PL16975B1 - Method for the production of sodium nitrate. - Google Patents
Method for the production of sodium nitrate. Download PDFInfo
- Publication number
- PL16975B1 PL16975B1 PL16975A PL1697530A PL16975B1 PL 16975 B1 PL16975 B1 PL 16975B1 PL 16975 A PL16975 A PL 16975A PL 1697530 A PL1697530 A PL 1697530A PL 16975 B1 PL16975 B1 PL 16975B1
- Authority
- PL
- Poland
- Prior art keywords
- sodium
- ammonium chloride
- solution
- carbonate
- ammonium
- Prior art date
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- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 title claims description 23
- 238000000034 method Methods 0.000 title claims description 19
- 235000010344 sodium nitrate Nutrition 0.000 title claims description 11
- 239000004317 sodium nitrate Substances 0.000 title claims description 8
- 238000004519 manufacturing process Methods 0.000 title description 3
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 26
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 claims description 22
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims description 16
- 235000019270 ammonium chloride Nutrition 0.000 claims description 14
- 239000011780 sodium chloride Substances 0.000 claims description 13
- 229910052602 gypsum Inorganic materials 0.000 claims description 11
- 239000010440 gypsum Substances 0.000 claims description 11
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 9
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 claims description 9
- 229910017604 nitric acid Inorganic materials 0.000 claims description 9
- 229910000019 calcium carbonate Inorganic materials 0.000 claims description 8
- 229910052938 sodium sulfate Inorganic materials 0.000 claims description 7
- 235000011152 sodium sulphate Nutrition 0.000 claims description 7
- 238000006243 chemical reaction Methods 0.000 claims description 6
- 238000000926 separation method Methods 0.000 claims description 5
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 claims description 3
- 239000001099 ammonium carbonate Substances 0.000 claims description 3
- 235000012501 ammonium carbonate Nutrition 0.000 claims description 3
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 claims description 3
- 238000001816 cooling Methods 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 239000007787 solid Substances 0.000 claims description 3
- 230000002349 favourable effect Effects 0.000 claims description 2
- 239000012452 mother liquor Substances 0.000 claims description 2
- 238000002360 preparation method Methods 0.000 claims description 2
- 239000002002 slurry Substances 0.000 claims description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 claims 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 claims 1
- 150000001450 anions Chemical class 0.000 claims 1
- FLNKWZNWHZDGRT-UHFFFAOYSA-N azane;dihydrochloride Chemical compound [NH4+].[NH4+].[Cl-].[Cl-] FLNKWZNWHZDGRT-UHFFFAOYSA-N 0.000 claims 1
- 239000011505 plaster Substances 0.000 claims 1
- 238000001179 sorption measurement Methods 0.000 claims 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 3
- 239000007832 Na2SO4 Substances 0.000 description 3
- 235000010216 calcium carbonate Nutrition 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- ZCCIPPOKBCJFDN-UHFFFAOYSA-N calcium nitrate Chemical compound [Ca+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ZCCIPPOKBCJFDN-UHFFFAOYSA-N 0.000 description 2
- 238000010411 cooking Methods 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 1
- 241000549556 Nanos Species 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 1
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 1
- 239000001166 ammonium sulphate Substances 0.000 description 1
- 235000011130 ammonium sulphate Nutrition 0.000 description 1
- 229910052925 anhydrite Inorganic materials 0.000 description 1
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 229910000069 nitrogen hydride Inorganic materials 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
Description
Do wytwarzania azotanu sodowego " u- zywa sie zwykle, jako materjalów wyjscio¬ wych, sody i kwasu azotowego. Sode wy¬ twarza sie w oddzielnej fabryce z soli ku¬ chennej, skutkiem czego stanowi ona drogi surowiec.Wyrób azotanu sodowego wprost z soli kuchennej i kwasu azotowego jest niedo¬ godny i dotychczas bez praktycznego zna¬ czenia. Proponowano co prawda rózne sposoby oddeistylowywania utworzonego kwasu solnego, jednakze oddzielenie wy¬ tworzonej mieszaniny kwasu solnego, kwa¬ su azotowego oraz produktów reakcji tych kwasów przedstawia znaczne trudnosci.Z siarczanu sodu i azotanu wapniowego mozna otrzymac azotan sodu w roztworze oraz gips, jako osad. Ponadto wiadomo, iz gips mozna przemienic weglanem amonu w siarczan amonu i weglan wapnia.Przy zastosowaniu obu przytoczonych reakcji wytwarza sie, wedlug niniejszego wynalazku, z NaCl, HN03 oraz NH3, jako surowców, w zamknietym procesie kolo¬ wym NaNOs i NH4Cl. W powyzszym pro¬ cesie kolowym kraza CaO, S03 i C02, jako srodki pomocnicze.Sposób przeprowadza sie nastepujaco.Roztwór otrzymany w procesie, zawie¬ rajacy (NHJ2SO4, NHJ21 i NaCl miesiza sie z NaCl w ilosci równowaznej do (NH4)2SO± i wprowadza NH3. PowstajeNc^SÓi, jako osad, który sie oddziela i V trakcje kwasem azotowym razem z wegla- * nem wapnia ohrzymiywainym w procesie ko¬ lowym, przyczem tworzy sie gips i roztwór NaN03, podczas gdy C02 uchodzi. Gips od¬ dziela sie przez dekamlacje