CN101244829A - Industrialization technique for processing alkali-making mother solution with hot method, producing ammonium chloride - Google Patents
Industrialization technique for processing alkali-making mother solution with hot method, producing ammonium chloride Download PDFInfo
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- CN101244829A CN101244829A CNA2008100309310A CN200810030931A CN101244829A CN 101244829 A CN101244829 A CN 101244829A CN A2008100309310 A CNA2008100309310 A CN A2008100309310A CN 200810030931 A CN200810030931 A CN 200810030931A CN 101244829 A CN101244829 A CN 101244829A
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- ammonium chloride
- alkali
- evaporation
- temperature
- mother liquor
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Abstract
The invention discloses an industrialized technology for alkali-making mother liquor with heat processing and ammonium chloride production, which comprises the technological processes of degassing, evaporation and separation; a multi-effect evaporation alkali-making mother liquor device is adopted to prepare ammonium chloride, and underground brine is adopted to produce raw material for alkali-making; in addition, hydrochloric acid is utilized to neutralize mother liquor for deamination and deaerating. The industrialization technology of the invention has the advantages of no freezing, low energy consumption, significantly reduced production cost, without water unbalance problem in technological process and without corrosion to titanium material and stainless steel since the temperature of the whole evaporation system is controlled below 105 DEG C; meanwhile, the Oslo and DTB type crystallizer are adopted to separate the ammonium chloride and the sodium chloride, then industrial production is realized.
Description
Technical field
The present invention relates to a kind of chemical production technical, particularly a kind of hot method is handled alkali-making mother solution, is produced the ammonium chloride industrialization technology.
Background technology
All need in the soda ash process industry filtrated stock is handled well, promptly reclaim ammonium chloride and sodium-chlor in the mother liquor.Soda and sociation center is that employing is freezing with mother liquor, drops into solid sodium chloride again, isolates ammonium chloride from mother liquor, the cold process system of being commonly called as ammonium chloride is owing to need to drop into fine solid salt, cost height, freezing energy consumption is big, and has the water imbalance problem that is difficult to overcome.In order to overcome the problems referred to above that exist in the cold process system ammonium chloride, begin one's study both at home and abroad and produce the ammonium chloride technology, but owing to the severe corrosive of ammonium chloride to multiple metal, the equipment corrosion problem is difficult to solve about hot method; System alkali filtrated stock must remove free ammonium and carbon dioxide earlier, and investment is high, and the steam consumption is big; Therefore ammonium chloride and sodium-chlor all are present in the filtrated stock with liquid phase, are difficult to make it to separate out respectively, fail suitability for industrialized production always.
Summary of the invention
The objective of the invention is in order to overcome the above-mentioned weak point of prior art, and provide a kind of cost low, energy consumption is little, and the little hot method of equipment corrosion is handled alkali-making mother solution, produced the ammonium chloride industrialization technology.
For achieving the above object, concrete processing, the production method of the present invention's employing are as follows:
1, the degassing: select for use in the hydrochloric acid and system alkali filtrated stock to PH5-7, remove carbonic acid gas and free ammonium ion.
2, evaporation: will be delivered to the end effect of multi-effect evaporation system, preceding effect successively in the adverse current feeding mode through the system alkali filtrated stock after the degassing, imitate to the head that adopts Olso vaporizer at last and carry out the vacuum temp control evaporation, the first temperature of imitating is controlled at 101 ℃-105 ℃, and 48 ℃-55 ℃ of temperature are imitated at the end.
3, separate: when the feed liquid in the evaporation reaches temperature controlling point, imitate the salt pin sedimentation precipitated sodium chloride of evaporating pot by head, clear liquid in again head being imitated is drawn to and enters draft tube baffle crystallizer after the flasher system cools is cooled to 30 ℃-35 ℃, mould temperature is controlled at 30 ℃-35 ℃, ammonium chloride is separated out with crystal state at low temperatures, and sodium chloride, ammonium chloride are promptly got product respectively after centrifugal drying.
The present invention uses multiple-effect evaporation alkali-making mother solution device and produces ammonium chloride, system alkali raw material can be without salt, and directly adopt subsurface brine production, uses in the hydrochloric acid and the degasification of mother liquor deamination, do not need freezing, energy consumption is little, can reduce production costs significantly, and technological process does not have the water imbalance problem, the temperature of whole vapo(u)rization system is controlled at below 105 ℃, titanium material or special stainless steel are not constituted corrosion, utilize Olso and DTB type crystallizer to carry out separating of ammonium chloride and sodium-chlor, realize suitability for industrialized production.
Embodiment
1, will make the alkali filtrated stock and be delivered to the neutralization reaction jar, adding the hydrochloric acid neutralization makes the mother liquor pH value be stabilized in PH5-7, remove carbonic acid gas and free ammonium ion, the mother liquor composition after the neutralization is roughly: ammonium chloride content 170-186 grams per liter, sodium chloride content 50-70 grams per liter.
