CN106929059A - A kind of coking process of the molding mass containing low-order coal, biomass and rubbish - Google Patents
A kind of coking process of the molding mass containing low-order coal, biomass and rubbish Download PDFInfo
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- CN106929059A CN106929059A CN201511020467.3A CN201511020467A CN106929059A CN 106929059 A CN106929059 A CN 106929059A CN 201511020467 A CN201511020467 A CN 201511020467A CN 106929059 A CN106929059 A CN 106929059A
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- order coal
- biomass
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Classifications
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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
-
- 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
- C10B55/00—Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material
- C10B55/02—Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material with solid materials
-
- 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
- C10B57/045—Other carbonising or coking processes; Features of destructive distillation processes in general using charges of special composition containing mineral oils, bitumen, tar or the like or mixtures thereof
-
- 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
-
- 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
- C10B57/08—Non-mechanical pretreatment of the charge, e.g. desulfurization
- C10B57/10—Drying
Abstract
The invention provides a kind of coking process of the molding mass containing low-order coal, biomass and rubbish, including, low order coal dust, biomass powder and rubbish powder are mixed and particulate matter is pressed into, the particulate matter and auxiliary agent are mixed to form compound, the compound is carried out to be press-formed to obtain molding mass, coking treatment is carried out to the molding mass, raw gas, tar, crude benzol and coke is obtained；Wherein described auxiliary agent is the mixture of scala media coal, the mixture of scala media coal and low-order coal, organic binder bond or organic binder bond and low-order coal.Coking process of the invention can not only reduce the cost of material of oil gas and coke product, can also effectively realize the recycling of biomass and rubbish so that the existing considerable economic benefit of technique of the invention has certain social benefit again.Coking process of the invention had both solved the problems, such as prior art because being limited biomass, spam application in the absence of large-scale industrialization equipment, overcame that existing tamping coke furnace availability is low, coking industry production capacity surplus problem again.
Description
Technical field
The present invention relates to the production field of Jiao of gasifying, more particularly to it is a kind of containing low-order coal, biomass and
The coking process of the molding mass of rubbish.
Background technology
Since 18th century, coal has turned into one of widely used energy of human world, with regard to China
Energy consumption structure for, current coal occupies 70% or so, is the national main energy sources depended on for existence.
According to the difference of structure and composition, coal is divided into lignite, bituminous coal and anthracite three major types, its metabituminous coal
It is divided into lower-grade metamorphic bituminous and mesometamorphism bituminous coal again, lower-grade metamorphic bituminous also referred to as ub-bituminous coal, itself and lignite one
Rise and be referred to as " low-order coal ".According to statistics, the reserves of China's low-order coal account for national explored coal reserves
More than 55%, up to 561,200,000,000 tons, but because low-order coal is used as the product at incoalation initial stage,
With phosphorus content it is low, moisture is high, easy efflorescence, easy spontaneous combustion, fugitive constituent high, immersion intensity difference, anti-dropping
The features such as intensity difference, thus the serious direct exploitation for limiting low-order coal, this undoubtedly causes huge
The big wasting of resources.In addition, increasingly increase and high-quality coal stock number with domestic energy demand
Fall sharply, the upgrading conversion of low-order coal already turns into current China's energy research with comprehensive utilization with exploitation
Major fields.
So far, the Upgrading Processes both at home and abroad for low-order coal are broadly divided into pyrolysis upgrading skill
Art, non-evaporating dehydrolysis upgrading technology and shaping upgrading technology three major types, wherein, for shaping upgrading skill
For art, in forming process, the physical action such as high pressure or shearing is to its gel structure and hole for low-order coal
Slot sytem generates irreversible destruction, it is thus possible to inherently lifts the coal rank of low-order coal, makes it
Degree of coalification is also improved therewith, so as to the dust for solving drying low-order coal is big, easily water suction, easily again
In deficiencies such as spontaneous combustions.But current low-order coal upgrading technology is in experimental study and engineering initially should
With the stage, the equipment in the absence of its heavy industrialization application is made thus limit the exploitation of low-order coal
Utilize.