Iruib saczenie od lugu NaN03, który odparowuje sie celem uzyskania stalego NaN03. Zamiast odparo¬ wywac roztwór NaN03, mozna go ochlo¬ dzic celem wydzielenia czesci NaN03, a lug macierzysty stosowac dio rozpuszczania dal¬ szych ilosci Na2S04. Lug, zawieraj apy Na^O^ otrzym lny przy pierwszym zabie¬ gu, ochladza sit^ celem wydzielenia pewnej czesci NH4Cl. Aby ulatwic wydzielanie NH4Cl, mozna juz w tern miejscu dodac NaCl uzywany jako surowiec. Po oddziele¬ niu od NH4Cl wysyca sie lug zapomoca CO2, celem wytworzenia (NHJ2C03. Po¬ trzebny do tego kwas weglowy otrzymuje sie przy opisanem juz traktowaniu Na2S04 i CO3 zapomoca HN03.Tak otrzymany roztwór (NH4)2C03, NH4Cl, NaCl miesza sie z gipsem, uzyska¬ nym przy wytwarzaniu NaN03, przyczem gips tworzy (NH4)2S04 i CaC03. Przemia¬ na ta odbywa sie gladko, dzieki zwieksza¬ nej rozpuszczalnosci gipsu w roztworze NH4Cl. Uzyskany w ten sposób roztwór, jest wspomnianym na wstepie roztworem (NHJ2S04~NH4Cl^NaCl, do którego do¬ daje sie NaCl i wprowadza NH3, skutkiem czego otrzymuje sie nowe ilosci Na2S04 i tak dalej.Dla lepszego wys&ilania NaJiOi jest ko¬ rzystny nadmiar NaCl, który pozostaje w obiegu kolowym w roztworze.Zamiast wprowadzac NH3 po przemia¬ nie CaS04 a (NHJ2C03, mozna NH3 rów* niez dodac przed powyzsza reakcja. Ma to te zalete, iz roztwór zimny po wydzieleniu przez ochlodzenie NH4Cl ogrzewa sie bez doplywu ciepla korzystniejszej dla reakcji, Poniewaz Na2S04 i CaCOs traktuje sie wspólnie za¬ pomoca HN03, nie pofceba ich oddzielnie saczyc. Przeciwnie, wspólne saczenie daje wielka praktyczna korzysc, poniewaz, jak wiadomo, chemicznie wydzielony CaC03 sa¬ czy sie sktrtlgiem swej drobnoziarnistosci z wielkim trudem, \ Oczywiscie tnózna amonjak przed rege¬ neracja chlorku amonu odzyskac i ponow¬ nie wprowadzac do procesu. PLSoda and nitric acid are usually used as starting materials for the production of sodium nitrate. Soda is produced in a separate factory from cooking salt, which makes it an expensive raw material. Production of sodium nitrate directly from cooking salt. and nitric acid is inexpensive and heretofore without practical significance. Although various methods have been proposed for the de-distillation of the hydrochloric acid formed, the separation of the resulting mixture of hydrochloric acid, nitric acid and the reaction products of these acids presents considerable difficulties. and calcium nitrate it is possible to obtain sodium nitrate in solution and gypsum as a precipitate.Moreover, it is known that gypsum can be converted with ammonium carbonate into ammonium sulphate and calcium carbonate. Using both of the mentioned reactions it is prepared, according to the present invention, from NaCl, HNO3 and NH3, as raw materials, in the closed circular process of NaNOs and NH4Cl. In the above circular process, the circulation of CaO, SO3 and CO2 as auxiliary means The process is carried out as follows. The solution obtained in the process, containing (NHJ2SO4, NHJ21 and NaCl, is mixed with NaCl in an amount equivalent to (NH4) 2SO ± and NH3 is introduced. The formation of SO2 as a precipitate which separates and is treated with nitric acid together with calcium carbonate which is chilled in the wheel process, resulting in the formation of gypsum and a NaNO3 solution, while the CO2 escapes. The gypsum is separated by decalcification and oozing from the NaNO3 moiety which is evaporated to give solid NaNO3. Instead of evaporating the NaNO 3 solution, it can be cooled to separate some of the NaNO 3 and the mother liquor used to dissolve further amounts of Na 2 SO 4. The lug, containing the Na 2 O.sub.3 moons obtained in the first run, cooled the sieve to separate some NH.sub.4 Cl. To facilitate the release of NH4Cl, NaCl can already be added here, used as a raw material. After separation from NH4Cl, the slurry is saturated with CO2 to produce (NHJ2CO3. The necessary carbonic acid is obtained by the treatment of Na2SO4 and CO3 already described with HNO3. The solution of (NH4) 2CO3, NH4Cl, NaCl thus obtained is mixed with gypsum, obtained in the preparation of NaNO3, while gypsum forms (NH4) 2SO4 and CaCO3. This transformation takes place smoothly, due to the increased solubility of the gypsum in the NH4Cl solution. The solution obtained in this way is the solution mentioned in the introduction (NHJ2SO4) NaCl, NaCl is added to which NaCl is added and NH3 is introduced, resulting in new amounts of Na2SO4 and so on. For better NaJiOi yield, an excess of NaCl, which remains in the circular circulation in the solution, is preferred. Instead of introducing NH3 after conversion of CaSO4 a (NHJ2CO3, NH3 can also be added before the above reaction. This has the advantage that the cold solution, after being separated by NH4Cl cooling, is heated without any more favorable heat for the reaction, because Na2SO4 and CaCOs are treated that you are using HNO3 together, you don't need to sip them separately. On the contrary, common desiccation gives a great practical advantage, because, as is known, the chemically separated CaCO 3 is soaked in its fineness with great difficulty. Of course, high ammonium chloride is recovered and reintroduced into the process before the regeneration of ammonium chloride. PL
Claims (6)
Publications (1)
| Publication Number | Publication Date |
|---|---|
| PL16975B1 true PL16975B1 (en) | 1932-10-31 |
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