Ammonia production

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Burrup_Fertilizers'_plant.jpg

Fertilizer plant that can produce 760,000 tonnes/year of anhydrous ammonia

Ammonia production facilities provide the base anhydrous liquid ammonia used predominantly in fertilizers supplying usable nitrogen for agricultural productivity. Ammonia is one of the most abundantly-produced inorganic chemicals. There are literally dozens of large-scale ammonia production plants throughout the industrial world, some of which produce as much as 2,000 to 3,000 tons per day of anhydrous ammonia in liquid form. The worldwide production in 2006 was 122,000,000 metric tons.[1] China produced 32.0% of the worldwide production followed by India with 8.9%, Russia with 8.2%, and the United States with 6.5%. Without such massive production, our agriculturally-dependent civilization would face serious challenges.

History

Before the start of World War I, most ammonia was obtained by the dry distillation of nitrogenous vegetable and animal products; the reduction of nitrous acid and nitrites with hydrogen; and the decomposition of ammonium salt]s by alkaline hydroxides or by quicklime, the salt most generally used being the ammonium chloride (sal-ammoniac).

The Haber process, which is the production of ammonia by combining hydrogen and nitrogen, was first patented by Fritz Haber in 1908. In 1910, Carl Bosch, while working for the German chemical company BASF, successfully commercialized the process and secured further patents. It was first used on an industrial scale by the Germans during World War I. Since then, the process has often been referred to as the "Haber-Bosch process".

Modern production process

A typical modern ammonia-producing plant first converts natural gas (i.e., methane) or LPG

Steam-Methane_Reformer.png

Block-flow diagram of ammonia synthesis process

(liquified 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".[2] [3] [4] [5] The hydrogen is then combined with nitrogen to produce ammonia.[6] [7]

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 organic sulfur compounds (RSH) in the feedstocks to gaseous hydrogen sulfide (H2S):

H2 + RSH → RH + H2S (gas)

The gaseous hydrogen sulfide is then passed through a reactor containing zinc oxide (ZnO) where it is converted to solid zinc sulfide (ZnS) in a batch process (i.e., when allof the zinc oxide has been converted to zinc sulfide, it is removed and replaced with fresh zinc oxide):

H2S + ZnO → ZnS + H2O

Catalytic steam reforming of the sulfur-free methane (CH4) feedstock is then used to form carbon monoxide (CO) plus hydrogen (H2):

CH4 + H2O → CO + 3H2

The next step then uses catalytic shift conversion to convert the carbon monoxide to carbon dioxide (CO2) 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 by converting them into methane:

CO + 3H2 → CH4 + H2O

CO2 + 4H2 → CH4 +2H2O

To produce the desired end-product ammonia, the hydrogen is then catalytically reacted with nitrogen (N2) derived from process air to form anhydrous liquid ammonia (NH3). This step is known as the "ammonia synthesis loop" (also referred to as the Haber-Bosch process):

3H2 + N2 → 2NH3

The nitrogen required for the Haber-Bosch process is obtained in either of these two ways:

The catalytic steam reformer has two sections: a primary reformer and a secondary reformer. By the introduction of air into the secondary reformer, the air reacts with some of the hydrogen produced in the primary reformer to form nitrogen and water:[8]

H2 + air → N2 + H2O

By the low-temperature distillation of air

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, Technip of France, Uhde GmbH of Germany, and Kellogg Brown & Root of the United States are among the most experienced companies in that field.

Uses of ammonia

About 80% or more of the ammonia produced is used for fertilizing agricultural crops in the form of aqua ammonia (an aqueous solution of ammonia), ammonium sulfate (NH4)2SO4, ammonium phosphate (NH4)3PO4, ammonium nitrate NH4NO3 and urea (NH2)2CO. Some anhydrous liquid ammonia is also used directly as a fertilizer.

Ammonia is also used for:

Manufacture of nitric acid (HNO3)

Manufacture of nylon and other polyamides

Refrigerant in household, commercial and industrial refrigeration systems

Manufacture of dyes

Manufacture of explosives

Cleaning solutions

Safety concerns with ammonia

There are several safety-related concerns with anhydrous ammonia and with aqueous solutions of ammonia. It is a respiratory irritant that is a highly hazardous chemical.[9] Release could take place through a simple industrial or transportation accident, a deliberate release caused by terrorists, or by improper handling by those using it in the illegal synthesis of methamphetamines.

Storage tanks on farms used for dispensing ammonia as fertilizer are referred to as ''nurse'' tanks and contain approximately 2,500 pounds (1134 kg) of anhydrous ammonia, so any farm with four or more nurse tanks needs to assess its safety. In fact, the U.S. Environmental Protection Agency (U.S. EPA) mandates the performance of an "Offsite Consequence Analysis" (OCA) as part of their "Risk Management Plan" (RMP) requirements for any facility that stores more than 10,000 pounds (4,536 kg) of anhydrous liquid ammonia or 20,000 pounds (9,072 kg) of aqueous solutions of ammonia.[10] The RMP requirements apply for ammonia refrigeration systems or any other ammonia storage facilities as well as farms. The U.S. Occupational Health & Safety Administration (OSHA) has mandated very similar requirements as part of their "Process Safety Management" (PSM) regulations for hazardous chemicals.[11]

In transport, ammonia containers must have proper hazardous material placards and, if the pertinent threshold quantity is exceeded, may need additional safeguards such as reporting the shipment to industry monitoring services such as CHEMTREC[12] or additional local agencies. There may be restrictions on transporting hazardous materials through tunnels, or possibly streets in high-density areas.

The U.S. Department of Homeland Security (DHS), citing its major concern as toxic release, lists anhydrous ammonia, or mixtures containing at least 1 percent ammonia, when stored in quantities of 10,000 pounds or more, as a chemical of interest, which falls under the Risk for Chemical Facility Anti-Terrorism Standards (CFATS) regulations and guidance.[13] Organizations that store or transport more than the threshold quantity of 10,000 pounds, or believe they are at a higher than normal risk, should use the Chemical Security Assessment Tool.[14]

The U.S. EPA has issued an additional safeguards document, with special emphasis on the theft of ammonia.[15]

Image credits

The credit for the photo in the lede of this article is: © Courtesy of Burrup Fertilisers Pty Ltd. The schematic diagram in this article was created by Milton Beychok and is released into the Public Domain.

References

^ United States Geological Survey publication

^ Gary Maxwell (2004),Synthetic Nitrogen Products: A Practical Guide to the Products and Processes, 1st Edition, Springer Publishing, ISBN 0-306-48225-8

^ Samuel Strelzoff (1987), Technology and Manufacture of Ammonia, Krieger Publishing, ISBN 0-89464-250-2}

^ Martyn V. Twygg (1989), Catalyst Handbook, 2nd Edition, Oxford University Press, ISBN 1-874545-36-7

^ Editor: John J. Mcketta (1993), Chemical Processing Handbook, 1st Edition, CRC Press, ISBN 0-8247-8701-3

^ Editor: J.R. Jennings (1991), Catalytic Ammonia Synthesis, 1st Edition, Springer Publishing, ISBN 0-306-43628-0

^ Sami Matar and Lewis F. Hatch (2001), Chemistry of Petrochemical Processes, 2nd Edition, Gulf Publishing, ISBN 0-8841-5315-0

^ See references 5 and 6 above

^ NIOSH Pocket Guide to Chemical Hazards

^ Risk Management Plan (From the website of the U.S. EPA)

^ Process Safety Management of Highly Hazardous Chemicals (From the website of the U.S. OSHA)

^ CHEMTREC: the 24-hour HAZMAT Communications Center

^ Federal Register (November 20, 2007) Part II, Department of Homeland Security, 6 CFR Part 27 Appendix to Chemical Facility Anti-Terrorism Standards; Final Rule

^ Chemical Security Assessment Tool (From the website of the U.S. DHS

^ Anhydrous Ammonia Theft (From the website of the U.S. EPA)

http://chemengineering.wikispaces.com/Ammonia+production