CN206521456U - Drum type continuous smoked grains equipment - Google Patents

Drum type continuous smoked grains equipment Download PDF

Info

Publication number
CN206521456U
CN206521456U CN201621409561.8U CN201621409561U CN206521456U CN 206521456 U CN206521456 U CN 206521456U CN 201621409561 U CN201621409561 U CN 201621409561U CN 206521456 U CN206521456 U CN 206521456U
Authority
CN
China
Prior art keywords
heating
horizontal drum
drum structure
header
drum
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.)
Active
Application number
CN201621409561.8U
Other languages
Chinese (zh)
Inventor
庞相国
范伟国
乔新建
牛家棒
朱广
桂树云
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shanxi Jinlongyu Liangfen Vinegar Industry Co ltd
Original Assignee
Prettech Machinery Making Co ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Prettech Machinery Making Co ltd filed Critical Prettech Machinery Making Co ltd
Priority to CN201621409561.8U priority Critical patent/CN206521456U/en
Application granted granted Critical
Publication of CN206521456U publication Critical patent/CN206521456U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Fertilizers (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Abstract

The utility model discloses in solid-state material heating field, especially, relate to unstrained spirits equipment is smoked in succession to rotary drum formula, the setting of stirring structure is in horizontal rotary drum structure, power structural connection horizontal rotary drum structure provides power, bearing structure sets up at horizontal rotary drum structure under bracing horizontal rotary drum structure, the respirator pipeline with external intercommunication is set up in the horizontal rotary drum structure, the zone of heating sets up outside horizontal rotary drum structure, the zone of heating adopts the collection case structure, heating intraformational heating water band intercommunication collection case and export collection case, it sets up and just to play water collection case slope to add the water band slope, add the water band and let in heating medium, the left end face center department of horizontal rotary drum structure sets up into discharge gate, right-hand member face center department sets up rotary. The utility model has the advantages that: the heating effect is greatly enhanced by simultaneously rotating in the heating process and matching with the stirring of blades in the barrel, the unstrained spirits are fully sealed in the smoking process, the waste of acetic acid is avoided, and the operation environment is greatly improved.

Description

转筒式连续熏醅设备Drum type continuous smoked grains equipment

技术领域technical field

本实用新型于固态物料加热领域,尤其涉及转筒式连续熏醅设备。The utility model relates to the field of solid material heating, in particular to a drum-type continuous smoked fermented grains equipment.

背景技术Background technique

固态物料的发酵酿造技术历史悠久,广泛用于酿酒,制曲,生物发酵,食品酿造等领域。目前,醋酸固态酿造行业,其熏醅方式:采取在方池内放入待加热醅料,再在底部夹层通入加热烟气(或蒸汽),进出料为人工或人工辅助,劳动强度大;熏醅时醅料静止不动,因醅料为热的不良导体,传热效果很差,且加热不均匀,热量浪费很大;熏醅过程中,敞口作业,醋酸挥发相当严重,作业环境恶劣,也造成了醋酸的浪费。The fermentation and brewing technology of solid materials has a long history and is widely used in wine making, koji making, biological fermentation, food brewing and other fields. At present, in the acetic acid solid-state brewing industry, the method of smoked grains is: put the grains to be heated in the square tank, and then pass in the heated flue gas (or steam) in the bottom interlayer. When fermenting unstrained spirits, the fermented grains are still, because the fermented grains are poor conductors of heat, the heat transfer effect is very poor, and the heating is uneven, and the heat is wasted a lot; during the process of smoking unstrained grains, the acetic acid volatilizes seriously, and the working environment is harsh , Also caused the waste of acetic acid.

实用新型内容Utility model content

为解决上述技术问题,本实用新型提供一种卧式转筒搅拌及进出装置。In order to solve the above-mentioned technical problems, the utility model provides a horizontal drum stirring and entering and exiting device.

本实用新型采用的技术方案是:一种卧式转筒搅拌及进出装置,包括卧式转筒结构、加热层、动力结构、支撑结构、搅拌结构,其特征在于所述搅拌结构设置在所述卧式转筒结构内,所述动力结构连接所述卧式转筒结构并提供动力,所述支撑结构设置在所述卧式转筒结构下支撑所述卧式转筒结构,所述卧式转筒结构内设置与外界连通的呼吸器管路,所述加热层设置在所述卧式转筒结构外,所述加热层采用集箱结构,所述加热层内设置进口集箱、加热水带和出口集箱,所述加热水带连通所述进口集箱和所述出口集箱,所述加热水带倾斜设置且向出水集箱倾斜,所述加热水带内通入加热介质。The technical solution adopted by the utility model is: a horizontal drum stirring and entering and exiting device, including a horizontal drum structure, a heating layer, a power structure, a supporting structure, and a stirring structure, which is characterized in that the stirring structure is arranged on the In the horizontal drum structure, the power structure is connected to the horizontal drum structure and provides power, the support structure is arranged under the horizontal drum structure to support the horizontal drum structure, and the horizontal drum structure The respirator pipeline communicating with the outside is arranged in the drum structure, the heating layer is arranged outside the horizontal drum structure, the heating layer adopts a header structure, and the inlet header, heating water The heating water belt is connected to the inlet header and the outlet header, the heating water belt is inclined to the water outlet header, and the heating medium is passed into the heating water belt.

进一步地,所述卧式转筒结构的两端设置左端面和右端面,所述左端面中心处设置进出料口,所述右端面中心处设置旋转接头;Further, both ends of the horizontal drum structure are provided with a left end face and a right end face, the center of the left end face is provided with a material inlet and outlet, and the center of the right end face is provided with a rotary joint;

进一步地,所述进口集箱通过进蒸汽支管与进蒸汽总管连通,所述出口集箱与冷凝水排出管连接,所述进蒸汽总管和所述冷凝水排出管均与旋转接头连接,所述冷凝水排出管出旋转接头后接疏水阀。Further, the inlet header is communicated with the steam inlet main pipe through the steam inlet branch pipe, the outlet header is connected with the condensed water discharge pipe, the steam inlet main pipe and the condensed water discharge pipe are connected with a rotary joint, the The condensate discharge pipe goes out of the swivel joint and is connected to the steam trap.

进一步地,所述加热水带倾斜度为0.5~1%。Further, the inclination of the heating water belt is 0.5-1%.

进一步地,所述支撑结构包括固定轴承座和调心滚轮座,所述固定轴承座固定在所述卧式转筒结构右端面上,所述调心滚轮座设置在所述卧式转筒结构左右两侧。Further, the support structure includes a fixed bearing seat and a self-aligning roller seat, the fixed bearing seat is fixed on the right end surface of the horizontal drum structure, and the self-aligning roller seat is arranged on the horizontal drum structure left and right sides.

进一步地,所述加热层外层设置保温层。Further, the outer layer of the heating layer is provided with a thermal insulation layer.

进一步地,接所述卧式转筒结构内的搅拌结构包括螺旋叶片和搅拌叶片,所述搅拌叶片均匀设置在所述卧式转筒结构的内壁上,所述螺旋叶片设置在所述卧式转筒结构内靠近进出料口处。Further, the stirring structure connected to the horizontal drum structure includes spiral blades and stirring blades, the stirring blades are uniformly arranged on the inner wall of the horizontal drum structure, and the spiral blades are arranged on the horizontal drum structure. The drum structure is close to the inlet and outlet.

进一步地,所述左端面采用锥形封头结构,所述右端面采用碟形封头结构。Further, the left end surface adopts a cone-shaped head structure, and the right end surface adopts a dish-shaped head structure.

进一步地,所述冷凝水排出管起始段设置截止阀。Further, a cut-off valve is set at the initial section of the condensed water discharge pipe.

进一步地,所述加热水带的横截面为半圆形。Further, the cross section of the heating water belt is semicircular.

进一步地,所述搅拌叶片轴向等距排列固定在所述卧式转筒结构的内壁上。Further, the stirring blades are arranged axially equidistantly and fixed on the inner wall of the horizontal drum structure.

本实用新型有益效果是:1、卧式转筒结构,使空间高度很低,耗用功率也较小,性价比较高。The beneficial effects of the utility model are as follows: 1. The horizontal drum structure makes the space height very low, the power consumption is also small, and the cost performance is high.

2、加热层采用集箱结构,加热水带连通进口集箱和出口集箱,且向出水集箱倾斜一定角度,通过出口集箱收集冷凝水,通过蒸汽压力将冷凝水压送到右端面的旋转接头后接疏水阀,实现只排水不排汽功能。2. The heating layer adopts a header structure. The heating water belt is connected to the inlet header and the outlet header, and is inclined at a certain angle to the outlet header. The condensed water is collected through the outlet header, and the condensed water is sent to the right end by steam pressure. The steam trap is connected behind the swivel joint to realize the function of only draining water but not exhausting steam.

