CN103341908A - Automated production line and automated production method of light-weight wall material - Google Patents
Automated production line and automated production method of light-weight wall material Download PDFInfo
- Publication number
- CN103341908A CN103341908A CN2013102863788A CN201310286378A CN103341908A CN 103341908 A CN103341908 A CN 103341908A CN 2013102863788 A CN2013102863788 A CN 2013102863788A CN 201310286378 A CN201310286378 A CN 201310286378A CN 103341908 A CN103341908 A CN 103341908A
- Authority
- CN
- China
- Prior art keywords
- control system
- electric control
- sent
- instruction
- feed
- 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.)
- Granted
Links
- 239000000463 material Substances 0.000 title claims abstract description 152
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 61
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 118
- 150000001875 compounds Chemical class 0.000 claims abstract description 32
- 239000002994 raw material Substances 0.000 claims abstract description 26
- 238000003756 stirring Methods 0.000 claims abstract description 23
- 239000004604 Blowing Agent Substances 0.000 claims description 109
- 238000003860 storage Methods 0.000 claims description 71
- 239000004615 ingredient Substances 0.000 claims description 43
- 238000000465 moulding Methods 0.000 claims description 42
- 238000005303 weighing Methods 0.000 claims description 39
- 239000002002 slurry Substances 0.000 claims description 31
- 239000004568 cement Substances 0.000 claims description 26
- 238000006243 chemical reaction Methods 0.000 claims description 22
- 238000005187 foaming Methods 0.000 claims description 19
- 238000002347 injection Methods 0.000 claims description 19
- 239000007924 injection Substances 0.000 claims description 19
- 239000010881 fly ash Substances 0.000 claims description 18
- 229920000642 polymer Polymers 0.000 claims description 17
- 238000007664 blowing Methods 0.000 claims description 9
- 238000010438 heat treatment Methods 0.000 claims description 9
- 239000003795 chemical substances by application Substances 0.000 claims description 6
- 235000021050 feed intake Nutrition 0.000 claims description 6
- 239000007921 spray Substances 0.000 claims description 5
- 239000000428 dust Substances 0.000 claims description 4
- 230000015572 biosynthetic process Effects 0.000 claims description 3
- 239000003365 glass fiber Substances 0.000 claims description 3
- 238000007789 sealing Methods 0.000 claims description 3
- 239000004088 foaming agent Substances 0.000 abstract description 3
- 238000009776 industrial production Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 8
- 230000001413 cellular effect Effects 0.000 description 6
- 239000006260 foam Substances 0.000 description 3
- 238000005192 partition Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 239000012774 insulation material Substances 0.000 description 2
- 239000011812 mixed powder Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000011398 Portland cement Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000004079 fireproofing Methods 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 239000006261 foam material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Images
Landscapes
- Preparation Of Clay, And Manufacture Of Mixtures Containing Clay Or Cement (AREA)
Abstract
The invention relates to a production line and production method of building wall material, in particular to an automated production line and automated production method of light-weight wall material. According to the specific technical scheme, the automated production line of the light-weight wall material comprises a raw material rationing system, a compound material mixing system, a constant temperature water supplying system, a foaming agent supplying system, a stirring reacting system, an electric control system, a mold box conveying device and an equipment connecting walking table. The automated production method of the light-weight wall material includes the steps of raw material rationing, compound material mixing, mixed material supplying, constant temperature water supplying, stirring, foaming agent supplying, reacting and mold box forming. According to the automated production line and automated production method of the light-weight wall material, quality stability of the light-weight wall material can be ensured, production efficiency is improved, and industrial production of the light-weight wall material is achieved.
Description
Technical field
The present invention relates to a kind of production line and production method of building walling, particularly relate to a kind of automatic production line and automatic production method of light-weight wall material.
Background technology
The foam cement of China is a kind of A level fire proofing material, and current the sector is in a starting stage, the product quality industry standard that also neither one is complete, the simple and easy backwardness of production equipment, environmental protection can not be up to standard, therefore product quality does not guarantee, is difficult to realize industrialization.
Chinese patent CN201010582361.3, name is called " the cellular foaming body insulation material of a kind of fire-proof wall ", discloses a kind of cellular light material, is tens kinds of materials such as cement, flyash to be mixed back generation chemical reaction make it foam to make.In order to make constant product quality, must scientific formula, accurately quantitatively, every index of any one material goes wrong, and all can exert an influence to product quality.Because the sensitivity of chemistry reflection, when the height of foamed products reached 35 centimeters, the defect ware of product will significantly increase.
In current the sector, daily output reaches the factory of 30 cubic metres of finished products, just needs workman 70-80 people, and efficiency is low, and factory does not have profit, causes the sector to develop, and product can not get good popularization.
Chinese patent CN201120218274.X, name is called " a kind of internal partition wall of cellular foaming wall material ", discloses a kind of internal partition wall of cellular foaming wall material, and it is materials for wall that cellular foam material is promoted by single fire-retardant heat-insulation material.This light-weight wall material presses for an automatic production line, by scientific formula and automation control, guarantees the stability of product quality, increases work efficiency by automation, realizes the industry industrialization.
Summary of the invention
The automatic production line and the automatic production method that the purpose of this invention is to provide a kind of light-weight wall material solve the problems referred to above.
