CN109609262A - A kind of wet dregs of rice evapo-separated machine - Google Patents
A kind of wet dregs of rice evapo-separated machine Download PDFInfo
- Publication number
- CN109609262A CN109609262A CN201811528704.0A CN201811528704A CN109609262A CN 109609262 A CN109609262 A CN 109609262A CN 201811528704 A CN201811528704 A CN 201811528704A CN 109609262 A CN109609262 A CN 109609262A
- Authority
- CN
- China
- Prior art keywords
- steam
- delamination
- rice
- channel
- dregs
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 235000007164 Oryza sativa Nutrition 0.000 title claims abstract description 128
- 235000009566 rice Nutrition 0.000 title claims abstract description 128
- 240000007594 Oryza sativa Species 0.000 title 1
- 241000209094 Oryza Species 0.000 claims abstract description 127
- 230000032798 delamination Effects 0.000 claims abstract description 115
- 238000010025 steaming Methods 0.000 claims abstract description 59
- 239000002904 solvent Substances 0.000 claims abstract description 49
- 238000010438 heat treatment Methods 0.000 claims abstract description 33
- 238000001035 drying Methods 0.000 claims abstract description 13
- 238000001816 cooling Methods 0.000 claims abstract description 5
- 238000000605 extraction Methods 0.000 claims abstract description 5
- 238000000034 method Methods 0.000 claims description 34
- 239000011120 plywood Substances 0.000 claims description 27
- 238000003756 stirring Methods 0.000 claims description 26
- 230000008569 process Effects 0.000 claims description 17
- 238000010079 rubber tapping Methods 0.000 claims description 13
- 238000007599 discharging Methods 0.000 claims description 12
- 238000009827 uniform distribution Methods 0.000 claims description 6
- 230000007246 mechanism Effects 0.000 claims description 4
- 238000013517 stratification Methods 0.000 claims 1
- 239000000463 material Substances 0.000 abstract description 28
- 230000000903 blocking effect Effects 0.000 abstract description 8
- 238000012423 maintenance Methods 0.000 abstract description 5
- 238000002156 mixing Methods 0.000 abstract description 5
- 239000010410 layer Substances 0.000 description 50
- 238000001556 precipitation Methods 0.000 description 36
- 230000000694 effects Effects 0.000 description 21
- 239000007921 spray Substances 0.000 description 11
- 230000008901 benefit Effects 0.000 description 5
- 235000018102 proteins Nutrition 0.000 description 5
- 108090000623 proteins and genes Proteins 0.000 description 5
- 102000004169 proteins and genes Human genes 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000003921 oil Substances 0.000 description 4
- 235000019198 oils Nutrition 0.000 description 4
- 230000000149 penetrating effect Effects 0.000 description 4
- 239000012071 phase Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 230000009471 action Effects 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 238000004925 denaturation Methods 0.000 description 3
- 230000036425 denaturation Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 238000007789 sealing Methods 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 238000005507 spraying Methods 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 235000004458 antinutrient Nutrition 0.000 description 2
- 235000013339 cereals Nutrition 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 239000003638 chemical reducing agent Substances 0.000 description 2
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 238000007701 flash-distillation Methods 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 238000002386 leaching Methods 0.000 description 2
- 230000001473 noxious effect Effects 0.000 description 2
- 238000012946 outsourcing Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 238000012827 research and development Methods 0.000 description 2
- 239000013557 residual solvent Substances 0.000 description 2
- 239000002356 single layer Substances 0.000 description 2
- 235000015112 vegetable and seed oil Nutrition 0.000 description 2
- 239000008158 vegetable oil Substances 0.000 description 2
- 108010082495 Dietary Plant Proteins Proteins 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 108010064851 Plant Proteins Proteins 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- 230000000433 anti-nutritional effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000007791 dehumidification Methods 0.000 description 1
- 238000004807 desolvation Methods 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 238000001784 detoxification Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000686 essence Substances 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000008246 gaseous mixture Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000010030 laminating Methods 0.000 description 1
- 235000012054 meals Nutrition 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 235000008935 nutritious Nutrition 0.000 description 1
- 230000000050 nutritive effect Effects 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 235000021118 plant-derived protein Nutrition 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000013022 venting Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B1/00—Production of fats or fatty oils from raw materials
- C11B1/10—Production of fats or fatty oils from raw materials by extracting
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Drying Of Solid Materials (AREA)
- Commercial Cooking Devices (AREA)
Abstract
The invention discloses a kind of wet dregs of rice evapo-separated machines comprising rack；Shell；Housing cavity is separated into the pre- delamination being arranged from top to bottom, mixed delamination, the distance member for steaming delamination；Agitating device；Steam heater；The cavity of shell is divided into the separator disc of baking zone and cold wind layer setting up and down below steaming delamination；Constitute the chassis at cold wind layer bottom；Respectively by gas in baking zone and cold wind layer or the first and second exhausting system of dregs of rice bits extraction；The air-cooled component of cold wind is provided into cold wind layer.One aspect of the present invention carries out indirect heating to the dregs of rice material positioned at every layer indirectly by steam, so that the solvent in the dregs of rice is deviate from, and is discharged with thermogenetic gas mixing is added from mixed gas outlet, while passing through the drying and cooling of bottom, directly draws off the finished product dregs of rice；The consumption of another aspect steam and dosage can be good at controlling, while the contact surface heated is big, and reduce the blocking probability of steam passage holes, and then reduce the workload of maintenance.
Description
Technical field
The present invention relates to a kind of wet dregs of rice evapo-separated machines.
Background technique
In oil extraction oil factory, the dregs of rice through draining naturally come out from infuser, generally all the solvent containing 25%-35% and
A certain amount of moisture.The content of solvent in the dregs of rice, containing molten referred to as in the dregs of rice, and the dregs of rice containing solvent and moisture are referred to as the wet dregs of rice.It will be molten
The process that agent is removed from the wet dregs of rice is known as wet dregs of rice precipitation on oil prodution industry.The main method of solvent removal is to steam to take off in the wet dregs of rice,
The solvent of the wet dregs of rice must all be evaporated, be reused after condensing recovery, economically rationally could could maintain production, will
Solvent contained in the wet dregs of rice reduces as far as possible, the height to oil extraction plant management and technical level be it is marginal, because of the dregs of rice
In containing the molten low reduction for meaning that solvent loss, it is safer in the storage and transportational process of the dregs of rice.For setting for wet dregs of rice precipitation
Standby is evapo-separated machine, has the double action that solvent steams the drying of de- and moisture concurrently.And it sloughs solvent and is reduced to water content therein
The dregs of rice of safe moisture, the then referred to as dry dregs of rice.Wet dregs of rice precipitation technique, according to the different and different of dry dregs of rice purposes.Usually it is made for feed
The dregs of rice, to destroy animal antinutriment, antinutritional factor therein, often using the precipitation technique under wet heat condition, i.e., conventional precipitation technique；And
The precipitation technique under lower temperature then can be used for the denaturation for preventing wherein protein as the dregs of rice for extracting protein product raw material,
That is low temperature desolventizing technique.The purpose of wet dregs of rice precipitation is that, according to the requirement to the dregs of rice, is removed fully and completely as far as possible
Remaining solvent in the wet dregs of rice, and the moisture of the dregs of rice is adjusted accordingly, so that the quality of the dregs of rice reaches the set quota.And it removes
The complexity of residual solvent is related with existence of the solvent in the dregs of rice in the wet dregs of rice.