3、实现在加热过程中同时旋转,配合筒体内部叶片搅拌,大大增强了加热效果,且加热均匀,提高了加热效率,节约了能耗。3. It realizes simultaneous rotation during the heating process, and cooperates with the stirring of the blades inside the cylinder, which greatly enhances the heating effect, and the heating is uniform, which improves the heating efficiency and saves energy consumption.

4、罐体外部设置保温层,降低热量损失。4. An insulation layer is set outside the tank to reduce heat loss.

5、熏醅过程中全封闭,避免了醋酸的浪费,也大大改善了作业环境。5. The process of fumigation is completely closed, which avoids the waste of acetic acid and greatly improves the working environment.

附图说明Description of drawings

图1是本实用新型的结构示意图。Fig. 1 is the structural representation of the utility model.

图2是图1的剖视图。FIG. 2 is a sectional view of FIG. 1 .

图3是是本实用新型的卧式转筒结构的结构示意图。Fig. 3 is a schematic structural view of the horizontal drum structure of the present invention.

图中,1.卧式转筒结构,2.加热层,3.支撑结构,4.搅拌结构,5.进口集箱,6.加热水带,7.出口集箱,8.左端面,9.右端面,10.旋转接头,11.进出料口,12.进蒸汽支管,13.进蒸汽总管,14.冷凝水排出管,15.疏水阀,16.螺旋叶片,17.搅拌叶片,18.截止阀,19.固定轴承座,20.调心滚轮座。In the figure, 1. Horizontal drum structure, 2. Heating layer, 3. Support structure, 4. Stirring structure, 5. Inlet header, 6. Heating water belt, 7. Outlet header, 8. Left end face, 9 .Right end face, 10. Rotary joint, 11. Material inlet and outlet, 12. Steam inlet branch pipe, 13. Steam inlet main pipe, 14. Condensed water discharge pipe, 15. Steam trap, 16. Spiral blade, 17. Stirring blade, 18 . Globe valve, 19. Fixed bearing seat, 20. Self-aligning roller seat.

具体实施方式detailed description

下面结合附图对本实用新型的具体实施方式做出说明。The specific embodiment of the utility model is described below in conjunction with the accompanying drawings.

附图中,1.卧式转筒结构,2.加热层,3.支撑结构,4.搅拌结构,5.进口集箱,6.加热水带,7.出口集箱,8.左端面,9.右端面,10.旋转接头,11.进出料口,12.进蒸汽支管,13.进蒸汽总管,14.冷凝水排出管,15.疏水阀,16.螺旋叶片,17.搅拌叶片,18.截止阀,19.固定轴承座,20.调心滚轮座。In the attached drawings, 1. Horizontal drum structure, 2. Heating layer, 3. Support structure, 4. Stirring structure, 5. Inlet header, 6. Heating hose, 7. Outlet header, 8. Left end face, 9. Right end face, 10. Rotary joint, 11. Material inlet and outlet, 12. Steam inlet branch pipe, 13. Steam inlet main pipe, 14. Condensed water discharge pipe, 15. Steam trap, 16. Spiral blade, 17. Stirring blade, 18. Globe valve, 19. Fixed bearing seat, 20. Self-aligning roller seat.

本实用新型涉及转筒式连续熏醅设备,包括卧式转筒结构1、加热层2、动力结构、支撑结构3、搅拌结构4,搅拌结构4设置在卧式转筒结构1内,保证物料均匀分布,提高热交换效率,并具有进料及出料的功能;动力结构连接卧式转筒结构1并提供动力,实现在加热过程中同时旋转,支撑结构3设置在卧式转筒结构1下支撑卧式转筒结构1,卧式转筒结构1,使空间高度很低,耗用功率也较小,性价比较高,卧式转筒结构1内设置与外界连通的呼吸器管路,卧式转筒结构1内的醅料温度升高时,筒内空气体积膨胀,通过呼吸器管路将多余气体排出筒外,保证筒内维持常压熏醅过程中全封闭,避免了醋酸的浪费,也大大改善了作业环境;加热层2设置在卧式转筒结构1外,加热层2采用集箱结构,集箱结构是将工质汇集起来,或将工质通过集箱结构重新分配到其它管道中,即汇集、混合、分配工质,保证工质均匀分配、均匀加热;加热层2内设置进口集箱5、加热水带6和出口集箱7,加热水带6连通进口集箱5和出口集箱7,加热水带6倾斜设置且向出水集箱倾斜,加热水带6内通入加热介质,加热介质可以是蒸汽、导热油等,对卧式转筒结构1内的物料进行加热,实现在加热过程中同时旋转,配合筒体内部叶片搅拌,大大增强了加热效果,且加热均匀。提高了加热效率,节约了能耗。The utility model relates to a drum-type continuous smoked unstrained spirits equipment, comprising a horizontal drum structure 1, a heating layer 2, a power structure, a support structure 3, and a stirring structure 4. The stirring structure 4 is arranged in the horizontal drum structure 1 to ensure that the material Evenly distributed, improving heat exchange efficiency, and has the function of feeding and discharging; the power structure is connected to the horizontal drum structure 1 and provides power to realize simultaneous rotation during the heating process, and the support structure 3 is set on the horizontal drum structure 1 The horizontal drum structure 1 is supported under the horizontal drum structure 1, so that the space height is very low, the power consumption is also small, and the cost performance is high. When the temperature of the fermented grains in the horizontal drum structure 1 rises, the volume of the air in the drum expands, and the excess gas is discharged out of the drum through the respirator pipeline, so as to ensure that the inside of the drum is fully closed during the process of maintaining the normal pressure of the fermented grains, and avoids the leakage of acetic acid. waste, and greatly improved the working environment; the heating layer 2 is set outside the horizontal drum structure 1, and the heating layer 2 adopts a header structure, which collects the working fluid or redistributes the working fluid through the header structure into other pipelines, that is, to collect, mix, and distribute working fluids to ensure uniform distribution and uniform heating of the working fluids; the inlet header 5, the heating water belt 6 and the outlet header 7 are set in the heating layer 2, and the heating water belt 6 is connected to the inlet collection The tank 5 and the outlet header 7, the heating water belt 6 is inclined to the water outlet header, and the heating medium is passed into the heating water belt 6. The heating medium can be steam, heat transfer oil, etc., for the horizontal drum structure 1 The material is heated to achieve simultaneous rotation during the heating process, and it is stirred with the blades inside the cylinder, which greatly enhances the heating effect and evenly heats. Improve heating efficiency and save energy consumption.

卧式转筒结构1的两端设置左端面8和右端面9,左端面8中心处设置进出料口11,通过左端面8中心处设置进出料口11排出产物,并且通过正转和反转卧式转筒结构1实现进出料口11进料和出料,右端面9中心处设置旋转接头10,采用多通道设计,即能够满足多种物料同时添加的需求,并满足进加热介质与排加热介质能同时进行,有效的提高生产及操作效率,减少发酵罐内混合物料接触外界的时间,提高发酵效率。The two ends of the horizontal drum structure 1 are provided with a left end surface 8 and a right end surface 9, and the center of the left end surface 8 is provided with an inlet and outlet 11, and the product is discharged through the inlet and outlet 11 provided at the center of the left end surface 8, and through forward rotation and reverse rotation The horizontal drum structure 1 realizes the feeding and discharging of the material inlet and outlet 11, and the rotary joint 10 is set at the center of the right end surface 9. It adopts a multi-channel design, which can meet the needs of adding multiple materials at the same time, and meet the heating medium and discharge requirements. The heating medium can be carried out at the same time, effectively improving production and operation efficiency, reducing the time for the mixed materials in the fermentation tank to contact the outside world, and improving fermentation efficiency.

进口集箱5通过进蒸汽支管12与进蒸汽总管13连通,出口集箱7与冷凝水排出管14连接,进蒸汽总管13和冷凝水排出管14均与旋转接头10连接,冷凝水排出管14出旋转接头10后接疏水阀,通过出口集箱7收集冷凝水,通过蒸汽压力将冷凝水压送到右端面9的旋转接头10后接疏水阀15,实现只排水不排汽功能。The inlet header 5 communicates with the steam inlet main pipe 13 through the steam inlet branch pipe 12, the outlet header 7 is connected with the condensed water discharge pipe 14, the steam inlet main pipe 13 and the condensed water discharge pipe 14 are connected with the rotary joint 10, and the condensed water discharge pipe 14 Out of the swivel joint 10, a steam trap is connected, and the condensed water is collected through the outlet header 7, and the condensed water is sent to the right end surface 9 of the swivel joint 10 by steam pressure, followed by a steam trap 15, so as to realize the function of only draining water but not exhausting steam.

加热水带6倾斜度为0.5~1%,便于冷凝水排出。The inclination of the heating water belt 6 is 0.5-1%, which is convenient for condensed water to be discharged.

