Heritage Foods Limited (HFL)

Presented by: N.Vamseedhar:GM op J.Rajasekhar: Manager Op MahenderMahender--Sr.ExeSr.Exe op AERIAL VIEW OF GOKUL PLANT

2 GOKUL PLANT

3 The Heritage Group was founded in 1992 by Sri Nara Chandrababu Naidu garu, with Three-business divisions viz., Dairy, Renewable Energy and NutriVet under its flagship Company Heritage Foods Limited (HFL).

4 HERITAGE PROFILE

Smt N.Bhuwaneswari Vice Chairman & Managing DirectoDirectorr Smt N.Brahmani Mrs. N Brahmani Executive Director

Heritage Golden Peacock Award for Excellence in Fortune List of 50 Most Powerful Business Woman Corporate Governance' for the year 2016 & 2017 5 VISION

Delighting Every Home With Fresh and Healthy Products and Empowering the Farmer.

6 MISSION

 To be a Nationally recognized brand for healthy and fresh products with a revenue of INR 6000 core by 2024.

 We anticipate, understand and respond to our customers needs by creating high quality products and making them available through innovative and convenient channels.

 We embrace the right technology to delight our customers.

 We are a strong supporter of balancing Economic, Social and Environmental aspects to create a better tomorrow.

 We are devoted to empowering the farming community through our unique "Relationship Farming model.

 We aim to be employer of choice by nurturing entrepreneurship, Promoting empowerment alongside transparent and open Communication.

7 HERITAGE INTRODUCTION At Present Heritage Foods Limited is with 18-Packing Stations & 199199--Chilling Centers & Bulk Coolers

3,00,000 Farmers - Supply Fresh, Pure Milk Twice a Day 199 Bulk Coolers, Mini Chilling &Chilling Centers - Procure Milk Daily 12663 Milk procurement villages 2.10 million liters per day - Chilling Capacity 2.6 million liters per day - Processing Capacity 1.7 million liters per day - Packaging Capacity 1400 Heritage Parlours - Operated by Our Franchisees 1,18,500 Retail Outlets - Sell Heritage Products From Their Stores 1.5 Million Families - Buy Heritage Milk Daily  Direct employment – 2,400  Indirect employment – 10,000

The annual turn over of Heritage Foods crossed Rs.2699.22 Crores in financial year 2019 – 20.

8 GOKUL : THE CROWN OF HERITAGE

 Was Commissioned in the Year 1996  The Biggest Plant Of Heritage  Present Capacity is 5.0 Lakhs Lits / day  Supplies Milk to Chennai and Tiruapti and Products across Several States  Accredited ISO 22000 Certification in 2007

 Accredited EIA Certification in 2010

 Certified with ISO 50001:2011 EnMS in 2015

 Winner of National Energy Conservation Awards in 2008, 2010, 2012, 2015 and 2017.

9 RANGE OF PRODUCTS

10 ENERGY POLICY

11 ISO 50001 : 2011 IMPLEMENTATION

12 EnMS Team

GOKUL EnMS team consists of 20 members

1) Production dept’s Heads -7 members 2) Utilities dept’s Heads - 5 members 3) ENCON team - 5 members 4) Plant Manager -1 member 5) QA Incharge - 1 member 6) Stores Incharge - 1 member

20 Members team work extensively and focus in such a way to lay BENCH MARKS in all ENCON aspects in Dairy Industry.

13 EnPI’s

12 Energy Performance Indicators selected each from  7 Production Departments and  5 Utility Departments

Given extensive training on variables affecting the EnPI’s in each department to give clarity on the GOAL.

This changes the attitude of total staff and the technology transferred to bottom line perfectly.

We went for Certification through BSI in 2015 and we are aiming 10% Energy Conservation every year.

