CN103478404A - Method and device applied to drying process of soybean protein isolate - Google Patents
Method and device applied to drying process of soybean protein isolate Download PDFInfo
- Publication number
- CN103478404A CN103478404A CN201310390203.1A CN201310390203A CN103478404A CN 103478404 A CN103478404 A CN 103478404A CN 201310390203 A CN201310390203 A CN 201310390203A CN 103478404 A CN103478404 A CN 103478404A
- Authority
- CN
- China
- Prior art keywords
- heat
- heat pipe
- hot
- flue gas
- heat exchange
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 108010073771 Soybean Proteins Proteins 0.000 title claims abstract description 12
- 238000001035 drying Methods 0.000 title claims abstract description 12
- 235000019710 soybean protein Nutrition 0.000 title claims abstract description 12
- 238000000034 method Methods 0.000 title claims abstract description 11
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 23
- 239000003546 flue gas Substances 0.000 claims abstract description 23
- 238000001694 spray drying Methods 0.000 claims abstract description 15
- 239000007789 gas Substances 0.000 claims abstract description 8
- 238000010438 heat treatment Methods 0.000 claims abstract description 5
- 230000003749 cleanliness Effects 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 claims description 2
- 239000003595 mist Substances 0.000 claims description 2
- 239000012530 fluid Substances 0.000 abstract description 3
- 238000005192 partition Methods 0.000 abstract description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000000428 dust Substances 0.000 description 2
- 235000018102 proteins Nutrition 0.000 description 2
- 108090000623 proteins and genes Proteins 0.000 description 2
- 102000004169 proteins and genes Human genes 0.000 description 2
- 235000019764 Soybean Meal Nutrition 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 210000000795 conjunctiva Anatomy 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 235000020776 essential amino acid Nutrition 0.000 description 1
- 239000003797 essential amino acid Substances 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 235000013373 food additive Nutrition 0.000 description 1
- 239000002778 food additive Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000004455 soybean meal Substances 0.000 description 1
- 239000002887 superconductor Substances 0.000 description 1
Images
Landscapes
- Drying Of Solid Materials (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
本发明公开本发明涉及大豆分离蛋白干燥过程中的一种加热方法,用燃煤炉的热烟气代替传统装置中蒸汽机产生的热蒸汽。以热管热风炉作为生产大豆分离蛋白过程的热风源。热管热风炉的热管主要由密封管,吸液芯三部分组成。热管采用变相传热,具有极高的传热效率。在热管的两侧装有强化传热翅片,热管风炉采用的是气-气换热器。在换热器壳体中用一块隔扳分为两个部分,形成的高温烟气和冷空气的流动通道,将两种流体间的换热全部移至管外,通过传热热管束进行热量转换。850-950℃的烟气进入热管换热器中与由鼓风机进入的-20-30℃冷空气相互接触换热,烟气由850-950℃降到160℃左右,冷空气升到160-250℃,最后得到160℃左右的气体被传送至喷雾干燥塔为备喷雾干燥使用。Disclosure of the invention The invention relates to a heating method in the drying process of soybean protein isolate, which uses hot flue gas from a coal-fired furnace to replace the hot steam generated by a steam engine in a traditional device. A heat pipe hot air furnace is used as a hot air source in the process of producing soybean protein isolate. The heat pipe of the heat pipe hot blast stove is mainly composed of three parts: a sealed tube and a liquid-absorbing core. The heat pipe adopts phase-changing heat transfer, which has extremely high heat transfer efficiency. Both sides of the heat pipe are equipped with enhanced heat transfer fins, and the heat pipe stove adopts a gas-gas heat exchanger. The heat exchanger shell is divided into two parts by a partition to form a flow channel for high-temperature flue gas and cold air, and all the heat exchange between the two fluids is moved outside the tube, and the heat is transferred through the heat transfer heat tube bundle. convert. The flue gas at 850-950°C enters the heat pipe heat exchanger and exchanges heat with the -20-30°C cold air entered by the blower. The flue gas drops from 850-950°C to about 160°C, and the cold air rises to 160-250°C °C, and finally the gas at about 160 °C is sent to the spray drying tower for spray drying.
