[go: up one dir, main page]

CN113069907A - Preparation method of wet-process complex iron desulfurizer - Google Patents

Preparation method of wet-process complex iron desulfurizer Download PDF

Info

Publication number
CN113069907A
CN113069907A CN202110498463.5A CN202110498463A CN113069907A CN 113069907 A CN113069907 A CN 113069907A CN 202110498463 A CN202110498463 A CN 202110498463A CN 113069907 A CN113069907 A CN 113069907A
Authority
CN
China
Prior art keywords
solution
complex iron
stirring
ferric chloride
edta
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
CN202110498463.5A
Other languages
Chinese (zh)
Inventor
齐建光
沈媛媛
孟凡庆
李鑫
王英龙
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Qingdao University of Science and Technology
Original Assignee
Qingdao University of Science and Technology
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 Qingdao University of Science and Technology filed Critical Qingdao University of Science and Technology
Priority to CN202110498463.5A priority Critical patent/CN113069907A/en
Publication of CN113069907A publication Critical patent/CN113069907A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/77Liquid phase processes
    • B01D53/78Liquid phase processes with gas-liquid contact
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/48Sulfur compounds

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)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

The invention discloses an improved technology for removing sulfide from a gas mixture by a complex iron method, and provides a desulfurization solution with a multi-component combination and a corresponding desulfurization process thereof. The complex iron desulfurizer solution synthesized by the process has the advantages of good desulfurization performance, safe equipment operation, good operation elasticity, simple preparation method and the like.

