CN203344185U - Automatic production line of light wall material - Google Patents
Automatic production line of light wall material Download PDFInfo
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- CN203344185U CN203344185U CN 201320407732 CN201320407732U CN203344185U CN 203344185 U CN203344185 U CN 203344185U CN 201320407732 CN201320407732 CN 201320407732 CN 201320407732 U CN201320407732 U CN 201320407732U CN 203344185 U CN203344185 U CN 203344185U
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Abstract
The utility model relates to a production line of a building wall material, and in particular relates to an automatic production line of a light wall material. According to the concrete technical scheme, the automatic production line of the light wall material comprises a quantitative raw material supply system, a combined type mixing system, a constant temperature water supply system, a foaming agent supply system, a mixing reaction system, an electrical control system, a molding box transporting device and a device connection walking board. The automatic production line has the advantages that the stability of the quality of the light wall material can be guaranteed, the production efficiency is improved and the industrialized production of the light wall material is realized.
Description
Technical field
The utility model relates to a kind of production line of building walling, particularly relates to a kind of automatic production line of light-weight wall material.
Background technology
The foam cement of China, be 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 " a kind of cellular foam thermal-insulation material for fireproof walls ", discloses a kind of cellular light material, is after tens kinds of materials such as cement, flyash are mixed, chemical reaction to occur to make it foam to make.In order to make constant product quality, necessary scientific formula, accurate quantitative analysis, the indices of any one material goes wrong, and all can exert an influence to product quality.Due to the sensitivity of chemistry reflection, when the height of foamed products reaches 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 honeycomb type foaming wall body materials ", discloses a kind of internal partition wall of honeycomb type foaming wall body materials, and honeycomb foam material is promoted to materials for wall by single fire-retardant heat-insulation material.This light-weight wall material, in the urgent need to an automatic production line, is controlled by scientific formula and automation, guarantees the stability of product quality, by automation, increases work efficiency, and realizes the industry industrialization.
The utility model content
The automatic production line that the purpose of this utility model is to provide a kind of light-weight wall material solves the problems referred to above.
Concrete technical scheme is:
A kind of automatic production line of light-weight wall material, comprise that raw material quantitative supply system, combined type mixing system, constant temperature water supply system, blowing agent supply system, stirring reaction system, electric control system, moulding box conveyer and equipment connection walk on stage;
Described raw material quantitative supply 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 quantitative storehouse, and described auxiliary material arranges electronic weighing balance two in quantitative storehouse; The quantitative storehouse of described major ingredient and the quantitative storehouse of described auxiliary material are set up in parallel; Described cement storage warehouse and described breeze storage warehouse are by described automatic conveying equipment to the quantitative storehouse of described major ingredient feed, and described flyash storage warehouse and described polymer storage warehouse pass through described automatic conveying equipment to the quantitative storehouse of described auxiliary material feed;
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 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 described charging aperture two feed to described batch mixer two by described drain hole one, the described drain hole two of described batch mixer two is by described automatic conveying equipment to described material stock storehouse feed, and described automatic conveying equipment is passed through to described quantitative storehouse feed in described material stock storehouse;
Described constant temperature water supply system comprises water heating apparatus, insulating box, the quantitative case of warm water and water output device; Water temperature is set in described water heating apparatus and controls inductor; 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 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 the first reactor, the second reactor; Described the first reactor comprises charging aperture three, agitator three and drain hole three, and described water jet is arranged in described the first reactor, and described quantitative storehouse is described charging aperture three feed to described the first reactor by described batch mixing batcher; Described the second reactor comprises charging aperture four, agitator four and drain hole four, described blowing agent spout is arranged in described the second reactor, described the second reactor is positioned at the below of described the first reactor, and the described drain hole three of described the first reactor is relative with the described charging aperture four of described the second reactor;
Described electric control system comprises operating console, and described operating console is placed on described equipment connection walks on stage; Described operating console comprises microcomputer and measuring instrument, by the described system of sensor and other, is connected;
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 quantitative supply 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 the first reactor and described the 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 described insulating box, so that the temperature of blowing agent reaches the equilibrium temperature the same with water in 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 processed.
Above-mentioned agitator one～tetra-can be the rotating vane structure, also can realize the structure of agitating function for other.
The automatic production line of light-weight wall material of the present utility model, its production method is carried out following steps:
One, raw material quantitative supply step: the program of setting according to electric control system, 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 shows that cement reaches technological requirement weight, described electric control system is 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 shows that breeze reaches technological requirement weight, described electric control system is 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 shows that flyash reaches technological requirement weight, described electric control system is 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 shows that polymer reaches technological requirement weight, described electric control system is 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 described batch mixer one; After having fed intake, described electric control system is sent instruction, starts described raw material quantitative supply step next time; This step is carried out in circulation.
Two, 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 as 4～15 minutes, the batch mixing amount can be for more than 2T, after described first mixing time arrives, described electric control system is sent and is stopped first batch mixing instruction to described batch mixer one, 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 completing, 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 has fed intake, described electric control system is 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 is set as 4～15 minutes, after the described rerolling time arrives, described electric control system is sent and is stopped the rerolling instruction to described batch mixer two, 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 by described automatic conveying equipment to described material stock storehouse; After described compound has fed intake, described electric control system is sent instruction, starts described combined type batch mixing step next time; Described first mixing time is set as identical numerical value with the described rerolling 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, described material stock storehouse is dropped into described compound by described automatic conveying equipment to described quantitative storehouse, when described electronic weighing balance three shows that described compound reaches technological requirement weight, described electric control system is sent and is stopped the feed instruction to described material stock storehouse; When described electric control system is sent the feed instruction to described quantitative storehouse, by described batch mixing batcher, the described charging aperture three to described the first reactor feeds intake in described quantitative storehouse, after having fed intake, described electric control system is sent feed instruction next time to described material stock storehouse, loops the step that described material stock storehouse feeds intake to described quantitative storehouse; When the number of times fed intake to described quantitative storehouse when described material stock storehouse reaches the predefined numerical value of described electric control system, the desired compound weight in described not quantitative storehouse of the material stock in described material stock storehouse now, 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, starts described compound supply step next time; This step is carried out in circulation.
Four, constant temperature water supply step: described water temperature is controlled inductor and is shown when the interior water temperature of described water heating apparatus reaches technological requirement numerical value, artificial means or autocontrol method are transported to warm water in 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 shows that the water yield reaches technological requirement weight, described electric control system is sent and is stopped the quantitative case water supply of described warm water instruction; When described electric control system is sent described the first reactor water supply instruction to the quantitative case of described warm water, the warm water of the quantitative case of described warm water feeds to described the first reactor by described water jet after described force (forcing) pump one pressurization, and water supply time is less than 20 seconds; After warm water is all confessed in the quantitative case of described warm water, described electric control system is sent again the quantitative case water supply of described warm water instruction to described insulating box, starts described constant temperature water supply step next time; This step is carried out in circulation.
Five, whipping step: described electric control system is sent the feed instruction to described quantitative storehouse, described electric control system is sent the water supply instruction to the quantitative case of described warm water simultaneously, described electric control system is sent the stirring instruction to described agitator three simultaneously, described agitator three starts to stir, mixing time is 4～6 minutes, and described compound and water form slurry; After described mixing time arrives, described electric control system is sent and is stopped stirring instruction to described agitator three, and described agitator three quits work; Described electric control system is sent the blowing instruction to described the first reactor, and described slurry leaks in described the 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.
Six, 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 shows that foaming dosage reaches technological requirement weight, described electric control system is 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 described blowing agent distributor spray to described the second reactor by described blowing agent spout after described force (forcing) pump two pressurizations, 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.
Seven, reactions steps: after the described slurry of described whipping step leaks into described the second reactor, described electric control system is sent the stirring instruction to described agitator four, 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 and is sprayed the blowing agent instruction to described blowing agent injection device, whole blowing agents in described blowing agent distributor spray to described the second reactor by described blowing agent spout after described force (forcing) pump two pressurizations, and the ejection time is in 3 seconds; Described slurry and described blowing agent react and within 30～120 seconds, form the foaming body cement 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 cement slurry leaks in described moulding box; After blowing completes, described electric control system is sent instruction, carries out reactions steps next time; This step is carried out in circulation.