Concrete technical scheme is:
A kind of automatic production line of light-weight wall material comprises that raw material rationing system, combined type mixing system, constant temperature water supply system, blowing agent supply system, stirring reaction system, electric control system, moulding box conveyer are connected with equipment to walk on stage;
Described raw material rationing system comprises cement storage warehouse, breeze storage warehouse, flyash storage warehouse, polymer storage warehouse, automatic conveying equipment, the quantitative storehouse of major ingredient and the quantitative storehouse of auxiliary material, described major ingredient arranges electronic weighing balance one in the quantitative storehouse, and described auxiliary material arranges electronic weighing balance two in the quantitative storehouse; The quantitative storehouse of described major ingredient and the quantitative storehouse of described auxiliary material are set up in parallel; To the quantitative storehouse of described major ingredient feed, described flyash storage warehouse and described polymer storage warehouse pass through described automatic conveying equipment to the quantitative storehouse of described auxiliary material feed by described automatic conveying equipment for described cement storage warehouse and described breeze storage warehouse;
Described combined type mixing system comprises batch mixer one, batch mixer two, material stock storehouse, quantitative storehouse, automatic conveying equipment and batch mixing batcher; In the described quantitative storehouse electronic weighing balance three is set; Described batch mixer one is positioned at the quantitative storehouse of described major ingredient and below, the quantitative storehouse of described auxiliary material, and described batch mixer two is positioned at described batch mixer one below; Described batch mixer one arranges agitator one, charging aperture one, drain hole one and dog-house, and described batch mixer two arranges agitator two, charging aperture two and drain hole two; The quantitative storehouse of described major ingredient and the quantitative storehouse of described auxiliary material are to described charging aperture one feed of described batch mixer one, described batch mixer one is by described charging aperture two feed of described drain hole one to described batch mixer two, to described material stock storehouse feed, described automatic conveying equipment is passed through to described quantitative storehouse feed in described material stock storehouse to the described drain hole two of described batch mixer two by described automatic conveying equipment;
Described constant temperature water supply system comprises water heating apparatus, insulating box, the quantitative case of warm water and water output device; Water temperature control inductor is set in the described water heating apparatus; In the quantitative case of described warm water electronic weighing balance four is set; Described water output device comprises force (forcing) pump one and water jet;
Described blowing agent supply system comprises blowing agent storage tank, blowing agent feed-line, blowing agent distributor and blowing agent injection device; Described blowing agent storage tank, described blowing agent distributor and described blowing agent injection device are connected by described blowing agent feed-line; In the described blowing agent distributor electronic weighing balance five is set; Described blowing agent injection device comprises force (forcing) pump two and blowing agent spout, and described blowing agent spout is a plurality of;
Described stirring reaction system comprises first reactor, second reactor; Described first reactor comprises charging aperture three, agitator three and drain hole three, and described water jet is arranged in described first reactor, and described quantitative storehouse is by described charging aperture three feed of described batch mixing batcher to described first reactor; Described second reactor comprises charging aperture four, agitator four and drain hole four, described blowing agent spout is arranged in described second reactor, described second reactor is positioned at the below of described first reactor, and the described drain hole three of described first reactor is relative with the described charging aperture four of described second reactor;
Described electric control system comprises operating console, described operating console be placed in described equipment connect walk on stage on; Described operating console comprises microcomputer and measuring instrument, and described system links to each other by sensor and other;
Described moulding box conveyer comprises moulding box, moulding box guide rail and cross moving track.
The described automatic conveying equipment of the automatic production line of light-weight wall material can be conveying worm.
The automatic production line of light-weight wall material, described raw material rationing system can also comprise the reclaimed materials automatic charging machine, described reclaimed materials automatic charging machine can be put into reclaimed materials in the quantitative storehouse of described major ingredient.
The automatic production line of light-weight wall material, described cement storage warehouse, described breeze storage warehouse, described flyash storage warehouse, described polymer storage warehouse, described batch mixer one, described batch mixer two, described material stock storehouse, described quantitative storehouse, described first reactor and described second reactor arrange pressure relief device, sealing device and air-borne dust cleaner.
The automatic production line of light-weight wall material, described blowing agent spout quantity is preferably 6～8.
The automatic production line of light-weight wall material, preferred version is: the described blowing agent feed-line of part spirals and is arranged in the described insulating box, so that the temperature of blowing agent reaches the equilibrium temperature the same with water in the insulating box.
Described moulding box volume can be 1～3 cubic metre as requested, the length size conforms building module requirement of described moulding box inside, thereby the light-weight wall material size conforms building module requirement that processes.
Above-mentioned agitator one～four can be the rotating vane structure, also can realize the structure of agitating function for other.
The present invention also provides a kind of automatic production method of light-weight wall material, utilizes the automatic production line of aforesaid light-weight wall material, comprises the steps:
(1) raw material rationing step: according to the program that electric control system is set, each storage warehouse feeds intake to the quantitative storehouse of major ingredient and the quantitative storehouse of auxiliary material successively; Described electric control system is sent the feed instruction to described cement storage warehouse, described cement storage warehouse passes through described automatic conveying equipment to the quantitative storehouse of described major ingredient feed, when described electronic weighing balance one showed that cement reaches technological requirement weight, described electric control system was sent and is stopped the feed instruction; Described electric control system is sent the feed instruction to described breeze storage warehouse, described breeze storage warehouse passes through described automatic conveying equipment to the quantitative storehouse of described major ingredient feed, when described electronic weighing balance one showed that breeze reaches technological requirement weight, described electric control system was sent and is stopped the feed instruction; Described electric control system is sent the feed instruction to described flyash storage warehouse, described flyash storage warehouse passes through described automatic conveying equipment to the quantitative storehouse of described auxiliary material feed, when described electronic weighing balance two showed that flyash reaches technological requirement weight, described electric control system was sent and is stopped the feed instruction; Described electric control system is sent the feed instruction to described polymer storage warehouse, described polymer storage warehouse passes through described automatic conveying equipment to the quantitative storehouse of described auxiliary material feed, when described electronic weighing balance two showed that polymer reaches technological requirement weight, described electric control system was sent and is stopped the feed instruction; Described electric control system is sent the feed instruction to the quantitative storehouse of described major ingredient and the quantitative storehouse of described auxiliary material, and the quantitative storehouse of described major ingredient and the quantitative storehouse of described auxiliary material are put into raw material in the described batch mixer one; Feed intake finish after, described electric control system is sent instruction, beginning described raw material rationing step next time; This step is carried out in circulation;
(2) combined type batch mixing step: artificial means or autocontrol method drop into the glass fibre of technological requirement weight to described dog-house; Described electric control system is sent first batch mixing instruction to described batch mixer one, described agitator is worked at the beginning, first mixing time is set at 4～15 minutes, the batch mixing amount can be for more than the 2T, after described first mixing time arrives, described electric control system is sent to described batch mixer one and is stopped first batch mixing instruction, and described agitator one quits work; Described electric control system is sent the feed instruction to described batch mixer one, and described batch mixer one is opened described drain hole one and dropped into first compound by described charging aperture two to described batch mixer two; After dropping into first compound and finishing, described electric control system is sent the feed instruction to the quantitative storehouse of described major ingredient and the quantitative storehouse of described auxiliary material, and after raw material fed intake and finishes, described electric control system was sent first batch mixing instruction next time to described batch mixer one; After first compound drops into described batch mixer two, described electric control system is sent the rerolling instruction to described batch mixer two, described agitator two is started working, the rerolling time set is 4～15 minutes, after the described rerolling time arrives, described electric control system is sent to described batch mixer two and is stopped the rerolling instruction, and described agitator two quits work; Described electric control system is sent the feed instruction to described batch mixer two, and described batch mixer two is opened described drain hole two and dropped into compound to described material stock storehouse by described automatic conveying equipment; After described compound fed intake and finishes, described electric control system was sent instruction, and beginning is described combined type batch mixing step next time; Described first mixing time is identical numerical value with described rerolling time set; This step is carried out in circulation;