Biomass energy is that green plants converts solar energy into chemical energy and is stored in the energy inside biomass
Amount, i.e., the form of energy with biomass as carrier, it is directly or indirectly from the light of green plants
Cooperation is used, and can be converted into conventional solid-state, liquid and fuel gas, inexhaustible, nexhaustible,
It is a kind of regenerative resource, while being also a kind of unique reproducible carbon source.The biology researched and developed in recent years
Matter curing molding technology changes traditional mode of biomass energy utilization, and loose biomass are converted into
Highdensity shaped fuel, directly burns or as gasification, liquefaction raw material, as biomass energy exploitation
A kind of effective way for utilizing, is also the effective ways for substituting conventional energy resource, Unfortunately, mesh
It is preceding not possess the equipment for making biomass fuel heavy industrialization application still.
China has the garbage compost work of current implementation for the recycling mode of house refuse at this stage
Skill and the garbage derivatived fuel technology studied, wherein for garbage derivatived fuel technology, though
The right technology has obtained commercial application in day, moral, Mei Deng developed countries, but because China is current
Do not possess the separate waste collection system of specification still, so foreign countries are for the sorting rubbish of component stabilization
Fuel manufacturing technology cannot be applied to the high humidity composting of China, therefore, the rubbish of China should be directed to
Rubbish reclaims present situation, and design research and development are adapted to the process for treating garbage as resource of China's national situation.
Tamping coke furnace be coal coking process in the maximization equipment that uses, its floor space is wide, investment
Capital cost is big.Coking of coal is to produce coke through high-temperature retorting by raw material of coal, while acquisition coal gas,
Coal tar simultaneously reclaims a kind of coal conversion process of other chemical products, and its coke product is mainly metallurgical coke
Or chemical industry is burnt.Because the quality requirements industrially to this kind of coke are very high so that production metallurgy is burnt or changes
The coal raw material that work Jiao is used is mainly coking coal, 1/3 coking coal, bottle coal, rich coal, lean coal, meager lean coal
Etc. coal, belong to mesometamorphism bituminous coal, but the shortage of coal resources in recent years, particularly for coking
The reduction of the middle high-quality coal raw material of industry so that the cost of material of coking industry is growing day by day, in addition
Steel, metallurgy etc. largely needed the decline of metallurgical coke or the burnt industry of chemical industry in recent years, caused coke to produce
The demand of product is reduced, price declines, so as to force coke-oven plant drastically to reduce coke output, thus band
Come consequence be tamping coke furnace out of service, once and coke oven disable will scrap, then in order to protect
Furnish a huge amount of money for the tamping coke furnace equipment invested to build, would have to be maintained in minimum level the operation of coke oven, this
Sample not only reduces the availability of tamping coke furnace, can also cause the production capacity surplus of coking industry.Therefore,
The coking industry for being on the verge of negative growth how is saved, the availability of tamping coke furnace is improved, coking industry is solved
The problem of production capacity surplus has turned into the bottleneck of current containment coking industry development.
In sum, how tamping coke furnace is applied to low-order coal, biology under current situation
The recycling field of matter and house refuse so that above mentioned problem is all readily solved, be puzzlement this
One technical barrier of art personnel.
The content of the invention
Present invention solves the technical problem that be overcome prior art cannot realize low-order coal, biomass and
The defect of the recycling of rubbish and the low problem of existing tamping coke furnace availability, and then provide one
Plant the coking process of the molding mass containing low-order coal, biomass and rubbish.
Therefore, the present invention realizes that the technical scheme of above-mentioned purpose is：
A kind of coking process of the molding mass containing low-order coal, biomass and rubbish, comprises the following steps：
(1) low-order coal dried, crushed, obtain low order coal dust；
(2) biomass dried, crushed, obtain biomass powder；
(3) combustiblerefuse and/or Compostable dried, crushed, obtain rubbish powder；
(4) by the low order coal dust, the biomass powder with the rubbish powder in mass ratio
(4-6)：(2-3)：(2-3) mixes, and is pressed into particulate matter；
(5) particulate matter and auxiliary agent are mixed to form compound, the compound is pressurizeed into
Type, obtains molding mass；
(6) coking treatment is carried out to the molding mass, it is 950-1050 DEG C, coking to control coking temperature
Time is not less than 16 hours, raw gas, tar and the crude benzol for overflowing is collected, while obtaining coke；
Wherein, the auxiliary agent be scala media coal, the mixture of scala media coal and low-order coal, organic binder bond or
The mixture of organic binder bond and low-order coal, the organic binder bond completely cuts off under air conditionses at 850 DEG C
Destructive distillation is weightless to be less than 50%.
In the particulate matter, the low order coal dust, the biomass powder and the rubbish powder
Mass ratio is 4:3:3, the moisture content of the low order coal dust is 13-17wt%, the biomass powder
Moisture content be less than 15wt%, the moisture content of the rubbish powder is less than 15wt%.
