CN105310063B - Mushroom concentrates powder production technology - Google Patents
Mushroom concentrates powder production technology Download PDFInfo
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- CN105310063B CN105310063B CN201510808450.8A CN201510808450A CN105310063B CN 105310063 B CN105310063 B CN 105310063B CN 201510808450 A CN201510808450 A CN 201510808450A CN 105310063 B CN105310063 B CN 105310063B
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Abstract
The invention discloses one kind production is easy, the fragrant degree of mushroom powder, purity, fineness are higher, and the mushroom concentration powder production technology that production efficiency is higher and inexpensive, its processing step is through extracting, filtering, centrifuging, vibrate filtering, dextrin mixing and vacuum and low temperature and instantaneously concentrate by mushroom stems or leftover bits and pieces, the liquid after concentration is spray-dried again, solid vapour separation, packed after the mushroom powder after separation is dried into cooling.
Description
Technical field
The present invention relates to a kind of mushroom to concentrate powder production technology.
Background technology
Mushroom is a kind of high protein, low fat, polysaccharide, several amino acids and multivitamin mushroom food, mushroom juice
Not only delicious, nutritive value height can also reduce blood pressure and reach health-care effect.Usual people can by mushroom umbrella and mushroom stems or under
Heel is separately eaten, and the use value of general mushroom stems or leftover bits and pieces is not fully utilized, causes to waste.
Chinese patent ZL89104134.6 discloses a kind of " process for forced extraction of mushroom juice with enzyme preparation ", using mushroom as material, uses
Biological enzyme forces catalystic, fermentative mushroom fruiting body crushed material or mushroom solid medium crushed material, ferment, filter by boiling,
Mushroom juice is concentrated to give, described biology enzyme refers to cellulase and amylase.But the patent strengthens extraction perfume in enzyme preparation
During mushroom juice, it is necessary to purer substrate and environment are provided for the procreation of enzyme, thus fermentation must use distilled water, and only
The equipment such as stainless steel or porcelain with constant temperature can be used, to prevent mould and Ag+、Hg++、Cn++、Fe++Deng caused by
Inhibitory action；The condition that reaction needs during production is more harsh, causes production inconvenience.Mushroom juice by the extraction method needs to add
Enzyme preparation, and the enzyme after catalysis is still remained in mushroom juice, enzyme stays influences pol in a liquid；Such as need to remove and need to inactivate step
Suddenly；Temperature control is needed in production process and adjusts the necessary condition that pH value ensures enzyme reaction, processing step is numerous and diverse.
Chinese patent ZL97123224.5 discloses a kind of " deep working methods and its product of a kind of mushroom stems ", by mushroom stems
Mushroom soy sauce is made by the technique such as sorting, washing, distillation, extraction, filtering, preparation and seasoning, sterilization.Distillation in the patent
The step of condensing reflux, is time-consuming longer, causes the production cycle to be grown；Temperature needed for distillation is high, causes the flavor of mushroom to be destroyed,
And the Brix degree of liquid too low is unfavorable for preserving.
The content of the invention
Therefore, for it is above-mentioned the problem of, the invention provides one kind production is easy, the fragrant degree of mushroom powder, purity, fineness are equal
It is higher, and the mushroom concentration powder production technology that production efficiency is higher and inexpensive.