Removing the common method of solvent in the wet dregs of rice is so that the solvent in the wet dregs of rice is obtained thermal energy and is vaporized by means of heating, from
And it is separated with the dregs of rice.It is this to be known as solid in chemical industry from the operation for removing hygroscopic water (solvent or moisture) in solid material by means of thermal energy
Drying, and the steaming for being then known as the wet dregs of rice in vegetable oil mill is de-, but solvent steams de- process in the wet dregs of rice and the difference of drying process exists
In: drying is just to finish when reaching certain material structure moisture, and steaming de- purpose is sufficiently to remove to the maximum extent
Solvent.It is steamed in de- operation in the wet dregs of rice, solvent is that surface is diffused into inside the wet dregs of rice, then re-vaporizes and is transferred in gas phase.Institute
It is the mass transport process that a solvent is transferred to gas phase from solid phase on the process nature taken off with the steaming of the wet dregs of rice.
The precipitation of the wet dregs of rice is that solvent steams de- process and is made of two stages with drying process similarity: constant speed is evaporated
It is evaporated with reduction of speed.When precipitation starts, solvent is evaporated from dregs of rice grain surface, and in this stage Shen, main removal is in non-knot with the dregs of rice
The solvent of conjunction state.Thus separation is easier, this stage is the first stage of precipitation --- constant rate period；And work as evaporating surface
After going deep into inside particles, mainly inside particles and the dregs of rice are in the separation of the solvent of bonding state, therefore carrying out for this stage is ratio
More difficult.This is the second stage of precipitation --- falling-rate period.In order to strengthen precipitation effect, answered in wet dregs of rice desolvation process
So that dregs of rice grain is in state of ceaselessly stirring, and improves rate of heat transfer as far as possible.As suitably reduced solvent vapour in surface of material again
Partial pressure, then be more advantageous to the removal of solvent in the dregs of rice.Therefore current wet dregs of rice precipitation technique, generallys use stirring and open steam
It is used in combination with indirect steam, or even reaches comparatively ideal precipitation effect with means such as vacuum.In order to guarantee to the maximum extent sufficiently
Steam desolventizing, it is necessary to improve the temperature for steaming de- process, but cause high temperature action that will cause protein when moisture in removing the dregs of rice
Excessive denaturation so that nutritious amino acid in conjunction with other substances in the dregs of rice, can thus make the feed value of the dregs of rice
Declined, thus reduce the quantity of the protein of effective nutritive value in the dregs of rice, it is therefore necessary to during guaranteeing that steaming is de- as possible
Protein is kept not to be denaturalized excessively to the maximum extent.
Modern steaming desorption method can be divided into following form: (1), steaming of the solvent in stirring layer it is de-；(2), the wet dregs of rice are in portion
Divide the steaming of part stirring thing material under suspended state de-；(3), steaming of the wet dregs of rice under suspended state is de-.Wherein, (1) and (2) class
Desolventizing method belongs to conventional precipitation technique, and the dregs of rice of feed are used as in production；And (3) class desolventizing method belongs to low temperature desolventizing technique,
The raw material of food vegetable protein is made in production.The wet dregs of rice desolventizing equipment of this patent is to belong to (1) class desolventizing method.
And be directed to the steaming of (1), solvent in stirring layer and take off, dehumidification is mainly steamed in laminar evapo-separated machine (vertical evapo-separated machine)
Solvent contained by the dregs of rice.The advantages of vertical evapo-separated machine has: precipitation effect is good, and the quality of product is easy to control；On each stage
It is adjustable the process of humid heat treatment, guarantees to obtain the dregs of rice in certain temperature and moisture；The wet dregs of rice are carried out in vertical evapo-separated machine molten
Agent, which is steamed, to be taken off, de- to the steaming of solvent more more effective and more abundant than in horizontal evapo-separated machine；Leaching meal obtains in evapo-separated machine
Hyther more evenly, can generate in dregs of rice layer can be passivated acting on from steaming for noxious material and anti-nutrient substance.The country is adopted at present
Vertical evapo-separated machine mainly has high bed desolventizer toaster, DTDC evapo-separated machine etc., and vertical evapo-separated machine is mainly by pre- delamination, air-permeable layer
(i.e. mixed delamination) steams delamination, hot wind layer, cold wind layer composition, is collection precipitation and drying, is cooled in integrated evapo-separated machine, pre- delamination
With air-permeable layer using solvent in the indirect steam heating evaporation dregs of rice, air-permeable layer also utilizes the gaseous mixture for being risen by steaming delamination and penetrating the bed of material
Body removes solvent by directly contacting the material dregs of rice, steams delamination and is directly contacted with the material dregs of rice using direct steam to remove the molten of remaining
The solvent of agent, these remainings cannot be stripped of by indirect heating to evaporate, primary disadvantage is that: power consumption is big, steam is used
Amount is big.
(2), the steaming of wet dregs of rice stirring thing material in part under partial suspended state is de-, and the de- dregs of rice are steamed mainly in horizontal evapo-separated machine
Contained solvent.The advantages of horizontal evapo-separated machine is: power consumption is few, easy to operate.The disadvantage is that: consumption steel are more, shaft end seal
Performance is poor, and the dregs of rice end of entrained with is more in mixed vapour；The ability for being passivated noxious material and anti-nutrient substance is weaker；With vertical type steaming
Off line is compared, all poor in terms of precipitation baking and detoxification effect.
(3), steaming of the wet dregs of rice under suspended state is de-, mainly in the flash distillation desolventizing equipment of low temperature desolventizing technique.Flash distillation is de-
The advantages of molten evapo-separated machine, is: because to the time of wet dregs of rice heat effect very short (generally 2 seconds), therefore albumen in the low denaturation dregs of rice after precipitation
Qualitative change is seldom, is the raw material for producing various food plant protein products.The shortcomings that flashing precipitation evapo-separated machine is: after precipitation,
It cannot be guaranteed that fully removing solvent in the dregs of rice, and still containing the residual solvent (2%~5%) for having more than permission limit in the dregs of rice, it is necessary to
It further processes under vacuum or with superheated steam.
