, 2927/4904, 2845, 2847, 2849, 2852, 2868, 2870, 2871, 2876, 2880, 2882, 2886, 2888, 2895, 2926, 2832, 3489, 3488, 3487, 3486, 2954/4905, 3042, 3042/4841, 3265, 3264/4259, 3056, 3535, 3110/4059, 3077/4056, 3076/4051, 2812, 2816, 2820, 2822, 2912, 2914, 2918, 2920, 2922, 2925, 2999, 3335, 3339, 3408, 2902, 3124/4375, 3288, 3127/4374, 3131/4376, 3107, 3349, 3048/4816, 3321/4817, 2984, 2989, 3337, 3342, 3344, 3360, 3000, 3415, 3426, 3442, 2986, 3410/4031, 3343/4405, 3350, 3019, 2905/4496, 3050, 2750/4908, 2862, 3340, 3369, 3136, 3449, 3274, 3502, 3503, 3519, 3520, 3536, 3092, 3354, 3356, 3355, 3358, 3540, 3539, 3252, 3357, 3561, 3562, 3563, 3569, 3584, 3438, 2730/3907, 3193, 3196, 3200, 3203, 3521, 3306, 2988, 3262/4810, 3262, 3101, 3098, 3276, 2768/4909, 2776/4910, 2817, 2818, 2821, 2913, 2917, 2919, 3275, 3283, 3571/4033, 3076/4054, 3076/4052, 3535/4064, 3110/4060, 3077/4057, 3238, 2901, 3045, 3044, 3162, 3260, 3545, 3550, 3586, 3552/3914, 3499, 3497, 3484, 3492, 3479, 3481, 3483, 3476, 3472, 3474, 3466, 3477, 2743, 2745, 2797, 2800, 2801, 2728, 3428, 3433, 3530, 3565, 2753, 2754, 2808, 2813, 2814, 2807, 2810, 2807/4854, 3813, 2843, 2853, 2854, 2878, 3371, 2865, 3451, 3510, 3174, 2846, 2848, 2872, 2877, 2923, 3043, 3380, 3397, 3600/4171, 3049, 3365, 3376, 3403, 3286, 3393, 3407, 3450, 3511, 2896, 3330, 3391, 3456, 3573, 3577, 3538, 3259, 3574, 3576, 3264, 3578, 3293, 2866, 2883, 2890, 2956, 3289, 2841, 3317, 2893, 2874, 3372, 3377, 3382, 3422, 2786, 2789, 2836, 2839, 2851, 2856, 3374, 3420, 3445, 2834, 3490/4065, 3491/4067, 3205, 3149, 3197, 3201, 3183, 3209, 3229, 3225, 3233, 3236, 3246, 3053/4167, 3188, 3187/4829, 3187, 3189, 3209/4883, 3231, 3212, 3039, 3041, 3153, 3427, 3404, 2861, 3392, 3456/3992, 3602, 3390, 3269, 3600/4408, 3600/4409, 3600/4409/4871, 3381, 3429, 3543, 3087, 3389, 3536/4503, 3010/4511, 3156, 1033/3861, 3878/4498, 3061/4620, 3150/3908, 3152, 3184, 3148/4622, 3249/4676, 3249/4677, 3908/4478, 3163/4556, 3164, 3144, 3162/4481, 3162/4522, 3162/4490, 2889, 2887, 2793, 2736, 3441, 3122, 3106/4513, 3145/4512, 2892, 3037/4520, 3147, 3146/4584, 3523, 3560, 3168, 3169, 3037/4541, 3192/4579, 3192/4580, 3192/4581, 3192/4590, 2713/4597, 3192/4527, 3037/4612, 3038/4613, 3111/4686, 3522/4689, 3364/4721, 3522/4748, 2720/4779, 3162/4480, 3390/4290, 2746/4903, 2752, 2790, 2792, 3192/4571,

ANNEXURE : III Contd..

[2/6]

2867, 2869, 3155/4822, 3155/4823, 3505/4842, 3071, 3068, 3070, 3067, 3072, 3111, 3112, 3116, 3119, 3176, 2829, 3090, 3097, 3099, 3079, 2928/4902, 3307, 3294, 3295, 3606, 3020/3884, 3017, 3581, 3464, 3465, 3470, 3471, 3473, 3478, 3480, 3475, 3482, 3485, 3493, 3495, 3494, 3496, 3498, 3467, 2724, 3813/3878, 2864, 2897, 3454, 3452, 3463, 3453, 3469, 3761, 2975, 3554/4008, 3580/4005, 3533/4009, 3327, 3506, 3251, 3310, 2783, 3290, 3291, 3298, 3301, 3304, 3308, 3571, 3057, 3058, 2721/4241, 2721/4242, 2909, 3059, 2730, 3150, 3051, 3600/4328, 3524, 3529, 3566, 3531, 2899, 2903, 2904, 2978, 3146, 3061, 2978/4878, 2908, 3148, 3003, 3009, 3010, 3012, 3015, 3104, 3123, 3128, 3132, 2916, 2995, 2806, 2809, 3094, 3100, 3113, 3115, 3125, 3126, 3157, 3181, 3185, 3190, 3195, 3211, 3202, 3223, 3228, 3232, 3237, 3241, 3212/4176, 3188/4601, 3268, 3063, 3036, 3064, 2788, 2885, 3399, 3401, 3513, 3541, 3258, 3459, 3460, 3323, 3338, 3351, 3367, 3387, 3395, 3418, 3421, 3582, 2976, 3518, 3507, 3508, 3322/4675, 3038, 3040, 3040/3847, 3037, 3551, 3546, 2957, 2961, 2955/4906, 2959, 2958, 2960, 3065, 3066, 3117, 3096, 3117/4063, 3060, 3159, 3182, 3198, 3207, 3210, 3218, 3220, 3224, 3234, 3245, 3517, 3522, 3047, 3048, 3250, 3284, 3318, 3320, 3321, 3325, 2990, 2991, 2952/4907, 3172, 3273, 3278, 3279, 3281, 3287, 3364, 3552, 3579, 2953, 3046, 3287/4877, 3046/4814, 3047/4815, 3192, 3191, 3192/4789, 2907, 2983, 3315, 3329, 3525, 3526, 3533, 3554, 3555, 3580, 3590, 3591, 3343, 3347, 3001, 2796, 2798, 3023, 3333, 3179, 3214, 3189/4501, 3197/4502, 3201/4500, 2980, 2900, 3199, 3208, 3215, 3219, 3227, 3230, 3235, 3242, 3247, 3240, 3244, 3212/4487, 3222, 2985, 2992, 2996, 2997, 3257, 3379, 3300, 3514, 3516, 2732, 2803, 2970, 3022, 3026, 3028, 3031, 3180, 2968, 3030, 3030/4863, 3030/4866, 2803/4868, 3105, 3124, 3129, 3014, 3081, 3127, 3131, 3083, 3255, 3557, 3568, 3506/3933, 3402, 3409, 3413, 3054, 3313, 3386, 3414, 3312, 3018, 3053, 3055, 3263, 3352, 3417, 3585, 3588, 3601/3831, 3314, 3585/4818, 3585/4819, 3585/4820, 3585/4821, 3585/4843, 3585/4844, 3439, 3462, 3577/3955, 2730/3906, 3150/3909, 2987, 2998, 3348, 3359, 3425, 3361, 2905/4592, 3266, 3011, 3006, 3108, 3130, 3139, 3141, 2858, 2863, 2981, 2994, 3135, 3341, 3363, 3366, 3368, 3370, 3384, 3396, 3431, 3455, 2860, 2898, 3394, 3424, 3435, 3448, 3362, 3534, 2897/4486, 3346, 2751, 2859, 3416, 3436, 3575, 3447, 3378, 3296, 3385, 3292, 3254, 3558, 3567, 2838, 2824, 3253, 3583, 2905, 2993, 2974, 2910, 2964, 3432, 2791, 2795, 3564, 2825, 2729/4183, 2727/4911, 3035, 3073, 3091, 3097/4482, 3102, 3034, 2777, 2811, 2911, 2915, 2924, 2769/4912, 2921, 2815, 2819, 2823, 3143, 3132/4516, 2720, 3167, 3167/4851, 3405, 3406, 3165, 3544, 2901/3860, 3020, 3261, 3461, 3587, 3163, 2857, 3038/4542, 3249, 3184/4572, 2780, 2781, 3192/4589, 2894, 2881, 2884, 2872/4602, 2881/4603, 2872/4606, 2848/4604, 3509, 3510/4701, 2779, 2979, 3515, 2929/4614, 3191/4681, 3194, 3226, 3248, 3446, 2855, 3061/4679, 3160/3944, 3160/3944/4837, 3440, 3468, 2906, 3075, 2879, 2805, 3592/4369, 3592/4371, 3592/4384, 3592/4370, 3155, 2844, 3502/8782, 3603, 3191/4526, 3193/4528, 3037/4565, 3187/4573, 3193/4600, 3192/4598, 3192/4599, 3192/4577 and 3192/4578


[3/6]

Pvt. Land Acquired in Village Galapada : Khata No. 731 Plot No. 3110, 3094, 3146, 3148, 3150, 3180, 3203, 3205, 3192, 3187, 2924, 2924/3612, 3154, 3157, 3225, 3226, 3226/3850, 3091, 3107, 3121, 3029, 3108, 3113, 3118, 3140, 3198, 3207, 3209, 3219, 3220, 3242, 2972, 3055, 2833/3573, 3032/3335, 3078/3358, 3171, 3125, 2979, 3109, 3119, 3139, 3195, 3197, 3210, 3037, 3090, 3114, 3260, 3032, 3078/3357, 3134, 3175, 3201, 3247, 3199, 2974, 3043, 3045, 3244, 3246, 3248, 3269, 2965, 3051, 3126, 2986, 3264, 3129/3410, 3079, 2980, 2933, 3170, 3167, 3026, 3115, 3117, 3141, 3208, 3229, 2985, 3176/3859, 3261/3860, 3127/3857, 3131/3858, 3127/3866, 3131/3867, 3176/3868, 3261/3869, 2987, 3089, 3064, 3049, 3102, 3035, 2995, 3155, 3254, 3255, 3270, 3271, 2937, 2959, 3021, 3024, 3166, 3168, 2934, 2940, 2950, 2958, 3087, 3098, 3177, 2936, 2938, 3023, 2991, 3237, 2833, 3100, 3234, 2968, 2929, 2833/3518, 3173, 3084, 3232, 3149, 3151, 3178, 3183, 3185, 3191, 3202, 3223, 3182, 3078/3359, 2971, 2964, 3050, 3088, 3093, 3106, 3120, 3122, 3169, 3078/3354, 2988, 3052, 3099, 3128, 3228, 3235, 3236, 2960, 2981, 2982, 2983, 2984, 3038, 3047, 3053, 3153, 3158, 3039, 3104, 3107/3418, 2941/3551, 3072, 3065, 3031, 3078/3356, 3075, 2927, 2967, 2928, 2966, 3133, 2928/3871, 3175/3533, 2962, 3233/3534, 2942, 2944, 2947, 3048, 2961, 2953/3613, 3106/3543, 2941, 3076, 3069, 3115/3877, 3117/3878, 2939, 3082, 3080, 3046, 2928/3875, 3243, 3218, 3243/3409, 3206, 3213, 3217, 3218/3906, 3112, 3136, 3135, 3081, 3083, 3085, 3103, 2931, 2976, 2930, 2975, 2932, 3022, 3025, 3101, 3044, 3250, 3039/3460, 3250/3462, 3189, 3193, 3239, 3078, 3058, 3070, 3073, 3123, 2990, 3059, 3172, 3174, 2973, 3124, 2935, 2951, 2955, 2957, 3086, 3127, 3131, 3176, 3261, 2969, 3127/3841, 3034, 3267, 3078/3355, 2832, 3105, 3105/3416, 3106/3417, 3056, 3061, 3067, 3143, 2996, 3159, 3252, 3253, 3256, 3257, 3188, 3194, 3238, 3036, 3041, 3039/3461, 3268, 3092, 3097, 3028, 3027, 3160, 3164, 3163, 3221, 3222, 3057, 3060, 3066, 3074, 3077, 3132, 3138, 3227, 3181, 3186, 3111, 3145, 3130, 3196, 3116, 3147, 3152, 3179, 3184, 3200, 3204, 3131/3507, 3033, 3030, 3156, 3165, 3162, 3262, 2952, 3273, 3272, 3275, 3277, 3279, 3278, 3274, 3276, 2953, 3040, 3096, 3161, 2989, 3054, 3063, 3068, 3071, 3062, 3142, 3078/3353, 3241, 3031/3334, 3137, 3224, 2970, 3265, 2964/3535, 2954, 3266, 3263/3539, 2965/3540, 3082/3541, 3120/3542, 3245, 3217/3575, 3211, 3212, 3205/3676, 3203/3683, 3205/3687, 3205/3688, 3245/3907, 3091/3548, 3154/3554, 3103/3562, 3263, 3088/3607, 3129, 3233, 2936/3596, 2938/3597, 2956/3598, 3023/3600, 2992, 2926, 2834/3919, 2925, 3231, 2956, 2977, 2978, 3094/3680, 3190, 3095, 3230, 2943, 2945, 2946, 2948 and 2949.


