CN1935642A - Method for preparing carbon molecular sieve by preoxidation of petrol coke - Google Patents
Method for preparing carbon molecular sieve by preoxidation of petrol coke Download PDFInfo
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- CN1935642A CN1935642A CN 200610047777 CN200610047777A CN1935642A CN 1935642 A CN1935642 A CN 1935642A CN 200610047777 CN200610047777 CN 200610047777 CN 200610047777 A CN200610047777 A CN 200610047777A CN 1935642 A CN1935642 A CN 1935642A
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- molecular sieve
- coke
- preoxidation
- carbon molecular
- preparing carbon
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Abstract
The invention relates to a method for preparing carbon molecular sieve by petroleum coke preoxidation treatment, comprising the steps of: firstly crushing petroleum coke, then adopting oxidant to make dipping oxidizing treatment on the petroleum coke powder to change its chemical composition and surface properties so as to benefit formation and development of hole structure in the follow-up carbonizing and activating courses; then adding in a proper amount of adhesive, bonding assistant and water to knead uniformly, moulding the kneaded matter, drying and carbonizing the moulded matter, and controlling activation and carbon deposition hole regulation treatments according to the requirements. And it has beneficial effects of: high product intensity, large micropore capacity, narrow aperture distribution, and the product can be used to make nitrogen by air separation with PSA process.
Description
Technical field
The invention belongs to chemical production technical field, relate to a kind of method of preparing carbon molecular sieve by preoxidation of petrol coke.
Background technology
Carbon molecular sieve (CMS) is meant the raw material of wood-charcoal material that has than the flourishing microvoid structure of homogeneous, pore size distribution is generally between 0.3～1.0nm, be widely used in fields such as fractionation by adsorption, purification and catalysis, as the sorbent material as transformation absorption (PSA) technology, the air separation that is widely used in middle and small scale is to prepare rich N
2Gas.CMS performance and manufacturing cost thereof are determined by technological process raw materials used and that adopt to a great extent.For industrial production CMS, develop new raw material and will bring huge economic benefit and social benefit to reduce production costs.The raw material that is used to prepare CMS is very wide, by containing charcoal plant or mineral (coal, pitch etc.) to synthesising macromolecule copolymer etc., all can be used to make carbon molecular sieve.Refining of petroleum byproduct refinery coke is one of alternative raw material of preparation CMS.Along with the continuous rising and the market requirement of refinery coke output is tending towards saturated, seeks the new approach that utilizes for refinery coke and more and more be subject to people's attention.With the refinery coke is the synthetic CMS of raw material, is the new way of a refinery coke increment and utilization.
It is generally acknowledged when having only raw material itself or raw material to have more uniform flourishing microvoid structure, just can prepare the CMS of excellent property through the intermediate product of suitable processing gained.Advantages such as that although refinery coke has is cheap, wide material sources, fixed carbon content height, and ash content is low, refinery coke dense micro-structure, easy greying, The book of Changes charing and activation form the space.Directly by refinery coke through charing, physically activated and carbon laydown path of preparing carbon molecular sieve, be difficult to the product that obtains conforming to quality requirements.
The open CN1631775A of Chinese patent is raw material with the refinery coke, after pre-charing, adds the potassium hydroxide activation of 3～8 times of quality, makes active carbon with high specific surface area, passes through the elevated temperature heat polycondensation again, makes nano-porous carbon molecular sieve with high specific surface area.Because the refinery coke dense micro-structure needs a large amount of activator (potassium hydroxide) activation, therefore causes production cost higher, equipment corrosion is serious, pollutes big; Chinese patent CN1462650A is raw material with the refinery coke, with petroleum pitch, ethylene cracking tar or coal tar is binding agent, add water and mediate aftershaping, adjust the aperture treatment process of the combined method of method after the dry charing through control activation and two component holes, obtain CMS.Adopt tar or bituminous cement, it is more to contain hazardous substance, contaminate environment; Adopt benzene class or gasoline class soaker pickling process to transfer the hole, be difficult to realize the finely regulating of pore size and pore volume; Adopt physical activation method to be difficult to open the microvoid structure of refinery coke densification, the CMS pore size distribution of being produced is wide, is not suitable for the separation of close blending ingredients of molecular scale such as air.The foreign patent that with the refinery coke is raw material production CMS is not appeared in the newspapers.
Summary of the invention
The objective of the invention is to overcome the shortcoming of refinery coke compact structure, pore-forming difficulty, a kind of method that is fit to the empty CMS of branch by the preparation of pre-oxidation treatment refinery coke is provided.CMS ash content obtained by this method is low, and micropore is abundant, narrow pore size distribution range, and empty branch excellent property and production cost are low, and environmental pollution is little.
