CN113398734A - Auxiliary agent for accelerating capture of carbon dioxide by nanofiltration of seawater - Google Patents
Auxiliary agent for accelerating capture of carbon dioxide by nanofiltration of seawater Download PDFInfo
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- CN113398734A CN113398734A CN202110700480.2A CN202110700480A CN113398734A CN 113398734 A CN113398734 A CN 113398734A CN 202110700480 A CN202110700480 A CN 202110700480A CN 113398734 A CN113398734 A CN 113398734A
- Authority
- CN
- China
- Prior art keywords
- carbon dioxide
- seawater
- auxiliary agent
- capture
- nanofiltration
- 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.)
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- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 title claims abstract description 59
- 229910002092 carbon dioxide Inorganic materials 0.000 title claims abstract description 33
- 239000013535 sea water Substances 0.000 title claims abstract description 30
- 239000001569 carbon dioxide Substances 0.000 title claims abstract description 29
- 238000001728 nano-filtration Methods 0.000 title claims abstract description 18
- 239000012752 auxiliary agent Substances 0.000 title claims abstract description 17
- FPAFDBFIGPHWGO-UHFFFAOYSA-N dioxosilane;oxomagnesium;hydrate Chemical compound O.[Mg]=O.[Mg]=O.[Mg]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O FPAFDBFIGPHWGO-UHFFFAOYSA-N 0.000 claims abstract description 17
- WVRXNIBQZAKZTE-UHFFFAOYSA-N 1-methylidene-2h-naphthalene Chemical compound C1=CC=C2C(=C)CC=CC2=C1 WVRXNIBQZAKZTE-UHFFFAOYSA-N 0.000 claims abstract description 6
- OMKBBIQIHSBGRL-UHFFFAOYSA-N 1-methylidene-2h-naphthalene;sodium Chemical group [Na].C1=CC=C2C(=C)CC=CC2=C1 OMKBBIQIHSBGRL-UHFFFAOYSA-N 0.000 claims abstract description 5
- -1 potassium methylene naphthalene Chemical compound 0.000 claims abstract description 4
- 238000002156 mixing Methods 0.000 claims abstract description 3
- 239000002245 particle Substances 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 1
- 239000002994 raw material Substances 0.000 abstract description 5
- 238000006243 chemical reaction Methods 0.000 abstract description 2
- 239000003795 chemical substances by application Substances 0.000 abstract description 2
- 238000002425 crystallisation Methods 0.000 abstract description 2
- 230000008025 crystallization Effects 0.000 abstract description 2
- 239000003337 fertilizer Substances 0.000 abstract description 2
- 239000000203 mixture Substances 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 7
- 229910052799 carbon Inorganic materials 0.000 description 7
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 4
- 238000001556 precipitation Methods 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000011777 magnesium Substances 0.000 description 3
- 230000009919 sequestration Effects 0.000 description 3
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 230000033558 biomineral tissue development Effects 0.000 description 2
- 239000012267 brine Substances 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- 229910052791 calcium Inorganic materials 0.000 description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 description 2
- 238000010612 desalination reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910052749 magnesium Inorganic materials 0.000 description 2
- 239000000395 magnesium oxide Substances 0.000 description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 2
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 1
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 description 1
- 239000000347 magnesium hydroxide Substances 0.000 description 1
- 229910001862 magnesium hydroxide Inorganic materials 0.000 description 1
- NEKPCAYWQWRBHN-UHFFFAOYSA-L magnesium;carbonate;trihydrate Chemical compound O.O.O.[Mg+2].[O-]C([O-])=O NEKPCAYWQWRBHN-UHFFFAOYSA-L 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/62—Carbon oxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/50—Carbon oxides
- B01D2257/504—Carbon dioxide
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/40—Capture or disposal of greenhouse gases of CO2
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treating Waste Gases (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention discloses an auxiliary agent for accelerating carbon dioxide capture of nanofiltration seawater, which is characterized by comprising the following components in percentage by weight: the talcum powder is prepared by mixing 85-95 wt% of talcum powder and 5-15 wt% of methylene naphthalene sulfonate; the talcum powder is 600-800 meshes and has the density of 0.41-0.45 g/cm3(ii) a The methylene naphthalene sulfonate is sodium methylene naphthalene sulfonate or potassium methylene naphthalene sulfonate. The auxiliary agent can not only remarkably accelerate the capture of carbon dioxide by the nanofiltration seawater, but also the reaction crystallization mixture can be used as an important raw material of a fertilizer anti-caking agent.
Description
Technical Field
The invention relates to the technical field of seawater resource utilization and carbon fixation, in particular to a method for trapping carbon dioxide by nanofiltration seawater, and particularly relates to an auxiliary agent for accelerating the trapping of carbon dioxide by nanofiltration seawater.
Background
In the face of the crisis caused by the continuously worsening greenhouse effect, various countries agree to take measures to reduce the carbon dioxide emission, and China has promised that the carbon emission reaches the peak value in about 2030 years. However, emission control and capture of carbon dioxide (CCS) remains a major challenge for the global environment. Sequestration and sequestration of carbon dioxide has been the focus of efforts and research by researchers, and attempts have been made to introduce a new approach to carbon dioxide utilization for more thorough and efficient carbon capture and sequestration. Research indicates that mineralization is a new direction for utilizing carbon dioxide, and the advantages of environmental protection, low cost and the like attract the research attention of people. Under another serious threat of shortage of fresh water resources, further research on carbon dioxide mineralization is pushed by carbon capture and utilization by seawater. The two are combined, so that not only is the fixed utilization of carbon dioxide realized, but also the utilization of seawater pretreatment or brine waste from a seawater desalination plant can be solved.
Thus by being Mg-rich2+、Ca2+May be another promising approach to the carbon dioxide problem. Especially the use of carbon dioxide by seawater/concentrated seawater is very attractive, since it solves two problems simultaneously, on the one hand CO2On the other hand, the problem of seawater pretreatment or brine waste from a seawater desalination plant can be solved. Especially CO-producing chemical products with high added value, is CO2A new approach to utilization.
Zhao et al examined carbon dioxide in CO under different conditions2The method comprises the steps of-a dissolution equilibrium process in a seawater system, and provides flue gas carbon fixation seawater decalcification process and mechanism research which are enhanced by taking sodium hydroxide as a medium, and then, the carbon fixation decalcification process which takes magnesium oxide, magnesium hydroxide and white mud as an alkali source is examined, wherein the carbon fixation decalcification effect and the economy of the magnesium oxide as the alkali source are the best. G.M.Jose-Luis et al propose to utilize rich calcium and magnesium seawater to capture and utilize CO2In the process, a multistage precipitation method is used, calcium carbonate is separated out in the first-stage precipitation method, and pure magnesium carbonate trihydrate is separated out in the second-stage precipitation method. Y.ZHao et al also propose a two-step precipitation method-using the calcium and magnesium resources in seawater to make CO2The carbonate radical and bicarbonate radical dissolved in sea water are respectively sealed and stored into calcium carbonate and magnesium carbonate salt.
Disclosure of Invention
The invention aims to solve the technical problem of providing the auxiliary agent for accelerating the capture of carbon dioxide by the nanofiltration seawater.
To solve the technical problems, the technical scheme adopted by the invention is as follows:
the auxiliary agent for accelerating carbon dioxide capture of nanofiltration seawater is characterized by comprising the following components in percentage by weight: the talcum powder is prepared by mixing 85-95 wt% of talcum powder and 5-15 wt% of methylene naphthalene sulfonate.
The particle size of the talcum powder is 600 meshes to 800 meshes, and the density of the talcum powder is 0.41g/cm to 0.45g/cm3。
The methylene naphthalene sulfonate is sodium methylene naphthalene sulfonate or potassium methylene naphthalene sulfonate.
The auxiliary agent of the invention not only can remarkably accelerate the capture of carbon dioxide by nanofiltration seawater, but also the reaction crystallization mixture can be used as one of important raw materials of a fertilizer anti-caking agent. Can effectively reduce the economic cost of carbon dioxide capture while realizing the high-efficiency removal of carbon dioxide, and is suitable for industrial use.
Detailed Description
The present invention will be described in further detail with reference to specific examples, but the present invention is not limited to the specific examples.
Example 1
The auxiliary agent for accelerating carbon dioxide capture by nanofiltration seawater in the embodiment comprises the following raw materials in percentage by weight: talcum powder 85% and sodium methylene naphthalene sulfonate 15%. The particle size of the talcum powder is 600 meshes, and the density is 0.41g/cm3。
Example 2
The auxiliary agent for accelerating carbon dioxide capture by nanofiltration seawater in the embodiment comprises the following raw materials in percentage by weight: 90% of talcum powder and 10% of potassium methylene naphthalene sulfonate. The particle size of the talcum powder is 800 meshes, and the density is 0.45g/cm3。
Example 3
The auxiliary agent for accelerating carbon dioxide capture by nanofiltration seawater in the embodiment comprises the following raw materials in percentage by weight: 95% of talcum powder and 5% of sodium methylene naphthalene sulfonate. The particle size of the talcum powder is 700 meshes, and the density is 0.43g/cm 3.
The auxiliary agent for accelerating carbon dioxide capture by nanofiltration seawater obtained in the embodiments 1 to 3 is used in an experiment for absorbing carbon dioxide by nanofiltration seawater according to a generally recommended amount of the auxiliary agent, and the detection result is as follows:
blank space | Example 1 | Example 2 | Example 3 | |
The dosage of the auxiliary agent is Kg/t | 5 | 5 | 5 | |
Nanofiltration of seawater for CO capture2Amount kg/m3 | 5.61 | 5.86 | 5.96 | 5.88 |
。
Claims (3)
1. The auxiliary agent for accelerating carbon dioxide capture of nanofiltration seawater is characterized by comprising the following components in percentage by weight: the talcum powder is prepared by mixing 85-95 wt% of talcum powder and 5-15 wt% of methylene naphthalene sulfonate.
2. The accelerated nanofiltration sea of claim 1The auxiliary agent for capturing carbon dioxide by water is characterized in that: the particle size of the talcum powder is 600 meshes to 800 meshes, and the density of the talcum powder is 0.41g/cm to 0.45g/cm3。
3. The auxiliary agent for accelerating carbon dioxide capture of nanofiltration seawater according to claim 1, which is characterized in that: the methylene naphthalene sulfonate is sodium methylene naphthalene sulfonate or potassium methylene naphthalene sulfonate.
Priority Applications (1)
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CN202110700480.2A CN113398734A (en) | 2021-06-23 | 2021-06-23 | Auxiliary agent for accelerating capture of carbon dioxide by nanofiltration of seawater |
Applications Claiming Priority (1)
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CN202110700480.2A CN113398734A (en) | 2021-06-23 | 2021-06-23 | Auxiliary agent for accelerating capture of carbon dioxide by nanofiltration of seawater |
Publications (1)
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CN113398734A true CN113398734A (en) | 2021-09-17 |
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CN202110700480.2A Withdrawn CN113398734A (en) | 2021-06-23 | 2021-06-23 | Auxiliary agent for accelerating capture of carbon dioxide by nanofiltration of seawater |
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Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101773766A (en) * | 2008-11-21 | 2010-07-14 | 林健峰 | Method for trapping carbon dioxide |
CN106731639A (en) * | 2017-03-03 | 2017-05-31 | 河北工业大学 | A kind of new sea water desulfuration Carbon fixation method |
CN107043292A (en) * | 2017-03-06 | 2017-08-15 | 广东新绿源化工有限公司 | A kind of oyster shell whiting chemical fertilizer anti-caking agent |
CN109701362A (en) * | 2019-02-28 | 2019-05-03 | 华能国际电力股份有限公司 | Liquid-solid phase change absorbent for capturing carbon dioxide and application thereof |
-
2021
- 2021-06-23 CN CN202110700480.2A patent/CN113398734A/en not_active Withdrawn
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101773766A (en) * | 2008-11-21 | 2010-07-14 | 林健峰 | Method for trapping carbon dioxide |
CN106731639A (en) * | 2017-03-03 | 2017-05-31 | 河北工业大学 | A kind of new sea water desulfuration Carbon fixation method |
CN107043292A (en) * | 2017-03-06 | 2017-08-15 | 广东新绿源化工有限公司 | A kind of oyster shell whiting chemical fertilizer anti-caking agent |
CN109701362A (en) * | 2019-02-28 | 2019-05-03 | 华能国际电力股份有限公司 | Liquid-solid phase change absorbent for capturing carbon dioxide and application thereof |
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Application publication date: 20210917 |