CN102728314A - Large-capacity porous activated ammonia storage activated mixture and preparation thereof - Google Patents
Large-capacity porous activated ammonia storage activated mixture and preparation thereof Download PDFInfo
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- CN102728314A CN102728314A CN2012102388258A CN201210238825A CN102728314A CN 102728314 A CN102728314 A CN 102728314A CN 2012102388258 A CN2012102388258 A CN 2012102388258A CN 201210238825 A CN201210238825 A CN 201210238825A CN 102728314 A CN102728314 A CN 102728314A
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Abstract
The invention relates to preparation of a large-capacity porous activated ammonia storage activated mixture. The preparation is characterized by comprising the following steps of: adopting industrial anhydrous magnesium chloride salt powder, doping with silica sol, activated carbon, deionized water and industrial alcohol which are in proper quantity; mechanically stirring and preparing the mixture into a semi-dry uniform mixed wet material; and filling the semi-dry uniform mixed wet material into a tank body so as to prepare an overall porous solid block. The solid block is internally rich in ammonia transmission pore passage, has a plurality of large holes in macro, has a faster ammonia charging property and a better ammonia storage property, can emit the ammonia rapidly, can be used in recycling without being crushed, has an efficient absorption and desorption property, is applicable for ammonia absorption storage and is used in an SCR (Selective Catalytic Reduction) and FCEV (Fuel Cell Electric Vehicle) system; and the application requirements in future automobile industry are met.
Description
Technical field
The present invention relates to a kind of jumbo porous active storage ammonia active mixture and preparation method thereof, be applied to the SCR after-treatment system and the FCEV fuel cell system of vehicle exhaust.
Background technology
Current, the whole world faces the comprehensive challenge of the energy and environment.Aspect the technological means selection of the emission compliance of orthodox car, and the fuel of new-energy automobile is supplied with the technical elements people and is still faced many difficult problems.
The SCR after-treatment system is to rely on the accurate supply of carbamide reducing agent and after the front end of catalyst resolves into ammonia, remove the NOX hazardous material; Reach the purpose of cleaning of off-gas; Realize state 4 or above standard up to standard of vehicle; But; In actual use, this dependence urea decomposition becomes the metered injection of the liquid area of ammonia to have many deficiencies and difficult point, for example; Urea liquid is icing blocking problem under-11 ℃ of environment, needs extra pipeline heating system to solve; Urea liquid could decompose under the temperature environment more than 135 ℃; And many vehicles of public transit system loiter; Can't reach urea liquid stable decomposition temperature at all; Can't the output ammonia; Can't eliminate predetermined NOX composition; Cause the accumulation of liquid area in blast pipe at last; Produce the polymer of melamine; Stop up the urea nozzle and the exhaust pipe of engine; Cause vehicles produces fault; Influence is normal to be used, in addition, if the main flow vehicle of state more than 4 uses the SCR system comprehensively; Relate to the whole nation about 150,000 oiling websites innovation and build the problem of liquid area filling infrastructure; Because investment is huge, do not see still that at present government and enterprise start to improve this infrastructure, become a potential huge problem in the SCR use;
For breaking through energy predicament, solve the new-energy automobile development problem of future source of energy problem, hydrogen fuel cell is a very important techniques route by generally acknowledging; But how stable acquisition hydrogen is originated is a no small difficult problem of restriction this area development, in institute's possible adopted hydrogen source mode; Technology path and the hydrogeneous presoma decomposition of other H-N or the technology path of cracking hydrogen production that the technology path of gas cylinder storage hydrogen, the technology path that water electrolysis hydrogen production is arranged, the technology path that high-purity hydro carbons petroleum fuel cracking hydrogen production is arranged, low mass molecule alcohol class cracking hydrogen production are arranged; In the above-mentioned technology path, all there are some problem and shortage, for example; Hydrogen production efficiency and cost; Hydrogen manufacturing precision and speed also comprise the problem of system aspects, in a word; The source of hydrogen is the bottleneck of fuel-cell vehicle development, needs people's idea to solve;
