CN1252392A - Technological process and subsidiary equipment for cement production in vertical kiln with directly added garbage - Google Patents
Technological process and subsidiary equipment for cement production in vertical kiln with directly added garbage Download PDFInfo
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- CN1252392A CN1252392A CN99123056A CN99123056A CN1252392A CN 1252392 A CN1252392 A CN 1252392A CN 99123056 A CN99123056 A CN 99123056A CN 99123056 A CN99123056 A CN 99123056A CN 1252392 A CN1252392 A CN 1252392A
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B28/00—Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements
- C04B28/02—Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements containing hydraulic cements other than calcium sulfates
- C04B28/021—Ash cements, e.g. fly ash cements ; Cements based on incineration residues, e.g. alkali-activated slags from waste incineration ; Kiln dust cements
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B20/00—Use of materials as fillers for mortars, concrete or artificial stone according to more than one of groups C04B14/00 - C04B18/00 and characterised by shape or grain distribution; Treatment of materials according to more than one of the groups C04B14/00 - C04B18/00 specially adapted to enhance their filling properties in mortars, concrete or artificial stone; Expanding or defibrillating materials
- C04B20/02—Treatment
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B7/00—Hydraulic cements
- C04B7/24—Cements from oil shales, residues or waste other than slag
- C04B7/243—Mixtures thereof with activators or composition-correcting additives, e.g. mixtures of fly ash and alkali activators
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/10—Production of cement, e.g. improving or optimising the production methods; Cement grinding
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/91—Use of waste materials as fillers for mortars or concrete
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The present invention has the main feature that the cement producing equipment has a garbage treating system, and the treated garbage together with industrial waste residue, limestone, low-grade coal, etc. is baked in a vertical kiln into cement clinker, which is further pulverized together with industria waste residues into cement. Compared with available technology, the present invention can reduce the secondary pollution of harmful gas produced in garbage incineration and utilize the inflammable matter in garbage to reduce fuel consumption. In addition, the lowered baking temperature can lower power consumption and adding large amound of industrial waste residues can save mineral resource.
Description
The present invention relates to a kind of Cement Production Technology, particularly utilize rubbish to produce the processing method and the optional equipment of cement as basic raw material.
Municipal wastes is a kind of waste of contaminate environment, and a large amount of rubbish are piled up as refuse, land occupation, contaminate environment, causes public hazards.For solving the recycling problem of rubbish, some countries have studied and have utilized garbage waste as the new technology of producing cement raw material in recent years.For example, New Energy and Industrial Technology Development Organization and Japanese Pacific Ocean company unite the ashes behind the municipal refuse incineration of utilizing of invention, water drain pollutent and natural limestone are blended in the rotary kiln to be fired, and the solid that burns till and gypsum is together pulverized to grind and make the technology of cement again.But there is the problem of the following aspects in this technology:
1, rubbish produces toxic and harmful when burning into ashes, still causes a large amount of atmospheric pollutions, is unfavorable for environment protection.
2, there are some combustiblesubstances in the rubbish, wasted effective combustiblesubstance energy after the burning.
3, fire production rubbish cement with rotary kiln, owing to contain chlorion in the rubbish, the structural performance of rotary kiln is limit in addition, therefore when firing temperature does not reach sintering temperature as yet, will produce alkali chloride, cause the ring formation skinning in the kiln and be prone to the obstruction accident, bring very big difficulty to production.In addition, use rotary kiln, the one, the investment of putting up a kiln is big, and the 2nd, burn till the fuel fat coal.Fuel consumption is big, thereby cost is increased.
The objective of the invention is to provide at the deficiency of prior art a kind of processing method and utility appliance of cement production in vertical kiln with directly added garbage, it makes rubbish without burning, directly mixes in the making of producing cement.
