CN205948961U - Production system of maize flour - Google Patents
Production system of maize flour Download PDFInfo
- Publication number
- CN205948961U CN205948961U CN201620707218.5U CN201620707218U CN205948961U CN 205948961 U CN205948961 U CN 205948961U CN 201620707218 U CN201620707218 U CN 201620707218U CN 205948961 U CN205948961 U CN 205948961U
- Authority
- CN
- China
- Prior art keywords
- conveyance conduit
- pipeline
- production system
- maize
- screening plant
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Cereal-Derived Products (AREA)
- Coloring Foods And Improving Nutritive Qualities (AREA)
- Seeds, Soups, And Other Foods (AREA)
Abstract
The utility model discloses a production system of full powder is given birth to to the maize, the production system form by breaker, the pipeline who connects gradually, the jar of keeping in, pipeline, grinding device, pipeline, a screening plant, pipeline, the 2nd screening plant, pipeline, dewatering device, pipeline, pipeline 1, pipeline, pipeline 3 and the pipeline 5 that connects on pipeline, adopt the utility model discloses a maize that production system preparation obtained is whitewashed entirely, and the opaque is fine and smooth, has promoted the flavor and the taste of maize, and it no longer is the coarse food grain to make it, can make dumpling, cook noodless, and evaporate the steamed stuffed bun, the wheatmeal can be cooked, and the maize can both be done, and remain whole nutrition and the coarse fibre in the maize, can promote the wriggling of intestines and stomach, avoid three high diseases. Therefore, the utility model discloses an application prospect that the production that gave birth to full powder for the maize provides a new technological means, have wide is proposed.
Description
Technical field
This utility model is related to a kind of production system of corn flour, belongs to grain processing field.
Background technology
The existing technology producing Semen Maydis flour is all by direct for niblet pulverizing, or Semen Maydiss peeling is taken off pulverizing after embryo.This two
The smell bad of the corn flour that the method for kind is produced, even is difficult to swallow sometimes.Someone is in corn flour making using swollen
After the ripe product of change mechanism, then pulverize and make Semen Maydis flour, this practice tedious process, power consumption is high, is difficult popularization and application.
The utility model proposes the production system method of the raw full powder of Semen Maydiss change going through of original Semen Maydis flour dry production
History, changes local flavor and the mouthfeel of Semen Maydiss, is no longer coarse grain, can make dumplings, cook noodles, steam stuffed bun, wheat flour can be cooked, Semen Maydiss
Raw full powder can do.Remain whole nutrition and the crude fibre in Semen Maydiss, promote the wriggling of gastrointestinal, it is to avoid three high diseases.
Content of the invention
The purpose of this utility model is for the problems referred to above, provides a kind of products taste good, easy and simple to handle corn flour
Production system.
For reaching above-mentioned purpose, this utility model employs following technological means：
A kind of production system of the raw full powder of Semen Maydiss, it is by the breaker 1 being sequentially connected, conveyance conduit 2, temporary storage tank 3, defeated
Send pipeline 4, refining device 5, conveyance conduit 6, the first screening plant 7, conveyance conduit 8, the second screening plant 9, conveyance conduit 10,
Dehydration device 11, conveyance conduit 12, drying device 13, conveyance conduit 14, packing device 15 and be connected on conveyance conduit 2
Injection apparatus 16 form；
Wherein, described breaker 1 is used for crushing the niblet after remove impurity, and the corn particle after crushing passes through conveying
Pipeline 2, enters temporary storage tank 3, in temporary storage tank 3 under the water under high pressure effect of the flow at high speed that injection apparatus 16 eject and turbulence
Corn particle enters refining device 5 with the mixed liquor of water by conveyance conduit 4, and the Semen Maydis pulp after defibrination process passes through conveyance conduit
6 entrance the first screening plants 7, the Semen Maydis pulp after screening enters the second screening plant 9, the second screening plant 9 by conveyance conduit 8
Semen Maydis pulp after screening enters dehydration device 11 by conveyance conduit 10, and the material after dehydration enters drying by conveyance conduit 12
Device 13, dried material enters packing device 15 by conveyance conduit 14.
