CN204848884U - Solid -state biological raw materials fermentation system of modularization - Google Patents

Solid -state biological raw materials fermentation system of modularization Download PDF

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Publication number
CN204848884U
CN204848884U CN201520472163.XU CN201520472163U CN204848884U CN 204848884 U CN204848884 U CN 204848884U CN 201520472163 U CN201520472163 U CN 201520472163U CN 204848884 U CN204848884 U CN 204848884U
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fermentation
unit
solid
door
raw material
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Chinese (zh)
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曹胜炎
刘汉明
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Henan Shuangcheng Biotechnology Co Ltd
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Henan Shuangcheng Biotechnology Co Ltd
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Abstract

The utility model discloses a solid -state biological raw materials fermentation system of modularization, include and mix unit and fermentation unit by raw material handling unit, the batching of industrial computer control, the fermentation unit is by forming at the scraper blade distributing device on top layer fermentation chamber upper portion, setting buffering play hopper and the ejection of compact scraper conveyor in bottom fermentation room lower part along transversely setting up multilayer fermentation chamber on the pylon, setting up from bottom to top, the box unit by the bottom plate for the upper shed box that turns over the plate structure with turn over board actuating mechanism and constitute, screw conveyer that the raw material handling unit links up by feed hopper, with the feed hopper discharge gate, the gas explosion machine that links up with the screw conveyer feed inlet are formed. The utility model discloses the modularization combination can be carried out to the fermentation unit according to production scale, product variety and the investment capacity to the advantage. Material top -down accomplishes fermentation and stirring by multilayer fermentation chamber intermittent type in proper order fermentation, gravity flow stirring, satisfied make, needs that the large -scale industry metaplasia of biological feed, bio -pharmaceuticals, bio -feritlizer fermentation was produced.

Description

Modular solid-state biological raw material fermentation system
Technical field
The utility model relates to biological raw material fermentation technical field, especially relates to the modular solid-state biological raw material fermentation system being suitable for suitability for industrialized production.
Background technology
Solid-state fermentation technology historical origin for a long time; but zymotechnique and fermentation equipment delayed, most employing is manually equipped with simple machine, and production process disconnects mutually; industrialization streamline can not be realized automatically produce, more can not adapt to current fermentation industry large-scale development needs.Traditional biological raw material solid-state fermentation process is (as biological organic fertilizer, biological protein feedstuff), general employing fermenting tank for fermentation, be about to artificial preparation, the artificial go-cart of material of mechanically mixing or diesel dumper fortune fill out and ferment in fermentation vat, certain interval of time artificial or tripper stirring in fermenting process, artificial detected temperatures is used, humidity and pH value in midway, adopts artificial or pushing device to proceed to next procedure after fermentation reaches requirement substantially.This fermenting tank for fermentation, floor space is large, and production environment is poor, and mechanical stirring exists dead angle, i.e. material fermentation non-uniform temperature, and fermenting process difficulty is controlled, and material fermentation quality is unstable, and labour intensity is large, consumes manpower many, and difficulty realizes large-scale industrial and produces.
Fermentation technique was through constantly development in the last few years, had occurred this new zymotechnique and an equipment, as vertical digester, and Horizontal revolving drum-type fermentor tank, Horizontal stirring formula fermentor tank, solid state fluidizing fermentation bed etc.Partial fermentation equipment have employed secondary ventilation in varying degrees, heats, is humidified and temperature-humidity detecting device, have employed PLC(programmable logic controller) controller control techniques, improve suitability and control techniques level, adapt to Small Scale Industry need of production to a certain extent.But also Shortcomings; stirring will consume larger power and temperature of charge lack of homogeneity; the residual difficult removing of material in proving room; limit output by volume little; manufacturing cost is higher relative to turnout with use cost, can not adapt to the biological fermentation need of production of annual output more than 5000 tons to several ten thousand tons, the mass-producing of hundreds of thousands of ton.Chinese patent application publication No.: CN101914432A openly establishes one " tower solid fermentation device "; but content disclosed in it is only a kind of thinking and does not provide enforceable technique means, the large-scale industrial that can not realize solid state fermentation according to the content of the disclosure is produced.
