CN104263396A - Briquette raw material for coking technique - Google Patents
Briquette raw material for coking technique Download PDFInfo
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- CN104263396A CN104263396A CN201410471536.1A CN201410471536A CN104263396A CN 104263396 A CN104263396 A CN 104263396A CN 201410471536 A CN201410471536 A CN 201410471536A CN 104263396 A CN104263396 A CN 104263396A
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
- C10B57/04—Other carbonising or coking processes; Features of destructive distillation processes in general using charges of special composition
- C10B57/06—Other carbonising or coking processes; Features of destructive distillation processes in general using charges of special composition containing additives
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
- C10B53/08—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form in the form of briquettes, lumps and the like
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- Oil, Petroleum & Natural Gas (AREA)
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Abstract
The invention provides a briquette raw material for a coking technique, which comprises a low-rank coal briquette layer formed by low-rank coal and an assistant, and a non-low-rank coal briquette layer formed by one or more of medium-rank coal, high-rank coal and medium-high-low coal, wherein the assistant is an organic binder of which the weight loss is less than 50% when being carbonized at 850 DEG C in the absence of air; the low-rank coal briquette layer is arranged on the non-low-rank coal briquette layer; and the low-rank coal accounts for 50-80 wt% of the briquette raw material. When being used for coking treatment, the briquette raw material solves the problems of low availability and surplus productivity of coking industry in the existing tamping cokery, and also solves the problem of limited application due to no large-scale industrialized equipment for low-rank coal. After the assistant and low-rank coal are mixed, the effective component in the assistant is beneficial to degradation of high-molecular polymers in the low-rank coal at high temperature and also beneficial to rupture of high polymers in the low-rank coal, thereby enhancing the oil gas yield in the technical process.
Description
Technical field
The present invention relates to a kind of coal raw material being applicable to coking process, be specifically related to a kind of employing and existingly make the moulded coal raw material that stove carries out coking process firm by ramming.
Background technology
Coal is the main energy sources of China, in primary energy structure, account for 70%.In very long geological changes process, the formation of coal, by the effect of many factors, causes categories of coal various.According to the difference of structure and composition, coal is divided into the large class of brown coal, bituminous coal and hard coal 3, and its metabituminous coal is divided into again lower-grade metamorphic bituminous and mesometamorphism bituminous coal, is lower-grade metamorphic bituminously sub-bituminous coal again, is referred to as " low-rank coal " together with brown coal.Low-rank coal is the product at incoalation initial stage, have that carbon content is low, moisture is high, easy efflorescence, easily spontaneous combustion, fugitive constituent be high, the feature of immersion intensity difference, anti-dropping intensity difference, these characteristics limit the direct exploitation to low-rank coal, but according to statistics, China's low-rank coal reserves account for the whole nation and have verified more than 55% of coal reserves, reach 5,612 hundred million tons, this causes a kind of waste of resource undoubtedly.And along with day by day increasing of domestic energy demand and falling sharply of high-quality coal stock number, the conversion of low-rank coal fully utilizes the focus becoming people and day by day pay close attention to.
The process for upgrading of low-rank coal is one of means of low-rank coal trans-utilization, its be under isolated air or nonoxidizing atmosphere condition, low-rank coal is heated to 200-800 DEG C carry out in low temperature upgrading, finally obtain the working method of tar, coal gas and semicoke.But current low-rank coal upgrading technology is all in experimental study and through engineering approaches original application stage, there is not the equipment making its heavy industrialization apply, thus limit the exploitation of low-rank coal.
Tamping coke furnace is the maximization equipment adopted in the coking process of coal, its floor space is wide, investment capital cost is large, the coking process adopting tamping coke furnace to carry out coking mainly refers to that high-temperature coking is to obtain coke and to reclaim chemical products, its coke product is metallurgical coke or chemical industry Jiao mainly, due to industrial to the quality requirements of metallurgical coke or chemical industry Jiao, the coal raw material making it adopt mainly comprises coking coal, 1/3 coking coal, bottle coal, rich coal, lean coal, the coals such as meager lean coal, belong to mesometamorphism bituminous coal, due to the shortage of coal resources in recent years, especially for the minimizing of high-quality coal raw material in coking industry, the raw materials cost of coking industry is grown with each passing day, in addition iron and steel in recent years, metallurgy etc. needs the decline of the industry of metallurgical coke or chemical industry Jiao in a large number, on the one hand, the price of coke product is sharply reduced, the rise of cost of material, the decline of product price, China's major part coking industry economic benefit is seriously glided, on the other hand, the minimizing of coke demand forces coke-oven plant to reduce coke output, but due to tamping coke furnace once out of servicely namely scrap, therefore in order to protect the tamping coke furnace equipment furnishing a huge amount of money for invest to build, it has to maintain the operation of coke oven in minimum level, not only reduce the availability of tamping coke furnace, also cause the production capacity surplus of coking industry.How to save the coking industry being on the verge of negative growth in sum, improve the availability of tamping coke furnace, the problem solving coking industry production capacity surplus has become coking industry letter major issue to be solved.