It is preferred that described refining device is Filing apparatus in this utility model.
It is preferred that described dehydration device is precoating type rotary drum vacuum filter in this utility model.
It is preferred that described drying device is pneumatic conveying drying unit in this utility model.
Compared to prior art, the utility model has the advantage of：
(1) corn powder being prepared using this utility model method, silty is fine and smooth, improves local flavor and the mouth of Semen Maydiss
Sense, so as to be no longer coarse grain, can be made dumplings, cook noodles, steam stuffed bun, wheat flour can be cooked, Semen Maydiss can do；
(2) remain whole nutrition and the crude fibre in Semen Maydiss, the wriggling of gastrointestinal can be promoted, it is to avoid three high diseases.
(3) in production system, batch mixing is carried out using spray regime, uniformly quickly.
(4) in production system, defibrination adopts rasion mode, and one's own profession was out of use in the industry.
(5) it is dehydrated using precoating type vacuum-type drum filter, it is to avoid the power using scraper dehydration is big, and interval is grasped
Make；The volume of filter press is big, intermittently operated, and filter cake is too hard, after being dried powder to sieve, the shortcoming of broken and feed back.
Brief description
Fig. 1 is the method flow diagram using this utility model system；
Fig. 2 is the structure chart of the production system of the raw full powder of Semen Maydiss of the present utility model.
Description of reference numerals：
1- breaker
2- conveyance conduit
3- temporary storage tank
4- conveyance conduit
5- refining device
6- conveyance conduit
7- first screening plant
8- conveyance conduit
9- second screening plant
10- conveyance conduit
11- dehydration device
12- conveyance conduit
13- drying device
14- conveyance conduit
15- packing device
16- injection apparatus
Specific embodiment
To further describe this utility model with reference to specific embodiment, advantage of the present utility model and feature will be with
Description and apparent.But these embodiments are only exemplary, any restriction is not constituted to scope of the present utility model.
It will be understood by those skilled in the art that can be to this utility model skill under without departing from spirit and scope of the present utility model
The details of art scheme and form are modified or are replaced, but these modifications and replacement each fall within protection domain of the present utility model
Interior.
Embodiment 1
The structure chart of the production system for the raw full powder of this utility model Semen Maydiss for the Fig. 2, described production system is by being sequentially connected
Breaker 1, conveyance conduit 2, temporary storage tank 3, conveyance conduit 4, refining device 5, conveyance conduit 6, the first screening plant 7, conveying
Pipeline 8, the second screening plant 9, conveyance conduit 10, dehydration device 11, conveyance conduit 12, drying device 13, conveyance conduit 14, bag
Assembling device 15 and the injection apparatus 16 being connected on conveyance conduit 2 form；
Wherein, described breaker 1 is used for crushing the niblet after remove impurity, and the corn particle after crushing passes through conveying
Pipeline 2, enters temporary storage tank 3, in temporary storage tank 3 under the water under high pressure effect of the flow at high speed that injection apparatus 16 eject and turbulence
Corn particle enters refining device 5 with the mixed liquor of water by conveyance conduit 4, and the Semen Maydis pulp after defibrination process passes through conveyance conduit
6 entrance the first screening plants 7, the Semen Maydis pulp after screening enters the second screening plant 9, the second screening plant 9 by conveyance conduit 8
Semen Maydis pulp after screening enters dehydration device 11 by conveyance conduit 10, and the material after dehydration enters drying by conveyance conduit 12
Device 13, dried material enters packing device 15 by conveyance conduit 14.