For realizing that the technical scheme that purpose of the present invention is taked is: adopt the mechanized cement shaft kiln production line to fire rubbish cement.For being changed into, garbage raw material meets the cement slurry that cement is made, in the technical process of producing cement raw equipment, set up refuse disposal system, by this system rubbish is carried out fragmentation, sterilization, deironing, classification separates, in small, broken bits, after oven dry etc. are handled, become particulate state drying garbage material, again with industrial residue, it is suitable that material such as Wingdale or carbide slag is prepared into composition, evenly, stable rubbish cement slurry, the mode of concrete preparation raw material is: rubbish after will handling (component 1) and industrial residue (component 2), Wingdale or carbide slag (component 3), low grade coal (component 4) carries out mixing match, and the proportioning component is: component 1: component 2: component 3: component 4=1: 0.3: 3.7: 0.5.The rubbish cement slurry that proportioning is good is sent into grinding machine, stir homogenizing storehouse and carry out grinding, stir, all change into meet the calcination of cement clinker requirement Chemical Composition promptly: CaO qualification rate＞80% in the raw material, can reach requirement into the kiln cement raw meal quality, the rubbish cement slurry that to go into kiln again is prefabricated into pellet, send in the mechanized cement shaft kiln and calcine, its calcining temperature is controlled at 1300C °～1400C °, than 100C ° of the temperature reduction of firing Portland cement～150C °, rubbish cement clinker after the calcining is got 50～70%, mix 25～45% industrial residue, add 5% retardant again, send in the chamotte powder grinding machine, be ground to finished cement.
Make raw material production cement with rubbish, have early strong, high-strength, coagulate property soon, thereby can mix a large amount of industrial residues, wherein, in the proportioning of cement slurry, the industrial residue that mixes can adopt sulfate slag, carbide slag, phosphogypsum, boiling slag, flyash cinder etc.In the proportioning of cement clinker, the industrial residue that mixes can adopt boiling slag, powdered coal cinder, slag, ironmaking slag etc., phosphogypsum, fluorgypsum in the also available industrial residue made retardant simultaneously, or adopts the spent pulping liquor of paper industry to make retardant, and the effect of playing grinding aid is arranged.Improve cement character thereby reach, improve the unusual effect of cement quality and reduction cement grinding power consumption.In addition, the chlorion that contains in the rubbish, most of chlorion can form the cement clinker mineralizer in the firing of shaft kiln, and another part chlorion returns again in the shaft kiln after handling with waste-gas cleaning, can reduce environmental pollution.
In the equipment of producing rubbish cement, additional refuse disposal system is made up of scrap heap canopy, bridge-type grab, roller path, crusher, conveyor, tramp iron separator, Sterilizers, rubbish material separating machine, knife mill, dryer, lift, storage warehouse.Various type equipment in the system are all arranged by the requirement of refuse treatment operation and are put, and assemble together, it is as follows that it assembles mode: the bottom of roller path is connected with the fines storehouse, the direction of motion end connects the coarse breaking machine, lower position in coarse breaking machine and particle storehouse is provided with conveyor, the delivery end of this machine leads to the rubbish material separating machine, and the bottom of separating machine is provided with conveyor and the fine crushing machine that different material is carried.One of them conveyor connects dryer, be used for the material that separated transmission is come is dried, and it is stand-by to storage warehouse to deliver to chain bucket.Be that isolated flammable light material is sent into knife mill on another conveyor, and it is standby to storage warehouse through the conveyor of knife mill below setting the material of chopping to be delivered to chain bucket.Be equipped with guard shield on transfer roller and conveyor, guard shield is made with transparent material, also can adopt the sheet iron material.Wherein transfer roller is provided with the arch form support with the conveyor guard shield that is positioned at this machine lower position, is fixed with Sterilizers and tramp iron separator on it respectively.The guard shield place at this position adopts the movably connected of window switching, can regularly draw back the guard shield at this place, in order to remove the ferrous metal thing on the tramp iron separator and to change Sterilizers.