加热水带6的横截面为半圆形,通常加热水带6横截面为圆形,与卧式转筒结构1表面不能完全贴合,热交换效率低,半圆形的半径选取应确保与卧式转筒结构1表面完全贴合,加热水带6与卧式转筒结构1表面完全贴合,提高热交换效率。The cross-section of the heating water belt 6 is semicircular. Usually, the cross-section of the heating water belt 6 is circular, which cannot completely fit the surface of the horizontal drum structure 1, and the heat exchange efficiency is low. The selection of the radius of the semicircle should ensure that The surface of the horizontal drum structure 1 is completely bonded, and the heating water belt 6 is completely bonded to the surface of the horizontal drum structure 1, thereby improving heat exchange efficiency.

支撑结构3包括固定轴承座19和调心滚轮座20,固定轴承座19固定在卧式转筒结构1右端面9上,支撑卧式转筒结构1左端并通过动力结构为卧式转筒结构1提供旋转动力,调心滚轮座20设置在卧式转筒结构1左右两侧,调心滚轮座20与固定轴承座19 配合保持卧式转筒结构1的水平。The support structure 3 includes a fixed bearing seat 19 and a self-aligning roller seat 20. The fixed bearing seat 19 is fixed on the right end surface 9 of the horizontal drum structure 1, supports the left end of the horizontal drum structure 1 and forms a horizontal drum structure through the power structure. 1 to provide rotational power, the self-aligning roller seat 20 is arranged on the left and right sides of the horizontal drum structure 1, and the self-aligning roller seat 20 cooperates with the fixed bearing seat 19 to maintain the level of the horizontal drum structure 1.

加热层2外层设置保温层,能有效降低热量损失。The outer layer of the heating layer 2 is provided with an insulating layer, which can effectively reduce heat loss.

卧式转筒结构1内的搅拌结构4包括螺旋叶片16和搅拌叶片17,搅拌叶片17均匀设置在卧式转筒结构1的内壁上,螺旋叶片16设置在卧式转筒结构1内靠近进出料口11处,螺旋叶片16起到导料作用,搅拌叶片17轴向等距排列固定在卧式转筒结构1的内壁上,大大增强了加热效果,且加热均匀,提高了加热效率,节约了能耗,螺旋叶片16设置实现正转进料,反转出料,进料出料速度均匀快速。The stirring structure 4 in the horizontal drum structure 1 includes a spiral blade 16 and a stirring blade 17, the stirring blade 17 is evenly arranged on the inner wall of the horizontal drum structure 1, and the spiral blade 16 is arranged in the horizontal drum structure 1 close to the entrance and exit At the material inlet 11, the spiral blade 16 acts as a material guide, and the stirring blade 17 is arranged in an axial equidistant manner and fixed on the inner wall of the horizontal drum structure 1, which greatly enhances the heating effect, and the heating is uniform, which improves the heating efficiency and saves energy. To reduce energy consumption, the screw blade 16 is set to realize forward rotation feeding and reverse rotation discharging, and the feeding and discharging speed is uniform and fast.

冷凝水排出管起始段设置截止阀18,方便维修时使用,排出冷凝水内带有的杂质。A cut-off valve 18 is arranged at the initial section of the condensed water discharge pipe, which is convenient for use during maintenance and discharges impurities contained in the condensed water.

实施例1:转筒式连续熏醅设备,包括卧式转筒结构、加热层、动力结构、支撑结构、搅拌结构,搅拌结构设置在卧式转筒结构内,保证物料均匀分布,提高热交换效率,并具有进料及出料的功能;动力结构连接卧式转筒结构并提供动力,实现在加热过程中同时旋转,支撑结构设置在卧式转筒结构下支撑卧式转筒结构,卧式转筒结构,使空间高度很低,耗用功率也较小,性价比较高,卧式转筒结构内设置与外界连通的呼吸器管路,卧式转筒结构内的醅料温度升高时,筒内空气体积膨胀,通过呼吸器管路将多余气体排出筒外,保证筒内维持常压,熏醅过程中全封闭,避免了醋酸的浪费,也大大改善了作业环境;加热层设置在卧式转筒结构外,加热层采用集箱结构,集箱结构是将工质汇集起来,或将工质通过集箱结构重新分配到其它管道中,即汇集、混合、分配工质,保证工质均匀分配、均匀加热;加热层内设置进口集箱、加热水带和出口集箱,加热水带连通进口集箱和出口集箱,加热水带倾斜设置且向出水集箱倾斜,加热水带内通入加热介质,加热介质可以是蒸汽、导热油等,对卧式转筒结构内的物料进行加热,实现在加热过程中同时旋转,配合筒体内部叶片搅拌,大大增强了加热效果,且加热均匀,提高了加热效率,节约了能耗。Embodiment 1: Drum-type continuous smoked unstrained spirits equipment, including a horizontal drum structure, a heating layer, a power structure, a support structure, and a stirring structure. The stirring structure is arranged in the horizontal drum structure to ensure uniform distribution of materials and improve heat exchange. efficiency, and has the function of feeding and discharging; the power structure is connected to the horizontal drum structure and provides power to realize simultaneous rotation during the heating process, and the support structure is set under the horizontal drum structure to support the horizontal drum structure. The vertical drum structure makes the space height very low, the power consumption is also small, and the cost performance is high. The respirator pipeline connected with the outside is set in the horizontal drum structure, and the temperature of the fermented grains in the horizontal drum structure rises. When the temperature is high, the volume of the air in the cylinder expands, and the excess gas is discharged out of the cylinder through the respirator pipeline to ensure that the pressure in the cylinder is maintained. Outside the horizontal drum structure, the heating layer adopts a header structure, which collects the working fluid or redistributes the working fluid to other pipelines through the header structure, that is, collects, mixes, and distributes the working fluid to ensure The working fluid is evenly distributed and heated; the heating layer is equipped with an inlet header, a heating water belt and an outlet header, and the heating water belt is connected to the inlet header and the outlet header. The heating medium is fed into the belt, and the heating medium can be steam, heat transfer oil, etc., to heat the material in the horizontal drum structure, and to realize simultaneous rotation during the heating process, and to cooperate with the internal blade stirring of the drum to greatly enhance the heating effect. And the heating is uniform, the heating efficiency is improved, and the energy consumption is saved.

卧式转筒结构的两端设置左端面和右端面,左端面采用锥形封头结构,右端面采用碟形封头结构,锥形封头结构的左端面中心处设置进出料口,通过左端面中心处设置进出料口排出产物,并且通过正转和反转卧式转筒结构实现进出料口进料和出料,方便物料进出,右端面中心处设置旋转接头,采用多通道设计,即能够满足多种物料同时添加的需求,并满足进加热介质与排加热介质能同时进行,有效的提高生产及操作效率,减少发酵罐内混合物料接触外界的时间,提高发酵效率。The two ends of the horizontal drum structure are provided with left and right end faces, the left end face adopts a conical head structure, the right end face adopts a dish-shaped head structure, and the center of the left end face of the conical head structure is provided with an inlet and outlet, through the left The inlet and outlet are set at the center of the surface to discharge the product, and the inlet and outlet are fed and discharged through the forward and reverse horizontal drum structure, which is convenient for the material to enter and exit. It can meet the demand of adding multiple materials at the same time, and meet the requirements of heating medium feeding and discharging heating medium at the same time, effectively improving production and operation efficiency, reducing the time for the mixed materials in the fermentation tank to contact the outside world, and improving fermentation efficiency.

进口集箱通过进蒸汽支管与进蒸汽总管连通,出口集箱与冷凝水排出管连接,进蒸 汽总管和冷凝水排出管均与旋转接头连接,冷凝水排出管出旋转接头后接疏水阀,通过出口集箱收集冷凝水,通过蒸汽压力将冷凝水压送到右端面的旋转接头后接疏水阀,实现只排水不排汽功能。The inlet header is connected with the steam inlet main pipe through the steam inlet branch pipe, the outlet header is connected with the condensed water discharge pipe, the steam inlet main pipe and the condensed water discharge pipe are connected with the rotary joint, and the condensed water discharge pipe is connected with the steam trap after exiting the rotary joint. The outlet header collects the condensed water, and sends the condensed water to the rotary joint on the right end face through the steam pressure, and then connects the steam trap to realize the function of only draining water but not exhausting steam.

