CN107324743A - A kind of preparation method of steam-pressing brisk - Google Patents
A kind of preparation method of steam-pressing brisk Download PDFInfo
- Publication number
- CN107324743A CN107324743A CN201710424716.8A CN201710424716A CN107324743A CN 107324743 A CN107324743 A CN 107324743A CN 201710424716 A CN201710424716 A CN 201710424716A CN 107324743 A CN107324743 A CN 107324743A
- Authority
- CN
- China
- Prior art keywords
- steam
- parts
- pressing brisk
- preparation
- ageing
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- 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
- C04B28/14—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 calcium sulfate cements
-
- 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
- C04B40/00—Processes, in general, for influencing or modifying the properties of mortars, concrete or artificial stone compositions, e.g. their setting or hardening ability
- C04B40/02—Selection of the hardening environment
- C04B40/024—Steam hardening, e.g. in an autoclave
-
- E—FIXED CONSTRUCTIONS
- E04—BUILDING
- E04C—STRUCTURAL ELEMENTS; BUILDING MATERIALS
- E04C1/00—Building elements of block or other shape for the construction of parts of buildings
-
- 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
- C04B2201/00—Mortars, concrete or artificial stone characterised by specific physical values
- C04B2201/50—Mortars, concrete or artificial stone characterised by specific physical values for the mechanical strength
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Structural Engineering (AREA)
- Architecture (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Civil Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Treatment Of Sludge (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The present invention relates to a kind of preparation method of steam-pressing brisk, belong to construction material preparing technical field.The present invention first mixes oil plant second pond activated sludge and river sand etc., after plate and frame filter press filtration washing, ageing is mixed with biogas slurry, ageing wet feed is made, straw is successively stacked at sealing and fermenting in ceramic pot with ageing wet feed again, after being centrifuged, by the compounding such as lower sediment thing and quick lime, gypsum, adobe is pressed into after being handled using edge runner, after autoclave curing, coordinate natural curing, it is to avoid the steam-pressing brisk later stage shrinks, and produces steam-pressing brisk.Steam-pressing brisk resistance to compression and flexural capacity prepared by the present invention is strong, not easy to break, has broad application prospects.
Description
Technical field
The present invention relates to a kind of preparation method of steam-pressing brisk, belong to construction material preparing technical field.
Background technology
Building brick in the past is generally fired brick, and materials are difficult, complex manufacturing and high energy consumption, can be produced in production process
Raw pernicious gas, it is big to the potential pollution of air, clay brick is prohibitted the use of now, while strictly limitation fired brick project, furthermore,
Existing sintering brick process is poor to slurry dewatering effect, and moisture content is still higher after dehydration, and at least 80%, so in brickmaker
During the mixture of skill, mud cake is easily agglomerating, then is equipped with other traditional raw materials, the brick poor-performing being finally made, it is impossible to wide
It is general to be applied to the fields such as materials for wall, municipal works, revetment brick.Steam-pressing brisk is to utilize flyash, cinder, slag, slag, bastard coal
The industrial residues such as stone, mine tailings, residue of chemical industry or natural sand, tidal land mud etc.(The one or several kinds of above raw material)As gathering materials,
Added cement, lime etc. as cementitious matter, be equipped with additive it is compressing after, what is manufactured without high-temperature calcination is a kind of new
Materials for wall.
Existing steam-pressing brisk technology is main using flyash, gypsum or sand as raw material, and traditional steam-pressing brisk can be with according to raw material
It is divided into three series:Fly ash autoclaved brick, gypsum steam-pressing brisk and sand-lime steam-pressing brisk.Continually developing and opening up with flyash purposes
Exhibition, can increasingly go up as the high-quality fly ash price of steam-pressing brisk raw material;It is used as the accessory substance in the fields such as wet desulphurization, gypsum
Dewater treatment is not only needed, and the solubility of the main component calcium sulfate of gypsum is larger, easily causes brick body scum, it is soft that it meets water
The characteristic of change needs to spend very big cost to overcome;Sand as building primary raw material, with the prosperity of building trade, its price
Also high all the way, the cost pressure that autoclaved lime-sand brick manufacturer faces is gradually increased, while these three steam-pressing brisk mechanical strengths
It is poor with anti-pressure ability, the problem of easily cracking when in use, limit it and use scope.Therefore, it is urgent to find a kind of machinery
Intensity is high, and anti-pressure ability is strong, and the steam-pressing brisk of cracking phenomena is less prone in use.