Summary of the invention
The utility model object is to provide a kind of modular solid-state biological raw material fermentation system, to realize the large-scale industrial automatic production of solid-state biological raw material fermentation.
For achieving the above object, the utility model takes following technical proposals:
Modular solid-state biological raw material fermentation system described in the utility model, comprises the material processing unit, batching mixed cell and the fermentation unit that are controlled by industrial computer; Described fermentation unit is made up of the multilayer fermentation room be transversely arranged on from bottom to top on pylon, the scraper plate distributor being arranged on described top layer proving room top, the buffering discharge bucket being arranged on bottom, sedimentary fermentation room and discharging scraper conveyor; Described scraper plate distributor opening for feed is connected with the second lift discharge port being vertically set on pylon side mutually by pendulum distributing device; Every layer of described proving room is by the horizontal arranged composition of the box unit that multiple structure is identical; Box unit in upper and lower adjacent layers proving room vertically superposes layout;
Described box unit is that the upper shed casing of reverse turning bed structure and turnover panel topworks form by base plate; The box bottom of described reverse turning bed structure is made up of at least two group lower turning type plate-turning doors, the described door-hinge two ends often organizing lower turning type plate-turning door are rotationally connected with the bearing body be fixed on the forward and backward side plate of upper shed casing respectively, are all provided with the Temperature Humidity Sensor detected for industrial computer in each upper shed casing; Described turnover panel topworks forms by being arranged on cylinder that upper shed cabinet front plate or back side panel external turret are controlled by industrial computer or hydro-cylinder, linkage assembly and being fixed on the connecting lever often organizing lower turning type plate-turning door door-hinge end; Described linkage assembly is made up of horizontally disposed first connecting rod, the second connecting rod be obliquely installed and swing arm, described swing arm is provided with the limit base for limiting cylinder or the hydrauliccylinder piston throw of lever; Described each connecting lever is all hinged with described first connecting rod, and first connecting rod is hinged by the piston rod of second connecting rod, swing arm and described cylinder or hydro-cylinder;
The side of pylon is provided with air intake passage and relative opposite side is provided with air exhaust passage, and the box unit being positioned at top layer following layer proving room is connected with described air intake passage, air exhaust passage respectively by pipeline; Described air intake passage is provided with air intake temp and humidity regulator, described air intake temp and humidity regulator is made up of the humidifier section be arranged in body and heat exchanging segment; Described humidifier section is made up of spaced multilayer cascade vertically, and described heat exchanging segment is made up of shell and tube heat exchanger; Humidifier section is connected with the tube side of described shell and tube heat exchanger, and the shell side of shell and tube heat exchanger is connected with low-temperature receiver with external heat source respectively by Electrocontrolled tee valve; The top of each cascade is connected with external water source by pipeline.
The described door-hinge often organizing lower turning type plate-turning door is become with the solid shaft head group being welded in described rectangular steel tube both ends by rectangular steel tube, described two solid spindle noses are rotationally connected with the corresponding bearing body be fixed on the forward and backward side plate of upper shed casing respectively, lower turning type plate-turning door is fixedly connected with rectangular steel tube by bolt, rectangular steel tube is fixed with guide duct vertically, and the gap that the tube wall of described guide duct offers 10mm ~ 40mm vertically penetrates material for importing air-flow.
The described door-hinge often organizing lower turning type plate-turning door is become with the solid shaft head group being welded in described rectangular steel tube two ends by rectangular steel tube, described two solid spindle noses are rotationally connected with the corresponding bearing body be fixed on the forward and backward side plate of upper shed casing respectively, and described lower turning type plate-turning door is fixedly connected with rectangular steel tube by bolt; To be positioned at above rectangular steel tube gap vertically and to be provided with the pressure reductor of " people " character form structure be made up of two swash plates, the angle between described two swash plates is less than 60 °, and the two ends of described pressure reductor are fixedly connected with the forward and backward side plate of described upper shed casing respectively.
The each box unit being arranged in top layer proving room is provided with the material-level measure sensor detected for industrial computer.
