CN103644708A - Method for continuously drying granular materials with heat pump technology - Google Patents
Method for continuously drying granular materials with heat pump technology Download PDFInfo
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- CN103644708A CN103644708A CN201310714288.4A CN201310714288A CN103644708A CN 103644708 A CN103644708 A CN 103644708A CN 201310714288 A CN201310714288 A CN 201310714288A CN 103644708 A CN103644708 A CN 103644708A
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- 238000001035 drying Methods 0.000 title claims abstract description 55
- 238000000034 method Methods 0.000 title claims abstract description 6
- 239000008187 granular material Substances 0.000 title claims abstract description 4
- 238000005516 engineering process Methods 0.000 title claims description 3
- 239000000463 material Substances 0.000 claims abstract description 64
- 238000001704 evaporation Methods 0.000 claims description 3
- 230000008020 evaporation Effects 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 3
- 230000009286 beneficial effect Effects 0.000 claims 1
- 238000007791 dehumidification Methods 0.000 claims 1
- 230000009191 jumping Effects 0.000 claims 1
- 238000007599 discharging Methods 0.000 abstract description 2
- 239000010410 layer Substances 0.000 description 14
- 238000010586 diagram Methods 0.000 description 3
- 235000013305 food Nutrition 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 235000013613 poultry product Nutrition 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
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Abstract
本发明属农业及农产品深加工领域,公开了涉及工业化用途的热泵干燥颗粒状物料的一种方法。本发明由热泵干燥除湿机组1、干燥室2、低速多层叠放式物料摊铺输送皮带机构3、斜向导料板4、齿状物料混合器5、旋转式隔风布料器6构成。本发明中,由于采用了连续进料和连续出料的干燥工作方式,使得同批次待干燥物料在干燥室中所经历的干燥过程是相同的,保证了干燥颗粒状农产品产成品含水率一致性。
The invention belongs to the field of agriculture and deep processing of agricultural products, and discloses a method for drying granular materials with a heat pump for industrial use. The present invention is composed of a heat pump drying and dehumidifying unit 1, a drying chamber 2, a low-speed multi-layer stacked material spreading and conveying belt mechanism 3, an oblique feeder plate 4, a toothed material mixer 5, and a rotary air-isolated distributor 6. In the present invention, since the drying working mode of continuous feeding and continuous discharging is adopted, the drying process experienced by the same batch of materials to be dried in the drying chamber is the same, which ensures that the moisture content of the dried granular agricultural products is consistent sex.
Description
技术领域 technical field
本发明属农业及农产品深加工领域,公开了涉及工业化用途的热泵干燥颗粒状物料的一种方法。 The invention belongs to the field of agriculture and deep processing of agricultural products, and discloses a method for drying granular materials with a heat pump for industrial use. the
背景技术 Background technique
