WO2020073350A1 - Processing technology of barley malt - Google Patents

Processing technology of barley malt Download PDF

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Publication number
WO2020073350A1
WO2020073350A1 PCT/CN2018/110786 CN2018110786W WO2020073350A1 WO 2020073350 A1 WO2020073350 A1 WO 2020073350A1 CN 2018110786 W CN2018110786 W CN 2018110786W WO 2020073350 A1 WO2020073350 A1 WO 2020073350A1
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Prior art keywords
barley
malt
wheat
germination
drying
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PCT/CN2018/110786
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French (fr)
Chinese (zh)
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徐根弟
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徐根弟
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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12CBEER; PREPARATION OF BEER BY FERMENTATION; PREPARATION OF MALT FOR MAKING BEER; PREPARATION OF HOPS FOR MAKING BEER
    • C12C1/00Preparation of malt
    • C12C1/125Continuous or semi-continuous processes for steeping, germinating or drying

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  • the invention belongs to the technical field of deep processing of crops, and specifically relates to a processing technology of barley malt.
  • Barley malt is obtained by germinating and drying the mature fruit of barley. It is a major barley processed product and an essential raw material for making beer.
  • beer malt has high quality requirements. Not only does it have a strict length for the leaf bud length, it should not exceed 80% of the grain, but also requires ultra-low inclusions, high cell lysis uniformity, suitable protein content, and malt color and PH meet the requirements. Therefore, the production of beer malt is very delicate, and each step has strict quality requirements, such as dipping method, temperature control, etc. More importantly, there are more stringent requirements on malt turbidity.
  • the wort made from malt has a high turbidity because it contains a large amount of fatty acids, cellulose, hemicellulose, and high molecular nitrogen. During the fermentation stage, yeast is in such a turbid wort, and it is very prone to bacterial degradation.
  • the purpose of the present invention is to provide a processing technology for barley malt which has the problems of high malt content, high wort turbidity, low pass rate, complicated procedures, and high cost in the existing wheat-making process.
  • the process is simple, It is suitable for mass production, and it has few malt inclusions, uniform length, containing trace elements such as selenium, high nutritional content, low malt wort turbidity, and good quality.
  • the technical solution provided by the present invention is: a processing technology of barley malt, including the following steps:
  • Raw material processing The raw material barley is sent to the air separation vibrating screen with a bucket elevator, passes through the stone remover, classifier, electronic scale, and enters the selected barley silo.
  • the barley selection uses the selected machine and is equipped with a pulse type
  • the bag dust collector is used, the content of the processed barley inclusions is within 0.2%, and the classification degree of the barley reaches more than 95%;
  • Germination 4 germination boxes are placed in the lower layer of the wheat immersion tank, the barley after impregnation in step (2) is transported layer by layer to the germination box, then flattened with a combination machine, and the wheat is turned every 8 hours , Spray twice at the 10th and 40th hours of germination. Before germination and spraying, add 0.005-0.015% sodium selenite to the barley, the germination time should be controlled at 70 ⁇ 100 hour;
  • step (3) The green malt germinated in step (3) is moved to the germination tower through the unloader, belt conveyor, bucket elevator, and sent to the drying box.
  • the green malt goes through the withering, drying and coking stage, and finally dried When the moisture content is ⁇ 5%, the drying time is controlled at 20-23 hours;
  • Root removal The malt after the drying in step (4) is sent to the dry malt temporary storage silo through the bucket elevator, and then the root is removed by the root removal machine, and then entered into the malt silo with the bucket elevator, and the malt is removed from the warehouse
  • the material system is sent to the air separation vibrating screen and packed after measurement.
  • the row of floating wheat in the step (2) adopts water suction overflow to remove floating wheat.
  • the step (2) is provided with a wheat soaking temperature regulating water tank, and the temperature of the wheat soaking water is adjusted at 13-18 ° C.
  • the mass ratio of 6-phytase and xylanase in the mixture of 6-phytase and xylanase in the step (2) is 1: 1, and the 6-plant
  • the mixture of acidase and xylanase is first made into an aqueous solution with a mass concentration of 10%, and then added uniformly by spraying.
  • the sodium selenite in the step (3) is first made into an aqueous solution with a mass concentration of 1%, and then evenly distributed to the two germination sprays and added evenly by spraying.
  • water should be sprayed according to the growth of malt, and gibberellic acid should be added at 0.5-1% of the total weight of the barley.
  • the cooling of the germination surface cooler in the step (3) is directly cooled by an ammonia pump, and a humidifying device and a hot water pipe spraying device are provided under the bed.
  • the step (4) drying uses steam indirect heating, and the drying temperature is 45-85 ° C.
  • the beneficial effects of the present invention are: the process adopts an improved tower germination process, and at the same time, a mixed enzyme of 6-phytase and xylanase is added to the wheat steeping process to promote the dissolution and separation of intercalation, and is added in the early stage of germination Sodium selenite solution, so that the wort turbidity is below 1.5EBC, the breakage rate is below 0.5%, the malt selenium content is above 28 ⁇ g / kg, the process is simple, suitable for batch production, the malt length is uniform, and the composition consistency is high , High nutritional value, especially suitable for the production of beer raw materials.
  • Figure 1 is a process flow diagram of the present invention.
  • the process flow of the present invention can be divided into five processes: raw material processing, wheat making, dry oven drying, rooting machine rooting, packaging, and storage.
  • raw material processing wheat making, dry oven drying, rooting machine rooting, packaging, and storage.
  • the following examples only deal with raw material processing
  • the processes of wheat making, drying in a drying oven, and root removing machine are described in detail.
  • the cone bottom dipping tank (180m 3 ) and the germination box are placed in the germination tower.
  • the dipping tank and the germination box are arranged above and below, and there is a tower transportation between the dipping tank and the germination box
  • the pipeline relies on gravity to run the barley.
  • the wheat immersion tank uses 180m 3 of the wheat immersion tank. 6 horizontal and parallel layouts.
  • the wheat immersion tank is made of stainless steel.
  • the bottom of the wheat immersion tank cone is equipped with an opening for cleaning the false bottom for cleaning and sanitation.
  • 1 1 ventilator for wheat immersion tank using water circulation air compressor to reduce the temperature of the air
  • each immersion tank is equipped with a CO 2 suction fan, and the floating wheat is removed by water suction to remove the floating wheat. It is equipped with a wheat soaking temperature regulating water tank to ensure that the wheat soaking water temperature can be adjusted in winter and summer to the temperature range required by the process in 13 ⁇ 18 °C;
  • step (1) The barley processed in step (1) is subjected to the integrated wheat immersion method of water immersion, blasting and CO 2 extraction.
  • the whole wheat immersion process is carried out according to the process of immersing three times and breaking four times.
  • the process is controlled by four processes: timed air blowing, spraying, floating wheat, and CO 2 suction.
  • timed air blowing, spraying, floating wheat, and CO 2 suction During the spraying process of wheat soaking, first add 6% phytase and 3% of the total weight of barley to the barley with a sprayer.
  • the mixture of xylanase, the mixture of 6-phytase and xylanase in the mixture of 6-phytase and xylanase has a mass ratio of 1: 1, 6-phytase and xylanase
  • the mixture is first prepared into an aqueous solution with a mass concentration of 10%, and the wheat is soaked for 20 hours, the barley soaking degree obtained is 42%, and the dew point rate is 72%;
  • the germination adopts 4 germination boxes, and the germination box with a diameter of 29 meters is selected. Each germination box is independent.
  • the germination room adopts independent air conditioning system, that is, each has its own ventilation, cooling and return air.
  • the germination fan is equipped with a frequency converter and a sieve plate It is made of stainless steel, the structure is flat screen surface and bottom frame, and the germination surface cooler is cooled by ammonia pump directly.
  • step (2) The impregnated barley obtained in step (2) is transported layer by layer to 4 germination boxes, then paved with a combination machine (ZP-90), and turned over with a wheat turning machine (ZFM7.0 * 2.0) every 8 hours Once, to ensure that the temperature difference between the upper and lower layers reaches 3-4 °C, spray them with water once at the 10th and 40th hours of germination, and divide the aqueous solution of sodium selenite formulated into a mass concentration of 1% into two parts first.
  • ZP-90 combination machine
  • ZFM7.0 * 2.0 a wheat turning machine
  • the total amount of sodium selenite is 0.005% of the total weight of barley, then spray with water, add 0.5% gibberellic acid to the total weight of the barley in the spray water, and control the germination time at 70 hours;
  • the germinated green malt obtained in step (3) is moved to the germination tower through a double pear point multi-point unloading belt conveyor and a bucket elevator, and sent to a drying box (GFG-20).