The content of the invention
The technical problems to be solved by the invention are:Poor for traditional steam-pressing brisk mechanical strength, anti-pressure ability is weaker, leads
There is provided a kind of preparation method of steam-pressing brisk for the problem of causing easy cracking phenomenon during using.
In order to solve the above technical problems, the technical solution adopted by the present invention is:
(1)Count by weight, by 800~1000 parts of oil refinery waste water process second pond activated sludge, 200~300 parts of river sands,
100~120 parts of flyash, after 30~40 parts of plant ash are mixed with 3000~5000 parts of water stirrings, through press filtration, washing, ageing, are obtained
It is aged wet feed;
(2)It is soaked in water after straw is cut, obtains the short stalk of preprocessing straw, then by the short stalk of preprocessing straw with being aged wet feed successively
After laying, add water sealing and fermenting, then is centrifuged, and obtains lower sediment thing;
(3)Count by weight, by 60~80 parts of lower sediment things, 10~15 parts of quick limes, 6~8 parts of gypsum, 10~15 parts
Water, mixes rolling, obtains rolling material, then will be pressed into adobe after rolling material injection molding, through autoclave curing and natural curing, produces
Steam-pressing brisk.
Step(1)In described ageing process, can also add oil refinery waste water process second pond activated sludge quality 2~
4 times of biogas slurry.
Step(2)In described successively laying, every layer of laying depth of the short stalk of preprocessing straw is 3~5cm, and ageing wet feed is every
Layer laying depth is 3~5cm, and laying gross thickness is 35~45cm.
Step(2)The described sealing and fermenting time is 25~30 days.
Step(3)Described autoclave curing condition is:It it is 180~200 DEG C in temperature, pressure is in still kettle
8~12h of autoclave curing is carried out under the conditions of 1.3~1.6MPa.
Step(3)The described natural curing time is 28~30 days.
The present invention is compared with other method, and advantageous effects are:
(1)The present invention is first with the microorganism enriched in oil refinery waste water process second pond activated sludge cheap and easy to get and has
Machine matter nutrition, originates by inorganic salts of plant ash, in ageing process, is aided with biogas slurry, makes microorganism in activated sludge and biogas slurry
Activated, and be uniformly distributed in activated sludge, river sand and flyash, during sealed fermenting, the microorganism after activation
Make organic matter degradation in straw, and leave the straw muscle of relative difficult degradation, as the vascular bundle composition in straw stem, straw muscle is equal
It is even to be distributed in adobe, as reinforcement, during autoclave curing, as supporting construction in adobe, improve brick body
Mechanical strength and compression strength, it is to avoid brick body ftractures in use;
(2)The present invention is by the way that during the fermentation, degradable organic matter degradation is small molecule carbohydrate in raw material, is centrifuged
It is in afterwards in sediment, the adhesive property of product can be improved, while after fermented, active group increasing number in raw material makes original
It is more firm that material is combined, and during the fermentation, because of the corrosion function of microorganism, form hole supporting construction, effectively dropping
While low brick body density, the composition such as quick lime and gypsum can be penetrated into effectively inside pore structure, further improve brick body
Mechanical strength.