Described material processing unit is made up of cast hopper, the worm conveyor be connected with described cast hopper discharge port, the gas explosion machine that is connected with described helical feed machine inlet capable; The described gas explosion machine discharge port material of discharging is entered in cylinder in described batching mixed cell or Conical screen extension set by the first lift.
Described batching mixed cell comprises cylinder or Conical screen extension set, the material outlet that sieves of described cylinder or Conical screen extension set is connected with batch bin opening for feed by rotary distributor, and described batch bin discharge port is connected with mixing machine opening for feed by bin discharger, batching hopper; Described mixer discharge mouth is connected with described second lift opening for feed with transfer roller mutually by buffering bucket; Mixing machine inner chamber is connected with bacterium liquid adding set liquid outlet by pipeline.
Discharging scraper conveyor discharge port in described fermentation unit is connected with dry materials unit mutually by the 3rd lift.
The utility model advantage is to carry out modular combination according to industrial scale, range of product and the investment ability to the fermentation volume of fermentation unit.After material completes the cloth in each box unit of top layer proving room by scraper plate distributor, industrial computer sends instruction and opens lower turning type plate-turning door to the turnover panel topworks in each box unit, material is scattered after in each box unit corresponding to adjacent lower proving room by gravity, industrial computer sends instruction and closes lower turning type plate-turning door to the turnover panel topworks in each box unit, material scatter in process complete stirring operation, therefore there is not stirring non-uniform phenomenon, enter the material in the corresponding each box unit of lower floor's proving room, ferment in airtight environment, the temperature of fermentation, humidity is undertaken detecting and transferring data to industrial computer by Temperature Humidity Sensor, after the data detected compare with the fermentation parameter of setting by industrial computer, regulated by air intake passage and air exhaust passage, after reaching set(ting)value when fermenting, industrial computer sends after instruction opens the discharging of lower turning type plate-turning door to the turnover panel topworks in this layer of each box unit and closes, repeat said process successively afterwards, until the material completing fermentation cushions discharge bucket bottom pylon be transported to the output of discharging scraper conveyor.Material completes fermentation and stirring by multilayer fermentation room successively batch fermentation, the gravity stirring that flows from top to bottom, therefore meet brewage, biological fodder, bio-pharmaceuticals, the solid state fermentation such as bio-feritlizer the needs of large-scale industrial production.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the first structural representation of box unit described in the utility model.
Fig. 2 .1 is A portion structure for amplifying schematic diagram in Fig. 2.
Fig. 3 is the second structural representation of box unit described in the utility model.
Fig. 3 .1 is B portion structure for amplifying schematic diagram in Fig. 3.
Fig. 4 is the structural representation of air intake temp and humidity regulator described in the utility model.
Embodiment
As Figure 1-4, modular solid-state biological raw material fermentation system described in the utility model, comprises the material processing unit 2, batching mixed cell 3 and the fermentation unit 4 that are controlled by industrial computer 1; Described fermentation unit 4 is by the ten floor proving room be transversely arranged on from bottom to top on pylon and be arranged on the scraper plate distributor 5 on top layer proving room top and be arranged on the buffering discharge bucket 6 of bottom, sedimentary fermentation room and discharging scraper conveyor 7 forms; Scraper plate distributor 5 opening for feed is connected with the second chapelet 9 discharge port being vertically set on pylon side mutually by pendulum distributing device 8; Every layer of proving room is by the identical horizontal arranged composition of box unit 10 of eight structures; Box unit 10 in upper and lower adjacent layers proving room vertically superposes layout;
As shown in Fig. 2 and Fig. 2 .1, box unit 10 is that the upper shed casing of reverse turning bed structure and turnover panel topworks form by base plate, the box bottom of described reverse turning bed structure is made up of five groups of lower turning type plate-turning doors 11, the door-hinge often organizing lower turning type plate-turning door 11 forms by rectangular steel tube 12 and the solid spindle nose 13 being welded in rectangular steel tube 12 both ends, two solid spindle noses 13 respectively with corresponding be fixed on upper shed casing before, bearing body 14 on back side panel is rotationally connected, lower turning type plate-turning door 11 is fixedly connected with rectangular steel tube 12 by bolt, rectangular steel tube 12 is fixed with guide duct 15 vertically, the gap 16 that the tube wall of guide duct 15 offers 10mm ~ 40mm vertically penetrates material for importing air-flow, simultaneously, when lower turning type plate-turning door 11 upset discharging downwards, guide duct 15 upwards rotates for axle center with solid spindle nose 13, play stirring and promote discharging effect, the Temperature Humidity Sensor 17 detected for industrial computer 1 is all installed in each upper shed casing.Turnover panel topworks forms by being arranged on cylinder 18, linkage assembly that upper shed cabinet front plate external turret is controlled by industrial computer 1 and being fixedly connected on the often connecting lever 19 organized on lower turning type plate-turning door 11 solid spindle nose 13; Linkage assembly is made up of horizontally disposed first connecting rod 20, the second connecting rod 21 be obliquely installed and swing arm 22, swing arm 22 is provided with the limit base 23 for limiting cylinder 18 piston rod stroke; Each connecting lever 19 is all hinged with first connecting rod 20, and first connecting rod 20 is hinged with the piston rod of cylinder 18 by second connecting rod 21, swing arm 22; The upper shed cabinet front plate of box unit 10 is provided with observation window 24; The upper shed casing left and right side plate of every layer of proving room adjacent boxes unit 10 is all connected by bolt.