  • the green malt is withered and dried 3.
  • the final drying is to a moisture content of 5% or less.
  • the entire drying process can adjust the steam flow according to the temperature and air volume of the drying chamber, and can also adjust the return air volume according to the outdoor temperature and process requirements in different stages to save energy and eliminate moisture.
  • the period air volume is 4000-4500 cubic meters per ton of green malt.
  • the drying time is controlled at 20 hours (including auxiliary time). It is completed by a ⁇ 42m round drying furnace (GFG-20).
  • Drying adopts indirect steam heating method, withered layer Drying temperature control 45-68 °C, time 16-18 hours, baking coke layer temperature control 65-85 °C, time 2-4 hours, equipped with waste heat recovery device in the drying furnace, waste heat recovery tube adopts aluminum alloy tube, drying furnace Equipped with 4 blowers (L52WD), equipped with frequency converter, to automatically control the power on and off according to the temperature;
  • step (4) drying the malt fresh air is used to cool the wheat layer to 40-45 ° C, and then it is sent to a dry malt temporary storage silo through a bucket elevator, and then passes through two de-rooting machines (model CG-15 ) Root removal, processing capacity is 40t / h, measurement after root removal, bucket elevator enters the malt silo, the malt out of the warehouse is sent to the air separation vibrating screen through the batching system, and is automatically packaged through the electronic weighing scale.
  • the root removal system is equipped with 1 set of pulses Bag dust collector.
  • the malt obtained was tested, the wort turbidity was 1.4EBC, the breakage rate was below 0.5%, and the selenium content was 28 ⁇ g / kg.
  • the cone bottom dipping tank (180m 3 ) and the germination box are placed in the germination tower.
  • the dipping tank and the germination box are arranged above and below, and there is a tower transportation between the dipping tank and the germination box
  • the pipeline relies on gravity to run the barley.
  • the wheat immersion tank uses 180m 3 of the wheat immersion tank. 6 horizontal and parallel layouts.
  • the wheat immersion tank is made of stainless steel.
  • the bottom of the wheat immersion tank cone is equipped with an opening for cleaning the false bottom for cleaning and sanitation.
  • 1 1 ventilator for wheat immersion tank using water circulation air compressor to reduce the temperature of the air
  • each immersion tank is equipped with a CO 2 suction fan, and the floating wheat is removed by water suction to remove the floating wheat.
  • Set the temperature control tank for soaking wheat to ensure that the temperature of soaking wheat can be adjusted to the temperature range of 13 ⁇ 18 °C in winter and summer;
  • step (1) The barley processed in step (1) is subjected to the integrated wheat immersion method of water immersion, blasting and CO 2 extraction.
  • the whole wheat immersion process is carried out according to the process of immersing three times and breaking four times.
  • the process is controlled by four processes: timed air blowing, spraying, floating wheat, and CO 2 suction.
  • timed air blowing timed air blowing
  • spraying floating wheat
  • CO 2 suction During the spraying process, the 6-phytase and 4% of the total weight of barley are added to the barley with a sprayer.
  • the mixture of xylanase, the mixture of 6-phytase and xylanase in the mixture of 6-phytase and xylanase has a mass ratio of 1: 1, 6-phytase and xylanase
  • the mixture is first formulated into an aqueous solution with a mass concentration of 10%, soaked in wheat for 21 hours, the barley soaking degree obtained is 48%, and the dew point rate is 82%;
  • the germination adopts 4 germination boxes, and the germination box with a diameter of 29 meters is selected, each germination box is independent, and an independent air conditioning system is used in the germination room, that is, each has its own ventilation, cooling and return air, and the germination fan is equipped with a frequency converter to achieve effective Control process parameters while saving electrical energy.
  • the sieve plate is made of stainless steel.
  • the structure is a flat screen surface with a bottom frame.
  • the germination surface cooler is cooled directly by an ammonia pump.
  • step (2) The impregnated barley obtained in step (2) is transported layer by layer to 4 germination boxes, then paved with a combination machine (ZP-90), and turned over with a wheat turning machine (ZFM7.0 * 2.0) every 8 hours Once, to ensure that the temperature difference between the upper and lower layers reaches 3-4 °C, spray them with water once at the 10th and 40th hours of germination, and divide the aqueous solution of sodium selenite formulated into a mass concentration of 1% into two parts first.
  • ZP-90 combination machine
  • ZFM7.0 * 2.0 a wheat turning machine
  • the total amount of sodium selenite is 0.010% of the total weight of barley, then spray with water, add gibberellic acid 0.75% of the total weight of the barley in the spraying water, and control the germination time at 85 hours;
  • the germinated green malt obtained in step (3) is moved to the germination tower through a double pear point multi-point unloading belt conveyor and a bucket elevator, and sent to a drying box (GFG-20).
  • the green malt is withered and dried 3.
  • the final drying is to a moisture content of 5% or less.
  • the entire drying process can adjust the steam flow according to the temperature and air volume of the drying chamber, and can also adjust the return air volume according to the outdoor temperature and process requirements in different stages to save energy and eliminate moisture.
  • the period air volume is 4000-4500 cubic meters per ton of green malt.
  • the drying time is controlled at 22 hours (including auxiliary time). It is completed by a ⁇ 42m circular drying furnace (GFG-20).
  • the drying uses steam indirect heating and the withered layer Drying temperature control 45-68 °C, time 16-18 hours, baking coke layer temperature control 65-85 °C, time 2-4 hours, equipped with waste heat recovery device in the drying furnace, waste heat recovery tube adopts aluminum alloy tube, drying furnace Equipped with 4 blowers (L52WD), equipped with frequency converter, to automatically control the power on and off according to the temperature;
  • step (4) drying the malt fresh air is used to cool the wheat layer to 40-45 ° C, and then it is sent to a dry malt temporary storage silo through a bucket elevator, and then passes through two de-rooting machines (model CG-15 ) Root removal, processing capacity is 40t / h, measurement after root removal, bucket elevator enters the malt silo, the malt out of the warehouse is sent to the air separation vibrating screen through the batching system, and is automatically packaged through the electronic weighing scale.
  • the root removal system is equipped with 1 set of pulses Bag dust collector.
  • the malt obtained was tested, the wort turbidity was 1.2EBC, the breakage rate was below 0.5%, and the selenium content was 30 ⁇ g / kg.
  • the cone bottom dipping tank (180m 3 ) and the germination box are placed in the germination tower.
  • the dipping tank and the germination box are arranged above and below, and there is a tower transportation between the dipping tank and the germination box
  • the pipeline relies on gravity to run the barley.
  • the wheat immersion tank uses 180m 3 of the wheat immersion tank. 6 horizontal and parallel layouts.
  • the wheat immersion tank is made of stainless steel.
  • the bottom of the wheat immersion tank cone is equipped with an opening for cleaning the false bottom for cleaning and sanitation.
  • 1 1 ventilator for wheat immersion tank using water circulation air compressor to reduce the temperature of the air
  • each immersion tank is equipped with a CO 2 suction fan, and the floating wheat is removed by water suction to remove the floating wheat.
  • Set the temperature control tank for soaking wheat to ensure that the temperature of soaking wheat can be adjusted to the temperature range of 13 ⁇ 18 °C in winter and summer;
  • step (1) The barley processed in step (1) is subjected to the integrated wheat immersion method of water immersion, blasting and CO 2 extraction.
  • the whole wheat immersion process is carried out according to the process of immersing three times and breaking four times.
  • the process is controlled by four processes: regular air blowing, spraying, floating wheat, and CO 2 suction.
  • the germination adopts 4 germination boxes, and the germination box with a diameter of 29 meters is selected, each germination box is independent, and an independent air conditioning system is used in the germination room, that is, each has its own ventilation, cooling and return air, and the germination fan is equipped with a frequency converter to achieve effective Control process parameters while saving electrical energy.
  • the sieve plate is made of stainless steel.
  • the structure is a flat screen surface with a bottom frame.
  • the germination surface cooler is cooled directly by an ammonia pump.