Making raw material production cement with rubbish, is that main chemical is CaO, SiO owing to contain multiple inorganic compositions such as stone, glass, ceramic tile, slag, dirt in the rubbish
2, AL
2O
3, Ft
2O
3, MgO etc., these compositions all are required compositions in the cement raw material.Therefore, the depleted refuse reclamation is utilized, turned waste into wealth, the protection environment has sizable economic worth and social benefit.Produce rubbish cement according to technique scheme, the advantage of its invention and beneficial effect have following some:
(1) in the present invention, rubbish need not burn in advance, in the time of can reducing waste incineration, produces the secondary pollution of toxic and harmful.
(2) cement raw material adopts pollutents such as rubbish, industrial residue, low grade coal, industrial effluent, can make full use of the Mineral resources that the refuse material replaces resource-constrained, as with the ardealite instead plaster of paris in the industrial residue etc., can save a large amount of natural resourcess.
(3) use the vertical kiln with directly added garbage cement baking, harmful poisonous gas and heavy metal in the rubbish, as carcinogenss such as chromium, lead, can at high temperature participate in forming the cement clinker mineral reaction, and in the machine shaft kiln, absorbed by CaO and other mineral, can form yellow ultramarine, chromium Calucium Silicate powder, chromium calcium aluminate etc., the useful harmless mineral of these generations are fixed in the cement clinker, can avoid secondary pollution.
(4) in the sintering procedure of shaft kiln, pellet in kiln oven dry, preheating and be heated to the required heat of firing temperature, a part produces from contained fuel spontaneous combustion in the rubbish, another part is to fire fuel by the low grade coal that mixes in the raw material, not only made full use of the combustible material in the rubbish, but also can reduce mark coal consumption more than 5%, and the quantity discharged of CO, power consumption and fat coal saved.
(5) replace rotary kiln with the machine shaft kiln and fire rubbish cement, less investment, it is fast to go into operation, and the investment of putting up a kiln of its machine shaft kiln only is 1/4 of a rotary kiln, can save the investment of putting up a kiln, and reduces cost.
Utilize accompanying drawing to further describe embodiments of the invention below.
Fig. 1 is a refuse disposal system synoptic diagram among the present invention;
Fig. 2 is a rubbish material separator structure synoptic diagram among Fig. 1;
Referring to Fig. 1, in the equipment of producing rubbish cement, except that the required various device line of production technology of original production Portland cement, mainly be to have set up refuse disposal system.This system comprises: scrap heap canopy 1, bridge-type grab 2, roller path 3, coarse breaking machine 4, conveyor 5,8,9,12, tramp iron separator 3a, 5a, Sterilizers 5b, rubbish material separating machine 6, fine crushing machine 7, knife mill 10, dryer 11, chain bucket 13, storage warehouse 14.
Various type equipment in the system, all the arrangement requirement by the refuse treatment operation assembles together on the layout of technical process, specifically assemble the processing method of mode and cement production in vertical kiln with directly added garbage, all implement by the described step of the technical scheme among the present invention.In addition, in the auxilliary refuse disposal system that adds, except that the rubbish material separating machine is new texture designed among the present invention, all the other types and parts all belong to the known equipment that can purchase on the market, its structure repeats no more, and comprises that the processing method of original known machine shaft kiln cement production line and device structure also repeat no more.