[4/6]

Pvt. Land Acquired in Village Tarkabeda: Khata No. 831 Plot No. 890, 891, 969, 970, 979, 980, 149, 150, 145, 147, 145/4872, 1059, 1039/4587, 1025, 1026, 1021, 1041, 1040, 1039, 1017, 983, 1011, 895, 895/4801, 902, 902/4813, 1003, 1014, 1015, 1019, 1020, 1003/4860, 906, 22, 20, 21, 23, 155, 156, 9, 93, 953, 972, 157, 972/4841, 927, 930, 931, 925, 33, 944/4857, 239, 251, 252, 253, 876, 883, 976, 901, 901/4814, 903, 904/4815, 994, 904, 1037, 1069, 11, 12, 13, 14, 15, 16, 151, 153, 154, 159, 160, 17, 87, 90, 92, 885, 955, 971, 867, Dec-34, 13/4835, 14/4836, 15/4837, Nov-33, 161, 1005, 8, 21/4725, 23/4732, Sep-33, 20/4724, 907, 1044/4727, 905/4763, 86/4762, 200/4761, 50, 51, 1039/4764, 88, 89, 1025/4612, 140/4207, 1004/4666, 1007, 1008/4385, 1007/4896, 7, 959/4600, 959/4600/4829, 959/4600/4830, 959/4600/4831, 51/4649, 222, 223, 19, 156/4771, 905/4772., 888/4773, 886/4775, 960/4774, 27/4776, 940/4777, 225, 255, 27, 180, 181, 1006, 250, 254, 137, 237, 35/4820, 118/4822, 137/4821, 237/4823, 129/4824, 117, 131, 138, 139, 237/4880, 129/4881, 892, 968, 978, 959, 975, 38, 44, 136, 166, 170, 171, 182, 193, 198, 206, 231, 909, 913, 915, 918, 934, 935, 947, 999, 40, 46, 125, 132, 135, 140, 165, 167, 172, 261, 280, 861, 872, 898, 900, 967, 981, 1044, 1022, 1043, 1017/4484, 1039/4586, 86, 91, 94, 954, 973, 1070, 1070/4852, 905, 1001, 1001/4832, 929, 987, 43, 48, 115, 205, 920, 924, 939, 941, 943, 945, 948, 984, 997, 186, 952, 177, 178, 179, 188, 200, 201, 913/4677, 907/4697, 1070/4753, 907/4701, 224, 998, 957/4372, 906/4729, 940/4692, 905/4772/4816, 912/4800, 893/4811, 914/4664, 995, 908/4734, 877, 1035/4856, 887, 953/4842, 155/4888, 10, 18, 208, 218, 262, 276/4901, 888, 960, 870, 886, 963, 871, 964, 889, 962, 869, 961, 215, 229, 230, 257, 279, 284, 285, 258, 260, 286, 859, 32, 39, 45, 141, 142, 143, 183, 233, 911, 914, 917, 922, 932, 937, 944, 154/4818, 17/4817, 87/4889, 152, 162, 1042, 109, 1027, 1029, 1030, 1034, 1028, 1033, 1036, 24, 1064, 956, 25, 26, 52, 957, 1063, 1066, 1009, 28, 1035/4827, 1035, 956/4847, 958, 1063/4848, 868, 897, 899, 966, 982, 1045, 220, 221, 226, 228, 283, 862, 863, 1061, 1038/4828, 1038, 256, 259, 884, 977, 36, 37, 41, 42, 47, 120, 121, 122, 124, 123, 126, 128, 133, 134, 144, 163, 173, 174, 175, 176, 202, 235, 238, 921, 923, 940, 942, 949, 985, 986, 996, 1008, 936, 940/4799, 896, 991, 34, 35, 118, 119, 129, 130, 169, 184, 195, 197, 232, 857/4900, 858, 910, 912, 916, 919, 933, 938, 946, 1000, 49, 114, 116, 127, 203, 1062, 1038/4212, 951, 951/4812, 893, 894, 965, 164, 168, 882, 875, 881, 873, 880, 995/4273, 908, 1002, 1016, 1018, 1023, 1024, 908/4819, 207, 209, 216, 217, 200/4332, 1060, 1038/4211, 1010, 1012, 1013, 158, 158/4825, 1013/4826, 110, 214, 860, 111/4271, 1032, 1040/4485, 29, 30, 49/4389, 146, 190, 111, 219, 227, 31, 196, 185, 187, 189, 236, 148, 1004, 1039/4597, 1039/4597/4838, 990, 53, 914/4645, 913/4646, 914/4654, 913/4655, 874, 879, 1039/4662, 913/4665, 194, 199 and 204


[5/6]

Govt. Land possession Taken Village: Jharbandh Plots No. 2416, 2721, 2723, 2735, 2827, 3175, 3216, 3243, 3601, 3765, 2720/4278, 3017/4320, 3058/4383, 3058/4385, 3572/4004, 3007, 3021, 3069, 3206, 3217, 3805, 2734, 2973, 3221, 3239, 3412, 3570, 3592, 3075/3900 and 3766 Village : Galapada Plots No. 2994, 3240, 3259, 2973/3313, 2974/3314, 2963, 2960(P), 3144, 3216 and 3249 Village : Tarkabeda Plots No. 234, 864, 865, 928, 950, 1031, 1065, 1004/4297, 1013/4296, 936/4387, 210, 211 and 212


[6/6]

Govt. Land under acquisition through IDCO Village : Jharbandh Plot No. 2831, 3080, 3177, 3491, 3600, 3601/3945, 2729, 3173, 3204, 3256, 3270, 3345, 3353, 3411, 2818/3965, 2819/3966, 2820/4271, 2821/3968, 2939/4000, 2951/4001, 2737, 2738, 3002, 3154, 3160, 3161, 3170, 3171, 3271, 3272, 3457, 3458 and 3602/3991, Village: Galapada Plot No. 3020/3298, 3001, 3042, 3089/3316, 3251, 2941/3301, 3129/3299, 3230/3300, 3214, 3215 and 3258, Village : Tarkabeda Plot No. 878, 926, 974, 1067, 1080(P), 191, 192, 866, 988, 989, 992, 993, 85, 213, 1068, 1039/4264 and 1042/4314,

Mahesh

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ANNEXURE : IV

Mahesh

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ANNEXURE : IV Contd..

SUMMARY OF AMENITIES AVAILABLE (CENSUS 2011) IN VILLAGES WITHIN THE STUDY AREA OF INTEGRATED STEEL PLANT AT JHARBANDH OF RUNGTA MINES LTD.AMENITIES NOS. AMENITIES NOS. AMENITIES NOS.

EDUCATION FACILITIES DRINKING WATER FACILITY APPROACH TO VILLAGEPPS (Pre-Primary School) 5 TWT (Tap Water-Treated) 0 NH (National Highway) 25PS (Primary school) 203 TWUT (Tap Water Untreated) 11 SH (State Highway) 11MS (Middle school) 103 CW (Covered Well) 1 MDR (Major District Road) 29SS (Secondary school) 53 UW (Uncovered Well) 151 ODR (Other District Road) 65SSS (Sr. Sec. School) 17 HP (Hand Pump) 159 BTPR (Black Topped (pucca) Road) 102DCAS (Deg. College Arts & Science only) 7 TW/ BW (Tube Wells/Borehole) 8 GCR (Gravel (kuchha) Roads) 150EC ( Engg. College) 3 S (Spring) 32 WBM (Water Bounded Macadam) 22MC (Medicine College) 2 R/C (River/Canal) 68 AWR (All Weather Road) 109MI (Management Institute) 2 T/P (Tank/Pond/Lake) 150 NWR/C (Navigable Waterways (River/Canal)) 32

P (Polytechnic) 3 WO (Others) 8 FP (Foot Path) 159VTS/ITI (Vocational Trg School/ITI) 9NFTC (Non Formal Training Centre) 0 COMMUNICATION SYSTEM BANKS AND COMMERCIAL SOCIETIESSFD (School For Disabled) 0 PO (Post Office) 26 ATM (ATM) 1EO (Others) 0 SPO (Sub Post Office) 6 CB (Commercial bank) 1

P&T (Post & Telegraph office) 10 COB (Co-operative bank) 2MEDICAL FACILITIES PIN (Village PIN code) 159 ACS (Agricultural Crredit Societies) 3CHC (Community Health Centres ) 0 T (Telephone (landline)) 99 SHG (Self-Help Group (SHG)) 156PHC (Primary Health Centre) 0 PCO (Public Call Office/ Mobile PCO) 35 PDS (Public Distribution System (PDS)) 104PHSC (Primary Health Sub-Centre) 19 MPC (Mobile phone coverage) 151 M/RM (Mandis/Regular Market) 22MCWC (Maternity And Child Welfare Centre) 8 IC/CSC (Internet Cafes/Common Service Centre) 3 WH (Weekly Haat) 32TBC (TB Clinic) 1 PCF (Private Courier Facility) 19 AMS (Agricultural Marketing Society) 14HA (Hospital Allopathic) 3 NCICDS (Nutritional Centres-ICDS) 34HAM (Hospiltal Alternative Medicine) 1 TRANSPORT SYSTEM NCAC (Nutritional Centres-Anganwadi Centre) 145

D (Dispensary) 10 PBS (Public Bus Service) 27 NCO (Nutritional Centres-Others) 3VH (Veterinary Hospital) 4 PvtBS (Private Bus Service) 51 ASHA (ASHA) 155MHC (Mobile Health Clinic) 0 RS (Railway station) 13 CC-TV (Community Centre with/without TV) 61

FWC (Family Welfare Centre) 3 MA (Auto/Modified Autos) 72NGMF-OP (Non Govt. Med. facilities Out Patient) 0 Taxi (Taxi) 45 SPORTS AND ENTERTAINMENTNGMF-IOP (Non Govt. Med. facilities In And Out Patient) 0 Van (Vans) 9 SF (Sports Field) 77

NGMF-C (Non Govt. Med. facilities Charitable) 0 T (Tractors) 78 SC/RC (Sports Club/Recreation Centre) 60NGMF-MBBS (Non Govt. Med. facilities Medical Prctitioner with MBBS Degree )

5 CPR-Man (Cycle-pulled Rickshaws (manual driven)) 159 C/VH (Cinema/Video Hall) 1

CPR-Mec (Cycle-pulled Rickshaws (machine driven)) 0 PL (Public Library) 13

NGMF-OD (Non Govt. Med. facilities Medical Prctitioner with other Degree )

1 CDA (Carts Drivens by Animals) 147 PRR (Public Reading Room) 13S/R/FS (Sea/River/Ferry Service) 26 DNS (Daily Newspaper Supply) 154

NGMF-ND (Non Govt. Med. facilities Medical Practitioner with no Degree )

1 APS (Assembly Polling Station) 120POWER SUPPLY BDRO (Birth and Death Registration Office) 3

NGMF-TPFH (Non Govt. Med. facilities Traditional Practitioner and Faith Healer )

1 PSDU (Power Supply For Domestic Use) 147PSIAU (Power Supply ForAgriculture Use) 54

NGMF-MS (Non Govt. Med. facilities Medicine Shop ) 56 PSCU (Power Supply For Commercial Use) 0NGMF-O (Non Govt. Med. facilities Others) 1 PSALL (Power Supply For All Users) 49

Mahesh

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ANNEXURE : VI

SUMMARY OF AMENITIES AVAILABLE (CENSUS 2011) IN TOWNS WITHIN THE STUDY AREA OF INTEGRATED STEEL PLANT AT JHARBANDH OF RUNGTA MINES LTD.AMENITIES NOS. AMENITIES NOS. AMENITIES NOS.

EDUCATION Private-MS Office (Nos.) 0 WATER SUPPLY AND SANITATIONGovt. Primary School (Nos.) 3 Govt.-Desk Top Publishing (Nos.)) 0 Latrines-Pit (Nos.) 412Private Primary School (Nos.) 0 Private-Desk Top Publishing (Nos.) 0 Latrines-Flush/Pour Flush (Nos.) 791Govt. Middle School (Nos.) 2 Govt.-Vocational(Others) (Nos.)) 0 Latrines-Service (Nos.) 0Private Middle School (Nos.) 0 Private-Vocational(Others) (Nos.) 0 Latrines-Others (Nos.) 9Govt. Secondary School (Nos.) 2 Govt.-Non Formal Education (Nos.)) 12 Protected Water Supply Source-1 0Private Secondary School (Nos.) 0 Private-Non Formal Education (Nos.) 0 Capacity Source-1 (KL) 0Govt. Senior Secondary School (Nos.) 0 Govt.-Special School for Disabled (Nos.)) 0 Protected Water Supply Source-2 0Private Senior Secondary School (Nos.) 0 Private-Special School for Disabled (Nos.) 0 Capacity Source-2 (KL) 0Govt. Degree College-Art Only (Nos.) 0 Govt.-Others(Specify) (Nos.)) 0 Protected Water Supply Source-3 0Private Degree College-Art Only (Nos.) 0 Private-Others(Specify) (Nos.) 0 Capacity Source-3 (KL) 0Govt. Degree College-Science Only (Nos.) 0 MEDICAL Protected Water Supply Source-4 0Private Degree College-Science Only (Nos.) 0 Hospital Allopathic (Nos.) 0 Capacity Source-4 (KL) 0Govt. Degree College-Commerce Only (Nos.)) 0 Hospital Alternative Medicine (Nos.) 0 Protected Water Supply Source-5 0Private Degree College-Commerce Only (Nos.) 0 Dispensary/Health Centre (Nos.) 2 Capacity Source-5 (KL) 0Govt. Degree College-Art and Science Only (Nos.)) 0 Family Welfare Centre (Nos.) 0 TRANSPORTPrivate Degree College-Art and Science Only (Nos.) 0 Maternity and Child Welfare Centre (Nos.) 0 Bus Route Road Distance (in kms.) 0Govt. Degree College-Art and Commerce Only (Nos.)) 0 Maternity Home (Nos.) 0 Pucca Road Length (in kms.) 8.0Private Degree College-Art and Commerce Only (Nos.) 0 Maternity Home Nearest facility Distance (in kms.) 6 Kutcha Road Length (in kms.) 10Govt. Degree College-Art,Science and Commerce (Nos.)) 0 T.B. Hospital/ Clinic (Nos.) 0 ENTERTAINMENT AND COMMODITYPrivate Degree College-Art,Science and Commerce (Nos.) 0 Nursing Home (Nos.) 1 Govt.-Stadium (Nos.)) 0Govt. Degree College-Law (Nos.)) 0 Veterinary Hospital (Nos.) 0 Private-Stadium (Nos.) 0Private Degree College-Law (Nos.) 0 Mobile Health Clinic (Nos.) 0 Govt.-Cinema Theatre (Nos.)) 0Govt. Degree College-University (Nos.)) 0 Others (Nos.) 0 Private-Cinema Theatre (Nos.) 0Private Degree College-University (Nos.) 0 Non-Government Out-Patient (Nos.) 0 Govt.-Auditorium/Community Hall (Nos.)) 0Govt. Degree College-Others (Nos.)) 0 Non-Government In and Out Patient (Nos.) 0 Private-Auditorium/Community Hall (Nos.) 0Private Degree College-Others (Nos.) 0 Non-Government Charitable-Hospital/Nursing Home (Nos.)0 Govt.-Public Library (Nos.)) 0Govt.-Medical College (Nos.)) 0 Non-Government Medicine Shop (Nos.) 3 Private-Public Library (Nos.) 0Private-Medical College (Nos.) 0 ELECTRICITY Govt.-Public Reading Room (Nos.)) 0Govt.-Engineering College (Nos.)) 0 Electricity-Domestic Connection (Nos.) 648 Private-Public Reading Room (Nos.) 0Private-Engineering College (Nos.) 0 Electricity-Industrial Connection (Nos.) 4 Manufactured Commodity (First) 0Govt.-Management Institute (Nos.)) 0 Electricity-Commercial Connection (Nos.) 25 Manufactured Commodity (Second) 0Private-Management Institute (Nos.) 0 Electricity-Road Lighting Connection (Nos.) 10 Manufactured Commodity (Third) 0Govt.-Polytechnic (Nos.)) 0 Electricity-Others Connection (Nos.) 10 HELP HOMESPrivate-Polytechnic (Nos.) 0 FINANCIAL Govt.-Orphanage Home (Nos.)) 0Govt.-Shorthand (Nos.)) 0 Nationalised Bank (Nos.) 1 Private-Orphanage Home (Nos.) 0Private-Shorthand (Nos.) 0 Private Commercial Bank (Nos.) 0 Govt.-Working Women's Hostel (Nos.)) 0Govt.-Typewriting (Nos.)) 0 Co-operative Bank (Nos.) 0 Private-Working Women's Hostel (Nos.) 0Private-Typewriting (Nos.) 0 Agricultural Credit Society (Nos.) 2 Govt.-Old Age Home (Nos.)) 0Govt.-Shorthand and Typewriting (Nos.)) 0 Non-Agricultural Credit Society (Nos.) 0 Private-Old Age Home (Nos.) 0Private-Shorthand and Typewriting (Nos.) 0 FIRE FIGHTINGGovt.-MS Office (Nos.)) 0 Fire Fighting Service (Status A(1)/NA(2)) 4