  • step (2) The impregnated barley obtained in step (2) is transported layer by layer to 4 germination boxes, then paved with a combination machine (ZP-90), and turned over with a wheat turning machine (ZFM7.0 * 2.0) every 8 hours Once, to ensure that the temperature difference between the upper and lower layers reaches 3-4 °C, spray them with water once at the 10th and 40th hours of germination, and divide the aqueous solution of sodium selenite formulated into a mass concentration of 1% into two parts first. Before spraying, spray with a sprayer. The total amount of sodium selenite is 0.015% of the total weight of barley. Then spray with water. Add 1% of gibberellic acid to the total weight of barley in the spraying water, and control the germination time at 100 hours;
  • the germinated green malt obtained in step (3) is moved to the germination tower through a double pear point multi-point unloading belt conveyor and a bucket elevator, and sent to a drying box (GFG-20).
  • the green malt is withered and dried 3.
  • the final drying is to a moisture content of 5% or less.
  • the entire drying process can adjust the steam flow according to the temperature and air volume of the drying chamber, and can also adjust the return air volume according to the outdoor temperature and process requirements in different stages to save energy and eliminate moisture.
  • the period of air volume is 4000-4500 cubic meters / ton of green malt.
  • the drying time is controlled at 23 hours (including auxiliary time). It is completed by a ⁇ 42m circular drying furnace (GFG-20).
  • Drying adopts steam indirect heating method, withered layer Drying temperature control 45-68 °C, time 16-18 hours, baking coke layer temperature control 65-85 °C, time 2-4 hours, equipped with waste heat recovery device in the drying furnace, waste heat recovery tube adopts aluminum alloy tube, drying furnace Equipped with 4 blowers (L52WD), equipped with frequency converter, to automatically control the power on and off according to the temperature;
  • step (4) drying the malt fresh air is used to cool the wheat layer to 40-45 ° C, and then it is sent to a dry malt temporary storage silo through a bucket elevator, and then passes through two de-rooting machines (model CG-15 ) Root removal, processing capacity is 40t / h, measurement after root removal, bucket elevator enters the malt silo, the malt out of the warehouse is sent to the air separation vibrating screen through the batching system, and is automatically packaged through the electronic weighing scale. Bag dust collector.
  • the malt obtained was tested, the wort turbidity was 1.3EBC, the breakage rate was below 0.5%, and the selenium content was 31 ⁇ g / kg.

Abstract

A processing technology of barley malt, comprising the following steps: (1) processing raw materials; (2) soaking barley malt; (3) germinating; (4) drying; (5) grubbing. A mixture of 6-phytase and xylanase is added in the barley malt soaking step, and sodium selenite is added in the germinating step. Barley malt with wort turbidity below 1.5 EBC, breakage rate below 0.5%, and selenium content above 28 μg/kg is obtained by the steps. The technology is simple in processes and suitable for mass production, and the obtained barely malt has less inclusions, and is uniform in length, high in component consistency and low in turbidity, thereby improving the quality of the barley malt and reducing production costs; the barely malt is particularly applicable to raw materials for producing beer.

Description

一种大麦麦芽的加工工艺Processing technology of barley malt 技术领域Technical field
本发明属于农作物深加工的技术领域,具体的涉及一种大麦麦芽的加工工艺。The invention belongs to the technical field of deep processing of crops, and specifically relates to a processing technology of barley malt.
背景技术Background technique
大麦麦芽是通过大麦的成熟果实经发芽干燥而得,是一种主要的大麦加工产品,也是制造啤酒的必备原料。Barley malt is obtained by germinating and drying the mature fruit of barley. It is a major barley processed product and an essential raw material for making beer.
众所周知,啤酒麦芽质量要求较高,不仅对叶芽长度有严格的长度,不宜超过麦粒的80%,还要求夹杂物超低,细胞溶解均一性高,蛋白质含量适宜,麦芽色度、PH符合要求,因而啤酒麦芽的生产非常精细,每一步都有严格的质量要求,比如浸渍方式、温度控制等。更重要的是对麦芽浊度有更苟刻的要求。麦芽制成的麦汁浊度高是因为其中含有大量的脂肪酸、纤维素、半纤维素及高分子氮等物质,在发酵阶段,酵母处于这样浑浊的麦汁中,极易出现菌种退化,在升压后酵母数会明显减少,双乙酰还原减慢,酒龄延长,对啤酒酿造产生极坏的影响。而产生这些浊度物质的主要原因是大麦原料质量个体差异较大,而目前的制麦工艺主要是作坊式作业,大麦麦芽质量不高,产量低,成本低,并且微量元素也会流失。As we all know, beer malt has high quality requirements. Not only does it have a strict length for the leaf bud length, it should not exceed 80% of the grain, but also requires ultra-low inclusions, high cell lysis uniformity, suitable protein content, and malt color and PH meet the requirements. Therefore, the production of beer malt is very delicate, and each step has strict quality requirements, such as dipping method, temperature control, etc. More importantly, there are more stringent requirements on malt turbidity. The wort made from malt has a high turbidity because it contains a large amount of fatty acids, cellulose, hemicellulose, and high molecular nitrogen. During the fermentation stage, yeast is in such a turbid wort, and it is very prone to bacterial degradation. After the pressure increase, the number of yeast will be significantly reduced, the reduction of diacetyl reduction, and the age of the wine will be prolonged, which will have a very bad effect on beer brewing. The main reason for producing these turbid substances is that the quality of barley raw materials varies greatly, and the current wheat-making process is mainly a workshop-style operation. The quality of barley malt is not high, the output is low, the cost is low, and trace elements are also lost.
发明内容Summary of the invention
本发明的目的为解决现有制麦工艺中存在麦芽杂质含量多,麦汁浊度高,同时合格率低,工序繁杂,成本高等问题而提供的一种大麦麦芽的加工工艺,该工艺简单,适合批量化生产,且麦芽夹杂少,长短均匀,含有硒等微量元素,营养成分高,麦芽麦汁浊度低,品质好。The purpose of the present invention is to provide a processing technology for barley malt which has the problems of high malt content, high wort turbidity, low pass rate, complicated procedures, and high cost in the existing wheat-making process. The process is simple, It is suitable for mass production, and it has few malt inclusions, uniform length, containing trace elements such as selenium, high nutritional content, low malt wort turbidity, and good quality.
为实现上述目的,本发明提供的技术方案为:一种大麦麦芽的加工工艺,包括以下步骤:In order to achieve the above object, the technical solution provided by the present invention is: a processing technology of barley malt, including the following steps:
(1)原料处理:将原料大麦用斗式提升机送至风选振动筛,经过除石机、分级机、电子称,进入精选大麦仓,大麦精选采用精选机,并配置脉冲式布袋除尘器进行,处理过的大麦夹杂物的含量在0.2%以内,大麦的分级度达到95%以上;(1) Raw material processing: The raw material barley is sent to the air separation vibrating screen with a bucket elevator, passes through the stone remover, classifier, electronic scale, and enters the selected barley silo. The barley selection uses the selected machine and is equipped with a pulse type The bag dust collector is used, the content of the processed barley inclusions is within 0.2%, and the classification degree of the barley reaches more than 95%;
(2)浸麦:采用塔式发芽工艺,采用六个水平、平行布置的锥底浸麦槽置于塔的最上层,每个浸麦槽分别配备通风机和二氧化碳吸风机,将步骤(1)处理过的原料大麦按照鼓风、喷淋、排浮麦、抽吸二氧化碳的步骤进行,侵麦喷淋前先向大麦中加入占大麦总重量的3~5%的6-植酸酶和木聚糖酶的混合物,浸麦度为42~48%、露点率达71~82%;(2) Wheat immersion: adopt the tower type germination process, adopt six horizontal and parallel arrangement cone-shaped wheat immersion tanks placed on the uppermost layer of the tower, each wheat immersion tank is equipped with a fan and a carbon dioxide suction fan respectively. ) The processed raw barley is carried out in accordance with the steps of blasting, spraying, floating wheat, and pumping carbon dioxide. Before invading and spraying, add 3-5% phytase and 3-phytase to the barley to the total weight of the barley. The mixture of xylanase has a immersion degree of 42-48% and a dew point rate of 71-82%;
(3)发芽:采用4个发芽箱置于浸麦槽的下层,将步骤(2)浸渍后的大麦通过管道逐层输送到发芽箱,再用组合机铺平,每隔8小时翻麦一次,在开始发芽的第10小时和第40小时分别喷淋两次,发芽喷淋前应先向大麦中添加占大麦总重量的0.005-0.015%的亚硒酸钠,发芽时间控制在70~100小时;(3) Germination: 4 germination boxes are placed in the lower layer of the wheat immersion tank, the barley after impregnation in step (2) is transported layer by layer to the germination box, then flattened with a combination machine, and the wheat is turned every 8 hours , Spray twice at the 10th and 40th hours of germination. Before germination and spraying, add 0.005-0.015% sodium selenite to the barley, the germination time should be controlled at 70 ~ 100 hour;
(4)干燥:将步骤(3)发芽完毕的绿麦芽通过卸料机、皮带机、斗式提升机移出发芽塔,送入干燥箱,绿麦芽经过凋萎、干燥、焙焦阶段,最终干燥到含水份≤5%,干燥时间控制在20~23小时;(4) Drying: The green malt germinated in step (3) is moved to the germination tower through the unloader, belt conveyor, bucket elevator, and sent to the drying box. The green malt goes through the withering, drying and coking stage, and finally dried When the moisture content is ≤5%, the drying time is controlled at 20-23 hours;
(5)除根:将步骤(4)干燥完成后的麦芽经斗式提升机送至干麦芽暂贮仓,然后经过除根机除根,再用斗式提升机进入麦芽立仓,麦芽出仓经过兑料系统送至风选振动筛,计量后打包。(5) Root removal: The malt after the drying in step (4) is sent to the dry malt temporary storage silo through the bucket elevator, and then the root is removed by the root removal machine, and then entered into the malt silo with the bucket elevator, and the malt is removed from the warehouse The material system is sent to the air separation vibrating screen and packed after measurement.
