CN114525161B - Coke passivating agent and preparation method thereof - Google Patents

Coke passivating agent and preparation method thereof Download PDF

Info

Publication number
CN114525161B
CN114525161B CN202210274666.0A CN202210274666A CN114525161B CN 114525161 B CN114525161 B CN 114525161B CN 202210274666 A CN202210274666 A CN 202210274666A CN 114525161 B CN114525161 B CN 114525161B
Authority
CN
China
Prior art keywords
coke
parts
passivating agent
portions
weight
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.)
Active
Application number
CN202210274666.0A
Other languages
Chinese (zh)
Other versions
CN114525161A (en
Inventor
项斌
郑怀峰
陈观堃
吴高峰
陈艳
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.)
Ningbo Fareasttech Catalyst Engineering Co ltd
Original Assignee
Ningbo Fareasttech Catalyst Engineering Co ltd
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 Ningbo Fareasttech Catalyst Engineering Co ltd filed Critical Ningbo Fareasttech Catalyst Engineering Co ltd
Priority to CN202210274666.0A priority Critical patent/CN114525161B/en
Publication of CN114525161A publication Critical patent/CN114525161A/en
Application granted granted Critical
Publication of CN114525161B publication Critical patent/CN114525161B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L9/00Treating solid fuels to improve their combustion
    • C10L9/10Treating solid fuels to improve their combustion by using additives
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/14Use of additives to fuels or fires for particular purposes for improving low temperature properties
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B5/00Making pig-iron in the blast furnace
    • C21B5/007Conditions of the cokes or characterised by the cokes used
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2200/00Components of fuel compositions
    • C10L2200/02Inorganic or organic compounds containing atoms other than C, H or O, e.g. organic compounds containing heteroatoms or metal organic complexes
    • C10L2200/0204Metals or alloys
    • C10L2200/0213Group II metals: Be, Mg, Ca, Sr, Ba, Ra, Zn, Cd, Hg
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2200/00Components of fuel compositions
    • C10L2200/02Inorganic or organic compounds containing atoms other than C, H or O, e.g. organic compounds containing heteroatoms or metal organic complexes
    • C10L2200/0204Metals or alloys
    • C10L2200/0218Group III metals: Sc, Y, Al, Ga, In, Tl
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2200/00Components of fuel compositions
    • C10L2200/02Inorganic or organic compounds containing atoms other than C, H or O, e.g. organic compounds containing heteroatoms or metal organic complexes
    • C10L2200/0268Phosphor containing compounds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2200/00Components of fuel compositions
    • C10L2200/02Inorganic or organic compounds containing atoms other than C, H or O, e.g. organic compounds containing heteroatoms or metal organic complexes
    • C10L2200/0272Silicon containing compounds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2200/00Components of fuel compositions
    • C10L2200/02Inorganic or organic compounds containing atoms other than C, H or O, e.g. organic compounds containing heteroatoms or metal organic complexes
    • C10L2200/029Salts, such as carbonates, oxides, hydroxides, percompounds, e.g. peroxides, perborates, nitrates, nitrites, sulfates, and silicates
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2200/00Components of fuel compositions
    • C10L2200/04Organic compounds
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Abstract

The invention relates to the technical field of coke production aids, in particular to a coke passivating agent and a preparation process thereof. The coke passivating agent comprises the following components in parts by weight: 30-40 parts of boron-containing compound, 10-15 parts of silicon dioxide, 5-10 parts of titanium dioxide, 3-5 parts of calcium carbonate, 3-5 parts of calcium phosphate and 1-3 parts of lanthanum chloride, wherein the boron-containing compound comprises boric acid, borax and boron oxide, and the boric acid is prepared from the following components in percentage by weight: borax: boron oxide = 1:1-3:1-3. The beneficial effects of the invention are as follows: the coke passivating agent can obviously reduce the reactivity of coke and improve the strength after reaction.