It is energy-saving to be with advances in technology with the development of social economy, and the environmental protection and the pressure of resource that face
One important trend of the research and development of vegetable oil processing technology and equipment, the R&D direction for leaching wet dregs of rice precipitation are how to reduce steaming
How vapour consumption improves the economic and technical norms etc. of equipment production, is the main path for reaching energy-saving this purpose.
Above-mentioned wet dregs of rice precipitation technique and the technical problem underlying of vertical evapo-separated machine are:
(1), high layered material causes power consumption is big, lacks control to indirect steam and direct steam to cause steam consumption big, especially
It is to lack control to direct steam.
(2), air-permeable layer indirect heating scarce capacity, only several are layered in the angle bar at the bottom plate back side logical steam, are heated
Area is small, reduces precipitation effect.
(3), steam delamination bottom plate spray direct steam mode carry out solvent steam it is de-, have on bottom plate thousands of diameters about 1.5~
The shortcomings that direct steam spray orifice of 2.5mm, this mode, is obvious, is difficult to control spray vapour amount, and such as spray vapour amount is excessive, then causes
The waste of direct steam and gas phase temperature it is excessively high, the valve of direct steam air intake must be turned down, then sprayed in this case
Vapour pressure at hole reduces, and is easy blocking spray orifice, if spray vapour amount is inadequate, the precipitation effect of the dregs of rice is bad.Also, jetted hole itself
It is easy for blocking, it is often necessary to which a tiny iron leading in turn one by one, maintenance for spray orifice is taken in artificial dredging
Workload it is very big.
Summary of the invention
It is de- the technical problem to be solved by the present invention is to overcome the deficiencies of the prior art and provide a kind of improved wet dregs of rice steaming
Machine.
In order to solve the above technical problems, the de- system of the steaming of the application first passes through pre- delamination, mixed delamination, the setting for steaming delamination,
Indirect heating is carried out to the dregs of rice material positioned at every layer indirectly by steam, so that the solvent in the dregs of rice is deviate from, then, in conjunction with steaming delamination
Contact of the direct steam with the dregs of rice, and add thermogenetic gas and solvent to arrange together from the mixed gas outlet at the top of pre- delamination the dregs of rice
Out, process is taken off with the steaming for completing the dregs of rice；Then the dregs of rice are dried and are cooled down by the baking zone and cold wind layer of bottom, finally become
The finished product dregs of rice that can directly store, pack or sell are drawn off；Indirect heating steam and to directly heat between steam be not mutual simultaneously
Logical, therefore, the consumption of steam and dosage can be good at controlling, while also reduce the blocking probability of steam passage holes, and then subtract
The workload of small maintenance.
Specifically, the present invention adopts the following technical scheme that:
A kind of wet dregs of rice evapo-separated machine comprising:
Rack；
Shell, with feeding-passage, tapping channel and mixed-gas channel, wherein the feeding-passage and the mixed gas
Channel is located at the opposite sides of case top, and the tapping channel is located at the bottom of the shell；
Distance member, be horizontally set with the enclosure interior and the housing cavity is separated into the pre- delamination being arranged from top to bottom,
Delamination is steamed in mixed delamination；
Agitating device；
Steam heater,
Wherein space disc component respectively constitutes pre- delamination, mixed delamination and the layer bottom for steaming delamination, and include top plate, lower plywood,
Multiple stay bolt pipes and discharge channel between top plate and lower plywood, wherein stay bolt pipe upper end is fixed on top plate
Bottom, lower end from lower plywood stretch out, between top plate, lower plywood, stay bolt pipe, discharge channel and corresponding place's inner walls
Form indirect steam heating channel；
Top plate region positioned at space disc component connection corresponding to stay bolt pipe of mixed delamination is provided with steam passage holes；
Space disc component positioned at pre- delamination is equipped with coaming plate on the periphery of top plate and lower plywood, wherein shape between coaming plate and shell
At the airflow channel being connected with mixed-gas channel, top plate, lower plywood, stay bolt pipe, discharge channel and coaming plate constitute pre-
Hot indirect steam heating channel；
Discharge channel includes the feeding port being formed on top plate and lower plywood and feed opening, is used for feeding port and feed opening phase
The communicating pipe of connection, wherein tapping channel is connected with discharge channel, and discharge valve is equipped on the channel being connected；
Steam heater includes feeding heating to each preheating indirect steam heating channel and indirect steam heating channel respectively
First steam supply unit of steam circumferentially steams the second steam supply unit that steam is passed directly into delamination from outside shell,
In the airflow channel that is formed from the second supplied steam of steam supply unit from steaming delamination to mixed delamination, again to pre- delamination and shell
Flowing, and be discharged from mixed-gas channel；
Wet dregs of rice evapo-separated machine further includes being located to steam that the cavity of shell is divided into baking zone and cold wind layer setting up and down below delamination
Separator disc, the chassis for constituting cold wind layer bottom, the first exhausting system for respectively extracting gas in baking zone and cold wind layer or dregs of rice bits out
The air-cooled component that cold wind makes the dregs of rice cooling is provided with the second exhausting system and into cold wind layer, wherein on separator disc and chassis
It is respectively equipped with the bin gate that can be automatically opened or be closed, and separator disc and the hollow setting of inside chassis, steam heater include
For to the third steam supply unit for being passed through steam inside separator disc and carrying out to the dregs of rice on separator disc contact drying；Air-cooled component
Cold wind is passed through chassis cavity and enters cold wind layer, the bin gate on chassis is connected with tapping channel.
Preferably, top plate and lower plywood are arranged in parallel, stay bolt pipe centered on the center of rotation of agitating device and around
The circumferential direction and radially uniform distribution of top plate and lower plywood.The caliber of stay bolt pipe is 250~350mm.
Further, steam passage holes are centered on the center of stay bolt pipe and around stay bolt pipe circumferential direction and radially uniform distribution.
The aperture of steam passage holes is 20 ~ 30mm.
Specifically, being located at pre- delamination, mixed delamination and three discharge channels steamed in delamination mutually staggers setting.It prevents
Dregs of rice material directly falls steaming delamination without overmulling delamination,
A specific implementation according to the present invention and preferred aspect, separator disc include upper plate and lower plate and blanking channel,
Wherein blanking channel, upper plate and lower plate and corresponding position inner walls constitute drying channel, and bin gate is arranged in blanking channel
On.