Embodiment
Weigh 800~1000g oil refinery waste water process second pond activated sludge successively first, 200~300g particle diameters are
0.25~0.35mm river sand, 100~120g flyash, 30~40g plant ash is poured into the batch mixer for filling 3~5L water, in
Temperature is 35~40 DEG C, and rotating speed is under the conditions of 800~1000r/min, constant temperature stirring mixes 3~5h;Treat constant temperature stirring mixing knot
Material in batch mixer, is delivered in plate and frame filter press and filtered by Shu Hou by delivery pump, and with 3~5L water washing plate and frame filter press
Middle material, then by the material discharging after washing into ageing tank, and addition 2~3L water and oil refinery waste water process into ageing tank
The biogas slurry of 2~4 times of second pond activated sludge quality, after 600~800r/min rotating speeds stirring mixing, 60~90min, stands old
Change 12~16h, separate except supernatant liquor, obtain lower floor's ageing wet feed;400~600g straw are weighed, clean 3 repeatedly with clear water~
After 5 times, length is cut into for the short stalks of 3~5cm, and the short stalk of gained is placed in water 3~5h of immersion, then the short stalk after immersion is taken
Go out, drain away the water, obtain the short stalk of preprocessing straw;It is to pre-process rice obtained by 3~5cm to lay a layer thickness in ceramic pot bottom even
The short stalk of grass, and be that 3~5cm lower floors are aged wet feed in the short evenly laid out a layer thickness in stalk surface of straw, and so on, one layer of straw
Short one layer of ageing wet feed of stalk is up added, until laying gross thickness reaches 35~45cm, then along ceramic top tank structure into ceramic pot
Clear water is added, until material in ceramic pot is flooded completely, is then placed ceramic pot sealing 25~30 days;Treat that ceramic pot is sealed
After placement terminates, material in ceramic pot is transferred to centrifuge, 15~20min is centrifuged with 6800~8800r/min rotating speeds, abandoned
Supernatant liquor is removed, lower sediment thing is collected;Count by weight, 60~80 parts of gained lower sediments are sequentially added in batch mixer
Thing, 10~15 parts of quick limes, 6~8 parts of gypsum, 10~15 parts of water, the stirring mixing 3 under the conditions of rotating speed is 600~800r/min
~5h, then material in batch mixer is transferred in edge runner, 10~15min of rolling obtains rolling material;Gained rolling material is evenly laid out
Moved into mould, then by mould in hydraulic press, compressing, the demoulding under the conditions of pressure is 18~24MPa obtains adobe, then
By gained adobe move into still kettle in, in temperature be 180~200 DEG C, pressure be 1.3~1.6MPa under the conditions of carry out high steam
8~12h is conserved, is discharged, natural curing 28~30 days, produce steam-pressing brisk under room temperature condition.
Example 1
Weigh 800g oil refinery waste water process second pond activated sludge successively first, 200g particle diameters are 0.25mm river sand, 100g
Flyash, 30g plant ash is poured into the batch mixer for filling 3L water, in temperature be 35 DEG C, it is permanent under the conditions of rotating speed is 800r/min
Temperature stirring mixing 3h;After constant temperature stirring mixing terminates, material in batch mixer is delivered in plate and frame filter press by delivery pump
Filtering, and with material in 3L water washing plate and frame filter press, then by the material discharging after washing into ageing tank, and into ageing tank
The biogas slurry of 2 times of 2L water and oil refinery waste water process second pond activated sludge quality is added, is stirred and mixed with 600r/min rotating speeds
After 60min, still aging 12h is separated except supernatant liquor, obtains lower floor's ageing wet feed;400g straw are weighed, it is repeatedly clear with clear water
Wash after 3 times, cut into length for the short stalks of 3cm, and the short stalk of gained is placed in water immersion 3h, then the short stalk after immersion is taken out,
Drain away the water, obtain the short stalk of preprocessing straw;It is short for preprocessing straw obtained by 3cm that a layer thickness is laid in ceramic pot bottom even
Stalk, and be that 3cm lower floors are aged wet feed in the short evenly laid out a layer thickness in stalk surface of straw, and so on, the short stalk one of one layer of straw
Layer ageing wet feed is up added, until laying gross thickness reaches 35cm, then clear water is added into ceramic pot along ceramic top tank structure, directly
To material in ceramic pot is flooded completely, then ceramic pot sealing is placed 25 days;After ceramic pot sealing placement terminates, it will make pottery
Material is transferred to centrifuge in porcelain jar, and 15min is centrifuged with 6800r/min rotating speeds, discards supernatant liquor, collects lower sediment
Thing;Count by weight, 60 parts of gained lower sediment things, 10 parts of quick limes, 6 parts of gypsum, 10 parts are sequentially added in batch mixer
Water, the stirring mixing 3h under the conditions of rotating speed is 600r/min, then material in batch mixer is transferred in edge runner, rolling 10min is obtained
Rolling material;Gained rolling material is evenly laid out in mould, then mould is moved into hydraulic press, under the conditions of pressure is 18MPa
Compressing, the demoulding obtains adobe, then gained adobe is moved into still kettle, is 180 DEG C in temperature, pressure is 1.3MPa conditions
Lower progress autoclave curing 8h, discharging, natural curing 28 days, produce steam-pressing brisk under room temperature condition.