Description

Coke passivating agent and preparation method thereof
Technical Field
The invention belongs to the technical field of coke production aids, and particularly relates to a coke passivating agent and a preparation method thereof.
Background
Coke is a solid fuel formed by pyrolysis, polycondensation, solidification, shrinkage and other complex physical and chemical processes of coking coal under the action of high-temperature carbonization. The carbon content is above 96%, and the heat value is 29 multiplied by 103kJ/kg. The coke is mainly used for blast furnace iron making and blast furnace smelting of nonferrous metals such as copper, lead, zinc, titanium, antimony, mercury and the like, and plays roles of a reducing agent, a heating agent and a material column framework. In the performance index of coke, the reactivity and the strength after reaction of the coke are more and more important for blast furnace ironmaking. At present, the coke passivating agent can reduce the reactivity of the coke and improve the strength of the coke after reaction.
Chinese patent publication No. CN101654634a discloses a coke passivating agent. The coke passivating agent comprises the following raw materials in parts by weight: 1-16 parts of glucose or calcium chloride, 1-45 parts of boric anhydride, 1-15 parts of titanium dioxide, 1-10 parts of silicon dioxide, 1-45 parts of anhydrous borax, 1-46 parts of calcium borate and 1-30 parts of barium metaborate. The coke passivating agent can improve the thermal performance of the coke, inhibit the dissolution loss reaction of the coke, reduce the reactivity of the coke, increase the thermal strength of the coke, optimize the carbon morphology and reduce the fragmentation of the coke after being charged into a furnace.
Based on this, the present inventors have desired to provide another coke passivating agent capable of reducing the reactivity of coke and improving the strength after the reaction.
Disclosure of Invention
The invention aims to provide a coke passivating agent which can obviously reduce the reactivity of coke and improve the strength after reaction. The above object of the present invention is achieved by the following technical solutions:
a coke passivating agent comprises the following components in parts by weight:
30-40 parts of boron-containing compound
10-15 parts of silicon dioxide
Titanium dioxide 5-10 parts
3-5 parts of calcium carbonate
1-3 parts of calcium phosphate
Lanthanum chloride 0.5-1 parts
The boron-containing compound comprises boric acid, borax and boron oxide, wherein the weight ratio of the boric acid to the borax to the boron oxide is 1:1-3:1-3.
Further, the coke passivating agent also comprises 20-30 parts of high magnesium powder according to parts by weight.
Further, the coke passivating agent also comprises 5-10 parts of silicon aluminum powder and 5-10 parts of silicon calcium powder according to the parts by weight.
Further, the coke passivating agent also comprises 1-5 parts of fructose according to parts by weight.
Further, the coke passivating agent comprises 1-3 parts of triethanolamine by weight.
The invention also aims to provide a preparation process of the coke passivating agent, which comprises the following steps:
step one: mixing boric acid, borax and boric oxide according to the weight ratio of boric acid to borax to boric oxide=1:1-3:1-3 to obtain a boron-containing compound;
step two: according to the weight portions, weighing 30-40 portions of boron-containing compound, 10-15 portions of silicon dioxide, 5-10 portions of titanium dioxide, 3-5 portions of calcium carbonate, 1-3 portions of calcium phosphate, 0.5-1 portion of lanthanum chloride, 20-30 portions of high magnesium powder, 5-10 portions of silicon aluminum powder, 5-10 portions of silicon calcium powder, 1-5 portions of fructose and 1-3 portions of triethanolamine, and uniformly mixing.
In summary, the invention has the following beneficial effects:
1. boric acid and boric acid radical in borax can be combined with carbon atoms around the crystal lattice under the condition of no water gas, so that the total amount of active sites such as edge carbon atoms and the like is reduced; boron intercalates between the layers of graphite crystals in the form of compounds in the coke, forming substitutional solid solutions in the carbon; boric acid and borax are covered on the surface of coke to play a role of a protective film; boron is a nonmetallic element, has the reaction performance of common nonmetallic elements, and in most cases, receives electrons, and forms electronegative ions on the surface of coke, so that the chemical adsorption potential of oxygen is increased, the reaction of oxygen on carbon is blocked, and the generation of CO is inhibited; when boric acid is heated to 1100 ℃ along with coke, partial dehydration is carried out to obtain metaboric acid HBO 2 Further dehydrating to obtain B 2 O 3 ,B 2 O 3 Is typically an acidic substance. Due to the dehydration of acidic substances by heating, in B 2 O 3 The surface forms B-O-B bonds. B is an electron-deficient body, has electrophilic tendency, and is easy to occur on the defect site of the coke surface due to the dissolution reaction of coke. The presence of a large number of carbon arc pairs on these surface defect sites causes the B-O-B bonds to readily aggregate toward lone pairs, thereby blocking the active sites upon which the dissolution reaction occurs, and the effective surface area of the active sites decreases, thereby preventing the dissolution reaction from occurring, and the blocking effect is enhanced by the increase in the number of B-O-B bonds. Therefore, the reactivity of the dissolution loss reaction of the coke is continuously reduced by adding boric acid and borax, and the strength after the reaction is continuously enhanced;
2. the addition of the boron oxide increases the number of B-O-B bonds, so that the blocking effect on the dissolution loss reaction is further enhanced;