实施例2:转筒式连续熏醅设备,包括卧式转筒结构、加热层、动力结构、支撑结构、搅拌结构,搅拌结构设置在卧式转筒结构内,保证物料均匀分布,提高热交换效率,并具有进料及出料的功能;动力结构连接卧式转筒结构并提供动力,实现在加热过程中同时旋转,支撑结构设置在卧式转筒结构下支撑卧式转筒结构,卧式转筒结构,使空间高度很低,耗用功率也较小,性价比较高,卧式转筒结构内设置与外界连通的呼吸器管路,卧式转筒结构内的醅料温度升高时,筒内空气体积膨胀,通过呼吸器管路将多余气体排出筒外,保证筒内维持常压,熏醅过程中全封闭,避免了醋酸的浪费,也大大改善了作业环境;加热层设置在卧式转筒结构外,加热层采用集箱结构,集箱结构是将工质汇集起来,或将工质通过集箱结构重新分配到其它管道中,即汇集、混合、分配工质,保证工质均匀分配、均匀加热;加热层内设置进口集箱、加热水带和出口集箱,加热水带连通进口集箱和出口集箱,加热水带倾斜设置且向出水集箱倾斜,加热水带内通入加热介质,加热介质可以是蒸汽、导热油等,对卧式转筒结构内的物料进行加热,实现在加热过程中同时旋转,配合筒体内部叶片搅拌,大大增强了加热效果,且加热均匀。提高了加热效率,节约了能耗。Embodiment 2: Drum-type continuous smoked unstrained spirits equipment, including a horizontal drum structure, a heating layer, a power structure, a support structure, and a stirring structure. The stirring structure is arranged in the horizontal drum structure to ensure uniform distribution of materials and improve heat exchange. efficiency, and has the function of feeding and discharging; the power structure is connected to the horizontal drum structure and provides power to realize simultaneous rotation during the heating process, and the support structure is set under the horizontal drum structure to support the horizontal drum structure. The vertical drum structure makes the space height very low, the power consumption is also small, and the cost performance is high. The respirator pipeline connected with the outside is set in the horizontal drum structure, and the temperature of the fermented grains in the horizontal drum structure rises. When the temperature is high, the volume of the air in the cylinder expands, and the excess gas is discharged out of the cylinder through the respirator pipeline to ensure that the pressure in the cylinder is maintained. Outside the horizontal drum structure, the heating layer adopts a header structure, which collects the working fluid or redistributes the working fluid to other pipelines through the header structure, that is, collects, mixes, and distributes the working fluid to ensure The working fluid is evenly distributed and heated; the heating layer is equipped with an inlet header, a heating water belt and an outlet header, and the heating water belt is connected to the inlet header and the outlet header. The heating medium is fed into the belt, and the heating medium can be steam, heat transfer oil, etc., to heat the material in the horizontal drum structure, and to realize simultaneous rotation during the heating process, and to cooperate with the internal blade stirring of the drum to greatly enhance the heating effect. And heat evenly. Improve heating efficiency and save energy consumption.

加热水带倾斜度为0.5~1%,便于冷凝水排出,通常加热水带横截面为圆形,与卧式转筒结构表面不能完全贴合,热交换效率低,加热水带的横截面为半圆形,半圆形的半径选取应确保与卧式转筒结构表面完全贴合,加热水带与卧式转筒结构表面完全贴合,提高热交换效率。The inclination of the heating hose is 0.5-1%, which is convenient for the discharge of condensed water. Usually, the cross section of the heating hose is circular, which cannot completely fit the surface of the horizontal drum structure, and the heat exchange efficiency is low. The cross section of the heating hose is Semicircle, the radius of the semicircle should be selected to ensure that it is completely attached to the surface of the horizontal drum structure, and the heating water belt is completely attached to the surface of the horizontal drum structure to improve heat exchange efficiency.

实施例3:转筒式连续熏醅设备,包括卧式转筒结构、加热层、动力结构、支撑结构、搅拌结构,搅拌结构设置在卧式转筒结构内,保证物料均匀分布,提高热交换效率,并具有进料及出料的功能;动力结构连接卧式转筒结构并提供动力,实现在加热过程中同时旋转,支撑结构设置在卧式转筒结构下支撑卧式转筒结构,卧式转筒结构,使空间高度很低,耗用功率也较小,性价比较高,卧式转筒结构内设置与外界连通的呼吸器管路,卧式转筒结构内的醅料温度升高时,筒内空气体积膨胀,通过呼吸器管路将多余气体排出筒外,保证筒内维持常压,熏醅过程中全封闭,避免了醋酸的浪费,也大大改善了作业环境;加热层设置在卧式转筒结构外,加热层采用集箱结构,集箱结构是将工质汇集 起来,或将工质通过集箱结构重新分配到其它管道中,即汇集、混合、分配工质,保证工质均匀分配、均匀加热;加热层内设置进口集箱、加热水带和出口集箱,加热水带连通进口集箱和出口集箱,加热水带倾斜设置且向出水集箱倾斜,加热水带内通入加热介质,加热介质可以是蒸汽、导热油等,对卧式转筒结构内的物料进行加热,实现在加热过程中同时旋转,配合筒体内部叶片搅拌,大大增强了加热效果,且加热均匀。提高了加热效率,节约了能耗。Embodiment 3: Drum-type continuous smoked unstrained spirits equipment, including a horizontal drum structure, a heating layer, a power structure, a support structure, and a stirring structure. The stirring structure is arranged in the horizontal drum structure to ensure uniform distribution of materials and improve heat exchange. efficiency, and has the function of feeding and discharging; the power structure is connected to the horizontal drum structure and provides power to realize simultaneous rotation during the heating process, and the support structure is set under the horizontal drum structure to support the horizontal drum structure. The vertical drum structure makes the space height very low, the power consumption is also small, and the cost performance is high. The respirator pipeline connected with the outside is set in the horizontal drum structure, and the temperature of the fermented grains in the horizontal drum structure rises. When the temperature is high, the volume of the air in the cylinder expands, and the excess gas is discharged out of the cylinder through the respirator pipeline to ensure that the pressure in the cylinder is maintained. Outside the horizontal drum structure, the heating layer adopts a header structure, which collects the working fluid or redistributes the working fluid to other pipelines through the header structure, that is, collects, mixes, and distributes the working fluid to ensure The working fluid is evenly distributed and heated; the heating layer is equipped with an inlet header, a heating water belt and an outlet header, and the heating water belt is connected to the inlet header and the outlet header. The heating medium is fed into the belt, and the heating medium can be steam, heat transfer oil, etc., to heat the material in the horizontal drum structure, and to realize simultaneous rotation during the heating process, and to cooperate with the internal blade stirring of the drum to greatly enhance the heating effect. And heat evenly. Improve heating efficiency and save energy consumption.

支撑结构包括固定轴承座和调心滚轮座,固定轴承座固定在卧式转筒结构右端面上,旋转接头与固定轴承座套接固定,支撑卧式转筒结构左端并通过动力结构为卧式转筒结构提供旋转动力,调心滚轮座设置在卧式转筒结构左右两侧,调心滚轮座与固定轴承座配合保持卧式转筒结构的水平。The support structure includes a fixed bearing seat and a self-aligning roller seat. The fixed bearing seat is fixed on the right end surface of the horizontal drum structure. The drum structure provides the rotating power, and the self-aligning roller seat is arranged on the left and right sides of the horizontal drum structure, and the self-aligning roller seat cooperates with the fixed bearing seat to maintain the level of the horizontal drum structure.

实施例4:转筒式连续熏醅设备,包括卧式转筒结构、加热层、动力结构、支撑结构、搅拌结构,搅拌结构设置在卧式转筒结构内,保证物料均匀分布,提高热交换效率,并具有进料及出料的功能;动力结构连接卧式转筒结构并提供动力,实现在加热过程中同时旋转,支撑结构设置在卧式转筒结构下支撑卧式转筒结构,卧式转筒结构,使空间高度很低,耗用功率也较小,性价比较高,卧式转筒结构内设置与外界连通的呼吸器管路,卧式转筒结构内的醅料温度升高时,筒内空气体积膨胀,通过呼吸器管路将多余气体排出筒外,保证筒内维持常压,熏醅过程中全封闭,避免了醋酸的浪费,也大大改善了作业环境;加热层设置在卧式转筒结构外,加热层采用集箱结构,集箱结构是将工质汇集起来,或将工质通过集箱结构重新分配到其它管道中,即汇集、混合、分配工质,保证工质均匀分配、均匀加热;加热层内设置进口集箱、加热水带和出口集箱,加热水带连通进口集箱和出口集箱,加热水带倾斜设置且向出水集箱倾斜,加热水带内通入加热介质,加热介质可以是蒸汽、导热油等,对卧式转筒结构内的物料进行加热,实现在加热过程中同时旋转,配合筒体内部叶片搅拌,大大增强了加热效果,且加热均匀。提高了加热效率,节约了能耗。Embodiment 4: Drum-type continuous smoked unstrained spirits equipment, including a horizontal drum structure, a heating layer, a power structure, a support structure, and a stirring structure. The stirring structure is arranged in the horizontal drum structure to ensure uniform distribution of materials and improve heat exchange. efficiency, and has the function of feeding and discharging; the power structure is connected to the horizontal drum structure and provides power to realize simultaneous rotation during the heating process, and the support structure is set under the horizontal drum structure to support the horizontal drum structure. The vertical drum structure makes the space height very low, the power consumption is also small, and the cost performance is high. The respirator pipeline connected with the outside is set in the horizontal drum structure, and the temperature of the fermented grains in the horizontal drum structure rises. When the temperature is high, the volume of the air in the cylinder expands, and the excess gas is discharged out of the cylinder through the respirator pipeline to ensure that the pressure in the cylinder is maintained. Outside the horizontal drum structure, the heating layer adopts a header structure, which collects the working fluid or redistributes the working fluid to other pipelines through the header structure, that is, collects, mixes, and distributes the working fluid to ensure The working fluid is evenly distributed and heated; the heating layer is equipped with an inlet header, a heating water belt and an outlet header, and the heating water belt is connected to the inlet header and the outlet header. The heating medium is fed into the belt, and the heating medium can be steam, heat transfer oil, etc., to heat the material in the horizontal drum structure, and to realize simultaneous rotation during the heating process, and to cooperate with the internal blade stirring of the drum to greatly enhance the heating effect. And heat evenly. Improve heating efficiency and save energy consumption.