Box unit 10 also can take the structure as shown in Fig. 3 and 3.1, and the solid spindle nose 13 often organizing lower turning type plate-turning door 11 is identical with the structure shown in turnover panel topworks with Fig. 2 with Fig. 2 .1, no longer repeats; Its difference is provided with the pressure reductor 25 being made up of " people " character form structure two swash plates being positioned at above rectangular steel tube 12 gap vertically, angle a between two swash plates selects between 50-55 °, and the two ends of pressure reductor 25 are fixedly connected with the forward and backward side plate of upper shed casing respectively.
The side of pylon is provided with air intake passage 26 and relative opposite side is provided with air exhaust passage 27, and the box unit 10 being positioned at top layer proving room (the tenth layer of proving room) each layer proving room is below connected with air intake passage 26, air exhaust passage 27 with pipeline respectively by the motorized valve controlled by industrial computer 1; Air intake passage 26 is provided with air intake temp and humidity regulator 28; The material-level measure sensor controlled by industrial computer 1 is provided with in the upper shed casing of top layer proving room box unit 10.
As described in Figure 4, air intake temp and humidity regulator 28 is made up of the humidifier section be arranged in body and heat exchanging segment; Humidifier section is made up of spaced five layers of cascade 29 vertically, and heat exchanging segment is made up of shell and tube heat exchanger; Humidifier section is connected with the tube side 30 of shell and tube heat exchanger, and the shell side 31 of shell and tube heat exchanger is connected with low-temperature receiver with external heat source respectively by the Electrocontrolled tee valve 32 controlled by industrial computer 1; Each cascade 29 top is connected with external water source with the electrically-controlled valve 34 controlled by industrial computer 1 by pipeline 33.
As shown in Figure 1, material processing unit 2 is made up of cast hopper 35, the worm conveyor 36 be connected with cast hopper 35 discharge port, the gas explosion machine 37 that is connected with worm conveyor 36 opening for feed; The material that gas explosion machine 37 discharge port is discharged is entered in the barrel sieving machine 39 in batching mixed cell 3 by the first chapelet 38.
Batching mixed cell 3 comprises barrel sieving machine 39, and the material outlet that sieves of barrel sieving machine 39 is connected with batch bin 41 opening for feed by rotary distributor 40, and batch bin 41 discharge port is connected with mixing machine 43 opening for feed by bin discharger and batching hopper 42; Mixing machine 43 discharge opening is connected with the second chapelet 9 opening for feed in fermentation unit 4 with transfer roller 45 mutually by buffering bucket 44; Mixing machine 43 inner chamber is connected with bacterium liquid adding set 46 liquid outlet by pipeline.
Need dry material for after some fermentation, the material that discharging scraper conveyor 7 discharge port in fermentation unit 4 is discharged is sent in existing dry materials unit 48 by the 3rd chapelet 47 and is carried out drying treatment.