Description
技术领域 technical field
本发明涉及大豆分离蛋白干燥过程中的一种加热方法,以及一种装置热风源--热管热风炉。 The invention relates to a heating method in the drying process of soybean protein isolate, and a device hot air source-heat pipe hot air stove. the
背景技术 Background technique
大豆分离蛋白是以低温脱溶大豆粕为原料生产的一种全价蛋白类食品添加剂。大豆分离蛋白中蛋白质含量在90%以上,氨基酸种类有近20种,并含有人体必需的氨基酸。其功能特性主要有乳化性、水合性、吸油性、胶凝性、溶解性、发泡性、粘性、结团性、结膜性、调色性等。 Soybean Protein Isolate is a full-price protein food additive produced from low-temperature desolvated soybean meal. The protein content of soybean protein isolate is more than 90%, and there are nearly 20 kinds of amino acids, which contain essential amino acids for human body. Its functional properties mainly include emulsification, hydration, oil absorption, gelling, solubility, foaming, viscosity, agglomeration, conjunctiva, toning, etc. the
喷雾干燥是大豆分离蛋白生产工艺中的重要单元,其工艺过程是利用洁净的热空气将蛋白凝乳粒子化(雾化)后瞬间脱去水分。喷雾干燥的最大优势:干燥时间短,出口温度低,能最大限度地保护热敏性成分。喷雾干燥的效果直接决定最终产品的质量和功能性。传统的干燥过程中使用的是蒸汽锅,有着耗能较高,换热系数低、所需的设备多、费水、噪音大、运行费用较高的缺点。 Spray drying is an important unit in the production process of soybean protein isolate. Its process is to use clean hot air to granulate (atomize) the protein curd and remove moisture instantly. The biggest advantage of spray drying: short drying time, low outlet temperature, and maximum protection of heat-sensitive components. The effect of spray drying directly determines the quality and functionality of the final product. The traditional drying process uses a steam boiler, which has the disadvantages of high energy consumption, low heat transfer coefficient, more equipment required, water consumption, high noise, and high operating costs. the
发明内容 Contents of the invention
本发明的目的就是针对上述现有技术存在的问题,研究提供一种生产大豆分离蛋白干燥过程的方法及装置,达到提高换热效率、经济节约、降低污染的目的。 The purpose of the present invention is to solve the problems in the above-mentioned prior art, research and provide a method and device for the drying process of producing soybean protein isolate, so as to achieve the purposes of improving heat exchange efficiency, saving money, and reducing pollution. the
本发明的目的是这样实现的:一种用于大豆分离蛋白干燥过程的加热方法,是直接利用燃煤锅炉产生的热烟气(850-950℃)代替传统蒸汽机产生的热空气(160-250℃)。高温烟气通过与冷空气换热得到适合干燥温度的热空气,进行喷雾干燥。 The object of the present invention is achieved in this way: a heating method for the drying process of soybean protein isolate is to directly use the hot flue gas (850-950°C) produced by the coal-fired boiler to replace the hot air (160-250°C) produced by the traditional steam engine ℃). The high-temperature flue gas is exchanged with cold air to obtain hot air with a suitable drying temperature for spray drying. the
一种热管热风炉装置来代替传统热风源(蒸气炉)。这种热管热风炉的热管主要由密封管,吸液芯三部分组成。热管采用变相传热,具有极高的传热效率,具有热超导体之称。在热管的两侧装有强化传热翅片,热管的数量取决于换热量的大小。根据通过换热器的流体种类不同,单管组合式热管换热器可分为气-气、气-液、气-蒸汽三种类型,我们热管风炉采用的是气-气换热器。在换热器壳体中用一块隔扳分为两个部分,形成高温烟气和冷空气的流动通道,将两种流体间的换热全部移至管外,通过传热热管束进行热量转换。当高温烟气和冷空气同时在各自的通道中逆向流过时,热管就将高温烟气的热量传给冷空气,实现了高温烟气和冷空气的热交换。它还可以根据加热空气温度的高低,分别设置不同温度的热管,使热管温度在最合适的温度区内工作。 