加热层外层设置保温层,能有效降低热量损失。The outer layer of the heating layer is provided with an insulation layer, which can effectively reduce heat loss.

实施例5:转筒式连续熏醅设备,包括卧式转筒结构、加热层、动力结构、支撑结构、搅拌结构,搅拌结构设置在卧式转筒结构内,保证物料均匀分布,提高热交换效率,并具有进料及出料的功能;动力结构连接卧式转筒结构并提供动力,实现在加热过程中同时旋转,支撑结构设置在卧式转筒结构下支撑卧式转筒结构,卧式转筒结构,使空间高 度很低,耗用功率也较小,性价比较高,卧式转筒结构内设置与外界连通的呼吸器管路,卧式转筒结构内的醅料温度升高时,筒内空气体积膨胀,通过呼吸器管路将多余气体排出筒外,保证筒内维持常压,熏醅过程中全封闭,避免了醋酸的浪费,也大大改善了作业环境;加热层设置在卧式转筒结构外,加热层采用集箱结构,集箱结构是将工质汇集起来,或将工质通过集箱结构重新分配到其它管道中,即汇集、混合、分配工质,保证工质均匀分配、均匀加热;加热层内设置进口集箱、加热水带和出口集箱,加热水带连通进口集箱和出口集箱,加热水带倾斜设置且向出水集箱倾斜,加热水带内通入加热介质,加热介质可以是蒸汽、导热油等,对卧式转筒结构内的物料进行加热,实现在加热过程中同时旋转,配合筒体内部叶片搅拌,大大增强了加热效果,且加热均匀。提高了加热效率,节约了能耗。Embodiment 5: Drum-type continuous smoked unstrained spirits equipment, including a horizontal drum structure, a heating layer, a power structure, a support structure, and a stirring structure. The stirring structure is arranged in the horizontal drum structure to ensure uniform distribution of materials and improve heat exchange. efficiency, and has the function of feeding and discharging; the power structure is connected to the horizontal drum structure and provides power to realize simultaneous rotation during the heating process, and the support structure is set under the horizontal drum structure to support the horizontal drum structure. The vertical drum structure makes the space height very low, the power consumption is also small, and the cost performance is high. The respirator pipeline connected with the outside is set in the horizontal drum structure, and the temperature of the fermented grains in the horizontal drum structure rises. When the temperature is high, the volume of the air in the cylinder expands, and the excess gas is discharged out of the cylinder through the respirator pipeline to ensure that the pressure in the cylinder is maintained. Outside the horizontal drum structure, the heating layer adopts a header structure, which collects the working fluid or redistributes the working fluid to other pipelines through the header structure, that is, collects, mixes, and distributes the working fluid to ensure The working fluid is evenly distributed and heated; the heating layer is equipped with an inlet header, a heating water belt and an outlet header, and the heating water belt is connected to the inlet header and the outlet header. The heating medium is fed into the belt, and the heating medium can be steam, heat transfer oil, etc., to heat the material in the horizontal drum structure, and to realize simultaneous rotation during the heating process, and to cooperate with the internal blade stirring of the drum to greatly enhance the heating effect. And heat evenly. Improve heating efficiency and save energy consumption.

卧式转筒结构的两端设置左端面和右端面,左端面中心处设置进出料口,通过左端面中心处设置进出料口排出产物,并且通过正转和反转卧式转筒结构实现进出料口进料和出料,方便物料进出,右端面中心处设置旋转接头,采用多通道设计,即能够满足多种物料同时添加的需求,并满足进加热介质与排加热介质能同时进行,有效的提高生产及操作效率,减少发酵罐内混合物料接触外界的时间,提高发酵效率。The two ends of the horizontal drum structure are provided with left and right end faces, and the center of the left end face is provided with an inlet and outlet, and the product is discharged through the inlet and outlet at the center of the left end face, and the inlet and outlet are realized through forward and reverse horizontal drum structures The feeding and discharging of the material port is convenient for the material to enter and exit. The rotary joint is set at the center of the right end face, and the multi-channel design is adopted, which can meet the needs of adding multiple materials at the same time, and can simultaneously enter the heating medium and discharge the heating medium, effectively Improve production and operation efficiency, reduce the time for the mixed materials in the fermentation tank to contact the outside world, and improve fermentation efficiency.

进口集箱通过进蒸汽支管与进蒸汽总管连通,出口集箱与冷凝水排出管连接,进蒸汽总管和冷凝水排出管均与旋转接头连接,冷凝水排出管出旋转接头后接疏水阀,通过出口集箱收集冷凝水,通过蒸汽压力将冷凝水压送到右端面的旋转接头后接疏水阀,实现只排水不排汽功能。The inlet header is connected with the steam inlet main pipe through the steam inlet branch pipe, the outlet header is connected with the condensed water discharge pipe, the steam inlet main pipe and the condensed water discharge pipe are connected with the rotary joint, and the condensed water discharge pipe is connected with the steam trap after exiting the rotary joint. The outlet header collects the condensed water, and sends the condensed water to the rotary joint on the right end face through the steam pressure, and then connects the steam trap to realize the function of only draining water but not exhausting steam.

卧式转筒结构内的搅拌结构包括螺旋叶片和搅拌叶片,搅拌叶片均匀设置在卧式转筒结构的内壁上,螺旋叶片设置在卧式转筒结构内靠近进出料口处,螺旋叶片起到导料作用,搅拌叶片轴向等距排列固定在卧式转筒结构的内壁上,大大增强了加热效果,且加热均匀,提高了加热效率,节约了能耗,螺旋叶片设置实现正转进料,反转出料,进料出料速度均匀快速。The stirring structure in the horizontal drum structure includes spiral blades and stirring blades. The stirring blades are evenly arranged on the inner wall of the horizontal drum structure, and the spiral blades are arranged in the horizontal drum structure near the inlet and outlet. The function of material guide, the axial equidistant arrangement of the stirring blades is fixed on the inner wall of the horizontal drum structure, which greatly enhances the heating effect, and the heating is uniform, which improves the heating efficiency and saves energy consumption. The spiral blade setting realizes forward rotation feeding , reversing the discharge, the feeding and discharging speed is uniform and fast.

实施例6:转筒式连续熏醅设备,包括卧式转筒结构、加热层、动力结构、支撑结构、搅拌结构,搅拌结构设置在卧式转筒结构内,保证物料均匀分布,提高热交换效率,并具有进料及出料的功能;动力结构连接卧式转筒结构并提供动力,实现在加热过程中同时旋转,支撑结构设置在卧式转筒结构下支撑卧式转筒结构,卧式转筒结构,使空间高度很低,耗用功率也较小,性价比较高,卧式转筒结构内设置与外界连通的呼吸器管路, 卧式转筒结构内的醅料温度升高时,筒内空气体积膨胀,通过呼吸器管路将多余气体排出筒外,保证筒内维持常压,熏醅过程中全封闭,避免了醋酸的浪费,也大大改善了作业环境;加热层设置在卧式转筒结构外,加热层采用集箱结构,集箱结构是将工质汇集起来,或将工质通过集箱结构重新分配到其它管道中,即汇集、混合、分配工质,保证工质均匀分配、均匀加热;加热层内设置进口集箱、加热水带和出口集箱,加热水带连通进口集箱和出口集箱,加热水带倾斜设置且向出水集箱倾斜,加热水带内通入加热介质,加热介质可以是蒸汽、导热油等,对卧式转筒结构内的物料进行加热,实现在加热过程中同时旋转,配合筒体内部叶片搅拌,大大增强了加热效果,且加热均匀。提高了加热效率,节约了能耗。Embodiment 6: Drum-type continuous smoked fermented grains equipment, including a horizontal drum structure, a heating layer, a power structure, a support structure, and a stirring structure. The stirring structure is arranged in the horizontal drum structure to ensure uniform distribution of materials and improve heat exchange. efficiency, and has the function of feeding and discharging; the power structure is connected to the horizontal drum structure and provides power to realize simultaneous rotation during the heating process, and the support structure is set under the horizontal drum structure to support the horizontal drum structure. The vertical drum structure makes the space height very low, the power consumption is also small, and the cost performance is high. The horizontal drum structure is equipped with a respirator pipeline connected with the outside world, and the temperature of the fermented grains in the horizontal drum structure rises. When the temperature is high, the volume of the air in the cylinder expands, and the excess gas is discharged out of the cylinder through the respirator pipeline to ensure that the pressure in the cylinder is maintained. Outside the horizontal drum structure, the heating layer adopts a header structure, which collects the working fluid or redistributes the working fluid to other pipelines through the header structure, that is, collects, mixes, and distributes the working fluid to ensure The working fluid is evenly distributed and heated; the heating layer is equipped with an inlet header, a heating water belt and an outlet header, and the heating water belt is connected to the inlet header and the outlet header. The heating medium is fed into the belt, and the heating medium can be steam, heat transfer oil, etc., to heat the material in the horizontal drum structure, and to realize simultaneous rotation during the heating process, and to cooperate with the internal blade stirring of the drum to greatly enhance the heating effect. And heat evenly. Improve heating efficiency and save energy consumption.