Eight, moulding box forming step: artificial means or autocontrol method, described moulding box is placed into to the below of described the 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 described moulding box solidifies the formation light-weight wall material, can meet carrying, folded high requirement, and described moulding box continues to recycle.
In this production method, described whipping step is preferably identical with the described reactions steps time used, is 4～8 minutes.
In this production method, when having reclaimed materials to add, in described raw material quantitative supply 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 shows that reclaimed materials meets technological requirement weight, described electric control system is sent and is stopped the feed instruction.
Application of the present utility model, can meet 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 honeycomb type foaming wall body materials ".
Advantage of the present utility model:
1, automatic production line of the present utility model 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 utility model 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 batch mixer of automatic production line of the present utility model, together compatible the dry powder blend of different densities, make the various uniform ingredients of mixed powder consistent, guaranteed light-weight wall material density and quality homogeneity.And shortened working time of stirring reaction system, increase work efficiency.
4, second metering is carried out to mixed powder in the quantitative storehouse of the batch mixing of automatic production line of the present utility model, guaranteed the accuracy of materials in the first reactor and the second reactor, guarantee the controllability of foamable reaction, guarantee the dry density of light-weight wall material and the stability of quality.
5, constant temperature water supply system of the present utility model, provide the water of constant-temperature quantitative, strictly controls temperature and the consumption of water, ensured uniformity and the stability of slurry, ensured the stability of foamable reaction simultaneously.
6, blowing agent supply system of the present utility model, the blowing agent distributor, to the foaming agent consumption accurate measurement, has guaranteed the stability of foamable reaction; Force (forcing) pump and a plurality of blowing agent spout are controlled blowing agent with uniform method and the fastest speed, both equivalent, equidistant, etc. the time, injection method simultaneously, be injected in the second reactor, guaranteed the consistent in time synchronous of foamable reaction, the light-weight wall material air entrapment size of producing is even, consistent in density.
7, stirring reaction system of the present utility model is carried out secondary agitation, has guaranteed that slurry stirs fully, and the light-weight wall material air entrapment of production size is accurately even, consistent in density.
8, automatic production line of the present utility model, the three dimensional designs of the first reactor and the second reactor is a compound mixing procedure, guarantees that two reactor reflecting times are identical, has not only guaranteed product quality but also the operating efficiency be doubled.
9, reclaimed materials automatic charging machine of the present utility model, 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, saved raw material, reduced product cost, realized 0 discharge.
10, pressure relief device of the present utility model, 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 utility model inside, the light-weight wall material of production meets the modulus design of building block, has effectively improved the product row yielding.
12, automatic production line of the present utility model, 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.
The accompanying drawing explanation
The automatic production line that Fig. 1 is light-weight wall material is faced structural representation
The automatic production line plan structure schematic diagram that Fig. 2 is light-weight wall material
The specific embodiment
As shown in Figure 1, 2, the automatic production line of light-weight wall material, comprise that raw material quantitative supply system, combined type mixing system, constant temperature water supply system, blowing agent supply system, stirring reaction system, electric control system, moulding box conveyer and equipment connection walk on stage 15.
Described raw material quantitative supply 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, the interior electronic weighing balance one that arranges in the quantitative storehouse 5 of described major ingredient, the interior electronic weighing balance two that arranges in the quantitative storehouse 6 of described auxiliary material; 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; The interior electronic weighing balance three that arranges in the quantitative storehouse 9 of described batch mixing; 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 described charging aperture two feed to described batch mixer 2 25 by described drain hole one, the described drain hole two of described batch mixer 2 25 is by described automatic conveying equipment 22 to described material stock storehouse 8 feed, and described automatic conveying equipment 22 is passed through to described quantitative storehouse 9 feed in described material stock storehouse 8.