农产品加工过程中,热泵技术国内外多用于木材干燥领域中。热泵亦用于食品加工业的物料干燥,但主要侧重于水产品、畜禽类产品(蛋白质、脂肪较多)及蔬菜类产品(高含水率)的干燥。目前热泵干燥机组在干燥物料时都是以风为水分传导介质,以间歇式工作方式,将同批次的待干燥的物料同时送入干燥室,干燥结束后同时出料。因热泵干燥机组工作温度较低,导致干燥时间较长,故待干燥的物料在干燥室中处于固定悬挂或固定盛放状态。干燥用风由进风口吹入干燥室,吸湿后从出风口离开干燥室,进风口的风较干燥,出风口的风较潮湿,导致同一批次产成品距进风口距离不一致,而含水率不一致的现象。国外的处理方法是将进出风口轮流切换,产成品含水率均匀性有所改善,但离风口距离不同,产成品含水率还是不同。 In the processing of agricultural products, heat pump technology is mostly used in the field of wood drying at home and abroad. Heat pumps are also used in the drying of materials in the food processing industry, but mainly focus on the drying of aquatic products, livestock and poultry products (more protein and fat) and vegetable products (high moisture content). At present, the heat pump drying unit uses wind as the moisture transfer medium when drying materials, and works intermittently to send the same batch of materials to be dried into the drying chamber at the same time, and discharge the materials at the same time after drying. Due to the low working temperature of the heat pump drying unit, the drying time is longer, so the materials to be dried are in a fixed suspension or fixed storage state in the drying chamber. The drying air is blown into the drying chamber from the air inlet, and leaves the drying chamber from the air outlet after absorbing moisture. The wind at the air inlet is relatively dry, while the wind at the air outlet is relatively humid, resulting in inconsistent distances between the same batch of finished products and the air inlet, and inconsistent moisture content. The phenomenon. The foreign treatment method is to switch the air inlet and outlet in turn, and the moisture content uniformity of the finished product is improved, but the moisture content of the finished product is still different due to the different distance from the air outlet. the
发明内容 Contents of the invention
本发明由热泵干燥除湿机组1、干燥室2、低速多层叠放式物料摊铺输送皮带机构3、斜向导料板4、齿状物料混合器5、旋转式隔风布料器6构成。
The present invention is composed of a heat pump drying and dehumidifying unit 1, a
本发明的目的是为解决热泵干燥装置干燥颗粒状农产品产成品含水率不均匀性问题。 The purpose of the present invention is to solve the problem of non-uniform moisture content of the finished product of dried granular agricultural products by a heat pump drying device. the
本发明的目的是通过如下措施来达到:热泵干燥除湿机组1用于干燥吸湿后的循环风。旋转式隔风布料器6用于将待干燥物料连续地送入干燥室2、隔断干燥室气体与室外空气的联系,并将待干燥物料均匀地分散到低速多层叠放式物料摊铺输送皮带机构3上。低速多层叠放式物料摊铺输送皮带机构3用于展开待干燥物料,增加待干燥物料表面积,以提高水分的蒸发量,并移动待干燥物料。为防止在低速多层叠放式物料摊铺输送皮带机构3上的物料由上层向下层跌落时产生的反弹跳动现象,设置了斜向导料板4。为增加物料在干燥过程中排布次序变化次数,在低速多层叠放式物料摊铺输送皮带机构3上表面设置了多组相互错位的齿状物料混合器5,增加了潮湿的物料由底层翻到表面的次数。
The object of the present invention is achieved through the following measures: the heat pump drying and dehumidifying unit 1 is used for drying the circulating air after absorbing moisture. The rotary air-isolated distributor 6 is used to continuously send the materials to be dried into the
附图说明 Description of drawings
图1为本发明的结构示意图。 Fig. 1 is a structural schematic diagram of the present invention. the
图2为齿状物料混合器5的示意图。 FIG. 2 is a schematic diagram of the toothed material mixer 5 . the
图3为旋转式隔风布料器6的示意图 Fig. 3 is the schematic diagram of rotary windproof distributor 6
具体实施方式 Detailed ways
待干燥物料旋转式隔风布料器6连续地进入干燥室2,并将待干燥物料均匀地分散到低速多层叠放式 物料摊铺输送皮带机构3上。由热泵干燥除湿机组1出来的干燥的风平行于低速多层叠放式物料摊铺输送皮带机构3吹过待干燥物料表面,吸湿后离开干燥室,进入热泵干燥除湿机组1,热泵干燥除湿机组1除去循环风中的水分后,再将干燥的风循环使用。待干燥物料在低速多层叠放式物料摊铺输送皮带机构3的第一层干燥一段时间后,表面层已失去水份,被移动跌落到第二层,物料排布次序发生变化,潮湿的物料翻到了表面,经干燥后再落到第三层;经多次翻转干燥后,物料的含水率达到产品要求即由出料输送机输出干燥室。斜向导料板4抑制了低速多层叠放式物料摊铺输送皮带机构3上的物料由上层向下层跌落时产生的反弹跳动现象,减少了物料在干燥过程中的损失,并减少了低速多层叠放式物料摊铺输送皮带机构3外形尺寸,缩小了干燥室的整体尺寸。为增加物料在干燥过程中排布次序变化次数,在低速多层叠放式物料摊铺输送皮带机构3上表面设置了多组相互错位的齿状物料混合器5,使得潮湿的物料在干燥过程中翻到表面的次数增加,提高了水分的蒸发量,减少了干燥时间。
The rotary air-isolated distributor 6 of the material to be dried continuously enters the
本发明中,由于采用了连续进料和连续出料的干燥工作方式,使得同批次待干燥物料在干燥室中所经历的干燥过程是相同的,保证了干燥颗粒状农产品产成品含水率一致性。 In the present invention, since the drying working mode of continuous feeding and continuous discharging is adopted, the drying process experienced by the same batch of materials to be dried in the drying chamber is the same, which ensures that the moisture content of the dried granular agricultural products is consistent sex. the
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106196999A (en) * | 2016-07-11 | 2016-12-07 | 天津金戈科技发展有限责任公司 | A kind of tipping arrangement of mesh belt dryer |
CN106322962A (en) * | 2016-09-09 | 2017-01-11 | 云南省能源研究院有限公司 | Amomum tsao-ko drying method |
CN106907914A (en) * | 2017-04-06 | 2017-06-30 | 吴棕雁 | Multi-layer flat-turning circulating grain dryer |
CN106989572A (en) * | 2017-05-27 | 2017-07-28 | 江苏省农业科学院 | A kind of soil batch Quick-air-drying device |
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US5537758A (en) * | 1993-06-30 | 1996-07-23 | Baggio Tecnologie Srl | Drier for the continuous drying and conditioning treatment of hides fabrics |
CN200986375Y (en) * | 2006-11-29 | 2007-12-05 | 由智光 | Multiple layer chain heat air smoke extraction dual firing drying furnace for formed coal |
CN101089526A (en) * | 2007-06-27 | 2007-12-19 | 查晓峰 | Vacuum continuous feeding and discharging device |
CN201429307Y (en) * | 2009-04-04 | 2010-03-24 | 迟永江 | Energy-saving dryer |
CN102661657A (en) * | 2012-06-01 | 2012-09-12 | 广州晟启能源设备有限公司 | Heat pump dehumidifying band-type drying machine |
CN202734473U (en) * | 2012-06-08 | 2013-02-13 | 郑州飞机装备有限责任公司 | Vacuum-pumping rotary impeller unloader used for vacuum drying equipment |
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2013
- 2013-12-23 CN CN201310714288.4A patent/CN103644708A/en active Pending
Patent Citations (6)
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US5537758A (en) * | 1993-06-30 | 1996-07-23 | Baggio Tecnologie Srl | Drier for the continuous drying and conditioning treatment of hides fabrics |
CN200986375Y (en) * | 2006-11-29 | 2007-12-05 | 由智光 | Multiple layer chain heat air smoke extraction dual firing drying furnace for formed coal |
CN101089526A (en) * | 2007-06-27 | 2007-12-19 | 查晓峰 | Vacuum continuous feeding and discharging device |
CN201429307Y (en) * | 2009-04-04 | 2010-03-24 | 迟永江 | Energy-saving dryer |
CN102661657A (en) * | 2012-06-01 | 2012-09-12 | 广州晟启能源设备有限公司 | Heat pump dehumidifying band-type drying machine |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
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CN106196999A (en) * | 2016-07-11 | 2016-12-07 | 天津金戈科技发展有限责任公司 | A kind of tipping arrangement of mesh belt dryer |
CN106322962A (en) * | 2016-09-09 | 2017-01-11 | 云南省能源研究院有限公司 | Amomum tsao-ko drying method |
CN106907914A (en) * | 2017-04-06 | 2017-06-30 | 吴棕雁 | Multi-layer flat-turning circulating grain dryer |
CN106989572A (en) * | 2017-05-27 | 2017-07-28 | 江苏省农业科学院 | A kind of soil batch Quick-air-drying device |
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Application publication date: 20140319 |