CN105797575A - Desulfurizer for gas-fired boiler - Google Patents
Desulfurizer for gas-fired boiler Download PDFInfo
- Publication number
- CN105797575A CN105797575A CN201610181242.4A CN201610181242A CN105797575A CN 105797575 A CN105797575 A CN 105797575A CN 201610181242 A CN201610181242 A CN 201610181242A CN 105797575 A CN105797575 A CN 105797575A
- Authority
- CN
- China
- Prior art keywords
- parts
- desulfurizing agent
- quaternary ammonium
- boiler
- desulfurizer
- 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
Links
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
- B01D53/86—Catalytic processes
- B01D53/8603—Removing sulfur compounds
-
- 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
- B01D53/48—Sulfur compounds
-
- 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
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)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
The invention discloses a desulfurizer for a gas-fired boiler.The desulfurizer is prepared from, by weight, 22-28 parts of sodium hydroxide, 40-48 parts of lime, 13-15 parts of magnesium carbonate, 5-8 parts of sulfoxide, 3-7 parts of MgO, 12-14 parts of activated carbon and 8-10 parts of quaternary ammonium sulfonated cobalt phthalocyanine.The desulfurizer has the advantages that the catalyst quaternary ammonium sulfonated cobalt phthalocyanine is used for carrying out adsorption desulfurization on dusty gas, and thus sulfide in dusty gas is effectively removed.
Description
Technical field
The present invention relates to boiler desulfurization technology, especially, relate to a kind of desulfurizing agent for gas fired-boiler.
Background technology
Dusty gas enters central canal from device bottom, after scrubbed water (certain density NaOH solution) shower humidification, and impact liquid level, finally wait until that form realizes the dust removal process of compound action with atomization, foam, liquid film.
Liquid after desulfation dust-extraction device absorbs, flows through neutralization pond voluntarily, fully reacts under the effect of eddy flow inertia, finally precipitates its mud and impurity, periodic cleaning in sedimentation tank, and clear liquid enters alkali liquor pond (regulation PH), again recycles.
Boiler desulfurization dedusting particular importance on formula, because boiler often uninterruptedly running in 24 hours, needs anticorrosion and high temperature resistant has extra high requirement.
Summary of the invention
Present invention aim at providing a kind of desulfurizing agent for gas fired-boiler, to solve in prior art boiler desulfurization dedusting to anticorrosion and the high temperature resistant problem having high request.
For achieving the above object, the present invention provides a kind of desulfurizing agent for gas fired-boiler, and wherein, described desulfurizing agent is made up of following component in parts by weight:
Sodium hydroxide 22-28 part;
Calx 40-48 part;
Magnesium carbonate 13-15 part;
Sulfoxide 5-8 part;
MgO 3-7 part;
Activated carbon 12-14 part;And
Quaternary ammonium sulfonated phthalocyanine cobalt 8-10 part.
Further, the invention provides a kind of desulfurizing agent for gas fired-boiler, wherein, described desulfurizing agent is made up of following component in parts by weight:
Sodium hydroxide 22 parts;40 parts of Calx;Magnesium carbonate 13 parts;Sulfoxide 6 parts;MgO 5 parts;Activated carbon 12 parts;And quaternary ammonium sulfonated phthalocyanine cobalt 8 parts.
Further, the invention provides a kind of desulfurizing agent for gas fired-boiler, wherein, described desulfurizing agent is made up of following component in parts by weight:
Sodium hydroxide 28 parts;48 parts of Calx;Magnesium carbonate 15 parts;Sulfoxide 6 parts;MgO 7 parts;Activated carbon 13 parts;And quaternary ammonium sulfonated phthalocyanine cobalt 9 parts.
The method have the advantages that and utilize catalyst quaternary ammonium sulfonated phthalocyanine cobalt to carry out dusty gas adsorbing desulfurization, can not only effectively remove the sulfide in dusty gas, and anticorrosion and high temperature resistant.
