CN109444274A - CO in a kind of high concentration NaOH leacheate2And CO32-The method of removal - Google Patents
CO in a kind of high concentration NaOH leacheate2And CO32-The method of removal Download PDFInfo
- Publication number
- CN109444274A CN109444274A CN201810871777.3A CN201810871777A CN109444274A CN 109444274 A CN109444274 A CN 109444274A CN 201810871777 A CN201810871777 A CN 201810871777A CN 109444274 A CN109444274 A CN 109444274A
- Authority
- CN
- China
- Prior art keywords
- mouth
- calcium hydroxide
- removal
- ultrapure water
- mouth flask
- 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
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Classifications
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N30/00—Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
- G01N30/02—Column chromatography
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/74—Separation; Purification; Use of additives, e.g. for stabilisation
- C07C29/88—Separation; Purification; Use of additives, e.g. for stabilisation by treatment giving rise to a chemical modification of at least one compound
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07H—SUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
- C07H1/00—Processes for the preparation of sugar derivatives
- C07H1/06—Separation; Purification
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07H—SUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
- C07H3/00—Compounds containing only hydrogen atoms and saccharide radicals having only carbon, hydrogen, and oxygen atoms
- C07H3/04—Disaccharides
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B37/00—Preparation of polysaccharides not provided for in groups C08B1/00 - C08B35/00; Derivatives thereof
- C08B37/0003—General processes for their isolation or fractionation, e.g. purification or extraction from biomass
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N30/00—Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
- G01N30/02—Column chromatography
- G01N30/04—Preparation or injection of sample to be analysed
- G01N30/06—Preparation
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N30/00—Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
- G01N30/96—Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation using ion-exchange
Abstract
The present invention relates to CO in a kind of high concentration NaOH leacheate2And CO3 2‑The method of removal, including operating as follows: preparing the two mouth flask of certain capacity, connect ultrapure water and be placed on spare on water-bath type magnetic stirring apparatus, and be wherein put into clean stirrer, stirring always in the process;One mouth of two mouth flask connects triple valve, and the triple valve lower end insertion bottleneck, upper termination helium, Centronics port connect air extractor;Another mouth of two mouth flask connects elbow drying tube, and the bottom end of the drying tube spreads one layer of absorbent cotton, prevents calcium hydroxide to be inhaled into, enough calcium hydroxide is filled in absorbent cotton upper end, covers one layer of absorbent cotton again on calcium hydroxide, prevents calcium hydroxide from spraying.The present invention provides a kind of methods of the carbon dioxide in removal leacheate, to achieve the effect that separation sugar and sugar alcohol.
Description
Technical field
The present invention relates to atmospheric science technical fields, and in particular to CO in a kind of high concentration NaOH leacheate2And CO3 2-It goes
The method removed.
Background technique
In the prior art, mostly be for ion chromatograph analysis zwitterion method, such as CN102749412, with from
Anion in sub- chromatography measurement milk.But it is fewer for the method for surveying sugar, and surveyed in the lab using the chromatography of ions
When sugared, can mostly encounter has the indissociable situation of 2-3 kind sugar, and this method passes through the CO in removal leacheate2, to reach
The purpose for allowing part sugar and sugar alcohol to separate.
Summary of the invention
The present invention provides CO in a kind of high concentration NaOH leacheate2And CO3 2-The method of removal removes in leacheate
Carbon dioxide, to achieve the effect that separation sugar and sugar alcohol.
To achieve the above object, present invention provide the technical scheme that
CO in a kind of high concentration NaOH leacheate2And CO3 2-The method of removal, including operate as follows:
1) two mouth flask for preparing certain capacity, connect ultrapure water be placed on it is spare on water-bath type magnetic stirring apparatus, and wherein
It is put into clean stirrer, is stirred always in the process;
2) mouth of two mouth flask connects triple valve, and bottleneck, upper termination helium, Centronics port are inserted into the triple valve lower end
Connect air extractor;
3) another mouth of two mouth flask connects elbow drying tube, and the bottom end of the drying tube spreads one layer of absorbent cotton, prevents hydrogen
Calcium oxide is inhaled into, and enough calcium hydroxide is filled in absorbent cotton upper end, covers one layer of absorbent cotton again on calcium hydroxide, is prevented
Only calcium hydroxide sprays;
4) ultrapure water degasification is first given, with air extractor, 30min is persistently evacuated, opens triple valve lower channel, replacement of helium
Into flask, in triplicate;
5) temperature control device for opening water-bath type magnetic stirring apparatus, ultrapure water is heated to boiling, is cooled to room temperature;
6) quantitative calcium hydroxide is added in cooling ultrapure water, with 0.25 μm of filter after waiting reactions a period of time
Filter ultrapure water;
Prepare two two mouth flasks, equally progress aforesaid operations, then takes one of two mouth flask that sodium hydroxide is added
Leacheate is prepared, another two mouth flask is taken to do rinse water.