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ANNEXURE : VI Contd..

ANNEXURE : VII

Proposed TOR 1

PROPOSED TERMS OF REFERENCE FOR EIA STUDY

The terms of reference on the basis of which the EIA will be prepared are given below:

1.0 DATA GENERATION The data has been generated during summer Season from March r 2018 to

May 2018 by NABL accredited laboratory in accordance with the requirement of statutory agencies, is given in Table 1. The monitoring and testing has been done as per the guidelines of MOEF and the IS standards. Monitoring conducted for the following parameters:

TABLE 1 : DATA GENERATED

Sl. No. Description No. of locations

Total No of samples

1.0 AIR Ambient air monitoring (24 hourly samples), twice a week for 3 months for one season Parameters : PM10, PM 2.5, SO2, NOx,

8 (one in core

zone and 7 in buffer zone)

192

1.1

Meteorological parameters will be measured at hourly duration simultaneously at one air monitoring station for 3 months. Parameters : a. Wind speed, direction b. Relative humidity c. Temperature d. Rainfall

1 90 days

2.0 WATER Water samples to be collected from various locations (surface and ground water) in core and buffer zone (10 km radius). Parameters tested for physical and chemical and biological parameters as well as according to applicable standards

Ground water 8 and surface

water 10 samples

upto 18

3.0 SOIL 2 2 4.0 NOISE

Hourly readings taken for 24 hours (Leq) 8 8

5.0 TRAFFIC DENSITY 1 1 2.0 DATA COLLECTION 10 km radius (buffer zone), both of which comprising the ‘study area’. The

following data, through field survey and other sources generated by consultant for preparing the EIA/EMP of the proposed project with related facilities:

i Study of fauna, flora, forests and cropping pattern. ii Major habitats, ecologically sensitive areas, biosphere reserves,

wildlife sanctuaries within 15 km of the project site. iii Major industries and places of historical/ archaeological importance.

ANNEXURE : VII Contd..

Proposed TOR 2

iv Land use pattern within core zone and buffer zone. v Geo-hydrological aspects based on available data from various

secondary sources. vi Demography and socio-economic status based on last available

census data for the entire study area. vii Relevant meteorological data for the previous decades from Indian

Meteorological Department (IMD). viii Identification of water bodies, hills, roads etc. ix In case of operational plant, emission data and details of

implemented pollution control systems. 3.0 PREPARATION OF EMP The EMP will include the following details:

a. Study of the reports, like Project report, FR for plant available with the client regarding the project.

b. Present Environmental Setting The base line data generated and collected as per para 1.0 and 2.0

will be used to establish the present environmental scenario. c. Identification, prediction and evaluation of Anticipated Environmental

Impacts due to the Proposed Plant and related facilities The environmental impacts would be anticipated in core and buffer zone on:

- Topography - Climate - Water resources & quality (Surface/Ground) - Air quality - Noise Levels - Flora and Fauna - Traffic density - Land-Use - Socio-Economic Conditions - Habitats - Health, culture, human environment including public health - Occupational health and safety - Sensitive Places/Historical Monuments

The impacts would be anticipated based on experience of similar projects. d. Proposed Environmental Safeguards and Monitoring Mechanism Relevant guidelines, as per Environmental Impact Assessment (EIA)

Notification no. S.O. 1533 dated the 14th September, 2006 and its amendments till date under the Environment (Protection) Act, 1986, will be kept in mind while spelling out mitigation measures. The following aspects would be covered.

ANNEXURE : VII Contd..

Proposed TOR 3

i Reclamation of areas disturbed during construction but not required for any activity during operation.

ii Measures to control the surface and ground water pollution due to various effluents to be discharged.

iii Measures to control air pollution due to proposed activities/ operation. iv Green belt development and identification of flora species which can be

planted in and around the project. v Measures to contain noise pollution and mitigate adverse impact on

workers and habitat in core and buffer zone. vi Pronounce the improvement in socio-economic conditions and benefits

the people will get on implementation of the project. vii Measures to control health hazard of workers and surrounding

population. viii Total and specific cost of implementation of pollution control measures. ix Environmental monitoring, implementation organization and feedback

mechanism to effect mid course corrections. x Solid Waste Management

The experience of similar project(s) will be made use of for envisaging the pollution control measures by pronouncing the success in the past.

The EIA report shall be prepared as per the generic structure prescribed in

MOEF Notification dated 14.09.2006 with following chapters:

1. An introduction covering background, location, surrounding features, compliance to TOR and salient features (Chapter 1)

2. Pre-feasibility Report (to prepare Chapter 2). 3. Present Environmental Setting The base line data generated by NABL/ MOEF accredited lab will be

used to establish the present environmental scenario. (Chapter 3) 4. Identification, prediction and evaluation of Anticipated Environmental

Impacts due to the Plant and related facilities (Chapter 4) 5. Justification of project technology (Chapter 5) 6. Environmental monitoring and control mechanisms with budget

(Chapter 6) which will include - Total investment for improving/mitigating environment - Recurring expenditure during stage of production 7. Additional studies – Public consultation, 8. Risk Assessment or any other study prescribed in TOR (Chapter 8) 9. Project benefits and commitment of the company to social welfare in

surrounding areas (Chapter 9) 10. EMP (Chapter 10) 11. Summary & Conclusion (Chapter 11) 12. Disclosure of consultants engaged (Chapter 12)

ffixngtx ffintx piruitetuRUNGTA HOUSE, CHAIBASA - 833 201, JHARKHAND

Phone (06582i 256761 . E-mart rungtas@rungtamines com

19TH SEPTEMBER, 2OL8

LETTER OF AUTHORISATION

All the concerned is hereby informed that Shri Pradeep Kumar Chaturued"i, agedabout 60 years, S/o Late Ram La1 chaturvedi, resident of Borapada, nearSyamacharanpur Station, Gahamkhunti, Dhenkanal-7s9o27, odisha, is herebyauthorized by the Board of Directors in their meeting held on 19.09.2018 to makean Application on behalf of the Company for its Dhenkanal Steel Plant Divisionsituate in the Village of Jharbandh in the Dhenkanal District of Odisha to theMinistry of Environment, Forests and Climate Change, Government of India forobtaining Environmeat Clearance.

Shri Pradeep Kumar Chaturvedi is hereby authorized by the Board to sign, submitor execute requisite form(s), document(s) etc. as may be required thereto on behalfof the Company in course of obtaining this Environment Clearance for itsDhenkanal Steel Plant Division which may include obtaining TOR for EnvironmentClearance, OIA / EMP Report, Consent to Establish, Consent to Operate etc. and todo all such acts, deeds and things as required in connection therewith.

Specimea Signature of Shri PRADEEP KUll{AR CHATURVEDI

Signature Attested by Shri ASHUTOSH MOHANTY(Director)

FoT RUNGTA MINES LIMITOD

(ASHUTOSH MOHAN?YIDirector

Dtlt- o22L97o.2

Regislered Ofiice I 8A, Express 1ower,7Phone (033) 22816580. Fa: 9r-33-22815380, Emair r rungta_car@rungtamines com

_es",U

Mahesh

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ANNEXURE : VIII

\c"\

ff*xgta $intx pirwitr,bRUNGTA HOUSE, CHAIBASA- 833 201, JHARKHAND

Phorre (06562) 256761, E,marl runglas@rungtamtnes com

19TH SEPTEMBER, 2OL8

LETTER OF AUTHORISATIOI{

All the concerned is hereby informed that Shri Pradeep Kumar Chaturuedi, agedabout 60 years, S/o Late Ram Lal Chaturvedi, resident of Borapada, nearSyamacharanpur Station, Gahamkhunti, Dhenkanal-759027, Odisha, is herebyauthorized by the Board of Directors in their meeting held on 19.09.2018 to makean Application on behalf of the Company for its Dhenkanal Steel Plant Divisionsituate in the Village of Jharbandh in the Dhenkanal District of Odisha to theMinistry of Environment, Forests and Climate Change, Government of India forobtaining Environment Cledrance.

Shri Pradeep Kumar Chaturvedi is hereby authorized by the Board to sign, submitor execute requisite form(s), document(s) etc. as may be required thereto on behalfof the Company in course of obtaining this Environment Clearance for itsDhenkanal Steel Plant Division which may include obtaining TOR for EnvironmentClearance, EIA / EMP Report, Consent to Establish, Consent to Operate etc. and todo all such acts, deeds and things as required in connection therewith.

spocimea srgnature of shri PRADEEP IIIIMAR cHAruRvE ,, &rL*rt (t, V\r/hli1Tutdv'

+e""q"^xSlguature Attested by $hrt ASHU?OSH MOHANTYlDirector|

FoT RUNGTA MIIYE$ LIMITED

-g.n#*}i'(ASHUTOSH MOHANTY)

DirectorDrN- O2219702

RegiSteredoffice;8A,ExpressTower,42Asr,aiespeareSaranrKolkata-Phone (033)22816580 Fax 91 33-22815380, Emaii rungta-cal@rungtaminescom

Mahesh

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ANNEXURE : VIII Contd..

ANNEXURE : IX

PRE-FEASIBILITY REPORT

FOR

TERMS OF REFERENCE

OF

INTEGRATED STEEL PLANT

AT

VILLAGE JHARBANDH, GALPADA AND TARKABEDA

DISTRICT DHENKANAL, ODISHA

(EXTENT : 674.765 ACRES)

PRODUCTION – 2.6 MTPA STEEL

SEPTEMBER, 2018

Submitted by:

RUNGTA MINES LIMITED RUNGTA HOUSE, CHAIBASA,

JHARKHAND-833201

ANNEXURE : IX Contd..

Pre-feasibility Report for Extension of validity of EC for Integrated Steel Plant of M/s Rungta Mines Ltd. i

CONTENTS Sl. No. Description Page No. 1.0 Executive summary 1 2.0 Introduction 1

2.1 Identification of project and project proponent 1 2.2 Brief description of nature of the project 1 2.3 Need for the project and its importance to the country and or

region 2

2.4 Demand-supply gap 3 2.5 Imports vs. indigenous production 3 2.6 Export possibility 3 2.7 Domestic / export markets 4 2.8 Employment generation (direct and indirect) 4

3.0 Project description 4

3.1 Type of project including interlinked and interdependent projects

4

3.2 Location with coordinates 4 3.3 Details of alternate sites & environmental considerations 4 3.4 Size or magnitude of operation 4 3.5 Project description with process details 8 3.6 Raw material required along with estimated quantity, likely

source, marketing area of final product’s mode of transport of raw material and finished product

28

3.7 Resource optimization/recycling and reuse envisaged in the project

29

3.8 Availability of water its source, energy/ power requirement and source

29

3.9 Quantity of wastes to be generated (liquid and solid) and scheme for their management /disposal

29

3.10 Schematic representations of the feasibility drawing which give information of EIA purpose

30

4.0 Site analysis 30

4.1 Connectivity 30 4.2 Land form, land use and land ownership 31 4.3 Topography 31 4.4 Existing land use pattern 31


Pre-feasibility Report for Extension of validity of EC for Integrated Steel Plant of M/s Rungta Mines Ltd. ii

Sl. No. Description Page No.

4.5 Existing infrastructure 31 4.6 Soil classification 31 4.7 Climatic data from secondary sources 31 4.8 Social infrastructure available 32

5.0 Planning brief 32

5.1 Planning concept 32 5.2 Population projection 32 5.3 Land use planning (break up along with green belt etc.) 32 5.4 Assessment of infrastructure demand (physical & social) 33 5.5 Amenities / facilities 34

6.0 Proposed infrastructure 34

6.1 Industrial area (processing area) 34 6.2 Residential area (non processing area) 34 6.3 Green belt 34 6.4 Social infrastructure 34 6.5 Connectivity 35 6.6 Drinking water management (source & supply of water) 35 6.7 Sewarage system & Industrial waste management 35 6.8 Solid waste management 35 6.9 Power requirement & supply / source 36

7.0 Rehabilitation and resettlement plan 37 8.0 Project schedule & cost estimates 37

8.1 Project schedule 37 8.2 Cost of the project 37

9.0 Analysis of proposal (final recommendations) 37


Pre-feasibility Report for Extension of validity of EC for Integrated Steel Plant of M/s Rungta Mines Ltd. iii

LIST OF TABLES

Table No. Description Page No.