As everyone knows, its object of traditional coking process is mainly in order to obtain coke, particularly metallurgical coke, first to solve coking industry negative growth problem, significantly reduce coking industry desired raw material coal price lattice or improve coke price or the two to have concurrently be selectable approach simultaneously, at present, coke price cannot realize getting warm again after a cold spell in a short time, so can only reduce feed coal price, but because Coke Industry is for the requirement of coke quality, then be traced in the requirement to feed coal, must the index of its volatile matter of considered critical and ash content.Low-rank coal is the coal that in feed coal, price is comparatively cheap, if effectively can utilize low-rank coal, so will contribute to coking industry and extricate oneself from a plight.But low-rank coal has high, the easy efflorescence of volatile matter, feature that ash content is high, and the index of the volatile matter that coking proposes feed coal and ash content is very strict, and this is just doomed the problem by using low-rank coal cannot solve coking industry feed coal price.
Summary of the invention
Problem and the coking process expensive starting materials of large-scale application cannot be realized, the problem that coking industry economic benefit is low, thus the raw material providing a kind of coking process for solving low-rank coal in prior art.
For this reason, the technical scheme that the present invention takes is,
Be applicable to a moulded coal raw material for coking process, comprise the low-rank coal moulded coal layer of low-rank coal and auxiliary agent formation, described auxiliary agent is the organic binder bonds being less than 50% 850 DEG C of isolated air destructive distillation weightlessness; Also comprise one or more the non-low-rank coal moulded coal layers formed in scala media coal, high-order coal or middle high-order coal, described low-rank coal moulded coal layer is arranged on described non-low-rank coal moulded coal layer, in mass, the add-on of described low-rank coal is the 50-80wt% of described moulded coal raw materials quality.
Above-mentioned is applicable in the moulded coal raw material of coking process, and described organic binder bond is the bituminous matter that softening temperature is greater than 100 DEG C.
Above-mentioned is applicable in the moulded coal raw material of coking process, and described auxiliary agent is coal-tar pitch or petroleum pitch, and its softening temperature is not less than 120 DEG C.
Above-mentioned is applicable in the moulded coal raw material of coking process, and the softening temperature of described pitch is not less than 140 DEG C.
Above-mentioned is applicable in the moulded coal raw material of coking process, and described pitch is hard pitch, and in mass, the fixed carbon content of described hard pitch is more than 25%, and ratio of carbon-hydrogen is 8-11.
Above-mentioned is applicable in the moulded coal raw material of coking process, and in mass, the add-on of described auxiliary agent is the 5-40wt% of described low-rank coal quality.
Above-mentioned is applicable in the moulded coal raw material of coking process, and in mass, the add-on of described auxiliary agent is the 10-30wt% of described low-rank coal quality.
Above-mentioned is applicable in the moulded coal raw material of coking process, and in mass, the add-on of described low-rank coal is the 50-60wt% of described moulded coal raw materials quality.
Above-mentioned is applicable in the moulded coal raw material of coking process, and the G value of described low-rank coal is less than 50, and volatile content is greater than 40%.
Compared with prior art, tool of the present invention has the following advantages,
(1) raw material of coking process in the present invention, not only solves that existing tamping coke furnace availability is low, the problem of coking industry production capacity surplus, also solves for low-rank coal owing to making it apply limited problem without large-scale industrialization equipment.
Be added in 850 DEG C of isolated air destructive distillation weightlessness in feed coal in the application and be less than the bituminous matter of 50% as binding agent, be conducive to low-rank coal on the one hand shaping in tamping machine, thus can push in tamping coke furnace and carry out coking, its solid product not easily efflorescence after the coking of another aspect low-rank coal completes, be easy to the coke pushing of tamping coke furnace, after the most important thing is that described auxiliary agent mixes with low order coal facies, effective constituent wherein in auxiliary agent contributes to high molecular fracture in the degraded at high temperature of high molecular polymer in low-rank coal and low-rank coal, thus the output of oil gas in raising technological process, oil gas total amount is made to increase production more than 10%.The quality that non-low-rank coal moulded coal layer contributes to improving the coke that low-rank coal moulded coal layer produces is infiltrated under the liquid that low-rank coal moulded coal layer produces in high temperature grading process simultaneously.And the main component in raw gas is hydrogen and methane, at present, the price of hydrogen, methane is far above the price of coke, the increase of its output improves the economic benefit of enterprise, meanwhile, with the coking process that middle and high rank coal is raw material compared to prior art, adopt low-rank coal as the raw material of coking process, raw materials cost can be reduced to a great extent, simultaneously significant to the development and utilization of low-rank coal.