The utility model Feedstock treating is as follows with batching hybrid working principle:
As shown in Figure 1, solid feed, by manually dropping into from cast hopper 35, cast hopper 35 is provided with fence, to protect the personal security and prevent large, foreign material material (as sack, the rope made of hemp) from falling in machine of feeding intake; Cast hopper 35 is equipped with pulse dust collector 49, to improve the environment that feeds intake, prevents from feeding intake and produce dirt and externally fly upward; The raw material dropped into is transported in gas explosion machine 37 by worm conveyor 36, pulverize through gas explosion machine 37, after sterilising treatment, be delivered in barrel sieving machine 39 by the first chapelet 38 and carry out Screening Treatment, it is better that the employing of commute conglomeration raw material has the Conical screen breaing up function, also should add pipe magnetic separator deironing to the raw material containing metallic impurity; Raw material after screening enters batch bin 41 by rotary distributor 40 with the blanking of gravity mode.The quantity of batch bin 41 is determined according to joined bulk raw material kind, general a kind of raw material enters a batch bin 41, batch bin 41, built with upper and lower level detector, is reported to the police when raw material in storehouse installs to send in limited time and stops upstream equipment charging, under raw material in storehouse reaches, notifying charging in limited time; Each batch bin respectively carries a bin discharger for 41 times, industrial computer 1 often criticizes batching parameter according to setting in advance, start a bin discharger to the charging of batching hopper 42, batching hopper 42 dynamic weighing also shows, industrial computer 1 tracing detection, stop charging when reaching the formula set(ting)value of this kind of raw material, the bin discharger restarting another batch bin 41 enters another kind of raw material, completes blending process successively.After batching completes, industrial computer 1 send instruction give batching hopper 42 open hopper gate batching is discharged in mixing machine 43 mix, meanwhile, bacterium liquid by bacterium liquid adding set 46 by pipeline enter in mixing machine 43 participate in mixing; After every batch of batching mixes 3 ~ 6 minutes in mixing machine 43, mixing machine 43 discharge port is opened, and mixed material enters in the pendulum distributing device 8 in fermentation unit 4 through buffering bucket 44, transfer roller 45 and the second chapelet 9.
The utility model fermenting raw materials principle of work is as follows:
As shown in figs 2-4, the material entered in pendulum distributing device 8 passes through
The scraper plate distributor 5 of tower top is transported in the upper shed casing of the tenth layer of each box unit 10 of (top layer) proving room, detected by material-level measure sensor when material in each upper shed casing reaches the fabric thickness of setting and transfer data to industrial computer 1, industrial computer 1 sends instruction and stops upstream equipment charging, the turnover panel topworks simultaneously controlling the tenth layer of each box unit of proving room 10 opens each lower turning type plate-turning door 11, material scatters (now the lower turning type plate-turning door 11 of the 9th layer of each box unit 10 of proving room is in closing condition) in the upper shed casing of the 9th layer of each box unit of proving room 10 under gravity, material obtains stirring scattering in process.After the time of setting, lower turning type plate-turning door 11 is closed by the turnover panel topworks that industrial computer 1 controls the tenth layer of each box unit 10 of proving room, enters next round charging cloth.
Material ferments to the time of setting in the upper shed casing of the 9th layer of each box unit 10 of proving room, industrial computer 1 sends instruction, open the lower turning type plate-turning door 11 of the 9th layer of each box unit 10 of proving room, material scatters in the upper shed casing of the 8th layer of each box unit 10 of proving room under gravity, material scatter in process obtain second time stirring.After the time of setting, the lower turning type plate-turning door 11 that industrial computer 1 controls the 9th layer of each box unit 10 of proving room is closed, and enters next round charging.
8th layer of proving room, to the same 9th layer of proving room of working process of the first layer proving room, no longer repeats.
Enter the first layer proving room after the fermentation time of setting when material successively ferments, industrial computer 1 controls the lower turning type plate-turning door 11 opening each box unit 10, and material is dumped into discharging scraper conveyor 7 by buffering discharge bucket 6 discharge port and is delivered to next process.