Description

Preparation method of wet-process complex iron desulfurizer
[ technical field ] A method for producing a semiconductor device
The invention discloses a preparation method of a complex iron desulfurizer by multi-component wet desulphurization, belonging to the field of acid gas purification. The complex iron desulfurizer solution synthesized by the invention has the advantages of good desulfurization performance, safe equipment operation, good operation elasticity, simple preparation method and the like.
[ background of the invention ]
Because of the enhancement of the environmental awareness of people and the relation to the national civilization, the desulfurization becomes an important working section in the chemical industry. Desulfurization analysis is an important component in desulfurization industrial production for monitoring key parameters such as gas components, desulfurization solution, catalyst concentration, suspended sulfur and the like in real time in order to ensure normal operation of a desulfurization process. The high-efficiency desulfurizer is not beneficial to large-scale industrial popularization due to high price, and a complex iron desulfurization system is researched and screened, has good stability under the condition of partial alkali and high sulfur capacity, and is beneficial to large-scale industrial application.
At present, many complex iron desulfurization systems are being researched, and China also conducts research on the research and development of complex iron desulfurizing agents. And adding a stabilizer of anhydrous glucose in the process, and adjusting the pH value of the desulfurization solution to 8-10 by using a buffer solution. The method improves the desulfurization efficiency of the complex iron desulfurizer; the corrosion of equipment is reduced; the generated sulfur particles and the desulfurization mother liquor are easy to separate; the regeneration needs short time and low energy consumption. But most of them stay at the laboratory level, and the purpose of this research is to carry out large-scale industrial popularization. The complex iron system studied by the process mainly comprises FeSO4EDTA, ammonia water, organic phosphate, stabilizer, compared with the commercial desulfurizing agents such as 888, MSQ, ADA and the like, the desulfurizing agent is more economical and has more market competitiveness. The screened desulfurizer has high sulfur capacity and good regeneration performance.
The invention adopts ferric chloride as a raw material to synthesize the complex iron desulfurizer, and provides a novel preparation method of the wet complex iron desulfurizer.
[ summary of the invention ]
[ problem to be solved ]
Aiming at the defects in the prior art, the invention aims to complex an iron desulfurizer by a wet method, so that the newly synthesized desulfurizer can efficiently remove sulfides from a gas mixture, thereby reducing equipment corrosion and solving the problems of poor stability of a desulfurization solution, high desulfurization cost, low reaction rate and the like in a desulfurization process.
[ solution ]
The invention is realized by the following technical scheme.
An improved complex iron method for removing sulfide from a gas mixture comprises the following components in percentage by weight: 10-100 ppm of an antioxidant, 5-50 ppm of a surfactant, and the balance of a complex iron catalyst and water, wherein the complex iron catalyst is composed of a complexing agent, deionized water, ammonia water and ferric chloride, and the complex iron desulfurizer is prepared by the following method.
Adding a complexing agent, deionized water and ammonia water into a reactor with a stirring function and a heating function, starting stirring, and heating to 100-150 ℃. EDTA was added with stirring.
Then, ferric chloride is dissolved in the aqueous solution, and the solution releases heat and is continuously stirred until all the solvent is obtained.
And finally, slowly dropwise adding the dissolved ferric chloride solution into the EDTA ammonia water solution, stirring for about 1h, and stabilizing to obtain the EDTA ferric amine solution after the improved process.
[ advantageous effects ]
Compared with the prior art, the invention mainly has the following beneficial effects:
(1) the complex iron desulfurizer solution prepared by the method can obtain a high-performance desulfurization effect, and solves the problem that sulfides in the mixture are difficult to remove.
(2) The method has the advantages of simple process, less investment equipment and high iron content in the iron-synthesizing desulfurizer.
[ description of the drawings ]
FIG. 1 is a diagram of the operating equipment of the preparation method of wet complex iron desulfurizer.
[ detailed description ] embodiments
Example 1:
100mL of deionized water, 97g of ferric chloride and 2mL of sulfuric acid are taken. 97g of ferric chloride is slowly dissolved into 100mL of deionized water, and then the mixture is continuously stirred, the reaction releases heat, and the ferric chloride is slowly dissolved without continuous stirring. After complete dissolution, the mixture is left to stand to room temperature. Then weighing 100g of EDTA and 200mL of ammonia water, dissolving while stirring in a fume hood, after the EDTA is completely dissolved, the solution is clear, slowly adding the ferric chloride solution into the EDTA ammonia water solution, and continuously stirring in the dissolving process to prevent the formation of precipitates. And finally, adding polyaspartic acid, glycerol and a sorbitol stabilizer into the solution, and stirring to completely dissolve the polyaspartic acid, glycerol and sorbitol stabilizer to obtain a solution, namely the reddish brown complex iron desulfurizer solution which has strong desulfurization performance.
Example 2:
100mL of deionized water, 97g of ferric chloride and 2mL of sulfuric acid are taken. 97g of ferric chloride is slowly dissolved into 100mL of deionized water, and then the mixture is continuously stirred, the reaction releases heat, and the ferric chloride is slowly dissolved without continuous stirring. After complete dissolution, the mixture is left to stand to room temperature. Then weighing 100g of EDTA and 200mL of ammonia water, dissolving while stirring in a fume hood, after the EDTA is completely dissolved, the solution is clear, slowly adding the ferric chloride solution into the EDTA ammonia water solution, and continuously stirring in the dissolving process to prevent the formation of precipitates. Adding polyaspartic acid, glycerol and sorbitol stabilizer in batches during stirring, and stirring to completely dissolve to obtain a solution, namely the reddish brown complex iron desulfurizer solution, which has strong desulfurization performance.
Example 3:
100mL of deionized water, 97g of ferric chloride and 2mL of sulfuric acid are taken. 97g of ferric chloride is slowly dissolved into 100mL of deionized water, then stirring is carried out continuously, the reaction releases heat, the ferric chloride needs to be slowly dissolved and stirring is not carried out continuously, and in addition, a part of content of stabilizer is additionally added. After complete dissolution, the mixture is left to stand to room temperature. Then weighing 100g of EDTA and 200mL of ammonia water, dissolving while stirring in a fume hood, after the EDTA is completely dissolved, the solution is clear, adding another part of stabilizer, then slowly adding the ferric chloride solution into the EDTA ammonia water solution, and continuously stirring in the dissolving process to prevent the formation of precipitates. Adding polyaspartic acid, glycerol and sorbitol stabilizer in batches during stirring, and stirring to completely dissolve to obtain a solution, namely the reddish brown complex iron desulfurizer solution, which has strong desulfurization performance.

