CN103484244B - A kind of High-vacuum grease deodorization device - Google Patents
A kind of High-vacuum grease deodorization device Download PDFInfo
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- CN103484244B CN103484244B CN201310474498.0A CN201310474498A CN103484244B CN 103484244 B CN103484244 B CN 103484244B CN 201310474498 A CN201310474498 A CN 201310474498A CN 103484244 B CN103484244 B CN 103484244B
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- 238000004332 deodorization Methods 0.000 title claims abstract description 35
- 239000004519 grease Substances 0.000 title claims abstract description 13
- 239000003921 oil Substances 0.000 claims abstract description 62
- 239000010779 crude oil Substances 0.000 claims description 2
- 230000000694 effects Effects 0.000 claims description 2
- 239000010913 used oil Substances 0.000 claims 4
- 238000000034 method Methods 0.000 abstract description 11
- 235000014113 dietary fatty acids Nutrition 0.000 abstract description 4
- 229930195729 fatty acid Natural products 0.000 abstract description 4
- 239000000194 fatty acid Substances 0.000 abstract description 4
- 150000004665 fatty acids Chemical class 0.000 abstract description 4
- 239000010724 circulating oil Substances 0.000 abstract description 2
- 238000007670 refining Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000002253 acid Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000004042 decolorization Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000008157 edible vegetable oil Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 235000021588 free fatty acids Nutrition 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 235000019645 odor Nutrition 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 235000021122 unsaturated fatty acids Nutrition 0.000 description 1
- 150000004670 unsaturated fatty acids Chemical class 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- Fats And Perfumes (AREA)
Abstract
本发明涉及一种高真空度油脂脱臭装置,具体涉及一种高真空度下的油脂脱臭装置,用于油脂脱臭。解决了目前脱臭塔应用中脱臭率不高,油脂反式脂肪酸较高,脱臭油色较深等问题,旨在为油脂脱臭工艺创造出一个合理可行的新型脱臭工艺设备。本发明为解决上述技术问题采取的技术方案是:一种高真空度下油脂的脱臭装置,它包括装置壳体、加热器和回油管,加热器由上至下设置在装置壳体内的中心处,多个圆形加热器组围绕内壳体,装置壳体的上端设置有进油管侧面设置有出油口,装置壳体的下端设置有循环油管。The invention relates to a high-vacuum oil deodorization device, in particular to a high-vacuum oil deodorization device for oil deodorization. It solves the problems of low deodorization rate, high oil trans fatty acid, and deep deodorized oil color in the current deodorization tower application, and aims to create a reasonable and feasible new deodorization process equipment for the oil deodorization process. The technical scheme adopted by the present invention to solve the above technical problems is: a deodorization device for grease under high vacuum, which includes a device housing, a heater and an oil return pipe, and the heater is arranged at the center of the device housing from top to bottom , a plurality of circular heater groups surround the inner casing, the upper end of the device casing is provided with an oil inlet pipe and the side is provided with an oil outlet, and the lower end of the device casing is provided with a circulating oil pipe.
Description
技术领域 technical field
本发明涉及一种油脂脱臭装置,具体涉及一种高真空度下的油脂脱臭装置。 The invention relates to a grease deodorization device, in particular to a grease deodorization device under high vacuum.
背景技术 Background technique
油脂的豆腥味产生主要来源于油脂中的某些可挥发性物质,而油脂豆腥味的品质与油脂中脂肪酸的组成含量密切相关。这主要是因为油脂中的游离脂肪酸特别是一些不饱和脂肪酸,它们的不饱和键极易发生加成等化学反应,生成具有独特“气味”的化合物而使油具有豆腥味。所以对于高品质的油脂产品尤其是食用油脂产品,采用脱臭的方法除去油脂中不必要的气味,以改善油的品质和稳定性。 The beany smell of oil is mainly derived from some volatile substances in oil, and the quality of beany smell of oil is closely related to the composition and content of fatty acids in oil. This is mainly because the free fatty acids in the oil, especially some unsaturated fatty acids, are very prone to chemical reactions such as addition to their unsaturated bonds, forming compounds with a unique "smell", which makes the oil have a beany smell. Therefore, for high-quality oil products, especially edible oil products, the deodorization method is used to remove unnecessary odors in the oil to improve the quality and stability of the oil.
在油脂的精炼加工过程中,脱臭工艺是非常重要的工序和操作单元,其主要设备脱臭塔又是整个油脂脱臭工艺中的核心;目前国内油脂精炼工艺中使用较多的脱臭塔主要分:板式塔、填料塔和软塔等几种;而在实际生产中应用最为普遍的是板式塔。 In the oil refining process, the deodorization process is a very important process and operation unit, and its main equipment, the deodorization tower, is the core of the entire oil deodorization process; at present, the deodorization towers used more in the domestic oil refining process are mainly divided into: plate type There are several types of towers, packed towers and soft towers; and the most commonly used in actual production is the plate tower.