Example 2
Weigh 1000g oil refinery waste water process second pond activated sludge successively first, 300g particle diameters are 0.35mm river sand, 120g
Flyash, 40g plant ash is poured into the batch mixer for filling 5L water, in temperature be 40 DEG C, it is permanent under the conditions of rotating speed is 1000r/min
Temperature stirring mixing 5h;After constant temperature stirring mixing terminates, material in batch mixer is delivered in plate and frame filter press by delivery pump
Filtering, and with material in 5L water washing plate and frame filter press, then by the material discharging after washing into ageing tank, and into ageing tank
The biogas slurry of 4 times of 3L water and oil refinery waste water process second pond activated sludge quality is added, is stirred and mixed with 800r/min rotating speeds
After 90min, still aging 16h is separated except supernatant liquor, obtains lower floor's ageing wet feed;600g straw are weighed, it is repeatedly clear with clear water
Wash after 5 times, cut into length for the short stalks of 5cm, and the short stalk of gained is placed in water immersion 5h, then the short stalk after immersion is taken out,
Drain away the water, obtain the short stalk of preprocessing straw;It is short for preprocessing straw obtained by 5cm that a layer thickness is laid in ceramic pot bottom even
Stalk, and be that 5cm lower floors are aged wet feed in the short evenly laid out a layer thickness in stalk surface of straw, and so on, the short stalk one of one layer of straw
Layer ageing wet feed is up added, until laying gross thickness reaches 45cm, then clear water is added into ceramic pot along ceramic top tank structure, directly
To material in ceramic pot is flooded completely, then ceramic pot sealing is placed 30 days;After ceramic pot sealing placement terminates, it will make pottery
Material is transferred to centrifuge in porcelain jar, and 20min is centrifuged with 8800r/min rotating speeds, discards supernatant liquor, collects lower sediment
Thing;Count by weight, 80 parts of gained lower sediment things, 15 parts of quick limes, 8 parts of gypsum, 15 parts are sequentially added in batch mixer
Water, the stirring mixing 5h under the conditions of rotating speed is 800r/min, then material in batch mixer is transferred in edge runner, rolling 15min is obtained
Rolling material;Gained rolling material is evenly laid out in mould, then mould is moved into hydraulic press, under the conditions of pressure is 24MPa
Compressing, the demoulding obtains adobe, then gained adobe is moved into still kettle, is 200 DEG C in temperature, pressure is 1.6MPa conditions
Lower progress autoclave curing 12h, discharging, natural curing 30 days, produce steam-pressing brisk under room temperature condition.
Example 3
Weigh 900g oil refinery waste water process second pond activated sludge successively first, 250g particle diameters are 0.30mm river sand, 110g
Flyash, 35g plant ash is poured into the batch mixer for filling 4L water, in temperature be 37 DEG C, it is permanent under the conditions of rotating speed is 900r/min
Temperature stirring mixing 4h;After constant temperature stirring mixing terminates, material in batch mixer is delivered in plate and frame filter press by delivery pump
Filtering, and with material in 4L water washing plate and frame filter press, then by the material discharging after washing into ageing tank, and into ageing tank
2L water is added, after 600r/min rotating speeds stirring mixing 60min, still aging 14h separates except supernatant liquor, obtains lower floor old
Dampness elimination material;500g straw are weighed, are cleaned repeatedly after 4 times with clear water, length are cut into for the short stalks of 4cm, and the short stalk of gained is placed in
4h is soaked in water, then the short stalk after immersion is taken out, drains away the water, obtains the short stalk of preprocessing straw;In ceramic pot bottom even paving
If a layer thickness is the short stalk of preprocessing straw obtained by 4cm, and is that 4cm lower floors are old in the short evenly laid out a layer thickness in stalk surface of straw
Dampness elimination material, and so on, one layer of straw, one layer of ageing wet feed of short stalk is up added, until laying gross thickness reaches 40cm, then edge
Ceramic top tank structure adds clear water into ceramic pot, until material in ceramic pot is flooded completely, then seals ceramic pot and places
27 days;After ceramic pot sealing placement terminates, material in ceramic pot is transferred to centrifuge, centrifuged with 7800r/min rotating speeds
17min, discards supernatant liquor, collects lower sediment thing;Count by weight, 70 parts of gained lower floors are sequentially added in batch mixer
Sediment, 13 parts of quick limes, 7 parts of gypsum, 12 parts of water, the stirring mixing 4h under the conditions of rotating speed is 700r/min, then by batch mixer
Middle material is transferred in edge runner, rolling 12min, obtains rolling material;Gained rolling material is evenly laid out in mould, then mould is moved
Enter in hydraulic press, compressing, the demoulding under the conditions of pressure is 22MPa obtains adobe, then gained adobe is moved into still kettle,
It it is 190 DEG C in temperature, pressure is progress autoclave curing 10h under the conditions of 1.4MPa, discharging is supported naturally under room temperature condition
Shield 29 days, produces steam-pressing brisk.