A heat pipe hot blast stove device to replace the traditional hot blast source (steam stove). The heat pipe of this heat pipe hot blast stove mainly consists of a sealed tube and a liquid-absorbing core. The heat pipe adopts heat transfer in disguise, has extremely high heat transfer efficiency, and is known as a thermal superconductor. Both sides of the heat pipe are equipped with enhanced heat transfer fins, and the number of heat pipes depends on the amount of heat exchange. According to the different types of fluid passing through the heat exchanger, the single-tube combined heat pipe heat exchanger can be divided into three types: gas-gas, gas-liquid, and gas-steam. Our heat pipe stove uses a gas-gas heat exchanger. The heat exchanger shell is divided into two parts with a partition plate to form a flow channel for high-temperature flue gas and cold air, and all the heat exchange between the two fluids is moved to the outside of the tube, and the heat is converted through the heat transfer heat tube bundle. . When the high-temperature flue gas and cold air flow in opposite directions in their respective channels at the same time, the heat pipe transfers the heat of the high-temperature flue gas to the cold air, realizing the heat exchange between the high-temperature flue gas and the cold air. It can also set heat pipes at different temperatures according to the temperature of the heated air, so that the heat pipes can work in the most suitable temperature zone. the
本发明的有益效果是:投资少,节能环保、节省燃料、节电, 省水不需要水处理、给水泵、冷凝水箱、热力除气器、省煤器、连续排污膨胀器、疏水器,噪音低,操作少,维修和运行费用低,安全,可长期连续运行,热效率高,综合性能好,不结垢,抗冻性好,易自动化控制等优点。 The beneficial effects of the present invention are: less investment, energy saving, environmental protection, fuel saving, electricity saving, water saving, no need for water treatment, feed water pump, condensate water tank, thermal degasser, economizer, continuous blowdown expander, steam trap, noise reduction Low cost, less operation, low maintenance and operating costs, safe, long-term continuous operation, high thermal efficiency, good overall performance, no scaling, good frost resistance, easy automatic control, etc. the
附图说明 Description of drawings
图1是本发明整体结构示意图。 Figure 1 is a schematic diagram of the overall structure of the present invention. the
具体实施方式 Detailed ways
具体实施方式一:这种用于大豆分离蛋白干燥过程的加热方法,是直接利用燃煤锅炉产生的热烟气(850-950℃)代替传统蒸汽机产生的热空气。高温烟气通过与冷空气换热得到适合干燥温度的热空气(160-250℃),进行喷雾干燥。 Embodiment 1: This heating method used in the drying process of soybean protein isolate is to directly use the hot flue gas (850-950°C) produced by the coal-fired boiler to replace the hot air produced by the traditional steam engine. The high-temperature flue gas is exchanged with cold air to obtain hot air (160-250°C) suitable for drying temperature, and then spray-dried. the
具体实施方式二:如图1所示,本实施方式包括热风炉(1)、热管换热器(2)、空气过滤器(3)、鼓风机(4)、除尘器(5)、锅炉引风机(6)、烟囱(7)、喷雾干燥塔(8)、沙克龙组分离器(9)、排潮风机(10)。如图所述热风炉(1)与热管换热器(2)相连。热管换热器(2)与空气过滤器(3)相连的同时也直接与雾干燥塔(8)相连通。除尘器(5)也与热管换热器(2)相连保证通入气体的洁净度。 Specific embodiment two: As shown in Figure 1, this embodiment includes a hot blast stove (1), a heat pipe heat exchanger (2), an air filter (3), a blower (4), a dust collector (5), and a boiler induced draft fan (6), chimney (7), spray drying tower (8), Sacron group separator (9), and exhaust fan (10). As shown in the figure, the hot blast stove (1) is connected to the heat pipe heat exchanger (2). While the heat pipe heat exchanger (2) is connected to the air filter (3), it is also directly connected to the mist drying tower (8). The dust remover (5) is also connected with the heat pipe heat exchanger (2) to ensure the cleanliness of the incoming gas. the
本实施方式保证了烟气通过在热管换热器(2)中的传热翅片是被换热至所需温度,并大大减少了热管数量,提高了换热效率。 This embodiment ensures that the flue gas is exchanged to the required temperature through the heat transfer fins in the heat pipe heat exchanger (2), greatly reduces the number of heat pipes, and improves the heat exchange efficiency.
具体实施方式三:如图1所示,燃煤锅炉产生了高温的烟气,850-950℃烟气进入热管换热器(2)中与由鼓风机(4)进入的-20- 30℃的冷空气相互接触换热,使烟气由850-950℃降到160℃左右,而冷空气升高到160-250℃,最后得到的160℃左右的气体被传送至喷雾干燥塔(8)中以备喷雾干燥使用。 Specific implementation method three: As shown in Figure 1, the coal-fired boiler produces high-temperature flue gas, and the flue gas at 850-950 °C enters the heat pipe heat exchanger (2) and the -20-30 °C flue gas entered by the blower (4) The cold air contacts each other to exchange heat, so that the flue gas drops from 850-950°C to about 160°C, while the cold air rises to 160-250°C, and the finally obtained gas at about 160°C is sent to the spray drying tower (8) Ready for spray drying. the
具体实施方式四:如图1所示,喷雾干燥塔(8)高温空气温度为160-250℃,最常采用的中压为2.3MPa-2.6MPa。 Embodiment 4: As shown in Figure 1, the high-temperature air temperature of the spray drying tower (8) is 160-250°C, and the most commonly used medium pressure is 2.3MPa-2.6MPa. the
Claims (4)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310390203.1A CN103478404B (en) | 2013-09-02 | 2013-09-02 | For a kind of method in soybean protein isolate dry run and device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310390203.1A CN103478404B (en) | 2013-09-02 | 2013-09-02 | For a kind of method in soybean protein isolate dry run and device |
Publications (2)
Publication Number | Publication Date |
---|---|
CN103478404A true CN103478404A (en) | 2014-01-01 |
CN103478404B CN103478404B (en) | 2015-08-26 |
Family
ID=49819267
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201310390203.1A Active CN103478404B (en) | 2013-09-02 | 2013-09-02 | For a kind of method in soybean protein isolate dry run and device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN103478404B (en) |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2200148Y (en) * | 1993-04-17 | 1995-06-07 | 天津市蓟县能源研究所 | Circulating hot pipe hot-air stove |
CN201129912Y (en) * | 2007-11-16 | 2008-10-08 | 沂源瑞丰高分子材料有限公司 | Heated air circulation heating apparatus of spray drying tower |
CN102763761A (en) * | 2012-06-21 | 2012-11-07 | 谷神生物科技集团有限公司 | Method for preparing enzymolysis low-sodium soybean isolated protein |
CN202993539U (en) * | 2012-12-26 | 2013-06-12 | 唐山拓普生物科技有限公司 | Energy-saving combustion blast furnace |
-
2013
- 2013-09-02 CN CN201310390203.1A patent/CN103478404B/en active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2200148Y (en) * | 1993-04-17 | 1995-06-07 | 天津市蓟县能源研究所 | Circulating hot pipe hot-air stove |
CN201129912Y (en) * | 2007-11-16 | 2008-10-08 | 沂源瑞丰高分子材料有限公司 | Heated air circulation heating apparatus of spray drying tower |
CN102763761A (en) * | 2012-06-21 | 2012-11-07 | 谷神生物科技集团有限公司 | Method for preparing enzymolysis low-sodium soybean isolated protein |
CN202993539U (en) * | 2012-12-26 | 2013-06-12 | 唐山拓普生物科技有限公司 | Energy-saving combustion blast furnace |
Also Published As
Publication number | Publication date |
---|---|
CN103478404B (en) | 2015-08-26 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102242946A (en) | Concentrated heat supply system for reclaiming smoke afterheat by absorption heat pump | |
CN105937773A (en) | Power station boiler condensing flue gas dehumidification and purification energy-saving system | |
CN108050731A (en) | A kind of flue gas drives residual heat recovery type absorption heat pump | |
CN108479287A (en) | A kind of device and method for eliminating fire coal boiler fume plume | |
CN203249228U (en) | An Air Preheating System Utilizing Turbine Extraction | |
CN204593353U (en) | A kind of integrated system of deep exploitation residual heat from boiler fume | |
CN206929794U (en) | The boiler exhaust gas total heat recoveries of nicotinic acids a kind of and flue gas disappear white device | |
CN104075388B (en) | A device for recovering waste heat and moisture in flue gas | |
CN104406144A (en) | Double-medium waste heat boiler | |
CN103557532A (en) | System and method for avoiding low-temperature corrosion of air preheater by using phase-change heat exchange | |
CN207214097U (en) | A kind of coal-burning boiler based on smoke evacuation vapor internal-circulation type condensing units | |
CN100520268C (en) | Fume-fume hot pipe heater exchanger for fume desulphurization in heat-engine plant | |
CN100572920C (en) | Evaporative cooling flue gas heater | |
CN205090596U (en) | Oil field heating furnace | |
CN204421052U (en) | A kind of waste heat recovery furnace | |
CN204574488U (en) | The condensation hot water boiler of the collapsible layout of a kind of three backhaul | |
CN106247314A (en) | A kind of residual heat from boiler fume recovery system of power station reheating embrittlement | |
CN217178486U (en) | A utility boiler waste heat utilization and smoke plume elimination system | |
CN103478404B (en) | For a kind of method in soybean protein isolate dry run and device | |
CN206608968U (en) | A kind of power plant's heat reclaiming system | |
CN206247373U (en) | A kind of pipe heat exchanger residual neat recovering system | |
CN202002140U (en) | Forced circulation air preheating system | |
CN204513978U (en) | Heat-conducting oil furnace flue gas waste heat spray drying system | |
CN108151050A (en) | A kind of dangerous waste burns wet method depickling flue gas and takes off white system and its application method | |
CN103195577A (en) | Air intake temperature regulating system of gas turbine |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C53 | Correction of patent of invention or patent application | ||
CB03 | Change of inventor or designer information |
Inventor after: Jiang Lianzhou Inventor after: Sun He Inventor after: Pan Mingzhe Inventor after: Yu Dianyu Inventor after: Wang Liqi Inventor after: Li Jun Inventor after: Zhou Shuang Inventor after: Liang Baosheng Inventor after: Ge Hongru Inventor after: Wang Wenhua Inventor before: Jiang Lianzhou Inventor before: Pan Mingzhe Inventor before: Yu Dianyu Inventor before: Wang Liqi Inventor before: Sun He |
|
COR | Change of bibliographic data |
Free format text: CORRECT: INVENTOR; FROM: JIANG LIANZHOU PAN MINGZHE YU DIANYU WANG LIQI SUN HE TO: JIANG LIANZHOU PAN MINGZHE YU DIANYU WANG LIQI LI JUN ZHOU SHUANG LIANG BAOSHENG GE HONGRU WANG WENHUA SUN HE |
|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
TR01 | Transfer of patent right |
Effective date of registration: 20240723 Address after: Building 4, Wurui Entrepreneurship Park, Balidian Town, Wuxing District, Huzhou City, Zhejiang Province, 313000 Patentee after: Huzhou Zhiran Food Technology Co.,Ltd. Country or region after: China Address before: 150030 No. 59 Wood Street, Xiangfang District, Heilongjiang, Harbin Patentee before: Northeast Agricultural University Country or region before: China |
|
TR01 | Transfer of patent right |