发明内容 Contents of the invention
本发明的目的是提供一种高真空度下油脂脱臭装置,以解决目前低真空度条件下脱臭,反式脂肪酸含量较高,油脂颜色较深,脱臭率较低,能源浪费较高的问题,旨在为油脂脱臭工艺发明出一个合理可行的脱臭工艺设备。 The purpose of the present invention is to provide a grease deodorization device under high vacuum degree to solve the problems of deodorization under low vacuum degree, high content of trans fatty acid, dark oil color, low deodorization rate and high energy waste. The purpose is to invent a reasonable and feasible deodorization process equipment for the oil deodorization process.
本发明为解决上述技术问题采取的技术方案是:一种高真空度下油脂脱臭装置,它包括装置壳体、加热器和回油管,加热器由上至下设置在装置壳体内的中心处,多个圆形加热器组围绕内壳体,装置壳体的上端设置有进油管侧面设置有出油口,装置壳体的下端设置有循环油管。 The technical solution adopted by the present invention to solve the above technical problems is: a high-vacuum grease deodorization device, which includes a device housing, a heater and an oil return pipe, and the heater is arranged at the center of the device housing from top to bottom. A plurality of circular heater groups surround the inner casing, the upper end of the device casing is provided with an oil inlet pipe and the side is provided with an oil outlet, and the lower end of the device casing is provided with a circulating oil pipe.
上述高真空度脱臭塔结构简单,可操作性强,脱色油进入脱臭塔后,物料在高真空度状态下进行加热,在脱除臭味组分的同时,由于每层塔板的独特均格结构,油脂的被动延长了油脂在脱臭塔中的停留时间,使得油脂中的热敏性色素彻底分解,从而起到很好的热脱色效果。 The above-mentioned high-vacuum deodorization tower has a simple structure and strong operability. After the decolorized oil enters the deodorization tower, the material is heated in a high-vacuum state. The passive structure of the oil prolongs the residence time of the oil in the deodorization tower, so that the heat-sensitive pigment in the oil is completely decomposed, thus achieving a good thermal decolorization effect.
本发明具有以下有益效果:每吨脱臭油脂蒸汽用量为15~25kg,脱臭后油脂酸价为0.17~0.27(KOH)/(mg/g),提高油脂精炼率0.5~0.7%,反式脂肪酸含量低为13.2%,油脂色泽降低17~33%,脱臭率提高26~33%,节省能源30%,有利于实现大规模的工业生产,具有很强的连续性和生产稳定性,可用于多种油料的生产精炼,且操作简便,维护保养简单易行。 The invention has the following beneficial effects: the amount of steam per ton of deodorized oil is 15-25kg, the acid value of oil after deodorization is 0.17-0.27 (KOH)/(mg/g), the refining rate of oil is increased by 0.5-0.7%, and the content of trans fatty acid The lowest is 13.2%, the color of oil is reduced by 17-33%, the deodorization rate is increased by 26-33%, and the energy is saved by 30%. It is beneficial to realize large-scale industrial production, has strong continuity and production stability, and can be used in various The production of oil is refined, and the operation is simple, and the maintenance is simple and easy.
附图说明 Description of drawings
图1是本发明的整体结构示意图。 Fig. 1 is a schematic diagram of the overall structure of the present invention.
具体实施方式 Detailed ways
具体实施方式一:结合图1说明本实施方式,本实施方式包括装置外壳体(3)、内壳体(6),回油管(2)和设置在反应器内壳体(6)内的多个加热器组(5),加热器(5)由上至下设置在装置壳体内的中心处,多个圆形加热器组(5)围绕内壳体(6)均匀排列成一个圆圈,内壳体(6)的上端设置有进油管(4),装置外壳体的上端设置有出油管(7)。 Specific embodiment 1: This embodiment is described in conjunction with Fig. 1. This embodiment includes the outer casing (3), the inner casing (6), the oil return pipe (2) and the multiple reactors arranged in the inner casing (6) of the reactor. A heater group (5), the heater (5) is arranged in the center of the device casing from top to bottom, a plurality of circular heater groups (5) are evenly arranged in a circle around the inner casing (6), and the inner An oil inlet pipe (4) is arranged on the upper end of the casing (6), and an oil outlet pipe (7) is arranged on the upper end of the outer casing of the device.