(3) compound supply step: described electric control system is sent the feed instruction to described material stock storehouse, described material stock storehouse is dropped into described compound by described automatic conveying equipment to described quantitative storehouse, when described electronic weighing balance three showed that described compound reaches technological requirement weight, described electric control system was sent to described material stock storehouse and is stopped the feed instruction; When described electric control system is sent the feed instruction to described quantitative storehouse, described quantitative storehouse feeds intake by the described charging aperture three of described batch mixing batcher to described first reactor, feed intake finish after, described electric control system is sent feed instruction next time to described material stock storehouse, the step that described material stock storehouse feeds intake to described quantitative storehouse is carried out in circulation; When the number of times that feeds intake to described quantitative storehouse when described material stock storehouse reaches the predefined numerical value of described electric control system, material stock in this moment described material stock storehouse is the desired compound weight in described quantitative storehouse inadequately, described electric control system is sent the feed instruction to described batch mixer, described batch mixer two feeds intake to described material stock storehouse again, and beginning is described compound supply step next time; This step is carried out in circulation;
(4) constant temperature water supply step: described water temperature control inductor shows when the water temperature in the described water heating apparatus reaches technological requirement numerical value, artificial means or autocontrol method are transported to warm water in the insulating box and store, described electric control system is sent the quantitative case water supply of described warm water instruction to described insulating box, described insulating box is transported to warm water in the quantitative case of described warm water, when described electronic weighing balance four showed that the water yield reaches technological requirement weight, described electric control system was sent and is stopped the quantitative case water supply of described warm water instruction; Send when described first reactor supplied water instruction to the quantitative case of described warm water when described electric control system, the warm water of the quantitative case of described warm water feeds to described first reactor through described force (forcing) pump one pressurization back by described water jet, and water supply time was less than 20 seconds; After warm water was all confessed in the quantitative case of described warm water, described electric control system was sent again the quantitative case of described warm water to be supplied water to described insulating box and is instructed, and beginning is described constant temperature water supply step next time; This step is carried out in circulation;
(5) whipping step: described electric control system is sent the feed instruction to described quantitative storehouse, described electric control system is sent the instruction of supplying water to the quantitative case of described warm water simultaneously, described electric control system is sent to described agitator three and is stirred instruction simultaneously, described agitator three begins to stir, mixing time is 4～6 minutes, and described compound and water form slurry; After described mixing time arrived, described electric control system was sent to described agitator three and is stopped to stir instruction, and described agitator three quits work; Described electric control system is sent the blowing instruction to described first reactor, and described slurry leaks in described second reactor by described drain hole three and described charging aperture four; Described electric control system is sent instruction, carries out described whipping step next time; This step is carried out in circulation;
(6) blowing agent supply step: described electric control system is sent for the agent instruction to described blowing agent storage tank, described blowing agent storage tank is carried blowing agent by described blowing agent feed-line to described blowing agent distributor, when described electronic weighing balance five showed that foaming dosage reaches technological requirement weight, described electric control system was sent and is stopped for the agent instruction; When described electric control system is sent the instruction of injection blowing agent to described blowing agent spout, whole blowing agents in the described blowing agent distributor spray to described second reactor by described blowing agent spout through described force (forcing) pump two pressurization backs, with uniform mode and the fastest speed be equivalent, equidistant, etc. the time, injection method ejection simultaneously, the ejection time is in 3 seconds; Described electric control system is sent instruction, carries out described blowing agent supply step next time; This step is carried out in circulation;
(7) reactions steps: after the described slurry of described whipping step leaked into described second reactor, described electric control system was sent to described agitator four and is stirred instruction, and described agitator four starts, and stirring the described slurry time is 3～6 minutes; After the described slurry time of described stirring arrives, described electric control system is sent to described blowing agent injection device and is sprayed the blowing agent instruction, whole blowing agents in the described blowing agent distributor spray to described second reactor by described blowing agent spout through described force (forcing) pump two pressurization backs, and the ejection time is in 3 seconds; Described slurry and described blowing agent react and formed the foaming body cement slurry in 30～120 seconds; Described electric control system is sent halt instruction to described agitator four, and described agitator four quits work; Described electric control system is sent the blowing instruction to described emptying door four, and described foaming body cement slurry leaks in the described moulding box; After blowing was finished, described electric control system was sent instruction, carried out reactions steps next time; This step is carried out in circulation;
(8) moulding box forming step: artificial means or autocontrol method, described moulding box is placed into the below of described second reactor along described moulding box guide rail, after described foaming body slurry fills up described moulding box, described moulding box is shifted out along described cross moving track; Foaming body slurry after 3-8 hour in the described moulding box solidifies the formation light-weight wall material, can satisfy carrying, folded high requirement, and described moulding box continues to recycle.
The automatic production method of described light-weight wall material, preferred version is: described whipping step is identical with the used time of described reactions steps, is 4～8 minutes.
The automatic production method of described light-weight wall material, preferred version is: when reclaimed materials can add, in described raw material rationing step, described electric control system is sent the feed instruction to described reclaimed materials automatic charging machine, described reclaimed materials automatic charging machine is to the quantitative storehouse of described major ingredient feed, when described electronic weighing balance one showed that reclaimed materials meets technological requirement weight, described electric control system was sent and is stopped the feed instruction.
Application of the present invention, can satisfy the foam production requirement of Portland cement and special cement, particularly can be applied to China Patent No. ZL201120218274.X, name is called the automated production of the light-weight wall material of " a kind of internal partition wall of cellular foaming wall material ".
Advantage of the present invention:
1, automatic production line of the present invention adopts the electric control system operation, and material usage and production time are accurately controlled, and has guaranteed the stability of product quality.
2, automatic production line of the present invention arranges the quantitative storehouse of major ingredient and the quantitative storehouse of auxiliary material, to the raw material metering quantitatively, has improved the accuracy rate of raw material proportioning respectively.
3, the combined type mixing system of automatic production line of the present invention, adopt three-dimensional combined type batch mixing, carried out the rerolling process, guarantee the quality of batch mixing: together compatible the dry powder blend of different densities, make the various uniform ingredients unanimities of mixed powder, guaranteed light-weight wall material density and quality homogeneity; And shortened working time of batch mixing, and shortened the working time of stirring reaction system simultaneously, significantly improved operating efficiency.
4, second metering is carried out to mixed powder in the quantitative storehouse of automatic production line of the present invention, has guaranteed the accuracy of materials in first reactor and second reactor, guarantees the controllability of foamable reaction, guarantees dry density and the quality of stability of light-weight wall material.
5, constant temperature water supply of the present invention system provides constant temperature quantitative water, and temperature and the consumption of strict control water have ensured uniformity and the stability of slurry, have ensured the stability of foamable reaction simultaneously.