The steam-pressing brisk for taking example 1 to be prepared to example 3, to mechanical properties such as its intensity, frost resistances with reference to JC239-2001
《Flyash brick》Standard, it detects data such as table 1.
As can be seen from Table 1, the steam-pressing brisk compression strength and High anti bending strength that prepared by the present invention, and other physical properties are also high
In standard value, physical property is superior.
Claims (6)
1. a kind of preparation method of steam-pressing brisk, it is characterised in that specifically preparation process is:
(1)Count by weight, by 800~1000 parts of oil refinery waste water process second pond activated sludge, 200~300 parts of river sands,
100~120 parts of flyash, after 30~40 parts of plant ash are mixed with 3000~5000 parts of water stirrings, through press filtration, washing, ageing, are obtained
It is aged wet feed;
(2)It is soaked in water after straw is cut, obtains the short stalk of preprocessing straw, then by the short stalk of preprocessing straw with being aged wet feed successively
After laying, add water sealing and fermenting, then is centrifuged, and obtains lower sediment thing;
(3)Count by weight, by 60~80 parts of lower sediment things, 10~15 parts of quick limes, 6~8 parts of gypsum, 10~15 parts
Water, mixes rolling, obtains rolling material, then will be pressed into adobe after rolling material injection molding, through autoclave curing and natural curing, produces
Steam-pressing brisk.
2. a kind of preparation method of steam-pressing brisk according to claim 1, it is characterised in that:Step(1)Described ageing
Cheng Zhong, can also add the biogas slurry of 2~4 times of oil refinery waste water process second pond activated sludge quality.
3. a kind of preparation method of steam-pressing brisk according to claim 1, it is characterised in that:Step(2)Described successively paving
If in, every layer of laying depth of the short stalk of preprocessing straw is 3~5cm, and every layer of laying depth of ageing wet feed is 3~5cm, lays total thickness
Spend for 35~45cm.
4. a kind of preparation method of steam-pressing brisk according to claim 1, it is characterised in that:Step(2)Described sealing hair
The ferment time is 25~30 days.
5. a kind of preparation method of steam-pressing brisk according to claim 1, it is characterised in that:Step(3)Described high pressure is steamed
Vapour curing condition is:It it is 180~200 DEG C in temperature, pressure steams to enter horizontal high voltage under the conditions of 1.3~1.6MPa in still kettle
Vapour conserves 8~12h.