1 Power supply position 3

2 Detail of raw Material and their sources 28

3 Details of product/ finished product 28

4 Solid waste generation (TPA) 30

5 Break up of plot area 32

6 Need evaluation for villages in and around plant area 33

7 Expenditure for CSR initiatives’ undertaken by Dhenkanal steel plant

35

8 Solid waste utilisation and disposal plan 36


Pre-feasibility Report for Extension of validity of EC for Integrated Steel Plant of M/s Rungta Mines Ltd. 1

1.0 EXECUTIVE SUMMARY

Project name Integrated Steel Plant (Dhenkanal Steel Plant) Project proponent Rungta Mines Limited

Location Jharbandh, Galpada and Tarkabeda, District Dhenkanal, Odisha

Latitude 85° 17' 12" to 85° 18' 45" E Longitude 20° 45' 14" to 20° 46' 24" N Total Area 674.765 acres Present Land use break up

LAND USE IN CORE ZONE (IN ACRES)

SSll.. NNoo..

NNaammee ooff tthhee VViillllaaggee

PPrriivvaattee LLaanndd ((IInn AAccrreess))

GGoovveerrnnmmeenntt LLaannddss ((IInn AAccrreess)) GGrraanndd TToottaall ((IInn

AAccrreess)) LLeeaassaabbllee GGoocchhaarr CCoommmmuunnaall FFoorreesstt TToottaall

11 JJhhaaddaabbaannddhhaa 226611..556655 4444..003300 1177..339900 1122..333300 77..554400 8811..229900 334422..885555

22 TTaarrkkaabbeeddaa 117755..887700 99..884400 00..338800 1155..117700 00..226600 2255..665500 220011..552200

33 GGaallaappaaddaa 110033..227700 11..880000 1166..771100 88..661100 00..000000 2277..112200 113300..339900

GGrraanndd TToottaall 554400..770055 5555..667700 3344..448800 3366..111100 77..880000 113344..006600 667744..776655

Possession Taken

554400..770055 4400..004400 1199..995500 00..000000 77..880000 6677..779900 660088..449955

BBaallaannccee 00..000000 1155..663300 1144..553300 3366..111100 00..000000 6666..227700 6666..227700

Product DRI, Power, Steel, Pig Iron, Ductile Pipe, Pellets, Coke, Cement

Rated Capacity Phase-I 1.45 MTPA Steel ; Phase-II 1.4 MTPA Steel

Working Days 350

Manpower Phase-I 1300 ; Phase-II 1300

Implementation Schedule

84 Months Phase-I 48 Months; Phase-II 36 Months

Expected cost of the project

Phase-I Rs.3888. 63 Crores Phase-II Rs. 3948.27 Crores

Elevation Approximate 90 m (Core zone) 60 to 312 m ( Buffer zone)

Topography Flat



Water Requirement 2950 Cum/ Hour

Source of water Brahmani River

Power Description Phase-I 217 MW; Phase-II 168 MW Power generated shall be utilised in its proposed Steel Plant

Power Source Captive Power Plant 2.0 INTRODUCTION 2.1 Identification of project and project proponent The proposed Integrated Steel plant is one of the projects of M/s Rungta

Mines Limited (RML), which is a one of the leading and the oldest mining group of the mineral rich belt of Odisha & Jharkhand.

The company's vision & mission is to utilise its core values & strengths,

complemented with the vast experience gained, to help it keep pace with the changing times and respond to domestic & international market forces by maintaining consistent quality & dispatch schedules, making RML synonymous with reliability.

2.2 Brief description of nature of the project The nature of the project is ferrous metallurgical industries and falls under

the category of primary metallurgical industry, Thermal Power Plant, Coal Washery, Mineral Beneficiation and Coke Oven Plant which is item no. 3(a), 1(d), 2(a), 2(b) and 4(b), respectively under category “A” of the schedule of EIA Notification, 2006.

2.3 Need for the project and its importance to the country and or region Steel: India’s economic growth is contingent upon the growth of the Indian

Steel Industry. Consumption of steel is taken to be an indicator of economic development. While steel continues to have a strong hold in traditional sectors such as construction, housing and ground transportation, special steels are increasingly used in engineering industries such as power generation, petrochemicals and fertilizers.

Power: The DRI Kiln operation produces substantial quantity of hot gases,

which can be utilised to power generation, further large quantity of waste produce char. Company will also installed AFBC based Power Plant. Also The Company will install WHRB for Blast Furnace & Coke Oven Flue Hot gases. The generated power will meet the power requirement of Beneficiation Plant, Pelletisation Plant, DRI, Blast Furnace, Sinter, Coke Oven, SMS, Caster, Finished Product Mill, Ductile Pipe Plant, Producer Gas Plant, Oxygen Plant, Lime Plant, Cement Plant, Coal Washery. Thus, power demand from the state grid will be not be there and will improve the power scenario locally as well as at state level.



2.4 Demand-supply gap Steel: The Indian Steel industry has entered into new development stage

from 2005-2006 riding high on the resurgent economy and rising demand of Steel. Rapid rise in production has resulted in India to become 5th largest producer of steel. It is estimated that, India’s Steel consumption will continue to grow at nearly 16% rate annually, fuelled by the demand of construction project. The National Steel Policy envisaged steel production to reach 110 million tonnes by 2020. So considering the huge demand of steel, this project is important for partially fulfilling of demand.

Power: Over the year electricity industry has made significant progress. It

may be seen that average gap between generation and demand in India is -1.9 %. Power supply position is given Table 1.

TABLE 1

POWER SUPPLY POSITION Region Peak demand Peak met Deficit %

Jan 15 Jan 16 Jan 15 Jan 16 Dec 14 Dec 15

All Northern 42387 44124 40774 42019 -3.8 -4.6

Western 42247 45236 41553 45173 -1.6 -0.1

Southern 37004 37301 35446 36745 -4.2 -1.5

Eastern 15575 17343 15373 17198 -1.3 -0.8

North eastern 2455 2367 2202 2332 -1.03 -1.5

All India 139662 140782 135348 138075 -3.1 -1.9 Source: CEA

2.5 Imports vs. indigenous production Steel : Imports from China had adversely affected the Indian Steel Market

and the policy change by Govt of India is now leading to recovery of the sector. There is no proposal for import of steel.

Power: There is no possibility of import and will be produced at plant site. 2.6 Export possibility Steel: First priority to meet domestic demand, should also take into account

the large export possibilities. Power: There is no possibility of export of power.



2.7 Domestic/ Export markets Sponge Iron shall be used as raw material from within house for producing

steel. The steel shall sell in domestic market. Total power generated from the 385 MW will be utilised in the Beneficiation Plant, Pelletisation Plant, DRI, Blast Furnace, Sinter, Coke Oven, SMS, Caster, Finished Product Mill, Ductile Pipe Plant, Producer Gas Plant, Oxygen Plant, Lime Plant, Cement Plant, Coal Washery, etc.

2.8 Employment generation (Direct and Indirect) The manpower requirement for steel plant is 1300 people in each phase

and an equal number in indirect employment. Many more persons will also get employment in the ancillary & other

services connected with this project. 3.0 PROJECT DESCRIPTION 3.1 Type of project including interlinked and interdependent projects No 3.2 Location with Coordinates District & State : Dhenkanal & Odisha

Village : Jharbandh, Galpada and Tarkabeda Latitudes : 20° 45’ 14’’ to 20° 46’ 24’’ E

Longitudes : 85° 17’ 12’’ to 85° 18’ 45’’ N Location map showing general location, specific location and project

boundary enclosed as Annexure III of Form 1. 3.3 Details of Alternate Sites & Environmental Considerations No alternatives under consideration since the project has already been

granted environmental clearance as well as several other clearances are in advanced stage of processing. Majority of the land has been acquired. The proposed project will be incorporated within the 667.39 acres.

3.4 Size/ Magnitude of operation Plant area: 674.765 acres



Proposed Manufacturing facilities

Sl. No.






No of

Units Unit Unit



Unit Unit Capacity


C1 C2 C3 C4 C5 C6 C7 C13 C14 C15 C16 C17 C18=C7+C12+C17 1 Sponge Iron Plant 1.001 0.546 1.547

DR Kilns 2 TPD 500 MTPA 0.455 0.455 2 TPD 600 MTPA 0.546 2 TPD 600 MTPA 0.55 1.092

2 Pelletisation Plant 1 MTPA 1.2 MTPA 1.47 1 MTPA 1.2 MTPA 1.47 2.948 3 Beneficiation Plant

(Based on input) 1 MTPA 2.69 MTPA 2.7 1 MTPA 2.69 MTPA 2.7 5.4

4 Coal Washery (Based on input ROM Coal)

1 TPH 400 MTPA 2.616 1 TPH 235 MTPA 1.524 4.141

5 Mini Blast Furnace 1 CUM 600 MTPA 0.567 1 CUM 1050 MTPA 0.992 1.559 6 Sinter Plant 1 SQM 64 MTPA 0.612 1 SQM 110 MTPA 1.051 1.663 7 Coke Oven Plant 6 TPA 70000 MTPA 0.420 10 TPA 70000 MTPA 0.70 1.12 8 Steel Melting Shop MTPA 1.232 MTPA 1.232 2.464 8.1 Steel Melting Via IF-

Route MTPA 0.539 0.539

a Induction Furnace 7 Ton 20 MTPA 0.539 0.539 b Laddle Furnace 4 Ton 20 0

8.2 Steel Melting via EAF- MTPA 0.693 MTPA 1.232 1.925



Sl. No.






No of

Units Unit Unit



Unit Unit Capacity


C1 C2 C3 C4 C5 C6 C7 C13 C14 C15 C16 C17 C18=C7+C12+C17 VD-AOF Route

a Electric Arc Furnace 1 Ton 90 MTPA 0.693 1 Ton 160 MTPA 1.232 1.925 b Laddle Furnace 1 Ton 90 1 Ton 160 0

8.3 Continuous Casting Machine

MTPA 1.207 MTPA 1.207 2.415

a Billets/ Bloom Caster/Slab Caster

2 Strands 3 MTPA 1.207 1 Strands 3 MTPA 1.207 2.415

9 Finished Product Facilities

MTPA 1.450 MTPA 1.400 2.850

9.1 Rolling Mill (TMT/ Flat/ Round/ Wire Rod/ Structural Mill/ others)

MTPA 0.800 0.800 1.600

a Rolling Mill-1 4 TPA 200000 MTPA 0.800 2 TPA 300,000.00 MTPA 0.600 1.400 b Rolling Mill-2 1 TPA 200,000.00 MTPA 0.200 0.200

9.2 Strip Mill/Sheet/Coil/ Wire & Bar Mill/Wire Rope

1 TPA 450000 MTPA 0.450 1 TPA 400,000.00 MTPA 0.400 0.8500

9.3 Ductile Pipe Plant 1 TPA 200000 MTPA 0.200 1 TPA 200,000.00 MTPA 0.200 0.400 10 Producer Gas Plant Nm3/Annum 240000000 Nm3/Annum 240000000 480000000

Producer Gas Plant 10 Nm3/Hr 3000 Nm3/Annum 240000000 10 Nm3/Hr 3000 Nm3/Annum 240000000 480000000 11 Oxygen Plant MTPA 0.0350 MTPA 0.0630 0.0980



Sl. No.






No of

Units Unit Unit



Unit Unit Capacity


C1 C2 C3 C4 C5 C6 C7 C13 C14 C15 C16 C17 C18=C7+C12+C17 Oxygen Plant 1 TPD 100 Nm3/Annum 24500000 1 TPD 180.00 Nm3/Annum 44100000 68600000

12 Lime Plant MTPA 0.105 MTPA 0.1995 0.3045 Lime Plant 1 TPD 300 TPA 105000 1 TPD 570 TPA 199500 304500

13 Cement Plant MTPA 0.884 MTPA 0.802 1.686 Cement Plant alongwith Clinker Plant

1 TPD 2600 TPA 884000 1 TPD 2300 TPD 801596 1685596

14 Captive Power Plant MW 217.00 MW 168.00 385.00 14.1 WHRB Based CPP MW 67.00 MW 68.00 135.00

a WHRB (500 TPD DR Kiln)

2 TPH 50 MW 20.00 20.00

b WHRB (600 TPD DR Kiln)

2 TPH 60 MW 24.00 2 TPH 60 MW 24.00 48.00

c WHRB (MBF) 1 TPH 50 MW 11.00 1 TPH 90 MW 20.00 31.00 d WHRB (Coke Oven) 1 TPH 60 MW 12.00 1 TPH 100 MW 24.00 36.00

14.2 AFBC/CFBC based CPP MW 150.00 MW 100.00 250.00 a AFBC/CFBC 2 TPH 125 MW 50.00 50.00 b AFBC/CFBC 2 TPH 250 MW 100.00 2 TPH 250 MW 100.00 200.00



3.5 Project description with process details 3.5.1 Sponge Iron Plant (DR Plant)

Production Facilities:

Quantity Unit Capacity Days Hours Total Capacity TPA

Phase-I 2 TPD 500 340 24 340,000 2 TPD 600 340 24 408,000

Phase-II 2 TPD 600 340 24 408,000

Total 850,000

Capacity after up-gradation:

DRI Plant Unit Capacity Up-gradation Total Capacity Phase-I

2 X 500 TPD TPA 340,000 115,000 455,000 2 X 600 TPD TPA 408,000 138,000 546,000

Phase-II 2 X 600 TPD TPA 408,000 138,000 546,000

Total TPA 1,156,000 391,000 1,547,000 Iron Ore (lumps or pellets) is reduced by heating with solid carbonaceous

material, such as coal, in a Rotary Kiln to temperature of about 1000°C. After reduction, products are cooled in a drum type rotary cooler and then separated into Sponge Iron and Char by magnetic separation. Main Raw Materials- iron ore, coal and dolomite are fed to the ground hoppers with the help of pay loaders and tippers and are carried away by belt conveyors to the crusher house. Screened and crushed raw material, calibrated by weigh feeders is fed into the kiln.

