Detailed Project Report (DPR) on Hydrogen Production (99.9% Pure) and Oxygen as by Product (Cap: 21,360 Kg/Day)

Detailed Project Report (DPR) on Hydrogen Production (99.9% Pure) and Oxygen as by Product (Cap: 21,360 Kg/Day)
4490
Original
India
Countries
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Industry Overview

Hydrogen can be produced from diverse domestic resources, including fossil fuels, biomass, and water electrolysis powered by electricity. Its environmental impact and energy efficiency depend significantly on the production pathway and the energy resources used. Several hydrogen production projects and technology-development initiatives are focused on reducing production costs and improving efficiency.

Natural gas reforming is one of the most common hydrogen production methods. In this process, natural gas reacts with high-temperature steam to produce synthesis gas, a mixture containing hydrogen, carbon monoxide, and a small amount of carbon dioxide. The carbon monoxide subsequently reacts with water to generate additional hydrogen. Natural gas reforming using steam has historically accounted for the majority of hydrogen produced annually in the United States.

Synthesis gas can also be produced from coal or biomass through gasification, in which the feedstock reacts with high-temperature steam and oxygen under pressure. The resulting synthesis gas contains hydrogen and carbon monoxide, with further processing used to separate and increase the hydrogen content. The project report also examines electrolysis, renewable liquid reforming, fermentation, advanced water-splitting technologies, hydrogen distribution, electrolyzer technologies, water treatment, plant layout, location factors, safety, project implementation, and project economics.

Cost Estimation

Particulars Value
Plant Capacity 21,360 KG/Day
Land & Building (40,000 sq.mt.) Rs. 24.00 Cr
Plant & Machinery Rs. 302.93 Cr
Working Capital for 1 Month Rs. 12.22 Cr
Total Capital Investment Rs. 343.91 Cr
Rate of Return 35%
Break Even Point 58%

