CN103963151A - Brine continuous supplying system for lightweight magnesite cement wallboard - Google Patents
Brine continuous supplying system for lightweight magnesite cement wallboard Download PDFInfo
- Publication number
- CN103963151A CN103963151A CN201310030335.3A CN201310030335A CN103963151A CN 103963151 A CN103963151 A CN 103963151A CN 201310030335 A CN201310030335 A CN 201310030335A CN 103963151 A CN103963151 A CN 103963151A
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- CN
- China
- Prior art keywords
- valve
- bittern
- brine
- controller
- signal
- 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.)
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B28—WORKING CEMENT, CLAY, OR STONE
- B28B—SHAPING CLAY OR OTHER CERAMIC COMPOSITIONS; SHAPING SLAG; SHAPING MIXTURES CONTAINING CEMENTITIOUS MATERIAL, e.g. PLASTER
- B28B13/00—Feeding the unshaped material to moulds or apparatus for producing shaped articles; Discharging shaped articles from such moulds or apparatus
- B28B13/02—Feeding the unshaped material to moulds or apparatus for producing shaped articles
Abstract
The invention belongs to the field of industrial manufacturing material supply, and in particular relates to a brine continuous supplying system for a lightweight magnesite cement wallboard. The brine continuous supplying system comprises a raw water pool, wherein a water outlet of the raw water pool is connected with a raw water pump; a water outlet of the raw water pump is connected with water inlets of brine tanks through a raw water valve; stirrers and feeders are arranged on the brine tanks; the system comprises two sets of the brine tanks; two brine valve outlets of the two sets of the brine tanks are connected; in each distribution unit, a brine dividing valve is connected with the brine valves; the brine dividing valve is connected with a flow meter through the brine pump; the flow meter is connected with a water injection pipe; each of the distribution units is further internally provided with a liquid auxiliary device and a liquid level meter. In the system, the two brine tanks are connected with the distribution units, so that the two brine tanks can supply the brine alternatively, and the brine raw material for follow-up production can be continuously supplied. The distribution unit can be arranged at different places to ensure continuous production.
Description
Technical field
The invention belongs to industrial production material and supply with field, be specifically related to a kind of magnesia cement Light trabs bittern continuous-flow system.
Background technology
In present magnesia cement Light trabs process, bittern and other auxiliary liquid, for requisite raw material in producing, mostly are manual operation in current production.There is very large randomness in manual operation, greatly affects end product quality.There is harmony problem in manual operation simultaneously, is also not easy to reach the continuity of production, and slightly step is not caught up with will cause to shut down and waited for.Also there is the problem that labour intensity is large in manual operation.
Summary of the invention
A kind of magnesia cement Light trabs bittern continuous-flow system that the present invention is directed to above-mentioned weak point and provide.The present invention realizes like this, a kind of magnesia cement Light trabs bittern continuous-flow system, comprise former pond, former pond outlet is connected and draws with raw water pump A, raw water pump A delivery port is connected with bittern tank A water inlet by former water valve A, agitator A and feeder A are set on bittern tank A, and bittern tank A is connected with bittern valve B by bittern valve A; Liquid level gauge A is connected with controller signals; Former pond outlet is connected and draws with raw water pump B, and raw water pump B delivery port is connected with bittern tank B water inlet by former water valve B, and agitator B and feeder B are set on bittern tank B, and bittern tank B is connected with bittern valve A by bittern valve B; In cloth material unit A, a point halogen valve is connected with bittern valve A and bittern valve B, and a point halogen valve is connected with flowmeter through brine pump, and flowmeter is connected with sparge pipe, and auxiliary liquid device is also set in cloth material unit A; Liquid level gauge B is connected with controller signals.
For raising the efficiency, system also arranges cloth unit B and is connected with bittern valve B and bittern valve A simultaneously.Produce in enormous quantities for meeting, bittern valve B can also connect more than 1 cloth material unit after being connected with bittern valve A simultaneously simultaneously.
Magnesia cement Light trabs bittern continuous-flow system of the present invention, also comprises controller, and raw water pump A is connected with controller signals; Former water valve A is magnetic valve, is connected with controller signals; Agitator A is connected with controller signals; Dosage unit A is connected with controller signals; Bittern valve A is that magnetic valve is connected with control device signal; Raw water pump B is connected with controller signals; Former water valve B is magnetic valve, is connected with controller signals; Agitator B is connected with controller signals; Dosage unit B is connected with controller signals; Bittern valve B is that solenoid valve controller signal connects; Dividing halogen valve is magnetic valve, is connected with controller signals; Brine pump is connected with controller signals; Auxiliary liquid device is connected with controller signals.
Magnesia cement Light trabs bittern continuous-flow system of the present invention, adopt two bittern tanks to be connected with cloth material unit, after in a bittern tank, bittern material uses, by another bittern tank supply subsequent production, the bittern tank that is simultaneously finished material is prepared material.Supplied in turn by two bittern tanks, subsequent production bittern raw material can uninterruptedly be supplied.Cloth material unit can arrange many places, all can produce continuously.
Brief description of the drawings
Fig. 1 is system diagram of the present invention
In accompanying drawing: the former pond of 1-, 21-raw water pump A, the former water valve A of 22-, 23-bittern tank A, 24-agitator A, 25-liquid level gauge A, 26-feeder A, 27-bittern valve A, 3-cloth material unit A, 31-divides halogen valve, 32-brine pump, 33-flowmeter, 34-sparge pipe, the auxiliary liquid device of 35-, 4-cloth unit B, 51-raw water pump B, the former water valve B of 52-, 53-bittern tank B, 54-agitator B, 55-liquid level gauge B, 56-feeder B, 57-bittern valve B, 6-controller.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the present invention is described in further detail, but the present invention is not limited to following embodiment, any change of making in the present embodiment principle or replacement scheme, all fall among the scope of protection of present invention.
By reference to the accompanying drawings 1, a kind of magnesia cement Light trabs bittern continuous-flow system, comprise former pond 1, former pond 1 delivery port is connected and draws with raw water pump A21, raw water pump A21 delivery port is connected with bittern tank A23 water inlet by former not valve A22, agitator A24 and feeder A26 are set on bittern tank A23, and bittern tank A23 is connected with bittern valve B57 by bittern valve A27; Liquid level gauge A25 is connected with controller 6 signals; Former pond 1 delivery port is connected and draws with raw water pump B51, raw water pump B51 delivery port is connected with bittern tank B53 water inlet by former water valve B52, agitator B54 and feeder B56 are set on bittern tank B53, and bittern tank B53 is connected with bittern valve A27 by bittern valve B57; In cloth material unit A3, a point halogen valve 31 is connected with bittern valve A27 and bittern valve B57, and a point halogen valve 31 is connected with flowmeter 33 through brine pump 32, and flowmeter 33 is connected with sparge pipe 34, and auxiliary liquid device 35 is also set in cloth material unit A3; Liquid level gauge B55 is connected with controller 6 signals.
For raising the efficiency, system also arranges cloth unit B 4 and is connected with bittern valve B57 and bittern valve A27 simultaneously.Produce in enormous quantities for meeting, bittern valve B57 can also connect more than 1 cloth material list after being connected with bittern valve A27 simultaneously simultaneously
Unit.
Magnesia cement Light trabs bittern continuous-flow system of the present invention, also comprises controller 6, and raw water pump A21 is connected with controller 6 signals; Former not valve A22 is magnetic valve, is connected with controller 6 signals; Agitator A24 is connected with controller 6 signals; Dosage unit A is connected with controller 6 signals; Bittern valve A27 is that magnetic valve is connected with control device signal; Raw water pump B51 is connected with controller 6 signals; Former water valve B52 is magnetic valve, is connected with controller 6 signals; Agitator B54 is connected with controller 6 signals; Dosage unit B is connected with controller 6 signals; Bittern valve B57 is that solenoid valve controller 6 signals connect; Dividing halogen valve 31 is magnetic valve, is connected with controller 6 signals; Brine pump 32 is connected with controller 6 signals; Auxiliary liquid device 35 is connected with controller 6 signals.
When in use, raw water pump A21 pumps into former water to bittern tank A23, and feeder A26 adds needed batching in bittern tank, agitator A24 starts work, mixed liquor in bittern tank A23 is stirred, stirred rear agitator and quit work, in bittern valve A27, bittern is ready to complete.Meanwhile, raw water pump B51 pumps into former water to bittern tank B53, and feeder B56 adds needed batching in bittern tank, agitator B54 starts work, mixed liquor in bittern tank B53 is stirred, stirred rear agitator and quit work, in bittern valve A27, bittern is ready to complete.Single bittern tank can be supplied separately cloth material unit and use.Also bittern valve A27 and bittern valve B57 outlet end can be linked together, bittern valve A27 opens when different with bittern valve B57, when supply bittern, only can there is the supply of a bittern tank, by the open and-shut mode of conversion bittern valve A27 and bittern valve B57, can ensure the continuity of subordinate's bittern supply.Cloth material unit can arrange one group, also can arrange many groups, all can ensure that bittern is without interruption, and cloth material unit can continuous operation.In the time being provided with controller 6, the startup of all pumps and valve stops all being controlled by controller 6, realizes the automation of producing.
Claims (4)
1. a magnesia cement Light trabs bittern continuous-flow system, it is characterized in that comprising former pond (1), former pond (1) delivery port and raw water pump A(21) be connected and draw, raw water pump A(21) delivery port is by former water valve A(22) with bittern tank A(23) water inlet is connected, bittern tank A(23) on agitator A(24 is set) and feeder A(26), bittern tank A(23) by bittern valve A(27) with bittern valve B(57) be connected; Former pond (1) delivery port and raw water pump B(51) be connected and draw, raw water pump B(51) delivery port is by former water valve B(52) with bittern tank B(53) water inlet is connected, bittern tank B(53) on agitator B(54 is set) and feeder B(56), bittern tank B(53) by bittern valve B(57) with bittern valve A(27) be connected; Cloth material unit A(3) in point halogen valve (31) and bittern valve A(27) and bittern valve B(57) be connected, divide halogen valve (31) to be connected with flowmeter (33) through brine pump (32), flowmeter (33) is connected with sparge pipe (34), cloth material unit A(3) in auxiliary liquid device (35) is also set.
2. magnesia cement Light trabs bittern continuous-flow system according to claim 1, is characterized in that also comprising cloth unit B (4) and bittern valve B(57) and bittern valve A(27) be connected simultaneously.
3. magnesia cement Light trabs bittern continuous-flow system according to claim 1, it is characterized in that cloth material unit be greater than 2 groups respectively with bittern valve B(57) and bittern valve A(27) be connected simultaneously.
4. magnesia cement Light trabs bittern continuous-flow system according to claim 1 and 2, is characterized in that also comprising controller (6), raw water pump A(21) be connected with controller (6) signal; Former water valve A(22) be magnetic valve, be connected with controller (6) signal; Agitator A(24) be connected with controller (6) signal; Dosage unit A is connected with controller (6) signal; Bittern valve A(27) be that magnetic valve is connected with control device signal; Liquid level gauge A(25) be connected with controller (6) signal; Raw water pump B(51) be connected with controller (6) signal; Former water valve B(52) be magnetic valve, be connected with controller (6) signal; Agitator B(54) be connected with controller (6) signal; Dosage unit B is connected with controller (6) signal; Bittern valve B(57) be that solenoid valve controller (6) signal connects; Liquid level gauge B(55) be connected with controller (6) signal; Dividing halogen valve (31) is magnetic valve, is connected with controller (6) signal; Brine pump (32) is connected with controller (6) signal; Auxiliary liquid device (35) is connected with controller (6) signal.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310030335.3A CN103963151A (en) | 2013-01-28 | 2013-01-28 | Brine continuous supplying system for lightweight magnesite cement wallboard |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310030335.3A CN103963151A (en) | 2013-01-28 | 2013-01-28 | Brine continuous supplying system for lightweight magnesite cement wallboard |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103963151A true CN103963151A (en) | 2014-08-06 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310030335.3A Pending CN103963151A (en) | 2013-01-28 | 2013-01-28 | Brine continuous supplying system for lightweight magnesite cement wallboard |
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Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH1177654A (en) * | 1997-09-09 | 1999-03-23 | Kubota Corp | Cement slurry supplying apparatus for flow-on molding method |
| CN101386517A (en) * | 2008-10-27 | 2009-03-18 | 陈小石 | Foaming magnesite compound material and processing method thereof |
| CN201511430U (en) * | 2009-09-11 | 2010-06-23 | 佛山市南海新元素板业有限公司 | Water diverging closed cycle system for calcium silicate board production |
| CN102189597A (en) * | 2010-03-02 | 2011-09-21 | 于永久 | Production line for producing wallboard and technological method thereof |
| CN102296712A (en) * | 2011-06-17 | 2011-12-28 | 山东华德隆建材科技有限公司 | Ultra-thin stone phenolic foam composite board |
| CN102493567A (en) * | 2011-12-30 | 2012-06-13 | 广东亿健绿色住宅材料工业有限公司 | Production method for composite thermal insulation boards |
| CN203125687U (en) * | 2013-01-28 | 2013-08-14 | 四川大广厦机械设备有限公司 | Magnesia cement light wallboard brine continuous feeding system |
-
2013
- 2013-01-28 CN CN201310030335.3A patent/CN103963151A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH1177654A (en) * | 1997-09-09 | 1999-03-23 | Kubota Corp | Cement slurry supplying apparatus for flow-on molding method |
| CN101386517A (en) * | 2008-10-27 | 2009-03-18 | 陈小石 | Foaming magnesite compound material and processing method thereof |
| CN201511430U (en) * | 2009-09-11 | 2010-06-23 | 佛山市南海新元素板业有限公司 | Water diverging closed cycle system for calcium silicate board production |
| CN102189597A (en) * | 2010-03-02 | 2011-09-21 | 于永久 | Production line for producing wallboard and technological method thereof |
| CN102296712A (en) * | 2011-06-17 | 2011-12-28 | 山东华德隆建材科技有限公司 | Ultra-thin stone phenolic foam composite board |
| CN102493567A (en) * | 2011-12-30 | 2012-06-13 | 广东亿健绿色住宅材料工业有限公司 | Production method for composite thermal insulation boards |
| CN203125687U (en) * | 2013-01-28 | 2013-08-14 | 四川大广厦机械设备有限公司 | Magnesia cement light wallboard brine continuous feeding system |
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Application publication date: 20140806 |