14 15 PROPJECTS IMPLEMENTED IN YEAR 2017-2018

TOTAL ANNUAL Electrical Thermal NO TITLE OF PROJECT YEAR SAVINGS (RS M KWh M KCal INR in MILLION) 1 Commissioning of High efficiency 10 KL pasteurizer 2017-2018 33.928 175591.4 0.41 2 commissioning of 125 TR cooling tower for BDF 1&2 2017-2018 32.452 0 0.23

3 Retort Heat recovery by Cooling tower elimination 2017-2018 3.415 12529.13 0.18 Pressure transducer fixing for milk packing line to eliminate the 4 2017-2018 7.665 470848.3 0.52 overhead tanks 5 Commissioning of Telescopic conveyor-4 NOS 2017-2018 5.13 0 0.04

6 Commissioning of Online Check Weigher conveyor 2017-2018 0.519 0 0.00

7 Flash steam Heat recovery from FM sterilizers,kova pans and retort 2017-2018 0 147219.1 0.15 Commissioning of Pneumatic Steam control valve fixing in place of 8 2017-2018 0 954.17 0.00 manual valve 9 Installation of servo controlled voltage stabilizer 2017-2018 11.957 0 0.08

10 Cold store automation for diffuser fans stopping 2017-2018 66.43 0 0.47

20 NB steam TD3 trap replaced with float trap to avoid the steam 11 2017-2018 0 26367.6 0.03 wastage and to get better processing time Commissioned 3 stage lassi chiller for improving the process 12 2017-2018 9.921 0 0.07 performance and energy savings

13 VFD 125HP for Powder plant exhaust fan 2017-2018 23.648 0 0.17 Total 2.35 16 PROPJECTS IMPLEMENTED IN YEAR 2018-2019

TOTAL ANNUAL Electrical Thermal NO TITLE OF PROJECT YEAR SAVINGS (RS INR MKWH Mkcal MILLION)

1 Agitator shuffling to DAF collection tank 2018-2019 14.703 0 0.10

DAF outlet untreated scum shifting by gravity through piping instead 2 2018-2019 24.506 0 0.17 of pumping 3 power saving by reducing the FAT load in aeration tank 2018-2019 10.95 0 0.08 Commissioned the 5 hp kirloskar treated water pump in place of 10 hp 4 2018-2019 5.526 0 0.04 beacon pump 5 Timer arranged for DAF system skimming mechanism to save power. 2018-2019 1.46 0 0.01

DAF/IC reactor running hours reduced by keeping the ms mesh 6 2018-2019 19.165 0 0.13 strainer in the pump suction area

7 Replacement of steam heaters in place of Electrical heater 2018-2019 26.28 0 0.18

8 Commissioning of High speed packing machine 2018-2019 5.224 0 0.04

9 5 Effect Evaporator system for steam conservation measure 2018-2019 63.6878 1416092.4 2.0

10 2 no’s Dimple jacket for cream silos for avoiding pump 2018-2019 13.578 0 0.10 Commissioning of THE for milk pasteurizer in place of hot water 11 2018-2019 0 21057.96 0.02 battery

12 Installed power analyzer for measuring the quality of power 2018-2019 0.063 0 0.00

13Air purgerunit 2018-2019 0.929 0 0.01 Total 2.88 17 PROPJECTS IMPLEMENTED IN YEAR 2019-2020

TOTAL ANNUAL Electrical Thermal NO TITLE OF PROJECT YEAR SAVINGS (RS MKWH Mkcal INRMILLION) Installation of Bio-gas balloon and utilization of bio 1097085 1 gas to 3 ton IFB boiler to improve the steam fuel 2019-20 0.00 ratio 3.78 tp 4.29 1.85 Replacement of IE3 Grundfos pump in place of 2 2019-20 2.02 0 normal pump 0.01 Installation of Steam flow meter in process and 3 2019-20 0.00 773997 boiler for measurement of steam 0.77 4 Single cooling tower for both the Condensers 400 TR 2019-20 51.84 0 0.36 Combining 2 conveyors in Sachet curd with chain 5 2019-20 6.42 0 and sprocket arrangement 0.04 Commissioning of Continuous SFM batch 6 2019-20 20.42 132109 preparation against batch method 0.27 7 VFD systems for CBMM 2019-20 2.55 0 0.02 8 PHE arranged for RCM cooling to reduce load on IBT 2019-20 3.84 0 0.03 PHE for Panner cooling vat temperature 9 2019-20 1.68 0 maintenance 0.01 VFD arranged for Cooling tower fan for VAM in line 10 2019-20 3.58 0 with load 0.03 Operating Crate washers with full capacity which 11 2019-20 7.08 0 saves almost 2 hours of operation per day 0.05 12 VFD for kc6 180 HP refrigeration compressor 2019-20 3.22 0 0.02 3.46 Total 18 PROPJECTS PROPOSED TO IMPLEMENTE IN THE YEAR 2020-2021

SAVING(R SAVINGS INVESTMEN INR S (RS T INR NO TITLE OF PROJECT YEAR MKWH Million Wood in KG MILLION) MILLION) MILLION) COMMENTS Screw 205 TR for ammonia refrigeration 2020- 0.8 KWH/TR compressor planned 1 system 2021 0.24 1.76 0.00 0.00 1.76 12.60 to install in place of 1 Kwh/TR 3.8 units per litre capacity DG is 750 KVA DG 2020- going to replace with old DG 3.5 2 set(Commins) 2021 0.13 0.91 0.00 0.00 0.91 4.00 units per litres Utilization of ETP BIO GAS-800 m3 per day from UASBR and IC 100 m3 bio gas storage ballon reactor to BOILER with blower to be arranged to expansion 800-1200m3 2020- utilize the excess bio gas after 3 capacity 2021 0.00 0.00 240000.00 1.57 1.57 0.40 canteen to wood boiler ETP power reduction Separation of COD by separating by separating the milk flushout of all the milk handling flushouts from all and milk touching equipmnet process sources to and area's , if diverted to USAB optimize the DAF 2020- can eliminate running of the DAF 4 system 2021 0.15 0.00 0.00 0.00 0.00 0.20 system Air cooling Thermoking unit was planned to fix at one dedicated Air Cooling area , and all PUF to be cooled unit(Thermokig)fixing by flexible cooling system at constant plance and 2020- instead of fixing individual 5 cooling every PUF 2021 0.11 0.00 0.00 0.00 0.00 0.80 cooling system

Glycol system capacity 2020- 2Kl tank glycol system to avoid 6 enhancenment 2021 0.11 0.00 0.00 0.00 0.00 0.50 individual glycol package system

Optimization of air 2020- Air compressor optimization 7 compressors utilization 2021 0.04 0.00 0.00 0.00 0.00 0.20 plan VFD for cooling tower- 2020- 10 hp -VFD to be planned for 400 8 400 TR -10 HP fan 2021 0.01 0.00 0.00 0.00 0.00 0.03 TR cooling tower fab Total 4.2491 18.73 19 MILK PROCESS AT GOKUL PLANT

MILK TANKER MILK STORAGE PASTEURIZER HOMOGENIZER CHILLER UNLOADING AREA TANK

LOADING MILK STORAGE COLD STORAGE MILK PACKING PUF TANK ROOM MILK HANDLING PER UNIT TREND

MILK LIT/UNIT 25 21.71 20 20.07 19.69 18.21 18.93 18.93 17.38 16.98 16.88 17.90 15 10 5 0 2000-01 2001-02 2002-03 2003-04 2004-05 2005-06 2006-07 2007-08 2008-09 2009-10

MILK LIT/UNIT 23 22 21.84 21 20.87 20 20.18 19.93 20.12 19.97 19 19.18 18.82 18.59 18.64 18 17 16 2011-12 2012-13 2013-14 2014-15 2015-16 2016-17 2017-18 2018-19 2019-20 2020-21 21 22 Ours is new generation Sterilization system, where all PP bottles are kept in baskets which are in rotation and immersed in hot water.

The water is heated to 120 degrees under controlled pressure and then cooled to 40 degrees with help of Plate Heat Exchanger and Cooling tower.

In preparation of Sterilized Flavour Milk, crucial step is sterilization, where each and every bottle is exposed to 120 degree centigrade and then cooled to 40 degrees.

While heating we will use direct steam injection but, during cooling our idea is instead of using Cooling tower, we will use OHT soft water to generate Hot water which can be used at different areas.

23 Process steps as per the SUPPLIER DESIGN

1. Storage vessel filling and Heating 2. Process vessel tank filling from storage vessel 3. Process vessel Heating 4. Process vessel Holding 5. 1st Cooling & storage vessel filling 6. 2nd Cooling 7. 3rd Cooling 8. Drain 24 STERLIZER AS PER THE SUPPLIER DESIGN

25 STERLIZER AS PER OUR MODIFICAITON

Overhead tank up to 45 deg cel3000 Liters Overhead tank up to 70 deg cel5000 Liters Storage vessel up to 90 deg cel3000 Liters

26 Retort Heat recovery by Cooling tower elimination

PROJECT JUSTIFICATION FOR ENCON MEASURE

Before ENCON project For PP bottle sterilizer, as per OEM Cooling Tower of 125 TR capacity is commissioned for cooling the PP bottles in 2nd & 3rd stages of cooling from 95 to 40 degrees centigrade. Average run hours per batch is 95 min

Power consumption (555 batches in 2017) Fan motor kW -2.238 X 555 X 1.5 hrs Circulation pump-5.595 kW x 555.1.5 hrs Total power consumption-6520 units

Encon Idea Instead of cooling tower, OHT soft water is pumped through the PHE to cool the water inside the Sterilizer. We will heat 5000Lts of the OHT soft water to 70 degrees and around 3000Lts soft water sent back to OHT in the process of cooling water inside the vessel to 40 degrees by eliminating the Cooling tower fan motor operation.

27 PROJECT JUSTIFICATION FOR ENCON MEASURE

After ENCON Project After modification of ENCON project average run hours per one batch has been reduced from 95 min to 60-min

Power consumption Pump power 5.595 X 555 X 1 hrs Consumption -3105 units Energy conservation is 6520-3105=3415 units @Rs.7/- = Rs.23905/- Thermal energy savings Per batch 5000 water heat generation from 30 deg to 70 deg Celsius with a delta T of 40 deg Celsius 200000 Kcal / 670 / 3.5 = 85 kg wood Total no of batches = 555 Wood savings = 47.34 tons @Rs.3400 per tons = 1.61 Lakhs Total savings are Rs.1.85 Lakhs

28 29 BASIS for ENCON PROJECT

Gokul plant is with 10 TPD Powder plant (4 effect evaporation) commissioned in 1996 by Alfa Laval. We have plans to expand the same to 20 TPD with minimum resources. After so many discussions, we had finalized to go for additional 5th Effect evaporation in evaporating the water and converting milk to condensed milk before drying.

Earlier with 4 Effects evaporation system, Steam required to condense 7236kgs of milk to 1206kgs of 48% condensed milk is 1435kgs per hour. i.,e., 6030kgs of water to be evaporated with 1435kgs of steam i.e., per kgs of water evaporation steam required is 0.238kgs of steam

After 5th effect addition, steam required to condense 12500Kgs of milk to 2083kgs of 48% condensed milk is 1373kgs per hour only. i.,e., 10417 kgs of water to be evaporated with 1373kgs of steam i.e., per kgs of water evaporation steam required is 0.131kgs of steam only. ALMOST 55% of steam consumption reduced after the project.