卧式转筒结构的两端设置左端面和右端面,左端面采用锥形封头结构,右端面采用碟形封头结构,锥形封头结构的左端面中心处设置进出料口,通过左端面中心处设置进出料口排出产物,并且通过正转和反转卧式转筒结构实现进出料口进料和出料,方便物料进出,右端面中心处设置旋转接头,采用多通道设计,即能够满足多种物料同时添加的需求,并满足进加热介质与排加热介质能同时进行,有效的提高生产及操作效率,减少发酵罐内混合物料接触外界的时间,提高发酵效率。The two ends of the horizontal drum structure are provided with left and right end faces, the left end face adopts a conical head structure, the right end face adopts a dish-shaped head structure, and the center of the left end face of the conical head structure is provided with an inlet and outlet, through the left The inlet and outlet are set at the center of the surface to discharge the product, and the inlet and outlet are fed and discharged through the forward and reverse horizontal drum structure, which is convenient for the material to enter and exit. It can meet the demand of adding multiple materials at the same time, and meet the requirements of heating medium feeding and discharging heating medium at the same time, effectively improving production and operation efficiency, reducing the time for the mixed materials in the fermentation tank to contact the outside world, and improving fermentation efficiency.

进口集箱通过进蒸汽支管与进蒸汽总管连通,出口集箱与冷凝水排出管连接,进蒸汽总管和冷凝水排出管均与旋转接头连接,冷凝水排出管出旋转接头后接疏水阀,通过出口集箱收集冷凝水,通过蒸汽压力将冷凝水压送到右端面的旋转接头后接疏水阀,实现只排水不排汽功能。The inlet header is connected with the steam inlet main pipe through the steam inlet branch pipe, the outlet header is connected with the condensed water discharge pipe, the steam inlet main pipe and the condensed water discharge pipe are connected with the rotary joint, and the condensed water discharge pipe is connected with the steam trap after exiting the rotary joint. The outlet header collects the condensed water, and sends the condensed water to the rotary joint on the right end face through the steam pressure, and then connects the steam trap to realize the function of only draining water but not exhausting steam.

实施例7:转筒式连续熏醅设备,包括卧式转筒结构、加热层、动力结构、支撑结构、搅拌结构,搅拌结构设置在卧式转筒结构内,保证物料均匀分布,提高热交换效率,并具有进料及出料的功能;动力结构连接卧式转筒结构并提供动力,实现在加热过程中同时旋转,支撑结构设置在卧式转筒结构下支撑卧式转筒结构,卧式转筒结构,使空间高度很低,耗用功率也较小,性价比较高,卧式转筒结构内设置与外界连通的呼吸器管路,卧式转筒结构内的醅料温度升高时,筒内空气体积膨胀,通过呼吸器管路将多余气体排出筒外,保证筒内维持常压,熏醅过程中全封闭,避免了醋酸的浪费,也大大改善了作业环境;加热层设置在卧式转筒结构外,加热层采用集箱结构,集箱结构是将工质汇集起来,或将工质通过集箱结构重新分配到其它管道中,即汇集、混合、分配工质,保证工质均匀分配、均匀加热;加热层内设置进口集箱、加热水带和出口集箱,加热水带连 通进口集箱和出口集箱,加热水带倾斜设置且向出水集箱倾斜,加热水带内通入加热介质,加热介质可以是蒸汽、导热油等,对卧式转筒结构内的物料进行加热,实现在加热过程中同时旋转,配合筒体内部叶片搅拌,大大增强了加热效果,且加热均匀。提高了加热效率,节约了能耗。Embodiment 7: Drum-type continuous smoked unstrained spirits equipment, including a horizontal drum structure, a heating layer, a power structure, a support structure, and a stirring structure. The stirring structure is arranged in the horizontal drum structure to ensure uniform distribution of materials and improve heat exchange. efficiency, and has the function of feeding and discharging; the power structure is connected to the horizontal drum structure and provides power to realize simultaneous rotation during the heating process, and the support structure is set under the horizontal drum structure to support the horizontal drum structure. The vertical drum structure makes the space height very low, the power consumption is also small, and the cost performance is high. The respirator pipeline connected with the outside is set in the horizontal drum structure, and the temperature of the fermented grains in the horizontal drum structure rises. When the temperature is high, the volume of the air in the cylinder expands, and the excess gas is discharged out of the cylinder through the respirator pipeline to ensure that the pressure in the cylinder is maintained. Outside the horizontal drum structure, the heating layer adopts a header structure, which collects the working fluid or redistributes the working fluid to other pipelines through the header structure, that is, collects, mixes, and distributes the working fluid to ensure The working fluid is evenly distributed and heated; the heating layer is equipped with an inlet header, a heating water belt and an outlet header, and the heating water belt is connected to the inlet header and the outlet header. The heating medium is fed into the belt, and the heating medium can be steam, heat transfer oil, etc., to heat the material in the horizontal drum structure, and to realize simultaneous rotation during the heating process, and to cooperate with the internal blade stirring of the drum to greatly enhance the heating effect. And heat evenly. Improve heating efficiency and save energy consumption.

卧式转筒结构的两端设置左端面和右端面,左端面采用锥形封头结构,右端面采用碟形封头结构,锥形封头结构的左端面中心处设置进出料口,通过左端面中心处设置进出料口排出产物,并且通过正转和反转卧式转筒结构实现进出料口进料和出料,方便物料进出,右端面中心处设置旋转接头,采用多通道设计,即能够满足多种物料同时添加的需求,有效的提高生产及操作效率,减少发酵罐内混合物料接触外界的时间,提高发酵效率。The two ends of the horizontal drum structure are provided with left and right end faces, the left end face adopts a conical head structure, the right end face adopts a dish-shaped head structure, and the center of the left end face of the conical head structure is provided with an inlet and outlet, through the left The inlet and outlet are set at the center of the surface to discharge the product, and the inlet and outlet are fed and discharged through the forward and reverse horizontal drum structure, which is convenient for the material to enter and exit. It can meet the demand of adding multiple materials at the same time, effectively improve production and operation efficiency, reduce the time for the mixed materials in the fermentation tank to contact the outside world, and improve fermentation efficiency.

进口集箱通过进蒸汽支管与进蒸汽总管连通,出口集箱与冷凝水排出管连接,进蒸汽总管和冷凝水排出管均与旋转接头连接,冷凝水排出管出旋转接头后接疏水阀,通过出口集箱收集冷凝水,通过蒸汽压力将冷凝水压送到右端面的旋转接头后接疏水阀,实现只排水不排汽功能。The inlet header is connected with the steam inlet main pipe through the steam inlet branch pipe, the outlet header is connected with the condensed water discharge pipe, the steam inlet main pipe and the condensed water discharge pipe are connected with the rotary joint, and the condensed water discharge pipe is connected with the steam trap after exiting the rotary joint. The outlet header collects the condensed water, and sends the condensed water to the rotary joint on the right end face through the steam pressure, and then connects the steam trap to realize the function of only draining water but not exhausting steam.

冷凝水排出管起始段设置截止阀,方便维修时使用,排出冷凝水内带有的杂质。A cut-off valve is installed at the beginning of the condensed water discharge pipe, which is convenient for maintenance and discharges impurities contained in the condensed water.