One of them is the hydrogeneous compound of H-N for the presoma of hydrogen, and wherein, what hydrogen-storage density was the highest is ammonia.Ammonia is a kind of modal industrial chemicals, and the ammonia molecule belongs to active polar molecule, and the diameter dimension of molecule is about 3 ~ 4A, therefore, very active under the normal temperature, very easily diffusion, and have toxic; The skin histology that its toxic is embodied in contact all has corrosion and spread effect, can absorb the moisture in the skin histology, makes the histone sex change, and makes the tissue fat saponification, destroys membrane structure; Ammonia in water solubility high, stimulate and corrosiveness so mainly the upper respiratory tract of animal or human's body is had, often be attracted on mucocutaneous and the eye conjunctiva; Stimulate and inflammation thereby produce, in addition, ammonia sucks human body with gas form usually; Ammonia gets into blood through alveolar after being inhaled into lung easily, combines with hemoglobin, destroys fortune oxygen function; Get into IA ammonia; Few part is neutralized by carbon dioxide, and remainder is absorbed into blood, suck in a short time can occur shedding tears behind a large amount of ammonias, pharyngalgia, cough, uncomfortable in chest, expiratory dyspnea, dizziness, vomiting, weak etc.; If the long-term ammonia that sucks is too much, cause ammonia excessive concentration in the blood, will cause heart stop fight and breath stopped threat to life safety; Therefore, the maximum hidden danger of the use of ammonia is safety problem.
This shows, resolve in the use of ammonia storing and safety problem, just can open up the technology path of a new ammonia utilization.
Traditional ammonia storing mode is a gas cylinder, or realizes with the water-soluble formation ammoniacal liquor of high concentration ammonia.If adopt gas cylinder to store ammonia, there is the potential safety hazard of operating aspect and seal aspect in the commercial Application in enormous quantities, if, have serious etching problem again with the mode of high concentrated ammonia liquor.
At China national patent information net; With the storage ammonia word and search that is the theme; The patent No. is that CN201120099229.7's ' a kind of urotropine by using gas phase method tail gas ammonia recovery unit ', the patent No. is that ' be used for freezer machine room join ammonia bindiny mechanism ' of CN201020677361.7, ' complex function type storage ammonia device ', the patent No. that the patent No. is CN201020269811.9 are CN200520057558.X ' a kind of ammonia steaming device '; Be one type the ammonia nitrogen industrial wastewater carried out the environment protection treating device that ammonia nitrogen is got rid of processing, also do not relate to the characteristic component among the present invention.Uncorrelated with the present invention;
The patent No. is that CN201010244091.5's ' be used for method and system that the work of SCR catalyst is tested ' and the patent No. is that this 2 inventions of CN200880104697.X ' operation method of SCR exhaust after treatment system and diagnostic method ' provide a kind of SCR (SCR) catalytic converter and traditional liquid ureaclastic ammonia dispensing module and control system of being used for, and does not relate to the characteristic component of compound;
The patent No. is that CN200910197860.8's the invention of ' a kind of preparation method of efficient low-temperature ammonia-storing material ' is applied to the SCR after-treatment system; Characteristic is to place closed container to the amino borane compound; Vacuumize, under 0-4 ℃ of temperature, contact with ammonia; Under 0-4 ℃ of temperature, kept 30-60 minute, prepare required product amino borane ammino-complex NH3BH3 (NH3) n (n=1-3); The maximum storage of room temperature ammonia amount can reach 62.4wt.%; About room temperature supply gas pressure 2.0bar; Room temperature supplies ammonia pressure moderate, inhales to put the ammonia completely reversibility, but the costing an arm and a leg of the extraordinary material amino borane of this patent; Have higher explosion danger and burning grade, be not suitable for applying in enormous quantities of general industry field;