A specific implementation according to the present invention and preferred aspect, chassis include that upper plate and lower plate and discharge are logical
Road, wherein discharging channel, upper plate and lower plate and corresponding position inner walls constitute air-cooled channel, and bin gate is arranged in discharge
On channel, air holes is offered on upper plate, the wind of hull outside enters air-cooled layer from air holes by inlet air cold passage.
Preferably, the first steam supply unit includes entering from the steam that hull outside is connected with indirect steam heating channel
Mouth, be connected steam pipework and steam supply positioned at the condensation-water drain of steam inlet opposite side and with steam inlet；The
Three steam supply units and the first steam supply unit structure are identical, and steam inlet is connected with drying channel.
Second steam supply unit include the steam pipe coil for steaming delamination is set, protrude into from the hull outside and
The connecting tube and steam supply being connected with the steam pipe coil, wherein the bottom of the steam pipe coil is sprayed equipped with steam
Pipe, the steam to raising up after the steaming delamination flows, transport upwards by the stay bolt pipe of process and the steam passage holes
After moving and will add thermogenetic gas and solvent to mix, it is discharged from the mixed-gas channel.
Preferably, the center of steam pipe coil is overlapped with the rotary centerline of agitating device.
Another specific implementation according to the present invention and preferred aspect, steam jet have multiple, and are divided into three groups, one group hangs down
Directly downward, one group inclined towards the steaming delamination center, and one group inclined towards the shell corresponding to the steaming delamination
Inner wall.
In this example, successively interval setting between three groups, so, the direct steam of penetrating is when steaming delamination, energy and object
Material comes into full contact with, and the utilization of steam is more abundant, therefore precipitation effect is more satisfactory, while after the completion of steaming de-, the steaming to raise up
Vapour will steam the gas in delamination and solvent mixes merga pass steam channel, upward dispatch, and successively and in mixed delamination and pre- delamination
Gas and solvent mixing, are finally discharged from the mixed-gas channel of case top.
In addition, steam pipe coil and connecting tube form one group of steam provisioning component, the second steam supply unit includes at least two
Group steam provisioning component, and steam provisioning component is evenly spaced on along the short transverse for steaming delamination, steam supply and every
Group steam provisioning component is connected, and the steam jet relative dislocation for being located at upper and lower two steam pipe coil bottoms is arranged.Such one
Come, the precipitation effect of dregs of rice material can be increased substantially.
Preferably, agitating device includes the agitating shaft for extending and being located at middle part along body height direction；It is located at pre-
Delamination, steams the stirring blade in delamination, baking zone and cold wind layer and being fixed on agitating shaft at mixed delamination；And driving agitating shaft
Around the driving mechanism of self-axis line rotation.
In this example, agitating shaft is connected by shaft coupling and speed reducer, then uses motor driven, while the bottom of shell is arranged in
Portion.
Preferably, the stirring blade being located in pre- delamination, mixed delamination, steaming delamination, baking zone and cold wind layer forms leaf
Piece component (also referred to as stirring knife) can be one or more sets, while every set blade assembly (can be divided into both arms stirring knife and single armed stirring knife)
Position is also different in respective layer, can be specifically configured according to actual needs.
As for the effect of stirring knife, that is, for stirring loose metal layer, prevent direct steam short-circuit, to improve precipitation effect, and
Keep blanking uniform.
Then, discharge valve, during discharging, by airlock, (the direct outsourcing of applicant, principle is similar to shape
At sealing gas curtain) control, blanking is not only just controlled, but also play sealing process, can completely cut off and steam delamination with possible between following baking zone
Gas leakage, avoid steam delamination there is solvent gas to be leaked to baking zone.
Due to the implementation of above technical scheme, the invention has the following advantages over the prior art:
One aspect of the present invention carries out indirect heating to the dregs of rice material positioned at every layer indirectly by steam, so that the solvent in the dregs of rice is deviate from,
Then, in conjunction with contact of the direct steam with the dregs of rice for steaming delamination, further by solvent deviate from and with add thermogenetic gas mixing
It is discharged from mixed gas outlet, while the dregs of rice is dried and is cooled down by the baking zone of bottom and cold wind layer, finally becoming can
It is drawn off with the finished product dregs of rice for directly storing, packing or sell；It another aspect indirect heating steam and directly heats between steam and is not
Intercommunication, therefore, the consumption of steam and dosage can be good at controlling, while the contact surface heated is big, and reduce steam
The blocking probability of through-hole, and then reduce the workload of maintenance.
Detailed description of the invention
The present invention will be further described in detail with specific embodiment with reference to the accompanying drawing.
Fig. 1 is the schematic front view of wet dregs of rice evapo-separated machine of the invention；
Fig. 2 is the schematic top plan view of distance member in Fig. 1；
Fig. 3 is the schematic cross-sectional view (main view direction) in Fig. 2 at a certain stay bolt pipe；
Fig. 4 is the schematic cross-sectional view (main view direction) in Fig. 2 at discharge channel；
Fig. 5 is the schematic structural cross-sectional view (main view direction) of separator disc in Fig. 1；
Fig. 6 is the schematic structural cross-sectional view (main view direction) on chassis in Fig. 1；
Wherein: G, rack；1, shell；1a, feeding-passage；1b, tapping channel；1c, mixed-gas channel；A, pre- delamination；B, it mixes
Delamination；C, delamination is steamed；2, distance member；20, top plate；F, steam passage holes；21, lower plywood；22, stay bolt pipe；23, discharging is logical
Road；23a, feeding port；23b, feed opening；23c, communicating pipe；24, coaming plate；A1, airflow channel；A, indirect steam heating channel；
A1, preheating indirect steam heating channel；3, agitating device；30, agitating shaft；31, stirring blade；32, driving mechanism；C, blade group
Part (stirring knife)；4, steam heater；41, the first steam supply unit；410, steam inlet；411, condensation-water drain；42,
Two steam supply units；420, steam pipe coil；G, steam jet；421, connecting tube；B, steam provisioning component；43, third steam
Supply unit；5, separator disc；50, upper plate；51, lower plate；52, blanking channel；D, drying channel；6, chassis；60, upper bottom
Plate；60a, stomata；61, lower plate；62, discharging channel；M, bin gate；E, air-cooled channel；7, the first exhausting system；8, the second exhausting
System；9, air-cooled component；F, discharge valve.