6, blowing agent supply system of the present invention, the blowing agent distributor has guaranteed the stable and consistent of foamable reaction to the foaming agent consumption accurate measurement; The blowing agent feed-line spirals and is arranged in the described insulating box, makes the temperature of blowing agent reach the equilibrium temperature the same with water in the insulating box, has guaranteed the stable and consistent of foamable reaction; Force (forcing) pump and a plurality of blowing agent spout control blowing agent are with uniform method and the fastest speed, both equivalent, equidistant, etc. the time, injection method simultaneously, be injected in second reactor, guaranteed foamable reaction consistent in time synchronously, the light-weight wall material air entrapment size of producing is even, consistent in density.
7, stirring reaction of the present invention system carries out secondary and stirs, and has guaranteed that slurry stirs fully, the light-weight wall material air entrapment of production size evenly accurately, consistent in density.
8, automatic production line of the present invention, the design of the solid of first reactor and second reactor is a high-efficient production technology, guarantees that two reactors reflect that the times are identical, has then not only guaranteed product quality but also the operating efficiency that is doubled.
9, reclaimed materials automatic charging machine of the present invention can be transported to the quantitative storehouse of major ingredient to reclaimed materials such as the leftover pieces that produce and waste products and carry out recycling, has saved raw material, has reduced product cost, has realized 0 discharging.
10, pressure relief device of the present invention has guaranteed safety in production; Sealing device and air-borne dust cleaner have been carried out strict control to dust, have effectively improved working environment, reduce and pollute.
11, the length size conforms building module requirement of moulding box of the present invention inside, the modulus requirement of the light-weight wall material size conforms building block of producing has effectively improved the product row yielding, has reduced waste, saves cost.
12, automatic production line of the present invention, the daily output can reach the 600-1000m3 light-weight wall material, and operating efficiency is 20-30 times of general individual workship, and cost of labor is one of 20 parts of individual workship, has improved production efficiency.
Description of drawings
Fig. 1 faces structural representation for the automatic production line of light-weight wall material
Fig. 2 is the automatic production line plan structure schematic diagram of light-weight wall material
The specific embodiment
As shown in Figure 1, 2, the automatic production line of light-weight wall material comprises that raw material rationing system, combined type mixing system, constant temperature water supply system, blowing agent supply system, stirring reaction system, electric control system, moulding box conveyer are connected with equipment to walk on stage 15.
Described raw material rationing system comprises cement storage warehouse 1, breeze storage warehouse 2, flyash storage warehouse 3, polymer storage warehouse 4, automatic conveying equipment 22, reclaimed materials automatic charging machine 20, the quantitative storehouse 5 of major ingredient and the quantitative storehouse 6 of auxiliary material, described major ingredient arranges electronic weighing balance one in the quantitative storehouse 5, and described auxiliary material arranges electronic weighing balance two in the quantitative storehouse 6; The quantitative storehouse 5 of described major ingredient is set up in parallel with the quantitative storehouse 6 of described auxiliary material; Described cement storage warehouse 1 and described breeze storage warehouse 2 pass through described automatic conveying equipment 22 to the quantitative storehouse of described major ingredient 5 feed, described reclaimed materials automatic charging machine 20 is to the quantitative storehouse of described major ingredient 5 feed, and described flyash storage warehouse 3 and described polymer storage warehouse 4 pass through described automatic conveying equipment 22 to the quantitative storehouse of described auxiliary material 6 feed.
Described combined type mixing system comprises batch mixer 1, batch mixer 2 25, material stock storehouse 8, quantitative storehouse 9, automatic conveying equipment 22 and batch mixing batcher 10; Described batch mixing arranges electronic weighing balance three in the quantitative storehouse 9; Described batch mixer 7 is positioned at the quantitative storehouse 5 of described major ingredient and 6 belows, the quantitative storehouse of auxiliary material; Described batch mixer 1 arranges agitator one, charging aperture one, drain hole one and dog-house 26, and described batch mixer 2 25 arranges agitator two, charging aperture two and drain hole two; The quantitative storehouse 5 of described major ingredient and the quantitative storehouse 6 of described auxiliary material are to described charging aperture one feed of described batch mixer 1, described batch mixer 1 is by described charging aperture two feed of described drain hole one to described batch mixer 2 25, to described material stock storehouse 8 feed, described automatic conveying equipment 22 is passed through to described quantitative storehouse 9 feed in described material stock storehouse 8 to the described drain hole two of described batch mixer 2 25 by described automatic conveying equipment 22.
Described constant temperature water supply system comprises water heating apparatus 16, insulating box 17, the quantitative case 21 of warm water and water output device; Water temperature control inductor is set in the described water heating apparatus 16; In the quantitative case 21 of described warm water electronic weighing balance four is set; Described water output device comprises force (forcing) pump one and water jet.
Described blowing agent supply system comprises blowing agent storage tank 18, blowing agent feed-line, blowing agent distributor 19 and blowing agent injection device; Described blowing agent storage tank 18, described blowing agent distributor 19 and described blowing agent injection device are connected by described blowing agent feed-line; Described blowing agent feed-line between described blowing agent storage tank 18 and the described blowing agent distributor 19 passes through in described insulating box 17, spirals to be arranged in the described insulating box 17; In the described blowing agent distributor 19 electronic weighing balance five is set; Described blowing agent injection device comprises force (forcing) pump two and blowing agent spout, and described blowing agent spout is seven.
Described stirring reaction system comprises first reactor 11, second reactor 12; Described first reactor 11 comprises material mouth three, agitator three and drain hole three, and described water jet is arranged in described first reactor 11, and described quantitative storehouse 9 is by described charging aperture one feed of described batch mixing batcher 10 to described first reactor 11; Described second reactor 12 comprises charging aperture four, agitator four and drain hole four, described blowing agent spout is arranged in described second reactor 12, described second reactor 12 is positioned at the below of described first reactor 11, and the described emptying door one of described first reactor is relative with the described charging aperture two of described second reactor.
Described electric control system comprises operating console 13, and described operating console 13 is placed in described equipment and connects and walk on stage on 15; Described operating console 13 comprises microcomputer and measuring instrument, and described system links to each other by sensor and other.
Described moulding box conveyer comprises moulding box 14, moulding box guide rail 23 and cross moving track 24.Moulding box 14 volumes are 3 cubic metres.