To reach above-mentioned purpose, the present invention is achieved by the following technical solutions：Mushroom concentrates powder production technology, including
Following step：
（1）Weight ratio is 1 as material by the clean mushroom stems of selection or leftover bits and pieces:10-1：20 material and water input
In extractor, 85-90 °C is stirred and heated to, constant temperature stirring 1-3 hours, 90-100 °C is again heated to, is entered by air pressurized
Row initial filter, the screen pack mesh number of the initial filter are 55-65 mesh, and the liquid after initial filter enters in fine filtering machine, then opens extractor
Slag is cleared to be produced next time；
（2）The screen pack mesh number of the fine filtering machine is 80-120 mesh, by the liquid after filtering by being pumped into the first buffering
In tank；
（3）Liquid in first surge tank enters in centrifuge, and the rotating speed of the centrifuge is 5000-6000 revs/min,
Debris is separated by centrifuge, the liquid after separation enters the second surge tank；
（4）Liquid in second surge tank enters duplex strainer, and the screen pack mesh number of the duplex filter is 190-
250 mesh, the liquid after filtering enter in shaking screen；
（5）The screen pack mesh number of the shaking screen is 380-420 mesh, and the liquid after shaking screen filters enters the 3rd buffering
Tank；
（6）Liquid in 3rd surge tank enters in concentration tower, and liquid carries out high temperature sterilization, the temperature of the high temperature sterilization
For 100-120 °C, the time is the 20-30 seconds, and dextrin is added into the liquid after sterilization and is stirred, the addition of dextrin
For the 18%-22% of liquid weight, the liquid added after dextrin enters seven grades of concentration tower evaporations of quadruple effect, ring of the concentration process in vacuum
Border and temperature control is below 90 °C, the time be no more than 30 seconds under conditions of carry out, the pol control of liquid during vacuum concentration
In 30 degree of Brix, the concentration tower is provided with aroma recovery system, and recovery system returns to aroma gases in concentrate；Concentration tower
Its Brix degree of the liquid of outlet is 60-70 degree, and the liquid after concentration enters drying tower；
（7）The lower rotation of drying tower is provided with spiral and accelerates cover, and it is in turbination that the spiral, which accelerates cover, the spiral
The side wall of cover is accelerated to offer spiral accelerated passage, the porch of spiral accelerated passage is provided with atomizer and compressed gas
Boosting nozzle, the outlet of spiral accelerated passage are set upward, and the spiral, which accelerates to rotate on the inside of the upper end of cover, is provided with interior do
Dry frame, the spiral accelerate the outside rotation of the upper end of cover to be provided with outer drying frame, are provided with the interior drying frame some
The interior dry nozzle of outward-dipping setting, some outer dry nozzles for sloping inwardly and setting, institute are provided with the outer drying frame
Stating the interior dry nozzle spiral relative with the outer dry nozzle accelerates the upper end of cover to be symmetrical arranged, the liquid after concentration by
Atomizer is atomized and sprayed into spiral accelerated passage, while compressed gas is together sprayed into spiral shell by compressed gas boosting nozzle
Revolve in accelerated passage, atomization concentrate, which mixes in spiral accelerated passage with the mixture of compressed gas and carries out spiral, to be accelerated most
Afterwards from the bottom to top in cylindrical penetrating drying tower, interior dry nozzle ejects inner side hot gas in turbination heating gas column
Its inner side is dried for the inner side for spraying to cylindric mixture, and the outside hot gas that outer dry nozzle ejects is in cone
Its outside is dried in the outside that heating gas column sprays to cylindric mixture, and two strands of heating gas columns form intersection heating will atomization
Concentrate is dried to dust, and the emitted dose of atomizer is 800-1000ml/min, interior dry nozzle and outer dry nozzle
Total hot gas intake is 6-6.5m3/min, and heat gas temperatures are 100-150 °C, and dried vapour solid mixture is by doing
Dry tower outlet enters cyclone separator；
（8）Cyclone separator carries out vapour to vapour solid mixture and separated admittedly, and the concentration powder after separation, which enters in drying chamber, to be carried out
Dry, the superheated vapor after separation is introduced in air preheater by air-introduced machine；
（9）Dried concentration powder be vacuum-packed after being air-cooled to normal temperature.
It is further improved to be：The drying tower includes dry heat section, powder raising section, steady defeated successively from the bottom to top
Section is sent, the diameter of dry heat section described in the diameter light rain of the powder raising section, the diameter of the dry heat section is less than institute
State and pass through between the diameter of steady transportation section, the powder raising section and the dry heat section and the steady transportation section
Cone connection is connected.
It is further improved to be：Stainless steel inner container is provided with the drying tower.
By using preceding solution, the beneficial effects of the invention are as follows：This production technology passes through mushroom stems or leftover bits and pieces
Hot water extraction mushroom juice is extracted, leaching liquor is after initial filter, fine filtering machine, centrifuge, duplex strainer and shaking screen multiple filtration
Into concentration tower, progress cryogenic vacuum instantaneously concentrates in concentration tower, to ensure not destroying the flavor of mushroom, farthest protects
Stay the taste of mushroom juice；Liquid after concentration sterilize to add after dextrin to enter in drying tower and is spray-dried, is sprayed
The cylindrical ejection after spiral accelerates cover to accelerate by the mushroom concentrate of atomization and compressed gas when drying, and to cylindrical shape
The inner side and outside of mixing fog intersect heating simultaneously, while shortening drying time saving heat energy, can break up atomized liquid
Pearl improves the fineness of mushroom powder, in addition sprays mixture from the bottom to top by the bottom of drying tower, prevents viscous wall and coke powder from showing
As producing, the purity of product is improved.