The main reduction process occurs in a rotary kiln. The iron ore is reduced

by carbon monoxide generated by burning coal. The material is discharged in the Rotary Cooler at a temperature of about 700ºC, which is cooled up to 90ºC. The product of kiln is taken to a sealed rotary cooler where the product is cooled by indirect water spray. The hot water is collected and passed through the cooling tower. The evaporation loss is made up with make-up water.

3.5.1.1 Raw Material Handling System Main Raw Materials Iron Ore, Coal & Dolomite shall be fed to the ground

hoppers with the help of Pay loaders and Tippers and carried by belt conveyors to the Crusher House. Screened and Crushed Material will be carried out by belt conveyers to the stock house, having 5 days bins. The



main raw material handling system consists of iron ore crusher, vibrating screen and conveyor belts for preparation of raw material as mentioned above.

3.5.1.2 Raw Material Feed System The stored Raw Material are calibrated by Weigh Feeders separately for

Iron Ore, Feed coal, Lump Coal, Injection Coal and Dolomite and fed to the Kiln through a Rotary Airlock Feeder. The feed mix will be fed through feed tube, which shall be sealed for leakage of gases with a sealing air fan, which creates a positive pressure to avoid the gas escape. The Injection Coal system injects coal at the discharge end of rotary kiln to avoid Coal starvation with 1 bar pressure at which leakages are not possible. There is a burner system, which shall be used for initial heating up of the kiln to 400C. Calibrated quantity of combustion air is also fed through the same opening.

3.5.1.3 Main Processing System - Kiln The main reduction process occurs in a Rotary Kiln made by boiler quality

Plate. The Drive unit consists of 2 nos. main drive gearbox and 1 no. auxiliary gearbox. The kiln is supported by four nos. tyres and 08 nos. support rollers, one girth gear and two pinions. Calibrated quantity of air is fed to the kiln by shell air fans mounted on the kiln shell. The iron ore is reduced by the carbon monoxide generated by burning coal.

The product of Kiln is taken to a Sealed Rotary Cooler where the product is

cooled by indirect water spray, which is discharged to a conveyor at about 90C.

The cooler discharge is also sealed with a collecting hopper. There are 4

nos. slip seals at Kiln Inlet, Kiln Outlet, Cooler Inlet & Cooler Outlet that shall be made up of Ni hard steel. The seals are also lubricated to avoid false air entry into the kiln and gas leakage from the kiln. At inlet side of the Kiln, a back flow chute is made which is sealed with a Double Pendulum Flap Gate Valve.

3.5.1.4 Cooling System The material is discharged in the Rotary Cooler at a temperature of about

700ºC, which is cooled up to 90o C. The Drive Unit consists of one Main gearbox and one Auxiliary gearbox. The cooler is supported by Two Tyres and four support rollers. This will be cooled by indirect circulating cooling water system, the hot water shall collected and passed through the cooling tower. The evaporation loss is made up with makeup water.

3.5.1.5 Product Separation System The Cooler Discharge material consists of Sponge Iron lumps, fines and

ash of coal (char), and is taken to a vibratory screen and two nos. magnetic separators by belt conveyor.



The Magnetic and Non Magnetic material are separated here and stored in fully closed hoppers. The Product House consists of silo for sponge iron lumps, sponge iron fines and char. The char shall be used as fuel in the proposed Power Plant.

3.5.1.6 Flue Gas Cleaning and Pollution Control The flue gas coming out from the Rotary Kiln is passes through a Dust

Settling Chamber, in which the heavier dust is settled down. The bottom of the dust settling chamber is immersed in the wet scrapper water which is working as the sealing to avoid the gas leakage and false air entry. The gas next passes through the After Burning Chamber (ABC) in which the carbon monoxide and un-burnt carbon are burnt completely. The flue gas is taken to the Waste Heat Recovery Boiler (WHRB), where the recoverable heat is utilized for generation of high pressure steam. The flue gas is next passed through an electro static precipitator (ESP), where the gas is cleaned up to maximum level. The clean gas passes to the atmosphere through the Chimney with the emission level of less than 100 mg/Nm3.

The boiler bottom hoppers and E.S.P hoppers are provided with a dense

phase ash handling system. The dust collected from these hoppers is sent to an ash silo by pneumatic conveying system. Finally the stored dust in the ash silo is taken to the solid waste disposal site for storage and final disposal to brick manufacturing plants/ cement plants.

3.5.1.7 Requirement of Raw Materials The main raw materials for sponge iron production are iron ore, coal, and

dolomite.

RAW Material for DRI Plant

Phase-I Raw Material Requirement (1,001,000.00) Raw Material

Inputs Specific

Consumption T/T of Production

/Generation

Quantity (TPA)

% Charge Mix

Iron Ore 1.5 1,501,500.00 64.10% Coal 0.8 800,800.00 34.19% Dolomite 0.04 40,040.00 1.71%

Total 2,342,340.00 100.00%

Phase-II Raw Material Requirement (530,400 TPA) Raw Material

Inputs Specific

Consumption T/T of Production

/Generation

Quantity (TPA)

% Charge Mix

Iron Ore 1.5 819,000.00 64.10%



Raw Material Inputs

Specific Consumption

T/T of Production /Generation

Quantity (TPA)

% Charge Mix

Coal 0.8 436,800.00 34.19% Dolomite 0.04 21,840.00 1.71%

Total 1,277,640.00 100.00%

Total Raw Material Requirement DRI Plant (1,196,800 TPA) Raw Material Specific

Consumption Unit Required Own

Source From

Outside Purchase

Iron Ore 1.5 TPA 2,320,500. 2,293,000 27,500

Coal 0.8 TPA - - -

Dolomite 0.04 TPA 1,237,600 1,237,600 -

Total Production / Generation from DRI Plant Product Unit Phase-I

Production Phase-II

Production Total

Production

DRI TPA 1,001,000 546,000 1,547,000

Char (18% of DRI Production)

TPA 180,180 98,280 278,460

Coal Fines (12% of Coal requirement)

TPA 96,096 52,416 148,512

3.5.2 Steel Melting Shop (SMS) A brief description of the manufacturing process is as follows.

3.5.2.1 Induction Furnace (IF) Induction furnace works on the principle of Induction melting of scrap/

sponge iron with the help of electric power. An alternating electromagnetic field induces eddy current in the metal so that the electrical energy converts into heat, whose quantity depends on the resistivity of the charge. Induction furnaces operate on current of commercial frequencies (50Hz) or on current of higher frequencies from 500 to 2000 Hz. These furnaces are beneficial in steel making for low melting loss.

An induction furnace constitutes a single larger primary coil made of water-

cooled copper tube. The working voltage is impressed across the terminals of the coil. The furnace has a rammed lining. The ramming material silica mass contains should more than 96% silica and minimum of Al2O3 & Fe2O3. Before ramming the material, a steel template is kept inside the furnace and the material is rammed between the template and the insulated coil of the



induction heater. To minimize the consumption of electric power and cut down the melting period, the crucible wall must be as thin as possible. The inside of crucible lining is in contact with liquid metal while it’s outside surface contacts the water-cooled induction.

3.5.2.2 Charging In order to control the air pollution in the induction furnace, dust extraction

system will be installed. It consists of suction hood, cyclone, wet scrubber etc. Suction hood mounts on the head of furnace; the flue gases will be sucked through the hood. The blower sucks the flue gases through hood along with pipe, which connected to the cyclone and wet scrubber. The wet scrubber cools the hot gases of furnace through water spray. The nozzles spray water uniformly and perform the fog. The cyclone and scrubber separates the solid particles, dust and it falls down in the bottom of the water tank. The cool and fresh air will be exhausting through the Air Vent, in which the dust concentration will be less than 100 mg/Nm3.

3.5.2.3 Ladle Refining Furnace (LRF) The LF installation will be single station system with provision for arc

heating, inert gas stirring, and addition of ferroalloys and additives. The LF will be complete with the transformer, Ladle stirring System, Aluminium wire feeder, Carbon injecting device, additives storage and addition system, Sampling and temperature measuring device. A fume extraction and cleaning system consisting of bag filters, ID fan and chimney with the related duct work will be provided.

Production Capacity

Quantity Unit Capacity Days Hours Heats Total Capacity

TPA

IF 7 Ton 20 350 24 11 539,000

LRF 4 Ton 20

Total 539,000

Raw Material Requirement for SMS Via IF route Raw Material Unit Required Own Source From Outside

Purchase

DRI (From DR Plant )

TPA 539,000 539,000 -

Pig Iron (From MBF )

TPA 87,880 87,880 -

Scrap TPA 29,293 - 29,293



3.5.2.4 Continuous Casting Machine (CCM)

Semi-Finished Product Caster IF Rote: The Caster is complete with ladle stand, mould assembly, Strand guide segments and supports withdrawal and straightening system, mould cooling system, Cut- off equipment incl. length measuring device, marking machine etc.

Production Capacity

Quantity Strands Days Hours Total Capacity TPA

1 3 350 24 528,220

Raw Material Requirement Raw Material Unit Required Own

Source From Outside

Purchase Hot Metal (From Induction Furnace)

TPA 539,000 539,000 -

3.5.2.5 Electric Arc Furnace (EAF)

In the electric steel making process, the necessary heat is generated by electrical power. This precludes the possibility of impurities being introduced into the melt. The industrial facilities employed for converting electrical energy into heat mainly take the form of electric arc furnaces and induction furnaces.

More than 90% of electric steel is produced in the electric arc furnace with the arc providing a concentrated source of heat. In the case of the AC furnace, there are three graphite electrodes striking three arcs. Each conducts the electric current through the metallic charge to the next electrode in accordance with the supply phase sequence. In the case of the alternative DC furnace developed to commercialization over the last few years, one graphite electrode, the cathode, conducts the electrical power via the arc through the metallic charge to the bottom anode. Temperatures of up to 3500oC are created in such arcs for melting the metallic charge.

The electric arc furnace (EAF) is thus particularly well suited to the production of the full range of alloy steel grades. In the case of the basic oxygen steel making processes, on the other hand, the danger arises that the expensive alloying elements will be absorbed at least in part by the slag. Owing to their high energy consumption and limited const-efficiency, for many years electric arc furnaces were only used for the production of high grade steels. The situation changed with the increase in tapping weights (heat volume) and a significant reduction in the cost of energy, electrodes, refractory materials and investment. Today, electric arc furnaces combined with scrap metallurgy and a secondary metallurgy processes are used for production of widely varying grades of steel, and in particular the tonnage qualities.



The main components of the electric arc furnace are the furnace shell with its tapping protrusion and work/slag opening, the removable roof with the electrodes, and the tilting device. The furnace shell is refractory-lined. EAF tapping weights start at just a few tones and can in some cases reach figures of 200 ton. The work/slag opening and tapping protrusion are arranged opposite each other. The complete furnace is inclined with the aid of the tilting device for tapping purposes. Normally, the furnace is charged with its roof removed. When scrap is added, a charging bucket travels over the furnace, its bottom opens and the scrap is discharged into the furnace, so filling it in just a few minutes. During the melting process, a control system advances the slowly burning “consumable” electrodes so that they gradually “slip” in a downward direction.

The requisite electrical power cannot simply be taken from public grid. High voltage must be converted into low voltage and high amperage by means of a transformer. The most important parameter for the efficiency of an electric arc furnace is the “specific apparent power of the transformer” related to 1 tonne of charge. Values range from 300 KVA/T to 750 KVA/T (KVA/T= kilovolt ampere per tonne). In be as much as 1,000 KVA/T.

3.5.2.6 The Melting Process

The melting process performed in an electric arc furnace essentially comprise the following stages.

Charging Melting Tapping

The charging operation involves not only the input of scrap or direct reduced iron but also addition of ores, fluxes (lime, fluorspar, reducing agents, carbon) and alloying elements in the form of Ferro-alloys.

The refining process begins with ignition of the arc. Once melting has been completed, further scrap may be added. The additional injection of oxygen or other fuel gas mixtures accelerates the melting phase. The duration of the melt-down period is determined by the maximum amount of electrical power that can be transferred and the thermal load capacity of the lining. The most advance furnaces with high specific apparent power ratings (=UHP or ultra-high power furnaces) are able to achieve melt-down times of approx. 40 to 60 minutes and thus tap-to=-tap times of less than one hour.

During the refining period, iron oxides contained in the slag react with the carbon of the bath. This gives rise to gaseous carbon monoxide which causes the heat to boil and flushes impurities such as phosphorous, hydrogen, nitrogen and non-metallic compounds out of the melt.



These impurities escape as gases or are absorbed in the slag. Sulphur is not completely eliminated in this process.

3.5.2.7 Current Status Of The Electric Arc Furnace Process :

The advantages of the electric arc furnace include its ability to produce any steel grade completely irrespective of the charge (scrap, direct reduced iron, pig iron or any mixture of these).

It is particularly suitable for the production of high-grade alloyed steels. It can be readily automated, it offers a high level of electrical efficiency and requires only a low capital out-lay.

Higher installed electrical power (UHP furnaces)

Acceleration of the melting phase through the addition of pure oxygen or through the use of gas/oxygen burners

Scrap preheating with the aid of process heat from the electric arc furnace

Improved tapping (bottom tapping technique)

Water cooling of the wall, roof and electrodes

Operations with foamed slag and residual slag held over for the next heat

Automated addition of alloying elements

Automated sampling

Improved process control

Interlinking of electric arc furnace and ladle furnace (secondary metallurgy)

As the installed electrical power increased and the melting process accelerated, a solution had to be found to the problem of handling the increased heat dissipation requirement. Operations with foamed slag to protect the walls from the radiation emanating from the electric arc, the installation of water-cooled furnace panels and the application of the eccentric bottom tapping technique have contributed to solving this problem. With the eccentric bottom tapping arrangement the furnace only has to be tilted by approx. 12°, as a result, both the furnace volume and the area covered by water cooled panels can be increased. With bottom tapping, it must be ensured that the slag is drawn off separately and / or largely retained in the furnace. The DC electric arc furnace has recently been developed to commercialization. The furnace operates with just one graphite electrode in



the roof operating as the cathode, and a bottom anode in the hearth. Aside from the more favorable conditions, which prevail during the melting of scrap, this also gives rise to a somewhat lower level of consumption in terms of electrical power input, electrode loss and refractory material wear. As the graphite electrode can be more heavily utilized (power levels up to 120 kA) the resultant increase in energy input leads to shorter melting times and thus a higher level of productivity. The temperature distribution around the furnace as a whole is more even and the melt exhibits a greater degree of homogeneity thanks to the electro-dynamic stirring effect that occurs between the cathode and anode. In order to achieve favorable contract conditions with the bottom anode as quickly as possible at the beginning of the scrap melting phase, the DC furnace is operated with a molten pool (hot heel) of 10 to 20% of the heat weight. This type of plant is DC electric arc furnace with arrangement of components thus suitable more for the production of tonnage steels than of special or stainless steels with often changing chemical compositions. The investment costs overall are higher than the capital outlay required for an AC furnace. As the system per duration (main pollution) caused by the DC source is smaller than with the AC furnace, this furnace type, particularly in the form of large-volume furnaces with heat weights up to 200 T, is often preferred in those geographical locations where the electrical power supply networks are less robust (Asia, certain areas of the USA). The integration of the electric arc furnace and the downstream ladle or secondary metallurgy facilities offers the following benefits:

Transfer of all metallurgical operations to the upstream melting stage

transfer of all non-melt-related work to the ladle for post-treatment with or without vacuum (ladle furnace)

Incorporation of the electric arc furnace, secondary metallurgy facilities and the continuous casting machine within a single production line can give rise to significant savings.

The EAF and continuous caster are decoupled with the secondary metallurgical stage performing a buffer function in which the temperature of the heat, the melt analysis (alloy content, desulphurization) and cleanness separation of oxidic in

a) Liquid Steel;

b) Slag;

c) Water-Cooled Coil;

d) Crucible Lining;

e) Pouring Channel;

f) Thermal Insulation;

g) Refractory Lining or bricks Selection through a coreless induction furnace Collusions are adjusted to the final values required.



The use of powerful computers for static and/or dynamic process control enhances the cost-effectiveness with which today’s electric steel works operate. High efficiency dust removal facilities have further promoted the acceptance of this technology.

As mentioned above, owing to these developments, the electric arc furnace is now no longer used exclusively for the production of alloy steels of high cleanness. Recently a special genus of EAF plant has come into being as a components of so-called “mini mills” designed for the production of basic steel grades.

3.5.2.8 Heating Practice

After tapping the ladle is transferred to the ladle furnace station on a ladle

car where slag builders are added. Inert gas (Argon or nitrogen) bubbling is performed during all operations in ladle and during car transportation.

The first heating period will last until the slag is fused, the steel analysis is

uniform and the steel temperature is high enough to enable good sampling.

While waiting for the sample analysis, heating is continued and main alloying additions are given as soon as the laboratory analysis is received. The temperature is increased to the aim temperature before casting.

The main operations in the secondary treatment station are as follows:

a) Tapping from the melting unit b) Transport to the ladle furnace station on a ladle car & positioning c) Temperature measurement and sampling d) Slag builder addition e) Slag melting, homogenization f) Temperature measurement and sampling g) Temperature and composition correction (alloy & flux addition

depending on steel grade) h) Wire feeding, if any i) Final temperature and sampling and necessary adjustment j) Timing to meet the schedule of casting

Production Capacity

Quantity Unit Capacity Days Hours Heats Total Capacity TPA

Phase-I EAF 1 Ton 90 350 24 22 693,000 LRF 1 Ton 90 350 24

Phase-II EAF 1 Ton 160 350 24 22 1,232,000 LRF 1 Ton 160 350 24



Raw Material Requirement for SMS Via EAF route Raw Material Unit Requirement Own

Source From

Outside Purchase

(Phase-I) (Phase-II) Total

DRI (From DR Plant)

TPA 462,000 546,000 1,008,000 1,008,000 -

Hot Metal (From MBF)

TPA 330,000 811,428 1,141,429 1,063,206 78,222

3.5.2.9 Semi-Finished Product Via EAF Route Continuous Casting Machine

(CCM)

Semi-Finished Product Caster EAF Rote: The Caster is complete with ladle stand, mould assembly, Strand guide segments and supports withdrawal and straightening system, mould cooling system, Cut- off equipment incl. length measuring device, marking machine etc.

Production Capacity

Quantity Strands Days Hours Total Capacity TPA

Phase-I 1 3 350 24 679,140 Phase-II 1 3 350 24 1,207,360

Total 1,886,500 Raw Material Requirement

Raw Material Unit Required Source

Phase-I Hot Metal (From EAF Furnace) TPA 693,000 Own Plant

Phase-II Hot Metal (From EAF Furnace) TPA 1,232,000 Own Plant

Total 1,925,000 3.5.3 Mini Blast Furnace The purpose of a blast furnace is to chemically reduce and physically

convert iron oxides into liquid iron called "hot metal". The blast furnace is a huge, steel stack lined with refractory brick, where iron ore, coke and limestone are dumped into the top, and preheated air is blown into the bottom. The raw materials require 6 to 8 hours to descend to the bottom of the furnace where they become the final product of liquid slag and liquid iron. These liquid products are drained from the furnace at regular intervals. The hot air that was blown into the bottom of the furnace ascends to the top in 6 to 8 seconds after going through numerous chemical reactions. The air is blown through tuyers in the bottom portion and liquid iron is tapped from the tap hole. The blast furnace complex will consist of two blast furnaces



and two pig casting machines along with the requisite support facilities, namely the stock house, coal injection system, cast house, gas cleaning plant, de-dusting facilities, slag granulation facilities, etc.

The blast furnace flue gas is passed through Gas Cleaning Plant. A part of

the clean gas is utilized for stove of blast furnace and balance clean gas is used as a fuel in the boiler.

Production Facility

Quantity Unit Capacity Days Hours Ton/ Cum

Total Capacity

TPA Phase-I 1 CUM 600 350 24 2.7 567,000 Phase-II 1 CUM 600 350 24 2.7 992,250

Total 1,559,250

Total Raw Material Requirement for Phase-I & Phase-II Raw Material Unit Required Own Source

Iron Ore TPA 701,662.50 Own Plant Sinter TPA 1,637,212.50 Own Plant Coke TPA 951,142.50 Own Plant

Coal Dust TPA 77,962.50 Talchir Coal field Dolomite TPA 218,295.00 Local Market

Quartz TPA 81,081.00 Local Market 3.5.4 WHRB Power Generation Unit Manufacturing of Sponge Iron in Rotary Kiln generates Flue Gases at 850 –

900°C from each Kiln. Also, Blast Furnace & Coke Oven generates hot flue gases during the process. As the flue gases contain substantial sensible heat, it is proposed to utilize the heat for power generation through waste heat recovery boilers.

Power Generation Facilities for Phase-I

Facilities Connected With

Each unit Waste gases generation quantity (Nm3/Hr)

Power Generation

(In MW) WHRB 2 Nos. X 50 TPH 2 X 500 TPD

DR Kilns 120,000 20

WHRB 2 Nos. X 60 TPH 2 X 600 TPD DR Kilns

145,000 24

WHRB 1 Nos. X 50 TPH MBF 135,000 11 WHRB 1 Nos. X 60 TPH Coke Oven 159,000 12

Total 67



Power Generation Facilities for Phase-II Facilities Connected

With Each unit Waste gases generation quantity (Nm3/Hr)

Power Generation

(In MW) WHRB 2 Nos. X 60 TPH 2 X 600 TPD

DR Kilns 145,000 24

WHRB 1 Nos. X 90 TPH MBF 243,000 20 WHRB 1 Nos. X 100 TPH Coke Oven 260,000 24

Total 68 The waste heat recovery boilers consist of radiation chambers to evaporate

steam at 34 kg/cm2 pressure. The steam is carried to super heater system where the temperature is maintained at 430°C. The boiler has an economizer, which utilizes the heat of outgoing gases to raise the temperature of feed water from 100 to 200°C. The steam is used to rotate the turbine and to generate power.

The condensed steam is collected and recycled to the boilers as boiler feed

water. A DM water plant is provided for preparation of de-mineralized water for make-up to the steam-condensate cycle. The flue gases are passed through ESPs, where the dust concentration is brought down to below 50 mg/m3.

3.5.5 FBC based Power Plant It is proposed to install 150 MW (Phase-I) & 100 MW Power Plant (Phase-II)

with 2X125 TPH & 2X250 TPH FBB capacity in Phase-I & 2X250 TPH FBB in Phase-II capacity, based on Char, Coal, Coal Fines & Middlings firing. The boiler will be of natural circulation, balanced draft, single drum type and will be equipped with fluidized bed firing system. The boiler will be provided with Electrostatic Precipitator to maintain particulate concentration in flue gas at chimney outlet below 50 mg/Nm3.

Power Generation Facilities for Phase-I

Facilities Quantity Fuel Capacity (in TPH)

Power Generation

(In MW) Phase I

AFBC / CFBC 2 Char, Coal Fines, Middlings & Coal

125 50

AFBC / CFBC 2 Char, Coal Fines, Middlings & Coal

250 100

Phase II AFBC / CFBC 2 Char, Coal Fines,

Middlings & Coal 250 100

Total 250



Total Raw Material Requirement for Phase-I & Phase-II Raw Material Specific

Consumption Unit Required Own Source

Char Generation from DR Plant 18% (CV@ 2000 KCal/Kg)

1.325 TPA 278,460 Own Plant

Middlings 42.5% in CW (CV@ 2200 KCal/Kg)

1.205 TPA 1,759,908 Own Plant

Coal Fines from DR Plant 12% (CV@3000 KCal/Kg)

0.883 TPA 148,512 Own Plant

Coal (CV@4600 KCal/Kg)

0.576 TPA 843,355 Talchir Coal field

3.5.6 Coal Washery The ROM coal needs crushing and washing to reduce the ash content

before it can be used in DRI Plant. Therefore a Coal Washery is provided, which will consist of a coal crusher, screening station and washing equipment.

Production / Generation Facilities

Quantity Unit Capacity Days Hours Unit Total Capacity

Phase-I 1 TPH 400 328 20 TPA 2,616,480 Phase-II 1 TPH 235 328 20 TPA 1,524,480

Total TPA 4,140,960

Total Raw Material Requirement for Phase-I & Phase-II Raw Material Unit Required Source

Phase-I ROM Coal TPA 2,616,480 Domestic/Imported/E auction

Phase-II ROM Coal TPA 1,524,480 Domestic/Imported/E auction

Total Requirement

TPA 4,140,960

Total Production / Generation

Product Unit Phase-I Production

Phase-II Production

Total Production

Washed Coal (50%) TPA 1,308,240 762,240 2,070,480 Middlings (42.5%) TPA 1,112,004 647,904 1,759,908 Reject (7.5%) TPA 196,236 114,336 310,572 Total TPA 2,616,480 1,524,480 4,140,960

3.5.7 Coke Oven Plant Raw coal is crushed in a crusher into powdered form and charged in the

oven for the purpose of carbonisation. In the process, the volatile matter in the raw coal gets released in the form of gas and is burnt in the oven as well as in the flues and after the completion of the carbonization process, within



the duration of 36 to 38 hours, the raw coal get converted in the form of coke. The coke is then pushed out from the oven and quenched by water.


Quantity Unit Capacity Days Hours Unit Total Capacity Phase-I 6 TPA 70000 350 24 TPA 420,000 Phase-II 15 TPA 70000 350 24 TPA 1,050,000

Total TPA 1,470,000


Phase-I Coking Coal TPA 634,200 Domestic/Imported/E auction

Phase-II Coking Coal TPA 1,585,500 Domestic/Imported/E auction

Total Requirement TPA 2,219,700

3.5.8 Beneficiation Plant, Pelletisation Plant and Sinter Plant Normally iron ores with Fe content above 65% are desirable to achieve

better productivity either in blast furnace or direct reduction. Due to non availability of quality iron ore, the run-off-mine (ROM) needed to be beneficiated to lower the impurities to improve the strength of sinter and pellet quality. Hydro-cyclone is proposed for the up-gradation of iron ore as well as for de-sliming of slime particles present in the feed. Beneficiation Plant shall be of 4.2 MTPA while the Pellitisation plant shall be of 2.4 MTPA. Mixture constituting of Ore Fines, Limestone, Bentonite, Coal and slurry ore fed into disc pelletisers. Pellets then go through drying, preheating, recuperation, induration and looking before use.

A Sinter Plant of 0.650 MTPA in Phase-I & 1.051 MTPA in Phase-II will

install to match the requirement of Sinter in Blast Furnace. Sintering is an agglomeration process of Iron Ore Fines/Blue Dust, Coke Breeze and Fluxes. The sinter generated will meet 70% of the charge mix of Blast Furnace.