工作过程:作业前,应先启动动力结构带动卧式转筒结构空载运转,确认螺旋叶片的旋转方向正转;熏醅开始时,动力结构带动卧式转筒结构正转实现进料,同时热介质进入采用集箱结构的加热层加热醅料,实现在加热过程中同时卧式转筒结构旋转,配合卧式转筒结构内的搅拌叶片的搅拌作业,大大增强了加热效果,且加热均匀,提高了加热效率,提高发酵效率,节约了能耗;达到发酵的指标熏醅结束时,动力结构带动卧式转筒结构正转实现进料,实现连续出料。Working process: Before operation, the power structure should be started to drive the horizontal drum structure to run without load, and the rotation direction of the spiral blades should be confirmed to be forward; The heat medium enters the heating layer of the header structure to heat the fermented grains, and realizes the rotation of the horizontal drum structure at the same time during the heating process. With the stirring operation of the stirring blades in the horizontal drum structure, the heating effect is greatly enhanced, and the heating is uniform , improve heating efficiency, improve fermentation efficiency, and save energy consumption; when the fermentation index is reached, the power structure drives the horizontal drum structure to rotate forward to realize feeding and continuous discharging.

具体过程:动力结构的减速电机通过传动装置带动带动滚动轴承转动,从而促使卧式转筒结构转动,锥形封头结构的左端面中心处的进出料口进入物料,物料沿旋转的螺旋叶片注入卧式转筒结构筒体处,多个搅拌叶片轴向等距排列固定在卧式转筒结构的内壁上,搅拌叶片均是向转筒内部倾斜10~25°角固定的,使得物料在随卧式转筒结构转动时,搅拌叶片将物料带起的同时往转筒内部推进,从而实现连续进料的功能,进料后需要对卧式转筒结构内物料进行搅拌时继续正转,搅拌叶片是矩形断开的,在转筒转动时,相当于单个的搅拌叶片,并且在卧式转筒结构内空腔翻转时,每一段子叶片长度的小范围的物料不断被子叶片带起后抛洒落料,其搅拌均匀度大大优于普通的连续螺旋叶 片形成的整体滚动方式;卧式转筒结构正转,支撑结构的调心滚轮座上的调心滚轮相应的跟随着反转,卧式转筒结构内的物料逐渐增加,卧式转筒结构内重量也在不断增加,并且伴随间断叶片的起落,物料会有轻微晃动,在调心滚轮的作用下保持卧式转筒结构平稳转动,保持轴线固定,平衡滚动轴承的受力情况;当保持卧式转筒结构平稳转动,保持轴线固定,平衡滚动轴承的受力情况,卧式转筒结构内的醅料温度升高时,筒内空气体积膨胀,通过呼吸器管路将多余气体排出筒外,保证筒内维持常压;Specific process: the geared motor of the power structure drives the rolling bearing to rotate through the transmission device, thereby promoting the rotation of the horizontal drum structure, the material inlet and outlet at the center of the left end face of the conical head structure enters the material, and the material is injected into the horizontal cylinder along the rotating spiral blade. At the cylinder body of the rotary drum structure, a plurality of stirring blades are axially equidistantly arranged and fixed on the inner wall of the horizontal drum structure. When the rotary drum structure is rotating, the stirring blades will push the material into the drum while carrying it up, so as to realize the function of continuous feeding. It is rectangular and disconnected. When the drum rotates, it is equivalent to a single mixing blade. When the cavity in the horizontal drum structure is turned over, the small-scale materials of each section of the sub-blade length are continuously picked up by the sub-blades and thrown down. The uniformity of mixing is much better than the overall rolling mode formed by ordinary continuous spiral blades; the horizontal drum structure rotates forward, and the self-aligning rollers on the self-aligning roller seat of the supporting structure follow the reverse direction accordingly, and the horizontal rotation The material in the drum structure is gradually increasing, and the weight in the horizontal drum structure is also increasing, and with the ups and downs of the intermittent blades, the material will shake slightly. The axis is fixed to balance the force of the rolling bearing; when the horizontal drum structure is kept rotating smoothly, the axis is kept fixed and the force of the rolling bearing is balanced. When the temperature of the fermented grains in the horizontal drum structure rises, the volume of the air in the drum expands , discharge the excess gas out of the cylinder through the respirator pipeline to ensure that the cylinder maintains normal pressure;

在搅拌物料的同时,加热介质通过蒸汽经进蒸汽总管进蒸汽支管进入加热层加热卧式转筒结构内的物料,加热层采用采用集箱结构,集箱结构是蒸汽通过进口集箱结构重新分配到加热水带中,加热水带即汇集、混合、分配工质,保证工质均匀分配、均匀加热,蒸汽的流量与压力合理设定,保证设备能稳定的运行与熏醅质量的稳定性;加热层内设置进口集箱、加热水带和出口集箱,加热水带连通进口集箱和出口集箱,加热水带倾斜设置且向出水集箱倾斜,通过出水集箱收集冷凝水,加热水带倾斜度为0.5~1%,便于冷凝水排出,通过蒸汽压力将冷凝水压送到右端面中心的旋转接头后接疏水阀,实现只排水不排蒸汽的功能,熏醅过程中全封闭,避免了醋酸的浪费,也大大改善了作业环境。While stirring the material, the heating medium enters the heating layer to heat the material in the horizontal drum structure through the steam inlet main pipe and the steam branch pipe. The heating layer adopts a header structure, and the header structure is that the steam is redistributed through the inlet header structure In the heating water belt, the heating water belt collects, mixes and distributes the working fluid to ensure the uniform distribution and uniform heating of the working fluid. The flow and pressure of the steam are set reasonably to ensure the stable operation of the equipment and the stability of the quality of the smoked grains; The heating layer is equipped with an inlet header, a heating water belt and an outlet header. The heating water belt is connected to the inlet header and the outlet header. The inclination of the belt is 0.5-1%, which is convenient for condensed water to discharge. The condensed water is sent to the rotary joint at the center of the right end face by steam pressure and then connected with a steam trap to realize the function of only draining water but not steam. The waste of acetic acid is avoided, and the working environment is greatly improved.

当熏醅发酵结束时,通过控制动力结构的减速电机使其带动卧式转筒结构反转,物料被搅拌叶片带起后落到前一排搅拌叶片上,从而将物料连续向搅拌叶片外的方向推进,卧式转筒结构内靠近进出料口处设置有螺旋叶片,到达进出料口的物料会经由螺旋叶片将物料推送到进出料口并推出进出料口,随着物料的排出从而实现连续出料的功能。When the fermentation of the smoked grains is over, the geared motor of the power structure is controlled to drive the horizontal drum structure to reverse, and the material is lifted by the stirring blades and then falls to the previous row of stirring blades, so that the materials are continuously sent to the outside of the stirring blades. The horizontal drum structure is equipped with a spiral blade near the inlet and outlet, and the material reaching the inlet and outlet will be pushed to the inlet and outlet through the spiral blade and pushed out of the inlet and outlet, and continuous discharge will be realized as the material is discharged. The function of output.

以上对本实用新型的一个实例进行了详细说明,但内容仅为本实用新型的较佳实施例,不能被认为用于限定本实用新型的实施范围。凡依本实用新型申请范围所作的均等变化与改进等,均应仍归属于本实用新型的专利涵盖范围之内。An example of the utility model has been described in detail above, but the content is only a preferred embodiment of the utility model, and cannot be considered as limiting the implementation scope of the utility model. All equal changes and improvements made according to the application scope of the utility model should still belong to the scope covered by the patent of the utility model.

Claims (10)