作为优选的技术方案,所述步骤(2)中排浮麦采用水吸式溢流,去除浮麦。As a preferred technical solution, the row of floating wheat in the step (2) adopts water suction overflow to remove floating wheat.
作为优选的技术方案,所述步骤(2)中设置浸麦调温水箱,调节浸麦水温在13~18℃。As a preferred technical solution, the step (2) is provided with a wheat soaking temperature regulating water tank, and the temperature of the wheat soaking water is adjusted at 13-18 ° C.
作为优选的技术方案,所述步骤(2)中6-植酸酶和木聚糖酶的混合物中6-植酸酶和木聚糖酶质量份数比为1:1,所述6-植酸酶和木聚糖酶的混合物先制成质量浓度为10%的水溶液,再以喷雾方式均匀加入。As a preferred technical solution, the mass ratio of 6-phytase and xylanase in the mixture of 6-phytase and xylanase in the step (2) is 1: 1, and the 6-plant The mixture of acidase and xylanase is first made into an aqueous solution with a mass concentration of 10%, and then added uniformly by spraying.
作为优选的技术方案,所述步骤(3)中所述亚硒酸钠先制成质量浓度为1%的水溶液,然后平均分配到两次发芽喷淋前以喷雾方式均匀加入。As a preferred technical solution, the sodium selenite in the step (3) is first made into an aqueous solution with a mass concentration of 1%, and then evenly distributed to the two germination sprays and added evenly by spraying.
作为优选的技术方案,所述步骤(3)中翻麦时应根据麦芽生长情况加水喷淋,添加大麦总重量的0.5~1%的赤霉酸。As a preferred technical solution, when turning wheat in the step (3), water should be sprayed according to the growth of malt, and gibberellic acid should be added at 0.5-1% of the total weight of the barley.
作为优选的技术方案,所述步骤(3)中发芽表冷器供冷由氨泵直接供冷,床下设有增湿装置和热水管喷淋装置。As a preferred technical solution, the cooling of the germination surface cooler in the step (3) is directly cooled by an ammonia pump, and a humidifying device and a hot water pipe spraying device are provided under the bed.
作为优选的技术方案,所述步骤(4)干燥采用蒸汽间接加热,所述干燥温度45-85℃。As a preferred technical solution, the step (4) drying uses steam indirect heating, and the drying temperature is 45-85 ° C.
本发明的有益效果为:该工艺采用改进的塔式发芽工艺,同时在浸麦过程加入了6-植酸酶和木聚糖酶的混合酶,促进夹质的溶解与分离,在发芽前期加入亚硒酸钠溶液,从而使麦汁浊度在1.5EBC以下,破损率在0.5%以下,麦芽硒含量达到28μg/㎏以上,工艺过程简单,适宜批量化生产,麦芽长短均匀,成分一致性高,营养价值高,尤其适用于生产啤酒的原料。The beneficial effects of the present invention are: the process adopts an improved tower germination process, and at the same time, a mixed enzyme of 6-phytase and xylanase is added to the wheat steeping process to promote the dissolution and separation of intercalation, and is added in the early stage of germination Sodium selenite solution, so that the wort turbidity is below 1.5EBC, the breakage rate is below 0.5%, the malt selenium content is above 28μg / ㎏, the process is simple, suitable for batch production, the malt length is uniform, and the composition consistency is high , High nutritional value, especially suitable for the production of beer raw materials.
附图说明BRIEF DESCRIPTION
图1为本发明的工艺流程图。Figure 1 is a process flow diagram of the present invention.
具体实施方式detailed description
下面结合附图通过具体的实施例对本发明进行详细的描述。The present invention will be described in detail below through specific embodiments with reference to the drawings.
如图1所示,本发明的工艺流程可以分为原料处理、制麦塔制麦、干燥箱干燥、除根机除根、包装、贮存五个工序,下面所列举的实施例只对原料处理、制麦塔制麦、干燥箱干燥、除根机除根工序作详细描述。As shown in FIG. 1, the process flow of the present invention can be divided into five processes: raw material processing, wheat making, dry oven drying, rooting machine rooting, packaging, and storage. The following examples only deal with raw material processing The processes of wheat making, drying in a drying oven, and root removing machine are described in detail.
实施例1Example 1
(1)原料处理:(1) Raw material processing:
将原料大麦用斗式提升机(型号为TD500)送至风选振动筛(TQLZ180x200),经过除石机(QSX-168比重除石机),分级机(平板分级筛0510),电子称,进入精选大麦仓,大麦精选采用精选机(杂谷分离机),并配置1套脉冲式布袋除尘器(型号ZC-90),精选过的大麦夹杂物含量在0.2%以内,大麦的分级度达到95%以上,原料处理能力为100t/h,大麦精选配,入仓能力为每小时300吨;Send the raw material barley with bucket elevator (model TD500) to the air separation vibrating screen (TQLZ180x200), pass the stone remover (QSX-168 specific gravity stone remover), classifier (flat plate classifier 0510), electronic scale, enter Selected barley silo, barley selection using a selection machine (grain separator), and equipped with a set of pulse bag filter (model ZC-90), the content of selected barley inclusions within 0.2%, barley The grading degree is above 95%, the raw material processing capacity is 100t / h, the barley is carefully selected, and the storage capacity is 300 tons per hour;
(2)浸麦:(2) Dipping wheat:
①采用塔式发芽工艺,锥底浸麦槽(180m 3)、发芽箱置于发芽塔内,浸麦槽与发芽箱呈上、下布置,浸麦槽与发芽箱之间设有塔内输送管道,依靠重力将 大麦进行运转,浸麦选用180m 3的浸麦槽6个水平、平行布置,浸麦槽采用不锈钢,浸麦槽锥底部加装清洗假底的开口,以便清洗卫生,1个浸麦槽1台通风机(采用水循环空压机,以降低出风的温度),每个浸麦槽各配1台CO 2吸风机,排浮麦采用水吸式溢流,去除浮麦,设置有浸麦调温水箱,以保证浸麦水温在冬、夏季可以调节至工艺要求的温度范围在13~18℃; ①Using the tower germination process, the cone bottom dipping tank (180m 3 ) and the germination box are placed in the germination tower. The dipping tank and the germination box are arranged above and below, and there is a tower transportation between the dipping tank and the germination box The pipeline relies on gravity to run the barley. The wheat immersion tank uses 180m 3 of the wheat immersion tank. 6 horizontal and parallel layouts. The wheat immersion tank is made of stainless steel. The bottom of the wheat immersion tank cone is equipped with an opening for cleaning the false bottom for cleaning and sanitation. 1 1 ventilator for wheat immersion tank (using water circulation air compressor to reduce the temperature of the air), each immersion tank is equipped with a CO 2 suction fan, and the floating wheat is removed by water suction to remove the floating wheat. It is equipped with a wheat soaking temperature regulating water tank to ensure that the wheat soaking water temperature can be adjusted in winter and summer to the temperature range required by the process in 13 ~ 18 ℃;
②将步骤(1)处理过的大麦采用水浸、鼓风、抽CO 2的综合浸麦法,整个浸麦过程按浸三断四的工艺进行,即浸渍3小时,断水4小时,浸麦过程采取定时鼓风、喷淋、排浮麦、抽吸CO 2四个工序进行控制,浸麦喷淋过程中,先用喷雾器向大麦中加入占大麦总重量3%的6-植酸酶和木聚糖酶的混合物,6-植酸酶和木聚糖酶的混合物中6-植酸酶和木聚糖酶质量份数比为1:1,6-植酸酶和木聚糖酶的混合物先配制成质量浓度为10%的水溶液,浸麦20小时,获得的大麦浸麦度为42%,露点率为72%; ②The barley processed in step (1) is subjected to the integrated wheat immersion method of water immersion, blasting and CO 2 extraction. The whole wheat immersion process is carried out according to the process of immersing three times and breaking four times. The process is controlled by four processes: timed air blowing, spraying, floating wheat, and CO 2 suction. During the spraying process of wheat soaking, first add 6% phytase and 3% of the total weight of barley to the barley with a sprayer. The mixture of xylanase, the mixture of 6-phytase and xylanase in the mixture of 6-phytase and xylanase has a mass ratio of 1: 1, 6-phytase and xylanase The mixture is first prepared into an aqueous solution with a mass concentration of 10%, and the wheat is soaked for 20 hours, the barley soaking degree obtained is 42%, and the dew point rate is 72%;
(3)发芽:(3) Germination:
①发芽采用4个发芽箱,选用直径29米的发芽箱,每个发芽箱各自独立,发芽间采用独立的空气调节系统,即各自通风、供冷和回风,发芽风机配置变频器,筛板采用不锈钢材质,结构形式为平筛面加底架,发芽表冷器供冷由氨泵直接供冷,床下有增湿装置和热水管喷淋装置,在冬天气温低时增加空气温度和湿度,发芽过程中控制温度在12-16℃,湿度在92-96%;①The germination adopts 4 germination boxes, and the germination box with a diameter of 29 meters is selected. Each germination box is independent. The germination room adopts independent air conditioning system, that is, each has its own ventilation, cooling and return air. The germination fan is equipped with a frequency converter and a sieve plate It is made of stainless steel, the structure is flat screen surface and bottom frame, and the germination surface cooler is cooled by ammonia pump directly. There is a humidifier and hot water pipe spray device under the bed to increase the air temperature and humidity when the temperature is low in winter , During the germination process, the temperature is controlled at 12-16 ℃, the humidity is 92-96%;
②将步骤(2)得到的浸渍大麦通过管道逐层输送到4个发芽箱,再用组合机(ZP-90)铺平,每隔8小时用翻麦机(ZFM7.0*2.0)翻麦一次,保证上、下层温差达3-4℃,开始发芽的第10和第40小时分别用水喷淋一次,将配制成质量浓度为1%的亚硒酸钠水溶液先平均分成两份,分别在发芽喷淋前用喷雾器喷洒,亚硒酸钠的总用量为大麦总重量0.005%,然后用水喷淋,喷淋水中添加大麦总重量的0.5%的赤霉酸,发芽时间控制在70小时;②The impregnated barley obtained in step (2) is transported layer by layer to 4 germination boxes, then paved with a combination machine (ZP-90), and turned over with a wheat turning machine (ZFM7.0 * 2.0) every 8 hours Once, to ensure that the temperature difference between the upper and lower layers reaches 3-4 ℃, spray them with water once at the 10th and 40th hours of germination, and divide the aqueous solution of sodium selenite formulated into a mass concentration of 1% into two parts first. Spray with a sprayer before germination and spray, the total amount of sodium selenite is 0.005% of the total weight of barley, then spray with water, add 0.5% gibberellic acid to the total weight of the barley in the spray water, and control the germination time at 70 hours;
(4)干燥:(4) Drying:
将步骤(3)获得的发芽完毕的绿麦芽通过双梨点式多点卸料皮带输送机、斗式提升机移出发芽塔、送入干燥箱(GFG-20),绿麦芽经过凋萎、干燥、焙焦阶段,最终干燥到含水份≤5%,整个干燥过程可根据干燥室温度和风量调节蒸汽流量,还可根据室外温度和不同阶段的工艺要求调节回风量,以节约能源,排潮期风量4000—4500立方米/吨绿麦芽,干燥时间控制在20小时(含辅助时间),由1个Φ42m圆型干燥炉(GFG-20)来完成,干燥采用蒸汽间接加热方式,凋萎层干燥温度控制45-68℃,时间16-18小时,焙焦层温度控制在65-85℃,时间2-4小时,在干燥炉带有余热回收装置,余热回收管采用铝合金管,干燥炉配4台鼓风机(L52WD),配置变频器,根据温度进行自动控制电源的开启与关闭;The germinated green malt obtained in step (3) is moved to the germination tower through a double pear point multi-point unloading belt conveyor and a bucket elevator, and sent to a drying box (GFG-20). The green malt is withered and dried 3. In the coking stage, the final drying is to a moisture content of 5% or less. The entire drying process can adjust the steam flow according to the temperature and air volume of the drying chamber, and can also adjust the return air volume according to the outdoor temperature and process requirements in different stages to save energy and eliminate moisture. The period air volume is 4000-4500 cubic meters per ton of green malt. The drying time is controlled at 20 hours (including auxiliary time). It is completed by a Φ42m round drying furnace (GFG-20). Drying adopts indirect steam heating method, withered layer Drying temperature control 45-68 ℃, time 16-18 hours, baking coke layer temperature control 65-85 ℃, time 2-4 hours, equipped with waste heat recovery device in the drying furnace, waste heat recovery tube adopts aluminum alloy tube, drying furnace Equipped with 4 blowers (L52WD), equipped with frequency converter, to automatically control the power on and off according to the temperature;
(5)除根:(5) Eradication:
将步骤(4)干燥完成后的麦芽通新鲜空气将麦层冷至40-45℃,然后经斗式提升机送至1个干麦芽暂贮仓,然后经过2台除根机(型号CG-15)除根,处理能力为40t/h,除根后计量,斗式提升机进入麦芽立仓,麦芽出仓经过兑料系统送至风选振动筛,经过电子计量称自动打包,除根系统配1套脉冲式布袋除尘器。After the step (4) drying the malt, fresh air is used to cool the wheat layer to 40-45 ° C, and then it is sent to a dry malt temporary storage silo through a bucket elevator, and then passes through two de-rooting machines (model CG-15 ) Root removal, processing capacity is 40t / h, measurement after root removal, bucket elevator enters the malt silo, the malt out of the warehouse is sent to the air separation vibrating screen through the batching system, and is automatically packaged through the electronic weighing scale. The root removal system is equipped with 1 set of pulses Bag dust collector.
所获得的麦芽经检测,麦汁浊度为1.4EBC,破损率在0.5%以下,硒含量28μg/㎏。The malt obtained was tested, the wort turbidity was 1.4EBC, the breakage rate was below 0.5%, and the selenium content was 28 μg / ㎏.
实施例2Example 2
(1)原料处理:(1) Raw material processing:
将原料大麦用斗式提升机(型号为TD500)送至风选振动筛(TQLZ180x200),经过除石机(QSX-168比重除石机),分级机(平板分级筛0510),电子称,进入精选大麦仓,大麦精选采用精选机(杂谷分离机),并配置1套脉冲式布袋除尘器(型号ZC-90),精选过的大麦夹杂物含量在0.2%以内,大麦的分级度达到95%以上,原料处理能力为100t/h,大麦精选配,入仓能力为每小时300吨;Send the raw material barley with bucket elevator (model TD500) to the air separation vibrating screen (TQLZ180x200), pass the stone remover (QSX-168 specific gravity stone remover), classifier (flat plate classifier 0510), electronic scale, enter Selected barley silo, barley selection using a selection machine (grain separator), and equipped with a set of pulse bag filter (model ZC-90), the content of selected barley inclusions within 0.2%, barley The grading degree is above 95%, the raw material processing capacity is 100t / h, the barley is carefully selected, and the storage capacity is 300 tons per hour;
(2)浸麦:(2) Dipping wheat:
①采用塔式发芽工艺,锥底浸麦槽(180m 3)、发芽箱置于发芽塔内,浸麦槽与发芽箱呈上、下布置,浸麦槽与发芽箱之间设有塔内输送管道,依靠重力将大麦进行运转,浸麦选用180m 3的浸麦槽6个水平、平行布置,浸麦槽采用不锈钢,浸麦槽锥底部加装清洗假底的开口,以便清洗卫生,1个浸麦槽1台通风机(采用水循环空压机,以降低出风的温度),每个浸麦槽各配1台CO 2吸风机,排浮麦采用水吸式溢流,去除浮麦,设置浸麦调温水箱,以保证浸麦水温在冬、夏季可以调节至工艺要求的温度范围在13~18℃; ①Using the tower germination process, the cone bottom dipping tank (180m 3 ) and the germination box are placed in the germination tower. The dipping tank and the germination box are arranged above and below, and there is a tower transportation between the dipping tank and the germination box The pipeline relies on gravity to run the barley. The wheat immersion tank uses 180m 3 of the wheat immersion tank. 6 horizontal and parallel layouts. The wheat immersion tank is made of stainless steel. The bottom of the wheat immersion tank cone is equipped with an opening for cleaning the false bottom for cleaning and sanitation. 1 1 ventilator for wheat immersion tank (using water circulation air compressor to reduce the temperature of the air), each immersion tank is equipped with a CO 2 suction fan, and the floating wheat is removed by water suction to remove the floating wheat. Set the temperature control tank for soaking wheat to ensure that the temperature of soaking wheat can be adjusted to the temperature range of 13 ~ 18 ℃ in winter and summer;
②将步骤(1)处理过的大麦采用水浸、鼓风、抽CO 2的综合浸麦法,整个浸麦过程按浸三断四的工艺进行,即浸渍3小时,断水4小时,浸麦过程采取定时鼓风、喷淋、排浮麦、抽吸CO 2四个工序进行控制,浸麦喷淋过程中,先用喷雾器向大麦中加入占大麦总重量4%的6-植酸酶和木聚糖酶的混合物,6-植酸酶和木聚糖酶的混合物中6-植酸酶和木聚糖酶质量份数比为1:1,6-植酸酶和木聚糖酶的混合物先配制成质量浓度为10%的水溶液,浸麦21小时,获得的大麦浸麦度为48%,露点率为82%; ②The barley processed in step (1) is subjected to the integrated wheat immersion method of water immersion, blasting and CO 2 extraction. The whole wheat immersion process is carried out according to the process of immersing three times and breaking four times. The process is controlled by four processes: timed air blowing, spraying, floating wheat, and CO 2 suction. During the spraying process, the 6-phytase and 4% of the total weight of barley are added to the barley with a sprayer. The mixture of xylanase, the mixture of 6-phytase and xylanase in the mixture of 6-phytase and xylanase has a mass ratio of 1: 1, 6-phytase and xylanase The mixture is first formulated into an aqueous solution with a mass concentration of 10%, soaked in wheat for 21 hours, the barley soaking degree obtained is 48%, and the dew point rate is 82%;
(3)发芽:(3) Germination:
①发芽采用4个发芽箱,选用直径29米的发芽箱,每个发芽箱各自独立,发芽间采用独立的空气调节系统,即各自通风、供冷和回风,发芽风机配置变频器以达到有效控制工艺参数的同时节约电能,筛板采用不锈钢材质,结构形式为平筛面加底架,发芽表冷器供冷由氨泵直接供冷,床下有增湿装置和热水管喷淋装置,在冬天气温低时增加空气温度和湿度,发芽过程中控制温度在12-16℃,湿度在92-96%;①The germination adopts 4 germination boxes, and the germination box with a diameter of 29 meters is selected, each germination box is independent, and an independent air conditioning system is used in the germination room, that is, each has its own ventilation, cooling and return air, and the germination fan is equipped with a frequency converter to achieve effective Control process parameters while saving electrical energy. The sieve plate is made of stainless steel. The structure is a flat screen surface with a bottom frame. The germination surface cooler is cooled directly by an ammonia pump. There is a humidification device and a hot water pipe spray device under the bed. Increase the air temperature and humidity when the temperature is low in winter, and control the temperature at 12-16 ° C and the humidity at 92-96% during the germination process;
②将步骤(2)得到的浸渍大麦通过管道逐层输送到4个发芽箱,再用组合机(ZP-90)铺平,每隔8小时用翻麦机(ZFM7.0*2.0)翻麦一次,保证上、下层温差达3-4℃,开始发芽的第10和第40小时分别用水喷淋一次,将配制成质量浓度为1%的亚硒酸钠水溶液先平均分成两份,分别在发芽喷淋前用喷雾器喷 洒,亚硒酸钠的总用量为大麦总重量0.010%,然后用水喷淋,喷淋水中添加占大麦总重量的0.75%的赤霉酸,发芽时间控制在85小时;②The impregnated barley obtained in step (2) is transported layer by layer to 4 germination boxes, then paved with a combination machine (ZP-90), and turned over with a wheat turning machine (ZFM7.0 * 2.0) every 8 hours Once, to ensure that the temperature difference between the upper and lower layers reaches 3-4 ℃, spray them with water once at the 10th and 40th hours of germination, and divide the aqueous solution of sodium selenite formulated into a mass concentration of 1% into two parts first. Before spraying, spray with a sprayer, the total amount of sodium selenite is 0.010% of the total weight of barley, then spray with water, add gibberellic acid 0.75% of the total weight of the barley in the spraying water, and control the germination time at 85 hours;
(4)干燥:(4) Drying:
将步骤(3)获得的发芽完毕的绿麦芽通过双梨点式多点卸料皮带输送机、斗式提升机移出发芽塔、送入干燥箱(GFG-20),绿麦芽经过凋萎、干燥、焙焦阶段,最终干燥到含水份≤5%,整个干燥过程可根据干燥室温度和风量调节蒸汽流量,还可根据室外温度和不同阶段的工艺要求调节回风量,以节约能源,排潮期风量4000—4500立方米/吨绿麦芽,干燥时间控制在22小时(含辅助时间),由1个Φ42m圆型干燥炉(GFG-20)来完成,干燥采用蒸汽间接加热方式,凋萎层干燥温度控制45-68℃,时间16-18小时,焙焦层温度控制在65-85℃,时间2-4小时,在干燥炉带有余热回收装置,余热回收管采用铝合金管,干燥炉配4台鼓风机(L52WD),配置变频器,根据温度进行自动控制电源的开启与关闭;The germinated green malt obtained in step (3) is moved to the germination tower through a double pear point multi-point unloading belt conveyor and a bucket elevator, and sent to a drying box (GFG-20). The green malt is withered and dried 3. In the coking stage, the final drying is to a moisture content of 5% or less. The entire drying process can adjust the steam flow according to the temperature and air volume of the drying chamber, and can also adjust the return air volume according to the outdoor temperature and process requirements in different stages to save energy and eliminate moisture. The period air volume is 4000-4500 cubic meters per ton of green malt. The drying time is controlled at 22 hours (including auxiliary time). It is completed by a Φ42m circular drying furnace (GFG-20). The drying uses steam indirect heating and the withered layer Drying temperature control 45-68 ℃, time 16-18 hours, baking coke layer temperature control 65-85 ℃, time 2-4 hours, equipped with waste heat recovery device in the drying furnace, waste heat recovery tube adopts aluminum alloy tube, drying furnace Equipped with 4 blowers (L52WD), equipped with frequency converter, to automatically control the power on and off according to the temperature;
(5)除根:(5) Eradication:
将步骤(4)干燥完成后的麦芽通新鲜空气将麦层冷至40-45℃,然后经斗式提升机送至1个干麦芽暂贮仓,然后经过2台除根机(型号CG-15)除根,处理能力为40t/h,除根后计量,斗式提升机进入麦芽立仓,麦芽出仓经过兑料系统送至风选振动筛,经过电子计量称自动打包,除根系统配1套脉冲式布袋除尘器。After the step (4) drying the malt, fresh air is used to cool the wheat layer to 40-45 ° C, and then it is sent to a dry malt temporary storage silo through a bucket elevator, and then passes through two de-rooting machines (model CG-15 ) Root removal, processing capacity is 40t / h, measurement after root removal, bucket elevator enters the malt silo, the malt out of the warehouse is sent to the air separation vibrating screen through the batching system, and is automatically packaged through the electronic weighing scale. The root removal system is equipped with 1 set of pulses Bag dust collector.
所获得的麦芽经检测,麦汁浊度为1.2EBC,破损率在0.5%以下,硒含量30μg/㎏。The malt obtained was tested, the wort turbidity was 1.2EBC, the breakage rate was below 0.5%, and the selenium content was 30 μg / ㎏.
实施例3Example 3
(1)原料处理:(1) Raw material processing:
将原料大麦用斗式提升机(型号为TD500)送至风选振动筛(TQLZ180x200),经过除石机(QSX-168比重除石机),分级机(平板分级筛0510),电子称,进入精选大麦仓,大麦精选采用精选机(杂谷分离机),并配置1套脉冲式布袋除 尘器(型号ZC-90),精选过的大麦夹杂物含量在0.2%以内,大麦的分级度达到95%以上,原料处理能力为100t/h,大麦精选配,入仓能力为每小时300吨;Send the raw material barley with bucket elevator (model TD500) to the air separation vibrating screen (TQLZ180x200), pass the stone remover (QSX-168 specific gravity stone remover), classifier (flat plate classifier 0510), electronic scale, enter Selected barley silo, barley selection using a selection machine (grain separator), and equipped with a set of pulse bag filter (model ZC-90), the content of selected barley inclusions within 0.2%, barley The grading degree is above 95%, the raw material processing capacity is 100t / h, the barley is carefully selected, and the storage capacity is 300 tons per hour;
(2)浸麦:(2) Dipping wheat:
①采用塔式发芽工艺,锥底浸麦槽(180m 3)、发芽箱置于发芽塔内,浸麦槽与发芽箱呈上、下布置,浸麦槽与发芽箱之间设有塔内输送管道,依靠重力将大麦进行运转,浸麦选用180m 3的浸麦槽6个水平、平行布置,浸麦槽采用不锈钢,浸麦槽锥底部加装清洗假底的开口,以便清洗卫生,1个浸麦槽1台通风机(采用水循环空压机,以降低出风的温度),每个浸麦槽各配1台CO 2吸风机,排浮麦采用水吸式溢流,去除浮麦,设置浸麦调温水箱,以保证浸麦水温在冬、夏季可以调节至工艺要求的温度范围在13~18℃; ①Using the tower germination process, the cone bottom dipping tank (180m 3 ) and the germination box are placed in the germination tower. The dipping tank and the germination box are arranged above and below, and there is a tower transportation between the dipping tank and the germination box The pipeline relies on gravity to run the barley. The wheat immersion tank uses 180m 3 of the wheat immersion tank. 6 horizontal and parallel layouts. The wheat immersion tank is made of stainless steel. The bottom of the wheat immersion tank cone is equipped with an opening for cleaning the false bottom for cleaning and sanitation. 1 1 ventilator for wheat immersion tank (using water circulation air compressor to reduce the temperature of the air), each immersion tank is equipped with a CO 2 suction fan, and the floating wheat is removed by water suction to remove the floating wheat. Set the temperature control tank for soaking wheat to ensure that the temperature of soaking wheat can be adjusted to the temperature range of 13 ~ 18 ℃ in winter and summer;
②将步骤(1)处理过的大麦采用水浸、鼓风、抽CO 2的综合浸麦法,整个浸麦过程按浸三断四的工艺进行,即浸渍3小时,断水4小时,浸麦过程采取定时鼓风、喷淋、排浮麦、抽吸CO 2四个工序进行控制,浸麦喷淋过程中,先用喷雾器向大麦中加入占大麦总重量5%的6-植酸酶和木聚糖酶的混合物,6-植酸酶和木聚糖酶的混合物中6-植酸酶和木聚糖酶质量份数比为1:1,6-植酸酶和木聚糖酶的混合物先配制成质量浓度为10%的水溶液,浸麦22小时,获得的大麦浸麦度为46%,露点率为78%; ②The barley processed in step (1) is subjected to the integrated wheat immersion method of water immersion, blasting and CO 2 extraction. The whole wheat immersion process is carried out according to the process of immersing three times and breaking four times. The process is controlled by four processes: regular air blowing, spraying, floating wheat, and CO 2 suction. During the spraying process of wheat soaking, first add 6-phytase and phytase, which account for 5% of the total weight of the barley, to the barley with a sprayer The mixture of xylanase, the mixture of 6-phytase and xylanase in the mixture of 6-phytase and xylanase has a mass ratio of 1: 1, 6-phytase and xylanase The mixture was first formulated into an aqueous solution with a mass concentration of 10%, soaked in wheat for 22 hours, the barley soaking degree obtained was 46%, and the dew point rate was 78%;
(3)发芽:(3) Germination:
①发芽采用4个发芽箱,选用直径29米的发芽箱,每个发芽箱各自独立,发芽间采用独立的空气调节系统,即各自通风、供冷和回风,发芽风机配置变频器以达到有效控制工艺参数的同时节约电能,筛板采用不锈钢材质,结构形式为平筛面加底架,发芽表冷器供冷由氨泵直接供冷,床下有增湿装置和热水管喷淋装置,在冬天气温低时增加空气温度和湿度,发芽过程中控制温度在12-16℃,湿度在92-96%;①The germination adopts 4 germination boxes, and the germination box with a diameter of 29 meters is selected, each germination box is independent, and an independent air conditioning system is used in the germination room, that is, each has its own ventilation, cooling and return air, and the germination fan is equipped with a frequency converter to achieve effective Control process parameters while saving electrical energy. The sieve plate is made of stainless steel. The structure is a flat screen surface with a bottom frame. The germination surface cooler is cooled directly by an ammonia pump. There is a humidification device and a hot water pipe spray device under the bed. Increase the air temperature and humidity when the temperature is low in winter, and control the temperature at 12-16 ° C and the humidity at 92-96% during the germination process;
②将步骤(2)得到的浸渍大麦通过管道逐层输送到4个发芽箱,再用组合机(ZP-90)铺平,每隔8小时用翻麦机(ZFM7.0*2.0)翻麦一次,保证上、下 层温差达3-4℃,开始发芽的第10和第40小时分别用水喷淋一次,将配制成质量浓度为1%的亚硒酸钠水溶液先平均分成两份,分别在发芽喷淋前用喷雾器喷洒,亚硒酸钠的总用量为大麦总重量0.015%,然后用水喷淋,喷淋水中添加占大麦总重量的1%的赤霉酸,发芽时间控制在100小时;②The impregnated barley obtained in step (2) is transported layer by layer to 4 germination boxes, then paved with a combination machine (ZP-90), and turned over with a wheat turning machine (ZFM7.0 * 2.0) every 8 hours Once, to ensure that the temperature difference between the upper and lower layers reaches 3-4 ℃, spray them with water once at the 10th and 40th hours of germination, and divide the aqueous solution of sodium selenite formulated into a mass concentration of 1% into two parts first. Before spraying, spray with a sprayer. The total amount of sodium selenite is 0.015% of the total weight of barley. Then spray with water. Add 1% of gibberellic acid to the total weight of barley in the spraying water, and control the germination time at 100 hours;
(4)干燥:(4) Drying:
将步骤(3)获得的发芽完毕的绿麦芽通过双梨点式多点卸料皮带输送机、斗式提升机移出发芽塔、送入干燥箱(GFG-20),绿麦芽经过凋萎、干燥、焙焦阶段,最终干燥到含水份≤5%,整个干燥过程可根据干燥室温度和风量调节蒸汽流量,还可根据室外温度和不同阶段的工艺要求调节回风量,以节约能源,排潮期风量4000—4500立方米/吨绿麦芽,干燥时间控制在23小时(含辅助时间),由1个Φ42m圆型干燥炉(GFG-20)来完成,干燥采用蒸汽间接加热方式,凋萎层干燥温度控制45-68℃,时间16-18小时,焙焦层温度控制在65-85℃,时间2-4小时,在干燥炉带有余热回收装置,余热回收管采用铝合金管,干燥炉配4台鼓风机(L52WD),配置变频器,根据温度进行自动控制电源的开启与关闭;The germinated green malt obtained in step (3) is moved to the germination tower through a double pear point multi-point unloading belt conveyor and a bucket elevator, and sent to a drying box (GFG-20). The green malt is withered and dried 3. In the coking stage, the final drying is to a moisture content of 5% or less. The entire drying process can adjust the steam flow according to the temperature and air volume of the drying chamber, and can also adjust the return air volume according to the outdoor temperature and process requirements in different stages to save energy and eliminate moisture. The period of air volume is 4000-4500 cubic meters / ton of green malt. The drying time is controlled at 23 hours (including auxiliary time). It is completed by a Φ42m circular drying furnace (GFG-20). Drying adopts steam indirect heating method, withered layer Drying temperature control 45-68 ℃, time 16-18 hours, baking coke layer temperature control 65-85 ℃, time 2-4 hours, equipped with waste heat recovery device in the drying furnace, waste heat recovery tube adopts aluminum alloy tube, drying furnace Equipped with 4 blowers (L52WD), equipped with frequency converter, to automatically control the power on and off according to the temperature;
(5)除根:(5) Eradication:
将步骤(4)干燥完成后的麦芽通新鲜空气将麦层冷至40-45℃,然后经斗式提升机送至1个干麦芽暂贮仓,然后经过2台除根机(型号CG-15)除根,处理能力为40t/h,除根后计量,斗式提升机进入麦芽立仓,麦芽出仓经过兑料系统送至风选振动筛,经过电子计量称自动打包,除根系统配1套脉冲式布袋除尘器。After the step (4) drying the malt, fresh air is used to cool the wheat layer to 40-45 ° C, and then it is sent to a dry malt temporary storage silo through a bucket elevator, and then passes through two de-rooting machines (model CG-15 ) Root removal, processing capacity is 40t / h, measurement after root removal, bucket elevator enters the malt silo, the malt out of the warehouse is sent to the air separation vibrating screen through the batching system, and is automatically packaged through the electronic weighing scale. Bag dust collector.