The addition of the particulate matter is the 10-70wt% of the molding mass quality, preferably 40-70wt%.
The density of the particulate matter is 1.2-1.4g/cm3。
The organic binder bond is one or more in bottom of towe oil, mink cell focus, residual oil or asphalitine.
The asphalitine is coal asphalt or petroleum asphalt of the softening point not less than 120 DEG C.
The auxiliary agent is scala media coal and low-order coal (5-8) in mass ratio:The mixture that (2-5) is formed；
Preferably, the auxiliary agent is scala media coal and low-order coal in mass ratio 7:3 mixtures for being formed.
The auxiliary agent is the organic binder bond and low-order coal (3-5) in mass ratio:(5-7) is formed
Mixture；
Preferably, the auxiliary agent is the organic binder bond and low-order coal in mass ratio 4:6 are formed
Mixture.
The G values of the low-order coal are more than 40% less than 50, volatile matter content.
The coking treatment is carried out in tamping coke furnace；The compound is carried out in tamping coke furnace
Make shaping firm by ramming.
Particulate matter in coking process of the present invention can be arbitrary shape, and its volume is not surpassing
Cross 25cm3It is advisable.
Above-mentioned technical proposal of the invention has the following advantages that：
1st, the coking process of the molding mass containing low-order coal, biomass and rubbish that the present invention is provided, leads to
Cross the mixture using scala media coal, scala media coal and low-order coal, the destructive distillation mistake under 850 DEG C of isolation air conditionses
The organic binder bond or the organic binder bond less than 50% are utilized with the mixture of low-order coal as auxiliary agent again
The particulate matter molding bonded that the caking property of above-mentioned auxiliary agent will be formed by low-order coal, biomass and rubbish,
On the one hand low-order coal, biomass and garbage raw material can be enable carries out high-temperature retorting in pushing tamping coke furnace,
On the other hand also cause that the solid product after low-order coal, biomass and rubbish destructive distillation is not pulverized easily, it is easy to
The coke pushing of tamping coke furnace, it is often more important that after above-mentioned auxiliary agent mixes with particulate matter, in auxiliary agent it is effective into
Point can promote the degraded at high temperature of high molecular polymer in low-order coal, biomass and rubbish, so that
The oil and gas production of low-order coal, biomass and garbage raw material is favorably improved, oil gas total amount is increased production 10%
More than.Also, auxiliary agent to be coated on the present invention outside of particulate matter by the effect of pressure so that
The liquid that grain thing is produced during high-temperature retorting can be penetrated into above-mentioned auxiliary agent, so contribute to carry
The quality of the coke that low-order and high-order coal, biomass and rubbish are produced.In summary, coking work of the invention
Skill can not only reduce the cost of material of oil gas and coke product, can also effectively realize biomass and rubbish
Recycling so that the existing considerable economic benefit of technique of the invention has certain society's effect again
Benefit.Thus, coking process of the invention to be not only solved and cannot realize low order existing for prior art
The problem that coal, biomass and garbage as resource are utilized, also effectively overcomes existing tamping coke furnace and utilizes
Low, coking industry production capacity surplus the problem of degree.
2nd, the coking process of the molding mass containing low-order coal, biomass and rubbish that the present invention is provided, excellent
The coal asphalt or petroleum asphalt comprising softening point not less than 120 DEG C in auxiliary agent is selected, low order can be so improved
The quality of the solid product-coke after coal, biomass and garbage raw material destructive distillation so that waving in coke
Hair point is not more than a 3-4%, so as to can be used to generating electricity, gas making and other chemical industry purposes.
Specific embodiment
Technical scheme will be clearly and completely described below, it is clear that described
Embodiment is a part of embodiment of the invention, rather than whole embodiments.Based in the present invention
Embodiment, it is all that those of ordinary skill in the art are obtained under the premise of creative work is not made
Other embodiment, belongs to the scope of protection of the invention.Additionally, invention described below is different
As long as involved technical characteristic does not constitute conflict and can just be combined with each other each other in implementation method.