6. a kind of preparation method of steam-pressing brisk according to claim 1, it is characterised in that:Step(3)Described supports naturally
The shield time is 28~30 days.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710424716.8A CN107324743A (en) | 2017-06-07 | 2017-06-07 | A kind of preparation method of steam-pressing brisk |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710424716.8A CN107324743A (en) | 2017-06-07 | 2017-06-07 | A kind of preparation method of steam-pressing brisk |
Publications (1)
Publication Number | Publication Date |
---|---|
CN107324743A true CN107324743A (en) | 2017-11-07 |
Family
ID=60194505
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201710424716.8A Pending CN107324743A (en) | 2017-06-07 | 2017-06-07 | A kind of preparation method of steam-pressing brisk |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN107324743A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108546067A (en) * | 2018-05-03 | 2018-09-18 | 佛山九陌科技信息咨询有限公司 | A kind of preparation method of high-strength water-resistance type steam-pressing brisk |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102431080A (en) * | 2011-08-29 | 2012-05-02 | 武汉理工大学 | Method for preparing colored autoclaved brick from lake sludge |
CN102531511A (en) * | 2011-08-19 | 2012-07-04 | 中国海洋大学 | Autoclaved brick prepared with dredged sludge and preparation method thereof |
CN103360103A (en) * | 2013-04-17 | 2013-10-23 | 安徽盛仁新型建材有限公司 | Fly ash concrete aerated insulating brick and production method thereof |
CN105271982A (en) * | 2015-09-30 | 2016-01-27 | 安徽坤隆新型建材有限公司 | Aerated brick and making method thereof |
CN105859232A (en) * | 2016-04-12 | 2016-08-17 | 东南大学 | Autoclaved sand-lime brick produced from industrial sludge, and production method thereof |
-
2017
- 2017-06-07 CN CN201710424716.8A patent/CN107324743A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102531511A (en) * | 2011-08-19 | 2012-07-04 | 中国海洋大学 | Autoclaved brick prepared with dredged sludge and preparation method thereof |
CN102431080A (en) * | 2011-08-29 | 2012-05-02 | 武汉理工大学 | Method for preparing colored autoclaved brick from lake sludge |
CN103360103A (en) * | 2013-04-17 | 2013-10-23 | 安徽盛仁新型建材有限公司 | Fly ash concrete aerated insulating brick and production method thereof |
CN105271982A (en) * | 2015-09-30 | 2016-01-27 | 安徽坤隆新型建材有限公司 | Aerated brick and making method thereof |
CN105859232A (en) * | 2016-04-12 | 2016-08-17 | 东南大学 | Autoclaved sand-lime brick produced from industrial sludge, and production method thereof |
Non-Patent Citations (1)
Title |
---|
李舒瑶等: "《土木工程材料》", 31 July 2015, 中国水利水电出版社 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108546067A (en) * | 2018-05-03 | 2018-09-18 | 佛山九陌科技信息咨询有限公司 | A kind of preparation method of high-strength water-resistance type steam-pressing brisk |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102964093B (en) | Regeneration concrete brick and preparation method thereof | |
CN106242428B (en) | A kind of sludge ceramsite water-permeable brick and preparation method thereof | |
CN102515681B (en) | Method for producing aerated building block with phosphogypsum as main raw material | |
CN102206073B (en) | Slit burning-free bricks and production method thereof | |
CN103541289A (en) | Colored high-titanium heavy slag permeable pavement brick and production method thereof | |
CN104177015A (en) | Baking-free brick mainly prepared from river/lake dredging sediment and natural-curing manufacturing method thereof | |
CN108715528A (en) | A kind of permeable pavement brick and preparation method thereof | |
CN102659376A (en) | Water proof baking-free brick with ardealite serving as main material and manufacturing method thereof | |
CN103964786B (en) | A kind of method utilizing paper white sludge and quartz slate waste to produce calcium silicon plate | |
CN101020611A (en) | Honeycomb ceramic preparing process | |
CN107602049A (en) | A kind of preparation method of high-strength waterproof clay sculpture material | |
CN104529334B (en) | Discarded fired brick regeneration C35 synthetic fiber concretes and preparation method thereof | |
CN107324743A (en) | A kind of preparation method of steam-pressing brisk | |
CN106626621A (en) | Double-sided decorative waterproof plate and production method thereof | |
CN102180636A (en) | Brick making process utilizing titanium gypsum blended with toxic sludge | |
CN108373304A (en) | A kind of building waste prefabricated component and its manufacturing method | |
CN101863647A (en) | Novel baking-free steaming-free environment-friendly rock debris and rock-magma bricks | |
CN107216103A (en) | A kind of steam-pressing brisk and its preparation technology | |
CN105906268B (en) | A kind of dredging silt no-firing brick and preparation method thereof | |
CN102070322A (en) | Method for preparing high-strength ceramic wall material from papermaking causticized white mud residues | |
CN107188497A (en) | A kind of water-permeable brick and preparation method | |
CN102690093A (en) | High-strength water resistance phosphogypsum steam-cured brick and preparation method thereof | |
CN105503234A (en) | Preparation method of vegetation form light high-strength concrete | |
CN115536357A (en) | River and lake dredging bottom mud brick and preparation method thereof | |
CN105948645B (en) | A kind of modified ecological nano particle enhancing cement-base composite material and preparation method thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20171107 |
|
WD01 | Invention patent application deemed withdrawn after publication |