According to shown in Figure 1, in the treating processes of rubbish, rubbish is layouted by bridge-type grab 2 in scrap heap canopy 1 and is got material and send into one group of roller path 3 that the gap is uniform, bulk rubbish is gone in the coarse breaking machine 4 after tramp iron separator 3a deironing along the inclined-plane by transfer roller 3, the slit of more broken fines through between roller gone among the rubbish particle storehouse 3b, through primary dcreening operation and just broken material by conveyor 5 after Sterilizers 5b tramp iron separator 5a sterilization deironing, send into rubbish material separating machine 6, by separating machine rubbish material is separated into fines, piece material and light-duty material such as waste paper, useless mould etc., the piece material is after 7 fragmentations of fine crushing machine, send in the dryer 10 by conveyor 8 together with fines and to dry moisture content, waste paper, useless moulding after knife mill 9 choppings, it is standby to send into storage warehouse through chain bucket by conveyor 12 together with the drying garbage material after drying.Be the too high power loss that causes of combustible material temperature in drying course that prevents to contain in the rubbish, its bake out temperature can be controlled by the thermosistor on the dryer, in case of necessity, can carry out oven drying at low temperature, and the rubbish material that oven dry is come out is a particulate state drying garbage material.Number in the figure 11a, 11b are original cleaner and electric precipitator on the dryer.In the present invention, be equipped with guard shield on transfer roller 3 and each conveyor, guard shield preferably adopts transparent material to make, and can see the situation of rubbish material in transport process clearly.Be equipped with in the guard shield of hauler 3 and conveyor 5 on the arch form support (not shown) frame and by fastening piece tramp iron separator 3a, 5a and Sterilizers 5b be housed, tramp iron separator adopts electro-magnet or magnet; Sterilizers can adopt spraying type, by being contained in the fog-spray nozzle on the arch form support and forming by the Herb of Common violet flow container of hose connection outside storing.
Referring to Fig. 2, the rubbish material separating machine is by the body 61 of accepting rubbish material, a roto-sifter 62 that is positioned at body 61 with the rubbish screening and separating, main exhaust fan 69, accessory fan 63, dust-precipitator 64, motor 70 is formed, wherein, be provided with particle I chamber in the body 61, piece material II chamber, light-duty material, waste paper, the useless III that moulds, the IV chamber, one end of body is equipped with the accessory fan 63 that is used to dispel separation of material, top drives by motor 70 can be around the roto-sifter 62 of its rotating shaft rotation, the other end is equipped with the cyclone type dust-precipitator 64 that is used to receive dust, the top of dust-precipitator connects main exhaust fan 69 and exhaust duct 65 by bend pipe 64a, the sidewall of exhaust duct 65 is equipped with blowback tracheae 67 and leads to blowback air chamber 68, purge gas is by air valve 66 controls that are provided with on the pipeline, the comb pipe 68a that band pore row shape is put is housed in the blowback air chamber 68, and the pipe 68a that combs stretches in body and is positioned at light-duty material III, the top of IV chamber, I, II, III, the bottom of IV chamber and dust-precipitator is the funnel type of downward contraction.In the rubbish sepn process, rubbish is entered in the roto-sifter 62 of separating machine by the conveyor transmission, part disentegrated particles sifts and enters particle I chamber, block material enters piece material II chamber by the roto-sifter outlet, under the effect of main exhaust fan 69 and accessory fan 63, gas constantly blows in the body by an end of body, and undersized material dispelled, dust is blown into dust-precipitator 64, light material floats into III, the IV chamber, waste paper, useless mould the sheet material and be blocked in or be adjacent on the comb pipe 68a of blowback air chamber, by the air valve 66 on the time opening blowback tracheae, make the aperture of purge gas on the pipe 68a that combs it be gone up the stationery or other dirt settling that adsorb and blow off to III, IV is indoor, and the supply of purge gas is to be supplied with by main exhaust fan 69, by regulating the air quantity of main exhaust fan, can regulate gas velocity in the body 1, make the weight feed separation, can in dust chamber, form whirlwind simultaneously, in order to the dust separation sedimentation in the gas, clean wind enters atmosphere by exhaust duct 65.