1.转筒式连续熏醅设备,包括卧式转筒结构、加热层、动力结构、支撑结构、搅拌结构,其特征在于所述搅拌结构设置在所述卧式转筒结构内,所述动力结构连接所述卧式转筒结构并提供动力,所述支撑结构设置在所述卧式转筒结构下支撑所述卧式转筒结构,所述卧式转筒结构内设置与外界连通的呼吸器管路,所述加热层设置在所述卧式转筒结构外,所述加热层采用集箱结构,所述加热层内设置进口集箱、加热水带和出口集箱,所述加热水带连通所述进口集箱和所述出口集箱,所述加热水带倾斜设置且向出水集箱倾斜,所述加热水带内通入加热介质。1. Drum-type continuous smoked unstrained spirits equipment, comprising a horizontal drum structure, a heating layer, a power structure, a support structure, and a stirring structure, characterized in that the stirring structure is arranged in the horizontal drum structure, and the power The structure is connected to the horizontal drum structure and provides power. The support structure is arranged under the horizontal drum structure to support the horizontal drum structure. The heating layer is arranged outside the horizontal drum structure, the heating layer adopts a header structure, the inlet header, the heating water belt and the outlet header are arranged in the heating layer, and the heating water The belt communicates with the inlet header and the outlet header, the heating water belt is inclined to the water outlet header, and the heating medium is passed into the heating water belt. 2.根据权利要求1所述的转筒式连续熏醅设备,其特征在于所述卧式转筒结构的两端设置左端面和右端面,所述左端面中心处设置进出料口,所述右端面中心处设置旋转接头;2. The drum-type continuous smoked fermented grains equipment according to claim 1, characterized in that the two ends of the horizontal drum structure are provided with a left end face and a right end face, the center of the left end face is provided with an inlet and outlet, and the A rotary joint is set at the center of the right end face; 所述进口集箱通过进蒸汽支管与进蒸汽总管连通,所述出口集箱与冷凝水排出管连接,所述进蒸汽总管和所述冷凝水排出管均与旋转接头连接,所述冷凝水排出管出所述旋转接头后接疏水阀。The inlet header is connected with the steam inlet main pipe through the steam inlet branch pipe, the outlet header is connected with the condensed water discharge pipe, the steam inlet main pipe and the condensed water discharge pipe are connected with the rotary joint, and the condensed water is discharged After the pipe comes out of the swivel joint, it is connected to the steam trap. 3.根据权利要求1所述的转筒式连续熏醅设备,其特征在于所述加热水带倾斜度为0.5~1%。3. The drum-type continuous smoked fermented grains equipment according to claim 1, characterized in that the inclination of the heating water belt is 0.5-1%. 4.根据权利要求1所述的转筒式连续熏醅设备,其特征在于所述支撑结构包括固定轴承座和调心滚轮座,所述固定轴承座固定在所述卧式转筒结构右端面上,所述调心滚轮座设置在所述卧式转筒结构左右两侧。4. The drum-type continuous smoked unstrained spirits equipment according to claim 1, characterized in that the supporting structure includes a fixed bearing seat and a self-aligning roller seat, and the fixed bearing seat is fixed on the right end surface of the horizontal drum structure Above, the self-aligning roller seat is arranged on the left and right sides of the horizontal drum structure. 5.根据权利要求1所述的转筒式连续熏醅设备,其特征在于所述加热层外层设置保温层。5. The drum-type continuous smoked fermented grains equipment according to claim 1, characterized in that the outer layer of the heating layer is provided with an insulating layer. 6.根据权利要求1或2所述的转筒式连续熏醅设备,其特征在于所述卧式转筒结构内的所述搅拌结构包括螺旋叶片和搅拌叶片,所述搅拌叶片均匀设置在所述卧式转筒结构的内壁上,所述螺旋叶片设置在所述卧式转筒结构内靠近进出料口处。6. The drum type continuous smoked fermented grains equipment according to claim 1 or 2, characterized in that the stirring structure in the horizontal drum structure includes a spiral blade and a stirring blade, and the stirring blade is evenly arranged on the On the inner wall of the horizontal drum structure, the helical blade is arranged in the horizontal drum structure near the material inlet and outlet. 7.根据权利要求2所述的转筒式连续熏醅设备,其特征在于所述左端面采用锥形封头结构,所述右端面采用碟形封头结构。7. The drum-type continuous smoked fermented grains equipment according to claim 2, characterized in that the left end surface adopts a cone-shaped head structure, and the right end surface adopts a dish-shaped head structure. 8.根据权利要求2所述的转筒式连续熏醅设备,其特征在于所述冷凝水排出管起始段设置截止阀。8. The drum-type continuous smoked fermented grains equipment according to claim 2, characterized in that a cut-off valve is set at the initial section of the condensed water discharge pipe. 9.根据权利要求1或3所述的转筒式连续熏醅设备,其特征在于所述加热水带的横截面为半圆形。9. The drum type continuous smoked fermented grains equipment according to claim 1 or 3, characterized in that the cross-section of the heating water belt is semicircular. 10.根据权利要求6所述的转筒式连续熏醅设备,其特征在于所述搅拌叶片轴向等距排列固定在所述卧式转筒结构的内壁上。10. The drum-type continuous smoked fermented grains equipment according to claim 6, characterized in that the stirring blades are arranged axially equidistantly and fixed on the inner wall of the horizontal drum structure.
CN201621409561.8U 2016-12-21 2016-12-21 Drum type continuous smoked grains equipment Active CN206521456U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621409561.8U CN206521456U (en) 2016-12-21 2016-12-21 Drum type continuous smoked grains equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621409561.8U CN206521456U (en) 2016-12-21 2016-12-21 Drum type continuous smoked grains equipment

Publications (1)

Publication Number Publication Date
CN206521456U true CN206521456U (en) 2017-09-26

Family

ID=59887756

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201621409561.8U Active CN206521456U (en) 2016-12-21 2016-12-21 Drum type continuous smoked grains equipment

Country Status (1)

Country Link
CN (1) CN206521456U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108165453A (en) * 2018-01-25 2018-06-15 河北工程大学 A kind of smoked vinegar fermented grain material process units
CN111793556A (en) * 2020-08-18 2020-10-20 山西水塔醋业股份有限公司 Horizontal vinegar culture fermentation tank
CN112011433A (en) * 2020-08-18 2020-12-01 山西水塔醋业股份有限公司 Horizontal fermented grain smoking tank and fermented grain smoking method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108165453A (en) * 2018-01-25 2018-06-15 河北工程大学 A kind of smoked vinegar fermented grain material process units
CN111793556A (en) * 2020-08-18 2020-10-20 山西水塔醋业股份有限公司 Horizontal vinegar culture fermentation tank
CN112011433A (en) * 2020-08-18 2020-12-01 山西水塔醋业股份有限公司 Horizontal fermented grain smoking tank and fermented grain smoking method

Similar Documents

Publication Publication Date Title
CN109055193B (en) Inclined drum type vacuum solid-state fermentation tank with built-in replaceable heating helical blades
CN110506945B (en) A kind of device for removing walnut inner skin and walnut kernel processing system
CN103509712B (en) A kind of device and technique possessing the continuous solid-state fermentation ethanol production of robot control system(RCS)
CN100558876C (en) Automatic feed-discharge closed solid-state fermenter and its fermentation process
CN206521456U (en) Drum type continuous smoked grains equipment
CN201837208U (en) Vacuum rake dryer for bentonite
CN207175915U (en) All-in-one is brewageed in mature vinegar intellectuality
CN105420017A (en) Fermented grain airing and yeast adding device and method for controlling pit entry temperature of yeast liquor fermentation fermented grains by virtue of device
CN108753609A (en) The adaptive equipment of integrated 3-phase dry type anaerobic fermentation and its production biogas method
CN108456633A (en) A kind of large arch dam organic waste sequence is into formula anaerobic ferment devices
CN106116707A (en) A kind of livestock manure fermented processing equipment
CN114315447A (en) A rapid fermentation device with controllable temperature and humidity
WO2017152476A1 (en) Large self-spinning interlaid heating and charging fermentor
CN201919595U (en) Grain dryer
CN206970434U (en) A kind of sludge multistage anaerobic fermentation vat
CN213984333U (en) High-efficient environmental protection drying-machine
CN210934902U (en) Sodium diacetate reactor
CN209669198U (en) Microorganism production and collection system
CN107651988A (en) A kind of organic fertilizer fermentation equipment
CN104745466A (en) Solid material fermentation device
CN204385188U (en) A kind of water-bath drum-type dry fermentation device
CN206467213U (en) A kind of fruit vinegar fermentation tank and fruit vinegar process units
CN204550595U (en) A kind of solid materials fermenting device
CN204555604U (en) Granular organic fertilizer grading drying device
CN114877638A (en) Steamer for preparing polyolefin by SPG (spray-steam-assisted gas) process

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
TR01 Transfer of patent right

Effective date of registration: 20190121

Address after: No. 172 Hongshan Road, Pudong New District, Shanghai, 200127

Patentee after: Shanghai Xiaorun Bioengineering Technology Service Co., Ltd.

Address before: 271000 No. 16 Nanguan Road, Taian City, Shandong Province

Patentee before: Prettech Machinery Making Co., Ltd.

TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20191205

Address after: 030600 Shanxi Jinzhong Shanxi demonstration zone Jinzhong Development Zone Huitong Industrial Park 12 Road

Patentee after: Shanxi Liangfen Vinegar Industry Co., Ltd.

Address before: No. 172 Hongshan Road, Pudong New District, Shanghai, 200127

Patentee before: Shanghai Xiaorun Bioengineering Technology Service Co., Ltd.

TR01 Transfer of patent right
CP01 Change in the name or title of a patent holder

Address after: 030600 Shanxi Jinzhong Shanxi demonstration zone Jinzhong Development Zone Huitong Industrial Park 12 Road

Patentee after: Shanxi Liangfen Jinlong fish vinegar Co., Ltd

Address before: 030600 Shanxi Jinzhong Shanxi demonstration zone Jinzhong Development Zone Huitong Industrial Park 12 Road

Patentee before: Shanxi Liangfen Vinegar Industry Co., Ltd.

CP01 Change in the name or title of a patent holder
CP03 Change of name, title or address

Address after: 030600 No. 12, Huitong Industrial Park, Jinzhong Development Zone, West demonstration zone, Jinzhong City, Shanxi Province

Patentee after: Shanxi Jinlongyu Liangfen vinegar industry Co.,Ltd.

Address before: 030600 Shanxi Jinzhong Shanxi demonstration zone Jinzhong Development Zone Huitong Industrial Park 12 Road

Patentee before: Shanxi Liangfen Jinlong fish vinegar Co.,Ltd.

CP03 Change of name, title or address