The automatic production line of this light-weight wall material is carried out following steps:
One, raw material rationing step: electric control system is sent the feed instruction to described cement storage warehouse 1, described cement storage warehouse 1 passes through described automatic conveying equipment 22 to the quantitative storehouse of described major ingredient 5 feed, when described electronic weighing balance one showed that cement reaches technological requirement weight, described electric control system was sent and is stopped the feed instruction; Described electric control system is sent the feed instruction to described breeze storage warehouse 2, described breeze storage warehouse 2 passes through described automatic conveying equipment 22 to the quantitative storehouse of described major ingredient 5 feed, when described electronic weighing balance one showed that breeze reaches technological requirement weight, described electric control system was sent and is stopped the feed instruction; In the time can adding reclaimed materials, described electric control system is sent the feed instruction to described reclaimed materials automatic charging machine 20, described reclaimed materials automatic charging machine 20 is to the quantitative storehouse of described major ingredient 5 feed, when described electronic weighing balance one demonstration met technological requirement weight, described electric control system was sent and is stopped the feed instruction; Described electric control system is sent the feed instruction to described flyash storage warehouse 3, described flyash storage warehouse 3 passes through described automatic conveying equipment 22 to the quantitative storehouse of described auxiliary material 6 feed, when described electronic weighing balance two showed that flyash reaches technological requirement weight, described electric control system was sent and is stopped the feed instruction; Described electric control system is sent the feed instruction to described polymer storage warehouse 4, described polymer storage warehouse 4 passes through described automatic conveying equipment 22 to the quantitative storehouse of described auxiliary material 6 feed, when described electronic weighing balance two showed that polymer reaches technological requirement weight, described electric control system was sent and is stopped the feed instruction; Described electric control system is sent the feed instruction to the quantitative storehouse 5 of described major ingredient and the quantitative storehouse 6 of described auxiliary material, and the quantitative storehouse 5 of described major ingredient and the quantitative storehouse 6 of described auxiliary material are put into raw material in the described batch mixer 1; Feed intake finish after, described electric control system is sent instruction, this step is carried out in circulation.
Two, combined type batch mixing step: manually drop into the glass fibre of technological requirement weight to dog-house 26; Described electric control system is sent first batch mixing instruction to described batch mixer 1, described agitator is worked at the beginning, first mixing time is 8 minutes, batch mixing amount 2T, after first mixing time arrives, described electric control system is sent to described batch mixer 1 and is stopped first batch mixing instruction, and described agitator one quits work; Described electric control system is sent the feed instruction to described batch mixer 1, and described batch mixer 1 is opened described drain hole one and dropped into first compound by described charging aperture two to described batch mixer 2 25; After dropping into first compound and finishing, described electric control system is sent the feed instruction to the quantitative storehouse 5 of described major ingredient and the quantitative storehouse 6 of described auxiliary material, and after raw material fed intake and finishes, described electric control system was sent first batch mixing instruction next time to described batch mixer 1; After first compound drops into described batch mixer 2 25, described electric control system is sent the rerolling instruction to described batch mixer 2 25, described agitator two is started working, the rerolling time set is 8 minutes, after the described rerolling time arrives, described electric control system is sent to described batch mixer 2 25 and is stopped the rerolling instruction, and described agitator two quits work; Described electric control system is sent feed instruction to described batch mixer 2 25, and described batch mixer 2 25 is opened described drain hole two and 8 dropped into compounds by described automatic conveying equipment 22 to described material stock storehouse; After described compound fed intake and finishes, described electric control system was sent instruction, and beginning is described combined type batch mixing step next time; This step is carried out in circulation.
Three, compound supply step: described electric control system is sent the feed instruction to described material stock storehouse 8, described material stock storehouse 8 feeds intake to described quantitative storehouse 9 by described automatic conveying equipment 22, when described electronic weighing balance three showed that compound reaches technological requirement weight, described electric control system was sent to described material stock storehouse 8 and is stopped the feed instruction; When described electric control system is sent the feed instruction to described quantitative storehouse 9, described quantitative storehouse 9 feeds intake by the described charging aperture one of described batch mixing batcher 10 to described first reactor 11, feed intake finish after, described electric control system is sent feed instruction next time to described material stock storehouse 8, circulation carry out this step; When the number of times that feeds intake to described quantitative storehouse 9 when described material stock storehouse 8 reaches the predefined numerical value of described electric control system, described electric control system is sent the feed instruction to described batch mixer 2 25, described batch mixer 2 25 feeds intake to described material stock storehouse 8 again, beginning is described compound supply step next time, and this step is carried out in circulation.
Four, constant temperature water supply step: described water temperature control inductor shows when the water temperature in the described water heating apparatus 16 reaches technological requirement numerical value, warm water is transported to storage in the insulating box 17, described electric control system is sent the quantitative case 21 water supply instructions of described warm water to described insulating box 17, described insulating box 17 is transported to warm water in the quantitative case 21 of described warm water, when described electronic weighing balance four showed that the water yield reaches technological requirement weight, described electric control system was sent and is stopped the quantitative case 21 water supply instructions of described warm water; Send when described first reactor 11 supplied water instruction to the quantitative case 21 of described warm water when described electric control system, the quantitative case 21 of described warm water supplies water to described first reactor 11 by described water jet, and water supply time is 10 seconds; After warm water was all confessed in the quantitative case 21 of described warm water, described electric control system was sent again the quantitative case 21 of described warm water to be supplied water to described insulating box 17 and is instructed, and beginning is described constant temperature water supply step next time, and this step is carried out in circulation.
Five, whipping step: described electric control system is sent the feed instruction to described quantitative storehouse 9, described electric control system is sent the instruction of supplying water to the quantitative case 21 of described warm water simultaneously, described electric control system is sent to described agitator three and is stirred instruction simultaneously, described agitator three begins to stir, mixing time is 4 minutes, and described compound and water form slurry; After described mixing time arrived, described electric control system was sent to described agitator three and is stopped to stir instruction, and described agitator three quits work; Described electric control system is sent the blowing instruction to described first reactor 11, and described slurry leaks in described second reactor 12 by described drain hole three and charging aperture four; Described electric control system is sent instruction, carries out described whipping step next time, and this step is carried out in circulation.
Six, blowing agent supply step: described electric control system is sent for the agent instruction to described blowing agent storage tank 18, described blowing agent storage tank 18 is carried blowing agent to described blowing agent distributor 19, when described electronic weighing balance five showed that foaming dosage reaches technological requirement weight, described electric control system was sent and is stopped for the agent instruction; When described electric control system is sent the instruction of injection blowing agent to described blowing agent injection device, whole blowing agents in the described blowing agent distributor 19 spray to described second reactor by described blowing agent spout through described force (forcing) pump two pressurization backs, and the ejection time is 1 second; Described electric control system is sent instruction, carries out described blowing agent supply step next time, and this step is carried out in circulation.
Seven, reactions steps: the described slurry of described whipping step enters into described second reactor 12, and described electric control system is sent to described agitator four and stirred instruction, and described agitator four starts, and stirring the described slurry time is 3 minutes; After 3 minutes arrived, described electric control system was sent to described blowing agent injection device and is sprayed the blowing agent instruction; After reacting 40 seconds, described slurry and described blowing agent form the foaming body slurry; Described electric control system is sent halt instruction to described agitator four, and described agitator four quits work; Described electric control system is sent the blowing instruction to described emptying door four, and described foaming body slurry leaks in the described moulding box 14; After blowing was finished, described electric control system was sent instruction, carried out reactions steps next time, and this step is carried out in circulation.
Eight, moulding box forming step: manually described moulding box 14 is placed into the below of described second reactor 12 along described moulding box guide rail 23, after described foaming body slurry fills up described moulding box 14, described moulding box 14 is shifted out along described cross moving track 24; Foaming body slurry after 3 hours in the described moulding box 14 solidifies the formation light-weight wall material, and described moulding box 14 continues to recycle.
Claims (10)
1. the automatic production line of a light-weight wall material, it is characterized in that, comprise that raw material rationing system, combined type mixing system, constant temperature water supply system, blowing agent supply system, stirring reaction system, electric control system, moulding box conveyer are connected with equipment to walk on stage;
Described raw material rationing system comprises cement storage warehouse, breeze storage warehouse, flyash storage warehouse, polymer storage warehouse, automatic conveying equipment, the quantitative storehouse of major ingredient and the quantitative storehouse of auxiliary material, described major ingredient arranges electronic weighing balance one in the quantitative storehouse, and described auxiliary material arranges electronic weighing balance two in the quantitative storehouse; The quantitative storehouse of described major ingredient and the quantitative storehouse of described auxiliary material are set up in parallel; To the quantitative storehouse of described major ingredient feed, described flyash storage warehouse and described polymer storage warehouse pass through described automatic conveying equipment to the quantitative storehouse of described auxiliary material feed by described automatic conveying equipment for described cement storage warehouse and described breeze storage warehouse;
Described combined type mixing system comprises batch mixer one, batch mixer two, material stock storehouse, quantitative storehouse, automatic conveying equipment and batch mixing batcher; In the described quantitative storehouse electronic weighing balance three is set; Described batch mixer one is positioned at the quantitative storehouse of described major ingredient and below, the quantitative storehouse of described auxiliary material, and described batch mixer two is positioned at described batch mixer one below; Described batch mixer one arranges agitator one, charging aperture one, drain hole one and dog-house, and described batch mixer two arranges agitator two, charging aperture two and drain hole two; The quantitative storehouse of described major ingredient and the quantitative storehouse of described auxiliary material are to described charging aperture one feed of described batch mixer one, described batch mixer one is by described charging aperture two feed of described drain hole one to described batch mixer two, to described material stock storehouse feed, described automatic conveying equipment is passed through to described quantitative storehouse feed in described material stock storehouse to the described drain hole two of described batch mixer two by described automatic conveying equipment;
Described constant temperature water supply system comprises water heating apparatus, insulating box, the quantitative case of warm water and water output device; Water temperature control inductor is set in the described water heating apparatus; In the quantitative case of described warm water electronic weighing balance four is set; Described water output device comprises force (forcing) pump one and water jet;
Described blowing agent supply system comprises blowing agent storage tank, blowing agent feed-line, blowing agent distributor and blowing agent injection device; Described blowing agent storage tank, described blowing agent distributor and described blowing agent injection device are connected by described blowing agent feed-line; In the described blowing agent distributor electronic weighing balance five is set; Described blowing agent injection device comprises force (forcing) pump two and blowing agent spout, and described blowing agent spout is a plurality of;
Described stirring reaction system comprises first reactor, second reactor; Described first reactor comprises charging aperture three, agitator three and drain hole three, and described water jet is arranged in described first reactor, and described quantitative storehouse is by described charging aperture three feed of described batch mixing batcher to described first reactor; Described second reactor comprises charging aperture four, agitator four and drain hole four, described blowing agent spout is arranged in described second reactor, described second reactor is positioned at the below of described first reactor, and the described drain hole three of described first reactor is relative with the described charging aperture four of described second reactor;
Described electric control system comprises operating console, described operating console be placed in described equipment connect walk on stage on; Described operating console comprises microcomputer and measuring instrument, and described system links to each other by sensor and other;
Described moulding box conveyer comprises moulding box, moulding box guide rail and cross moving track.
2. the automatic production line of light-weight wall material according to claim 1 is characterized in that, described automatic conveying equipment is conveying worm.
3. the automatic production line of light-weight wall material according to claim 1 is characterized in that, described raw material rationing system also comprises the reclaimed materials automatic charging machine, and described reclaimed materials automatic charging machine is put into reclaimed materials in the quantitative storehouse of described major ingredient.
4. the automatic production line of light-weight wall material according to claim 1, it is characterized in that described cement storage warehouse, described breeze storage warehouse, described flyash storage warehouse, described polymer storage warehouse, described batch mixer one, described batch mixer two, described material stock storehouse, described quantitative storehouse, described first reactor and described second reactor arrange pressure relief device, sealing device and air-borne dust cleaner.
5. the automatic production line of light-weight wall material according to claim 1 is characterized in that, described blowing agent spout quantity is 6～8.
6. the automatic production line of light-weight wall material according to claim 1 is characterized in that, the described blowing agent feed-line of part spirals and is arranged in the described insulating box.
7. the automatic production line of light-weight wall material according to claim 1 is characterized in that, described moulding box volume is 1～3 cubic metre, the length size conforms building module requirement of described moulding box inside.