Specific embodiment
Referring to Fig. 1, according to the wet dregs of rice evapo-separated machine of the present embodiment comprising rack G, there is feeding-passage 1a, tapping channel
The shell 1 of 1b and mixed-gas channel 1c；The inside of shell 1 is set and inner cavity is separated into the pre- delamination a being arranged from top to bottom,
Mixed delamination b and the distance member 2 for steaming delamination c；Agitating device 3 and steam heater 4, positioned at steaming shell 1 below delamination c
Cavity is divided into the separator disc 5 of baking zone d and cold wind layer e setting up and down, the chassis 6 at the composition bottom cold wind layer e, respectively by baking zone
The first exhausting system 7 and the second exhausting system 8 and provided into cold wind layer e that gas or dregs of rice bits are extracted out in d and cold wind layer e
The air-cooled component 9 that cold wind makes the dregs of rice cooling.
Specifically, feeding-passage 1a and mixed-gas channel 1c are located at the opposite sides at 1 top of shell, tapping channel
1b is located at the side of the bottom cold wind layer e.
In conjunction with shown in Fig. 2 and Fig. 3, space disc component 2 respectively constitutes pre- delamination a, mixed delamination b and the layer bottom for steaming delamination c,
And it is logical including top plate 20, lower plywood 21, multiple stay bolt pipes 22 between top plate 20 and lower plywood 21 and discharging
Road 23.
It is stretched out specifically, 22 upper end of stay bolt pipe is fixed on the bottom of top plate 20, lower end from lower plywood 21.At this point,
Indirect steam heating is formed between top plate 20, lower plywood 21, stay bolt pipe 22, discharge channel 23 and corresponding 1 inner wall of place's shell
Channel A.
Then, 20 region of top plate positioned at the connection corresponding to stay bolt pipe 22 of space disc component 2 of mixed delamination b is provided with
Steam passage holes f.
In conjunction with shown in Fig. 4, discharge channel 23 include the feeding port 23a being formed on top plate 20 and lower plywood 21 and under
Material mouth 23b, the communicating pipe 23c for feeding port 23a to be connected with feed opening 23b, wherein tapping channel 1b and discharge channel
23 are connected, and discharge valve F is equipped on the channel being connected.
Specifically, multiple 22 peripheries of stay bolt pipe, top plate 20 and the outer wall and shell of lower plywood 21 and communicating pipe 23c 1
Inner wall formed indirect steam heating channel A.
Top plate 20 and lower plywood 21 are arranged in parallel, and stay bolt pipe 22 is centered on the center of rotation of agitating device and around upper
The circumferential direction and radially uniform distribution of laminate 20 and lower plywood 21.
In this example, the caliber of stay bolt pipe 22 is 300mm.
Steam passage holes f is centered on the center of stay bolt pipe 22 and around 22 circumferential direction of stay bolt pipe and radially uniform distribution.This example
In, the aperture of steam passage holes f is 25mm.
Space disc component 2 positioned at pre- delamination a is equipped with coaming plate 24 on the periphery of top plate 20 and lower plywood 21, wherein coaming plate
The airflow channel a1 being connected with mixed-gas channel 1c is formed between 24 and shell 1, therefore, top plate 20, is drawn lower plywood 21
Stay tube 22, discharge channel 23 and coaming plate 24 constitute preheating indirect steam heating channel A1.
Meanwhile it being located at pre- delamination a, mixed delamination b and three discharge channels 23 steamed on delamination c and mutually staggering setting.
In this way in discharge process, prevents dregs of rice material from falling directly into without overmulling delamination b and steam delamination c.
Steam heater 4 includes respectively to each preheating indirect steam heating channel A1 and indirect steam heating channel A
It feeds the first steam supply unit 41 of heating steam, circumferentially steam the second steam for being passed directly into steam in delamination c from outside shell 1
Supply unit 42, wherein from the supplied steam of the second steam supply unit 42 from steaming delamination c to mixed delamination b, again to pre- delamination a with
The airflow channel a1 flowing that shell 1 is formed, and be discharged from mixed-gas channel 1c.
Specifically, the first steam supply unit 41 includes indirect from 1 outside of shell and indirect steam heating channel A or preheating
Steam heats steam inlet 410, condensation-water drain 411, the Yi Jiyu positioned at 410 opposite side of steam inlet that channel A1 is connected
Steam inlet 410 be connected steam pipework (do not shown in figure, but it is contemplated that) and steam supply (do not shown in figure, but not
Difficulty is expected).
Second steam supply unit 42 include be arranged in steam the steam pipe coil 420 of delamination c, protrude into from the outside of shell 1 and with
The connecting tube 421 and steam supply that steam pipe coil 420 is connected, wherein the bottom of steam pipe coil 420 is equipped with steam jet
G, to raising up after steaming delamination c flows, the stay bolt pipe 22 and steam passage holes f of process move upwards and will add thermogenetic steam
After gas and solvent mixing, it is discharged from mixed-gas channel 1c.
The center of steam pipe coil 420 is overlapped with the rotary centerline of agitating device 3.
Steam jet g has multiple, and is divided into three groups, and one group is vertically downward, and one group is inclined towards steaming delamination center, and one group
Inclined direction steams inner walls corresponding to delamination.
In this example, successively interval setting between three groups, so, the direct steam of penetrating is when steaming delamination, energy and object
Material comes into full contact with, and the utilization of steam is more abundant, therefore precipitation effect is more satisfactory, while after the completion of steaming de-, the steaming to raise up
Vapour will steam the gas in delamination and solvent mixes merga pass steam channel, upward dispatch, and successively and in mixed delamination and pre- delamination
Gas and solvent mixing, are finally discharged from the mixed-gas channel of case top.
Meanwhile being arranged positioned at the steam jet g relative misalignment of the bottom upper and lower two steam jet g.
Then, steam pipe coil 420 and connecting tube 421 form one group of steam provisioning component B, the second steam supply unit 42 packet
Two groups of steam provisioning component B are included, and steam provisioning component B is evenly spaced on along the short transverse for steaming delamination c, steam supply
Device is connected with every group of steam provisioning component B.So, the precipitation effect of dregs of rice material can be increased substantially.
Meanwhile in conjunction with shown in attached drawing 5 and Fig. 6, be respectively equipped on above-mentioned separator disc 5 and chassis 6 can automatically open or
The bin gate m of closure, and separator disc 5 and the setting of 6 inner hollow of chassis.
Separator disc 5 includes upper plate 50 and lower plate 51 and blanking channel 52, wherein blanking channel 52, upper plate 50
Drying channel D is constituted with lower plate 51 and 1 inner wall of corresponding position shell, bin gate m is arranged on blanking channel 52.
As on separator disc 5 bin gate m automatically control can using the butterfly valve of common sense is automatically opened or is closed in such a way that reality
Dregs of rice material connection between existing baking zone d and cold wind layer e.