The patent No. is that CN200580026626.9's the invention of ' storage and carry the solid material of ammonia ' relates to storage and carries the solid material of ammonia.The solid material of this storage ammonia comprises that a kind of ammonia absorbs salt, and wherein this ammonia absorption salt is that general formula is M
a(NH
3)
nX
zIonic salt; Wherein M is selected from for example one or more cations of Mn, Fe, Co, Ni, Cu and/or Zn of alkaline-earth metal and/or one or more transition metal, and X is one or more anion, and a is the cation number that comprises in each molecules of salt; Z is the anion number that comprises in each molecules of salt; N is 2～12 ligancy, and wherein M is Mg, and it is auto industry that this ammonia absorbs salt provides a kind of safety, lightweight, cheap and fine and close storage with ammonia.This patent is the direct compression molding of solid material, and ammonia is resolved in the electric heating heating, more lays particular emphasis on the control strategy of system, does not relate to the modification and the optimization of mixture;
The patent No. be CN200580009219.7's ' purposes of ammonia storage device in energy production ' invention relate to a kind of generator unit, this unit comprises the ammonia storage device of (i) container (2) form, comprising general formula is M
a(NH
3)
NXzAmmonia absorb and discharge salt; Wherein M is one or more cations, is selected from alkali metal, alkaline-earth metal and transition metal such as Li, K, Mg, Ca, V, Cr, Mn, Fe, Co, Ni, Cu or Zn, and X is one or more anion; Be selected from fluorine root, chlorine root, bromine root, iodine root, nitrate anion, thiocyanate radical, sulfate radical, molybdate, phosphate radical and chloranion; A is the cation number of each molecules of salt, and z is the anion number of each molecules of salt, and n is the ligancy of 2-12; (ii) being used to heat said container (2) and ammonia absorbs and discharges the fuel cell that salt with the device (3a) that discharges ammonia and (iiia) is used for ammonia is converted into electrical power; Perhaps (iiib1) is used for ammonia is dissociated into the reactor (6) of hydrogen and nitrogen; (iiib2) be used for hydrogen is converted into the fuel cell (4) of electrical power; This patent is mainly used in fuel cell; Mentioned property material in the claim 4 and be such salt or be positioned on the porous carrier materials, which kind of material statement is not;
The disclosure of the Invention of CN200710156866.1 ' a kind of amido complex compound ' a kind of amido complex compound.The composition of this amido complex compound is MX
m(NH
3)
n, M is one or more among Li, Mg, Al, Ca, Sc, V, Cr, Mn, Fe, Co, Ni, Cu, Zn, Sr, Ba, the Sn in the formula; X is F, Cl, Br, NO
3, SO
4In one or more; M decides according to chemical valence, 1≤m≤5; N decides according to ligancy, 1≤n≤15.With the absorbent of the amido complex compound behind the deamination, put separation, purification, storage and the transportation that ammonia is realized ammonia through low temperature suction ammonia, high temperature as ammonia.This patent only relates to the preparation technology and the process of this amido complex compound itself;
The patent No. is solid ammonia storage and the conveying material that CN200680005886.2's the high density of the ammonia ' storage ' patent comprises ammonia absorptions/desorb solid material; The said density that has been compacted to is greater than 50% storage of theoretical skeletal density with carry material that the solid ammonia storage medium is provided; The storage ammonia that this storage medium prepares and handles and have very high-density easily; Said storage ammonia discharges under controlled condition easily; Even the porosity of said material is very low still like this, and this storage medium does not need special safety measure for storage with to carry ammonia be safe.This patent is to adopt the direct compression molding of solid material; Adopt binding agent; Only stated it possibly is the silicon dioxide fibre binding agent, do not had the dosage ratio, the solid material of also only stating among other claim item and the embodiment possibly comprise granular materials, porous material, crystalline material, amorphous materials or their bond composition; Do not have thin of clear and definite claim, industry technology personage almost can't implement.Produced the present invention therefrom.
Summary of the invention
The object of the present invention is to provide the preparation of a kind of jumbo porous active storage ammonia mixture,, increase the ammonia transmission channel in order to improve the hole of storage ammonia active material solid block, weaken or avoid adsorbing repeatedly with desorption process in MgCl
2The caking that takes place and the efflorescence of solid block are broken, and that satisfies industrial occasions repeatedly recycles requirement, possesses and fills ammonia faster and store up the ammonia performance preferably; Can discharge ammonia fast; Can recycle not brokenly, possess efficient absorption and conciliate characterization of adsorption, the absorption that is fit to ammonia stores; Be used for SCR and FCEV system, satisfy the application demand of following auto industry.
Technical scheme of the present invention is achieved in that a kind of jumbo porous active storage ammonia mixture; It is characterized in that: press the powder of mass fraction by 48 ~ 90 parts industrial anhydrous chlorination magnesium salts; Mix 2.5 ~ 15 parts Ludox, 0.5 ~ 6 part of active carbon, mix with 4 ~ 16 parts deionized water and 3 ~ 15 parts industrial alcohol.
Described preparation process of mixture is following: with the powder of the anhydrous chlorination magnesium salts of industry; Mix Ludox, active carbon, deionized water and industrial alcohol; Become uniform mixture wet feed through mechanical agitation; Be filled in the tank body, addition is no more than 80% of tank body volume, and machinery concussion 5 ~ 10min eliminates the air gap; Whole tank body is put in the vacuum drying oven, and normal pressure is slowly heating down, and temperature is controlled at 65 ~ 160 ℃; Get rid of water and ethanol to mixture constant weight, substep is evacuated to 550mbar, constant temperature and pressure 0.5 ~ 3h; Take out tank body, the sealing charge door is processed the whole porosu solid piece of storage ammonia active mixture; Ammonia fills in the tank body under 0.05 ~ 0.8MPa pressure, and is saturated to the mixture absorbing ammonia.
Described Ludox particle diameter is at 10 ~ 20nm, and density is at 1.15g/cm
3, dioxide-containing silica 25%, disperse becomes suspension in water.
Described active carbon pore size distribution range at 2 ~ 50nm, specific surface greater than 800m
2/ g.
Good effect of the present invention is optionally to have added Ludox, and the particle diameter here is at 10 ~ 20nm, and density is at 1.15g/cm
3, dioxide-containing silica 25%, pH value 8 ~ 10, disperse becomes suspension in water, by means of mechanical agitation and MgCl
2Reach other fillers and fully mix, at MgCl
2Bridging between the particle, dry back forms higher " the integrated solid piece " of mechanical strength, can weaken effectively or avoid adsorbing with desorption process in the expansion of solid block to shrink the efflorescence that causes broken; The diffusing MgCl of water that adds and dissolve with ethanol and differential
2And other fillers, improve between the liquid-solid two-phase wetting with sprawl, in addition, water and ethanol are deviate from the hole of process formation, have enriched the transmission channel of ammonia; The active carbon that adds has promoted MgCl
2Dispersion; Can weaken or avoid the generation of caking phenomenon effectively, improve the richness of microscopic void, increase the transmission channel of ammonia; Improve the permeance property of ammonia greatly; Promote the formation of ammino magnesium chloride complex compound, the loose structure of active carbon itself possesses certain absorption and memory function to ammonia simultaneously; The active carbon pore size distribution range of here selecting at 2 ~ 50nm, specific surface greater than 800m
2/ g; In order to guarantee security under elevated pressures, used tank body is the withstand voltage tank body of stainless steel, inner tank wall thermal spraying nylon heat-insulation layer.
To sum up, contain the abundant activity storage ammonia mixture of microcosmic nano pore of Ludox, guaranteeing under the constant prerequisite of storage ammonia active material characteristic; Ludox that adds and the phenomenon that active carbon weakens or the ammonia adsorption-desorption of having avoided caking, fragmentation etc. to cause attaches; Improve the richness of microscopic void, increased the quantity of macroscopic pores, improved the mechanical strength of composition appearance piece; Have very high practical value, be suitable for the SCR post processing or the FCEV system of automobile industry.
Description of drawings
The thermogravimetric curve of the active mixture of the absorbing ammonia of Fig. 1 embodiment of the invention 1.
The specific embodiment
Through embodiment the present invention is further described below, embodiment is not equal to restriction the present invention for further illustrating characteristics of the present invention,, all should be included within protection scope of the present invention according to the change that the present invention carries out for those skilled in the art.
Embodiment 1
Water with 71 parts magnesium chlorides, 3 parts of active carbons, 6 parts of Ludox and 12 parts mixes 1h in homogenizer, add 8 parts of ethanol; Continue mechanical agitation 3h, process uniform mixture wet feed, be filled in the tank body; Be added into 80% of tank body volume, machinery concussion 10min eliminates the air gap;
Whole tank body is put in the vacuum drying oven, and the heating rate with 2 ℃/min under the normal pressure as shown in Figure 1 rises to 120 ℃, constant temperature 6h; Get rid of water and ethanol, substep is evacuated to 550mbar, constant temperature and pressure 1h; Take out tank body, the sealing charge door is processed the whole porosu solid piece of storage ammonia active mixture.
Embodiment 2
Water with 2 parts of active carbons, 15 parts of Ludox and 15 parts; In homogenizer, mix 1h; The magnesium chloride mixing 1h that adds 58 parts; Add 10 parts of ethanol; Continue mechanical agitation 3h, make uniform mixture wet feed, be filled in the tank body; Be added into 75% of tank body volume, machinery concussion 10min eliminates the air gap;
Whole tank body is put in the vacuum drying oven, and the heating rate with 2 ℃/min under the normal pressure rises to 120 ℃, constant temperature 6h; Get rid of water and ethanol, substep is evacuated to 550mbar, constant temperature and pressure 1h; Take out tank body, the sealing charge door is processed the whole porosu solid piece of storage ammonia active mixture.
Embodiment 3
Water with 5 parts of Ludox and 6 parts; In homogenizer, mix 1h; The magnesium chloride mixing 1h that adds 80 parts; Add 3 parts of active carbon mixing 1h, add 6 parts of ethanol, continue mechanical agitation 3h; Make uniform mixture wet feed; Be filled in the tank body, be added into 80% of tank body volume, machinery concussion 10min eliminates the air gap;
Whole tank body is put in the vacuum drying oven, and the heating rate with 5 ℃/min under the normal pressure rises to 100 ℃, constant temperature 8h; Get rid of water and ethanol, substep is evacuated to 550mbar, constant temperature and pressure 2h; Take out tank body, the sealing charge door is processed the whole porosu solid piece of storage ammonia active mixture.
Embodiment 4
The tank body that the storage ammonia active mixture of accomplishing for embodiment 1 installs additional adopts high-purity industrial ammonia bottle through subsequent use pipe valve, in the outlet pressure scope of 0.4Mpa slowly fill ammonia, filling the ammonia time is 3h, fill ammonia before and after the tank body quality increase by 44%;
The tank body that completion is filled behind the ammonia is connected with automobile SCR system, and under the situation of ammonia leakage rate less than 10ppm, quality reduces 38% before and after the test tank body desorption.
Embodiment 5
The tank body that the storage ammonia active mixture of accomplishing for embodiment 2 installs additional adopts high-purity industrial ammonia bottle through subsequent use pipe valve, in the outlet pressure scope of 0.2Mpa slowly fill ammonia, filling the ammonia time is 6h, fill ammonia before and after the tank body quality increase by 39%;
The tank body that completion is filled behind the ammonia is connected with automobile SCR system, and under the situation of ammonia leakage rate less than 10ppm, quality reduces 35% before and after the test tank body desorption.
Embodiment 6
The tank body that the storage ammonia active mixture of accomplishing for embodiment 3 installs additional adopts high-purity industrial ammonia bottle through subsequent use pipe valve, in the outlet pressure scope of 0.5Mpa slowly fill ammonia, filling the ammonia time is 5h, fill ammonia before and after the tank body quality increase by 40%;
The tank body that completion is filled behind the ammonia is connected with automobile SCR system, and under the situation of ammonia leakage rate less than 10ppm, quality reduces 35% before and after the test tank body desorption.
Claims (4)
1. a jumbo porous active stores up the ammonia mixture; It is characterized in that: press the powder of mass fraction by 48 ~ 90 parts industrial anhydrous chlorination magnesium salts; Mix 2.5 ~ 15 parts Ludox, 0.5 ~ 6 part of active carbon, mix with 4 ~ 16 parts deionized water and 3 ~ 15 parts industrial alcohol.
2. a kind of jumbo porous storage ammonia active mixture according to claim 1; It is characterized in that described preparation process of mixture is following: with the powder of the anhydrous chlorination magnesium salts of industry; Mix Ludox, active carbon, deionized water and industrial alcohol, become uniform mixture wet feed, be filled in the tank body through mechanical agitation; Addition is no more than 80% of tank body volume, and machinery concussion 5 ~ 10min eliminates the air gap; Whole tank body is put in the vacuum drying oven, and normal pressure is slowly heating down, and temperature is controlled at 65 ~ 160 ℃; Get rid of water and ethanol to mixture constant weight, substep is evacuated to 550mbar, constant temperature and pressure 0.5 ~ 3h; Take out tank body, the sealing charge door is processed the whole porosu solid piece of storage ammonia active mixture; Ammonia fills in the tank body under 0.05 ~ 0.8MPa pressure, and is saturated to the mixture absorbing ammonia.
3. a kind of jumbo porous storage ammonia active mixture according to claim 1 is characterized in that described Ludox particle diameter at 10 ~ 20nm, and density is at 1.15g/cm
3, dioxide-containing silica 25%, disperse becomes suspension in water.
4. a kind of jumbo porous storage ammonia active mixture according to claim 1, it is characterized in that described active carbon pore size distribution range at 2 ~ 50nm, specific surface greater than 800m
2/ g.
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109692663A (en) * | 2017-10-23 | 2019-04-30 | 中国石化扬子石油化工有限公司 | A kind of adsorbent and preparation method thereof utilized for Ammonia recovery |
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| JPH01236941A (en) * | 1988-03-16 | 1989-09-21 | Kuraray Chem Corp | Gaseous ammonia adsorbent |
| CN1093794A (en) * | 1992-08-14 | 1994-10-19 | 罗基研究公司 | In order to obtain the improved method and apparatus of high reactivity |
| DE102008002335A1 (en) * | 2008-06-10 | 2009-12-17 | Robert Bosch Gmbh | Ammonia storage unit for automotive exhaust system incorporates an embedded powder additive |
| US20110218095A1 (en) * | 2008-09-08 | 2011-09-08 | Amminex A/S | Additives for Highly Compacted Ammonia Storage Materials |
| EP2428490A1 (en) * | 2010-09-10 | 2012-03-14 | Aaqius & Aaqius S.A. | System for reducing the amount of NOx in the exhaust fumes of a motor vehicle |
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2012
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Patent Citations (5)
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| JPH01236941A (en) * | 1988-03-16 | 1989-09-21 | Kuraray Chem Corp | Gaseous ammonia adsorbent |
| CN1093794A (en) * | 1992-08-14 | 1994-10-19 | 罗基研究公司 | In order to obtain the improved method and apparatus of high reactivity |
| DE102008002335A1 (en) * | 2008-06-10 | 2009-12-17 | Robert Bosch Gmbh | Ammonia storage unit for automotive exhaust system incorporates an embedded powder additive |
| US20110218095A1 (en) * | 2008-09-08 | 2011-09-08 | Amminex A/S | Additives for Highly Compacted Ammonia Storage Materials |
| EP2428490A1 (en) * | 2010-09-10 | 2012-03-14 | Aaqius & Aaqius S.A. | System for reducing the amount of NOx in the exhaust fumes of a motor vehicle |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109692663A (en) * | 2017-10-23 | 2019-04-30 | 中国石化扬子石油化工有限公司 | A kind of adsorbent and preparation method thereof utilized for Ammonia recovery |
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