Carbonate concentration in step 6) ultrapure water is 0.09~0.9mg/L.
Further, in step 6), 0.001g calcium hydroxide is added in every 1L ultrapure water.
The two mouth flask is 2L two mouth flask.
Compared with prior art, the beneficial effects of the present invention are:
Ion chromatograph survey sugar during, influenced by carbon dioxide in leacheate, cannot separate it is some sugar and
Sugar alcohol, such as: D-sorbite, trehalose and mannosan, antierythrite and D- threitol.Of the invention is handled by this method
Later, to be not completely separated sugar, sugar alcohol separation can improve separation.
Detailed description of the invention
Fig. 1: the device of the invention structural schematic diagram.
Fig. 2: method flow schematic diagram of the invention.
Fig. 3: separating effect figure is improved.
Specific embodiment
The present invention is further explained in the light of specific embodiments.
(1) with the two mouth flask (such as Fig. 1) of two 2L connect respectively 2L ultrapure water be placed on it is spare on water-bath type magnetic stirring apparatus,
It is wherein being put into clean stirrer, is being stirred always in the process;
(2) triple valve is connect flatly wherein, bottleneck, upper termination helium are inserted into triple valve lower end, and Centronics port connects pumping dress
It sets;
(3) elbow drying tube is connect in another mouth, drying tube bottom end spreads one layer of absorbent cotton, calcium hydroxide is prevented to be inhaled into, and takes off
Enough calcium hydroxide is filled in rouge cotton upper end, covers one layer of absorbent cotton again on calcium hydroxide, prevents calcium hydroxide from spraying;
(4) ultrapure water degasification is first given, with air extractor, 30min is persistently evacuated, opens triple valve lower channel, replace helium
Gas is into flask, in triplicate;
(5) temperature control device for opening water-bath type magnetic stirring apparatus, ultrapure water is heated to boiling, is cooled to room temperature;
(6) quantitative calcium hydroxide is added in cooling ultrapure water, with 0.25 μm of filtering after waiting reactions a period of time
Device filters ultrapure water;
(7) take wherein one bottle of addition sodium hydroxide prepare leacheate, another bottle does rinse water;
(8) it is verified on ion chromatograph.
In operation it is noted that container pressure problem, prevents calcium hydroxide to be inhaled into or spray.Through the invention
Experiment separation can be improved to sugar indissociable in leacheate.
The above is only presently preferred embodiments of the present invention, is not intended to limit the present invention in any form, any ripe
Professional and technical personnel is known, without departing from the scope of the present invention, according to the technical essence of the invention, to above
Any simple modifications, equivalent substitutions and improvements etc., fall within the scope of protection of the technical scheme of the present invention made by embodiment
Within.
Claims (5)
1. CO in a kind of high concentration NaOH leacheate2And CO3 2-The method of removal, it is characterised in that: including operating as follows:
1) two mouth flask for preparing certain capacity connects ultrapure water and is placed on spare on water-bath type magnetic stirring apparatus, and is put into wherein
Clean stirrer, is stirred always in the process;
2) mouth of two mouth flask connects triple valve, and the triple valve lower end insertion bottleneck, upper termination helium, Centronics port connect pumping
Device of air;
3) another mouth of two mouth flask connects elbow drying tube, and the bottom end of the drying tube spreads one layer of absorbent cotton, prevents hydroxide
Calcium is inhaled into, and enough calcium hydroxide is filled in absorbent cotton upper end, is covered one layer of absorbent cotton again on calcium hydroxide, is prevented hydrogen-oxygen
Change calcium to spray;
4) ultrapure water degasification is first given, with air extractor, is persistently evacuated 30min, opens triple valve lower channel, replacement of helium is into burning
Bottle, in triplicate;
5) temperature control device for opening water-bath type magnetic stirring apparatus, ultrapure water is heated to boiling, is cooled to room temperature;
6) quantitative calcium hydroxide is added in cooling ultrapure water, is filtered after waiting reactions a period of time with 0.25 μm of filter
Ultrapure water.
2. CO in high concentration NaOH leacheate according to claim 12And CO3 2-The method of removal, it is characterised in that: prepare
Then two two mouth flasks, equally progress aforesaid operations take one of two mouth flask that sodium hydroxide is added and prepare leacheate, take
Another two mouth flask does rinse water.
3. CO in high concentration NaOH leacheate according to claim 12And CO3 2-The method of removal, it is characterised in that: step
6) carbonate concentration in ultrapure water is 0.09~0.9mg/L.
4. CO in high concentration NaOH leacheate according to claim 12And CO3 2-The method of removal, it is characterised in that: step
6) in, 0.001g calcium hydroxide is added in every 1L ultrapure water.
5. CO in high concentration NaOH leacheate according to claim 12And CO3 2-The method of removal, it is characterised in that: described
Two mouth flask be 2L two mouth flask.
Priority Applications (1)
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CN201810871777.3A CN109444274A (en) | 2018-08-02 | 2018-08-02 | CO in a kind of high concentration NaOH leacheate2And CO32-The method of removal |
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CN201810871777.3A CN109444274A (en) | 2018-08-02 | 2018-08-02 | CO in a kind of high concentration NaOH leacheate2And CO32-The method of removal |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112569793A (en) * | 2020-12-25 | 2021-03-30 | 苏州明昊色谱技术有限公司 | Degassing-free trace anion impurity online remover and removing method in strong alkali solution |
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CN202478952U (en) * | 2012-02-22 | 2012-10-10 | 凤台县精华助剂有限公司 | Seal device for distillation flask |
US20150306564A1 (en) * | 2014-04-28 | 2015-10-29 | Korea University Research And Business Foundation | Carbon dioxide adsorbent including alkali metal double salts and methods for preparing the same |
CN105638552A (en) * | 2016-03-18 | 2016-06-08 | 中国水产科学研究院淡水渔业研究中心 | Fishery culture device capable of removing carbon dioxide in water body and use method |
-
2018
- 2018-08-02 CN CN201810871777.3A patent/CN109444274A/en active Pending
Patent Citations (3)
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CN202478952U (en) * | 2012-02-22 | 2012-10-10 | 凤台县精华助剂有限公司 | Seal device for distillation flask |
US20150306564A1 (en) * | 2014-04-28 | 2015-10-29 | Korea University Research And Business Foundation | Carbon dioxide adsorbent including alkali metal double salts and methods for preparing the same |
CN105638552A (en) * | 2016-03-18 | 2016-06-08 | 中国水产科学研究院淡水渔业研究中心 | Fishery culture device capable of removing carbon dioxide in water body and use method |
Non-Patent Citations (5)
Title |
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刘玉峰等: "离子色谱法在糖和糖醇分析检测中的应用研究", 《北京工商大学学报(自然科学版)》 * |
北京医学院药学系药化教研组: "《药物化学》", 31 December 1960 * |
唐坤甜等: "高效阴离子交换色谱分离-脉冲安培检测法测定烟草料液中的糖、糖醇和醇类化合物", 《分析化学》 * |
夏玉宇: "《化验员实用手册》", 31 May 2001 * |
张水锋等: "梯度洗脱优化-离子色谱-脉冲安培法分析婴幼儿配方乳粉中的糖和糖醇", 《色谱》 * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112569793A (en) * | 2020-12-25 | 2021-03-30 | 苏州明昊色谱技术有限公司 | Degassing-free trace anion impurity online remover and removing method in strong alkali solution |
CN112569793B (en) * | 2020-12-25 | 2021-11-23 | 苏州明昊色谱技术有限公司 | Degassing-free trace anion impurity online remover and removing method in strong alkali solution |
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Application publication date: 20190308 |
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