The present invention is based on following result of study, promptly to after the refinery coke pre-oxidation treatment, make the refinery coke surface generate a series of oxygen-containing functional group, its charing behavior changes thereupon, becomes the precursor material that is suitable for preparing carbon molecular sieve.Analysis revealed: through H
2O
2(PC-H
2O
2) and refinery coke (PC-AIR) spectrogram of atmospheric oxidation in wave number at 1700cm
-1The feature honeybee of more weak C=O all appears in the place; Through HNO
3Refinery coke (the PC-HNO of oxidation
3) wave number 1322cm in the spectrogram
-1And 1522cm
-1Be symmetry and the asymmetrical stretching vibration absorption honeybee of N=O, 1592cm
-1Be the C=C on the phenyl ring and C=O or N=O conjugation absorption honeybee to the lower wave number migration; Through H
2SO
4Refinery coke (the PC-H of oxidation
2SO
4) wave number is 1172cm in the spectrogram
-1And 1031cm
-1The peak at place is respectively R-SO
2R and-SO
3The absorption peak of H; And the considerable change of refinery coke is at wave number 2900cm after the oxidation
-1And 3080cm
-1C h bond stretching vibration caused absorption peak in the left and right sides disappears substantially, and wave number is at 1600cm
-1Near for the stretching vibration peak of the C=C of aromatic hydrocarbons dies down, wave number is at 1450cm
-1The place-CH
2-absorption peak dies down or disappears, illustrate refinery coke most C-H in oxidising process be oxidized to other oxy radicals (C=O, N=O ,-SO
3H etc.).
By thermogravimetic analysis (TGA), we find mainly deviating from the fugitive constituent with the thermolysis and the polycondensation of refinery coke itself except about 600 ℃, 300
~Ratio zero-g period has faster all appearred in 400 ℃ of intervals, the petroleum coke powder after the oxidation, and the raw material refinery coke does not occur.Illustrate that the oxy radical that forms in the oxidising process deviates from multi-form in charing, and played the effect that changes the refinery coke pore structure.Table 1 is the pore structure parameter of the CMS sample of experiment acquisition.No matter from pore volume and pore size distribution, can not satisfy the needs of gas delivery with the CMS of the direct preparation of refinery coke raw material as can be seen from the table.Refinery coke can improve its pore texture through after the different oxygenant oxidations apparent in viewly, increases its micro pore volume, dwindles mean pore size, and the CMS of empty branch performance has established certain basis for preparation has preferably.
Table 1 CMS sample well structural parameter
| Processing mode | BET specific surface area (m 2/g) | Total pore volume (ml/g) | Micro pore volume (ml/g) | Mean pore size (nm) |
| PC-H 2SO 4 | 64 | 0.060 | 0.012 | 3.75 |
| PC-HNO 3 | 82 | 0.062 | 0.041 | 3.02 |
| PC-H 2O 2 | 48 | 0.051 | 0.020 | 4.25 |
| PC-AIR | 55 | 0.053 | 0.029 | 3.85 |
| PC | 5 | 0.019 | 0.008 | 15.2 |
Based on above-mentioned principle and experiment basis, technical scheme of the present invention is: a kind of method of preparing carbon molecular sieve by preoxidation of petrol coke, and its method steps is:
(1) at first petroleum coke powder is broken to particle diameter less than 5～10 μ m, wherein 90% less than 5 μ m.
(2) pre-oxidation treatment: it is in 10～98% Oxidant solution that the refinery coke immersion is prepared mass concentration, at room temperature continuously stirring is 0.5～4 hour, make it to mix, it was 5～6 that reaction is washed to filtrate pH value after stopping again, 100～110 ℃ of dryings 2～6 hours.
(3) add binding agent, adhesive aid and water and mediate, extrusion molding again, the mass ratio of material is when kneaded and formed, petroleum coke powder: binding agent: adhesive aid: water is 1: 0.2～0.7: 0.02～0.1: 0.4～0.8.
(4) carry out charing, activation and carbon laydown after the forming composition drying is handled and transfer the hole to handle, promptly obtain carbon molecular sieve of the present invention, carbonization condition is: the converter charing, and 2～10 ℃/min of temperature rise rate, temperature is 800～900 ℃, nitrogen or argon shield; Carbon laydown transfers the hole treatment condition to be: carbon laydown reagent is benzene or methane, and volumetric concentration is 3～20%, and carrier gas is nitrogen or argon gas, and depositing temperature is 700～800 ℃, and the time is 0.5～3h; Activation condition is: activator is water vapour or carbonic acid gas, and volumetric concentration is 30～80%, and carrier gas is nitrogen or argon gas, and activation temperature is 800～900 ℃, and soak time is 0.5～3h.The ash content of refinery coke≤1.0%, moisture≤5.0%, volatile matter≤18%, carbon content 〉=90%.Oxygenant is 90～98wt%H
2SO
4, 10～30wt%H
2O
2, or 10～40wt%HNO
3Solution.Binding agent is a heat-reactive phenolic resin, and its performance meets following index: viscosity 0.3～1.5Pas/20 ℃, solid content is 55～75%, and adhesive aid is water soluble starch or carboxymethyl cellulose.
The present invention compares with existing technology has following advantage:
1. refinery coke is carried out the character that pre-oxidation treatment can change refinery coke, make it generate a large amount of oxy radicals, and these groups are deviate from multi-form in carbonization process, thereby form more rich gap structure, and help further activation and transfer the hole to handle.
2. pre-oxidation treatment is at room temperature carried out, operation control easily, and used oxygenant can reclaim sharp again.
3. adopt this kind method pre-treatment refinery coke, can avoid in a large number shortcomings such as the pollution that produces with the alkali activation treatment and production cost costliness.
4. resol is binding agent, and water soluble starch or cellulose family are adhesive aid, and the pollution level of generation is relatively low, and production cost is reduced.
5. the CMS ash content of being produced is low, and micropore is abundant, narrow pore size distribution range, the empty excellent property of dividing.
Embodiment
The invention will be further described below in conjunction with embodiment.
Embodiment 1 (Comparative Examples):
Get the refinery coke raw material 300g after the pulverizing, add an amount of binding agent (heat-reactive phenolic resin), auxiliary agent (starch) and water and mix and pinch evenly, wherein coke powder: binding agent: auxiliary agent: water=1: 0.2: 0.05: 0.6, extrusion molding again.At 110 ℃ of oven dry 2h, make diameter 2mm, long 3
~The right cylinder small-particle of 5mm.Particle temperature rise rate with 5 ℃/min in the electric heating converter after the moulding oven dry is raised to 800 ℃ of charing 1h, carrier gas N
2Flow velocity 130ml/min; Feed water activation 0.5h with 0.45ml/min speed again after the charing; Feed benzene 1h at last when 750 ℃ of temperature, transfer the hole, benzene flow velocity 0.135ml/min promptly obtains CMS after the cooling.The intensity that prepared CMS measures with rotary drum reaches 99.5%, N
2The total hole volume of determining adsorption is 0.021ml/g, and the exit concentration of the sky branch performance N2 that the double tower pressure-swing absorption apparatus is measured is 88.0%.The test result of commodity carbon molecular sieve is under the equal conditions: barrate strength 99.0%, total hole volume are 0.030ml/g, and N2 concentration is 97.9%.
Embodiment 2:
Get the 300g coke powder and 98% vitriol oil 300ml mixes, reaction 1h, being washed till the pH value with deionized water then is 5
~6, dry 2h about 100 ℃ makes pretreated petroleum coke powder.Then moulding, charing, activation, the deposition step according to embodiment 1 carries out.The intensity that prepared CMS measures with rotary drum reaches 99.1%, N
2The total hole volume of determining adsorption is 0.060ml/g, and the sky that the double tower pressure-swing absorption apparatus is measured divides performance N
2Exit concentration be 97.2%.
Embodiment 3:
Get the 300g coke powder and 20% salpeter solution 300ml mixes, reaction 1h, being washed till the pH value with deionized water then is 5
~6, dry 2h about 100 ℃ makes pretreated petroleum coke powder.Then moulding, charing, activation, the deposition step according to embodiment 1 carries out.The intensity that prepared CMS measures with rotary drum reaches 99.1%, N
2The total hole volume of determining adsorption is 0.062ml/g, and the exit concentration of the sky branch performance N2 that the double tower pressure-swing absorption apparatus is measured is 97.9%.
Embodiment 4:
Get the 300g coke powder and 30% hydrogen peroxide 300ml mixes, reaction 1h, being washed till the pH value with deionized water then is 5
~6, dry 2h about 100 ℃ makes pretreated petroleum coke powder.Then moulding, charing, activation, the deposition step according to embodiment 1 carries out.The intensity that prepared CMS measures with rotary drum reaches 99.3%, N
2The total hole volume of determining adsorption is 0.051ml/g, and the sky that the double tower pressure-swing absorption apparatus is measured divides performance N
2Exit concentration be 95.7%.
Claims (5)
1, a kind of method of preparing carbon molecular sieve by preoxidation of petrol coke is characterized in that: its method steps is:
(1) at first petroleum coke powder is broken to particle diameter less than 5～10 μ m, wherein 90% less than 5 μ m;
(2) pre-oxidation treatment: it is in 10～98% Oxidant solution that the refinery coke immersion is prepared mass concentration, at room temperature continuously stirring is 0.5～4 hour, make it to mix, it was 5～6 that reaction is washed to filtrate pH value after stopping again, 100～110 ℃ of dryings 2～6 hours;
(3) add binding agent, adhesive aid and water and mediate, extrusion molding again, the mass ratio of material is when kneaded and formed, petroleum coke powder: binding agent: adhesive aid: water is 1: 0.2～0.7: 0.02～0.1: 0.4～0.8;
(4) carry out charing, activation and carbon laydown after the forming composition drying is handled and transfer the hole to handle, promptly obtain carbon molecular sieve of the present invention, carbonization condition is: the converter charing, and 2～10 ℃/min of temperature rise rate, temperature is 800～900 ℃, nitrogen or argon shield; Carbon laydown transfers the hole treatment condition to be: carbon laydown reagent is benzene or methane, and volumetric concentration is 3～20%, and carrier gas is nitrogen or argon gas, and depositing temperature is 700～800 ℃, and the time is 0.5～3h; Activation condition is: activator is water vapour or carbonic acid gas, and volumetric concentration is 30～80%, and carrier gas is nitrogen or argon gas, and activation temperature is 800～900 ℃, and soak time is 0.5～3h.
2, according to the method for claim 1 described a kind of preparing carbon molecular sieve by preoxidation of petrol coke, it is characterized in that the ash content of described refinery coke≤1.0%, moisture≤5.0%, volatile matter≤18%, carbon content 〉=90%.
According to the method for claim 5 described a kind of preparing carbon molecular sieve by preoxidation of petrol coke, it is characterized in that 3, described oxygenant is 90～98wt%H
2SO
4, 10～30wt%H
2O
2, or 10～40wt%HNO
3Solution.
4, according to the method for claim 1 described a kind of preparing carbon molecular sieve by preoxidation of petrol coke, it is characterized in that, described binding agent is a heat-reactive phenolic resin, and its performance meets following index: viscosity is 0.3～1.5Pas/20 ℃, and solid content is 55～75%.
According to the method for claim 1 described a kind of preparing carbon molecular sieve by preoxidation of petrol coke, it is characterized in that 5, described adhesive aid is water soluble starch or carboxymethyl cellulose.
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| CN100595142C CN100595142C (en) | 2010-03-24 |
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| CN104826588A (en) * | 2015-04-29 | 2015-08-12 | 长沙清能环保科技有限公司 | Preparation and regeneration method of fluorine removing material on basis of coal-based coke powder |
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| CN101973542B (en) * | 2010-11-26 | 2013-06-12 | 深圳市今朝时代新能源技术有限公司 | Preparation method of porous carbon material for supercapacitor |
| CN103894150A (en) * | 2014-03-31 | 2014-07-02 | 沈阳工业大学 | Preparation method of carbon membrane for oil-water separation |
| CN103894150B (en) * | 2014-03-31 | 2016-01-20 | 沈阳工业大学 | A kind of preparation method of the carbon membrane for water-oil separating |
| CN104826588A (en) * | 2015-04-29 | 2015-08-12 | 长沙清能环保科技有限公司 | Preparation and regeneration method of fluorine removing material on basis of coal-based coke powder |
| CN107866199A (en) * | 2016-09-26 | 2018-04-03 | 中国石化扬子石油化工有限公司 | A kind of carbon molecular sieve for liquefied gas adsorption dewatering, and preparation method thereof |
| CN107866199B (en) * | 2016-09-26 | 2020-06-02 | 中国石化扬子石油化工有限公司 | Carbon molecular sieve for adsorption and dehydration of liquefied gas and preparation method thereof |
| CN107572539A (en) * | 2017-09-19 | 2018-01-12 | 常州朋悦纺织品有限公司 | A kind of preparation method of plural gel heat-barrier material |
| CN108160108A (en) * | 2018-02-11 | 2018-06-15 | 安徽海德化工科技有限公司 | For the preparation method of the molecular sieve of phenol hydroxylation |
| CN108435232A (en) * | 2018-02-11 | 2018-08-24 | 安徽海德化工科技有限公司 | The preparation method of molecular sieve for catalytic oxidation of cyclohexane |
| CN108467035A (en) * | 2018-02-11 | 2018-08-31 | 安徽海德化工科技有限公司 | The preparation method of carbon molecular sieve based on petroleum coke |
| CN111573667A (en) * | 2020-06-28 | 2020-08-25 | 中国石油化工股份有限公司 | Energy storage carbon material, supercapacitor and preparation method thereof |
| CN111573667B (en) * | 2020-06-28 | 2022-02-01 | 中国石油化工股份有限公司 | Energy storage carbon material, supercapacitor and preparation method thereof |
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|---|---|
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