所获得的麦芽经检测,麦汁浊度为1.3EBC,破损率在0.5%以下,硒含量31μg/㎏。The malt obtained was tested, the wort turbidity was 1.3EBC, the breakage rate was below 0.5%, and the selenium content was 31 μg / ㎏.
以上所述仅为本发明的较佳实施例,并不用以限制本发明,凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。The above are only preferred embodiments of the present invention and are not intended to limit the present invention. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention should be included in the protection of the present invention Within range.

Claims (8)

  1. 一种大麦麦芽的加工工艺,包括以下步骤:A processing technology of barley malt includes the following steps:
    (1)原料处理:将原料大麦用斗式提升机送至风选振动筛,经过除石机、分级机、电子称,进入精选大麦仓,大麦精选采用精选机,并配置脉冲式布袋除尘器进行,处理过的大麦夹杂物的含量在0.2%以内,大麦的分级度达到95%以上;(1) Raw material processing: The raw material barley is sent to the air separation vibrating screen with a bucket elevator, passes through the stone remover, classifier, electronic scale, and enters the selected barley silo. The barley selection uses the selected machine and is equipped with a pulse type The bag dust collector is used, the content of the processed barley inclusions is within 0.2%, and the classification degree of the barley reaches more than 95%;
    (2)浸麦:采用塔式发芽工艺,采用六个水平、平行布置的锥底浸麦槽置于塔的最上层,每个浸麦槽分别配备通风机和二氧化碳吸风机,将步骤(1)处理过的原料大麦按照鼓风、喷淋、排浮麦、抽吸二氧化碳的步骤进行,侵麦喷淋前先向大麦中加入占大麦总重量的3~5%的6-植酸酶和木聚糖酶的混合物,浸麦度为42~48%、露点率达71~82%;(2) Wheat immersion: adopt the tower type germination process, adopt six horizontal and parallel arrangement cone-shaped wheat immersion tanks placed on the uppermost layer of the tower, each wheat immersion tank is equipped with a fan and a carbon dioxide suction fan respectively. ) The processed raw barley is carried out in accordance with the steps of blasting, spraying, floating wheat, and pumping carbon dioxide. Before invading and spraying, add 3-5% phytase and 3-phytase to the barley to the total weight of the barley. The mixture of xylanase has a immersion degree of 42-48% and a dew point rate of 71-82%;
    (3)发芽:采用4个发芽箱置于浸麦槽的下层,将步骤(2)浸渍后的大麦通过管道逐层输送到发芽箱,再用组合机铺平,每隔8小时翻麦一次,在开始发芽的第10小时和第40小时分别喷淋两次,发芽喷淋前应先向大麦中添加占大麦总重量的0.005-0.015%的亚硒酸钠,发芽时间控制在70~100小时;(3) Germination: 4 germination boxes are placed in the lower layer of the wheat immersion tank, the barley after impregnation in step (2) is transported layer by layer to the germination box, then flattened with a combination machine, and the wheat is turned every 8 hours , Spray twice at the 10th and 40th hours of germination. Before germination and spraying, add 0.005-0.015% sodium selenite to the barley, the germination time should be controlled at 70 ~ 100 hour;
    (4)干燥:将步骤(3)发芽完毕的绿麦芽通过卸料机、皮带机、斗式提升机移出发芽塔,送入干燥箱,绿麦芽经过凋萎、干燥、焙焦阶段,最终干燥到含水份≤5%,干燥时间控制在20~23小时;(4) Drying: The green malt germinated in step (3) is moved to the germination tower through the unloader, belt conveyor, bucket elevator, and sent to the drying box. The green malt goes through the withering, drying and coking stage, and finally dried When the moisture content is ≤5%, the drying time is controlled at 20-23 hours;
    (5)除根:将步骤(4)干燥完成后的麦芽经斗式提升机送至干麦芽暂贮仓,然后经过除根机除根,再用斗式提升机进入麦芽立仓,麦芽出仓经过兑料系统送至风选振动筛,计量后打包。(5) Root removal: The malt after the drying in step (4) is sent to the dry malt temporary storage silo through the bucket elevator, and then the root is removed by the root removal machine, and then entered into the malt silo with the bucket elevator, and the malt is removed from the warehouse The material system is sent to the air separation vibrating screen and packed after measurement.
  2. 根据权利要求1所述的一种大麦麦芽的加工工艺,其特征在于:所述步骤(2)中排浮麦采用水吸式溢流,去除浮麦。The processing technology of barley malt according to claim 1, characterized in that: in the step (2), the row of floating wheat adopts water suction overflow to remove the floating wheat.
  3. 根据权利要求1所述的一种大麦麦芽的加工工艺,其特征在于:所述步骤(2)中设置浸麦调温水箱,调节浸麦水温在13~18℃。The processing technology for barley malt according to claim 1, wherein the step (2) is provided with a wheat-soaking temperature-regulating water tank to adjust the temperature of the wheat-soaking water at 13-18 ° C.
  4. 根据权利要求1所述的一种大麦麦芽的加工工艺,其特征在于:所述步骤(2)中6-植酸酶和木聚糖酶的混合物中6-植酸酶和木聚糖酶质量份数比为1: 1,所述6-植酸酶和木聚糖酶的混合物先制成质量浓度为10%的水溶液,再以喷雾方式均匀加入。The processing technology of barley malt according to claim 1, characterized in that: the quality of 6-phytase and xylanase in the mixture of 6-phytase and xylanase in the step (2) The portion ratio is 1: 1. The mixture of 6-phytase and xylanase is first made into an aqueous solution with a mass concentration of 10%, and then added uniformly by spraying.
  5. 根据权利要求1所述的一种大麦麦芽的加工工艺,其特征在于:所述步骤(3)中所述亚硒酸钠先制成质量浓度为1%的水溶液,然后平均分配到两次发芽喷淋前以喷雾方式均匀加入。The processing technology of barley malt according to claim 1, characterized in that: in the step (3), the sodium selenite is first made into an aqueous solution with a mass concentration of 1%, and then evenly distributed to two germinations Before spraying, add evenly by spraying.
  6. 根据权利要求1所述的一种大麦麦芽的加工工艺,其特征在于:所述步骤(3)中翻麦时应根据麦芽生长情况加水喷淋,添加大麦总重量的0.5~1%的赤霉酸。The processing technology of barley malt according to claim 1, characterized in that: in the step (3), when turning the wheat, water spray should be added according to the growth status of the malt, and 0.5-1% of the total weight of barley is added acid.
  7. 根据权利要求1所述的一种大麦麦芽的加工工艺,其特征在于:所述步骤(3)中发芽表冷器供冷由氨泵直接供冷,床下设有增湿装置和热水管喷淋装置。The processing technology of barley malt according to claim 1, characterized in that: in step (3), the cooling of the germination surface cooler is directly supplied by an ammonia pump, and a humidifying device and a hot water pipe spray are provided under the bed淋 装置。 Shower device.
  8. 根据权利要求1所述的一种大麦麦芽的加工工艺,其特征在于:所述步骤(4)干燥采用蒸汽间接加热,所述干燥温度45-85℃。The processing technology of barley malt according to claim 1, characterized in that: the step (4) drying adopts steam indirect heating, and the drying temperature is 45-85 ° C.
PCT/CN2018/110786 2018-10-13 2018-10-18 Processing technology of barley malt WO2020073350A1 (en)

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