CN207204833U - 工业渣盐的分选、粉碎及输送装置 - Google Patents
工业渣盐的分选、粉碎及输送装置 Download PDFInfo
- Publication number
- CN207204833U CN207204833U CN201720976105.XU CN201720976105U CN207204833U CN 207204833 U CN207204833 U CN 207204833U CN 201720976105 U CN201720976105 U CN 201720976105U CN 207204833 U CN207204833 U CN 207204833U
- Authority
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- China
- Prior art keywords
- drier
- vulcanization
- crushing
- feeding trough
- pans
- Prior art date
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- 239000011780 sodium chloride Substances 0.000 title claims abstract description 34
- 150000003839 salts Chemical class 0.000 title claims abstract description 33
- 239000002893 slag Substances 0.000 title claims abstract description 29
- 238000004073 vulcanization Methods 0.000 claims abstract description 22
- 238000011084 recovery Methods 0.000 abstract description 4
- 238000010276 construction Methods 0.000 abstract description 3
- 239000002440 industrial waste Substances 0.000 abstract description 2
- -1 vulcanizing drier Chemical class 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 7
- 239000005416 organic matter Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 239000005864 Sulphur Substances 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- IKDUDTNKRLTJSI-UHFFFAOYSA-N hydrazine hydrate Chemical compound 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O.NN IKDUDTNKRLTJSI-UHFFFAOYSA-N 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M sodium chloride Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound 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[S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 230000002588 toxic Effects 0.000 description 2
- 231100000331 toxic Toxicity 0.000 description 2
- YHAROSAFXOQKCZ-UHFFFAOYSA-N 1-benzofuran-2-ol Chemical compound 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Abstract
本实用新型一种工业渣盐的分选、粉碎及输送装置，包括硫化干燥器，所述硫化干燥器一侧设置有进料管，所述硫化干燥器另一侧设置有第一中间罐，所述第一中间罐顶部连通有第一旋风分离器，所述第一中间罐底部连通有喂料槽，所述硫化干燥器顶部与第一旋风分离器由第一输送管道连通；所述硫化干燥器的下方设置有暂储罐，所述暂储罐顶部与硫化干燥器下方连通，所述暂储罐下方设置有粉碎筛选器并与其连通，所述粉碎筛选器与喂料槽之间设置有螺旋输送机；所述喂料槽外接有吸风管。本实用新型结构简单，操作方便，其工业废盐回收、利用效率高，利于环境保护，经济效益显著。
Description
工业遼盐的分选、粉碎及输送装置