Quantity Unit Capacity Days Hours Total Capacity

Phase-I 1 TPD 4000 300 24 1,200,000 Phase-II 1 TPD 4000 300 24 1,200,000

Total 2,400,000

Capacity after up-gradation: Pelletization

Plant Unit Capacity Up-

gradation Total

Capacity Phase-I 4000 TPD TPA 1,200,000 274,000 1,474,000 Phase-II 4000 TPD TPA 1,200,000 274,000 1,474,000

Total TPA 2,400,000 548,000 2,948,000




Iron Ore Fines TPA 3,233,956.00 Own Mines Dolomite (Flux) TPA 41,272.00 Local Market Bentonite TPA 44,220.00 Gujarat Coke Breeze TPA 50,116.00 Domestic/Imported/ E auction Coal >= 5500 Kcal /kg TPA 98,463.20 Domestic/Imported/ E auction

Beneficiation Plant


Quantity Unit Capacity Days Hours Total Capacity Phase-I 1 MTPA 2.69 330 24 2,694,963.33 Phase-II 1 MTPA 2.69 330 24 2,694,963.33

Total MTPA 5,389,926.66

Raw Material Requirement for Phase-I Raw Material Unit Required Source

Low Grade Iron Ore Fines (0 to 5 mm) TPA 8,983,211.32 Own Mines Flocculent TPA 269.50 Local Market

Sinter Plant

Production Facility

Quantity Unit Capacity Days Hours Ton/ SQM

Total Capacity

TPA Phase-I 1 SQM 64 325 21 1.4 611,520 Phase-II 1 SQM 110 325 21 1.4 1,051,050

Total 1,662,570

Total Raw Material Requirement for Phase-I & Phase-II Raw Material Unit Required Own Source

Iron Ore Fines TPA 1,579,441.50 Own mines Coke Fines TPA 108,067.05 Domestic/Imported/ E

auction Lime Stone TPA 249,385.50 Local Market Dolomite TPA 83,128.30 Local market

3.5.9 Lime and Dolo Plant Lime stone and dolomite of size 25-55 mm will be received from mines and

stored in raw material storage yard. From there these material will be conveyed to raw materials storage bunker (capacity 650 ton). The limestone and dolomite from storage bunkers will be fed to a screen by belt conveyor



and under size limestone and dolomite of size 0-25 mm will be screened out and stored in another bunker 9 capacity 300 ton) which is meant to store the undersize limestone and dolomite will be stored onward disposal to outside agencies. Screened material of size 25-55 mm will be fed to shaft kilns by means of skip hoist through a weigh hopper. The sequence for feeding limestone / dolomite from raw materials storage bunker to screen and from screen to weight hopper is same of all the kilns. Limestone and dolomite will be calcined at temperature of 1050-1150 deg C.

The Lime & dolomite from the kiln will be discharged to two different

conveyors, which area placed below the kiln. The lime will then be screened by single deck screen to separate out 0-10 mm size and 10-55 mm size of lime and stored in separate bunkers. The sized lime 10-55 mm will be stored in 2 separate bunkers (each capacity 160 ton). The undersized lime 0-10 mm will be stored in another bunkers (capacity 130 ton). The calcined dolomite will then be single deck screen to separate out 0-10 mm sizes and will be stored in 2 separate bunkers (capacity 160 ton). The undersized dolomite 0-10 mm will be stored in another bunker (capacity 130 ton). Lime and dolomite size 10-55 mm will be conveyed to SMS through belt conveyor. Undersize lime and dolomite of size 0-10 mm will then be transported to other consumers.

Capacity of lime & dolo Plant shall be 300 TPD. Air pollution control measures are given below: 1. Raw waste gas dust before bag filter - 5-10 gm/Nm3 2. Bag filter out put dust - 45-50 mg/NM3 3. Stack height - 50 m 3.5.10 Oxygen Plant (100 TPD ) An air separation unit of 100 TPD for EAF-1 & EAF-2 capacities has been

envisaged to meet the requirement of oxygen, nitrogen and argon of the steel plant. Oxygen will be consumed in steel melting shop for oxygen blowing in EAF. In the continuous casting plant to meet the cutting needs and also to meet the general purpose requirement of various shops of the steel plant. The average demand of the oxygen with 99.6 % purity is estimated to be about 68.6 MNm3/year.

Argon will be required for rinsing in ladles and also to maintain inert

atmosphere in the mould/ tundish in the continuous casting plant and for stirring in the ladle during secondary refining. Argon will also be required for laboratory purpose. Nitrogen will be required for purging of fuel pipelines and equipments, etc.

Oxygen, nitrogen and argon will be produced by air separation process

based on low pressure cryogenic cycle and double column rectification system. List of equipment pertaining to oxygen plant is indicated below:



Sl. No.

Items Description

1. Suction air filter Dry type of high efficiency self cleaning type for use on a process compressor having dust removal efficiency of 99.9 % for 1 micron and above

2. Air compressor Centrifugal, multistage, capacity controlled by inlet guide vane

3. Pre- cooling unit consisting of air water tower

Construction – carbon steel with SS internals and inert packing complete with moisture separator.

4. Air purification unit CS vessels with SS internals with beds of alumina and molecular sieve and also regeneration heaters

5. Cold box consisting of a. Main exchanger Aluminium fin- plate type b. Exchanger turbine For Air c. Medium pressure column SS/Aluminium d. Low pressure column SS/Aluminium e. Main vaporizer/ cryogenic

heat exchanger Aluminium fin plate type

6. Miscellaneous equipment outside cold box such as deriming heater evaporation

7. Oxygen compression storage and distribution systems consisting of a. Oxygen compression by I/C systems with LOX pumps and booster

air compressor b. Gaseous oxygen storage

tanks 6 nos vertical vessel made of CS complete with isolation valve, manhole, drain, vent, pressure & temperature gauge etc.

c. Oxygen pressure regulating station

d. Oxygen filter at inlet to pressure regulating station

e. Cooling 3.5.11 Producer Gas Plant The Oil, Natural Gas, Raw Coal, LPG firing could have been an ideal source

of energy, had the Oil prices been within the range that was prevailing in sixties and earlier. But from mid-seventies onwards, due to global energy crisis, the prices of various Petro-fuels jumped up by leaps and bounds and the oil intensive industries in the country are now in a total jeopardy with respect to erosion of their profitability.

The prices are still sky-rocketing. Under such circumstances, there is no

other alternative but to change over to cheaper fuel based on Coal which is abundantly available in the country at a much cheaper rate. But from the



experience of 19th century design of Single Stage Gas Producers, which were associated with many problems, viz. low thermal efficiency, inconsistent gas quality, lower calorific value etc., industries might become a little hesitant to resort to gas produced from such Gasifiers.

Here comes the recent generation technology of Gas Producer which could

give a consistent gas supply at a much higher calorific value (1500 to 1650 Kcal/Nm< as against a C.V of only 1150 to 1250 Kcal/Nm3 from old single stage design) owing to its unique feature of pre distillation of feed coal in its deep coal bed in the extended shaft while moving downwards to the reduction and oxidation zone counter current to the upward flow of product gas which strips off the considerable quality of volatile matter from the in-coming feed stock making it semi-coke and highly reactive for a faster gasification.

Simultaneously, the product gas also becomes enriched with the volatile

matter of coal to a higher calorific value. Obviously, in this recent development, the full quantity of product gas comes out from the top of the extended shaft instead of a major quantity of the same coming from the middle of the gasifier as in the old design of double stage Gasifier.

Process description The process stages for Producer Gas are as follows: Crushed coal of the specified quality and size is carried to the top of the

bunker by means of Bucket Elevator and is put to the bunker. The screen between the bunker and the Bucket Elevator separates out fines from the feed stock of Coal which is taken down through a chute.

Coal from the bunker is fed into the Extended Shaft of the Gasifier through a

Sector Gate and two Bell Cones operated by pneumatic power cylinders which open out the Sector Gate and Bell Cones sequentially after getting signal from the LTC temperature whenever it touches the set temperature of 1400C or so.

Fed coal travels downwards and gets dried first and then gradually

preheated up to a distillation temperature of about 4500C by the product gas moving upwards which itself gets gradually cooled down and picks up the volatile matter of coal and gets auto-carbureted to a much higher calorific value before it comes out to the L.T.C off take pipes. The coal, on the other hand, gets carbonized to nearly coke stage and its reactivity increases for a faster gasification.

When the coal enters through the generator bottom shaft, reaction between

coal and (air + steam) occurs and following reactions take place from bottom oxidation zone to top reduction zones

Oxidation zones: Reaction is: C + O2 CO2 + 42643 K. Cal



Primary Reduction zone : Reactions are: C + H2O CO + H2. 19000 K. Cal C + 2H2O CO2 + 2H2. 19307 K. Cal C + CO2 2CO. 18689 K. Cal (Within 300 mm from Oxidation zone) Secondary Reduction zone : Reactions are: CO + H2O CO2 + H2. 326 K. Cal C + CO2 2CO Besides above reaction zones, there is an ash zone under the oxidation

zone through which calculated quantity of air saturated with steam enters and receives heat from the ash, gets preheated and proceeds upwards to the oxidation zone. The ash on the other hand gets cooled down before it comes out to the ash pan.

The distillation zone starts from the top of Secondary Reduction Zone and

extends upward to about 2500 mm or so in which considerable quantity of volatile matter (about more than 75%) gets stripped and picked up by gas.

At the top, there is preheating zone and above all there is drying zone. The

essential physical characteristics should be: Type : Hard Bituminous Non-caking Swelling Index : Less than 1.0 (BS) Caking Index : Maximum 5.0 (ROGA) Ash Fusion Temp. : More than 14000C Size : + 20 mm to 45 mm

Phase-I Phase-II Total (Phase-I + Phase-II)

Capacity (Nm3/Annum)

240,000,000.00 240,000,000.00 480,000,000.00

C1 C2 C3 C4 C5 C6 C7 Raw Material

Inputs Quantity

(TPA) Specific

Consumption (Kg/Nm3 of PG)

Quantity (TPA)


(Kg/Nm3 of PG)

Quantity (TPA)


(Kg/Nm3 of PG) Coal 107,040.00 0.446 107,040.00 0.446 214,080.00 0.446

Total 107,040.00 0.446 107,040.00 0.446 214,080.00 0.000 Outputs Quantity

(TPA) % Quantity

(TPA) % Quantity

(TPA) %

Coal Ash 52,449.60 49.00% 52,449.60 49.00% 104,899.20 49.00% Coal Tar 6,422.40 6.00% 6,422.40 6.00% 12,844.80 6.00% Losses on ignition & gas

48,168.00 45.00% 48,168.00 45.00% 96,336.00 45.00%

Total 107,040.00 100.00% 107,040.00 100.00% 214,080.00 100.00%



3.5.12 Cement Plant

Phase-I Phase-II Total (Phase-I + Phase-II)

Capacity (TPA) 917,374.33 755,409.05 1,672,783.38 C1 C2 C3 C4 C5 C6 C7

Raw Material Inputs Quantity (TPA)

% Quantity (TPA)

% Quantity (TPA)

%

Slag Generation from Blast Furnace

170,100.00 15.58% 297,675.00 34.24% 467,775.00 23.85%

Fly Ash from Middlings 622,722.24 57.03% 362,826.24 41.74% 985,548.48 50.25% Fly Ash from Char 117,117.00 10.73% 63,882.00 7.35% 180,999.00 9.23% Raw Material Binder 181,987.85 16.67% 144,876.65 16.67% 326,864.50 16.67%

Total 1,091,927.09 100.00% 869,259.89 100.00% 1,961,186.98 100.00% Outputs Quantity

(TPA) % Quantity

(TPA) % Quantity

(TPA) %

Cement 917,374.33 84.01% 755,409.05 86.90% 1,672,783.38 85.29% Handling Loss & others 174,552.75 15.99% 113,850.84 13.10% 288,403.60 14.71%

Total 1,091,927.09 100.00% 869,259.89 100.00% 1,961,186.98 100.00% 3.6 Raw material required along with estimated quantity, likely source,

marketing area of final product and mode of transport of raw material and Finished product

The detail of raw material and their sources is given below in Table 2. It is

planned to have own railway siding within the plant to eliminate road movement for raw materials as well as finished products.

TABLE 2

DETAIL OF RAW MATERIAL AND THEIR SOURCES Sl. No. Description Qty (MTPA) Source

1. Iron ore 8.9 Own mines 2. BF grade iron ore 0.701 Own mines 3. Coal (non coking) 6.39 Import/ domestic 4. Coal coking 1.6 South Africa

Details of product/ finished product The detail of product and captive use as well as outside sale is given in

Table 3.

TABLE 3 DETAILS OF PRODUCT/ FINISHED PRODUCT (MTPA)

Product Phase-I PHASE-II

Beneficiation Ore 2.7 2.7 Pellets 1.47 1.47 Sponge Iron 1.001 0.546 Sinter 0.612 1.051 Pig iron 0.567 0.992



Product Phase-I PHASE-II

Billets, Blooms & Slabs 1.207 1.207 Rolled product 1.45 1.40

3.6.1 Mode of transport of raw material Raw material will be transport through Rail/ Road. 3.7 Resource optimization/ recycling and reuse envisaged in the project Recirculating cooling water system shall be provided in the plant. The

recirculating cooling water pumps to the various consumers in the plant will pump cold water from the cooling tower basin. The hot water return from the consumers will return to the cooling tower for cooling and recirculation.

To meet the requirement of demineralization water as make-up water for

boiler, de-mineralization plant of suitable capacity will be provided. Water quality shall meet the Turbine and Boiler Manufacturers’ recommendation.

Entire waste water from the SMS and CPP complex shall be treated and

reused for afforestation, green belt watering, sprinkling and dust suppression. There is no liquid waste discharge from the Plant premises except during monsoon when the sprinkling and watering demand will be almost negligible.

Fly ash shall be utilised in brick making, road embankments, filling the low

lying area, etc. 3.8 Availability of water its source, energy / power requirement and source The estimated make-up water requirement for the Complete Steel Plant is

2950 cum per hour. Water allocation committee (WAC) has advised for provisional allotment of 2950 cum/hr. Final allotment is awaited. The plant shall be generate 385 MW energy in form of electricity from its captive power plant and shall be utilized in DRI, SMS, IF LR, EAF Beneficiation plant and coal washery, etc.

3.9 Quantity of wastes likely to be generated (liquid and solid) and

scheme for their management /disposal The main solid waste will be fly ash generated from power plant. Fly ash

shall be utilised in brick making, road embankments, filling the low lying area and cement plant, etc.

Electrostatic Precipitator and Bag Filters Systems will be installed for

pollution control of air emissions. Dust particles collected in the hoppers (below ESP) and conveyed pneumatically. This shall be disposed by trucks. Wastes like slag, runners & raiser from IF and scales and return scrap, etc. from Bar and Rod Mill will be recycled and reused in the process. Domestic



waste shall be generated from the plant office, organic component of which shall be composted/ vermi composted. Quantity of waste generation is given in Table 4.

TABLE 4

SOLID WASTE GENERATION (TPA) Sl. No.

Source Phase I

Phase II

Total

1 Oil and Lubricant 250 KL 250 KL 500 KL 2 DM plant resin 18 KL 18 KL 36 KL DRI Plant 3 Char 1,80,180 98,280 2,78,460 4 ESP & In plant Dust 50050 27300 77350 5 Kiln Accretion 5005 2730 7735 BLAST FURNACE 6 Slag 170100 297675 467775 7 MBF Flue Dust 28350 49612 77962 8 GCP Sludge 2835 4961 7796 SMS 9 EAF/IF & LRF Slag 10780 - 10780 POWER PLANT 10 Fly Ash 622722 362826 985548 COAL WASHERY 11 Middlings 1112004 647904 1759908 12 Reject 196236 114336 310572 COKE OVEN PLANT 13 Dust 19026 47612 66638 SINTER PLANT 14 Solids 33633 57807 91440

3.10 Schematic Representations of the Feasibility Drawing which give

Information of EIA Purpose Project feasibility report has been prepared by M/s Predominant Engineers

Pvt. Ltd., Gurugram 4.0 SITE ANALYSIS 4.1 Connectivity Road link The proposed plant is accessible by all weather road from the district

headquarter Dhenkanal and town Angul, which are located at distances of 36 km and 22 km, respectively. The site is located on NH-42, at a distance of 4.1 km, which connects Bhubaneswar to Angul.

Rail link The nearest railway station is Meramandali at a distance of 3.6 km.



Air link The nearest airport is at Bhubaneswar, which is approximately 150 km from

the site. 4.2 Land form, land use and land ownership Total land required for the project is 674.765 acres. Company has acquired

608.495 acres (comprising 540.705 acres private land + 67.790 acres Government land). Balance is pending with Tehsildar, Hindol. This will change to industrial use.

4.3 Topography The ground elevation in the study area varies from approximately 60 m to

312 m. Change in topography is envisaged due to construction of buildings, making raw material and finished good yards.

4.4 Existing land use pattern As given in section 4.2 above. 4.5 Existing infrastructure Infrastructure like office building, canteen, strengthening of roads, waste or

waste water treatment is proposed. Temporary sheds for workers will be established at the site. Jharbandh village has a primary school, power supply for domestic use. Besides this the village also have bank, post and telegraph office and cultural facilities.

4.6 Soil classification The colour of the soil is usually reddish to light black, silty clay in texture

and pH is Neutral in nature. 4.7 Climatic data from secondary sources Temperature As per the nearest IMD station, Angul (1994-2001), the mean of minimum

temperatures recorded at IMD station Angul ranges from 12.69°C in December to 21.46°C in May. The mean of maximum temperature ranges from 28.63°C in December to 40.21°C in May.

Rainfall Rainfall shows wide and erratic variations. The average annual rainfall at

IMD station Angul was recorded as 1266.80 mm from 1994 to 2001. The monsoon season is spread over the months from June to September.



Relative Humidity Relative humidity is higher during the period of SW monsoon and lower

during other months. The relative humidity varies from 40% (March) to 81% (August) during evening hours and 40% (March) to 81% (August) during morning.

4.8 Social infrastructure available Hospitals, school, community facilities are present in the villages in buffer

zone within 10 km of study area. Social infrastructures are existing as per Census.

5.0 PLANNING BRIEF 5.1 Planning concept We have not completed installation of Plant Facilities within validity for

environmental clearance.So company is applying for extension of environmental clearance validity.

5.2 Population projection During operation phase, around 1300 persons will be under direct

employment of the company in each phase. Many more persons will be indirectly engaged either on contract basis or in transportation of materials in provision of different services associated with the project. As majority of unskilled and semi-skilled persons will be from the surrounding villages, benefits will extend to the local population.

5.3 Land use planning (break up along with green belt etc.) The land use of the core area will be changed during the construction and

the operation phases. Land use of the entire project area will be changed from waste & barren and low-yield agricultural land to industrial use. The proposed integrated steel plant is spread over 667.39 acres land. During construction phase, parts of the project area will be converted into internal roads, water reservoir, buildings, green belt and plantation, etc. From almost barren land, the features of the plot will undergo changes due to construction. Break up of land use is given in Table 5.

TABLE 5

BREAK UP OF PLOT AREA Sl. No. Description Area

(Acres) Percentage

1. Plants & facilities 273.676 40.56 2. Stock yards 51.81 7.68 3. Area for solid waste disposal 55.2 8.18 4. Green belt & plantation 222.67 33.00



Sl. No. Description Area (Acres)

Percentage

5. Administration building 1.4 0.21 6. Water reservoir 30 4.45 7. Roads 40 5.93

Total 674.756 100.00 5.4 Assessment of infrastructure demand (physical & social) An assessment of the facilities available in the villages in and adjacent to

the plant site is education, hospitals, drinking water, communication and approach road. An assessment of the facilities available in the villages in the study area based on Census 2011 has been done and given in Table 6.

TABLE 6

NEED EVALUATION FOR VILLAGES IN AND AROUND PLANT AREA Sl. No.

Parameter Present Status in villages within 10 km of the project

Scope for improvement

1. Education Description - nos. Primary School -206 Middle School - 103 Secondary School - 53 Senior Secondary School - 17 Graduate college - 7 Eng college - 3 Medical college - 2 Management college - 2

Provision of middle school, in villages/ panchayats

2. Medical Primary Health sub centre - 19 Maternity & Child welfare centre - 8 TB clinic - 1 Hospital Allopathic - 3 Hospital alternative medicine -1 Family welfare centre - 3

Provision of medical facilities such as primary health centre, maternity and child welfare centre, etc. in village

3. Drinking water

Tap water - 11 Covered Well water -1 Uncovered well - 151 Hand pump - 159 Tube well - 8 River water - 68 Tank - 150 Sping water - 32

Provision of potable drinking water supply through hand pumps is available. Nearby villages can be gradually supplied with tab water as the project is established, as part of the CSR plan.

4. Power supply

Power for domestic Purpose - 147 Power for agricultural - 54

The government can be interacted with on behalf of the villages to provide power for agriculture and other purposes.

5. Communication

Post office – 26 Sub post office – 6

Transportation facility to hospital and nearest town could be maintained and strengthened.



Sl. No.

Parameter Present Status in villages within 10 km of the project

Scope for improvement

6. Approach to village

NH-25 SH- 11 Major district road - 29 Other district road - 65 Pucca Road - 102 Kuccha road - 150 Foot path - 159 Navigable river - 32

Approach road to most of the villages is already strong & pucca. Few villages where road is not well developed can be developed.

7 Banks/ credit societies

Commercial bank - 2 Agricultural credit society - 3

Provision for bank within the project site/ colony will be made

9 Cultural facilities

Sports field - 77 Sport club - 60 Cinema - 1

Provision for sports club will be made in colony and villages volunteering for maintaining a sports club can be monetarily supported as part of the CSR plan

5.5 Amenities / facilities Education, Hospitals, drinking water, power supply, post and telegraph,

banks, communication and approach roads are present in the villages in buffer zone within 10 Km of study area.

6.0 PROPOSED INFRASTRUCTURE 6.1 Industrial area (processing area) The manufacturing facilities will be established in the proposed plant

premises. 6.2 Residential area (non processing area) Residential colony will be construction near plant, approximately 1 km away

near village Jharbhandh. 6.3 Green belt The green belt equivalent to 33% of the plot area will be developed. 6.4 Social infrastructure No private social infrastructure is proposed. The social infrastructure in the

surrounding villages will be improved as a part of the CSR activities of the company. Approximate expenditure for CSR Initiatives’ undertaken by Dhenkanal Steel Plant from the period 2009-2016 are given in Table 7.



TABLE 7 EXPENDITURE FOR CSR INITIATIVES’ UNDERTAKEN BY

DHENKANAL STEEL PLANT Sl. No.

Financial Year

Health Services

Education & Communication

Infrastructure Development

Sustainable Livelihood

Culture & Sports

Total

1 2009-2010 3,09,379 3,48,669 13,38,610 624,700 4,67,298 30,88,656 2 2010-2011 16,59,266 47,22,483 18,23,930 18,22,994 34,19,228 1,34,47,901 3 2011-2012 4,26,748 30,46,861 12,07,992 16,93,468 12,98,234 76,73,303 4 2012-2013 1,31,208 20,43,672 9,16,217 19,74,623 10,26,253 60,91,973 5 2013-2014 33,953 5,83,134 3,49,355 24,65,958 2,55,941 36,88,341 Total 25,60,554 1,07,44,819 56,36,104 85,81,743 64,66,954 3,39,90,174

Sl. No.

Financial Year

Drinking Water / Health /

Eradicating Poverty

Education, Vocational Training,

Livelihood Projects

Environment / Ecology

/NRM

Culture & Tradition/ Heritage

Contribu-tion to

PMNRF & Welfare of

SC, ST, OBC etc.

Rural Development

projects

Total

1 2014-2015 59,58,159 26,74,725 15,88,825 13,11,015 0.00 26,98,780 1,42,31,504 2 2015-2016 11,94,785 43,36,026 11,30,227 16,29,241 0.00 16,34,437 99,24,716 3 2016-2017 6,39,017 9,69,720 3,78,708 2,28,254 10,000 16,00,235 38,25,934

6.5 Connectivity Refer section 4.1 6.6 Drinking water management (source & supply of water) Refer section 3.8 6.7 Sewerage system & industrial waste management Domestic waste will be generated from the manpower in plant office,

organic component of which will be composted/ vermi composted. The sewage from the Plant and colony shall be led to Sewage Treatment Plant. It will be provided with biological treatment facility to control BOD and suspended solids. The treated effluent, conforming to prescribed standards, will be continued to be used for watering plantation and in monsoons, discharged to the nearest nala. The plant will be based on zero discharge principle. All the domestic and industrial effluents will be properly treated and completely recycled in the system and maintained in future also. Thus, there is no discharge of effluents envisaged from the plant.

6.8 Solid waste management The principal solid waste produced by any steel plant is slag, scrap, scale

and dust. The dust from dust catcher of DRI unit and dust from SMS section will be recycled to the extent possible in the plant itself or sold to outside parties.



SMS slag from EAF will be used in land fill at low-lying areas. Slag from Blast furnace will be granulated and sold to the cement plants for slag cement. Scrap from SMS and other areas will be recycled in the steel plant to the extent possible. Scale and debris from HSM will be recycled to the maximum extent possible in the plant itself.

Huge quantity of solid waste is generated from power plant as ash, which is

collected through ESP, economiser and hopper. The ash is then conveyed to silo through dense phase system and it is mixed with water to make it moist in ash conditioners and finally loaded into tipper for disposal. The main users of fly ash are cement plants, brick manufacturing units, land fill sites, etc. The quantum of solid waste generation from the different units of proposed plant are given in Table 8.

TABLE 8

SOLID WASTE UTILISATION AND DISPOSAL PLAN Sl. No.

Source Phase I

Phase II

Total

Management

1 Oil and Lubricant 250 KL 250 KL 500 KL Shall be sold 2 DM plant resin 18 KL 18 KL 36 KL Send back to

manufacturer for regeneration

DRI Plant 3 Char 1,80,180 98,280 2,78,460 CFBC boiler 4 ESP & In plant Dust 50050 27300 77350 CFBC boiler 5 Kiln Accretion 5005 2730 7735 Into disposal site

BLAST FURNACE 6 Slag 170100 297675 467775 To cement plants 7 MBF Flue Dust 28350 49612 77962 Sinter plant 8 GCP Sludge 2835 4961 7796 Into disposal site

SMS 9 EAF/IF & LRF Slag 10780 - 10780 Village road

construction & low land filling, disposal

POWER PLANT 10 Fly Ash 622722 362826 985548 To cement plant/ bricks

manufacturing units of own & others

COAL WASHERY 11 Middlings 1112004 647904 1759908 CFBC boiler 12 Reject 196236 114336 310572 CFBC boiler after re-

beneficiation COKE OVEN PLANT 13 Dust 19026 47612 66638 Will be re-used in sinter

making within plant SINTER PLANT 14 Solids 33633 57807 91440 Will be re-used in sinter

making within plant Note : The waste is to be treated as by product, and therefore, maximum use of solid waste

has been proposed. 6.9 Power requirement & supply / source Refer section 3.8



7.0 REHABILITATION AND RESETTLEMENT PLAN There is displacement of 54 families which have been rehabilitated &

resettled as per R&R Policy, Government of Odisha. Compensation has already been paid through IDCO.

The plant and allied activities will provide job opportunities for eligible

persons and many will find employment in ancillary & other services connected with this project.

102 educated unemployed youths from among the affected families have

already been trained in local Industrial Training Centres (ITC) for up-gradation of their skills and employability. 170 (one hundred seventy) of them have successfully passed out in All Odisha Trade Test (AITT). 30 (thirty) other candidates presently are under training in two batches in the local Industrial Training Centres (ITC) who would pass out shortly in two years. The management is also establishing its own ITC in the locality for providing training on skill development and employability.

The proposed long term activity will open up market and opportunities

growth for self employed and cultivators. To this extent, the impact will be significantly beneficial since un-employment and under employment is the main socio-economic problem faced by the people in this area.

8.0 PROJECT SCHEDULE & COST ESTIMATES 8.1 Project Schedule The completion schedule of the all facilities within 50 months after received

Environmental Clearance. 8.2 Cost of the project The total cost of the project for Phase-I is Rs.3888. 63 Crores and for

Phase-II is Rs. 3948.27 Crores 9.0 ANALYSIS OF PROPOSAL (FINAL RECOMMENDATIONS) Local persons will be provided with either direct employment or indirect

employment. They would be mostly recruited in unskilled, semi skilled office assistant categories, etc. This will improve the economic condition of the local people. The employment of local people in primary and secondary sectors of project will upgrade the prosperity of the region.

With the advancement in technology and the stringency in permissible limits

of emission along with regular monitoring, it is possible to operate plants of this type by having minimal impact on the environment.

ANNEXURES · 2018-09-30 · [3] Sl. No. Generatio Phase-1 Phase-2 Total Capacity Plant Facilities...

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Transcript of ANNEXURES · 2018-09-30 · [3] Sl. No. Generatio Phase-1 Phase-2 Total Capacity Plant Facilities...