Steam heater 4 further includes for being done indirectly to the dregs of rice on separator disc 5 to being passed through steam inside separator disc 5
Dry third steam supply unit 43；
It is identical as the first steam supply unit 41 as the structure of third steam supply unit 43, it is not carried out repeating to state herein
It says.
Chassis 6 includes upper plate 60 and lower plate 61 and discharging channel 62, wherein discharging channel 62,60 and of upper plate
Lower plate 61 and 1 inner wall of corresponding position shell constitute air-cooled channel E, and bin gate m is arranged on discharging channel 62 on chassis 6, upper bottom
Air holes 60a is offered on plate 60, the wind outside shell 1 enters air-cooled layer f from air holes 60a by inlet air cold passage E.
Bin gate m on chassis 6, is connected with tapping channel 1b, and specifically automatically opens and closed manners and separation
Bin gate m is identical on disk 5.
In this example, the bin gate m on bin gate m and chassis 6 on separator disc 5 is relative dislocation setting.
In this example, agitating device 3 includes the agitating shaft 30 for extending and being located at middle part along 1 short transverse of shell；Position respectively
In pre- delamination a, mixed delamination b, steam the stirring blade 31 in delamination c, baking zone d and cold wind layer e and being fixed on agitating shaft 30；With
And the driving mechanism 32 that driving agitating shaft 30 is rotated around self-axis line.
In this example, agitating shaft 30 is connected by shaft coupling and speed reducer, then uses motor driven, while being arranged in shell 1
Bottom.
Meanwhile being located at 31 shape of stirring blade in pre- delamination a, mixed delamination b, steaming delamination c, baking zone d and cold wind layer e
Can be one or more sets at blade assembly, while every set blade assembly C(can be divided into both arms stirring knife and single armed stirring knife) right
Position in layer is answered also to be different, completion is configured according to actual needs.
In this example, pre- delamination a is divided into upper layer and lower layer by distance member 2；Mixed delamination b is divided into upper layer and lower layer, and funnel-shaped；
Steaming delamination c by distance member 2 is single layer；Baking zone d is divided into upper layer and lower layer；Cold wind layer e is single layer, is then correspondingly provided with for every layer
Above-mentioned stirring knife, under normal circumstances, stirring knife are settings in respective layer bottom, and the upper surface of laminating layer bottom is arranged, and therefore, stirs
The effect of knife is mainly two aspects: one, for stirring loose metal layer, dregs of rice material is evenly heated, and to improve precipitation effect, while making blanking
Also relatively uniform；Two, direct steam or cold wind short circuit are prevented, and then prevents the blocking of spray orifice and steam passage holes and air holes.
Identical as vaccum-pumping equipment as the first exhausting system 7 and the second exhausting system 8, being used for will be inside respective layer
Gas and dregs of rice bits extraction shell 1 outside, it is ensured that dregs of rice material steam it is de- after quality.
Air-cooled component 9, and be exactly the air-cooled channel E that outside air is pumped directly to cold wind layer e, then from stomata 60a
Dregs of rice material is blowed to, therefore, realizes the cooling of dregs of rice material.As for the structure used for conventional blower and communicating pipe etc., herein not to it
It is described in detail.
Finally, being directed to discharge valve F, during discharging, (the direct outsourcing of applicant) is controlled by airlock, was both just controlled
Blanking processed, and sealing process is played, it can completely cut off and steam delamination with gas leakage possible between following baking zone, avoid steaming delamination c
There is solvent gas to be leaked to baking zone.
In conclusion steaming de- system involved in this implementation compared with the existing, precipitation effect is improved, steam is reduced
Consumption, the evapo-separated machine effect for reducing power consumption, especially large-tonnage become apparent from.
It embodies as follows:
1, the mode for steaming delamination penetrating direct steam is changed to open steam coil spraying steam by original bottom plate spraying steam.In this way
One, spray vapour direction is downward, and circumferentially can uniformly scatter, and convenient for coming into full contact with dregs of rice material, guarantees precipitation effect,
Spraying vapour amount simultaneously might as well control, and spray orifice and steam passage holes are all not easy by the dregs of rice or dregs of rice bits blocking, and maintenance is also very convenient, workload
It is small.
, indirect steam heating channel be sandwich, steam passage holes are arranged on the top plate corresponding to stay bolt pipe, steam indirectly
Vapour heats the steam of channel interior, carries out indirect heating to the material dregs of rice, therefore, heating surface (area) (HS is big, and structural strength is big, it is not easy to become
Shape also ensures venting capability, therefore precipitation effect is more preferable.
, under the action of direct steam, can will be located in every layer gas and solvent caused by heating and mix, so
It is discharged afterwards from mixed-gas channel, so that mixed gas can make full use of, while also improve precipitation effect, then using this
Steaming in example takes off system, can reduce power consumption and steam consumption, when especially yield is larger (>=200 ton per day), than existing
The power consumption of evapo-separated machine reduces about 15~20%, reduces steam consumption about 15%, improves the economic benefit of client.
, by the setting of agitating device, on the one hand convenient for stirring loose metal layer, so that dregs of rice material is evenly heated, to improve precipitation effect
Fruit, while keeping blanking also relatively uniform；On the other hand in conjunction with steam and air-cooled pressure, in the case where stirring knife is struck off, further
The blocking for preventing spray orifice and steam passage holes and air holes.
The present invention is described in detail above, its object is to allow the personage for being familiar with this field technology that can understand this
The content of invention is simultaneously implemented, and it is not intended to limit the scope of the present invention, and the present invention is not limited to above-mentioned implementations
, equivalent change or modification made by all Spirit Essences according to the present invention should all cover in protection scope of the present invention.