3. di-oxidationSilicon, titanium dioxide, calcium carbonate and calcium phosphate have negative catalysis on the reactivity of coke, so that the reactivity of the coke is reduced, and the strength of the coke after reaction is improved; phosphorus intercalates between layers of graphite crystals in the form of compounds in coke, forming substitutional solid solutions in carbon; phosphorus is a nonmetallic element, has the reaction performance of common nonmetallic elements, and in most cases, receives electrons, and forms electronegative ions on the surface of coke, so that the chemical adsorption potential of oxygen is increased, the reaction of oxygen on carbon is blocked, and the generation of CO is inhibited; the phosphate radical is partially dehydrated to obtain metaphosphoric acid HPO when the coke is heated to 1100 DEG C 3 Further dehydrating to obtain P 2 O 5 ,P 2 O 5 Is typically an acidic substance. Due to the dehydration of acidic substances by heating, at P 2 O 5 The surface forms P-O-P bonds. P is an electron-deficient body, has a tendency to be electrophilic, and the coke dissolution reaction is likely to occur at the defective site on the coke surface. The presence of a large number of carbon arc pairs on these surface defect sites causes the P-O-P bonds to readily aggregate toward lone pairs, thereby blocking the active sites upon which the dissolution reaction occurs, and the effective surface area of the active sites decreases, thereby preventing the dissolution reaction from occurring, and the blocking effect is enhanced by the increase in the number of P-O-P bonds. Therefore, the reactivity of the dissolution loss reaction of the coke is continuously reduced by adding the calcium phosphate, and the strength after the reaction is continuously enhanced;
4. lanthanum chloride is a trace element lanthanum introduced into a coke thermal-strength material system, and the addition of lanthanum can enhance the passivation effect of a passivating agent, so that the reactivity of the coke is further reduced, and the strength of the coke after reaction is improved;
5. alumina, high magnesium powder, silicon aluminum powder, silicon calcium powder and fructose are used as fillers, and are filled in micropores on the surface of coke, so that the production cost is reduced;
6. the triethanolamine is used as an antifreezing agent, and can endow the coke antifreezing agent with good antifreezing effect, so that the usability of the coke passivating agent in cold weather is enhanced.
Detailed Description
Examples 1-5 are presented to illustrate the composition of coke thermal strength materials. The components of examples 1-5 are shown in Table 1.
Table 1, examples 1-5 Coke Heat-Strength Material composition Table
Example 1 Example 2 Example 3 Example 4 Example 5
Boron-containing compound(s) 40 30 33 35 38
Boric acid, borax and boric oxide 1∶1∶3 1∶1∶1 1∶1∶2 1∶3∶2 1∶2∶1
Silica/part 15 10 12 13 14
Titanium dioxide/part 10 8 6 5 7
Calcium carbonate/part 5 4 3 5 4
Calcium phosphate/part 3 2 1 2 3
Lanthanum chloride/part 1 0.8 0.5 0.7 1
High magnesium powder 30 20 22 25 27
Silicon aluminum powder/part 10 5 8 7 6
Silicon-calcium powder 5 10 7 8 9
Fructose/serving 5 4 3 1 2
Triethanolamine/part 3 2 1 1 2
Note that: the unit "parts" refers to parts by weight
The preparation process of the coke passivating agent of examples 1-5 is described in detail below in conjunction with table 1.
A preparation process of a coke passivating agent comprises the following steps:
step one: mixing boric acid, borax and boron oxide according to a weight ratio to obtain a boron-containing compound;
step two: weighing boron-containing compound, silicon dioxide, titanium dioxide, calcium carbonate, calcium phosphate, lanthanum chloride, high-magnesium powder, silicon aluminum powder, silicon calcium powder, fructose and triethanolamine according to parts by weight, and uniformly mixing.
The method of using the coke passivating agent of examples 1-5 is described in detail below.
The application method of the coke passivating agent comprises the following steps:
step 1: adding a coke passivating agent into water, and stirring for 5min to prepare a coke passivating agent solution with the concentration of 5%;
step 2: uniformly spraying the coke passivating agent solution on the surface of the coke, wherein the spraying amount is 10% of the mass of the coke, and storing the coke for 1h after the spraying is finished.
Reactivity and post-reaction Strength test
Step 1: the reactivity and the post-reaction strength of the coke sprayed with the coke passivating agent of examples 1 to 5 respectively were tested by referring to GB/T4000-1996 method for testing coke reactivity and post-reaction strength, and the coke sprayed with the coke passivating agent of examples 1 to 5 was measured as a control;
step 2: after repeating step 1 4 times, the obtained 5 times coke reactivity and post-reaction intensity were averaged.
Table 2, table of coke reactivity and post-reaction strength test record
From table 2 the following conclusions can be drawn:
1. comparative and examples 1-5, the reactivity of the coke sprayed with the coke passivating agent of examples 1-5 was much lower than that of the comparative example, and the strength after reaction was much higher than that of the comparative example;
2. comparative examples 1-5, spray example 3 was less reactive than the other examples and was stronger after reaction than the other examples.
Mechanical Strength test
The mechanical strength of the coke after spraying the coke passivating agent of examples 1 to 5 respectively was measured with reference to GB/T2006-2008 "method for measuring mechanical strength of Coke", while the coke without spraying the coke passivating agent of examples 1 to 5 was measured as a control.
Table 3, table of mechanical strength test record of coke
Comparative example Example 1 Example 2 Example 3 Example 4 Example 5
M 40 /% 82.1 84.5 84.6 84.8 84.7 84.6
M 10 /% 6.9 5.3 5.1 5.0 5.2 5.4
Note that: m is M 40 The larger the surface crushing strength is, the higher is; m is M 10 The smaller the indicating higher the abrasion resistance.
From table 3 the following conclusions can be drawn:
1. the comparative examples and comparative examples 1 to 5 were higher in crushing strength and abrasion resistance of the coke sprayed with the coke passivating agent of examples 1 to 5, i.e., the mechanical strength of the coke sprayed with the coke passivating agent of examples 1 to 5 was higher;
2. in comparison with comparative examples 1 to 5, the crushing strength and abrasion resistance of the coke sprayed with the coke passivating agent of example 3 were higher than those of the other examples, i.e., the mechanical strength of the coke sprayed with the coke passivating agent of example 3 was higher.
Comparative example 1
Example 4 of chinese patent publication No. CN101654634a was chosen as comparative example 1.
The coke sprayed with the coke passivating agent of example 3 and the coke sprayed with the coke passivating agent of comparative example 1 were tested with reference to the reactivity and strength after reaction test procedure, and the coke sprayed with the coke passivating agent of example 3 and the coke sprayed with the coke passivating agent of comparative example 1 were tested with reference to the mechanical strength test procedure.
Table 4, comparative example 1 and example 3 comparative test record table
Example 3 Comparative example 1
Reactivity/% 21.47 28.19
Post reaction intensity/% 72.04 64.28
M 40 /% 84.8 83.2
M 10 /% 5.0 6.6
Note that: the larger M40, the higher the surface crushing strength; the smaller M10 indicates higher wear resistance.
From table 4, it can be concluded that the reactivity of the coke sprayed with the coke passivating agent of example 3 is lower, the strength after reaction is higher, and the crushing strength and the abrasion resistance are higher, compared to comparative example 1. Therefore, the invention can obviously reduce the reactivity of the coke and improve the strength and mechanical strength of the coke after reaction.
Comparative example 2
Comparative example 2 differs from example 3 in that ferroferric oxide was removed, and the other is the same as example 3.
Comparative example 3
Comparative example 3 differs from example 3 in that lanthanum chloride was removed, and the other is the same as example 3.
Comparative example 4
Comparative example 4 differs from example 3 in that the ferroferric oxide and lanthanum chloride were removed simultaneously, and the other is the same as example 3.
The coke sprayed with the coke passivating agent of example 3 and the coke sprayed with the coke passivating agents of comparative examples 2 to 4, respectively, were tested with respect to the reactivity and the post-reaction strength test procedure, and the coke sprayed with the coke passivating agent of example 3 and the coke sprayed with the coke passivating agent of comparative examples 2 to 4, respectively, were tested with respect to the mechanical strength test procedure.
Table 5, example 3 and comparative examples 2-4 comparative test record Table
Example 3 Comparative example 2 Comparative example 3 Comparative example 4
Reactivity/% 21.47 25.74 25.89 26.12
Post reaction intensity/% 72.04 66.96 67.01 66.34
M 40 /% 84.8 83.6 83.5 83.4
M 10 /% 5.0 6.3 6.4 6.7
Note that: the larger M40, the higher the surface crushing strength; the smaller M10 indicates higher wear resistance.
From table 5 the following conclusions can be drawn:
the coke sprayed with the coke passivating agent of example 3 is superior to the coke sprayed with the coke passivating agents of comparative examples 2 and 3, respectively, in reactivity, strength after reaction, crushing strength, abrasion resistance, and the like.
The coke sprayed with the coke passivating agent of comparative example 4 was inferior to the coke sprayed with the coke passivating agents of comparative example 2 and comparative example 3, respectively, in both reactivity and strength after reaction. Thus, both calcium phosphate and lanthanum chloride can reduce the reactivity and improve the strength after the reaction. However, the degree of decrease in reactivity and the degree of increase in post-reaction strength caused by the combination of calcium phosphate and lanthanum chloride are greater than the sum of the degree of decrease in reactivity and the degree of increase in post-reaction strength caused by the separate use of calcium phosphate and lanthanum chloride. Therefore, the calcium phosphate and the lanthanum chloride can generate a compounding effect in the invention, and the reduction degree of the reactivity and the improvement degree of the strength after the reaction are increased.
The coke sprayed with the coke passivating agent of comparative example 2 was inferior to the coke sprayed with the coke passivating agent of comparative example 4 in both crushing strength and abrasion resistance, but was closer to the coke sprayed with the coke passivating agent of comparative example 3. It can be seen that lanthanum chloride has little effect on crushing strength and abrasion resistance, while calcium phosphate can improve crushing strength and abrasion resistance. However, the combination of calcium phosphate and lanthanum chloride results in a greater degree of improvement in crushing strength and abrasion resistance than lanthanum chloride alone. Therefore, the calcium phosphate and the lanthanum chloride can produce a compound effect in the invention, and the improvement degree of crushing strength and wear resistance is increased.
The present embodiment is merely illustrative of the present invention and is not intended to be limiting, and modifications thereof without creative contribution can be made by those skilled in the art after reading the present specification, as long as they are protected by patent laws within the scope of claims of the present invention.

Claims (6)

1. A coke passivating agent, which comprises the following components in parts by weight:
30-40 parts of boron-containing compound
10-15 parts of silicon dioxide
Titanium dioxide 5-10 parts
3-5 parts of calcium carbonate
1-3 parts of calcium phosphate
Lanthanum chloride 0.5-1 parts
The boron-containing compound comprises boric acid, borax and boron oxide, wherein the boric acid comprises the following components in percentage by weight: borax: boron oxide = 1:1-3:1-3.
2. The coke passivating agent of claim 1, wherein the coke thermal strength material further comprises 20-30 parts by weight of high magnesium powder.
3. The coke passivating agent according to claim 1, further comprising 5-10 parts by weight of silicon aluminum powder and 5-10 parts by weight of silicon calcium powder.
4. The coke passivating agent of claim 1, further comprising 1-5 parts by weight of fructose.
5. The coke passivating agent of claim 1, further comprising 1-3 parts by weight of triethanolamine.
6. The preparation process of the coke passivating agent is characterized by comprising the following steps of:
step one: boric acid, borax and boric oxide are mixed according to the weight ratio: borax: mixing boron oxide=1:1-3:1-3 to obtain a boron-containing compound;
step two: according to the weight portions, weighing 30-40 portions of boron-containing compound, 10-15 portions of silicon dioxide, 5-10 portions of titanium dioxide, 3-5 portions of calcium carbonate, 1-3 portions of calcium phosphate, 0.5-1 portion of lanthanum chloride, 20-30 portions of high magnesium powder, 5-10 portions of silicon aluminum powder, 5-10 portions of silicon calcium powder, 1-5 portions of fructose and 1-3 portions of triethanolamine, and uniformly mixing.
CN202210274666.0A 2022-03-18 2022-03-18 Coke passivating agent and preparation method thereof Active CN114525161B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202210274666.0A CN114525161B (en) 2022-03-18 2022-03-18 Coke passivating agent and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202210274666.0A CN114525161B (en) 2022-03-18 2022-03-18 Coke passivating agent and preparation method thereof

Publications (2)

Publication Number Publication Date
CN114525161A CN114525161A (en) 2022-05-24
CN114525161B true CN114525161B (en) 2023-08-01

Family

ID=81626062

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202210274666.0A Active CN114525161B (en) 2022-03-18 2022-03-18 Coke passivating agent and preparation method thereof

Country Status (1)

Country Link
CN (1) CN114525161B (en)

Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR689738A (en) * 1930-02-11 1930-09-10 Process for reducing the reactivity of metallurgical cokes
JPH02120393A (en) * 1988-10-28 1990-05-08 Nippon Steel Chem Co Ltd Coke
BR9805156A (en) * 1998-11-27 2000-06-06 Elbert Leonardo Lopes Coal fines recycling process
JP2009094231A (en) * 2007-10-05 2009-04-30 Mitsubishi Chemicals Corp Light-emitting device
CN101654634A (en) * 2009-09-09 2010-02-24 重庆汉砧科技有限公司 Coke passivating agent
CN101932383A (en) * 2008-01-25 2010-12-29 道达尔石油化学产品研究弗吕公司 Process for obtaining modified molecular sieves
CN101932384A (en) * 2008-01-25 2010-12-29 道达尔石油化学产品研究弗吕公司 Process for obtaining catalyst composites comprising meapo and their use in conversion of organics to olefins
CN107904272A (en) * 2011-02-14 2018-04-13 希乐克公司 Processing biomass
CN108473484A (en) * 2015-10-01 2018-08-31 赛诺米克斯公司 It can be used as the compound of TRPM8 conditioning agents
CN109022098A (en) * 2018-08-17 2018-12-18 宁波敬业控股集团有限公司 Coke deactivator and preparation method thereof
KR20190005108A (en) * 2017-07-05 2019-01-15 상명이엔텍 주식회사 Additive to reduce the amount of fine dist and increase the collection efficiency of dust collector
CN109762622A (en) * 2019-02-25 2019-05-17 谭祖伍 A kind of preparation method of oxidizing solids

Patent Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR689738A (en) * 1930-02-11 1930-09-10 Process for reducing the reactivity of metallurgical cokes
JPH02120393A (en) * 1988-10-28 1990-05-08 Nippon Steel Chem Co Ltd Coke
BR9805156A (en) * 1998-11-27 2000-06-06 Elbert Leonardo Lopes Coal fines recycling process
JP2009094231A (en) * 2007-10-05 2009-04-30 Mitsubishi Chemicals Corp Light-emitting device
CN101932383A (en) * 2008-01-25 2010-12-29 道达尔石油化学产品研究弗吕公司 Process for obtaining modified molecular sieves
CN101932384A (en) * 2008-01-25 2010-12-29 道达尔石油化学产品研究弗吕公司 Process for obtaining catalyst composites comprising meapo and their use in conversion of organics to olefins
CN101654634A (en) * 2009-09-09 2010-02-24 重庆汉砧科技有限公司 Coke passivating agent
CN107904272A (en) * 2011-02-14 2018-04-13 希乐克公司 Processing biomass
CN108473484A (en) * 2015-10-01 2018-08-31 赛诺米克斯公司 It can be used as the compound of TRPM8 conditioning agents
KR20190005108A (en) * 2017-07-05 2019-01-15 상명이엔텍 주식회사 Additive to reduce the amount of fine dist and increase the collection efficiency of dust collector
CN109022098A (en) * 2018-08-17 2018-12-18 宁波敬业控股集团有限公司 Coke deactivator and preparation method thereof
CN109762622A (en) * 2019-02-25 2019-05-17 谭祖伍 A kind of preparation method of oxidizing solids

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
降低1#高炉燃料消耗的生产实践;陈艳等;《钢铁冶炼》;19-21 *

Also Published As

Publication number Publication date
CN114525161A (en) 2022-05-24

Similar Documents

Publication Publication Date Title
CN109022098B (en) Coke passivator and preparation method thereof
CN102225780B (en) High-activity calcium oxide and production method thereof
CN100453658C (en) Deoxygenation furnace-curing agent and its production
CN102676799B (en) Preparation method for boron-magnesium composite additive for pellets and product
CN102041422A (en) Silicon nitride ferrovanadium and production method thereof
CN100519711C (en) Coke passivator and preparation method thereof
CN111977997B (en) Control method for realizing steel slag reduction modification, water-quenched slag and application thereof
CN110330314A (en) A kind of steel-making refining inner lining of furnace low-carbon Ultra-low carbon mg-ca-carbon refractory and preparation method thereof
CN114525161B (en) Coke passivating agent and preparation method thereof
CN114525160B (en) Coke heat strong auxiliary material and preparation process thereof
CN101531939A (en) Coke deterioration inhibitor and preparation method thereof
CN103881741A (en) Pulverized coal activator and method for coking
CN112979189B (en) Modification method of converter slag applied to cement production
CN102312049B (en) Desulfurizing agent suitable for high-aluminum silicon steel and preparation method thereof
KR101267642B1 (en) Method for manufacturing of heat resistant cement
CN1873030A (en) Assistant deoxidizer in use for smelting cold rolled and hot rolled low carbon aluminium-killed steel
CN112899052B (en) Hydrogen inhibitor and method for producing coke by adding large-proportion high-volatility bituminous coal
CN102071081B (en) Passivated coke and preparation method thereof
CN104087698B (en) Pig iron carburization technique by coal-base direct reduction
CN1318609C (en) Agglomerate surface additive for ironmaking
CN112811884A (en) Magnesium-carbon modifier prepared from middle ladle residual lining
CN111334643A (en) Deoxidizing and slagging material for steelmaking, preparation method and use method thereof
KR101320083B1 (en) Binder for manufacturing Fe-containing briquettes using electric furnace reduction slag and manufacturing method thereof
CN102453785A (en) Pre-molten desulfurizing agent and preparation method thereof
CN110760320A (en) Coke thermal structure reinforcer

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
GR01 Patent grant
GR01 Patent grant