装置内壳体(6)与外壳体(3)为圆形,外壳体内有回油管(2),回油管(2)的下端连接有电动机(1),原油由进油管(4)进入装置内壳体(6)内,在加热器(5)作用下,经回油管(2)进入外壳体(3)内对内壳体(6)内油进行换热,然后经出油管(7)出油。 The inner casing (6) and the outer casing (3) of the device are circular, and there is an oil return pipe (2) in the outer casing, and the lower end of the oil return pipe (2) is connected to the motor (1), and the crude oil enters the device through the oil inlet pipe (4) In the casing (6), under the action of the heater (5), it enters the outer casing (3) through the oil return pipe (2) to exchange heat with the oil in the inner casing (6), and then exits through the oil outlet pipe (7) Oil.
每吨脱臭油脂需要蒸汽用量为15~25kg,脱臭后油脂酸价为0.17~0.27(KOH)/(mg/g),能耗节省30%,提高油脂精炼率0.5~0.7%,色泽降低17~32%,脱臭率提高26~33%。 Each ton of deodorized oil requires 15~25kg of steam, the acid value of the oil after deodorization is 0.17~0.27 (KOH)/(mg/g), the energy consumption is saved by 30%, the oil refining rate is increased by 0.5~0.7%, and the color is reduced by 17~ 32%, and the deodorization rate increased by 26~33%.
设备参数指标:脱臭塔高13m,外壳体直径5m,内壳体直径为4m,进油管与出油管直径为300mm,圆形加热器每层共6个,直径为0.5m,回油管高10m,出油管高为8m。工作原理:待脱臭油脂由进油管4进入脱臭塔,经过加热器5进行加热,依次进入六个层面进行加热,带加热完成后经由回油管2再次进入到脱臭塔中,再依次经过二至四层面,再经出油管7出油。 Equipment parameters and indicators: the height of the deodorization tower is 13m, the diameter of the outer shell is 5m, the diameter of the inner shell is 4m, the diameter of the oil inlet pipe and the oil outlet pipe is 300mm, there are 6 circular heaters in each layer, the diameter is 0.5m, and the height of the oil return pipe is 10m. The oil outlet pipe is 8m high. Working principle: The oil to be deodorized enters the deodorization tower from the oil inlet pipe 4, is heated by the heater 5, and enters six levels for heating in turn. After the heating is completed, it enters the deodorization tower again through the oil return pipe 2, and then passes through the second to fourth level, and then through the oil outlet pipe 7 oil.
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Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB648310A (en) * | 1946-02-21 | 1951-01-03 | Girdler Corp | Method and apparatus for removing gaseous and readily vaporizable materials from liquids |
CN101185466A (en) * | 2007-12-18 | 2008-05-28 | 杨孟君 | Alkalization, decolorizing and deodorization integration pan for camellia oil precision machining |
CN201686672U (en) * | 2010-04-16 | 2010-12-29 | 武汉友谊食品工程有限公司 | Combined double-casing deacidification deodorizing tower |
CN203200235U (en) * | 2013-01-18 | 2013-09-18 | 武汉友谊食品工程有限公司 | Deodorization tower for grease processing |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
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ATE312151T1 (en) * | 2001-05-14 | 2005-12-15 | Smet Engineering N V De | APPARATUS AND METHOD FOR THE PHYSICAL REFINING AND/OR DEODORIZATION OF EDIBLE OILS AND FATS |
CN203999549U (en) * | 2013-10-12 | 2014-12-10 | 东北农业大学 | Fuel-displaced deodorization device under a kind of condition of high vacuum degree |
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Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB648310A (en) * | 1946-02-21 | 1951-01-03 | Girdler Corp | Method and apparatus for removing gaseous and readily vaporizable materials from liquids |
CN101185466A (en) * | 2007-12-18 | 2008-05-28 | 杨孟君 | Alkalization, decolorizing and deodorization integration pan for camellia oil precision machining |
CN201686672U (en) * | 2010-04-16 | 2010-12-29 | 武汉友谊食品工程有限公司 | Combined double-casing deacidification deodorizing tower |
CN203200235U (en) * | 2013-01-18 | 2013-09-18 | 武汉友谊食品工程有限公司 | Deodorization tower for grease processing |
Non-Patent Citations (1)
Title |
---|
"五层双壳体脱臭塔在生产中的应用";严有兵等;《中国油脂》;20001231;第25卷(第5期);第10-12页 * |
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Effective date of registration: 20170822 Address after: Xiangfang District of Heilongjiang city of Harbin province haping road 150001 No. 1 Patentee after: The 93 group Harbin Wellcome Food Co. Ltd. Address before: 150030 Xiangfang City, Harbin Province Wood Street, No. 59, No. Patentee before: Northeast Agricultural University |
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Address after: 150001 No.1, haping East Road, Xiangfang District, Harbin City, Heilongjiang Province Patentee after: Jiusan Food Co.,Ltd. Address before: 150001 No.1, haping East Road, Xiangfang District, Harbin City, Heilongjiang Province Patentee before: THE NINE THREE GROUP HARBIN WELLCOME FOOD Co.,Ltd. |
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