Because of its many uses, ammonia is one of the most highly produced inorganic chemicals. There are numerous large-scale ammonia production plants worldwide, producing a total of 131 million tonnes of nitrogen (equivalent to 159 million tonnes of ammonia) in 2010. China produced 32.1% of the worldwide production, followed by India with 8.9%, Russia with 7.9%, and the United States with 6.3%. 80% or more of the ammonia produced is used for fertilizing agricultural crops. Ammonia is also used for the production of plastics, fibers, explosives, nitric acid (via the Ostwald process) and intermediates for dyes and pharmaceuticals.
Before the start of World War I, most ammonia was obtained by the dry distillation of nitrogenous vegetable and animal products; by the reduction of nitrous acid and nitrites with hydrogen; and also by the decomposition of ammonium salts by alkaline hydroxides or by quicklime, the salt most generally used being the chloride (sal-ammoniac).
Today, most ammonia is produced on a large scale by the Haber process with capacities of up to 3,300 metric tons per day. 1) Ammonia is manufactured on a large scale by Haber's process. 2) In this process,N2 and H2 gases are allowed to react at high pressure of 200 bar (a).
Modern ammonia-producing plants
A typical modern ammonia-producing plant first converts natural gas (i.e., methane) or LPG (liquefied petroleum gases such as propane and butane) or petroleum naphtha into gaseous hydrogen. The method for producing hydrogen from hydrocarbons is referred to as "Steam Reforming". The hydrogen is then combined with nitrogen to produce ammonia via the Haber-Bosch process.
Starting with a natural gas feedstock, the processes used in producing the hydrogen are:
- The first step in the process is to remove sulfur compounds from the feedstock because sulfur deactivates the catalysts used in subsequent steps. Sulfur removal requires catalytic hydrogenation to convert sulfur compounds in the feedstocks to gaseous hydrogen sulfide:
- H2 + RSH → RH + H2S(gas)
- The gaseous hydrogen sulfide is then adsorbed and removed by passing it through beds of zinc oxide where it is converted to solid zinc sulfide:
- H2S + ZnO → ZnS + H2O
- Catalytic steam reforming of the sulfur-free feedstock is then used to form hydrogen plus carbon monoxide:
- CH4 + H2O → CO + 3H2
- The next step then uses catalytic shift conversion to convert the carbon monoxide to carbon dioxide and more hydrogen:
- CO + H2O → CO2 + H2
- The carbon dioxide is then removed either by absorption in aqueous ethanolamine solutions or by adsorption in pressure swing adsorbers (PSA) using proprietary solid adsorption media.
- The final step in producing the hydrogen is to use catalytic methanation to remove any small residual amounts of carbon monoxide or carbon dioxide from the hydrogen:
- CO + 3H2 → CH4 + H2O
- CO2 + 4H2 → CH4 +2H2O
To produce the desired end-product ammonia, the hydrogen is then catalytically reacted with nitrogen (derived from process air) to form anhydrous liquid ammonia. This step is known as the ammonia synthesis loop (also referred to as the Haber-Bosch process):
- 3H2 + N2 → 2NH3
Due to the nature of the (typically multi-promoted magnetite) catalyst used in the ammonia synthesis reaction, only very low levels of oxygen-containing (especially CO, CO2 and H2O) compounds can be tolerated in the synthesis (hydrogen and nitrogen mixture) gas. Relatively pure nitrogen can be obtained by Air separation, but additional oxygen removal may be required.
Because of relatively low single pass conversion rates (typically less than 20%), a large recycle stream is required. This can lead to the accumulation of inerts in the loop gas.
The steam reforming, shift conversion, carbon dioxide removal and methanation steps each operate at absolute pressures of about 25 to 35 bar, and the ammonia synthesis loop operates at absolute pressures ranging from 60 to 180 bar depending upon which proprietary design is used. There are many engineering and construction companies that offer proprietary designs for ammonia synthesis plants. Haldor Topsoe of Denmark, Uhde GmbH of Germany, Ammonia Casale of Switzerland and Kellogg Brown & Root of the United States are among the most experienced companies in that field.
Sustainable ammonia production
Ammonia production depends on plentiful supplies of energy, predominantly natural gas. Due to ammonia's critical role in intensive agriculture and other processes, sustainable production is desirable. This is possible by using renewable energy to generate hydrogen by electrolysis of water. This would be straightforward in a hydrogen economy by diverting some hydrogen production from fuel to feedstock use. For example, in 2002, Iceland produced 2,000 tons of hydrogen gas by electrolysis, using excess electricity production from its hydroelectric plants, primarily for the production of ammonia for fertilizer. The Vemork hydroelectric plant in Norway used its surplus electricity output to generate renewable ammonia from 1911 to 1971. In practice, natural gas will remain the major source of hydrogen for ammonia production as long as it is cheapest.
As an alternative to the relatively inefficient electrolysis, hydrogen can be generated from organic wastes (such as biomass or food-industry waste), using catalytic (thermal) reforming. This releases hydrogen from carbonaceous substances at only 10-20% of energy used by electrolysis and may lead to hydrogen being produced from municipal wastes at below zero cost (allowing for the tipping fees and efficient catalytic reforming, such as cold-plasma). Catalytic reforming is possible in small, distributed (even mobile) plants, to take advantage of stranded biomass/biowastes or natural gas deposits. Conversion of such wastes into ammonia solves the problem of hydrogen storage, as hydrogen can be released economically from ammonia on-demand, without the need for high-pressure or cryogenic storage.
It is also easier to store ammonia on-board of vehicles than to store hydrogen, as ammonia is less flammable than gasoline or LPG.
Waste water is often high in ammonia. Because discharging ammonia laden water into the environment can cause problems, nitrification is often necessary to remove the ammonia. This may be a potentially sustainable source of ammonia in the future because of its abundance and the need to remove it from the water anyway.
- United States Geological Survey publication
- Twygg, Martyn V. (1989). Catalyst Handbook (2nd Edition ed.). Oxford University Press. ISBN 1-874545-36-7.
- "Iceland launches energy revolution". BBC News. 2001-12-24. Archived from the original on 7 April 2008. Retrieved 2008-03-23.
- Bradley, David (2004-02-06). "A Great Potential: The Great Lakes as a Regional Renewable Energy Source" (PDF). Archived from the original (PDF) on 29 October 2008. Retrieved 2008-10-04.
- Today's Hydrogen Production Industry
- Energy Use and Energy Intensity of the U.S. Chemical Industry, Report LBNL-44314, Lawrence Berkeley National Laboratory (Scroll down to page 39 of 40 PDF pages for a list of the ammonia plants in the USA)
- Ammonia: The Next Step includes a detailed process flow diagram.
- Ammonia production process plant flow sheet in brief with three controls.