Detailed description of the invention
A kind of desulfurizing agent for gas fired-boiler that this preferred embodiment provides, it is as follows that it implements process:
Wherein, described desulfurizing agent is made up of following component in parts by weight::
Sodium hydroxide 22-28 part;
Calx 40-48 part;
Magnesium carbonate 13-15 part;
Sulfoxide 5-8 part;
MgO 3-7 part;
Activated carbon 12-14 part;And
Quaternary ammonium sulfonated phthalocyanine cobalt 8-10 part.
Embodiment 1:
Wherein, described desulfurizing agent is made up of following component in parts by weight::
Sodium hydroxide 22 parts;40 parts of Calx;Magnesium carbonate 13 parts;Sulfoxide 6 parts;MgO 5 parts;Activated carbon 12 parts;And quaternary ammonium sulfonated phthalocyanine cobalt 8 parts.
Embodiment 2:
Wherein, described desulfurizing agent is made up of following component in parts by weight::
Sodium hydroxide 28 parts;48 parts of Calx;Magnesium carbonate 15 parts;Sulfoxide 6 parts;MgO 7 parts;Activated carbon 13 parts;And quaternary ammonium sulfonated phthalocyanine cobalt 9 parts.
Wherein, sodium hydrate aqueous solution can extract partially acidic sulfide, the concentration adding sulfoxide polar solvent or raising alkali in sodium hydrate aqueous solution can improve extraction efficiency, and utilize quaternary ammonium cobalt sulfonated phthalocyanine, dusty gas in boiler is processed by alkaline solution, mercaptan therein can be removed, thus effectively remove the sulfide in dusty gas.
As can be seen from the above description, the above embodiments of the present invention achieve following technique effect:
Utilize catalyst quaternary ammonium sulfonated phthalocyanine cobalt to carry out dusty gas adsorbing desulfurization, can not only effectively remove the sulfide in dusty gas, and anticorrosion and high temperature resistant.
The foregoing is only the preferred embodiments of the present invention, be not limited to the present invention;For a person skilled in the art, the present invention can have various modifications and variations.All within the spirit and principles in the present invention, any modification, equivalent substitution and improvement etc. made, should be included within the scope of the present invention.
Claims (3)
1. the desulfurizing agent for gas fired-boiler, it is characterised in that described desulfurizing agent is made up of following component in parts by weight:
Sodium hydroxide 22-28 part;
Calx 40-48 part;
Magnesium carbonate 13-15 part;
Sulfoxide 5-8 part;
MgO 3-7 part;
Activated carbon 12-14 part;And
Quaternary ammonium sulfonated phthalocyanine cobalt 8-10 part.
A kind of desulfurizing agent for gas fired-boiler the most according to claim 1, it is characterised in that described desulfurizing agent is made up of following component in parts by weight:
Sodium hydroxide 22 parts;40 parts of Calx;Magnesium carbonate 13 parts;Sulfoxide 6 parts;MgO 5 parts;Activated carbon 12 parts;And quaternary ammonium sulfonated phthalocyanine cobalt
8 parts.
A kind of desulfurizing agent for gas fired-boiler the most according to claim 1, it is characterised in that described desulfurizing agent is made up of following component in parts by weight:
Sodium hydroxide 28 parts;48 parts of Calx;Magnesium carbonate 15 parts;Sulfoxide 6 parts;MgO 7 parts;Activated carbon 13 parts;And quaternary ammonium sulfonated phthalocyanine cobalt
9 parts.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610181242.4A CN105797575A (en) | 2016-03-28 | 2016-03-28 | Desulfurizer for gas-fired boiler |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610181242.4A CN105797575A (en) | 2016-03-28 | 2016-03-28 | Desulfurizer for gas-fired boiler |
Publications (1)
Publication Number | Publication Date |
---|---|
CN105797575A true CN105797575A (en) | 2016-07-27 |
Family
ID=56453947
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201610181242.4A Pending CN105797575A (en) | 2016-03-28 | 2016-03-28 | Desulfurizer for gas-fired boiler |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN105797575A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106905992A (en) * | 2017-03-13 | 2017-06-30 | 宜兴市星光宝亿化工有限公司 | A kind of environment protection treating efficient desulfurizing agent and preparation method thereof |
CN112072187A (en) * | 2020-10-12 | 2020-12-11 | 天能集团(河南)能源科技有限公司 | Lead-acid storage battery electrolyte and preparation method thereof |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1621133A (en) * | 2003-11-24 | 2005-06-01 | 杨军 | Absorption liquid for gas desulfurization and its application |
CN101785962A (en) * | 2009-01-23 | 2010-07-28 | 莱克斯坦有限公司 | Method for removing acid gas from waste gas |
CN102921464A (en) * | 2012-10-30 | 2013-02-13 | 陕西启源科技发展有限责任公司 | Preparation method of sulfonated cobalt phthalocyanine catalyst |
-
2016
- 2016-03-28 CN CN201610181242.4A patent/CN105797575A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1621133A (en) * | 2003-11-24 | 2005-06-01 | 杨军 | Absorption liquid for gas desulfurization and its application |
CN101785962A (en) * | 2009-01-23 | 2010-07-28 | 莱克斯坦有限公司 | Method for removing acid gas from waste gas |
CN102921464A (en) * | 2012-10-30 | 2013-02-13 | 陕西启源科技发展有限责任公司 | Preparation method of sulfonated cobalt phthalocyanine catalyst |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106905992A (en) * | 2017-03-13 | 2017-06-30 | 宜兴市星光宝亿化工有限公司 | A kind of environment protection treating efficient desulfurizing agent and preparation method thereof |
CN112072187A (en) * | 2020-10-12 | 2020-12-11 | 天能集团(河南)能源科技有限公司 | Lead-acid storage battery electrolyte and preparation method thereof |
CN112072187B (en) * | 2020-10-12 | 2021-11-19 | 天能集团(河南)能源科技有限公司 | Lead-acid storage battery electrolyte and preparation method thereof |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR101329523B1 (en) | Ammonium/ammonia removal from a stream | |
ES2552629T3 (en) | Method to remove flue gas condensate impurities | |
CN101678268A (en) | Removal of carbon dioxide from flue gas streams using mixed ammonium/alkali solutions | |
CN105797575A (en) | Desulfurizer for gas-fired boiler | |
CN104437056B (en) | A kind of flue gas desulfurization device | |
EA200701642A1 (en) | TREATMENT OF A WATER MIXTURE CONTAINING ALKYLENE OXIDE WITH THE HELP OF ION EXCHANGE RESIN | |
CN102423612A (en) | Method for producing thiosulfate and recovering carbon dioxide by utilizing industrial flue gas | |
CN204338002U (en) | A kind of flue gas desulfur device | |
CN209501361U (en) | Novel energy-conserving Complexing Iron desulphurization plant | |
CN104689700A (en) | Zinc oxide desulfurization process | |
CN109464889A (en) | A kind of technique and its system for ocean platform gas cleaning | |
KR101549089B1 (en) | Method for acidic gas absorption comprising regenerating process of anion exchang resin using anion metal hydroxide regenerent | |
CN112403214B (en) | Flue gas desulfurization tower | |
CN111729474B (en) | Method for circulating flue gas desulfurization and sulfur dioxide recovery by using organic acid magnesium solution | |
CN206262350U (en) | Smoke-gas wet desulfurization equipment based on sodium carbonate | |
JP2016515044A5 (en) | ||
CN102452674B (en) | Processing method for recycling sodium sulfate from waste alkali liquor in ethylene unit | |
CN207581563U (en) | A kind of novel ammonia water circulation desulfurization system | |
CN105771594A (en) | Zinc oxide desulfurization process | |
CN208512244U (en) | A kind of dual-alkali flue gas desulfurization device | |
JP2013188649A (en) | Sulfur trioxide removal system, sulfur trioxide removing method, and carbon dioxide recovery system | |
CN205461743U (en) | Two alkali flue gas desulfurization systems of sodium calcium | |
TWI675698B (en) | Settling film hydrogen sulfide absorption tower for waste tire cracking gas | |
CN102085450A (en) | Integrated desulfuration and dust removal method for medium and small boiler flue gas | |
CN102553423A (en) | Method for removing sulfur dioxide in flue gas by using brine purifying residues |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20160727 |
|
RJ01 | Rejection of invention patent application after publication |