Content Index

INTRODUCTION
THERE ARE SEVERAL WAYS TO PRODUCE HYDROGEN:
NATURAL GAS REFORMING/GASIFICATION:
ELECTROLYSIS:
RENEWABLE LIQUID REFORMING:
FERMENTATION:
SEVERAL HYDROGEN PRODUCTION METHODS ARE IN DEVELOPMENT:
HIGH-TEMPERATURE WATER SPLITTING:
PHOTOBIOLOGICAL WATER SPLITTING:
PHOTOELECTROCHEMICAL WATER SPLITTING:
DISTRIBUTION OF HYDROGEN
CURRENTLY, HYDROGEN IS DISTRIBUTED THROUGH THREE METHODS:
PIPELINE:
HIGH-PRESSURE TUBE TRAILERS:
LIQUEFIED HYDROGEN TANKERS:
DETAILS OF ELECTROLYSIS FOR HYDROGEN PRODUCTION
POLYMER ELECTROLYTE MEMBRANE ELECTROLYZERS
ALKALINE ELECTROLYZERS
SOLID OXIDE ELECTROLYZERS
GLOBAL MARKET OVERVIEW OF HYDROGEN
REGIONAL INSIGHTS
FUTURE OF GREEN HYDROGEN
POTENTIAL FOR GREEN HYDROGEN ADOPTION IN INDIA
POTENTIAL ROADMAP FOR GREEN HYDROGEN ADOPTION IN INDIA
(SOURCE: NITI AAYOG)
INTERNATIONAL CLIMATE SUMMIT:
HYDROGEN FUEL TRAINS:
HYDROGEN FUEL BUSES:
GREEN HYDROGEN MOBILITY PROJECT:
FUTURE OUTLOOK
PRODUCTION OF HYDROGEN USING DIFFERENT FEED STOCK
HYDROGEN FROM FOSSIL FUELS
PRODUCTION FROM NATURAL GAS
TABLE: COMPARISON OF TECHNOLOGIES FOR H2 PRODUCTION
FROM NATURAL GAS
PRODUCTION FROM COAL
HYDROGEN FROM SPLITTING OF WATER
WATER ELECTROLYSIS
FIGURE: FUTURE POTENTIAL COSTS OF ELECTROLYTIC HYDROGEN
ALKALINE ELECTROLYSIS
FIGURE: PROCESS DIAGRAM OF ALKALINE ELECTROLYSIS
POLYMER ELECTROLYTE MEMBRANE (PEM) ELECTROLYSIS
HIGH-TEMPERATURE ELECTROLYSIS
PHOTO-ELECTROLYSIS (PHOTOLYSIS)
FIGURE: PRINCIPLE OF PHOTO-ELECTROLYTIC CELL
PHOTO-BIOLOGICAL PRODUCTION (BIOPHOTOLYSIS)
FIGURE: PRINCIPLE OF PHOTO-BIOLOGICAL HYDROGEN PRODUCTION
HIGH-TEMPERATURE DECOMPOSITION
THERMO-CHEMICAL WATER SPLITTING
FIGURE: PRINCIPLE DRAWING OF IODINE/SULFUR THERMO
-CHEMICAL PROCESS
ELECTROLYSIS FOR H2 PRODUCTION
WATER ELECTROLYSIS:
COMMERCIAL TECHNIQUES WATER ELECTROLYSIS
ALKALINE WATER ELECTROLYSIS
ALKALINE WATER ELECTROLYSER
INSIDE A WATER ELECTROLYSER
SOLID POLYMER ELECTROLYTE ELECTROLYSIS
ALKALINE MEMBRANE CELLS
STEAM ELECTROLYSIS AT 1000OC:
TECHNOLOGIES FOR WATER ELECTROLYSIS
HIGH TEMPERATURE STEAM ELECTROLYSIS (SOEC)
DETAILS OF ELECTROLYSIS
ALKALINE ELECTROLYSIS (AEL)
PROTON EXCHANGE MEMBRANE ELECTROLYSIS (PEM)
SOLID OXIDE ELECTROLYSER (SOE)
ANION EXCHANGE MEMBRANE ELECTROLYSIS (AEM)
METHODS OF WATER TREATMENTS
METHODS OF WATER TREATMENT (REVERSE OSMOSIS):
REVERSE OSMOSIS:
BASIC COMPONENTS OF A COMMON REVERSE OSMOSIS SYSTEM
COLD WATER LINE VALVE:
REVERSE OSMOSIS MEMBRANE:
AUTOMATIC SHUT OFF VALVE (SOV):
CHECK VALVE:
FLOW RESTRICTOR:
STORAGE TANK:
FAUCET:
ADVANTAGES
DISADVANTAGES
ION EXCHANGE RESINS
MINI DM PLANT SPECIFICATIONS:
APPLICATIONS:
ADVANTAGES AND LIMITATIONS
PRINCIPLES OF PLANT LAYOUT
STORAGE LAYOUT:
EQUIPMENT LAYOUT:
SAFETY:
PLANT EXPANSION:
FLOOR SPACE:
UTILITIES SERVICING:
BUILDING:
MATERIAL-HANDLING EQUIPMENT:
RAILROADS AND ROADS:
MAJOR PROVISIONS IN ROAD PLANNING FOR MULTIPURPOSE
SERVICE ARE:
PLANT LOCATION FACTORS
PRIMARY FACTORS
1. RAW-MATERIAL SUPPLY:
2. MARKETS:
3. POWER AND FUEL SUPPLY:
4. WATER SUPPLY:
5. CLIMATE:
SPECIFIC FACTORS
6. TRANSPORTATION:
A. AVAILABILITY OF VARIOUS SERVICES AND PROJECTED RATES
7. WASTE DISPOSAL:
8. LABOR:
9. REGULATORY LAWS:
10. TAXES:
11. SITE CHARACTERISTICS:
12. COMMUNITY FACTORS:
13. VULNERABILITY TO WARTIME ATTACK:
14. FLOOD AND FIRE CONTROL:
EXPLANATION OF TERMS USED IN THE PROJECT REPORT
1. DEPRECIATION:
2. FIXED ASSETS:
3. WORKING CAPITAL:
4. BREAK-EVEN POINT:
5. OTHER FIXED EXPENSES:
6. MARGIN MONEY:
7. TOTAL LOAD:
8. LAND AREA/MAN POWER RATIO:
PROJECT IMPLEMENTATION SCHEDULES
INTRODUCTION
PROJECT HANDLING
PROJECT SCHEDULING
PROJECT CONSTRUCTION SCHEDULE
TIME SCHEDULE
ADDRESSES OF PLANT AND MACHINERY SUPPLIERS

