Additional Information submitted during the information exchange on ...
Additional Information submitted during the information exchange on ... Additional Information submitted during the information exchange on ...
This document has not been fully peer reviewed and
This document has not been fully peer reviewed and
- Page 1 and 2: EUROPEAN COMMISSION DIRECTORATE-GEN
- Page 3 and 4: 2 PURIFICATION OF NON-FERTILISER GR
- Page 5: List of tables Table 1.1: Typical c
- Page 9 and 10: This document has not been fully pe
- Page 11 and 12: This document has not been fully pe
- Page 13 and 14: This document has not been fully pe
- Page 15 and 16: This document has not been fully pe
- Page 17 and 18: This document has not been fully pe
- Page 19 and 20: This document has not been fully pe
- Page 21 and 22: This document has not been fully pe
- Page 23 and 24: This document has not been fully pe
- Page 25 and 26: This document has not been fully pe
- Page 27 and 28: This document has not been fully pe
- Page 29 and 30: This document has not been fully pe
- Page 31 and 32: This document has not been fully pe
- Page 33 and 34: This document has not been fully pe
- Page 35 and 36: This document has not been fully pe
- Page 37 and 38: This document has not been fully pe
- Page 39 and 40: This document has not been fully pe
- Page 41: This document has not been fully pe
- Page 46 and 47: This document has not been fully pe
- Page 48 and 49: References 41 Solvay S.A. (2003). "
- Page 50 and 51: References 95 CEFIC-Brunner Mond (2
- Page 52 and 53: Glossary SS Suspended Solids (conte
- Page 54 and 55: Glossary Ca 2+ Calcium ion CaC2 Cal
- Page 56: Glossary (NH4)2SO4 Ammonium sulphat
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