2, the mother liquor after will neutralizing, outgasing is pumped to triple effect, two effects, an effect of triple effect vacuum vaporation system successively in the adverse current feeding mode, carry out the vacuum temp control evaporation, one imitates temperature is controlled at 101 ℃-105 ℃, 48 ℃-55 ℃ of triple effect temperature, the thermal source steam directly enters a heating chamber of imitating with downbeam, one secondary steam of imitating the evaporation generation enters two heating chambers of imitating, two secondary steams of imitating the evaporation generation enter the triple effect heating chamber, the secondary steam that triple effect produces enters surface cooler, discharges after being condensed into water.
3, system alkali filtrated stock is through after the vacuum-evaporation, liquid concentration increases, solubility property according to ammonium chloride and sodium-chlor, when feed liquid reaches temperature controlling point, by a salt pin sedimentation precipitated sodium chloride of imitating evaporating pot, enter draft tube baffle crystallizer after again a clear liquid of imitating being drawn to the flasher system cools, mould temperature is controlled at 30 ℃-35 ℃, ammonium chloride is separated out with crystal state at low temperatures, and sodium-chlor, ammonium chloride are promptly got product respectively after centrifugal drying.
Claims (1)
1, a kind of hot method is handled alkali-making mother solution, is produced the ammonium chloride industrialization technology, it is characterized in that through following technical process:
(1), the degassing: select for use in the hydrochloric acid and system alkali filtrated stock to PH5-7, remove carbonic acid gas and free ammonium ion;
(2), evaporation: will be delivered to the end effect of multi-effect evaporation system, preceding effect successively in the adverse current feeding mode through the system alkali filtrated stock after the degassing, imitate to the head that adopts Olso vaporizer at last and carry out the vacuum temp control evaporation, the first temperature of imitating is controlled at 101 ℃-105 ℃, and 48 ℃-55 ℃ of temperature are imitated at the end;
(3), separate: when the feed liquid in the evaporation reaches temperature controlling point, imitate the salt pin sedimentation precipitated sodium chloride of evaporating pot by head, clear liquid in again head being imitated is drawn to and enters draft tube baffle crystallizer after the flasher system cools is cooled to 30 ℃-35 ℃, mould temperature is controlled at 30 ℃-35 ℃, ammonium chloride is separated out with crystal state at low temperatures, and sodium-chlor, ammonium chloride are promptly got product respectively after centrifugal drying.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2008100309310A CN100562493C (en) | 2008-03-26 | 2008-03-26 | Hot method is handled alkali-making mother solution, is produced the ammonium chloride industrialization technology |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2008100309310A CN100562493C (en) | 2008-03-26 | 2008-03-26 | Hot method is handled alkali-making mother solution, is produced the ammonium chloride industrialization technology |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101244829A true CN101244829A (en) | 2008-08-20 |
| CN100562493C CN100562493C (en) | 2009-11-25 |
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| CNB2008100309310A Active CN100562493C (en) | 2008-03-26 | 2008-03-26 | Hot method is handled alkali-making mother solution, is produced the ammonium chloride industrialization technology |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101935128A (en) * | 2010-07-22 | 2011-01-05 | 上海西恩化工设备有限公司 | Process for treating wastewater comprising high-concentration ammonium salt and sodium salt |
| CN101544437B (en) * | 2009-04-30 | 2011-04-27 | 河北工业大学 | Process method for recovering ammonium chloride and sodium chloride from waste water containing ammonium chloride and sodium chloride |
| CN102139983A (en) * | 2011-02-16 | 2011-08-03 | 神华集团有限责任公司 | Waste water treatment method and system |
| CN102992353A (en) * | 2012-12-27 | 2013-03-27 | 衡阳市海联盐卤化工有限公司 | Technology for producing industrial-grade ammonium chloride by quadruple-effect evaporation heat method |
| CN103011199A (en) * | 2012-12-27 | 2013-04-03 | 衡阳市海联盐卤化工有限公司 | Process for deamination and degasification of filtrated stock generated during alkali making |
-
2008
- 2008-03-26 CN CNB2008100309310A patent/CN100562493C/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101544437B (en) * | 2009-04-30 | 2011-04-27 | 河北工业大学 | Process method for recovering ammonium chloride and sodium chloride from waste water containing ammonium chloride and sodium chloride |
| CN101935128A (en) * | 2010-07-22 | 2011-01-05 | 上海西恩化工设备有限公司 | Process for treating wastewater comprising high-concentration ammonium salt and sodium salt |
| CN102139983A (en) * | 2011-02-16 | 2011-08-03 | 神华集团有限责任公司 | Waste water treatment method and system |
| CN102992353A (en) * | 2012-12-27 | 2013-03-27 | 衡阳市海联盐卤化工有限公司 | Technology for producing industrial-grade ammonium chloride by quadruple-effect evaporation heat method |
| CN103011199A (en) * | 2012-12-27 | 2013-04-03 | 衡阳市海联盐卤化工有限公司 | Process for deamination and degasification of filtrated stock generated during alkali making |
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| Publication number | Publication date |
|---|---|
| CN100562493C (en) | 2009-11-25 |
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Address after: 421001 Ring Road in Hunan city of Hengyang province Yanfeng District No. 131 Patentee after: Hunan Hai Lian 31 baking soda Co., Ltd. Address before: 421001 Ring Road in Hunan city of Hengyang province Yanfeng District No. 131 Patentee before: Hengyang Hailian Salt Solution Chemistry Co., Ltd. |