Claims (3)

1.一种改进的络合铁法从气体混合物中脱出硫化物,包括以下重量百分比的成分:抗氧化剂10~100ppm,表面活性剂5~50ppm,其余的为络合铁催化剂和水,其中,所述络合铁催化剂是由络合剂,去离子水,氨水,氯化铁组成,所述络合铁脱硫剂是通过以下方法制备得到的;1. an improved complex iron method removes sulfide from gas mixture, comprising the composition of the following percentage by weight: antioxidant 10~100ppm, surfactant 5~50ppm, and the rest are complex iron catalyst and water, wherein, The complex iron catalyst is composed of a complexing agent, deionized water, ammonia water and ferric chloride, and the complex iron desulfurizing agent is prepared by the following method; 将络合剂,去离子水,氨水,加入带搅拌功能和加热功能的反应器中,开启搅拌,升温至100~150℃,边搅拌边加入EDTA;Add the complexing agent, deionized water and ammonia water into the reactor with stirring function and heating function, start stirring, heat up to 100-150 °C, and add EDTA while stirring; 然后,将氯化铁溶于水溶液中,溶解放热,不断搅拌,直至全部溶剂;Then, ferric chloride is dissolved in the aqueous solution, the dissolution is exothermic, and the stirring is continued until all the solvent is present; 最后将溶解的氯化铁溶液缓慢滴加到EDTA氨水溶液中,搅拌1h左右,稳定后即得改进后工艺的络合铁脱硫剂溶液;Finally, the dissolved ferric chloride solution was slowly added dropwise to the EDTA ammonia solution, stirred for about 1 hour, and stabilized to obtain a complex iron desulfurizer solution with the improved process; (1)分别取100mL去离子水,氯化铁97g,硫酸2mL,先将97g氯化铁缓慢溶解到100mL去离子水中,然后不断搅拌,反应放热,一定要缓慢溶解,不停搅拌;(1) Take 100mL of deionized water, 97g of ferric chloride, and 2mL of sulfuric acid, respectively, first slowly dissolve 97g of ferric chloride into 100mL of deionized water, and then keep stirring, the reaction is exothermic, and must be slowly dissolved and kept stirring; (2)取EDTA100g,氨水200mL,在通风橱内一边搅拌一边溶解,待EDTA完全溶解后,溶液清澈,这时将氯化铁溶液缓慢加入EDTA氨水溶液中,溶解过程中不断搅拌,防止沉淀的形成;(2) Take 100 g of EDTA and 200 mL of ammonia water and dissolve them in a fume hood while stirring. After the EDTA is completely dissolved, the solution is clear. At this time, the ferric chloride solution is slowly added to the EDTA ammonia solution. form; (3)在溶液中加入聚天冬氨酸,甘油,山梨糖醇稳定剂,搅拌完全溶解后所得溶液即为红棕色络合铁脱硫剂溶液,具有较强的脱硫性能。(3) Add polyaspartic acid, glycerol, and sorbitol stabilizer to the solution, and after stirring to dissolve completely, the obtained solution is a reddish-brown complex iron desulfurizer solution, which has strong desulfurization performance. 2.根据权利要求1所述的一种湿法络合铁脱硫剂的制备方法,其特征在于:所述制备络合铁催化剂所需的络合剂,去离子水,氨水,氯化铁等原料均易得,并且实验装置简单,可操作弹性大等优点。2. the preparation method of a kind of wet method complex iron desulfurizer according to claim 1, is characterized in that: described preparation required complexing agent of complex iron catalyst, deionized water, ammoniacal liquor, ferric chloride etc. The raw materials are readily available, the experimental device is simple, and the maneuverability is large. 3.根据权利要求1所述的一种湿法络合铁脱硫剂的制备方法,其特征在于:所述湿法络合铁脱硫剂的稳定性强,用氨水调节溶液PH至8~10,碱性环境脱硫效果更强。3. the preparation method of a kind of wet method complex iron desulfurizer according to claim 1, is characterized in that: the stability of described wet method complex iron desulfurizer is strong, adjust solution pH to 8~10 with ammoniacal liquor, Alkaline environment desulfurization effect is stronger.
CN202110498463.5A 2021-05-08 2021-05-08 Preparation method of wet-process complex iron desulfurizer Pending CN113069907A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202110498463.5A CN113069907A (en) 2021-05-08 2021-05-08 Preparation method of wet-process complex iron desulfurizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202110498463.5A CN113069907A (en) 2021-05-08 2021-05-08 Preparation method of wet-process complex iron desulfurizer

Publications (1)

Publication Number Publication Date
CN113069907A true CN113069907A (en) 2021-07-06

Family

ID=76616512

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202110498463.5A Pending CN113069907A (en) 2021-05-08 2021-05-08 Preparation method of wet-process complex iron desulfurizer