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; The interior water temperature that arranges of described water heating apparatus 16 is controlled inductor; The interior electronic weighing balance four that arranges of the quantitative case 21 of described warm water; 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 described blowing agent distributor 19 passes through in described insulating box 17, spirals and is arranged in described insulating box 17; The interior electronic weighing balance five that arranges of described blowing agent distributor 19; 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 the first reactor 11, the second reactor 12; Described the first reactor 11 comprises material mouth three, agitator three and drain hole three, and described water jet is arranged in described the first reactor 11, and described quantitative storehouse 9 is described charging aperture one feed to described the first reactor 11 by described batch mixing batcher 10; Described the second reactor 12 comprises charging aperture four, agitator four and drain hole four, described blowing agent spout is arranged in described the second reactor 12, described the second reactor 12 is positioned at the below of described the first reactor 11, and the described emptying door one of described the first reactor is relative with the described charging aperture two of described the second reactor.
Described electric control system comprises operating console 13, and described operating console 13 is placed in described equipment connection and walks on stage on 15; Described operating console 13 comprises microcomputer and measuring instrument, by the described system of sensor and other, is connected.
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.
Claims (7)
1. the automatic production line of a light-weight wall material, it is characterized in that, comprise that raw material quantitative supply system, combined type mixing system, constant temperature water supply system, blowing agent supply system, stirring reaction system, electric control system, moulding box conveyer and equipment connection walk on stage;
Described raw material quantitative supply 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 quantitative storehouse, and described auxiliary material arranges electronic weighing balance two in quantitative storehouse; The quantitative storehouse of described major ingredient and the quantitative storehouse of described auxiliary material are set up in parallel; Described cement storage warehouse and described breeze storage warehouse are by described automatic conveying equipment to the quantitative storehouse of described major ingredient feed, and described flyash storage warehouse and described polymer storage warehouse pass through described automatic conveying equipment to the quantitative storehouse of described auxiliary material feed;
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 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 described charging aperture two feed to described batch mixer two by described drain hole one, the described drain hole two of described batch mixer two is by described automatic conveying equipment to described material stock storehouse feed, and described automatic conveying equipment is passed through to described quantitative storehouse feed in described material stock storehouse;
Described constant temperature water supply system comprises water heating apparatus, insulating box, the quantitative case of warm water and water output device; Water temperature is set in described water heating apparatus and controls inductor; 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 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 the first reactor, the second reactor; Described the first reactor comprises charging aperture three, agitator three and drain hole three, and described water jet is arranged in described the first reactor, and described quantitative storehouse is described charging aperture three feed to described the first reactor by described batch mixing batcher; Described the second reactor comprises charging aperture four, agitator four and drain hole four, described blowing agent spout is arranged in described the second reactor, described the second reactor is positioned at the below of described the first reactor, and the described drain hole three of described the first reactor is relative with the described charging aperture four of described the second reactor;
Described electric control system comprises operating console, and described operating console is placed on described equipment connection walks on stage; Described operating console comprises microcomputer and measuring instrument, by the described system of sensor and other, is connected;
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 quantitative supply 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 the first reactor and described the 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 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.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320407732 CN203344185U (en) | 2013-07-10 | 2013-07-10 | Automatic production line of light wall material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320407732 CN203344185U (en) | 2013-07-10 | 2013-07-10 | Automatic production line of light wall material |
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| CN203344185U true CN203344185U (en) | 2013-12-18 |
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| CN 201320407732 Withdrawn - After Issue CN203344185U (en) | 2013-07-10 | 2013-07-10 | Automatic production line of light wall material |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103341908A (en) * | 2013-07-10 | 2013-10-09 | 丹东市兄弟建材有限公司 | Automated production line and automated production method of light-weight wall material |
| CN115008615A (en) * | 2022-07-04 | 2022-09-06 | 朱东敏 | Integrated production line for field mixing and construction for preparing green (ultra) high-performance concrete |
-
2013
- 2013-07-10 CN CN 201320407732 patent/CN203344185U/en not_active Withdrawn - After Issue
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103341908A (en) * | 2013-07-10 | 2013-10-09 | 丹东市兄弟建材有限公司 | Automated production line and automated production method of light-weight wall material |
| CN103341908B (en) * | 2013-07-10 | 2015-03-11 | 丹东市兄弟建材有限公司 | Automated production line and automated production method of light-weight wall material |
| CN115008615A (en) * | 2022-07-04 | 2022-09-06 | 朱东敏 | Integrated production line for field mixing and construction for preparing green (ultra) high-performance concrete |
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