The first layer proving room is all connected with air intake passage 26, air exhaust passage 27 with the air intake motorized valve 50 controlled by industrial computer 1, air draft motorized valve 51 by pipeline to the upper shed casing of the tenth layer of each box unit 10 of proving room.When material fermentation temperature in industrial computer 1 to detect certain layer of proving room (existing for third layer proving room) each box unit 10 upper shed casing by Temperature Humidity Sensor 17, when humidity departs from the fermentation value of setting, industrial computer 1 sends instruction and opens gas blower 52, vacuum fan 53, open the air intake motorized valve 50 towards second layer proving room each box unit 10 upper shed casing simultaneously, towards the air draft motorized valve 51 of third layer proving room each box unit 10 upper shed casing, the wind that gas blower 52 is carried is by air intake temp and humidity regulator 28, air intake passage 26 enters in second layer proving room each box unit 10 upper shed casing, and the crack between a door and its frame of lower turning type plate-turning door 11 in each box unit 10 of third layer proving room, the tube wall gap 16(of guide duct 15 is as shown in Fig. 2 .1), after penetrating the material in third layer proving room each box unit 10 upper shed casing, discharge from air exhaust passage 27.When the material of proving room 10 is in oxygen consumption yeast phase, ventilation oxygen supply can be carried out by above-mentioned steps appropriateness unlatching air intake motorized valve 50 and air draft motorized valve 51, in fermentation resting stage, can close or turn down air intake motorized valve 50 and air draft motorized valve 51.
The epidemic disaster of air-supply is regulated and is realized by the air intake temp and humidity regulator 28 of UNICOM on air intake passage 26.As shown in Figure 4, when needs send hot blast, industrial computer 1 controls Electrocontrolled tee valve 32 and opens and the valve of external heat source UNICOM, heats in the shell side 31 that external heat working medium enters shell and tube heat exchanger to the wind by tube side 30; Otherwise industrial computer 1 controls Electrocontrolled tee valve 32 and opens and the valve of external source UNICOM, in the shell side 31 that outside cold working medium enters shell and tube heat exchanger, the wind by tube side 30 is lowered the temperature.When needs humidification, industrial computer 1 controls electrically-controlled valve 34 and opens, and external water source enters humidifier section by pipeline 33, carries out humidification by cascade 29 to the wind through humidifier section, meanwhile, also obtains dust removal process by the wind of humidifier section.Certainly, also can carry out humidification and cooling process to air-supply simultaneously, or humidification and cooling process.

Claims (7)

1. a modular solid-state biological raw material fermentation system, comprises the material processing unit, batching mixed cell and the fermentation unit that are controlled by industrial computer; It is characterized in that: described fermentation unit is made up of the multilayer fermentation room be transversely arranged on from bottom to top on pylon, the scraper plate distributor being arranged on described top layer proving room top, the buffering discharge bucket being arranged on bottom, sedimentary fermentation room and discharging scraper conveyor; Described scraper plate distributor opening for feed is connected with the second lift discharge port being vertically set on pylon side mutually by pendulum distributing device; Every layer of described proving room is by the horizontal arranged composition of the box unit that multiple structure is identical; Box unit in upper and lower adjacent layers proving room vertically superposes layout;
Described box unit is that the upper shed casing of reverse turning bed structure and turnover panel topworks form by base plate; The box bottom of described reverse turning bed structure is made up of at least two group lower turning type plate-turning doors, the described door-hinge two ends often organizing lower turning type plate-turning door are rotationally connected with the bearing body be fixed on the forward and backward side plate of upper shed casing respectively, are all provided with the Temperature Humidity Sensor detected for industrial computer in each upper shed casing; Described turnover panel topworks forms by being arranged on cylinder that upper shed cabinet front plate or back side panel external turret are controlled by industrial computer or hydro-cylinder, linkage assembly and being fixed on the connecting lever often organizing lower turning type plate-turning door door-hinge end; Described linkage assembly is made up of horizontally disposed first connecting rod, the second connecting rod be obliquely installed and swing arm, described swing arm is provided with the limit base for limiting cylinder or the hydrauliccylinder piston throw of lever; Described each connecting lever is all hinged with described first connecting rod, and first connecting rod is hinged by the piston rod of second connecting rod, swing arm and described cylinder or hydro-cylinder;
The side of pylon is provided with air intake passage and relative opposite side is provided with air exhaust passage, and the box unit being positioned at top layer following layer proving room is connected with described air intake passage, air exhaust passage respectively by pipeline; Described air intake passage is provided with air intake temp and humidity regulator, described air intake temp and humidity regulator is made up of the humidifier section be arranged in body and heat exchanging segment; Described humidifier section is made up of spaced multilayer cascade vertically, and described heat exchanging segment is made up of shell and tube heat exchanger; Humidifier section is connected with the tube side of described shell and tube heat exchanger, and the shell side of shell and tube heat exchanger is connected with low-temperature receiver with external heat source respectively by Electrocontrolled tee valve; The top of each cascade is connected with external water source by pipeline.