Country Status (1)

Country Link
CN (1) CN113069907A (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20090246106A1 (en) * 2008-03-17 2009-10-01 Research Institute Of Petroleum Industry (Ripi) Redox gas sweetening solutions
CN106237844A (en) * 2016-08-31 2016-12-21 陕西省石油化工研究设计院 A kind of Complexing Iron doctor solution for wet desulphurization and preparation method thereof
CN110559831A (en) * 2019-09-19 2019-12-13 天津领碳能源环保科技有限责任公司 Complex iron desulfurizer
CN111265993A (en) * 2020-01-15 2020-06-12 四川西油致诚石油技术有限公司 A kind of complex iron desulfurizer
CN111822051A (en) * 2020-05-11 2020-10-27 天津市众天科技发展有限公司 Complex iron desulfurization catalyst

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20090246106A1 (en) * 2008-03-17 2009-10-01 Research Institute Of Petroleum Industry (Ripi) Redox gas sweetening solutions
CN106237844A (en) * 2016-08-31 2016-12-21 陕西省石油化工研究设计院 A kind of Complexing Iron doctor solution for wet desulphurization and preparation method thereof
CN110559831A (en) * 2019-09-19 2019-12-13 天津领碳能源环保科技有限责任公司 Complex iron desulfurizer
CN111265993A (en) * 2020-01-15 2020-06-12 四川西油致诚石油技术有限公司 A kind of complex iron desulfurizer
CN111822051A (en) * 2020-05-11 2020-10-27 天津市众天科技发展有限公司 Complex iron desulfurization catalyst

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
汪多仁: "《绿色净水处理剂》", 30 November 2006, 北京:科学技术文献出版社 *

Similar Documents

Publication Publication Date Title
CN108660326A (en) A method of reduction acidolysis-leaching is simultaneously except iron handles manganese oxide ore
CN102040225B (en) Process for preparing precipitated white carbon black by decomposing carbon dioxide
CN109550365A (en) A kind of ionic liquid absorbent and the method for improving ionic liquid absorption performance
CN109529567B (en) Process for desulfurizing hydrogen sulfide and sulfur dioxide through reaction
CN104177766A (en) Graphene furan resin composite material and preparation method thereof
CN104211104A (en) Separation and recovery method of thermal coal power plant flue gas desulfurization gypsum waste residues
CN113069907A (en) Preparation method of wet-process complex iron desulfurizer
CN112473742A (en) Desulfurization catalyst for simultaneously removing hydrogen sulfide and carbonyl sulfide and preparation method thereof
CN111592474A (en) Preparation method of complex iron catalyst for wet desulphurization
CN108067216A (en) The recovery method of base metal catalysts in a kind of catalytic coal gasifaction lime-ash
CN110252090B (en) A kind of method that utilizes triethanolamine to improve absorption capacity and utilization ratio of sodium sulfite desulfurization process
CN115650243B (en) A method for one-step separation and recovery of fluorine and silicon in fluorine-containing silicon slag
CN109626411B (en) Production process of anhydrous cuprous chloride
CN109534297B (en) Method for desulfurizing hydrogen sulfide and sulfur dioxide through reaction
CN113355511B (en) Method for selectively reducing vanadium and titanium content in vanadium-titanium magnetite concentrate through ammonium-ammonia oxidation leaching system
CN102476829B (en) A kind of preparation method of vanadyl sulfate
CN109400909A (en) A kind of preparation method of coal base fulvic acid
CN107790192B (en) Preparation method of modified ionic liquid catalyst for removing sulfur dioxide
CN1103238C (en) Production method of binuclear phthalocyanine cobalt sulfone desulfurization and decyanation catalyst
CN106140300A (en) Preparation method of one kind fenton catalyst and products thereof and application
CN103878029B (en) A kind of supplements-iron for complex iron desulphurization solution and preparation method thereof
CN107034353A (en) A kind of method of low-temperature bake acidleach dissociation gold
CN106637294B (en) The method for decoppering of nickel solution
CN112194605A (en) Method for preparing N, N' -diisopropyl thiourea
CN105561981B (en) A kind of derived energy chemical spent lye processing high-efficiency desulfurization catalyst and preparation method thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20210706

RJ01 Rejection of invention patent application after publication