Urea
245
05/01/2025
1.Physical and Chemical Properties
1.1Fundamental Properties
- Molecular Characteristics:
- Chemical formula: CO(NH₂)₂
- Molecular weight: 60.06 g/mol
- Structure: Planar molecule with carbonyl group bonded to two amino groups
- Melting point: 132.7°C (pure)
- Heat of fusion: 247 J/g
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- Solubility Parameters:
- Water solubility: 119g/100g water at 25°C, 167g/100g at 40°C, 251g/100g at 80°C
- Solution enthalpy: -57.8 kJ/mol (highly endothermic dissolution)
- Solubility in alcohols: 5-15g/100g (methanol, ethanol)
- Solubility in non-polar solvents: Negligible
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- Physical Characteristics:
- Commercial forms: White crystalline solid (prills or granules)
- Crystal structure: Tetragonal
- Bulk density: 0.72-0.80 g/cm³ (depending on form)
- Angle of repose: 32-38° (affecting flow properties)
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1.2 Chemical Reactivity
- Hydrolysis: Conversion to ammonium carbamate/carbonate in aqueous solutions
- First-order rate constant: 10⁻⁶ to 10⁻⁷ s⁻¹ at 25°C
- pH effect: Rate increases in acidic and basic conditions
- Temperature effect: Rate doubles every 10°C increase
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- Thermal Decomposition: Occurs above 132.7°C
- Initial decomposition: Formation of isocyanic acid and ammonia
- Secondary reactions: Biuret formation at 150-200°C (undesired in fertilizer)
- Decomposition products: NH₃, HNCO, cyanuric acid, biuret, CO₂
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1.3 Analytical Characterization
- Quantitative Analysis:
- Spectrophotometric methods: Modified Berthelot reaction (sensitivity: 0.1-10 mg/L)
- Enzymatic methods: Urease-based analyses (specificity: >98%)
- Chromatographic techniques: HPLC and GC methods (detection limit: 0.01-0.05%)
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- Structure Verification:
- IR spectroscopy: Characteristic bands at 3500-3200 cm⁻¹ (N-H), 1680-1630 cm⁻¹ (C=O)
- NMR spectroscopy: ¹H-NMR (5.5-6.0 ppm), ¹³C-NMR (160-165 ppm)
- X-ray diffraction: Unit cell parameters a=5.59Å, c=4.69Å
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- Purity Assessment:
- Biuret content: TypicallyFree ammonia:Moisture content:
2.Production Technologies
2.1Conventional High-Pressure Processes
- Basic Chemistry: Two-step reaction between ammonia and carbon dioxide
2NH₃ + CO₂ ⇌ NH₂COONH₄ (exothermic)
NH₂COONH₄ ⇌ (NH₂)₂CO + H₂O (endothermic)
- Operating Parameters: 130-250 bar pressure, 170-200°C temperature
- Process Variants: CO₂ stripping (Stamicarbon), NH₃ stripping (Saipem), self-stripping (TEC)
- Conversion Efficiency: 60-70% per pass, >99% with recycle systems
- Energy Consumption: 26-30 GJ/ton urea (total steam and electricity)
2.2 Carbamate Decomposition Technologies
- Conventional Decomposition: Thermal decomposition at reduced pressure
- Stripping Technology: Using CO₂ or NH₃ as stripping agent, improving efficiency by 15-20%
- Heat Recovery Systems: Integrated designs recovering 60-75% of reaction heat
- Recycle Compression: MP and LP compression stages for unconverted materials
- Condensation Systems: Water-cooled and refrigerated systems for carbamate recovery
2.3 Finishing and Formulation
- Prilling: Molten urea (99.7%) fed to prilling tower (heights 40-120m)
- Product characteristics: 1-3mm spherical prills, 0.72-0.76 g/cm³ bulk density
- Cooling parameters: 2-4°C/min cooling rate, final temperatureQuality indicators: Size distribution CVGranulation: Fluid bed or drum granulation with 0.5-1.5% formaldehyde (anti-caking)
- Product characteristics: 2-4mm granules, 0.74-0.80 g/cm³ bulk density
- Process parameters: Seed recycle ratio 3:1 to 5:1, bed temperature 95-110°C
- Quality indicators: Dust generation
3. Applications
3.1 Agricultural Applications
- Nitrogen Fertilizer: Primary use (>80% of global production)
- Nitrogen content: 46% by weight (highest among solid fertilizers)
- Application rates: 80-300 kg/ha depending on crop and soil conditions
- Release characteristics: Rapid initial availability, susceptible to leaching
- Environmental impact: Potential for volatilization, nitrate leaching, and N₂O emissions
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- Enhanced Efficiency Formulations:
- Slow-release technologies: Polymer coatings, sulfur coatings, occlusion compounds
- Urease inhibitors: NBPT (N-(n-butyl) thiophosphoric triamide), reduces NH₃ losses by 40-70%
- Nitrification inhibitors: DCD, DMPP, delays conversion to leachable nitrate by 4-10 weeks
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- Foliar Applications:
- Concentration range: 1-5% solutions (crop-dependent)
- Absorption mechanism: Direct uptake through leaf cuticle and stomata
- Efficiency: 30-60% utilization compared to 30-40% for soil application
- Application timing: Critical growth stages for maximum effect
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3.2 Industrial Applications
- Melamine Production:
- Process chemistry: 6(NH₂)₂CO → C₃H₆N₆ + 6NH₃ + 3CO₂
- Operating conditions: 350-400°C, catalyzed process
- Yield: 85-90% based on urea input
- Integration: Often co-located with urea plants for process integration
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- NOx Reduction (SCR/SNCR):
- SCR systems: 32.5% urea solution (AdBlue®/DEF) at 180-450°C with catalyst
- SNCR systems: 40-50% urea solution at 850-1100°C without catalyst
- Reduction efficiency: 60-95% NOx removal for SCR, 30-50% for SNCR
- Consumption rate: 1.5-2.0 kg urea per kg NOx removed
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- Resins and Adhesives:
- Urea-formaldehyde resins: Molar ratio 1:1.2-1.8, acid catalyzed condensation
- Physical properties: Tg 70-100°C, tensile strength 40-60 MPa
- Formulation additives: Melamine (improves water resistance), fillers, crosslinkers
- Environmental considerations: Formaldehyde emissions regulations driving reformulation
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3.3 Speciality Applications
- Pharmaceutical and Cosmetic Uses:
- Dermatological applications: 10-40% in creams for keratolytic effects
- Oral medications: Component in combination therapies (typically 10-15%)
- Dental products: 10-20% in toothpastes and mouthwashes
- Stability requirements: USP/EP grade,Feed Additive:
- Non-protein nitrogen source for ruminants: Up to 1% in feed formulations
- Metabolic conversion: Converted to microbial protein by rumen microorganisms
- Efficiency: 80-90% utilization compared to protein nitrogen
- Safety considerations: Toxicity threshold >0.4 g/kg body weight
Laboratory and Specialty Chemicals:- Protein denaturing agent: 6-8M solutions for unfolding tertiary structures
- Crystallography: Precipitant and additive in protein crystallization
- Electrophoresis: Component in urea-PAGE systems for RNA/DNA analysis
- Purification requirements: >99.5% purity, ultra-low metal content
4.Market Analysis
4.1 Global Production and Consumption
- Production Capacity:
- Global capacity: ~220 million tons/year (2022)
- Regional distribution: China (30%), India (15%), Middle East (10%), Europe (8%)
- Capacity utilization: 75-85% industry average
- Production costs: 200−300/���(���−�����),200−300/ton(gas−based),300-400/ton (coal-based)
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- Consumption Patterns:
- Agricultural use: 80-85% of total consumption
- Industrial applications: 10-15% (melamine, resins, AdBlue)
- Regional demand: Asia (55%), Americas (20%), Europe (15%), Africa (7%)
- Seasonal factors: 60-70% of fertilizer demand in spring/early summer in temperate zones
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- Trade Flows:
- Major exporters: Russia, Qatar, Saudi Arabia, China, Egypt
- Major importers: India, Brazil, US, Thailand, Turkey
- Trade volume: ~50 million tons/year international trade
- Freight impact: $30-80/ton depending on routes and vessel sizes
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4.2 Price Dynamics and Economics
- Price Determinants:
- Natural gas prices: 65-75% correlation with urea pricing
- Seasonal demand: 15-25% price fluctuation between peak and off-season
- Regional availability: $20-50/ton premium in deficit regions
- Transportation costs: Significant factor for inland locations
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- Manufacturing Economics:
- Production cost breakdown: Feedstock (65-75%), energy (10-15%), maintenance (5-8%)
- Scale economies: 25-30% cost advantage for world-scale plants
- Technology impact: 5-15% cost differential between modern and older plants
- Co-product credits: Steam export, CO₂ recovery, integration benefits
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- Investment Parameters:
- CAPEX requirements: $800-1,200 per ton of annual capacity
- Payback period: 5-7 years at average market conditions
- IRR expectations: 15-20% for new greenfield projects
- Capacity addition rate: 5-7 million tons/year global capacity growth
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4.3Future Trends and Developments
- Technological Innovations:
- Energy efficiency improvements: Targeting 5-10% reduction in consumption
- Carbon capture integration: CO₂ recycling from downstream processes
- Catalyst developments: Higher conversion rates, longer catalyst life
- Digital transformation: Advanced process control, predictive maintenance
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- Market Transitions:
- Shift toward enhanced efficiency products: 10-15% annual growth
- Regional capacity redistribution: Growth in gas-rich regions
- Consolidation trends: Increasing average plant size by 25-30%
- Value chain integration: Backward integration by agricultural companies
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- Sustainability Initiatives:
- Carbon footprint reduction: Green ammonia and low-carbon technologies
- Water conservation: Zero liquid discharge implementations
- Circular economy approaches: Nutrient recovery from waste streams
- Biodegradable coating technologies: Plant-based polymer research
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5.Upsteam and Downstream Linkages
5.1 Key Raw Material Inputs
- Ammonia (NH₃):
- Primary source: Synthesized via Haber-Bosch process, predominantly from natural gas (SMR) or coal gasification.
- Stoichiometric requirement: Approximately 0.57 tons of ammonia per ton of urea.
- Economic impact: Ammonia cost typically represents 60-70% of urea production cash cost.
- Integration: Most modern urea plants are integrated with upstream ammonia production.
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- Carbon Dioxide (CO₂):
- Primary source: Captured as a byproduct from the syngas purification stage in ammonia plants (e.g., from SMR).
- Stoichiometric requirement: Approximately 0.73 tons of CO₂ per ton of urea.
- Availability: Excess CO₂ from ammonia plants is often vented if not fully utilized in urea production or other applications.
- Alternative sources: Industrial flue gases, though purification is required.
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- Energy (Natural Gas, Coal, Electricity):
- Usage: For process heat (steam generation for reactions, stripping, decomposition) and power (compression, pumping, granulation).
- Consumption benchmark: Modern plants aim for 20-25 GJ/ton of urea (net energy, including feedstock equivalent for ammonia).
- Cost component: Energy costs can account for 10-20% of total production costs, highly dependent on local energy prices.
- Efficiency: Waste heat recovery and process integration are critical for economic viability.
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5.2 Major Downstream Derivatives and Co-products
- Urea Ammonium Nitrate (UAN) Solutions:
- Composition: Liquid fertilizer containing urea, ammonium nitrate, and water (typically 28-32% N).
- Production: Either by mixing urea and ammonium nitrate solutions or by neutralizing nitric acid with ammonia and then adding urea.
- Market: Offers advantages in handling, blending with other nutrients/pesticides, and application precision.
- Relationship: A direct downstream value-added product for urea producers, often integrated.
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- Melamine (C₃H₆N₆):
- Application: A thermosetting plastic raw material used in laminates, coatings, adhesives, and flame retardants.
- Production: Catalytic gas-phase process from urea at high temperatures (
6(NH₂)₂CO → C₃H₆N₆ + 6NH₃ + 3CO₂
). - Integration: Often co-located with urea plants to utilize molten urea directly and recycle off-gases (NH₃, CO₂) back to the urea/ammonia complex.
- Value addition: Significant upgrade in value from urea to melamine.
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- Biuret (C₂H₅N₃O₂):
- Formation: A condensation product of two urea molecules, formed at elevated temperatures in the urea synthesis and finishing sections.
- Impact: Phytotoxic to plants, especially seedlings and in foliar applications. Its content is a key quality parameter for fertilizer-grade urea (typicallyControl: Minimized by controlling temperature, residence time, and pressure in urea processing.By-product status: Generally considered an impurity to be minimized, though some niche applications exist.
5.3 Value Chain Integration and Synergies
- Backward Integration (Feedstock Security):
- Strategy: Urea producers often integrate backward into ammonia production to secure NH₃ supply and manage cost volatility.
- Prerequisite: Access to competitive natural gas or coal resources.
- Benefit: Captures margin from ammonia, reduces logistical costs, and allows for CO₂ utilization from ammonia plant for urea.
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- Forward Integration (Market Access & Diversification):
- Strategy: Urea producers extend into manufacturing UAN, compound fertilizers (NPK), melamine, or specialty urea products (e.g., coated urea).
- Benefit: Accesses higher-margin markets, diversifies product portfolio, and provides tailored solutions to end-users.
- Examples: Agricultural companies integrating fertilizer production, chemical companies expanding into performance materials.
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- Industrial Complex Synergies (Co-location Benefits):
- Concept: Locating multiple interlinked chemical plants (e.g., ammonia, urea, nitric acid, ammonium nitrate, melamine) at a single site.
- Advantages:
- Shared utilities (steam, power, cooling water) and infrastructure (storage, transport).
- Efficient transfer and utilization of intermediate products (e.g., NH₃, CO₂, nitric acid).
- Reduced transportation costs and energy losses.
- Optimized waste heat recovery and overall energy efficiency.
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