8. the automatic production method of a light-weight wall material is characterized in that, this automatic production method utilizes automatic production line as claimed in claim 1, comprises the steps:
(1) raw material rationing step: described electric control system is sent the feed instruction to described cement storage warehouse, described cement storage warehouse passes through described automatic conveying equipment to the quantitative storehouse of described major ingredient feed, when described electronic weighing balance one showed that cement reaches technological requirement weight, described electric control system was sent and is stopped the feed instruction; Described electric control system is sent the feed instruction to described breeze storage warehouse, described breeze storage warehouse passes through described automatic conveying equipment to the quantitative storehouse of described major ingredient feed, when described electronic weighing balance one showed that breeze reaches technological requirement weight, described electric control system was sent and is stopped the feed instruction; Described electric control system is sent the feed instruction to described flyash storage warehouse, described flyash storage warehouse passes through described automatic conveying equipment to the quantitative storehouse of described auxiliary material feed, when described electronic weighing balance two showed that flyash reaches technological requirement weight, described electric control system was sent and is stopped the feed instruction; Described electric control system is sent the feed instruction to described polymer storage warehouse, described polymer storage warehouse passes through described automatic conveying equipment to the quantitative storehouse of described auxiliary material feed, when described electronic weighing balance two showed that polymer reaches technological requirement weight, described electric control system was sent and is stopped the feed instruction; Described electric control system is sent the feed instruction to the quantitative storehouse of described major ingredient and the quantitative storehouse of described auxiliary material, and the quantitative storehouse of described major ingredient and the quantitative storehouse of described auxiliary material are put into raw material in the described batch mixer one by described charging aperture one; Feed intake finish after, described electric control system is sent instruction, beginning described raw material rationing step next time;
(2) combined type batch mixing step: the glass fibre that drops into technological requirement weight to described dog-house; Described electric control system is sent first batch mixing instruction to described batch mixer one, described agitator is worked at the beginning, first mixing time is set at 4～15 minutes, after described first mixing time arrives, described electric control system is sent to described batch mixer one and is stopped first batch mixing instruction, and described agitator one quits work; Described electric control system is sent the feed instruction to described batch mixer one, and described batch mixer one is opened described drain hole one and dropped into first compound by described charging aperture two to described batch mixer two; After dropping into first compound and finishing, described electric control system is sent the feed instruction to the quantitative storehouse of described major ingredient and the quantitative storehouse of described auxiliary material, and after raw material fed intake and finishes, described electric control system was sent first batch mixing instruction next time to described batch mixer one; After first compound drops into described batch mixer two, described electric control system is sent the rerolling instruction to described batch mixer two, described agitator two is started working, the rerolling time set is 4～15 minutes, after the described rerolling time arrives, described electric control system is sent to described batch mixer two and is stopped the rerolling instruction, and described agitator two quits work; Described electric control system is sent the feed instruction to described batch mixer two, and described batch mixer two is opened described drain hole two and dropped into compound to described material stock storehouse by described automatic conveying equipment; After described compound fed intake and finishes, described electric control system was sent instruction, and beginning is described combined type batch mixing step next time; Described first mixing time is identical numerical value with described rerolling time set;
(3) compound supply step: described electric control system is sent the feed instruction to described material stock storehouse, described material stock storehouse is dropped into described compound by described automatic conveying equipment to described quantitative storehouse, when described electronic weighing balance three showed that described compound reaches technological requirement weight, described electric control system was sent to described material stock storehouse and is stopped the feed instruction; When described electric control system is sent the feed instruction to described quantitative storehouse, described quantitative storehouse feeds intake by the described charging aperture three of described batch mixing batcher to described first reactor, feed intake finish after, described electric control system is sent feed instruction next time to described material stock storehouse, the step that described material stock storehouse feeds intake to described quantitative storehouse is carried out in circulation; When the number of times that feeds intake to described quantitative storehouse when described material stock storehouse reaches the predefined numerical value of described electric control system, described electric control system is sent the feed instruction to described batch mixer, described batch mixer two feeds intake to described material stock storehouse again, and beginning is described compound supply step next time;
(4) constant temperature water supply step: described water temperature control inductor shows when the water temperature in the described water heating apparatus reaches technological requirement numerical value, warm water is transported in the insulating box stores, described electric control system is sent the quantitative case water supply of described warm water instruction to described insulating box, described insulating box is transported to warm water in the quantitative case of described warm water, when described electronic weighing balance four showed that the water yield reaches technological requirement weight, described electric control system was sent and is stopped the quantitative case water supply of described warm water instruction; Send when described first reactor supplied water instruction to the quantitative case of described warm water when described electric control system, the warm water of the quantitative case of described warm water feeds to described first reactor through described force (forcing) pump one pressurization back by described water jet, and water supply time was less than 20 seconds; After warm water was all confessed in the quantitative case of described warm water, described electric control system was sent again the quantitative case of described warm water to be supplied water to described insulating box and is instructed, and beginning is described constant temperature water supply step next time;
(5) whipping step: described electric control system is sent the feed instruction to described quantitative storehouse, described electric control system is sent the instruction of supplying water to the quantitative case of described warm water simultaneously, described electric control system is sent to described agitator three and is stirred instruction simultaneously, described agitator three begins to stir, mixing time is 4～6 minutes, and described compound and water form slurry; After described mixing time arrived, described electric control system was sent to described agitator three and is stopped to stir instruction, and described agitator three quits work; Described electric control system is sent the blowing instruction to described first reactor, and described slurry leaks in described second reactor by described drain hole three and described charging aperture four; Described electric control system is sent instruction, carries out described whipping step next time;
(6) blowing agent supply step: described electric control system is sent for the agent instruction to described blowing agent storage tank, described blowing agent storage tank is carried blowing agent by described blowing agent feed-line to described blowing agent distributor, when described electronic weighing balance five showed that foaming dosage reaches technological requirement weight, described electric control system was sent and is stopped for the agent instruction; When described electric control system is sent the instruction of injection blowing agent to described blowing agent injection device, whole blowing agents in the described blowing agent distributor spray to described second reactor by described blowing agent spout through described force (forcing) pump two pressurization backs, and the ejection time is in 3 seconds; Described electric control system is sent instruction, carries out described blowing agent supply step next time;
(7) reactions steps: after the described slurry of described whipping step leaked into described second reactor, described electric control system was sent to described agitator four and is stirred instruction, and described agitator four starts, and stirring the described slurry time is 3～6 minutes; After the described slurry time of described stirring arrives, described electric control system is sent to described blowing agent injection device and is sprayed the blowing agent instruction, whole blowing agents in the described blowing agent distributor spray to described second reactor by described blowing agent spout through described force (forcing) pump two pressurization backs, and the ejection time is in 3 seconds; Described slurry and described blowing agent react and formed the foaming body cement slurry in 30～120 seconds; Described electric control system is sent halt instruction to described agitator four, and described agitator four quits work; Described electric control system is sent the blowing instruction to described emptying door four, and described foaming body cement slurry leaks in the described moulding box; After blowing was finished, described electric control system was sent instruction, carried out reactions steps next time;
(8) moulding box forming step: after described moulding box was placed into the below of described second reactor along described moulding box guide rail, described foaming body cement slurry leaked into described moulding box, and described moulding box is shifted out along described cross moving track; Foaming body cement slurry after 3～8 hours in the described moulding box solidifies the formation light-weight wall material, can satisfy carrying, folded high requirement, and described moulding box continues to recycle.
9. the automatic production method of light-weight wall material according to claim 8 is characterized in that, described whipping step is identical with the used time of described reactions steps, is 4～8 minutes.
10. the automatic production method of light-weight wall material according to claim 8, it is characterized in that, utilize automatic production line as claimed in claim 3, in described raw material rationing step, when adding reclaimed materials, described electric control system is sent the feed instruction to described reclaimed materials automatic charging machine, and described reclaimed materials automatic charging machine is to the quantitative storehouse of described major ingredient feed, when described electronic weighing balance one demonstration met technological requirement weight, described electric control system was sent and is stopped the feed instruction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310286378.8A CN103341908B (en) | 2013-07-10 | 2013-07-10 | Automated production line and automated production method of light-weight wall material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310286378.8A CN103341908B (en) | 2013-07-10 | 2013-07-10 | Automated production line and automated production method of light-weight wall material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103341908A true CN103341908A (en) | 2013-10-09 |
| CN103341908B CN103341908B (en) | 2015-03-11 |
Family
ID=49276757
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310286378.8A Expired - Fee Related CN103341908B (en) | 2013-07-10 | 2013-07-10 | Automated production line and automated production method of light-weight wall material |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103341908B (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103660036A (en) * | 2013-12-10 | 2014-03-26 | 中联重科股份有限公司 | Feeding control method and device and feeding system of dry-mixed mortar production line |
| CN106956355A (en) * | 2017-04-28 | 2017-07-18 | 四川美霖科技有限责任公司 | A kind of production system and its control method for automating gypsum lightweight hollow partition board |
| CN108568891A (en) * | 2017-03-13 | 2018-09-25 | 四川国正环保科技有限公司 | Light wall board product line control system and control method |
| CN108724435A (en) * | 2017-04-24 | 2018-11-02 | 北新集团建材股份有限公司 | A kind of control method of plasterboard formation system |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20080273415A1 (en) * | 2007-05-02 | 2008-11-06 | Jonel Engineering | Apparatus and method for producing concrete |
| CN201320803Y (en) * | 2008-12-31 | 2009-10-07 | 朱桂华 | Automatic proportioning and feed system for production of gypsum-based wall material |
| CN101554751A (en) * | 2009-05-26 | 2009-10-14 | 南阳天意保温耐火材料有限公司 | Production line of inorganic light weight thermal insulation composite mortar drier and production process thereof |
| CN202572586U (en) * | 2012-03-20 | 2012-12-05 | 南京天印科技有限公司 | Automatic production line for producing foam cement plates |
| CN202640529U (en) * | 2012-05-09 | 2013-01-02 | 丹东市兄弟建材有限公司 | Automatic injection machine for foamed cement slurry |
| CN203344185U (en) * | 2013-07-10 | 2013-12-18 | 丹东市兄弟建材有限公司 | Automatic production line of light wall material |
-
2013
- 2013-07-10 CN CN201310286378.8A patent/CN103341908B/en not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20080273415A1 (en) * | 2007-05-02 | 2008-11-06 | Jonel Engineering | Apparatus and method for producing concrete |
| CN201320803Y (en) * | 2008-12-31 | 2009-10-07 | 朱桂华 | Automatic proportioning and feed system for production of gypsum-based wall material |
| CN101554751A (en) * | 2009-05-26 | 2009-10-14 | 南阳天意保温耐火材料有限公司 | Production line of inorganic light weight thermal insulation composite mortar drier and production process thereof |
| CN202572586U (en) * | 2012-03-20 | 2012-12-05 | 南京天印科技有限公司 | Automatic production line for producing foam cement plates |
| CN202640529U (en) * | 2012-05-09 | 2013-01-02 | 丹东市兄弟建材有限公司 | Automatic injection machine for foamed cement slurry |
| CN203344185U (en) * | 2013-07-10 | 2013-12-18 | 丹东市兄弟建材有限公司 | Automatic production line of light wall material |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103660036A (en) * | 2013-12-10 | 2014-03-26 | 中联重科股份有限公司 | Feeding control method and device and feeding system of dry-mixed mortar production line |
| CN103660036B (en) * | 2013-12-10 | 2015-09-16 | 中联重科股份有限公司 | Feeding control method and device and feeding system of dry-mixed mortar production line |
| CN108568891A (en) * | 2017-03-13 | 2018-09-25 | 四川国正环保科技有限公司 | Light wall board product line control system and control method |
| CN108724435A (en) * | 2017-04-24 | 2018-11-02 | 北新集团建材股份有限公司 | A kind of control method of plasterboard formation system |
| CN108724435B (en) * | 2017-04-24 | 2019-09-13 | 北新集团建材股份有限公司 | A kind of control method of plasterboard formation system |
| CN106956355A (en) * | 2017-04-28 | 2017-07-18 | 四川美霖科技有限责任公司 | A kind of production system and its control method for automating gypsum lightweight hollow partition board |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103341908B (en) | 2015-03-11 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103341908B (en) | Automated production line and automated production method of light-weight wall material | |
| CN103626436B (en) | A kind of Fireproof thermal insulation mortar production technique and production equipment | |
| CN101743104A (en) | Systems and methods for a controlled process for producing mixtures of lightweight construction materials and systems for automatic production of lightweight bricks | |
| CN202572586U (en) | Automatic production line for producing foam cement plates | |
| CN206201198U (en) | A kind of special foam concrete fully-automatic production process equipment of laboratory | |
| CN205364193U (en) | Cement fire prevention foam thermal insulation board production line | |
| KR20090050384A (en) | Tne traveling manufacturing equipment of the foaming concrete | |
| CN203344185U (en) | Automatic production line of light wall material | |
| CN204398146U (en) | The automatic matching device of a kind of construction site cement mixing equipment | |
| CN104118050A (en) | Three-dimensional mixing and stirring mechanism for cement foamed heat insulation board | |
| CN112405820B (en) | Special light concrete production device and process | |
| CN102632538A (en) | Combined type multifunctional foam slurry core filling method | |
| CN206982997U (en) | concrete batching stirring system | |
| CN203156934U (en) | Stereoscopic mixed material stirring mechanism for cement foamed insulation boards | |
| CN113733300A (en) | Full-automatic flow line production method of phosphogypsum building blocks | |
| KR20000052017A (en) | Method and structure of manufacturing a cellular concrete using a powdered forming agent | |
| KR101477561B1 (en) | Vermiculite using the Vermiculite panel manufacturing apparatus and manufacturing method systematized | |
| CN202983645U (en) | Automatic charging system | |
| CN216442816U (en) | Timing feeding device for concrete processing | |
| CN202753285U (en) | Full-automatic premixing device of cement and coal ash foaming insulation board | |
| CN102672797A (en) | Slip casting method of foam slurry heat-preservation wallboard | |
| CN211054047U (en) | Automatic preparation facilities of concrete sample | |
| CN114211621A (en) | Premixed mortar concrete production equipment capable of improving strength and production efficiency | |
| CN102700001A (en) | Grout producing machine for foam concrete | |
| CN203317502U (en) | Combined-type multifunctional foaming and grouting machine for producing foam slurry thermal-insulating wallboards |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150311 |