In the present embodiment, specifically, the equipment being adopted and its source are shown in Table 1：
Table 1 equipment and its source
Using this utility model system produce the raw full powder of Semen Maydiss method flow diagram as shown in figure 1, concrete operation step such as
Under：
(1) remove impurity, broken
After niblet remove impurity, using breaker 1, niblet being crushed to particle diameter is 2～3mm；
(2) spray
Sprayed by injection apparatus 16, with the water of 6bar pressure, broken corn particle is injected into temporary storage tank 3, in height
Under the water under high pressure of speed flowing and turbulence acts on, water is sufficiently mixed with material, and spraying the water yield is 25 times of Semen Maydiss volume, per hour
Till the broken corn particle of regulation inlet amount has all been mixed with water, 1 hour is sprayed once；
(3) soak
The water temperature soaked is 40 DEG C, duration 20～24h, fully the corn particle after crushing being soaked, is twisted with the fingers with handss
No hard core is defined；
(4) defibrination
Defibrination is carried out on the Filing apparatus (refining device 5) of high-speed rotation, and the linear velocity of rotor periphery is up to 92.3m/s,
Under so high rotating speed, thoroughly levigate in the presence of corn particle file and mill；
(5) sieve
Semen Maydis pulp after defibrination is sieved using the first screening plant 7, the Semen Maydis pulp that collection cut size is less than 80 μm；
(6) adopt the second screening plant 9 repeat step (5) once；
(7) it is dehydrated
It is dehydrated using precoating vacuum-type drum filter (dehydration device 11), the depth of cut per minute is 0.007mm.Dehydration
Moisture content≤38% of material afterwards；
(8) it is dried
Drying is carried out in pneumatic conveying drying unit (drying device 13), the cold wind being sucked in by steam heating, heating
Hot blast temperature is 145～155 DEG C afterwards, needs dry wet stock to enter vertical drying tube under the drive of the hot blast of high speed
Interior lifting, drying tube is the stainless steel pipes of a sky with the high about 20m of two-stage pulse tube, here, hot blast with bring up
Wet stock fully carry out heat exchange, for a moment fast for a moment slow in speed drying tube and pulse tube, abundant turbulence completes dry run,
In cyclone separator below, dried powder is separated with the damp-heat air after heat exchange, and the damp-heat air after heat exchange becomes
For waste gas, air is entered by blower fan, temperature is at 55～65 DEG C.So far complete the dry run of material, wind band sets in entirely drying
Standby interior speed is the process of a change, and substantially between 15m/s～24m/s, the time that drying completes, not over 2s, is dried
Complete material water ratio is less than 13%；
(9) pack
The material being dried enters packing device 15 by conveyance conduit, carries out the packaging of product.
The corn powder being prepared using system of the present utility model, silty is fine and smooth, therefore improves the local flavor of Semen Maydiss
With mouthfeel so as to be no longer coarse grain, can make dumplings, cook noodles, steam stuffed bun, wheat flour can be cooked, Semen Maydiss can do, and protect simultaneously
Stay whole nutrition and the crude fibre in Semen Maydiss, there is the wriggling promoting gastrointestinal, it is to avoid the effect of three high diseases.
Claims (4)
1. the production system of the raw full powder of Semen Maydiss is it is characterised in that described production system is by the breaker (1) being sequentially connected, defeated
Send pipeline (2), temporary storage tank (3), conveyance conduit (4), refining device (5), conveyance conduit (6), the first screening plant (7), conveying
Pipeline (8), the second screening plant (9), conveyance conduit (10), dehydration device (11), conveyance conduit (12), drying device (13),
Conveyance conduit (14), packing device (15) and the injection apparatus (16) being connected on conveyance conduit (2) form；
Wherein, described breaker (1) is used for crushing the niblet after remove impurity, and the corn particle after crushing passes through delivery pipe
Road (2), enters temporary storage tank (3), temporary storage tank under the water under high pressure effect of the flow at high speed that injection apparatus (16) eject and turbulence
(3) corn particle in enters refining device (5), the Semen Maydis pulp after defibrination process with the mixed liquor of water by conveyance conduit (4)
First screening plant (7) is entered by conveyance conduit (6), the Semen Maydis pulp after screening enters the second screening by conveyance conduit (8)
Device (9), the Semen Maydis pulp after the second screening plant (9) screening enters dehydration device (11) by conveyance conduit (10), after dehydration
Material by conveyance conduit (12) enter drying device (13), dried material pass through conveyance conduit (14) enter packaging dress
Put (15).