技术领域
[0001]本实用新型涉及化工废料的环保利用，具体涉及一种工业渣盐的分选、粉碎及输 送装置。
背景技术
[0002]在生产水合肼、呋喃酚、农药、中间体等产品的过程中，会产生大量工业渣盐，其成 分主要包括:氯化钠80〜90%、水分2〜8%、毒害性有机物2〜10%。目前由于缺乏节能环保的 处理方法，该种废弃物主要使用填埋方式处理，造成资源浪费和环境污染。现行办法是回收 工艺中生成的渣盐，去除渣盐内水分、有机物后再循环利用。现有工艺中，渣盐经硫化干燥 器初步干燥后由风机吸入煅烧塔对其内所含的毒害有机物焚烧，而渣盐颗粒大小不一直接 影响到焚烧质量，进而影响到回收渣盐的品质。
发明内容
[0003]本实用新型所要解决的技术问题是提供一种结构简单，作业高效，节能降耗、环保 的工业渣盐的分选、粉碎及输送装置。
[0004]为解决上述技术问题，本实用新型一种工业渣盐的分选、粉碎及输送装置，包括硫 化干燥器，所述硫化干燥器一侧设置有进料管，所述硫化干燥器另一侧设置有第一中间罐， 所述第一中间罐顶部连通有第一旋风分离器，所述第一中间罐底部连通有喂料槽，所述硫 化干燥器顶部与第一旋风分离器由第一输送管道连通;所述硫化干燥器的下方设置有暂储 罐，所述暂储罐顶部与硫化干燥器下方连通，所述暂储罐下方设置有粉碎筛选器并与其连 通，所述粉碎筛选器与喂料槽之间设置有螺旋输送机;所述喂料槽外接有吸风管。
[0005] 本实用新型吸风管工作时带动第一中间罐、暂储罐内气体流动，渣盐则随流动气 体在工艺设备间内行进，细小渣盐重量较轻，随流动气体导入喂料槽，大颗粒渣盐具较大重 量，只能随流动气体进入暂储罐，由粉碎筛选器破碎后再导入喂料槽。其作业高效，能耗低， 经济效益显著。
[0006] 作业时，渣盐经硫化干燥器初步干燥后，细小颗粒随流动气体由第一输送管道导 入第一旋风分离器后进入第一中间罐再导入喂料槽，较大渣盐颗粒则吸入暂储罐，经粉碎 筛选器破碎筛选后由螺旋输送机再导入喂料槽。
[0007] 本实用新型利用流动气体实现渣盐自动分选，并对较大颗粒渣破碎后再同步处 理，其在确保作业效率的同时还能保证成品盐的质量。
[0008] 综上，本实用新型具以下有益效果：
[0009] 1、能耗低，渣盐随流动气体自动分选；
[0010] 2、作业效率高，较大颗粒渣盐经破碎后在与前期细小渣盐一并导入下道工艺；
[0011] 3、工业渣盐中含有的毒害性有机物经焚烧处理排出，水分蒸发排出，所得无害化 盐纯度较高，有利于后续二次利用；
[0012] 4、处理过程完全密闭，对环境影响较小；
[0013] 5、可进行流水线连续作业，也可进行批次处理，工艺手段灵活。
附图说明
[0014] 图1是本实用新型的结构示意图。
具体实施方式
[0015] 下面结合附图对本实用新型作进一步说明：
[0016] 一种工业渣盐的分选、粉碎及输送装置，包括硫化干燥器1，所述硫化干燥器1 一侧 设置有进料管la，所述硫化干燥器1另一侧设置有第一中间罐7,所述第一中间罐7顶部连通 有第一旋风分离器2,所述第一中间罐7底部连通有喂料槽9,所述硫化干燥器1顶部与第一 旋风分离器2由第一输送管道8连通;所述硫化干燥器1的下方设置有暂储罐6，所述暂储罐6 顶部与硫化干燥器1下方连通，所述暂储罐6下方设置有粉碎筛选器5并与其连通，所述粉碎 筛选器5与喂料槽9之间设置有螺旋输送机4;所述喂料槽9外接有吸风管3。 实施例
[0017] 1、工业渣盐由进料管la导入硫化千燥器1干燥；
[0018] 2、吸风管3带动设备内气体流动；
[0019] 3、细小渣盐经第一旋风分离器2、第一中间罐7导入喂料槽9;
[0020] 4、较大渣盐经暂储罐6导入粉碎筛选器5破碎，符合工艺要求的细小渣盐再导入喂 料槽9;
[0021] 5、满足工艺要求的渣盐经吸风管3导入下道工艺。
[0022]本实用新型结构简单，操作方便，其工业废盐回收、利用效率高，利于环境保护，经 济效益显著。
Claims (1)
- 、1 •-种皿巧选、_及输送装置，傭硫化干燥器⑴，臓硫化干燥器⑴— 侧设置有进料管(la)，其特征是:所述硫化干燥器⑴另一侧设置有第—中间罐(乃，所述第 一中间罐(7)顶部连通有第一旋风分离器(2)，所述第一中间罐⑺底部连通有喂料槽(9)， 所述硫化干燥器(1)顶部与第一旋风分离器(2)由第一输送管道(8)连通;所述硫化干燥器 (1)的下方设置有暂储罐⑹，所述暂储罐⑹顶部与硫化干燥器(1)下方连通，所述暂储罐 ⑹下方丨體補_»⑸胸難^腿_筛麟(5)与喂浦(9)之置有螺 旋输送机(4);所述喂料槽⑼外接有吸风官⑶。
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| CN109622576A (zh) * | 2019-01-31 | 2019-04-16 | 河北工业大学 | 一种利用铁尾矿处理高盐固体废弃物的方法 |
| CN109622576B (zh) * | 2019-01-31 | 2021-04-06 | 河北工业大学 | 一种利用铁尾矿处理高盐固体废弃物的方法 |
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