2. modular solid-state biological raw material fermentation system according to claim 1, it is characterized in that: the described door-hinge often organizing lower turning type plate-turning door is become with the solid shaft head group being welded in described rectangular steel tube both ends by rectangular steel tube, described two solid spindle noses are rotationally connected with the corresponding bearing body be fixed on the forward and backward side plate of upper shed casing respectively, lower turning type plate-turning door is fixedly connected with rectangular steel tube by bolt, rectangular steel tube is fixed with guide duct vertically, and the gap that the tube wall of described guide duct offers 10mm ~ 40mm vertically penetrates material for importing air-flow.
3. modular solid-state biological raw material fermentation system according to claim 1, it is characterized in that: the described door-hinge often organizing lower turning type plate-turning door is become with the solid shaft head group being welded in described rectangular steel tube two ends by rectangular steel tube, described two solid spindle noses are rotationally connected with the corresponding bearing body be fixed on the forward and backward side plate of upper shed casing respectively, and described lower turning type plate-turning door is fixedly connected with rectangular steel tube by bolt; To be positioned at above rectangular steel tube gap vertically and to be provided with the pressure reductor of " people " character form structure be made up of two swash plates, the angle between described two swash plates is less than 60 °, and the two ends of described pressure reductor are fixedly connected with the forward and backward side plate of described upper shed casing respectively.
4. the modular solid-state biological raw material fermentation system according to claim 1,2 or 3, is characterized in that: each box unit being arranged in top layer proving room is provided with the material-level measure sensor detected for industrial computer.
5. the modular solid-state biological raw material fermentation system according to claim 1,2 or 3, is characterized in that: described material processing unit is made up of cast hopper, the worm conveyor be connected with described cast hopper discharge port, the gas explosion machine that is connected with described helical feed machine inlet capable; The described gas explosion machine discharge port material of discharging is entered in cylinder in described batching mixed cell or Conical screen extension set by the first lift.
6. the modular solid-state biological raw material fermentation system according to claim 1,2 or 3, it is characterized in that: described batching mixed cell comprises cylinder or Conical screen extension set, the material outlet that sieves of described cylinder or Conical screen extension set is connected with batch bin opening for feed by rotary distributor, and described batch bin discharge port is connected with mixing machine opening for feed by bin discharger, batching hopper; Described mixer discharge mouth is connected with described second lift opening for feed with transfer roller mutually by buffering bucket; Mixing machine inner chamber is connected with bacterium liquid adding set liquid outlet by pipeline.
7. the modular solid-state biological raw material fermentation system according to claim 1,2 or 3, is characterized in that: the discharging scraper conveyor discharge port in described fermentation unit is connected with dry materials unit mutually by the 3rd lift.
CN201520472163.XU 2015-06-30 2015-06-30 Solid -state biological raw materials fermentation system of modularization Expired - Fee Related CN204848884U (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104962469A (en) * 2015-06-30 2015-10-07 河南双成生物科技有限公司 Modularized solid biological raw material fermenting system
CN106418616A (en) * 2016-10-12 2017-02-22 武汉贵言机械制造有限公司 Multifunctional efficient feed fermentation production process equipment

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104962469A (en) * 2015-06-30 2015-10-07 河南双成生物科技有限公司 Modularized solid biological raw material fermenting system
CN106418616A (en) * 2016-10-12 2017-02-22 武汉贵言机械制造有限公司 Multifunctional efficient feed fermentation production process equipment

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