Low-order coal composition in coking process of the present invention be applied to all of low-order coal coal or its
Mixture, scala media coal are applied to all of scala media coal coal or its mixture.For purposes of illustration only, following
By taking ub-bituminous coal or lignite as an example, the coal raw material of scala media coal is with 1/3 coking coal or fertilizer for low-order coal in embodiment
As a example by coal.For ease of comparing and illustrating, in following examples, wt% represents weight/mass percentage composition, shaping
The quality of the material=(matter of (quality of the quality+rubbish of low-order coal+biomass quality) × 85%+ auxiliary agents
Amount × 90%), " kg/t molding mass " refers to kilogram number, " Nm of the product that molding mass per ton is obtained3/ t into
Moulding mixture " refers to that the volume of the raw gas that molding mass per ton is obtained is converted into 25 DEG C, 1 normal atmosphere pressure
Cubic meter number.
Embodiment 1
(1) after being 15wt% to moisture content by the brown coal drying that G values are 0, volatile matter content is 42%,
Crush to obtain coal dust；
(2) stalk drying to moisture content is crushed into obtain fibrous straw powder less than after 15wt%；
(3) by combustiblerefuse drying to moisture content be 14wt% after, crush to obtain rubbish powder；
(4) by coal dust and fibrous straw powder, rubbish powder in mass ratio 4:3:3 ratio is mixed, gained
Mixture feeding hydraulic press in, pressurize 2min is obtained particulate matter under 20MPa, and its density is
1.2g/cm3, volume be 25cm3；
(5) it is 7 by mass ratio:3 particulate matter and 1/3 coking coal are mixed to form compound, using making firm by ramming
Equipment carries out making shaping firm by ramming to compound, the molding mass of rectangular-shape is obtained, in the inside of the molding mass
Particulate matter is embedded with surface so that the outside of each particulate matter is coated with 1/3 coking coal；
(6) will the molding mass push tamping coke furnace in carry out coking treatment, control the coking temperature to be
1050 DEG C, scorch time is 16 hours, raw gas, tar and the crude benzol for overflowing is collected, while obtaining
Byproduct coke.
The amount of the raw gas that the present embodiment is obtained is 470Nm3/ t molding mass, tar amount for 32kg/t into
Moulding mixture, the amount of crude benzol are 11kg/t molding mass, the amount of coke is 610kg/t molding mass, in mass,
Solids carbon content wherein in coke is not more than 3%, coke screening not less than 80%, volatile matter content
Afterwards particle diameter more than 40mm particle gross mass for coke gross mass 20%, particle diameter 25mm with
On particle gross mass for coke gross mass 40%.
Embodiment 2
(1) after being 13wt% to moisture content by the brown coal drying that G values are 0, volatile matter content is 45%,
Crush to obtain coal dust；
(2) by stalk drying to moisture content be 14wt% after, crush to obtain fibrous straw powder；
(3) combustiblerefuse drying to moisture content is crushed into obtain rubbish powder less than after 15wt%；
(4) by coal dust and fibrous straw powder, rubbish powder in mass ratio 5:3:2 ratio is mixed, gained
Mixture feeding hydraulic press in, pressurize 2min is obtained particulate matter under 18MPa, and its density is
1.3g/cm3, volume be 25cm3；
(5) it is 4 by mass ratio:6 particulate matter is mixed to form compound with auxiliary agent, using tamping machine
Compound is carried out to make shaping firm by ramming, the molding mass of rectangular-shape is obtained, in the inside of the molding mass and table
Face is embedded with particulate matter so that the outside of each particulate matter is coated with the auxiliary agent；
Wherein, the auxiliary agent is rich coal and ub-bituminous coal in mass ratio 7:The formed mixture of 3 mixing, institute
The G values of ub-bituminous coal are stated for 45, volatile matter content is more than 40%；
(6) will the molding mass push tamping coke furnace in carry out coking treatment, control the coking temperature to be
1025 DEG C, scorch time is 18 hours, raw gas, tar and the crude benzol for overflowing is collected, while obtaining
Byproduct coke.
The amount of the raw gas that the present embodiment is obtained is 460Nm3/ t molding mass, tar amount for 40kg/t into
Moulding mixture, the amount of crude benzol are 13kg/t molding mass, the amount of coke is 640kg/t molding mass, in mass,
Solids carbon content wherein in coke is not more than 3%, coke screening not less than 80%, volatile matter content
Afterwards particle diameter more than 40mm particle gross mass for coke gross mass 60%, particle diameter 25mm with
On particle gross mass for coke gross mass 85%.
