CN101966997B - 一种由十水硫酸钠生产无水芒硝的工艺及其装置 - Google Patents

一种由十水硫酸钠生产无水芒硝的工艺及其装置 Download PDF

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CN101966997B
CN101966997B CN2010105251224A CN201010525122A CN101966997B CN 101966997 B CN101966997 B CN 101966997B CN 2010105251224 A CN2010105251224 A CN 2010105251224A CN 201010525122 A CN201010525122 A CN 201010525122A CN 101966997 B CN101966997 B CN 101966997B
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翁关云
周光明
洪厚军
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Jiangsu Ruineng Anticorrosion Equipment Co ltd
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Abstract

本发明涉及一种由十水硫酸钠生产无水芒硝的工艺及其装置,工艺如下:(1)将十水硫酸钠投入热熔槽内熔融,形成硫酸钠溶液;(2)硫酸钠溶液经加热后送入蒸发器浓缩蒸发,部分无水硫酸钠结晶析出;(3)蒸发器的二次蒸汽经压缩后送到蒸发器加热室;(4)将析出的硫酸钠溶液固液分离,得到固体无水硫酸钠,干燥后称重包装。装置包括依次连接的热熔槽、储液槽、输料泵、换热器及蒸发器;蒸发器依次与离心机、母液槽、母液泵和蒸发器连接;蒸发器设有真空泵,其蒸汽出口与分离器、压缩机和蒸发器加热室连接。本发明采用蒸汽压缩技术熔融蒸发十水芒硝,能降低蒸发能耗,产品纯度达99%以上;本发明投资小、经济效益高、又十分节能。

Description

一种由十水硫酸钠生产无水芒硝的工艺及其装置
技术领域
本发明涉及化工工艺及装备技术领域,尤其是一种由十水硫酸钠生产无水芒硝的工艺以及用于该工艺的装置。
背景技术
现有化工企业用十水硫酸钠(十水芒硝)制取无水芒硝的工艺方法一般有以下几种:蒸汽加热、热管加热、热风干燥,现有化工企业每生产一吨无水芒硝需消耗蒸汽0.8-1.6吨,电力消耗40-60kwh。现有大型多效蒸发装置的能耗较小,通常消耗蒸汽0.6-1.2吨,但大型多效蒸发装置的投资规模大、占地面积大、结构复杂。
目前,国内有许多副产芒硝的化工企业,这些企业的芒硝产能有限,无法投资大型装置,造成芒硝生产能耗高,甚至无法处理副产的芒硝,使得企业的经济效益较低。
发明内容
针对以上现有工艺和装备的不足,本发明的目的在于提供由十水硫酸钠生产无水芒硝的方法,通过熔融十水硫酸钠,并采用蒸汽压缩技术进行蒸发,以降低蒸发能耗,再进行离心、干燥得到无水芒硝。
本发明的目的是通过采用以下技术方案来实现的:
由十水硫酸钠生产无水芒硝的工艺,包括以下步骤:
(1)将芒硝热熔槽内的温度控制在33-90℃,将十水硫酸钠投入芒硝热熔槽内熔融,形成硫酸钠溶液;
(2)将步骤(1)所得的硫酸钠溶液,经过加热后输送进入蒸发器,在蒸发器内浓缩蒸发,部分无水硫酸钠结晶析出;
(3)将从所述蒸发器输出的二次蒸汽,经压缩机压缩,压缩比维持在1:1.2到1:2.5,使蒸汽的压力、温度升高、热焓增加,然后送到所述蒸发器的加热室当作加热蒸汽使用,使料液维持沸腾状态,并使加热蒸汽本身冷凝成水;
(4)将步骤(2)得到的部分结晶析出的硫酸钠溶液经离心机进行固液分离,得到固体无水硫酸钠,溶液返回蒸发器进一步浓缩。
作为本发明的优选技术方案,所述步骤(2)中通过真空泵调节所述蒸发器内的压力,使水的沸点降低,从而使蒸发器内的硫酸钠溶液无需加热并直接沸腾蒸发。
作为本发明的优选技术方案,所述步骤(2)中硫酸钠溶液直接沸腾蒸发的温度范围控制在40-90℃。
作为本发明的优选技术方案,将步骤(3)产生的冷凝水输送进入换热器与步骤(1)产生的所述硫酸钠溶液换热,以提高硫酸钠溶液的温度;然后再将换热后的热水输送到热熔槽加热十水硫酸钠。
作为本发明的优选技术方案,将步骤(4)中产生的无水硫酸钠,经过干燥除去附着的微量水分,达到成品的含水要求,再称重包装。
由十水硫酸钠生产无水芒硝的装置,包括芒硝热熔槽、芒硝储液槽、输料泵、蒸发器、离心机、离心母液槽、离心母液泵、烘干机和称重包装机,所述芒硝热熔槽与芒硝储液槽连通,芒硝储液槽通过输料泵及管道与所述蒸发器的进料口连接;
所述蒸发器的出料口通过输料管道与离心机连接,离心机通过管道依次与离心母液槽、离心母液泵和所述蒸发器的进料口连接;
所述离心机通过送料装置依次与烘干机和称重包装机连接。
作为本发明的优选技术方案,所述芒硝储液槽与所述蒸发器之间还设有换热器,芒硝储液槽通过输料泵及管道与换热器的进口连接,换热器的出口与蒸发器的进料口连接。
作为本发明的优选技术方案,所述装置还包括冷凝水泵,所述蒸发器的冷凝水出口通过冷凝水泵和管道与换热器的进口连接。
作为本发明的优选技术方案,所述蒸发器的蒸汽出口通过管道依次与分离器、压缩机和蒸发器的加热室连接。
作为本发明的优选技术方案, 所述装置还包括真空泵,所述真空泵通过管道与所述蒸发器的料室连接。
本发明的有益效果是:相对于现有技术,本发明通过熔融十水硫酸钠,并采用蒸汽压缩技术进行蒸发,以降低蒸发能耗,再进行离心、干燥得到无水芒硝,产品纯度可以达到99%以上,符合国家产品质量标准GB/T6009-2003,每生产一吨芒硝耗能在90-130kwh之间,能耗相对于普通蒸汽蒸发节能50-70%以上,具有很高的经济效益。
本发明的工艺流程短、装置结构紧凑、占地面积小、所需空间也小,并且无需循环水冷却***。本发明既能节省投资,又能取得较好的节能效果。
附图说明
图1是本发明的工艺流程示意图;
图2是本发明装置的结构示意图。
具体实施方式
下面结合附图与具体实施例对本发明作进一步说明:
如图1和图2所示,由十水硫酸钠生产无水芒硝的工艺,包括以下步骤:
(1)通过芒硝热熔槽1内的加热棒或加热盘管,将热熔槽1内的温度控制在33-90℃,将十水硫酸钠投入芒硝热熔槽1内熔融,形成硫酸钠溶液;
(2)将步骤(1)所得的硫酸钠溶液,经过加热后输送进入蒸发器5,在蒸发器5内浓缩蒸发,部分无水硫酸钠结晶析出;
(3)将从所述蒸发器5输出的二次蒸汽,经压缩机7压缩,压缩比维持在1:1.2到1:2.5,使蒸汽的压力、温度升高、热焓增加,然后送到所述蒸发器5的加热室当作加热蒸汽使用,使料液维持沸腾状态,并使加热蒸汽本身冷凝成水;
(4)将步骤(2)得到的部分结晶析出的硫酸钠溶液经离心机10进行固液分离,得到固体无水硫酸钠,溶液返回蒸发器5进一步浓缩。
(5)将步骤(4)中产生的固体无水硫酸钠,经过干燥除去附着的微量水分,达到成品的含水要求,再称重包装。
作为本发明较好的实施方式,在所述步骤(2)中,通过真空泵8调节所述蒸发器5内的压力,使水的沸点降低,从而使蒸发器5内的硫酸钠溶液无需加热并直接沸腾蒸发,所述步骤(2)中硫酸钠溶液直接沸腾蒸发的温度范围控制在40-90℃。将步骤(3)产生的冷凝水输送进入换热器4与步骤(1)产生的所述硫酸钠溶液换热,以提高硫酸钠溶液的温度;然后再将换热后的热水输送到热熔槽1加热十水硫酸钠,以降低能耗,节省能源。
如图2所示,由十水硫酸钠生产无水芒硝的装置,包括芒硝热熔槽1、芒硝储液槽2、输料泵3、蒸发器5、离心机10、离心母液槽11、离心母液泵12、烘干机13和称重包装机14,所述芒硝热熔槽1与芒硝储液槽2连通,芒硝储液槽2通过输料泵3及管道与所述蒸发器5的进料口连接;所述蒸发器5的出料口通过输料管道与离心机10连接,离心机10通过管道依次与离心母液槽11、离心母液泵12和所述蒸发器5的进料口连接;所述离心机10通过送料装置依次与烘干机13和称重包装机14连接。
本实施例中,所述芒硝储液槽2与所述蒸发器5之间还设有换热器4,芒硝储液槽2通过输料泵3及管道与换热器4的进口连接,换热器4的出口与蒸发器5的进料口连接。本实施例还包括真空泵8和冷凝水泵9,所述真空泵8通过管道与所述蒸发器5的料室连接,用于降低蒸发器5内料液的沸点。蒸发器5的冷凝水出口通过冷凝水泵9和管道与换热器4的进口连接,用于提高硫酸钠溶液的温度,同时将换热后的热水输送到热熔槽1加热十水硫酸钠,以节省能源、降低能耗。所述蒸发器5的蒸汽出口通过管道依次与分离器6、压缩机7和蒸发器5的加热室连接,通过压缩使蒸汽的压力、温度升高、热焓增加,然后送到蒸发器5的加热室当作加热蒸汽使用,使蒸发器5内的料液维持沸腾状态,并使加热蒸汽本身冷凝成水。本实施例中,所述换热器4和蒸发器5的材料均采用316L不锈钢。

Claims (6)

1.一种由十水硫酸钠生产无水芒硝的工艺,其特征是包括以下步骤:
(1)将芒硝热熔槽内的温度控制在33-90℃,将十水硫酸钠投入芒硝热熔槽内熔融,形成硫酸钠溶液;
(2)将步骤(1)所得的硫酸钠溶液,经过加热后输送进入蒸发器,在蒸发器内浓缩蒸发,部分无水硫酸钠结晶析出;
(3)将从所述蒸发器输出的二次蒸汽,经压缩机压缩,压缩比维持在1∶1.2到1∶2.5,使蒸汽的压力、温度升高、热焓增加,然后送到所述蒸发器的加热室当作加热蒸汽使用,使料液维持沸腾状态,并使加热蒸汽本身冷凝成水;
(4)将步骤(2)得到的部分结晶析出的硫酸钠溶液经离心机进行固液分离,得到固体无水硫酸钠,溶液返回蒸发器进一步浓缩。
2.根据权利要求1所述的由十水硫酸钠生产无水芒硝的工艺,其特征是:所述步骤(2)中通过真空泵调节所述蒸发器内的压力,使水的沸点降低,从而使蒸发器内的硫酸钠溶液无需加热并直接沸腾蒸发。
3.根据权利要求2所述的由十水硫酸钠生产无水芒硝的工艺,其特征是:所述步骤(2)中硫酸钠溶液直接沸腾蒸发的温度范围控制在40-90℃。
4.根据权利要求1所述的由十水硫酸钠生产无水芒硝的工艺,其特征是:将步骤(3)产生的冷凝水输送进入换热器与步骤(1)产生的所述硫酸钠溶液换热,以提高硫酸钠溶液的温度;然后再将换热后的热水输送到热熔槽加热十水硫酸钠。
5.根据权利要求1所述的由十水硫酸钠生产无水芒硝的工艺,其特征是:将步骤(4)中产生的无水硫酸钠,经过干燥除去附着的微量水分,达到成品的含水要求,再称重包装。
6.一种由十水硫酸钠生产无水芒硝的装置,其特征是:所述装置包括芒硝热熔槽、芒硝储液槽、输料泵、蒸发器、离心机、离心母液槽、离心母液泵、烘干机和称重包装机,所述芒硝热熔槽与芒硝储液槽连通,芒硝储液槽通过输料泵及管道与所述蒸发器的进料口连接;
所述蒸发器的出料口通过输料管道与离心机连接,离心机通过管道依次与离心母液槽、离心母液泵和所述蒸发器的进料口连接;
所述离心机通过送料装置依次与烘干机和称重包装机连接;
所述芒硝储液槽与所述蒸发器之间设有换热器,芒硝储液槽通过输料泵及管道与换热器的进口连接,换热器的出口与蒸发器的进料口连接;
所述装置还包括冷凝水泵,所述蒸发器的冷凝水出口通过冷凝水泵和管道与换热器的进口连接;
所述蒸发器的蒸汽出口通过管道依次与分离器、压缩机和蒸发器的加热室连接;
所述装置还包括真空泵,所述真空泵通过管道与所述蒸发器的料室连接。
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