(2) raw material of coking process in the present invention, described auxiliary agent is the pitch that coal or petroleum raw material reaction are formed, and the softening temperature of described pitch is not less than 120 DEG C, improve low-rank coal coking complete after the quality of its solid product-coke, in coke, volatile matter is not more than the by-product coke that 3-4% makes to obtain and can be used for generating, gas making and other chemical industry object.
Embodiment
Coal composition in the raw material of the coking process of composition the application is applicable to all low-rank coal, scala media coal, high-order coal or middle high-order coal raw material, for ease of explanation, in following embodiment, low-rank coal is for sub-bituminous coal or brown coal, and the coal raw material of non-low-rank coal is for 1/3 coking coal or coking coal.
Wherein, the quality of the quality × 90%+ auxiliary agent of the non-low-rank coal of quality × 75%+ of the quality=low-rank coal of dry coal, what " kg/t dry coal " referred to dry coal per ton obtains product how many kilograms.
Embodiment 1
(1) sub-bituminous coal pulverized and be mixed to form low-rank coal raw material with auxiliary agent, for subsequent use;
(2) adopt tamping machine to make firm by ramming shaping to 1/3 coking coal pulverized, form non-low-rank coal moulded coal layer; And on non-low-rank coal moulded coal layer, continue to add described low-rank coal raw material continue to adopt tamping machine to make firm by ramming shaping to described low-rank coal raw material, form the low-rank coal moulded coal layer be positioned at above described non-low-rank coal moulded coal layer, thus form final moulded coal raw material; Wherein, in mass, the add-on of auxiliary agent is the 40wt% of sub-bituminous coal quality, the add-on of described sub-bituminous coal is the 65wt% of described moulded coal raw material, the G value of described sub-bituminous coal is 45, volatile content is 65%, and described auxiliary agent is the bituminous matter of softening temperature 105 DEG C, and described bituminous matter is 850 DEG C of isolated air destructive distillation weightlessness 45%;
(3) moulded coal raw material pushed in coke oven carry out upgrading, control upgrading temperature 850 DEG C, 16 hours upgrading time, collect overflow raw gas, tar, crude benzol mixture, obtain byproduct coke simultaneously;
Adopt common process to be separated raw gas, tar, and from tar, be separated crude benzol further, the amount of the described raw gas obtained is 450Nm
3/ t dry coal, the amount of described tar is 54kg/t dry coal, and the amount of described byproduct coke is 570kg/t dry coal, and the amount of described crude benzol is 16kg/t dry coal.Described coke comprises the low-rank coal coke of the low-rank coal moulded coal layer generation formed by layering after coke oven release coke and the non-low-rank coal coke of non-low order coal seam generation, in mass, in described low-rank coal coke, solids carbon content is not less than 60%, volatile content is not more than 6%, after coke screening, particle diameter is 20% of coke total mass in the particle total mass of more than 40mm, and particle diameter is 60% of coke total mass in the particle total mass of more than 25mm; In the non-low-rank coal coke that described non-low-rank coal produces, solids carbon content is not less than 82%, volatile content is not more than 5%, after coke screening, particle diameter is 81% of coke total mass in the particle total mass of more than 40mm, and particle diameter is 92% of coke total mass in the particle total mass of more than 25mm.
Embodiment 2
(1) sub-bituminous coal pulverized and be mixed to form low-rank coal raw material with auxiliary agent, for subsequent use;
(2) adopt tamping machine to make firm by ramming shaping to 1/3 coking coal pulverized, form non-low-rank coal moulded coal layer; And on non-low-rank coal moulded coal layer, continue to add described low-rank coal raw material continue to adopt tamping machine to make firm by ramming shaping to described low-rank coal raw material, form the low-rank coal moulded coal layer be positioned at above described non-low-rank coal moulded coal layer, thus form final moulded coal raw material; Wherein, in mass, auxiliary agent add the 35wt% that quality is sub-bituminous coal quality, the add-on of described sub-bituminous coal is the 50wt% of described moulded coal raw materials quality, the G value of described sub-bituminous coal is 40, volatile content is 70%, and described auxiliary agent is the bituminous matter of softening temperature 115 DEG C, and described bituminous matter is 850 DEG C of isolated air destructive distillation weightlessness 40%;
(3) moulded coal raw material pushed in coke oven carry out upgrading, control upgrading temperature 900 DEG C, 15.5 hours upgrading time, collect overflow raw gas, tar, crude benzol mixture, obtain byproduct coke simultaneously;
Adopt common process to be separated raw gas, tar, and from tar, be separated crude benzol further, the amount of the described raw gas obtained is 500Nm
3/ t dry coal, the amount of described tar is 54kg/t dry coal, and the amount of described byproduct coke is 505kg/t dry coal, and the amount of described crude benzol is 16kg/t dry coal.Described coke comprises the low-rank coal coke of the low-rank coal moulded coal layer generation formed by layering after coke oven release coke and the non-low-rank coal coke of non-low order coal seam generation, in mass, in described low-rank coal coke, solids carbon content is not less than 58%, volatile content is not more than 5%, after coke screening, particle diameter is 15% of coke total mass in the particle total mass of more than 40mm, particle diameter is 55% of coke total mass in the particle total mass of more than 25mm, in the non-low-rank coal coke that described non-low-rank coal produces, solids carbon content is not less than 82%, volatile content is not more than 5%, after coke screening, particle diameter is 81% of coke total mass in the particle total mass of more than 40mm, particle diameter is 92% of coke total mass in the particle total mass of more than 25mm.
Embodiment 3
(1) sub-bituminous coal pulverized and be mixed to form low-rank coal raw material with auxiliary agent, for subsequent use;
(2) adopt tamping machine to make firm by ramming shaping to 1/3 coking coal pulverized, form non-low-rank coal moulded coal layer; And on non-low-rank coal moulded coal layer, continue to add described low-rank coal raw material continue to adopt tamping machine to make firm by ramming shaping to described low-rank coal raw material, form the low-rank coal moulded coal layer be positioned at above described non-low-rank coal moulded coal layer, thus form final moulded coal raw material; Wherein, in mass, auxiliary agent add the 30wt% that quality is sub-bituminous coal quality, the add-on of described sub-bituminous coal is the 70wt% of described moulded coal raw materials quality, the G value of described sub-bituminous coal is 35, volatile content is 45%, and described auxiliary agent is the bituminous matter of softening temperature 120 DEG C, and described bituminous matter is 850 DEG C of isolated air destructive distillation weightlessness 42%;
(3) moulded coal raw material pushed in coke oven carry out upgrading, control upgrading temperature 950 DEG C, 17 hours upgrading time, collect overflow raw gas, tar, crude benzol mixture, obtain byproduct coke simultaneously;
Adopt common process to be separated raw gas, tar, and from tar, be separated crude benzol further, the amount of the described raw gas obtained is 500Nm
3/ t dry coal, the amount of described tar is 54kg/t dry coal, and the amount of described byproduct coke is 505kg/t dry coal, and the amount of described crude benzol is 16kg/t dry coal.Described coke comprises the low-rank coal coke of the low-rank coal moulded coal layer generation formed by layering after coke oven release coke and the non-low-rank coal coke of non-low order coal seam generation, in mass, in described low-rank coal coke, solids carbon content is not less than 72%, volatile content is not more than 4%, after coke screening, particle diameter is 15% of coke total mass in the particle total mass of more than 40mm, particle diameter is 55% of coke total mass in the particle total mass of more than 25mm, in the non-low-rank coal coke that described non-low-rank coal produces, solids carbon content is not less than 82%, volatile content is not more than 5%, after coke screening, particle diameter is 81% of coke total mass in the particle total mass of more than 40mm, particle diameter is 92% of coke total mass in the particle total mass of more than 25mm.
Embodiment 4
(1) sub-bituminous coal pulverized and be mixed to form low-rank coal raw material with auxiliary agent, for subsequent use;
(2) adopt tamping machine to make firm by ramming shaping to 1/3 coking coal pulverized, form non-low-rank coal moulded coal layer; And on non-low-rank coal moulded coal layer, continue to add described low-rank coal raw material continue to adopt tamping machine to make firm by ramming shaping to described low-rank coal raw material, form the low-rank coal moulded coal layer be positioned at above described non-low-rank coal moulded coal layer, thus form final moulded coal raw material; Wherein, in mass, auxiliary agent add the 25wt% that quality is sub-bituminous coal quality, the add-on of described sub-bituminous coal for the G value of sub-bituminous coal described in the 75wt% of described moulded coal raw materials quality be 30, volatile content is 65%, described auxiliary agent is the bituminous matter of softening temperature 130 DEG C, and described bituminous matter is 850 DEG C of isolated air destructive distillation weightlessness 40%;
(3) moulded coal raw material pushed in coke oven carry out upgrading, control upgrading temperature 1000 DEG C, 16.5 hours upgrading time, collect overflow raw gas, tar, crude benzol mixture, obtain byproduct coke simultaneously;
Adopt common process to be separated raw gas, tar, and from tar, be separated crude benzol further, the amount of the described raw gas obtained is 680Nm
3/ t dry coal, the amount of described tar is 93kg/t dry coal, and the amount of described byproduct coke is 390kg/t dry coal, and the amount of described crude benzol is 27kg/t dry coal.Described coke comprises the low-rank coal coke of the low-rank coal moulded coal layer generation formed by layering after coke oven release coke and the non-low-rank coal coke of non-low order coal seam generation, in mass, in described low-rank coal coke, solids carbon content is not less than 72%, volatile content is not more than 4%, after coke screening, particle diameter is 15% of coke total mass in the particle total mass of more than 40mm, particle diameter is 55% of coke total mass in the particle total mass of more than 25mm, in the non-low-rank coal coke that described non-low-rank coal produces, solids carbon content is not less than 82%, volatile content is not more than 5%, after coke screening, particle diameter is 81% of coke total mass in the particle total mass of more than 40mm, particle diameter is 92% of coke total mass in the particle total mass of more than 25mm.
Embodiment 5
(1) sub-bituminous coal pulverized and be mixed to form low-rank coal raw material with auxiliary agent, for subsequent use;
(2) adopt tamping machine to make firm by ramming shaping to 1/3 coking coal pulverized, form non-low-rank coal moulded coal layer; And on non-low-rank coal moulded coal layer, continue to add described low-rank coal raw material continue to adopt tamping machine to make firm by ramming shaping to described low-rank coal raw material, form the low-rank coal moulded coal layer be positioned at above described non-low-rank coal moulded coal layer, thus form final moulded coal raw material; Wherein, in mass, auxiliary agent add the 20wt% that quality is sub-bituminous coal quality, the add-on of described sub-bituminous coal is the 80wt% of described moulded coal raw materials quality, the G value of described sub-bituminous coal is 20, volatile content is 60%, and described auxiliary agent is the bituminous matter of softening temperature 140 DEG C, and described bituminous matter is 850 DEG C of isolated air destructive distillation weightlessness 35%;
(3) moulded coal raw material pushed in coke oven carry out upgrading, control upgrading temperature 1100 DEG C, 18 hours upgrading time, collect overflow raw gas, tar, crude benzol mixture, obtain byproduct coke simultaneously;
Adopt common process to be separated raw gas, tar, and from tar, be separated crude benzol further, the amount of the described raw gas obtained is 680Nm
3/ t dry coal, the amount of described tar is 90kg/t dry coal, and the amount of described byproduct coke is 407kg/t dry coal, and the amount of described crude benzol is 27kg/t dry coal.Described coke comprises the low-rank coal coke of the low-rank coal moulded coal layer generation formed by layering after coke oven release coke and the non-low-rank coal coke of non-low order coal seam generation, in mass, in described low-rank coal coke, solids carbon content is not less than 64%, volatile content is not more than 4%, after coke screening, particle diameter is 15% of coke total mass in the particle total mass of more than 40mm, particle diameter is 55% of coke total mass in the particle total mass of more than 25mm, in the non-low-rank coal coke that described non-low-rank coal produces, solids carbon content is not less than 82%, volatile content is not more than 5%, after coke screening, particle diameter is 81% of coke total mass in the particle total mass of more than 40mm, particle diameter is 92% of coke total mass in the particle total mass of more than 25mm.
Embodiment 6
(1) sub-bituminous coal pulverized and be mixed to form low-rank coal raw material with auxiliary agent, for subsequent use;
(2) adopt tamping machine to make firm by ramming shaping to 1/3 coking coal pulverized, form non-low-rank coal moulded coal layer; And on non-low-rank coal moulded coal layer, continue to add described low-rank coal raw material continue to adopt tamping machine to make firm by ramming shaping to described low-rank coal raw material, form the low-rank coal moulded coal layer be positioned at above described non-low-rank coal moulded coal layer, thus form final moulded coal raw material; Wherein, in mass, auxiliary agent add the 15wt% that quality is sub-bituminous coal quality, the add-on of described sub-bituminous coal is the 55wt% of described moulded coal raw materials quality, and the G value of described sub-bituminous coal is 15, and volatile content is 55%, described auxiliary agent is the hard pitch of softening temperature 150 DEG C, described hard pitch is less than 40%, fixed carbon content 28% 850 DEG C of isolated air destructive distillation weightlessness, and ratio of carbon-hydrogen is 8;
(3) shaping feed coal pushed in coke oven carry out upgrading, control upgrading temperature 950 DEG C, 20 hours upgrading time, collect overflow raw gas, tar, crude benzol mixture, obtain byproduct coke simultaneously;
Adopt common process to be separated raw gas, tar, and from tar, be separated crude benzol further, the amount of the described raw gas obtained is 570Nm
3/ t dry coal, the amount of described tar is 62kg/t dry coal, and the amount of described byproduct coke is 492kg/t dry coal, and the amount of described crude benzol is 18kg/t dry coal.Described coke comprises the low-rank coal coke of the low-rank coal moulded coal layer generation formed by layering after coke oven release coke and the non-low-rank coal coke of non-low order coal seam generation, in mass, in described low-rank coal coke, solids carbon content is not less than 64%, volatile content is not more than 5%, after coke screening, particle diameter is 15% of coke total mass in the particle total mass of more than 40mm, particle diameter is 55% of coke total mass in the particle total mass of more than 25mm, in the non-low-rank coal coke that described non-low-rank coal produces, solids carbon content is not less than 82%, volatile content is not more than 5%, after coke screening, particle diameter is 81% of coke total mass in the particle total mass of more than 40mm, particle diameter is 92% of coke total mass in the particle total mass of more than 25mm.
Embodiment 7
(1) sub-bituminous coal pulverized and be mixed to form low-rank coal raw material with auxiliary agent, for subsequent use;
(2) adopt tamping machine to make firm by ramming shaping to 1/3 coking coal pulverized, form non-low-rank coal moulded coal layer; And on non-low-rank coal moulded coal layer, continue to add described low-rank coal raw material continue to adopt tamping machine to make firm by ramming shaping to described low-rank coal raw material, form the low-rank coal moulded coal layer be positioned at above described non-low-rank coal moulded coal layer, thus form final moulded coal raw material; Wherein, in mass, auxiliary agent add the 10wt% that quality is sub-bituminous coal quality, the add-on of described sub-bituminous coal is the 60wt% of described moulded coal raw materials quality, and the G value of described sub-bituminous coal is 20, and volatile content is 50%, described auxiliary agent is the hard pitch of softening temperature 170 DEG C, described hard pitch 850 DEG C of isolated air destructive distillation weightlessness 42%, fixed carbon content 30%, ratio of carbon-hydrogen is 11;
(3) moulded coal raw material pushed in coke oven carry out upgrading, control upgrading temperature 1200 DEG C, 24 hours upgrading time, collect overflow raw gas, tar, crude benzol mixture, obtain byproduct coke simultaneously;
Adopt common process to be separated raw gas, tar, and from tar, be separated crude benzol further, the amount of the described raw gas obtained is 550Nm
3/ t dry coal, the amount of described tar is 54kg/t dry coal, the amount 600kg/t dry coal of described byproduct coke, and the amount of described crude benzol is 16kg/t dry coal.Described coke comprises the low-rank coal coke of the low-rank coal moulded coal layer generation formed by layering after coke oven release coke and the non-low-rank coal coke of non-low order coal seam generation, in mass, in described low-rank coal coke, solids carbon content is not less than 55%, volatile content is not more than 3%, after coke screening, particle diameter is 5% of coke total mass in the particle total mass of more than 40mm, particle diameter is 50% of coke total mass in the particle total mass of more than 25mm, in the non-low-rank coal coke that described non-low-rank coal produces, solids carbon content is not less than 82%, volatile content is not more than 5%, after coke screening, particle diameter is 81% of coke total mass in the particle total mass of more than 40mm, particle diameter is 92% of coke total mass in the particle total mass of more than 25mm.
Embodiment 8
(1) sub-bituminous coal pulverized and be mixed to form low-rank coal raw material with auxiliary agent, for subsequent use;
(2) adopt tamping machine to make firm by ramming shaping to 1/3 coking coal pulverized, form non-low-rank coal moulded coal layer; And on non-low-rank coal moulded coal layer, continue to add described low-rank coal raw material continue to adopt tamping machine to make firm by ramming shaping to described low-rank coal raw material, form the low-rank coal moulded coal layer be positioned at above described non-low-rank coal moulded coal layer, thus form final moulded coal raw material; Wherein, in mass, auxiliary agent add the 5wt% that quality is sub-bituminous coal quality, the add-on of described sub-bituminous coal is the 50wt% of described moulded coal raw materials quality, and the G value of described sub-bituminous coal is 15, and volatile content is 45%, described auxiliary agent is the hard pitch of softening temperature 190 DEG C, described hard pitch 850 DEG C of isolated air destructive distillation weightlessness 45%, fixed carbon content 28%, ratio of carbon-hydrogen is 10;
(3) moulded coal raw material pushed in coke oven carry out upgrading, control upgrading temperature 950 DEG C, 20 hours upgrading time, collect overflow raw gas, tar, crude benzol mixture, obtain byproduct coke simultaneously;
Adopt common process to be separated raw gas, tar, and from tar, be separated crude benzol further, the amount of the described raw gas obtained is 380Nm
3/ t dry coal, the amount of described tar is 46kg/t dry coal, and the amount of described byproduct coke is 653kg/t dry coal, and the amount of described crude benzol is 16kg/t dry coal.Described coke comprises the low-rank coal coke of the low-rank coal moulded coal layer generation formed by layering after coke oven release coke and the non-low-rank coal coke of non-low order coal seam generation, in mass, in described low-rank coal coke, solids carbon content is not less than 64%, volatile content is not more than 4%, after coke screening, particle diameter is 5% of coke total mass in the particle total mass of more than 40mm, particle diameter is 55% of coke total mass in the particle total mass of more than 25mm, in the non-low-rank coal coke that described non-low-rank coal produces, solids carbon content is not less than 82%, volatile content is not more than 5%, after coke screening, particle diameter is 81% of coke total mass in the particle total mass of more than 40mm, particle diameter is 92% of coke total mass in the particle total mass of more than 25mm.
Embodiment 9
(1) brown coal pulverized and be mixed to form low-rank coal raw material with auxiliary agent, for subsequent use;
(2) adopt tamping machine to make firm by ramming shaping to 1/3 coking coal pulverized, form non-low-rank coal moulded coal layer; And on non-low-rank coal moulded coal layer, continue to add described low-rank coal raw material continue to adopt tamping machine to make firm by ramming shaping to described low-rank coal raw material, form the low-rank coal moulded coal layer be positioned at above described non-low-rank coal moulded coal layer, thus form final moulded coal raw material; Wherein, in mass, auxiliary agent add the 10wt% that quality is brown coal quality, the add-on of described brown coal is the 80wt% of described moulded coal raw materials quality, the G value of described brown coal is 20, volatile content is 55%, and described auxiliary agent is the bituminous matter that softening temperature is greater than 110 DEG C, and described bituminous matter is 850 DEG C of isolated air destructive distillation weightlessness 45%;
(3) shaping feed coal pushed in coke oven carry out upgrading, control upgrading temperature 850 DEG C, 16 hours upgrading time, collect overflow raw gas, tar, crude benzol mixture, obtain byproduct coke simultaneously;
Adopt common process to be separated raw gas, tar, and from tar, be separated crude benzol further, the amount of the described raw gas obtained is 550Nm
3/ t dry coal, the amount of described tar is 62kg/t dry coal, and the amount of described byproduct coke is 458kg/t dry coal, and the amount of described crude benzol is 18kg/t dry coal.Described coke comprises the low-rank coal coke of the low-rank coal moulded coal layer generation formed by layering after coke oven release coke and the non-low-rank coal coke of non-low order coal seam generation, in mass, in described low-rank coal coke, solids carbon content is not less than 57%, volatile content is not more than 6%, after coke screening, particle diameter is 15% of coke total mass in the particle total mass of more than 40mm, particle diameter is 50% of coke total mass in the particle total mass of more than 25mm, in the non-low-rank coal coke that described non-low-rank coal produces, solids carbon content is not less than 82%, volatile content is not more than 5%, after coke screening, particle diameter is 81% of coke total mass in the particle total mass of more than 40mm, particle diameter is 92% of coke total mass in the particle total mass of more than 25mm.
Embodiment 10
(1) brown coal pulverized and be mixed to form low-rank coal raw material with auxiliary agent, for subsequent use;
(2) adopt tamping machine to make firm by ramming shaping to 1/3 coking coal pulverized, form non-low-rank coal moulded coal layer; And on non-low-rank coal moulded coal layer, continue to add described low-rank coal raw material continue to adopt tamping machine to make firm by ramming shaping to described low-rank coal raw material, form the low-rank coal moulded coal layer be positioned at above described non-low-rank coal moulded coal layer, thus form final moulded coal raw material; Wherein, in mass, auxiliary agent add the 30wt% that quality is brown coal quality, the add-on of described brown coal is the 60wt% of described moulded coal raw materials quality, and the G value of described brown coal is 20, and volatile content is 55%, described auxiliary agent is the hard pitch of softening temperature 150 DEG C, described hard pitch 850 DEG C of isolated air destructive distillation weightlessness 30%, fixed carbon content 30%, ratio of carbon-hydrogen 8;
(3) moulded coal raw material pushed in coke oven carry out upgrading, control upgrading temperature 950 DEG C, 24 hours upgrading time, collect overflow raw gas, tar, crude benzol mixture, obtain byproduct coke simultaneously;
Adopt common process to be separated raw gas, tar, and from tar, be separated crude benzol further, the amount of the described raw gas obtained is 400Nm
3/ t dry coal, the amount of described tar is 48kg/t dry coal, and the amount of described byproduct coke is 635kg/t dry coal, and the amount of described crude benzol is 17kg/t dry coal.Described coke comprises the low-rank coal coke of the low-rank coal moulded coal layer generation formed by layering after coke oven release coke and the non-low-rank coal coke of non-low order coal seam generation, in mass, in described low-rank coal coke, solids carbon content is not less than 72%, volatile content is not more than 4%, after coke screening, particle diameter is 20% of coke total mass in the particle total mass of more than 40mm, particle diameter is 55% of coke total mass in the particle total mass of more than 25mm, in the non-low-rank coal coke that described non-low-rank coal produces, solids carbon content is not less than 82%, volatile content is not more than 5%, after coke screening, particle diameter is 81% of coke total mass in the particle total mass of more than 40mm, particle diameter is 92% of coke total mass in the particle total mass of more than 25mm.
Comparative example 1
(1) adopt tamping machine to make firm by ramming shaping to 1/3 coking coal pulverized, form non-low-rank coal moulded coal layer; And on non-low-rank coal moulded coal layer, continue to add the low-rank coal raw material that described brown coal and auxiliary agent formed continue to adopt tamping machine to make firm by ramming shaping to described low-rank coal raw material, form the low-rank coal moulded coal layer be positioned at above described non-low-rank coal moulded coal layer, thus form final moulded coal raw material; Wherein, the add-on of described brown coal is the 60wt% of described moulded coal raw materials quality, and the G value of described brown coal is 20, and volatile content is 55%, and described auxiliary agent is the bituminous matter that softening temperature is greater than 80 DEG C, and described bituminous matter is 850 DEG C of isolated air destructive distillation weightlessness 60%;
(2) moulded coal raw material pushed in coke oven carry out upgrading, control upgrading temperature 950 DEG C, 24 hours upgrading time, collect overflow raw gas, tar, crude benzol mixture, obtain byproduct coke simultaneously;
Adopt common process to be separated raw gas, tar, and from tar, be separated crude benzol further, the amount of the described raw gas obtained is 320Nm
3/ t dry coal, the amount of described tar is 44kg/t dry coal, and the amount of described byproduct coke is 870kg/t dry coal, and the amount of described crude benzol is 18kg/t dry coal.Described coke comprises the low-rank coal coke of the low-rank coal moulded coal layer generation formed by layering after coke oven release coke and the non-low-rank coal coke of non-low order coal seam generation, in mass, in described low-rank coal coke, solids carbon content is not less than 55%, volatile content is not more than 4%, after coke screening, particle diameter is 15% of coke total mass in the particle total mass of more than 40mm, particle diameter is 55% of coke total mass in the particle total mass of more than 25mm, in the non-low-rank coal coke that described non-low-rank coal produces, solids carbon content is not less than 82%, volatile content is not more than 5%, after coke screening, particle diameter is 70% of coke total mass in the particle total mass of more than 40mm, particle diameter is 86% of coke total mass in the particle total mass of more than 25mm.
Obviously, above-described embodiment is only for clearly example being described, and the restriction not to embodiment.For those of ordinary skill in the field, can also make other changes in different forms on the basis of the above description.Here exhaustive without the need to also giving all embodiments.And thus the apparent change of extending out or variation be still among the protection domain of the invention.
Claims (9)
1. be applicable to a moulded coal raw material for coking process, it is characterized in that,
Comprise the low-rank coal moulded coal layer of low-rank coal and auxiliary agent formation, described auxiliary agent is the organic binder bonds being less than 50% 850 DEG C of isolated air destructive distillation weightlessness;
Also comprise one or more the non-low-rank coal moulded coal layers formed in scala media coal, high-order coal or middle high-order coal, described low-rank coal moulded coal layer is arranged on described non-low-rank coal moulded coal layer, in mass, the add-on of described low-rank coal is the 50-80wt% of described moulded coal raw materials quality.
2. the moulded coal raw material being applicable to coking process according to claim 1, is characterized in that, described organic binder bond is the bituminous matter that softening temperature is greater than 100 DEG C.
3. the moulded coal raw material being applicable to coking process according to claim 1 and 2, is characterized in that, described auxiliary agent is coal-tar pitch or petroleum pitch, and its softening temperature is not less than 120 DEG C.
4. the moulded coal raw material being applicable to coking process according to claim 3, is characterized in that, the softening temperature of described pitch is not less than 140 DEG C.
5. the moulded coal raw material being applicable to coking process according to claim 3, is characterized in that, described pitch is hard pitch, and in mass, the fixed carbon content of described hard pitch is more than 25%, and ratio of carbon-hydrogen is 8-11.
6., according to the arbitrary described moulded coal raw material being applicable to coking process of claim 1-5, it is characterized in that, in mass, the add-on of described auxiliary agent is the 5-40wt% of described low-rank coal quality.
7. the moulded coal raw material being applicable to coking process according to claim 6, is characterized in that, in mass, the add-on of described auxiliary agent is the 10-30wt% of described low-rank coal quality.
8., according to the arbitrary described moulded coal raw material being applicable to coking process of claim 1-7, it is characterized in that, in mass, the add-on of described low-rank coal is the 50-60wt% of described moulded coal raw materials quality.
9., according to the arbitrary described moulded coal raw material being applicable to coking process of claim 1-8, it is characterized in that, the G value of described low-rank coal is less than 50, and volatile content is greater than 40%.
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| CN106929044A (en) * | 2015-12-30 | 2017-07-07 | 北京三聚环保新材料股份有限公司 | A kind of process for upgrading of the moulded coal raw material containing low-order coal and particulate matter |
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