Claims (5)
1, a kind of processing method of cement production in vertical kiln with directly added garbage is characterized in that: it comprises following step:
(1) processing of rubbish: municipal wastes sent into carry out in the additional refuse disposal system among the present invention that fragmentation, sterilization, deironing, classification separate, after in small, broken bits, oven dry etc. handles, become particulate state drying garbage material;
(2) proportioning of rubbish cement slurry: drying garbage material (component 1) is become the rubbish cement slurry with industrial residue (component 2), Wingdale or carbide slag (component 3), low grade coal (component 4) mixing match, and its proportioning component is: component 1: component 2: component 3: component 4=1: 0.3: 3.7: 0.5;
(3) the suitable rubbish cement slurry of preparation composition: the rubbish cement slurry of proportioning is sent into grinding machine, after the stirring homogenizing storehouse is carried out grinding, stirring, homogenizing, make Chemical Composition CaO qualification rate＞80% in its raw material, reach requirement into the kiln cement raw meal quality;
(4) the rubbish cement slurry is prefabricated into pellet, sends in the mechanized cement shaft kiln and calcine, its firing temperature is controlled at 1300C °～1400C °, is sintered into the rubbish cement clinker;
(5) get rubbish cement clinker 50～70%, mix 25～45% industrial residue, and add 5% the slow agent of coagulating, send in the chamotte powder grinding machine grinding to finished cement.
2, the processing method of cement production in vertical kiln with directly added garbage according to claim 1 is characterized in that: the industrial residue in the described cement slurry proportioning adopts sulfate slag, carbide slag, phosphogypsum, boiling slag, flyash cinder etc.; Industrial residue in the cement clinker proportioning adopts boiling slag, flyash cinder, slag, ironmaking slag etc.; Retardant can adopt industrial residues such as phosphogypsum, fluorgypsum, also can adopt the spent pulping liquor of paper industry.
3, a kind of optional equipment of processing method of cement production in vertical kiln with directly added garbage as claimed in claim 1, it is characterized in that: in the technical process of producing the cement existing equipment, set up refuse disposal system, this system is by scrap heap canopy (1), bridge-type grab (2), roller path (3), slightly, fine crushing machine (4,7), conveyor (5,8,9,12), Sterilizers (5b), tramp iron separator (3a, 5a), rubbish material separating machine (6), knife mill (10), dryer (11), chapelet (13), storage warehouse (14) is formed, each machine in the system assembles according to the refuse treatment process flow respectively, wherein, the bottom of roller path (3) is connected with particle storehouse (3b), the direction of motion end connects coarse breaking machine (4), belt conveyor (5) is arranged on the lower position of coarse breaking machine (4) and particle storehouse (3b), conveyor (5) delivery end leads to rubbish material separating machine (6), the bottom of separating machine is provided with two conveyors (8,9) and fine crushing machine (7), conveyor (9) connects dryer (11), conveyor (8) leads to knife mill (10), and the below of knife mill is provided with conveyor (12).The delivery end of this machine leads to chain bucket (13).
4, the optional equipment of cement production in vertical kiln with directly added garbage according to claim 2, it is characterized in that: transfer roller (3), conveyor all are equipped with guard shield on (5,8,9,12), guard shield can be made with transparent material or sheet iron, wherein, in transfer roller 3, conveyor 5 guard shields, be provided with the arch form support, be fixed with tramp iron separator (3a, 5a) and Sterilizers (5b) on it respectively, the guard shield at this position adopts the movably connected of window switching.
5, the optional equipment of cement production in vertical kiln with directly added garbage according to claim 2, it is characterized in that: rubbish material separating machine (6) is by body (61), roto-sifter (62), accessory fan (63), main exhaust fan (69), dust-precipitator (64), motor (70) is formed, be provided with particle I chamber in the body (61), piece material II chamber, light paper, material III such as mould, the IV chamber, the bottom of each chamber and dust-precipitator (64) is the doline of shrinking downwards, one end of body (61) is equipped with accessory fan (63), roto-sifter (62) is equipped with on top, the other end is equipped with dust-precipitator (64), its top connects main exhaust fan (69) and exhaust duct (65) by bend pipe (64a), the sidewall of exhaust duct (65) is equipped with blowback tracheae (67), one control air valve (66) is housed on the pipeline, this pipe leads to blowback air chamber (68), row's shape comb pipe (68a) of band pore is housed in the chamber, and the pipe (68a) of combing stretches in body and is positioned at light-duty material III, the top of IV chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN99123056A CN1091432C (en) | 1999-11-18 | 1999-11-18 | Technological process and subsidiary equipment for cement production in vertical kiln with directly added garbage |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN99123056A CN1091432C (en) | 1999-11-18 | 1999-11-18 | Technological process and subsidiary equipment for cement production in vertical kiln with directly added garbage |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1252392A true CN1252392A (en) | 2000-05-10 |
| CN1091432C CN1091432C (en) | 2002-09-25 |
Family
ID=5282766
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN99123056A Expired - Fee Related CN1091432C (en) | 1999-11-18 | 1999-11-18 | Technological process and subsidiary equipment for cement production in vertical kiln with directly added garbage |
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| Country | Link |
|---|---|
| CN (1) | CN1091432C (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1296305C (en) * | 2005-06-03 | 2007-01-24 | 郑维平 | Cement clinker using carbide slag as raw material and drying production process thereby |
| CN100339329C (en) * | 2006-03-17 | 2007-09-26 | 宜宾天原股份有限公司 | Cement clinker calcinated on vertical kiln using full calcium carbide slag to instead limestone and its preparation method |
| CN102753497A (en) * | 2009-12-28 | 2012-10-24 | 霍尔辛姆科技有限公司 | Method for recovering phosphorus-containing alternative fuels in cement production |
| CN103418484A (en) * | 2013-08-12 | 2013-12-04 | 江苏融达新材料股份有限公司 | Closed-loop feedback iron-selecting system for vertical mill |
| CN103739215A (en) * | 2014-01-10 | 2014-04-23 | 洛阳水泥工程设计研究院有限公司 | Technology for treating domestic garbage by use of cement clinker production line |
| CN110925771A (en) * | 2019-12-17 | 2020-03-27 | 江西南方锅炉股份有限公司 | Municipal refuse incinerator that anticorrosive ability is strong |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1311919C (en) * | 2004-12-17 | 2007-04-25 | 中材国际工程股份有限公司 | Method for inhibiting urban house refuse fermentation |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1122784A (en) * | 1994-11-11 | 1996-05-22 | 蒋里军 | Composite silicate cement and prodn. method and equipment thereof |
-
1999
- 1999-11-18 CN CN99123056A patent/CN1091432C/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1296305C (en) * | 2005-06-03 | 2007-01-24 | 郑维平 | Cement clinker using carbide slag as raw material and drying production process thereby |
| CN100339329C (en) * | 2006-03-17 | 2007-09-26 | 宜宾天原股份有限公司 | Cement clinker calcinated on vertical kiln using full calcium carbide slag to instead limestone and its preparation method |
| CN102753497A (en) * | 2009-12-28 | 2012-10-24 | 霍尔辛姆科技有限公司 | Method for recovering phosphorus-containing alternative fuels in cement production |
| CN102753497B (en) * | 2009-12-28 | 2016-07-13 | 霍尔辛姆科技有限公司 | The method utilizing phosphorous alternative fuel in manufacture of cement |
| CN103418484A (en) * | 2013-08-12 | 2013-12-04 | 江苏融达新材料股份有限公司 | Closed-loop feedback iron-selecting system for vertical mill |
| CN103739215A (en) * | 2014-01-10 | 2014-04-23 | 洛阳水泥工程设计研究院有限公司 | Technology for treating domestic garbage by use of cement clinker production line |
| CN103739215B (en) * | 2014-01-10 | 2015-09-30 | 洛阳建材建筑设计研究院有限公司 | A kind of technique utilizing cement clinker production line process domestic refuse |
| CN110925771A (en) * | 2019-12-17 | 2020-03-27 | 江西南方锅炉股份有限公司 | Municipal refuse incinerator that anticorrosive ability is strong |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1091432C (en) | 2002-09-25 |
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