Claims (10)
1. a kind of wet dregs of rice evapo-separated machine comprising:
Rack；
Shell, with feeding-passage, tapping channel and mixed-gas channel, wherein the feeding-passage and the mixed gas
Channel is located at the opposite sides of case top, and the tapping channel is located at the bottom of the shell；
Distance member, be horizontally set with the enclosure interior and the housing cavity is separated into the pre- delamination being arranged from top to bottom,
Delamination is steamed in mixed delamination；
Agitating device；
Steam heater,
It is characterized by:
The space disc component respectively constitutes the pre- delamination, mixed delamination and the layer bottom for steaming delamination, and includes top plate, lower layer
Plate, multiple stay bolt pipes and discharge channel between the top plate and the lower plywood, wherein stay bolt pipe upper end
Portion is fixed on the bottom of the top plate, lower end and stretches out from the lower plywood, the top plate, lower plywood, the stay bolt
Indirect steam heating channel is formed between pipe, the discharge channel and corresponding place's inner walls；
The top plate region positioned at space disc component connection corresponding to the stay bolt pipe of the mixed delamination is arranged
There are steam passage holes；
The space disc component positioned at the pre- delamination is equipped with coaming plate on the periphery of the top plate and the lower plywood, wherein
Form the airflow channel that is connected with the mixed-gas channel between the coaming plate and the shell, the top plate, under
Laminate, the stay bolt pipe, the discharge channel and the coaming plate constitute preheating indirect steam heating channel；
The discharge channel includes being formed in the top plate and feeding port on the lower plywood and feed opening, for by institute
The communicating pipe that the feeding port stated is connected with feed opening, wherein the tapping channel is connected with the discharge channel, and
The channel being connected is equipped with discharge valve；
The steam heater includes adding respectively to each indirect steam heating channel and the preheating indirect steam
The passage of heat feeds that the first steam supply unit of steam, circumferential described steam is passed directly into the of steam from outside the shell in delamination
Two steam supply units, wherein from second the supplied steam of steam supply unit from the steaming delamination to mixed delamination, again
The airflow channel formed to the pre- delamination and the shell flows, and is discharged from the mixed-gas channel；
The wet dregs of rice evapo-separated machine further includes being located at below the steaming delamination for the cavity of the shell to be divided into baking setting up and down
The separator disc of dried layer and cold wind layer, the chassis for constituting the cold wind layer bottom, respectively by gas in the baking zone and cold wind layer or
The first exhausting system and the second exhausting system of dregs of rice bits extraction and the wind that offer cold wind makes the dregs of rice cooling into the cold wind layer
Cold component, wherein being respectively equipped with the bin gate that can be automatically opened or be closed, and the separator disc on the separator disc and chassis
With the hollow setting of the inside chassis, the steam heater includes for being passed through steam to institute inside the separator disc
State the third steam supply unit that the dregs of rice on separator disc carry out contact drying；Cold wind is passed through the chassis by the air-cooled component
Inner cavity enters the cold wind layer, and the bin gate on the chassis is connected with the tapping channel.
2. wet dregs of rice evapo-separated machine according to claim 1, it is characterised in that: the top plate is parallel with the lower plywood to be set
It sets, the stay bolt pipe is centered on the center of rotation of the agitating device and around the week of the top plate and the lower plywood
To with radially uniform distribution.
3. wet dregs of rice evapo-separated machine according to claim 2, it is characterised in that: the steam passage holes are in the stay bolt pipe
Centered on the heart and around the stay bolt pipe circumferential direction and radially uniform distribution.
4. wet dregs of rice evapo-separated machine according to claim 1, it is characterised in that: the separator disc includes upper plate and lower wall
Body and blanking channel dry wherein inner walls described in the blanking channel, upper plate and lower plate and corresponding position are constituted
Dry passage, the bin gate are arranged on the blanking channel.
5. wet dregs of rice evapo-separated machine according to claim 1, it is characterised in that: the chassis include upper plate and lower plate,
And discharging channel, wherein inner walls described in the discharging channel, upper plate and lower plate and corresponding position constitute air-cooled lead to
Road, the bin gate are arranged on the discharging channel, and air holes, the wind warp of the hull outside are offered on the upper plate
It crosses and enters the air-cooled layer from the air holes into the air-cooled channel.
6. wet dregs of rice evapo-separated machine according to claim 1, it is characterised in that: the first steam supply unit includes from institute
State steam inlet that hull outside is connected with the indirect steam heating channel, positioned at the cold of the steam inlet opposite side
Condensate outlet and be connected with the steam inlet steam pipework and steam supply；The third steam supply unit
It is identical with the first steam supply unit structure.
7. wet dregs of rice evapo-separated machine according to claim 1, it is characterised in that: the second steam supply unit includes setting
It is described steam delamination steam pipe coil, protrude into from the hull outside and be connected with the steam pipe coil connecting tube, with
And steam supply, wherein the bottom of the steam pipe coil is equipped with steam jet, the steam is flowed to the steaming delamination bottom
It raises up after dynamic, the stay bolt pipe of process and the steam passage holes move upwards and will add thermogenetic gas and solvent to mix
Afterwards, it is discharged from the mixed-gas channel.
8. wet dregs of rice evapo-separated machine according to claim 7, it is characterised in that: the steam jet has multiple, and is divided into three
Group, one group vertically downward, and one group inclined towards the steaming delamination center, and one group inclined towards corresponding to the steaming delamination
The inner walls.
9. wet dregs of rice evapo-separated machine according to claim 7 or 8, it is characterised in that: the steam pipe coil and the connecting tube
Form one group of steam provisioning component, the second steam supply unit include at least two groups described in steam provisioning component, and institute
State steam provisioning component along it is described steam delamination short transverse be evenly spaced on, the steam supply with every group described in
Steam provisioning component is connected, and is located at the steam jet relative dislocation setting of the upper and lower two steam pipe coil bottoms.