Appendix

APPENDIX – A:
1. PLANT ECONOMICS
2. LAND & BUILDING
3. PLANT AND MACHINERY
4. OTHER FIXED ASSESTS
5. FIXED CAPITAL
6. RAW MATERIAL
7. SALARY AND WAGES
8. UTILITIES AND OVERHEADS
9. TOTAL WORKING CAPITAL
10. TOTAL CAPITAL INVESTMENT
11. COST OF PRODUCTION
12. TURN OVER/ANNUM
13. BREAK EVEN POINT
14. RESOURCES FOR FINANCE
15. INSTALMENT PAYABLE IN 5 YEARS
16. DEPRECIATION CHART FOR 5 YEARS
17. PROFIT ANALYSIS FOR 5 YEARS
18. PROJECTED BALANCE SHEET FOR (5 YEARS)

Frequently Asked Questions

The main hydrogen production methods include natural gas reforming or gasification, electrolysis, renewable liquid reforming, and fermentation.

The report also discusses emerging approaches such as high-temperature water splitting, photobiological water splitting, photoelectrochemical water splitting, photo-electrolysis, biophotolysis, high-temperature decomposition, and thermochemical water splitting. The environmental performance and energy efficiency of hydrogen vary according to the feedstock, process technology, and energy source used for production.

Hydrogen can be produced from natural gas by reacting the gas with high-temperature steam to create synthesis gas.

The synthesis gas contains hydrogen, carbon monoxide, and a small amount of carbon dioxide. The carbon monoxide can then react with water to produce additional hydrogen. Natural gas reforming using steam is described in the report as one of the most common and economically established hydrogen production routes. Gasification provides another route for producing synthesis gas from coal or biomass using high-temperature steam and oxygen under pressure.

Water electrolysis produces hydrogen by using electricity to split water into hydrogen and oxygen.

The report covers several electrolyzer technologies, including alkaline electrolysis, polymer electrolyte membrane electrolysis, solid oxide electrolysis, and anion exchange membrane electrolysis. High-temperature steam electrolysis is also discussed. When the electricity used for electrolysis comes from renewable sources, the resulting hydrogen is commonly associated with the term green hydrogen, although the overall environmental performance depends on the characteristics of the electricity supply and the complete production system.

The report covers alkaline, polymer electrolyte membrane, solid oxide, and anion exchange membrane electrolyzer technologies.

Alkaline electrolyzers are a well-established technology, while polymer electrolyte membrane systems use a solid polymer electrolyte and are discussed separately in the report. Solid oxide electrolyzers operate at high temperatures and are considered under high-temperature steam electrolysis. Anion exchange membrane systems are also included among the water electrolysis technologies. The selection of a suitable technology depends on process requirements, operating conditions, water quality, electricity supply, integration needs, and project objectives.

Water treatment is important because electrolyzers require suitable water quality for reliable operation.

The report includes reverse osmosis, ion exchange resins, and mini demineralization plant specifications as part of its water-treatment discussion. It also identifies common reverse-osmosis system components such as valves, membranes, automatic shut-off valves, check valves, flow restrictors, storage tanks, and faucets. Proper water treatment can support equipment performance and help control impurities entering the electrolysis system, with the appropriate treatment configuration depending on the source-water characteristics and electrolyzer requirements.

A hydrogen plant location should be evaluated against raw-material supply, markets, power and fuel, water, climate, transportation, waste disposal, labor, regulations, taxes, and site characteristics.

The report also identifies community factors, vulnerability to wartime attack, and flood and fire control as specific considerations. Plant planning should additionally account for storage and equipment layouts, safety, future expansion, floor space, utility servicing, buildings, material-handling equipment, railroads, and roads. Considering these factors together helps support practical plant operations, logistics, safety, and future development.

The report specifies a plant capacity of 21,360 KG/Day and provides project cost and economic indicators.

The stated figures include Land & Building (40,000 sq.mt.) of Rs. 24.00 Cr, Plant & Machinery of Rs. 302.93 Cr, Working Capital for 1 Month of Rs. 12.22 Cr, and Total Capital Investment of Rs. 343.91 Cr. It also reports a Rate of Return of 35% and a Break Even Point of 58%. These figures are reproduced exactly from the supplied project report and have not been recalculated or independently estimated.

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