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CN203222551U - Flexible multifunctional production equipment for calcium hydroxide - Google Patents

Flexible multifunctional production equipment for calcium hydroxide Download PDF

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CN203222551U
CN203222551U CN201320135894.6U CN201320135894U CN203222551U CN 203222551 U CN203222551 U CN 203222551U CN 201320135894 U CN201320135894 U CN 201320135894U CN 203222551 U CN203222551 U CN 203222551U
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machine
calcium hydroxide
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digestion
bin
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周政
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Abstract

一种氢氧化钙柔性多功能生产设备包括破碎机、原料仓、消解机、选粉机、雷蒙粉磨机、二次消化储料仓和成品仓,其特征在于所述的破碎机通过提升机和胶带输送机与原料仓连接,所述的原料仓经过电子计量称和胶带输送机与消解机连接,所述的消解机末端置有选粉机和雷蒙粉磨机,所述的二次消化储料仓通过刮板输送机、提升机和电子计量称与选粉机和雷蒙粉磨机串联,所述的成品仓前端有刮板输送机和提升机,后端有装包机。该氢氧化钙柔性多功能生产设备通过对原料仓、消解机、选粉机、雷蒙粉磨机及成品仓的设计、调整,实现了在一条生产线能根据原料和需要生产出不同要求的氢氧化钙粉体。

Figure 201320135894

A calcium hydroxide flexible multifunctional production equipment includes a crusher, a raw material bin, a digestion machine, a powder classifier, a Raymond mill, a secondary digestion storage bin, and a finished product bin, and is characterized in that the crusher is lifted The machine and the belt conveyor are connected with the raw material warehouse, and the raw material warehouse is connected with the digestion machine through the electronic weighing scale and the belt conveyor. The end of the digestion machine is equipped with a powder separator and a Raymond mill. The secondary digestion storage bin is connected in series with the powder classifier and Raymond mill through a scraper conveyor, hoist and electronic weighing scale. The front end of the finished product bin has a scraper conveyor and hoist, and a packing machine at the rear end. The calcium hydroxide flexible multi-functional production equipment realizes the production of hydrogen with different requirements according to raw materials and needs in one production line through the design and adjustment of raw material bins, digestion machines, powder separators, Raymond mills and finished product bins. Calcium oxide powder.

Figure 201320135894

Description

一种氢氧化钙柔性多功能生产设备A flexible multifunctional production equipment for calcium hydroxide

所属技术领域 Technical field

本实用新型是用于氢氧化钙生产的一种柔性多功能生产设备。  The utility model is a kind of flexible and multifunctional production equipment for calcium hydroxide production. the

背景技术 Background technique

一般的氢氧化钙生产企业目前大多都建在氧化钙生产厂,上游主要原料氧化钙受工艺、煅烧、原料质量、季节等因素变化质量波动大,更造成了氢氧化钙的生产线建设复杂化和多样化,目前的氢氧化钙生产设备还都很单纯,随着经济的发展对氢氧化钙的要求也越来越多样化,很多生产厂家找不到合适的生产设备和建设方案,更不能在一条生产线生产不同质量批次的产品,增加生产线有可能解决但同时又增加了人力、物力、材力非常不划算,为此特推出一种氢氧化钙柔性多功能生产设备来满足市场需求。  Most of the general calcium hydroxide production enterprises are currently built in calcium oxide production plants. The upstream main raw material calcium oxide is subject to changes in process, calcination, raw material quality, seasons and other factors. The quality fluctuates greatly, which makes the construction of calcium hydroxide production lines complicated and Diversification. The current calcium hydroxide production equipment is still very simple. With the development of the economy, the requirements for calcium hydroxide are becoming more and more diverse. Many manufacturers cannot find suitable production equipment and construction plans, let alone in A production line produces different quality batches of products. It is possible to solve the problem by adding production lines, but at the same time it increases manpower, material resources, and material resources. the

实用新型内容 Utility model content

一种氢氧化钙柔性多功能生产设备,能实现在同一条生产线上根据原料的不同生产不同品位的氢氧化钙粉体。设置了三个不同品位的原料仓调节不同原料的搭配, 采用了可拆分使用的单独变频控制的消解机消解不同品位要求的氢氧化钙粉体,设置了2套选粉装置对不同品位要求的氢氧化钙粉体进行选粉,增加了一个二次消化储料仓,对未完全消解的氧化钙进行再消解和储存,配套了三个不同品位的储料仓进行储料。  A calcium hydroxide flexible multifunctional production equipment can realize the production of calcium hydroxide powders of different grades according to different raw materials on the same production line. Three raw material warehouses with different grades are set up to adjust the mix of different raw materials. A detachable independent frequency conversion control digestion machine is used to digest calcium hydroxide powder with different grade requirements. Two sets of powder selection devices are set up to meet different grade requirements. The calcium hydroxide powder is selected for powder, and a secondary digestion storage bin is added to re-digest and store the incompletely digested calcium oxide, and three storage bins of different grades are equipped for storage. the

本实用新型解决其技术问题所采用的技术方案  The technical solution adopted by the utility model to solve its technical problems

通过一套破碎系统设置了三个原料仓,分别存储三种不同品位的氧化钙,每个料仓的底部都单独配置了一套电子计量输送秤,即可单独使用也可根据质量情况混搭使用,设备可根据下游的生产要求随意调节。  Three raw material bins are set up through a set of crushing system, which store three different grades of calcium oxide respectively. The bottom of each bin is equipped with a set of electronic weighing and conveying scales, which can be used alone or mixed according to the quality. , the equipment can be freely adjusted according to the downstream production requirements. the

采用可拆分使用的多级消解机来消解不同品位要求的氢氧化钙粉体,采用变频调速来控制不同消解要求时的一、二、三级消解机转速,PLC全自动物料双向跟踪法来调节不同品位氧化钙与水的配比,三级消解机具可用可不用的单独调节功能能满足不同品味氧化钙消化时间的需求。  The detachable multi-stage digestion machine is used to digest calcium hydroxide powder with different grade requirements, and the frequency conversion speed regulation is used to control the speed of the first, second, and third-stage digestion machines when different digestion requirements are required. PLC automatic material two-way tracking method To adjust the ratio of different grades of calcium oxide to water, the three-stage digestion machine can be used or not with a separate adjustment function to meet the needs of different grades of calcium oxide digestion time. the

经过可拆分使用的多级消解机消化的氢氧化钙粉体按成品质量要求的不同选粉要求也不同,本实用新型设置了二套选粉系统,具体有以下:  The calcium hydroxide powder digested by the detachable multi-stage digestion machine has different powder selection requirements according to the quality requirements of the finished product. The utility model has two sets of powder selection systems, which are as follows:

质量优等的消解机消化后的氢氧化钙粉体经刮板输送机18直接输送到旋风式选粉机19进行风选,风选后达到细度、白度等要求的粉体(细度一般大于325目)经提升机27直接进入精粉成品仓28,不合格的粗粉经提升机20进入二次消化储料仓22进行再消解备用。  The calcium hydroxide powder digested by the high-quality digestion machine is directly transported to the cyclone powder separator 19 through the scraper conveyor 18 for winnowing. greater than 325 mesh) directly enters the fine powder finished product bin 28 through the elevator 27, and the unqualified coarse powder enters the secondary digestion storage bin 22 through the elevator 20 for further digestion and standby. the

质量一般的消解机消化后的氢氧化钙粉体经刮板输送机18直接输送到雷蒙粉磨机24,调整雷蒙粉磨机24滚轮至闲置状态后开始选粉,细度、白度等达到要求的(一般150目-300目),经除尘器25负压吸收后直接有提升机27提升到刮板输送机30后进入普通成品仓29,不合格的粗粉从雷蒙粉磨机24的底部的旁开粗粉出口排出,经提升机20进入二次消化储料仓22再消解备用。  Calcium hydroxide powder digested by general quality digestion machines is directly transported to Raymond mill 24 via scraper conveyor 18, and after adjusting the rollers of Raymond mill 24 to the idle state, powder selection begins, fineness, whiteness After reaching the requirements (generally 150 mesh-300 mesh), after being absorbed by the negative pressure of the dust collector 25, it is directly lifted by the hoist 27 to the scraper conveyor 30 and then enters the ordinary finished product warehouse 29. The unqualified coarse powder is grinded from Raymond The coarse powder outlet of the bottom of the machine 24 is discharged, and enters the secondary digestion storage bin 22 through the hoist 20 and then digested for subsequent use. the

质量较差的消解机消化后的氢氧化钙粉体经刮板输送机18直接输送到雷蒙粉磨机24,调整雷蒙粉磨机24滚轮至工作状态后开始研磨与选粉,此时储存在二次消化储料仓22的经再进一步消化后的粗粉物料,经电子计量秤23计量后按比例再均匀输送到雷蒙粉磨机24一起研磨和选粉,细度等达到要求的(一般50目-150目),经提升机27直接 进入较差档成品仓32,不合格的粗粉也经提升机20进入二次消化储料仓22再消解循环备用。经过以上组合调整就实现了在一条生产线生产不同质量批次的产品。  Calcium hydroxide powder digested by the digestion machine with poor quality is directly transported to the Raymond mill 24 through the scraper conveyor 18, after adjusting the rollers of the Raymond mill 24 to the working state, grinding and powder selection are started. The further digested coarse powder material stored in the secondary digestion storage bin 22 is measured by the electronic weighing scale 23 and then uniformly transported to the Raymond mill 24 for grinding and powder selection, and the fineness meets the requirements. (generally 50 mesh-150 mesh), directly enter the poor grade finished product bin 32 through the hoist 27, and the unqualified coarse powder also enters the secondary digestion storage bin 22 through the hoist 20 and then digests and circulates for standby. After the above combination adjustments, it is possible to produce different quality batches of products in one production line. the

本实用新型的有益效果  Beneficial effects of the utility model

实现了在同一条生产线上能生产不同品位和要求的氢氧化钙粉体,提高了效率,减少了投资,降低了成本。  It realizes the production of calcium hydroxide powders of different grades and requirements on the same production line, which improves efficiency, reduces investment and reduces costs. the

附图说明 Description of drawings

图1是一种氢氧化钙柔性多功能生产设备示意图。  Fig. 1 is a schematic diagram of calcium hydroxide flexible multifunctional production equipment. the

其中1、氧化钙原料仓2、电子计量称3、提升机4、破碎机5、胶带输送机6、电子计量称7、优等品原料仓8、普通品原料仓9、较差品原料仓10、电子计量称11、电子计量称12、胶带输送机13、一级消解机14、卸料阀15、二级消解机16、消解机除尘器17、三级消解机18、刮板输送机19、旋风式选粉机20、提升机21、刮板输送机22、二次消化储料仓23、电子计量称24、雷蒙粉磨机25、除尘器26、刮板输送机27、提升机28、精粉成品仓29、普通成品仓30、刮板输送机31、装包机32、较差成品仓33、散罐车34、注水 阀35、变频调速电机  Among them: 1. Calcium oxide raw material warehouse 2. Electronic measuring scale 3. Elevator 4. Crusher 5. Belt conveyor 6. Electronic measuring scale 7. Superior product raw material warehouse 8. Ordinary product raw material warehouse 9. Inferior product raw material warehouse 10 , electronic measuring scale 11, electronic measuring scale 12, belt conveyor 13, first-level digestion machine 14, discharge valve 15, second-level digestion machine 16, digestion machine dust collector 17, third-level digestion machine 18, scraper conveyor 19 , cyclone powder separator 20, elevator 21, scraper conveyor 22, secondary digestion storage bin 23, electronic weighing scale 24, Raymond mill 25, dust collector 26, scraper conveyor 27, elevator 28. Fine powder finished product warehouse 29, ordinary finished product warehouse 30, scraper conveyor 31, packing machine 32, poor finished product warehouse 33, bulk tanker 34, water injection valve 35, frequency conversion speed regulation motor

具体实施方式 Detailed ways

分批次来自于原料仓1的氧化钙经电子计量称2计量后进入到破碎机4中进行破碎处理,将氧化钙破碎到5-10mm以下,有提升机3提升到胶带输送机5,胶带输送机5根据不同批次氧化钙质量的不同,分别输送到对应的原料仓7、8、9中储存待用,当下游需要优等品原料时开启电子计量称6和胶带输送机12进行计量和输送。当下游需要普通品原料时开启电子计量称10和胶带输送机12进行计量和输送,或者同时开启电子计量称6、11视化验结果情况进行一定的比例搭配后同时进行计量和输送到胶带输送机12。当下游需要较差品原料时开启电子计量称11和胶带输送机12进行计量和输送,当较差原料仓9的原料质量太差不能满足要求时,也可同时开启电子计量称10、11视化验结果情况进行一定的比例搭配后同时进行计量和输送到胶带输送机12完成输送。  Calcium oxide from raw material bin 1 in batches is measured by electronic weighing scale 2 and then enters crusher 4 for crushing treatment. The calcium oxide is crushed to a size below 5-10mm, and then lifted to belt conveyor 5 by hoist 3, and the belt The conveyor 5 is transported to the corresponding raw material bins 7, 8, and 9 according to the quality of different batches of calcium oxide, and is stored for use. When the downstream needs high-quality raw materials, the electronic weighing scale 6 and the belt conveyor 12 are used to measure and delivery. When the downstream needs ordinary raw materials, turn on the electronic weighing scale 10 and the belt conveyor 12 to measure and transport, or turn on the electronic weighing scale 6 and 11 at the same time, and then measure and transport them to the belt conveyor at the same time according to the test results. 12. When the raw materials of poor quality products are needed in the downstream, the electronic weighing scale 11 and the belt conveyor 12 are turned on for measuring and conveying. After the test results are matched in a certain proportion, they are simultaneously measured and transported to the belt conveyor 12 to complete the transport. the

当有优等品(氧化钙)原料,生产优质氢氧化钙精粉的方法是先开启PCL全自动控制系统,调整好电子计量 称6中的原料流量与经过注水阀34的水流量配比后自动打开,经电子计量称6计量后的原料有胶带输送机12输送到一级消解机13,同时注水阀34开启直接将水注入一级消解机13与原料反应,视消化和熟化的反应程度有变频器来分别调整一级、二级、三级的电机转速从而控制反应时间和过程,消解机产生的高温高湿粉尘有除尘器16收集后和消化机消化后的粉体一块有刮板输送机18输送到旋风式选粉机19进行选粉,合格的粉体(细度一般大于325目甚至更高)有刮板输送机26进入提升机27,有提升机27提升到刮板输送机30后直接进入精粉成品仓28进行储存,最后有装包机31装包出厂,选粉后不合格的粗粉或颗粒落入刮板输送机21,再有提升机20提升至二次消化储料仓22进行再消化和储存。  When there are high-quality (calcium oxide) raw materials, the method of producing high-quality calcium hydroxide fine powder is to first open the PCL automatic control system, adjust the ratio of the raw material flow in the electronic metering scale 6 to the water flow through the water injection valve 34, and then automatically Open, the raw materials measured by the electronic measuring scale 6 are transported to the first-level digestion machine 13 by the belt conveyor 12, and at the same time, the water injection valve 34 is opened to directly inject water into the first-level digestion machine 13 to react with the raw materials, depending on the reaction degree of digestion and aging. The frequency converter is used to adjust the motor speed of the primary, secondary, and tertiary motors to control the reaction time and process. The high-temperature and high-humidity dust generated by the digestion machine is collected by the dust collector 16 and conveyed by the scraper together with the powder digested by the digestion machine. The machine 18 is transported to the cyclone powder separator 19 for powder selection. The qualified powder (fineness is generally greater than 325 mesh or even higher) enters the elevator 27 by the scraper conveyor 26, and is lifted by the elevator 27 to the scraper conveyor. After 30, it directly enters the fine powder finished product warehouse 28 for storage, and finally there is a packing machine 31 to pack and leave the factory. After the powder is selected, the unqualified coarse powder or particles fall into the scraper conveyor 21, and then the hoist 20 is lifted to the secondary digestion storage. Silo 22 performs redigestion and storage. the

当生产普通品位氢氧化钙粉体时,先开启PCL全自动控制系统,调整好电子计量称10中的原料流量与经过注水阀34的水流量配比后自动打开,经电子计量称10计量后的原料有胶带输送机12输送到一级消解机13,或者开启电子计量称6、11视化验结果情况进行一定的比例搭配后调 整好与经过注水阀34的水流量配比后自动打开,经电子计量秤6和11分别计量后的原料有胶带输送机12输送到一级消解机13,同时注水阀34开启直接将水注入一级消解机13与原料反应,视消化和熟化的反应程度有变频器来分别调整一级、二级、三级的电机转速从而控制反应时间和过程,消解机产生的高温高湿粉尘有除尘器16收集后和消化机消化后的粉体一块有刮板输送机18输送到雷蒙粉磨机24进行选粉,此时的雷蒙粉磨机24的滚轮置于闲置状态,不进行挤压、研磨,细度、白度等达到要求的(一般150目-300目),经除尘器25负压吸收后直接有提升机27提升到刮板输送机30后进入普通成品仓29储存,最后有装包机31装包出厂,不合格的粗粉从雷蒙粉磨机24的底部的旁开粗粉出口排出(没有的需要在底部新开排出口),有提升机20进入二次消化储料仓22再消解备用。  When producing ordinary grade calcium hydroxide powder, first turn on the PCL automatic control system, adjust the ratio of the raw material flow in the electronic weighing scale 10 to the water flow through the water injection valve 34, and then open it automatically. The raw materials are transported to the first-level digestion machine 13 by the belt conveyor 12, or the electronic measuring scales 6 and 11 are matched according to the test results and adjusted to the water flow ratio of the water injection valve 34, and then opened automatically. The raw materials measured by the electronic weighing scales 6 and 11 are transported to the first-level digestion machine 13 by the belt conveyor 12, and at the same time, the water injection valve 34 is opened to directly inject water into the first-level digestion machine 13 to react with the raw materials, depending on the reaction degree of digestion and aging There is a frequency converter to adjust the motor speed of the first, second and third stages respectively to control the reaction time and process. The high-temperature and high-humidity dust generated by the digestion machine is collected by the dust collector 16 and the powder digested by the digestion machine is equipped with a scraper. Conveyor 18 transports to Raymond mill 24 for powder selection. At this time, the rollers of Raymond mill 24 are placed in an idle state without extrusion or grinding, and the fineness and whiteness meet the requirements (generally 150 Mesh-300 mesh), after being absorbed by the negative pressure of the dust collector 25, it is directly lifted by the hoist 27 to the scraper conveyor 30, and then enters the ordinary finished product warehouse 29 for storage. The coarse powder outlet is opened at the bottom of the powder mill 24 to discharge (if there is none, a new discharge outlet needs to be opened at the bottom), and the hoist 20 enters the secondary digestion storage bin 22 for further digestion and standby. the

生产要求不高质量较差的氢氧化钙粉体的方法是先开启PCL全自动控制系统,调整好电子计量称11中的原料流量与经过注水阀34的水流量配比后自动打开,经电子计量称11计量后的原料有胶带输送机12输送到一级消解机 13,同时注水阀34开启直接将水注入一级消解机13与原料反应,当较差原料仓9的原料质量太差不能满足要求时,也可同时开启电子计量称10、11视化验结果情况进行一定的比例搭配调整好与注水阀34的水流量配比后自动打开,经电子计量秤10和11分别计量后的原料有胶带输送机12输送到一级消解机13,同时注水阀34打开直接将水注入一级消解机13与原料反应,视消化和熟化的反应程度有变频器来分别调整一级、二级的电机转速从而控制反应时间和过程,因为大部分较差的氢氧化钙粉体对熟化程度、消解时间要求也不高,所以此时的三级消解机可以不参与工作,处于停止状态(有利于降低电耗、能耗),经一、二级消化后的粉体有二级消解机尾部的卸料阀14(没有的需要在底部新开排出口)直接落入刮板输送机18,有刮板输送机18直接输送到雷蒙粉磨机24进行研磨和选粉,消解机产生的高温高湿粉尘有除尘器16收集后和消化机消化后的粉体也一块有刮板输送机18输送到雷蒙粉磨机24进行选粉,此时雷蒙粉磨机24滚轮置于工作状态,对进入物料挤压、研磨和选粉,储存在二次消化储料仓22的经再进一步长时间消化后的各 阶段粗粉物料,此时经电子计量秤23计量后按比例再均匀输送到雷蒙粉磨机24一起研磨和选粉,细度等达到要求的(一般50目-150目),经除尘器25负压吸收后有提升机27提升到刮板输送机30,进入较差成品仓32,最后有散罐车33装车出厂,不合格的粗粉也经提升设备进入二次消化储料仓再消解循环备用,最后直至全部循环到较差成品仓32。  The method of producing calcium hydroxide powder that does not require high quality and poor quality is to first open the PCL automatic control system, adjust the ratio of the raw material flow in the electronic metering scale 11 to the water flow through the water injection valve 34, and then automatically open it. The raw materials measured by the measuring scale 11 are transported to the first-level digestion machine 13 by the belt conveyor 12, and at the same time, the water injection valve 34 is opened to directly inject water into the first-level digestion machine 13 to react with the raw materials. When the requirements are met, the electronic weighing scales 10 and 11 can also be turned on at the same time according to the test results and a certain ratio is adjusted to adjust the water flow ratio with the water injection valve 34. After the ratio is automatically opened, the raw materials measured by the electronic weighing scales 10 and 11 respectively The belt conveyor 12 transports it to the first-level digestion machine 13, and at the same time, the water injection valve 34 is opened to directly inject water into the first-level digestion machine 13 to react with the raw materials. Depending on the reaction degree of digestion and aging, there are frequency converters to adjust the first-level and second-level respectively. The motor speed controls the reaction time and process, because most poor calcium hydroxide powders do not have high requirements on the degree of ripening and digestion time, so the three-stage digestion machine can not participate in the work at this time, and is in a stopped state (favorable reduce power consumption and energy consumption), the powder after primary and secondary digestion will fall directly into the scraper conveyor 18 through the unloading valve 14 at the tail of the secondary digestion machine (if there is no need to open a new discharge port at the bottom), there is The scraper conveyor 18 is directly transported to the Raymond mill 24 for grinding and powder selection. The high-temperature and high-humidity dust generated by the digestion machine is collected by the dust collector 16 and the powder digested by the digester is also sent by the scraper conveyor 18 Transport to the Raymond mill 24 for powder selection. At this time, the rollers of the Raymond mill 24 are placed in the working state, and the incoming materials are squeezed, ground and powder-selected, and stored in the secondary digestion storage bin 22. Coarse powder materials at various stages after long-term digestion are measured by the electronic weighing scale 23 and then evenly transported to the Raymond mill 24 in proportion to be ground and selected, and the fineness meets the requirements (generally 50 mesh-150 mesh) mesh), after being absorbed by the negative pressure of the dust collector 25, the hoist 27 is lifted to the scraper conveyor 30, and enters the poor finished product warehouse 32, and finally the bulk tanker 33 is loaded to leave the factory, and the unqualified coarse powder also enters the second The secondary digestion storage bin is then digested and circulated for standby, and finally until it is all recycled to the poor finished product bin 32. the

Claims (6)

1. calcium hydroxide flexible multi-functional production unit, comprise crusher, former feed bin, clear up machine, powder separating machine, thunder covers pulverizer, secondary digestion storage bin and finished bin, it is characterized in that described crusher is connected with former feed bin with rubber conveyer by lift, described former feed bin through electronic weighing balance and rubber conveyer with clear up machine and be connected, the described machine end of clearing up is equipped with powder separating machine and Lei Meng pulverizer, described secondary digestion storage bin passes through scraper conveyor, lift and electronic weighing balance are connected with powder separating machine and Lei Meng pulverizer, described finished bin front end has scraper conveyor and lift, and there is the dress chartered plane rear end.
2. a kind of calcium hydroxide flexible multi-functional production unit according to claim 1 is characterized in that being provided with three former feed bins by a cover crushing system, can store the calcium oxide of three kinds of different grades respectively.
3. a kind of calcium hydroxide flexible multi-functional production unit according to claim 1 is characterized in that adopting the multistage machine of clearing up of detachable use and independent variable frequency control.
4. a kind of calcium hydroxide flexible multi-functional production unit according to claim 1 is characterized in that being provided with two cover powder selection devices.
5. a kind of calcium hydroxide flexible multi-functional production unit according to claim 1 is characterized in that being provided with a secondary digestion storage bin and the material do not cleared up fully or meal are digested again and stores.
6. a kind of calcium hydroxide flexible multi-functional production unit according to claim 1 is characterized in that carrying the finished product branch of three kinds of different grades to be clipped to three finished bin by a lift.
CN201320135894.6U 2013-03-22 2013-03-22 Flexible multifunctional production equipment for calcium hydroxide Expired - Fee Related CN203222551U (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104291370A (en) * 2014-10-13 2015-01-21 陶纪琛 Calcium hydroxide production line
CN106145714A (en) * 2016-08-29 2016-11-23 绵竹市拱星氧化钙厂 High-temperature energy-conservation burnt lime slaking device
CN109437603A (en) * 2018-12-27 2019-03-08 江苏省建筑材料研究设计院有限公司 A kind of system of full negative pressure calcium oxide digestion production calcium hydroxide
CN114736004A (en) * 2022-03-29 2022-07-12 何猛 Wet-process ball pressing production process and production line for synthesizing magnesium and aluminum magnesium by light-burned magnesium and calcium

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104291370A (en) * 2014-10-13 2015-01-21 陶纪琛 Calcium hydroxide production line
CN104291370B (en) * 2014-10-13 2015-12-16 陶纪琛 A kind of calcium hydroxide production line
CN106145714A (en) * 2016-08-29 2016-11-23 绵竹市拱星氧化钙厂 High-temperature energy-conservation burnt lime slaking device
CN109437603A (en) * 2018-12-27 2019-03-08 江苏省建筑材料研究设计院有限公司 A kind of system of full negative pressure calcium oxide digestion production calcium hydroxide
CN109437603B (en) * 2018-12-27 2023-11-14 江苏省建筑材料研究设计院有限公司 System for full negative pressure calcium oxide slakes and produces calcium hydroxide
CN114736004A (en) * 2022-03-29 2022-07-12 何猛 Wet-process ball pressing production process and production line for synthesizing magnesium and aluminum magnesium by light-burned magnesium and calcium

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