10. wet dregs of rice evapo-separated machine according to claim 1, it is characterised in that: the agitating device includes along the shell
Body short transverse extends and is located at the agitating shaft at middle part；It is located at the pre- delamination, mixed delamination, steams delamination, baking zone and cold
In stratification of wind and the stirring blade that is fixed on the agitating shaft；And the driving that the driving agitating shaft is rotated around self-axis line
Mechanism.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811528704.0A CN109609262B (en) | 2018-12-13 | 2018-12-13 | Wet dreg desolventizer-toaster |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811528704.0A CN109609262B (en) | 2018-12-13 | 2018-12-13 | Wet dreg desolventizer-toaster |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN109609262A true CN109609262A (en) | 2019-04-12 |
| CN109609262B CN109609262B (en) | 2021-12-21 |
Family
ID=66009303
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811528704.0A Active CN109609262B (en) | 2018-12-13 | 2018-12-13 | Wet dreg desolventizer-toaster |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109609262B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115537265A (en) * | 2022-09-09 | 2022-12-30 | 江苏丰尚油脂工程技术有限公司 | Desolventizer-toaster |
| CN116491668A (en) * | 2023-06-13 | 2023-07-28 | 华南理工大学 | Rotary disc type miscellaneous beans steam rubbing and peeling all-in-one machine and peeling method |
Citations (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2201400Y (en) * | 1994-03-28 | 1995-06-21 | 丛培建 | Verticle bean dreg steam-removing machine |
| CN202626140U (en) * | 2012-06-05 | 2012-12-26 | 太仓市宝马油脂设备有限公司 | Oil wet meal desolventizing system and vertical evaporative desolventizer |
| CN203021526U (en) * | 2013-03-12 | 2013-06-26 | 北京中天金谷粮油工程技术有限公司 | Special tea seed cake evapo-separated machine |
| CN203582830U (en) * | 2013-09-29 | 2014-05-07 | 东北农业大学 | Evapo-separated machine for wet meal desolvation |
| CN103805333A (en) * | 2012-11-12 | 2014-05-21 | 北京中天金谷粮油工程技术有限公司 | Desolventizer toaster special for tea seed meal |
| CN104560373A (en) * | 2013-10-09 | 2015-04-29 | 宁夏琪凯节能设备有限公司 | Novel energy-saving evapo-separated machine |
| CN104673487A (en) * | 2015-03-19 | 2015-06-03 | 艾和美 | Improved toast-desolventizing machine |
| CN204490838U (en) * | 2015-02-20 | 2015-07-22 | 贾云 | The evapo-separated machine that novel intelligent controls |
| CN105176672A (en) * | 2015-09-07 | 2015-12-23 | 安徽中盛食用油科技有限公司 | Novel steaming and drying machine for soybean meal |
| CN205011730U (en) * | 2015-09-30 | 2016-02-03 | 山东凯斯达机械制造有限公司 | Evaporate energy -conserving mechanism of offline steam |
| CN205653422U (en) * | 2016-05-17 | 2016-10-19 | 山东三星玉米产业科技有限公司 | Maize dregs of rice desolventizer -toaster |
| CN206646083U (en) * | 2017-02-24 | 2017-11-17 | 湖南淳湘农林科技有限公司 | The production system that a kind of camellia oil cake circulation comprehensive utilizes |
| CN207130225U (en) * | 2017-08-10 | 2018-03-23 | 金寨县人海农业开发有限公司 | A kind of tea seed cake exsolution apparatus |
-
2018
- 2018-12-13 CN CN201811528704.0A patent/CN109609262B/en active Active
Patent Citations (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2201400Y (en) * | 1994-03-28 | 1995-06-21 | 丛培建 | Verticle bean dreg steam-removing machine |
| CN202626140U (en) * | 2012-06-05 | 2012-12-26 | 太仓市宝马油脂设备有限公司 | Oil wet meal desolventizing system and vertical evaporative desolventizer |
| CN103805333A (en) * | 2012-11-12 | 2014-05-21 | 北京中天金谷粮油工程技术有限公司 | Desolventizer toaster special for tea seed meal |
| CN203021526U (en) * | 2013-03-12 | 2013-06-26 | 北京中天金谷粮油工程技术有限公司 | Special tea seed cake evapo-separated machine |
| CN203582830U (en) * | 2013-09-29 | 2014-05-07 | 东北农业大学 | Evapo-separated machine for wet meal desolvation |
| CN104560373A (en) * | 2013-10-09 | 2015-04-29 | 宁夏琪凯节能设备有限公司 | Novel energy-saving evapo-separated machine |
| CN204490838U (en) * | 2015-02-20 | 2015-07-22 | 贾云 | The evapo-separated machine that novel intelligent controls |
| CN104673487A (en) * | 2015-03-19 | 2015-06-03 | 艾和美 | Improved toast-desolventizing machine |
| CN105176672A (en) * | 2015-09-07 | 2015-12-23 | 安徽中盛食用油科技有限公司 | Novel steaming and drying machine for soybean meal |
| CN205011730U (en) * | 2015-09-30 | 2016-02-03 | 山东凯斯达机械制造有限公司 | Evaporate energy -conserving mechanism of offline steam |
| CN205653422U (en) * | 2016-05-17 | 2016-10-19 | 山东三星玉米产业科技有限公司 | Maize dregs of rice desolventizer -toaster |
| CN206646083U (en) * | 2017-02-24 | 2017-11-17 | 湖南淳湘农林科技有限公司 | The production system that a kind of camellia oil cake circulation comprehensive utilizes |
| CN207130225U (en) * | 2017-08-10 | 2018-03-23 | 金寨县人海农业开发有限公司 | A kind of tea seed cake exsolution apparatus |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115537265A (en) * | 2022-09-09 | 2022-12-30 | 江苏丰尚油脂工程技术有限公司 | Desolventizer-toaster |
| CN115537265B (en) * | 2022-09-09 | 2024-02-13 | 江苏丰尚油脂工程技术有限公司 | Steam separator |
| CN116491668A (en) * | 2023-06-13 | 2023-07-28 | 华南理工大学 | Rotary disc type miscellaneous beans steam rubbing and peeling all-in-one machine and peeling method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN109609262B (en) | 2021-12-21 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202626140U (en) | Oil wet meal desolventizing system and vertical evaporative desolventizer | |
| CN101103761B (en) | Method and equipment for continuous gradient counterflow extraction for producing soybean concentrate protein | |
| CN208891620U (en) | Suitable black tea fermentation device | |
| CN109609262A (en) | A kind of wet dregs of rice evapo-separated machine | |
| CN209383732U (en) | A kind of de- system of the steaming of wet dregs of rice evapo-separated machine | |
| CN105249502A (en) | Vegetable dehydration-drying machine | |
| CN106472726A (en) | A kind of energy-efficient raw dark green tea process equipment | |
| CN208282581U (en) | A kind of tea green-keeping and drying comprehensive utilization system for heat energy | |
| CN102524519A (en) | Novel fish meal processing method | |
| CN205701013U (en) | A kind of foodstuff drying device with impurity removal function | |
| CN108619746A (en) | A kind of ammonium sulfate liquor concentration Distallation systm and its distillation technique | |
| CN204949379U (en) | Low temperature exsolution system of dregs of beans | |
| CN109077332A (en) | A kind of jujube cleaning, drying mechanism | |
| CN107337707A (en) | A kind of drying enrichment facility of high efficiency extraction Fish protein | |
| CN209660419U (en) | Biological feed additive production system with boiling fermentation | |
| CN105831296A (en) | Energy-saving type tea leaf drying machine and tea leaf drying method | |
| CN106500462A (en) | A kind of paddy centrum feed bin low temperature smashes storehouse drying means | |
| CN206341849U (en) | A kind of tea water-removing machine with steam beating function | |
| CN205040629U (en) | Vegetable dehydrating dryer | |
| CN113040275B (en) | Device for preparing molasses bean skin by spraying molasses on bean skin and processing technology of device | |
| CN105028892B (en) | A kind of low temperature desolventizing system of dregs of beans | |
| CN113368770B (en) | Albumen powder processing is with mixing stirring device | |
| CN203723380U (en) | Spray dryer for drying alligator snapping turtle powder | |
| CN108387100A (en) | A kind of tea green-keeping and drying comprehensive utilization system for heat energy | |
| CN106720533A (en) | One kind is used for tealeaves fried dry device after improving |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |