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This document has not been fully peer reviewed and ong>theong> ong>informationong> within is not validated nor endorsed by ong>theong> TWG on LVIC-S or by ong>theong> European Commission, it is meant for ong>informationong>, only In oong>theong>r cases (for instance in some of ong>theong> sites producing detergent phosphates), ong>theong> purification (starting from unpurified “green”, merchant commodity phosphoric acid) takes place in ong>theong> same process as ong>theong> production of a given inorganic phosphate. Phosphoric acids of various degrees of purity are available as global merchant commodities or, in some cases, can be produced at ong>theong> same site where both acid purification installations and inorganic phosphate production plants are situated. Operators will purchase purified acid of ong>theong> degree of purity required for ong>theong> range of inorganic phosphates ong>theong>y are manufacturing, or will purify phosphoric acid onsite to ong>theong> degree of purity required in downstream operations. Depending on ong>theong> purity of ong>theong> acid used, some sites can manufacture inorganic phosphates for different applications (detergent, animal feed, food). A high purity phosphoric acid may also be obtained by ong>theong> ong>theong>rmal route. White phosphorus, derived by ong>theong>rmal reduction from phosphate rock or oong>theong>r phosphate sources, is combusted in air, followed by ong>theong> absorption of phosphorus pentoxide (P2O5) in water (refer to ong>theong> BREF on LVIC-AAF). In general, this process route is seldom used in Western Europe for ong>theong> production of detergentgrade STPP or for ong>theong> production of inorganic feed phosphates, as ong>theong> phosphoric acid produced from elemental phosphorus is of a high purity, not required for detergent or animal feed applications. Some inorganic phosphate products have a range of uses which require different levels of purity: for example STPP, which is used in detergents and cleaning products, but also as a human food and pharmaceutical ingredient which requires higher grades of purity. In some cases, ong>theong> same installation can be used to manufacture an inorganic phosphate product for various purposes; different quality grades being achieved by using different quality feedstocks (phosphoric acid or phosphate rock of different levels or purity) and/or by additional purification steps operated optionally within ong>theong> production process. The purification of phosphoric acid has not been described in ong>theong> BREF on LVIC-AAF as, for most fertiliser production processes, such a step is not necessary. Also, data and ong>informationong> on ong>theong> purification of phosphoric acid have not been ong>submittedong> ong>duringong> ong>informationong> ong>exchangeong> on ong>theong> BREF on LVIC-S and, ong>theong>refore, detailed ong>informationong> on consumption and emission levels from ong>theong> phosphoric acid purification step is not available. As ong>theong> description of processes and unit operations applied in ong>theong> purification of non fertiliser grade wet phosphoric acid was not covered in detail eiong>theong>r in ong>theong> BREF on LVIC-AAF or in ong>theong> BREF on LVIC-S, ong>theong>re is, ong>theong>refore, a clear ong>informationong> gap in this area between ong>theong> two large volume inorganic chemical industry BREFs. In order not to loose partial ong>informationong> from ong>theong> BREF on LVIC-S (Chapter 6), it was considered important to include in this document one of ong>theong> “Techniques to consider in ong>theong> determination of BAT” (deleted from ong>theong> BREF on LVIC-S upon ong>theong> recommendation of ong>theong> TWG on LVIC-S), as it may be of value in future for ong>theong> revision of one of ong>theong> LVIC BREFs and ong>informationong> ong>exchangeong> on ong>theong> routes available for ong>theong> purification of “green” phosphoric acid, eiong>theong>r by a chemical process or a physical process (solvent extraction). It should be noted that as ong>theong> purification of ong>theong> phosphoric acid, typically (but not always) takes place upstream of ong>theong> site of ong>theong> inorganic phosphates plants, ong>theong>refore, in most cases (but not always), ong>theong> main environmental benefits are outside of ong>theong> scope of ong>theong> feed phosphates sector. 2

This document has not been fully peer reviewed and ong>theong> ong>informationong> within is not validated nor endorsed by ong>theong> TWG on LVIC-S or by ong>theong> European Commission, it is meant for ong>informationong>, only 2.2 Purification of non-fertiliser grade wet phosphoric acid – ong>theong> options Description Since, in most cases, ong>theong> purified non-fertiliser-grade wet phosphoric acid is selected for ong>theong> production of inorganic phosphates, ong>theong> techniques available for ong>theong> purification of “green” phosphoric acid (to remove sulphate, arsenic, fluoride and oong>theong>r impurities) need to be analysed and compared in detail from ong>theong> technical, economical, and environmental point of view in order to reduce ong>theong> impact of ong>theong> production of feed-phosphates on ong>theong> environment in ong>theong> whole chain of operations, starting from ong>theong> intermediate phosphoric acid product and ending at ong>theong> final food-grade phosphate product. Such a comparison needs to be carried out for two typical cases A and B pertaining to ong>theong> plant location, and for two alternative process routes X and Y available to achieve ong>theong> different degree (depth) of purification of “green” phosphoric acid: and A. Phosphoric acid purification at ong>theong> wet phosphoric acid production site, typically (but not always) outside of ong>theong> inorganic phosphates production site B. Phosphoric acid purification at ong>theong> inorganic phosphates production site (in some cases it may also be ong>theong> site of ong>theong> phosphoric acid plant), X. Desulphation (adding lime), neutralisation (adding NaOH/Na2CO3) and purification by precipitation, involving various techniques available for chemical purification of ong>theong> wet phosphoric acid, dependent on ong>theong> required degree of acid quality Y. Concentration, desulphation, and very deep purification of ong>theong> wet phosphoric acid by solvent extraction, involving more elaborate physico-chemical techniques. Wet process phosphoric acid is purified by numerous methods and to a wide variety of standards depending on ong>theong> furong>theong>r application of ong>theong> acid. The most basic method, and ong>theong> one which all suppliers of merchant-grade acid carry out before shipment, is clarification, by settling or oong>theong>r mechanical means, to remove suspended solids. In case ong>theong> acid is used for ong>theong> production of fertilisers no furong>theong>r treatment is usually applied. Chemical purification methods can be employed if ong>theong> acid is to be used for specific purposes, not requiring a high quality. Active carbon treatment is ong>theong> usual means of removing organic impurities. Fluorine is removed by adding reactive silica and distilling off silicon tetrafluoride. Phosphate rock or lime may be added to ong>theong> impure acid to remove excess sulphate. Metals ions can be selectively precipitated by various chemicals. By adding a Na2S solution to ong>theong> acid, arsenic can be precipitated as arsenic sulphide. Removal of oong>theong>r cationic impurities, especially Fe, Al, Mg and Ca, can be achieved by neutralising ong>theong> acid with sodium carbonate or caustic soda. The phosphoric acid in this process is converted to a phosphate salt solution. More elaborate techniques involving (organic) solvent treatment are used to obtain purer acid such as that required for animal feed supplements (mainly cadmium removal) and especially ong>theong> food industry. Liquid/liquid extraction processes are most commonly used. Processes are operated for ong>theong> separation of single components (e.g. uranium and cadmium) as well as of practically all impurities in wet phosphoric acid. The quality of such purified acid nearly equals that of ong>theong>rmally produced acid. Besides liquid/liquid extraction processes, precipitation processes are also being employed. 3

This document has not been fully peer reviewed and <str<strong>on</strong>g>the</str<strong>on</strong>g> <str<strong>on</strong>g>informati<strong>on</strong></str<strong>on</strong>g> within is not validated nor endorsed by <str<strong>on</strong>g>the</str<strong>on</strong>g> TWG<br />

<strong>on</strong> LVIC-S or by <str<strong>on</strong>g>the</str<strong>on</strong>g> European Commissi<strong>on</strong>, it is meant for <str<strong>on</strong>g>informati<strong>on</strong></str<strong>on</strong>g>, <strong>on</strong>ly<br />

2.2 Purificati<strong>on</strong> of n<strong>on</strong>-fertiliser grade wet phosphoric acid –<br />

<str<strong>on</strong>g>the</str<strong>on</strong>g> opti<strong>on</strong>s<br />

Descripti<strong>on</strong><br />

Since, in most cases, <str<strong>on</strong>g>the</str<strong>on</strong>g> purified n<strong>on</strong>-fertiliser-grade wet phosphoric acid is selected for <str<strong>on</strong>g>the</str<strong>on</strong>g><br />

producti<strong>on</strong> of inorganic phosphates, <str<strong>on</strong>g>the</str<strong>on</strong>g> techniques available for <str<strong>on</strong>g>the</str<strong>on</strong>g> purificati<strong>on</strong> of “green”<br />

phosphoric acid (to remove sulphate, arsenic, fluoride and o<str<strong>on</strong>g>the</str<strong>on</strong>g>r impurities) need to be analysed<br />

and compared in detail from <str<strong>on</strong>g>the</str<strong>on</strong>g> technical, ec<strong>on</strong>omical, and envir<strong>on</strong>mental point of view in<br />

order to reduce <str<strong>on</strong>g>the</str<strong>on</strong>g> impact of <str<strong>on</strong>g>the</str<strong>on</strong>g> producti<strong>on</strong> of feed-phosphates <strong>on</strong> <str<strong>on</strong>g>the</str<strong>on</strong>g> envir<strong>on</strong>ment in <str<strong>on</strong>g>the</str<strong>on</strong>g><br />

whole chain of operati<strong>on</strong>s, starting from <str<strong>on</strong>g>the</str<strong>on</strong>g> intermediate phosphoric acid product and ending at<br />

<str<strong>on</strong>g>the</str<strong>on</strong>g> final food-grade phosphate product.<br />

Such a comparis<strong>on</strong> needs to be carried out for two typical cases A and B pertaining to <str<strong>on</strong>g>the</str<strong>on</strong>g> plant<br />

locati<strong>on</strong>, and for two alternative process routes X and Y available to achieve <str<strong>on</strong>g>the</str<strong>on</strong>g> different degree<br />

(depth) of purificati<strong>on</strong> of “green” phosphoric acid:<br />

and<br />

A. Phosphoric acid purificati<strong>on</strong> at <str<strong>on</strong>g>the</str<strong>on</strong>g> wet phosphoric acid producti<strong>on</strong> site, typically (but not<br />

always) outside of <str<strong>on</strong>g>the</str<strong>on</strong>g> inorganic phosphates producti<strong>on</strong> site<br />

B. Phosphoric acid purificati<strong>on</strong> at <str<strong>on</strong>g>the</str<strong>on</strong>g> inorganic phosphates producti<strong>on</strong> site (in some cases it<br />

may also be <str<strong>on</strong>g>the</str<strong>on</strong>g> site of <str<strong>on</strong>g>the</str<strong>on</strong>g> phosphoric acid plant),<br />

X. Desulphati<strong>on</strong> (adding lime), neutralisati<strong>on</strong> (adding NaOH/Na2CO3) and purificati<strong>on</strong> by<br />

precipitati<strong>on</strong>, involving various techniques available for chemical purificati<strong>on</strong> of <str<strong>on</strong>g>the</str<strong>on</strong>g> wet<br />

phosphoric acid, dependent <strong>on</strong> <str<strong>on</strong>g>the</str<strong>on</strong>g> required degree of acid quality<br />

Y. C<strong>on</strong>centrati<strong>on</strong>, desulphati<strong>on</strong>, and very deep purificati<strong>on</strong> of <str<strong>on</strong>g>the</str<strong>on</strong>g> wet phosphoric acid by<br />

solvent extracti<strong>on</strong>, involving more elaborate physico-chemical techniques.<br />

Wet process phosphoric acid is purified by numerous methods and to a wide variety of<br />

standards depending <strong>on</strong> <str<strong>on</strong>g>the</str<strong>on</strong>g> fur<str<strong>on</strong>g>the</str<strong>on</strong>g>r applicati<strong>on</strong> of <str<strong>on</strong>g>the</str<strong>on</strong>g> acid.<br />

The most basic method, and <str<strong>on</strong>g>the</str<strong>on</strong>g> <strong>on</strong>e which all suppliers of merchant-grade acid carry out before<br />

shipment, is clarificati<strong>on</strong>, by settling or o<str<strong>on</strong>g>the</str<strong>on</strong>g>r mechanical means, to remove suspended solids. In<br />

case <str<strong>on</strong>g>the</str<strong>on</strong>g> acid is used for <str<strong>on</strong>g>the</str<strong>on</strong>g> producti<strong>on</strong> of fertilisers no fur<str<strong>on</strong>g>the</str<strong>on</strong>g>r treatment is usually applied.<br />

Chemical purificati<strong>on</strong> methods can be employed if <str<strong>on</strong>g>the</str<strong>on</strong>g> acid is to be used for specific purposes,<br />

not requiring a high quality. Active carb<strong>on</strong> treatment is <str<strong>on</strong>g>the</str<strong>on</strong>g> usual means of removing organic<br />

impurities. Fluorine is removed by adding reactive silica and distilling off silic<strong>on</strong> tetrafluoride.<br />

Phosphate rock or lime may be added to <str<strong>on</strong>g>the</str<strong>on</strong>g> impure acid to remove excess sulphate. Metals i<strong>on</strong>s<br />

can be selectively precipitated by various chemicals. By adding a Na2S soluti<strong>on</strong> to <str<strong>on</strong>g>the</str<strong>on</strong>g> acid,<br />

arsenic can be precipitated as arsenic sulphide. Removal of o<str<strong>on</strong>g>the</str<strong>on</strong>g>r cati<strong>on</strong>ic impurities, especially<br />

Fe, Al, Mg and Ca, can be achieved by neutralising <str<strong>on</strong>g>the</str<strong>on</strong>g> acid with sodium carb<strong>on</strong>ate or caustic<br />

soda. The phosphoric acid in this process is c<strong>on</strong>verted to a phosphate salt soluti<strong>on</strong>.<br />

More elaborate techniques involving (organic) solvent treatment are used to obtain purer acid<br />

such as that required for animal feed supplements (mainly cadmium removal) and especially <str<strong>on</strong>g>the</str<strong>on</strong>g><br />

food industry. Liquid/liquid extracti<strong>on</strong> processes are most comm<strong>on</strong>ly used. Processes are<br />

operated for <str<strong>on</strong>g>the</str<strong>on</strong>g> separati<strong>on</strong> of single comp<strong>on</strong>ents (e.g. uranium and cadmium) as well as of<br />

practically all impurities in wet phosphoric acid. The quality of such purified acid nearly equals<br />

that of <str<strong>on</strong>g>the</str<strong>on</strong>g>rmally produced acid. Besides liquid/liquid extracti<strong>on</strong> processes, precipitati<strong>on</strong><br />

processes are also being employed.<br />

3

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