2. production system as claimed in claim 1 is it is characterised in that described refining device is Filing apparatus.
3. production system as claimed in claim 1 is it is characterised in that described dehydration device is precoating type rotating drum vacuum filtration
Machine.
4. production system as claimed in claim 1 is it is characterised in that described drying device is pneumatic conveying drying unit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620707218.5U CN205948961U (en) | 2016-07-06 | 2016-07-06 | Production system of maize flour |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620707218.5U CN205948961U (en) | 2016-07-06 | 2016-07-06 | Production system of maize flour |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205948961U true CN205948961U (en) | 2017-02-15 |
Family
ID=57968739
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620707218.5U Active CN205948961U (en) | 2016-07-06 | 2016-07-06 | Production system of maize flour |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205948961U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111111847A (en) * | 2019-12-30 | 2020-05-08 | 宁安市粮油淀粉机械制造有限公司 | Apparatus for producing of whole powder is given birth to maize |
-
2016
- 2016-07-06 CN CN201620707218.5U patent/CN205948961U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111111847A (en) * | 2019-12-30 | 2020-05-08 | 宁安市粮油淀粉机械制造有限公司 | Apparatus for producing of whole powder is given birth to maize |
| CN111111847B (en) * | 2019-12-30 | 2022-05-10 | 宁安市粮油淀粉机械制造有限公司 | Apparatus for producing of whole powder is given birth to maize |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP7365027B2 (en) | Circulation mill, its operating method, and products processed with the circulation mill | |
| CN209362666U (en) | It is a kind of that rice straw is crushed, is sieved, drying integrated device | |
| CN104848663A (en) | Cassava starch production equipment and method using three-pass drum and air flow combined drying | |
| CN203505499U (en) | Peanut peeling machine | |
| CN210425787U (en) | Herbal pieces-drying-machine | |
| CN209646649U (en) | One kind is pulverized and mixed and drying integrated Chinese medicine powder preparation facilities | |
| CN205948961U (en) | Production system of maize flour | |
| CN109772551A (en) | Potato full-powder preparation system and its application method | |
| CN106632586B (en) | Method for simultaneously extracting starch and protein | |
| CN206751763U (en) | A kind of tea seeds drying and hulling device | |
| CN106509943A (en) | Dust removal type dry fruit grading dryer | |
| CN106173831A (en) | A kind of production method of the raw full powder of Semen Maydis, for the production system of the method and product | |
| CN101904490B (en) | Method for extracting dietary fiber in production of bean starch | |
| CN208956960U (en) | A kind of dry crushing device of camellia oleifera fruit | |
| CN207662146U (en) | A kind of organic fertilizer production drying device | |
| CN208832956U (en) | Potato high moisture material second drying apparatus | |
| CN107259511A (en) | A kind of preparation method without alum sweet potato noodles | |
| CN207370903U (en) | A kind of Pleurotus tuber-regium medicinal extract extracts production line | |
| CN109497404B (en) | Cooling and powder collecting process and equipment cleaning method for edible and edible rice food powder | |
| CN207803394U (en) | A kind of novel energy-conserving peanut automatic sheller | |
| CN218898278U (en) | Cassava whole powder processing system | |
| CN206565252U (en) | A kind of oil tea is peeled off sterilization machine | |
| CN106722167A (en) | A kind of production method of five-cereal health-care powder | |
| CN110050950A (en) | A kind of processing technology of high fine low-sugar type health-care flour | |
| CN204768854U (en) | Bitter buckwheat peel machine |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |