真空制盐盐腿设置浅析

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真空制盐工艺设计

真空制盐工艺设计摘要：随着人民生活水平的提高，食盐作为人们日常生活中必不可少的调味品，需求量不断增长。

为了满足日益增长的需求，提高盐产品品质，改善工艺生产环境，本文设计了一种真空制盐工艺。

该工艺可有效降低生产过程中食盐的浓度，提高盐的结晶度和纯度，节约能源消耗。

一、引言食盐作为人们日常生活中的重要调味品，用途广泛，需求量大。

此外，食盐还是一种重要的化工原料，应用于医药、化工、冶金等行业。

为了满足日益增长的需求，提高盐产品的品质，改善生产工艺，本文提出了一种真空制盐工艺设计方案。

二、工艺流程1.真空蒸发：将盐水进入真空蒸发器，通过加热和真空吸附的方式，使盐水蒸发，同时将水分和气体抽走，以提高盐水的浓度。

2.结晶：将浓缩后的盐水送入结晶槽，通过加热和冷却的交替操作，让盐水逐渐结晶，形成盐晶。

3.脱水：将结晶槽中的盐晶送入离心机，通过高速旋转离心，将盐水和残余水分分离。

4.干燥：将离心机分离出的湿盐晶送入干燥器，通过加热和通风的方式，将湿盐晶中的水分蒸发掉，使盐晶干燥。

5.粉碎：将干燥后的盐晶送入粉碎机，通过机械碾磨的方式，将盐晶粉碎成所需的粒度。

三、工艺优势1.降低浓度：真空蒸发可以有效降低盐水的浓度，减少蒸发过程中的能源消耗。

同时，通过结晶和脱水的操作，进一步提高盐的结晶度和纯度。

2.节约能源：真空制盐工艺中，通过真空蒸发和干燥器的加热操作，可有效利用热量，减少能源的消耗。

同时，通过离心机的高速旋转，将盐水和残余水分分离，减少脱水过程中的能源消耗。

3.环保健康：真空制盐工艺中，运用了真空吸附和离心分离的技术，减少了对环境的污染，提高了工艺生产环境的安全性和卫生程度。

四、工艺参数优化为了达到最佳的工艺效果，需要对工艺参数进行优化。

主要的优化参数包括加热温度、真空度、结晶温度、离心机转速和干燥温度等。

1.加热温度：加热温度是影响盐水蒸发速度和结晶效果的关键参数。

合理的加热温度可以加快水分的蒸发速度，加大盐水的浓度。

浅谈真空制盐范文

浅谈真空制盐范文真空制盐，又称真空结晶法或真空蒸馏法，是一种利用真空蒸发技术来制取盐的方法。

真空制盐工艺的基本原理是利用恒温恒压条件下的低温蒸发过程。

在真空环境下，将含有盐分的溶液加热至沸腾，水分蒸发后，通过冷凝器将蒸发出的盐分重新结晶。

这个过程使得盐分析中的杂质被除去，从而制得较纯净的食盐。

与传统的晒盐和煮盐相比，真空制盐有以下几个优势：首先，真空制盐能够更好地保留盐中的有机质。

在晒盐和煮盐过程中，由于高温和阳光的作用，盐中的有机质会被分解或氧化，从而降低了食盐的品质。

而真空制盐在低温环境下进行，可以减少这些反应的发生，保持食盐的营养成分和滋味。

其次，真空制盐能够更彻底地去除杂质。

在真空蒸馏过程中，盐水中的杂质会随着水分的蒸发被除去。

在晒盐和煮盐中，由于没有这种蒸发的过程，杂质会随盐分晶体一同沉积下来，导致食盐中含有一定的杂质。

而真空制盐通过结晶过程，可以得到较为纯净的食盐。

再次，真空制盐可以提高产量和效率。

由于真空蒸发的高效性，相比较传统的方法，真空制盐可以缩短生产周期，提高盐的产量和利用率。

这对于盐工业来说是非常重要的，因为盐是人们日常生活中常用的调料，需求量大。

此外，真空制盐还具有一定的环境保护效应。

晒盐和煮盐过程中，由于需要大量的阳光和燃料，会造成大量的能源浪费和环境污染。

而真空制盐由于在低温环境下进行，不需要大量能源和化学药剂，有效减少了对环境的破坏。

综上所述，真空制盐是一种高效、环保且质量较高的盐的制取方法。

它通过真空蒸发技术，能够更好地保留盐中的有机质、去除杂质，提高产量和效率。

在未来的生产实践中，真空制盐有望得到更广泛的应用和推广，为人们提供更加健康、纯净的食盐。

真空制盐实验报告

真空制盐实验报告
真空制盐实验报告
1.盐的生产过程：工业上用海水晒盐或用井水、盐湖水煮盐，使食盐晶体析出。

这样制得的食盐含有较多的杂质，叫做粗盐。

粗盐经溶解、沉淀、过滤、蒸发，可制得精盐。

2.现代食盐的制造是使用的"真空制盐"技术，纯净的盐水注入蒸发罐，高温蒸汽通过热交换方式给盐水加热，使盐水中的水份蒸发掉，盐就结晶出来了。

科学家又运用了液体在低气压条件下，沸点降低的原理，采用降低蒸发罐中的气压的方法，降低热能的消耗，使盐尽快结晶出来。

这就是"真空制盐"技术。

3.制盐是连续生产的，刚生产出来的盐是还是一种盐浆。

要用离心胶水的方法甩去多余的盐水，返回到蒸发罐中回收利用。

脱水后的盐还是湿盐，要用干热的压缩空气吹干。

干燥后的盐就是工业生产用盐。

如果是用来食用的，还得有一个关键的工序——"加碘"。

人如果缺碘就会患上“碘缺乏症(IDD)"大脖子病，智力损害什么的。

加碘后的食盐经过包装，运输，然后才走进千家万户，走进人们的生活。

真空制盐工艺设计

真空制盐工艺设计引言：制盐是一项古老而重要的工艺，以满足人类对食盐的需求。

然而，传统的制盐方法存在一些局限性，包括能耗高、污染严重等。

为了解决这些问题，科学家们研究出了一种新型的制盐工艺，真空制盐工艺。

本文将详细介绍真空制盐工艺的设计原理、工艺流程和设备选型。

一、设计原理：1.降低盐水的沸点：通过减压操作，可以降低盐水的沸点，从而在低温下蒸发水分。

2.提高盐的产量：在真空环境下，盐水的蒸发速度更快，可以提高盐的产量。

3.节约能源：真空制盐工艺可以大幅度降低能耗，减少对环境的污染。

4.控制盐的质量：通过控制真空度、温度和蒸发时间等参数，可以获得高质量的食盐。

二、工艺流程：1.蒸发器预热：首先，将蒸发器预热到一定温度，以确保加热效果。

2.加盐水：将盐水加入蒸发器，并封闭设备，建立真空环境。

3.降压操作：通过减压系统降低蒸发器内的压力，从而降低盐水的沸点。

4.蒸发过程：在真空环境下，盐水开始蒸发，水分子从盐水中脱离，形成盐蒸汽。

5.盐蒸汽处理：将盐蒸汽引入除湿器进行处理，去除残余的水分和其它杂质。

6.盐收集：将经过处理的盐蒸汽传输到盐收集器中，将蒸发的盐进行收集和储存。

7.盐水循环：将剩余的盐水重新回收到蒸发器中，进行下一轮的蒸发。

三、设备选型：要实现真空制盐工艺，需要选用合适的设备来完成各个工艺步骤。

1.蒸发器：选择性能稳定、耐高温、耐腐蚀的蒸发器，包括加热管、蒸发室等。

2.泵系统：选择真空泵和减压系统，确保能够实现所需的真空度。

3.除湿器：选择能够有效去除水分和杂质的除湿器，以确保蒸汽的纯度。

4.收集器：选择合适的盐收集器，以便将蒸发的盐进行收集和储存。

5.控制系统：选择先进的自动控制系统，以实现对温度、真空度和蒸发时间等参数的精确控制。

结论：真空制盐工艺是一种高效、节能、环保的制盐方法，可以从根本上解决传统制盐方法存在的问题。

通过合理的设计原理、工艺流程和设备选型，可以实现真空制盐工艺的顺利进行。

2010年度《中国井矿盐》总目次

６情系员工以服务创新为落脚点
力、有成效的思想政治工作，往就是为员工服最往
务最积极、到位的思想政治工作。只要不拘泥于最提供服务，新时期加强和改进思想政治工作是
的根本思路。过去人们总认为思想政治工作就是说教，总是着眼于开导人、导人，眼于 “ 教着管住 ” 和人 “ 限制 ” ，人的需求和利益关注不够。社会主义人对市场经济 “ 个多样化 ” 件下的人的自我意识和五条
过去，足现在，拓创新，立开真正做到像胡锦涛同志所要求的那样，为民所用、为民所系、为民所权情利谋，为员工诚心诚意办实事，心竭力解难事，持尽坚不懈做好事，时刻把群众的安危冷暖挂在心上，把关心和服务群众的各项政策和举措落到实处，思想政治工作的作用、功能和形象就会重放异彩。新是无创
资源与开发
全卤制碱盐井运行总结 … … … … … … … … 米丰忠等（１１１６ —
浅析 Ⅱ效冷凝水的回收及对锅炉的影响 … … 黄伟等ｆ７２） — 浅析食用盐中碘剂的应用 … … … … … … … 梁廷霞等ｆ— １２９
顶板稳定性较差的盐矿开采方案设计中应遵循的原则
… … … … … … … … … … … … … … … … … … …

浅议真空制盐真空系统

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Ａｂｓｔｒａｃｔ：ｍｕｌｔｉｐｌｅｅｆｆｅｃｔｖａｃｕｕｍｅｖａｐｏｒａｔｉｏｎｃａｎｉｍｐｒｏｖｅｓｔｅａｍｅｃｏｎｏｍｉｃａｌｌｅｖｅｌ，ｗｈｉｃｈｈａｓｂｅｃｏｍｅｔｈｅｉｎｅｖｉｔａｂｌｅｃｈｏｉｃｅｏｆｌｏｗｃａｒｂｏｎｃｙｃｌｅａｎｄｇｒｅｅｎｐｒｏｄｕｃｔｉｏｎｉｎｔｈｅｈｉｇｈｅｎｅｒｇｙｃｏｎｓｕｍｐｔｉｏｎｓｌｔａｉｎｄｕｓｔ￣ａｎｄｗｈｉｃｈｉｓｔｈｅｋｅｙｏｆｖａｃｕｕｍｓａｌｔｍａｋｉｎｇａｎｄｔｈｅｄｅｔｅｒｍｉｎｅｒｏｆｉｍｐａｃｔｉｎｇｔｈｅｏｕｔｐｕｔｏｆｓａｌｔｍａｋｉｎｇｄｅｖｉｃｅｓ．Ｔｈｉｓｐａｐｅｒｂｉｒｅｌｆｙａｎａｌｙｚｅｓｔｈｅｓｅｌｅｃｔｉｏｎｏｆｔｈｅｐｒｏｃｅｓｓｏｆｖａｃｕｕｍ

16.EN 热压制盐与真空制盐之优劣比较及发展浅析

Analysis on the comparison of the advantages and disadvantages of the hot pressure salt and vacuum salt and the development.Peng Chuan-Feng, Fu yuhang(Light Industry Design Institute Co., Ltd. of Zigong City, Sichuan Zigong 643000) Abstract: one way that couple the vacuum salt and hot pressure salt was developed in this paper through the vacuation on the principle of hot pressure salt and the analysis on the advantages and disadvantages of hot pressure salt at home. Which can not only make full use of the excess heat of vacuum salt power station to attain the steam-power balance, but also play the advantages of hot pressure salt to achieve better energy efficiency.Key words: hot pressure salt，gains and losses，steam power balance1 INTRODUCTIONIn the face of keen competition, the energy consumption、environment protection and product quality gap of vacuum salt industry between home and abroad come to emerge. Especially in the wake of the progress of industrial technology, energy saving has become the focus of attention of various enterprises, in order to improve the technological level of domestic vacuum salt, making use of a more advanced way is the inevitable trend of the salt manufacture technology development.At present, the common way of vacuum salt manufacture is the multi-effect evaporation, from 3 to 4 effect, up to now, some manufacturers are adopting the 5-effect evaporation, all those way is to make full use of heat and reduce energy consumption. but some Foreign companies utilize the hot pressure salt to reduce power consumption. The purpose of this paper is to find a more energy-efficient, more cost-effective production way through the comparison of hot pressure salt and vacuum evaporation salt, the summary of the gains and losses of the heat pressure salt which had been used by domestic enterprises. Also hope to throw a sprat to catch a herring, discuss with colleagues in order to better achieve the purpose of saving energy and reducing energy consumption.2 INTRODUCTION OF HOT PRESSURE SAL tHot pressure salt, also called as heat pumps or mechanical secondary steam pressuring salt. It consume some part of high quality energy (heat, mechanical energy, electricity, etc.), shifted from the low-temperature steam to the high-temperature steam through the thermodynamic cycle compression process. The characteristics of the process are only one evaporation tank and positive pressure involved. In order to enable the temperature of brine toreach or approach the boiling point of liquid in chamber, the brine was preheated in the plate type preheater with the condensed water from the heating chamber before flowing into evaporating chamber. The brine was heated by the heating tube after it flowed into the tank, and it reached the boiling point soon when flow into the evaporating chamber again. The generated secondary steam was under a treatment of foam elimination, gas-liquid separation, washing-up and compressed through centrifugal compressor. The compressed steam returned into the heating chamber as heating media when the degree of superheat had been eliminated. The discharged condensed water from heating chamber was mainly used to preheat brine, and the other part was used to wash the secondary steam to eliminate the degree of superheat. Thus, the whole processes circulate continuously to enable long-term continuous operation. Heating chamber don’t require supply of steam in normal circumstances, and its advancement lie in the consumption of less energy, so that a large number of secondary steam can to re-use. Which is a better way to save energy..The heat pump itself is not heat source, but is the way to utilize low temperature energy effectively, and it can achieve the purpose of energy conservation and improve the energy efficiency. Its flow chart is as follows:3, THE SITUATION AT HOME AND ABROADHot pressure salt isreceivingincreasing attention for its energy-saving effect which can reduce the cost of salt manufacture. The development of hot pressure salt technology is earlier abroad, as early as 1930, Escher Wyss Co. of Switzerland has manufactured a centrifugal turbine compressor which give rise to the wide usage of hot pressure salt. To the 70s 20th century, hot pressure technology has been established. At present, there are many European companies to use hot salt, it become more popular especially in the areas with adequate power and low-price electricity. such as the hot pressure salt evaporation equipment with production capacity of 1.5 million tons established in Italy by French company, achieve a high degree of automation control.There are many domestic enterprises are to introduce this technology, improve the competitiveness of the industry.4 GAINS AND LOSSES OF HOT PRESSURE SALT4.1 introduction of the overall situationSichuang Zhangjiaba Zigong salt chemical plant had imported the hot pressure salt manufacture technology in the late 80's of 20th century, which is the first company adopted this technology. Zhang salt factory has two devices with a total production capacity of 230,000 tons at that time, of which the vacuum salt production capacity is 130,000 tons (the actual production capacity is up to 150,000 tons), and the hot pressure salt production capacity is 100,000 tons. From the material point of view, the entire hot pressure salt equipment including devices and pipes were imported, the evaporation Tank was made from Monel alloy, the others were made from copper-nickel alloy or stainless steel, recycling pumps, centrifuges, vibration dry bed all were advanced equipment, so the quality of the salt production in term of particle size, whiteness and chemical composition reach the domestic advanced level.Since 1989, the hot salt installation of Zhangjiaba salt chemical plant Zhang have been running for more than 4 years, the cumulative salt production was close to 200,000 tons. But it suspended production for a variety of reasons. The reason why the device failed to achieve its main purpose is not technical problem, but some other aspects. Several reasons were elaborated as follow:.4.2 Output matchZhangjiaba salt production plant had manufactured salt with hot pressure salt for more than 4 years, the cumulative production of salt is only 196,000 tons, only account for 47% of the design capacity (100,000 tons), which significantly lower than the designed capacity. Take the 1992 with he highest and 1993 with the lowest production yield as an example, the percentage of the annual production capacity to design production capacity as follows:from design capability, low production capacity lead to the substantial increase in the fixed unit costs. Which give rise to the illusion that advanced technology produce the of low-efficiency products. It is due to the planned economy at that time, manufacturing salt in accordance with national plans. Since the output of salt was far more than the market demand in those days, the salt production plan issued by government is short, so that the production can not be carried out at full capacity, which the equipment.4.3 Cost ComparisonFrom the cost point of view, the long-term intermittent production resulted in the higher cost of hot pressure salt than that of vacuum salt, But it is not the case. Take the vacuum salt and hot pressure salt cost of 1992, 1993 as an example to compare the cost of production, the data is as follows:As can be observed from the item composing of cost in table, the indirect costs is the main reasons the caused high cost of hot pressure salt. And indirect expenses consisted of the workshop expenses. And hot salt depreciation is the main reason for the issue of increased funding of workshop.The fixed assets of hot pressure salt is 36.86 million yuan, more than 1,000 million that the fixed assets of vacuum salt, only one-third of hot pressure salt; compared in term with the production capacity, the capacity of the vacuum salt is 130,000 tons, which is 1.3 times that of the hot salt. As the hot pressure salt has more fixed assets, the extracted depreciation charges according to the ratio was higher; combined with the production of salt in accordance with national plans, the productionis small,so the depreciation charges per ton iseven more. Depreciation charges asfollows:As can be seen from the table, dueto the short running time, this set ofdevice is mainly reflected in thedepreciation charge that the cost of hotsalt were much higher than that of thevacuum salt. However, the direct cost ofhot pressure salt is obviously lower thanthat of the vacuum salt. Direct costcomparison is as follows:As can be seen from the above analysis, the main reason that the cost of hot pressure salt is higher than that of vacuum salt in Zhangjiaba salt production plant at that time is mainly due to the fact that the cost burden did n’t base on the same level, the former cost more 30 yuan depreciation charge than the latter when produce one ton of salt, as a result that the cost-effective of the former is higher than that of the latter. However, just consider the direct costs alone, the cost of hot pressure salt is lower than that of vacuum salt.Therefore, it should be sure that the main reason why the hot pressure salt device did not achieve the desired purpose is not technical issues: hot pressure salt is an advanced technique and can be used to produce high qualitythe hot pressure technology is mature, reliable and economically feasible.As for the multi-effect vacuum salt, the number of the steam use rise with the increase in efficiency number, but regardless of efficiency number, the secondary steam has always been cool when it had come from the end-effect, which resulting in the waste of a large number of steam latent heat (about 540 kcal / kg). And hot pressure salt can overcome such waste of energy, it reuse the steam potential energy directly, which is the reason for the energy-saving. The comparison of energy consumption index in hot pressure and vacuum salt is as follows:Hot pressure salt and vacuum salt both have its advantages anddisadvantages. If combining the vacuum evaporation salt and hot-pressure salt to co-generate power, will be the solution to the current district steam salt imbalance of power the best way. In this way, not only can have a high fever Reactive evaporation heating efficiency advantages, but also the use of multi-effect vacuum evaporation with a high fever of economic advantages, to overcome the shortcomings of each, salt areas to achieve a basic balance between steam power; it is also energy-efficient the best way to technical and economic good, especially for places where electricity sufficient.In the operational process, the hot pressure salt should be carried out on a smooth condition to make sure that the compressor produces a steady amount of steam. brine should also be treated in order to decrease equipment corrosion, improve the heat transfer coefficient, extend the operation cycle and achieve long-term economic benefits.5. CONCLUSIONAs can be seen through the analysis and comparison, the combination of the hot pressure salt and vacuum salt not only can take full advantage of the surplus steam of the vacuum salt power station, to achieve the steam power balance, but also is an effective way to save energy. With the growing concern on the energy, combining multi-effect vacuum evaporation salt and hot-pressure salt will be the new direction for the development of the salt industry.References[1] Zigong City Board technical design, light rooms, Zhang Xiangjiaba Zigong salt chemical heat pump technology and equipment, the introduction of modified energy-saving vacuum salt project feasibility study report, in August 1985[2] Songjiong, Xiangjiaba Zhang Zigong salt chemical heat pump technology and equipment to introduce the transformation project on energy-saving vacuum salt, "Feasibility Study" comments, and "heat pump technology to use under what conditions can better energy-saving effect and economic benefits of "exposition, in August 1984.[3] LI Yu-Ling, the rule of law salt pump profile technology 1970-1989 Mineral Wells Featured in this。

真空精制盐工艺优化设计思路

真空精制盐工艺优化设计思路
1、开发背景
随着盐用量的不断增加，精制盐工艺也受到了越来越多的重视。

精制盐生产所需的原料和设备要求严格，工艺要求也十分严格，必须根据实际情况精心设计。

然而，近几年来，精制盐的生产工艺仍然采用较低的技术水平，设备和设施抗污、抗腐蚀性能差，工艺仍然单一，普遍存在节能环保等方面的不足。

为了改善这一状况，本文结合精制盐生产工艺的特点，提出以真空工艺为基础的精制盐工艺优化设计思路。

2、工艺优化设计思路
（1）选择相应的真空炉形式
由于精制盐要求高温熔融，建议采用真空电炉，以减少精制盐中的水分含量。

（2）选择适当的控制系统
真空工艺的操作非常脆弱，容易受到外界的碰撞和冲击，因此应使用高精度的控制系统来保证精制盐的质量。

（3）采用有效的抗腐蚀工艺
在真空工艺的操作过程中，由于高温、高压、恒定供电等因素，工艺设备容易受到腐蚀，影响其工作效率，因此，应采用有效的抗腐蚀工艺，如采用防腐层、添加抗腐剂等以提高设备的耐腐蚀性能。

（4）采用有效的抗氧化技术
真空工艺中的抗氧化技术可以有效地提高精制盐的质量，防止氧
化物的形成。

常用的技术包括用紫外光照射、添加抗氧化剂和采用极端环境的催化等。

（5）选用环保材料
环保材料可以有效减少精制盐生产过程中产生的有害物质，保护环境和人类健康，可以采用低碳材料、环保涂料、环保塑料等。

3、总结
精制盐工艺的优化设计可以有效提高精制盐的产量，降低成本，同时也有助于保护环境。

本文以真空工艺为基础，结合现有技术，提出了一套精制盐工艺优化设计思路，即选用相应的真空炉形式，采用有效的抗腐蚀和抗氧化技术，选用环保材料来实现精制盐的优化设计。

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１前
言
类和增稠。
蒸发结晶器内不断结晶出来的盐晶，因重力关系向下运动．锥体逐步落人到盐腿，洗卤从盐从淘
腿下部进入，腿壁上升与盐晶逆流洗涤，沿将石膏、
在真空制盐生产过程中，发结晶器底部通常蒸
３盐腿设计的形式及优化设计的目的３１国内目前采用的盐腿形式．目前，内制盐行业采用的盐腿形式主要有三国种，ｌＡ所示盐腿主要应用在自贡轻工设计研究图 — 院近年来设计的以石膏型卤水为原料，用石膏晶采
第４卷１
ＶＯ．１Ｉ４
中国
井
矿
盐
ＣＨＩＮＡＥＬＬＡＮＤＷＲＯＣＫＡＩＳ
许景媛．聪张
（自贡市轻工业设计研究院有限责任公司，四川自贡６３０４￣）
摘要：文章概述了真空制盐主体设备一蒸发结晶器底部盐腿设置的应用现状，简要介绍了盐腿的工作原理
Ａｂｔａｔｈｓｐｐｒｏｅｖｅｈｐｌａｉｎｏｅｓｔｆｓｌｌｇｗｈｃｓｉｓｌｄａｈｏｔｍｆｔｅｅａｏａｏ，ｔｅｍａｎｓｒｃ：Ｔｉａｅｖｒｉｗｓｔｅａｐｉｔｆｔｅａｔｅｉｈｉｎｔｌｔｔｅｂｔｃｏｈｏａｅｏｏｖｐｒｔｒｈｉｈ
盐腿的设计利用其特殊设计的内部结构提供适当的速度和均匀的流态化，高效淘洗、能冷却、分
作者简介：景媛（９４，，川开江县人，科，许１６－）女四本高级工程师，津科技大学海洋与生物学院无机化＿专业毕业，为自贡市轻Ｘ天Ｔ－现－业设计研究院有限责任公司＿艺设计专业副总。Ｔ－
ｘｕＪｎｙａＺａｇＣｏｇｉｇｕｎｈｎｎ
（ｉｎｉｈｄｓｙＤｓｎａｄＲｓａｃｎｔｕｅＣ．ＬｄｉｏｇＳｃｕｎ６３ｏ）ＺｇｇＬｇｔｎｕｔｅｉｎｅｅｒｈＩｓｉｔｏ，ｔ．Ｚｇｎｉｈａ４ｏｏｏＩｒｇｔ
及其结构形式。
关键词：空制盐；真盐腿设置；能；质节盐中图分类号：ＳＴ３文献标识码：Ｂ文章编号：０１０３（０００ — ０３０１０ — ３５２１）６００ — ４
ＢｒｅｎｌｓｓｏｔｔｏａｔＬｅｆＶａｃｍａｔＭａｎｇｉｆＡａｙｉｎｈｅＳｅｆＳｌｇｏｃｕＳｌｋｉ
种法生产的制盐装置，在转排盐工艺中还是比较实
用的。图１Ｂ所示盐腿主要应用在以芒硝型卤水一为原料，引进苏尔寿及麦索公司技术的盐硝联产制盐装置，图１Ｃ所示盐腿应用在久大集团引进一
随着我国能源政和盐产品供需关系的改变，节能降耗不仅能为企业带来可观的效益，还能提高
企业的竞争能力，已成为各制盐企业的工作重点，
探寻盐腿技术同样具有重要的意义。
２盐腿设计的工作原理
烈的制盐行业，盐腿的作用理所当然的不可小视。
近年来，随着我国制盐企业的迅猛发展和用盐
单位对盐质的要求越来越高，高盐的品质，提已关
系到了各制盐企业的生存与发展，寻盐腿技术具探
有重要的意义。
兰１月１！
许景媛等：空制盐盐腿设置浅析真ＨＤ技术制盐装置，装置生产原料为净化后的石Ｐ该膏型卤水。本盐腿设计在其内部增加了一个倒锥简料、分效预热、效排盐五效生产工艺，效盐腿排分各出的盐浆温度均控制在５ ℃左右，２盐腿淘洗卤温度控制在４ ℃（７设计值）蒸发气耗在０７ — ．ｔ（，．５０８ｔ设计／值为０７ｔ）．／。２ｔ盐腿也是一个增稠的装置。结晶器中的物料在１— ５５２％稠液浓度下运行。晶体将沉降入盐腿内，并
设置有盐腿，腿起到集盐、级、涤、盐分洗回溶可溶
性杂质、却、送等作用，提高盐的品质、低冷输是降
制盐系统能耗的关键部件之一，如今竞争非常激在
细小的硫酸钠和盐颗粒带入蒸发结晶器内继续参与循环和长大；同时可将可溶性杂质溶解去除，如回溶Ｎ２Ｏ、ａ１等，利于盐质的提高；可通ａＣＣＳ有还过淘洗卤与逆向运行的盐浆进行热交换，降低排盐温度，少排盐热损失。减
ｆｃｌｔｎａｕａｉｉｉｖｃｕｍａｔｍａｎｇｎｎｒｄｅｈｅｏｅａｉｎｐｒｎｃｐｅａｄｉｓｓｒｔｅｙｓｌｋｉ，ａｄｉｔｏｕｃｓｔｐｒｔｏｉｉｌｎｔｔｕｃｕｒ．Ｋｅｙｗｏｒｓａｕｄ：ｖｃｕｍａｔｍａｎｇａｔｌｇｓｔｎｅｇａｉ，ｓｌｕａｉｙｓｌｋｉ，ｓｌｅｅ，ｅｒｙｓｖｎｇａｔｑｌｔ