Embodiment 3
(1) G values are 45, ub-bituminous coal drying to the moisture content that volatile matter content is 45% is 17wt%
Afterwards, coal dust is crushed to obtain；
(2) by stalk drying to moisture content be 14wt% after, crush to obtain fibrous straw powder；
(3) by Compostable drying to moisture content be 14wt% after, crush to obtain rubbish powder；
(4) by coal dust and fibrous straw powder, rubbish powder in mass ratio 5:2:3 ratio is mixed, gained
Mixture feeding hydraulic press in, pressurize 1min is obtained particulate matter under 20MPa, and its density is
1.4g/cm3, volume be 25cm3；
(5) it is 11 by mass ratio:9 particulate matter is mixed to form compound with organic binder bond, using smashing
It is fixed it is standby compound is carried out to make shaping firm by ramming, the molding mass of prepared rectangular-shape, in the molding mass
Portion and surface are embedded with particulate matter so that the outside of each particulate matter is coated with described organic viscous
Knot agent；
Wherein, the organic binder bond is weightless for 40% in 850 DEG C of destructive distillation completely cut off under air conditionses
Residual oil；
(6) will the molding mass push tamping coke furnace in carry out coking treatment, control the coking temperature to be
1000 DEG C, scorch time is 16 hours, raw gas, tar and the crude benzol for overflowing is collected, while obtaining
Byproduct coke.
The amount of the raw gas that the present embodiment is obtained is 480Nm3/ t molding mass, tar amount for 44kg/t into
Moulding mixture, the amount of crude benzol are 13kg/t molding mass, the amount of coke is 580kg/t molding mass, in mass,
Solids carbon content wherein in coke is not more than 3%, coke screening not less than 80%, volatile matter content
Afterwards particle diameter more than 40mm particle gross mass for coke gross mass 35%, particle diameter 25mm with
On particle gross mass for coke gross mass 60%.
Embodiment 4
(1) G values are 45, ub-bituminous coal drying to the moisture content that volatile matter content is 45% is 14wt%
Afterwards, coal dust is crushed to obtain；
(2) by stalk drying to moisture content be 13wt% after, crush to obtain fibrous straw powder；
(3) by Compostable drying to moisture content be 14wt% after, crush to obtain rubbish powder；
(4) by coal dust and fibrous straw powder, rubbish powder in mass ratio 6:2:2 ratio is mixed, gained
Mixture feeding hydraulic press in, pressurize 1.5min is obtained particulate matter under 19MPa, and its density is
1.2g/cm3, volume be 25cm3；
(5) it is 1 by mass ratio:9 particulate matter is mixed to form compound with auxiliary agent, using tamping machine
Compound is carried out to make shaping firm by ramming, the molding mass of rectangular-shape is obtained, in the inside of the molding mass and table
Face is embedded with particulate matter so that the outside of each particulate matter is coated with the auxiliary agent；
Wherein, the auxiliary agent is organic binder bond and ub-bituminous coal in mass ratio 4:The formed mixing of 6 mixing
Thing, the G values of the ub-bituminous coal are that 40, volatile matter content is 45%, and the organic binder bond is at 850 DEG C
Destructive distillation weightlessness under isolation air conditionses is 45% coal tar pitch, and its softening point is 120 DEG C；
(6) will the molding mass push tamping coke furnace in carry out coking treatment, control the coking temperature to be
950 DEG C, scorch time is 20 hours, raw gas, tar and the crude benzol for overflowing is collected, while obtaining
Byproduct coke.
The amount of the raw gas that the present embodiment is obtained is 500Nm3/ t molding mass, tar amount for 44kg/t into
Moulding mixture, the amount of crude benzol are 12kg/t molding mass, the amount of coke is 590kg/t molding mass, in mass,
Solids carbon content wherein in coke is not more than 3%, coke screening not less than 60%, volatile matter content
Afterwards particle diameter more than 40mm particle gross mass for coke gross mass 40%, particle diameter 25mm with
On particle gross mass for coke gross mass 60%.
Obviously, above-described embodiment is only intended to clearly illustrate example, and not to embodiment party
The restriction of formula.For those of ordinary skill in the field, may be used also on the basis of the above description
To make other changes in different forms.There is no need and unable to give all of implementation method
With exhaustion.And the obvious change thus extended out or change guarantor still in the invention
Among shield scope.
Claims (10)
1. a kind of coking process of the molding mass containing low-order coal, biomass and rubbish, including following step
Suddenly：
(1) low-order coal dried, crushed, obtain low order coal dust；
(2) biomass dried, crushed, obtain biomass powder；
(3) combustiblerefuse and/or Compostable dried, crushed, obtain rubbish powder；
(4) by the low order coal dust, the biomass powder with the rubbish powder in mass ratio
(4-6)：(2-3)：(2-3) mixes, and is pressed into particulate matter；
(5) particulate matter and auxiliary agent are mixed to form compound, the compound is pressurizeed into
Type, obtains molding mass；
(6) coking treatment is carried out to the molding mass, it is 950-1050 DEG C, coking to control coking temperature
Time is not less than 16 hours, raw gas, tar and the crude benzol for overflowing is collected, while obtaining coke；
Wherein, the auxiliary agent be scala media coal, the mixture of scala media coal and low-order coal, organic binder bond or
The mixture of organic binder bond and low-order coal, the organic binder bond completely cuts off under air conditionses at 850 DEG C
Destructive distillation is weightless to be less than 50%.
2. coking process according to claim 1, it is characterised in that in the particulate matter,
The low order coal dust, the biomass powder are 4 with the mass ratio of the rubbish powder:3:3；
The moisture content of the low order coal dust is 13-17wt%, and the moisture content of the biomass powder is less than
15wt%, the moisture content of the rubbish powder is less than 15wt%.
3. coking process according to claim 1 and 2, it is characterised in that the particulate matter
Addition is the 10-70wt% of the molding mass quality, preferably 40-70wt%.
4. the coking process according to claim any one of 1-3, it is characterised in that the particle
The density of thing is 1.2-1.4g/cm3。
5. the coking process according to claim any one of 1-4, it is characterised in that described organic
Binding agent is one or more in bottom of towe oil, mink cell focus, residual oil or asphalitine.
6. coking process according to claim 5, it is characterised in that the asphalitine is to soften
Coal asphalt or petroleum asphalt of the point not less than 120 DEG C.
7. the coking process according to claim any one of 1-6, it is characterised in that the auxiliary agent
It is scala media coal and low-order coal (5-8) in mass ratio:The mixture that (2-5) is formed；
Preferably, the auxiliary agent is scala media coal and low-order coal in mass ratio 7:3 mixtures for being formed.
8. the coking process according to claim any one of 1-6, it is characterised in that the auxiliary agent
It is the organic binder bond and low-order coal (3-5) in mass ratio:The mixture that (5-7) is formed；
Preferably, the auxiliary agent is the organic binder bond and low-order coal in mass ratio 4:6 are formed
Mixture.
9. the coking process according to claim any one of 1-8, it is characterised in that the low order
The G values of coal are more than 40% less than 50, volatile matter content.
10. the coking process according to claim any one of 1-9, it is characterised in that the coking
Treatment is carried out in tamping coke furnace；The compound carries out making shaping firm by ramming in tamping coke furnace.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN112625705A (en) * | 2020-11-08 | 2021-04-09 | 北京科技大学 | Method for disposing refuse derived fuel by coke oven and realizing gradient resource utilization of product |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101643656A (en) * | 2009-08-20 | 2010-02-10 | 韩大海 | Coke making method by adding biomass energy to mixed coal |
| CN104327873A (en) * | 2014-09-16 | 2015-02-04 | 北京三聚环保新材料股份有限公司 | Raw material for increasing quality of low-rank coal by present tamping coke oven |
-
2015
- 2015-12-30 CN CN201511020467.3A patent/CN106929059A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101643656A (en) * | 2009-08-20 | 2010-02-10 | 韩大海 | Coke making method by adding biomass energy to mixed coal |
| CN104327873A (en) * | 2014-09-16 | 2015-02-04 | 北京三聚环保新材料股份有限公司 | Raw material for increasing quality of low-rank coal by present tamping coke oven |
Non-Patent Citations (2)
| Title |
|---|
| 环境保护部办公厅: "《环境保护文件选编2010下册》", 30 September 2014, 中国环境出版社 * |
| 雷勇等: "废塑料与炼焦配煤共焦化产物的分析", 《废塑料与炼焦配煤共焦化产物的分析》 * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112625705A (en) * | 2020-11-08 | 2021-04-09 | 北京科技大学 | Method for disposing refuse derived fuel by coke oven and realizing gradient resource utilization of product |
| CN112625705B (en) * | 2020-11-08 | 2022-03-08 | 北京科技大学 | Method for disposing refuse derived fuel by coke oven and realizing gradient resource utilization of product |
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Application publication date: 20170707 |