CN1270923A - Non-stop cylinder washing technology for producing sodium carbonate evaportating and crystallizing natural soda - Google Patents

Non-stop cylinder washing technology for producing sodium carbonate evaportating and crystallizing natural soda Download PDF

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Publication number
CN1270923A
CN1270923A CN 99105321 CN99105321A CN1270923A CN 1270923 A CN1270923 A CN 1270923A CN 99105321 CN99105321 CN 99105321 CN 99105321 A CN99105321 A CN 99105321A CN 1270923 A CN1270923 A CN 1270923A
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CN
China
Prior art keywords
stop cylinder
sodium carbonate
evaporating
washing technology
cylinder washing
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN 99105321
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Chinese (zh)
Inventor
李武
丁喜梅
钟志
张永胜
吕斌
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Inner Mongolia Yikezhao Chemical Research And Design Institute
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Inner Mongolia Yikezhao Chemical Research And Design Institute
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Inner Mongolia Yikezhao Chemical Research And Design Institute filed Critical Inner Mongolia Yikezhao Chemical Research And Design Institute
Priority to CN 99105321 priority Critical patent/CN1270923A/en
Publication of CN1270923A publication Critical patent/CN1270923A/en
Pending legal-status Critical Current

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Abstract

The present invention relates to the field of chemical technology. A non-intermittent pot scrubbing technology for making sodium carbonate from trona includes three points of solving the problem in crystallization, the first is to raise the smoothness of evaporating pot and heat-exchanging inner wall; the second is to control the one-effect evaporation temperature at 114-124 deg.C and the two-effect evaporation temperature at 91-101 deg.C to ensure no crystallization of bittern; and the third is to use two evaporating pots alternately during the three-effect evaporation. The technology makes it possible to prolong greatly the scrubbing period of the two-effect evaporating pot.

Description

Urao evaporative crystallization system soda ash non-stop cylinder washing technology
The present invention is a kind of urao evaporative crystallization system soda ash non-stop cylinder washing technology, belongs to chemical field.
In the process of urao evaporative crystallization system soda ash, generally will pass through triple effect evaporation at present, the effect of preceding two-effect evaporation is to concentrate saltwater brine, and triple effect evaporation is to separate out crystal.But a problem that often runs into is in preceding two-effect evaporation process, and evaporating pot and heat transfer tube inwall just begin fouling, when fouling to a certain degree will influencing normal production, thereby have to stop production and remove to clean evaporating pot.So both influenced production, pretty troublesome again, also caused certain waste simultaneously.
In order to solve in the process of urao evaporative crystallization system soda ash, the problem of evaporating pot crystallization fouling, spy of the present invention has proposed a kind of urao evaporative crystallization system soda ash non-stop cylinder washing technology.
Urao evaporative crystallization system soda ash non-stop cylinder washing technology of the present invention, mainly start with and solve the crystallization scale problems from three aspects, first aspect improves the smooth finish of evaporating pot and heat transfer tube inwall, for spraying in the evaporating pot, or make composition board, as titanium steel, stainless steel etc., heat transfer tube also adopts ganoid material, makes as 316L, 314,304 steel; Second aspect is imitated vaporization temperature with one and is controlled between 114~124 ℃, and two temperature of imitating evaporation are controlled between 91~101 ℃, and is non-crystallizable to guarantee saltwater brine; The 3rd is when triple effect evaporation, adopts two evaporating pots, uses by turns.
Evaporating pot in the past adopts carbon steel material more, and its surface is comparatively coarse, form fouling easily, and present technique adopts ganoid material just to overcome this problem; Temperature plays a part very crucial for the crystallization of soda ash, temperature is too high to produce crystallize sodium carbonate easily in advance, and temperature is crossed the low sesquialter alkali crystallization that is easy to generate; One imitates vaporization temperature is controlled between 114~124 ℃, and two temperature of imitating evaporation are controlled between 91~101 ℃, and after tested, in the said temperature section, saltwater brine crystallization fouling probability is minimum; The purpose of triple effect evaporator produces crystallization exactly, and cleaning is inevitably, thereby adopts two evaporating pots to clean by turns and work, can guarantee to produce and normally carry out.Adopt present technique can prolong the cleaning interval that the first two imitates evaporating pot widely.
Embodiment:
Urao evaporative crystallization system soda ash non-stop cylinder washing technology of the present invention, the evaporating pot inwall is made composition board, and outer wall is a plain carbon stool, and inwall is that titanium steel or stainless steel are made, and heat transfer tube adopts the 316L steel to make; One imitates vaporization temperature is controlled between 119 ± 2 ℃, and two temperature of imitating evaporation are controlled between 96 ± 2 ℃; Adopt two triple effect evaporators, use by turns.

Claims (1)

1. urao evaporative crystallization system soda ash non-stop cylinder washing technology is characterized in that:
A. improve the smooth finish of evaporating pot and heat transfer tube inwall, for spraying in the evaporating pot, or make composition board, as titanium steel, stainless steel etc., heat transfer tube also adopts ganoid material, makes as 316L, 314,304 steel;
B. imitate vaporization temperature with one and be controlled between 114~124 ℃, two temperature of imitating evaporation are controlled between 91~101 ℃;
C. when triple effect evaporation, adopt two evaporating pots, use by turns.
CN 99105321 1999-04-19 1999-04-19 Non-stop cylinder washing technology for producing sodium carbonate evaportating and crystallizing natural soda Pending CN1270923A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 99105321 CN1270923A (en) 1999-04-19 1999-04-19 Non-stop cylinder washing technology for producing sodium carbonate evaportating and crystallizing natural soda

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 99105321 CN1270923A (en) 1999-04-19 1999-04-19 Non-stop cylinder washing technology for producing sodium carbonate evaportating and crystallizing natural soda

Publications (1)

Publication Number Publication Date
CN1270923A true CN1270923A (en) 2000-10-25

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ID=5271956

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 99105321 Pending CN1270923A (en) 1999-04-19 1999-04-19 Non-stop cylinder washing technology for producing sodium carbonate evaportating and crystallizing natural soda

Country Status (1)

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CN (1) CN1270923A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105732411A (en) * 2016-03-04 2016-07-06 广东立国制药有限公司 System and process for recovering dimethylacetamide from cefuroxime axetil production waste liquor
CN109084602A (en) * 2018-06-28 2018-12-25 新疆华泰重化工有限责任公司 A method of improving the tubular heat exchanger cycle of operation

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105732411A (en) * 2016-03-04 2016-07-06 广东立国制药有限公司 System and process for recovering dimethylacetamide from cefuroxime axetil production waste liquor
CN109084602A (en) * 2018-06-28 2018-12-25 新疆华泰重化工有限责任公司 A method of improving the tubular heat exchanger cycle of operation

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