30 5 Effect Evaporator system for steam conservation measure

BEFORE MODIFICATION

AFTER MODIFICAITON

31 5 Effect Evaporator system for steam conservation measure

32 5 Effect Evaporator system for steam conservation measure PROJECT JUSTIFICATION FOR ENCON MEASURE

Before SMP Production - 2087925 kgs Power consumption - 486094 kwh Steam consumption - 11836121 kgs Kwh consumed per kg - 0.232 Steam consumed per kg - 5.66

After SMP Production - 2894900 kg Power consumption - 616417 kwh Steam consumption - 14875380kg Kwh consumed per kg - 0.21 Steam consumed per kg - 5.1

Net savings are Power savings - 63688 Units @Rs.7/- per KWH – 4.45 Lakhs Wood savings - 470 Tons @ Rs.3400/- per Tons – 15.99 Lakhs Total Cost savings - 20.44 Lakhs 33 34 ETP plant Overview

35 We had commissioned 750KLD Effluent Treatment Plant as a part of expansion from 3.5LLPD milk handling to 5.0 LLPD.

The newly commissioned project is 4th Generation IC reactor from an MNC Paques through Aqua Matrix inaugurated by our mentor Sri Nara Chandrababu Naidu on 14th Jan’2019.

The new project contains DAF (Dissolved Air Floatation system) and IC reactor. Our Old UASBR (Upflow Anaerobic Sludge Bed Reator) is converted as Solid sludge digester to digest solid sludge coming from DAF system.

The BIO GAS generated from both IC reactor and UASBR is connected to our Canteen and Employee quarters. We are utilizing the Biogas for the above purposes for only 6hours a day and balance time the biogas is flaring at our ETP itself.

36 3 ton IFB Performance improvement after installation of bio gas ballon

IFB-30 boiler performance in the year 2018-2019 IFB-30 boiler performance in the year 2019-2020

Steam Steam generated Wood generated Wood Savings per day in consuption Steam to per day in consuption Steam to Wood in KG Month Kg in Kg fuel ratio Month Kg in Kg fuel ratio per day Apr-18 50923 13507 3.77 May-18 48770 12936 3.77 May-19 48570 11151 4.36 1698 Jun-18 50480 13390 3.77 Jun-19 59116 13853 4.27 1786 Jul-18 52702 13942 3.78 Jul-19 58546 13529 4.33 1959 Aug-18 49454 13118 3.77 Aug-19 58044 13875 4.18 1481 Sep-18 49653 13206 3.76 Sep-19 58699 13744 4.27 1785 Oct-18 49856 13437 3.71 Oct-19 59285 14159 4.19 1525 Nov-18 54092 13969 3.87 Nov-19 54239 12840 4.22 1509 Dec-18 50266 13195 3.81 Dec-19 45226 9727 4.65 2238 Jan-19 45760 12261 3.73 Jan-20 42725 10004 4.27 1299 Feb-19 42730 11342 3.77 Feb-20 46769 11069 4.23 1304 Mar-19 45211 11812 3.83 Mar-20 47866 11336 4.22 1327 Average 49158 13010 3.78 579085 12299 4.29 1628 37 Encon team suggested to install a 50 M3 gas balloon to store the BIO gas and through blower connect the Bio gas to different destinations like Canteen, employee quarters and balance Biogas to be given to Multi star Thermax Boiler (IFB30D) instead of flaring to the atmosphere.

We had given the biogas to 50M3 gas balloon and connect the balloon to the destination with the following * 100m3/Hr bio gas blower which is equipped with * Piping with expansion joint to remove moisture * VFD to give consistent supply and * Auto switch off if the pressure crosses 0.5kg/sqcm in view of safety.

With this arrangement our steam fuel ratio has been enhanced from 3.7 to 4.2 kg of steam per kg wood consumption We have saved around 1628 Kg of wood per day after using for our Canteen and Employee qurters. 38 Installation of Bio-gas balloon and utilization

Open firing, gas flare 50 m3 gas balloon

IFB -30 Boiler Canteen burner

39 PROJECT JUSTIFICATION FOR ENCON MEASURE

Impact of the ENCON Project

In the ENCON proejct, we had connected the Biogas Balloon to the IFB30D boiler with Blower, Piping, NRV mechanism, Flame arrester, Moisture traps through expansion joints, Auto switch off mechanism with a set point of 0.5kgs/sqcm and indication at the Boiler to have an idea for the Boiler staff.

Thermax IFB 30D boiler is with maximum pressure of 10.56kg/sqcm with an operating limits of 9.5 to 7.5kg/sqcm.

IFB boiler performance is 3.77kgs of steam per Kg of wood for the previous year. After the Biogas given to the Boiler, the un burnt is less and the fuel ratio increased to 4.29 kgs of steam per Kgs of Wood.

Steam generated from May’19 to March’20 is 17635 Tons. Wood consumed if we operate the boiler with Fuel ratio of 3.78Kgs 4665 Tons Wood consumed after Biogas line is with the Fuel ratio of 4.29kgs 4120 Tons Saving of Wood for the year 2019-20 is 545 Tons Savings in Rs @Rs.3400/- per tons of wood is Rs.1853000/-

40 PLANT ENERGY OVERVIEW 2017-2018

AVERAGE Energy consumption for 2017-2020 0.81%

45.32 % WIND% EB% 53.87 % DG%

41 SPECIFIC ENERGY CONSUPTION SECTION WISE

Section wise MKwH for year 2017-18 7000 6096 6000

5000

4000

3000 2633 2017-18 2000 846 1000 790 624 315 308 56 117 47 145 61 152 0

42 SPECIFIC ENERGY CONSUPTION EnPI’s

Section wise MKwH for year 2018-19 7000 6273 6000

5000

4000 2942 3000 2018-19 2000

1000 753 768 585 327 75 236 131 49 152 92 162 0

43 SPECIFIC ENERGY CONSUPTION EnPI’s Section wise MKWh for year 2019-20 7000 6352 6000

5000

4000 3305 3000 2019-20 2000

1000 876 643 503 283 69 94 131 47 164 83 153 0

44 SPECIFIC ENERGY CONSUPTION EnPI’s section wise

Sachet curd EnPI Cup curd EnPI

95 45 40 90 90 40 90 34.634.6 35 84.64 83.91 30 30 85 84.64 30 28 28 85 83.91 26 26 ENPI 25 ENPI 77.22 BASE LINE 80 20 BASE LINE 77.22 TARGET 15 TARGET 75 10 5 70 0 2017-18 2018-19 2019-20 2017-18 2018-19 2019-20 Process curd EnPI Powder EnPI

205 1040 200 1020 200 1020 1000 1000 998998 195 1000 190 190 975975 190 ENPI 980 ENPI 184184 184 184 185 BASE LINE 960 951951 BASE LINE 181181 TARGET TARGET 180 940

175 920

170 900 2017-18 2018-19 2019-20 2017-18 2018-19 2019-20 45 SPECIFIC ENERGY CONSUPTION EnPI’s Byproducts EnPI 9 B&Ghee EnPI 8 1010 8 7.61 7.6 7.5 1000 1000 1000 6.9 6.9 1000 7 990 6 6 5.6 5.6 980 5 ENPI 970 967 967 ENPI 4 957 957 BASE LINE 960 953 953 BASE LINE 3 TARGET 950 TARGET 2 940 1 930 920 0 2017-18 2018-19 2019-20 2017-18 2018-19 2019-20

4 Ton boiler EnPI 3 Ton boiler EnPI 3.61 3.6 3.6 3.6 3.6 3.82 3.8 3.8 3.59 3.58 3.58 3.8 3.58 3.78 3.57 3.78 3.57 3.77 ENPI 3.56 3.76 3.753.75 3.75 3.55 BASE LINE ENPI 3.55 3.54 3.54 TARGET 3.74 3.73 3.73 BASE LINE 3.54 TARGET 3.53 3.72 3.52 3.7 3.51 2017-18 2018-19 2019-20 3.68 2017-18 2018-19 2019-20 46 SPECIFIC ENERGY CONSUPTION EnPI’s

ETP EnPI Water EnPI 600 2 1.8 500 1.8 500 1.651.641.64 1.621.651.62 1.62 440 1.6 1.5 400 400 371 384 400 350 350 360 1.4 ENPI 1.2 300 ENPI BASE LINE 1 BASE LINE 0.8 200 TARGET TARGET 0.6 100 0.4 0.2 0 0 2017-18 2018-19 2019-20 2017-18 2018-19 2019-20

PF EnPI Lighting EnPI 1.0002 445 441 1 1 1 440 437 437 437 1 0.9999 0.99990.9999 0.9999 0.9998 435 0.9998 430 425 425 425 0.9996 ENPI 425 422 ENPI 420 0.9994 0.9993 BASE LINE 416 BASE LINE TARGET 415 TARGET 0.9992 410 0.999 405 0.9988 400 2017-18 2018-19 2019-20 2017-18 2018-19 2019-20 47 UTILIZATION OF RENEWABLE ENERGYS SOURCES Wind energy MKwh 3650 3616.628 3600

3550

3500

Wind energy MKwh 3450 3432.252 3418.777 3400

3350

3300 2017-2018 2018-2019 2019-2020 48 EMISSION DATA Kg Co2 per ton of production 43.5 43.2 43 42.57 42.5

41.5

41 Kg Co2 per ton of production 40.5 40.28 40

39.5

38.5 Year2017-2018 Year2018-2019 Year2019-2020 49 BENCH MARKING

Kwh/Ton of Production 150 121 100 65 52.07 50 Kwh/Ton of Production

0 HERITAGE DAIRY JERSEY DAIRY TIRUMALA DAIRY

Kcal/ Ton of Production 400000 378517 300000 200000 156474 160000 Kcal/ Ton of Production 100000 0 HERITAGE DAIRY JERSEY DAIRY TIRUMALA DAIRY 50 GREEN SUPPLY CHAIN

Canteen waste is being utilized in USSBR and BIO gas is generated to use in the Canteen cooking purpose

75-100 kg of waste is being generated with a canteen capacity of 400 meals per day including Tiffin's

Near by 200 m3 of gas is generating and this gas is utilized in canteen only

51 INNOVATIVE AND NEW TECHNOLOGY IMPLEMENTED Yakogawa monitoring, Online weighing flue gas analyser

52 Team work, Employee Involvement & Monitoring

 Energy monitoring system

Energy meters-80 no’s Steam flow meters-2 no’s Water flow meteres-30 no’s Hot water flow meters-2 no’s EnPI Daily update on watts up by energy team Monthly Energy Review

53 Team work, Employee Involvement & Monitoring

EXTERNAL TRAINING Energy conservation, Six sigma ,Process loss . ISO 50001 INTERNAL training

54 Long term vision on EE

205 TR 0.8KWh/TR Frick chiller Falling film chillers hydropnematic pumping unit for chill water circulation 6 Ton automated steam boiler 750 KVA high efficient DG set ETP plant optimization

55 AWARDS & CERTIFICATION

56 Golden Peacock Award for Excellence in Corporate Governance” for the year 2017,

The Golden Peacock Award Trophy and a Certificate was received by Smt. N. Bhuvaneswari, Vice Chairperson and Managing Director at a specially organized 'Golden Peacock Awards Presentation Ceremony', held on Wednesday, 25th October 2017, 57 FTAPCCI Excellence Awards in Corporate Social Responsibility.- 25th June, 2017

Our Company was declared as the Winner of the FTAPCCI Excellence Awards in Corporate Social Responsibility. The award was given by Federation of Telangana and Andhra Pradesh Chambers of Commerce and Industry. 25th June, 2017 . 58 Golden Peacock Award for Excellence in Corporate Governance' for the year 2016

Heritage Foods Bags "Golden Peacock Award for Excellence in Corporate Governance' for the year 2016" received by Smt. N Bhuvaneswari, Vice Chairperson & Managing Director 59 ENERGY CONSERVATION AWARD 2008

60 ENERGY CONSERVATION AWARD 2010

61 ENERGY CONSERVATION AWARD 2012

62 ENERGY CONSERVATION AWARD 2014

63 1st Prize in National Energy Conservation Awards-2015

64 1st Prize in National Energy Conservation Awards-2016

65 2nd Prize in National Energy Conservation Awards-2017

66 CERTIFICATIONS