Brief description of the drawings
Fig. 1 is drying tower schematic diagram；
Fig. 2 is enlarged drawing at Fig. 1 A；
Fig. 3 is enlarged drawing at Fig. 2 B.
Wherein 1, spiral accelerates cover；2nd, compressed gas boosting nozzle；3rd, atomizer；4th, dry heat section；5th, powder carries
Rise section；6th, steady transportation section；7th, interior drying frame；8th, interior dry nozzle；9th, outer drying frame；10th, outer dry nozzle.
Embodiment
Embodiment one：The present embodiment discloses a kind of mushroom concentration powder production technology, and its production stage is as follows：
（1）It is 1 by weight ratio:In 13 mushroom pin and water input extractor, lasting stirring and by mixed liquor（Mushroom pin and
The solution of water）90 °C, after constant temperature stirs 1.5 hours are heated to, then mixed liquor is heated to 95 °C, mixed liquor passes through extractor bottom
The screen pack of the mesh of portion 60 carries out initial filter, now because the debris on 60 mesh screen packs is excessive, causes the rate of filtration slower, toward extraction
Air pressurized is carried out in tank to improve the rate of filtration, the liquid after filtering enters fine filtering machine；After filtering, extraction is opened
Tank, the progress so as to technique productions next time is purged to the residue in extractor.
The structure of the extractor is hollow structure, and extractor is provided with inlet, liquid outlet and slag-drip opening, extracts pot bottom
Provided with screen pack.
（2）The mesh number of the fine filtering machine screen pack is 80 mesh, and the liquid after the filtering of fine filtering machine is passed through into stainless steel pump
It is pumped into the first surge tank；The structure of first surge tank is hollow structure, and first surge tank is provided with inlet and goes out liquid
Mouthful.
（3）Liquid in first surge tank is pumped into centrifuge, the rotating speed of the centrifuge is 5500 revs/min, from
Scheming is mainly used in separating the solid particle in liquid and liquid, and after solid sundries are separated by centrifuge, liquid enters
Second surge tank；Centrifuge can known to the centrifuge use, it can buy from disclosed in the market.Described
The structure of two surge tanks is hollow structure, and second surge tank is provided with inlet and liquid outlet.
（4）Liquid in second surge tank is pumped into duplex strainer, the filtering mesh number of the duplex strainer is 200
Mesh, the liquid after filtering is pumped into shaking screen；The duplex strainer is formed in parallel, it is necessary to remove by two stainless steel filters
During slag, a filter only need to be closed, another can carry out normal work；The main reason for being filtered using duplex strainer be
The good airproof performance of duplex strainer, negotiability are strong and easy to operate, can accurately insure that filtering accuracy, and can quickly change
Filter bag, filter substantially without supplies consumption so that running cost reduce, clean filter when need not be out of service, ensure production
It is carried out continuously.
（5）Liquid after being filtered in shaking screen is pumped into the 3rd surge tank, the filtering mesh number of the shaking screen is 400 mesh；
The vibratory sieve is mainly made up of screen box, supporting arrangement, vibrator and transmission device, and the screen box is by screen frame, compass screen surface and its pressure
Tight device composition, the supporting arrangement are mainly made up of rubber spring.
The main reason for being filtered using shaking screen is that shaking screen produces judder in operation, reduces feed blocking sieve
The phenomenon in hole, there is higher screening efficiency and productivity ratio；And its simple structure, dismounting maintenance clean are convenient；
（6）Liquid in 3rd surge tank is pumped into concentration tower, concentration tower temperature rises to 110 °C, the operating time 25
Second is tentatively sterilized to liquid, and dextrin is added into the liquid after sterilization and is stirred, the addition of dextrin is liquid
The 20% of body weight, the liquid added after dextrin carry out seven grades of concentration tower evaporations of quadruple effect, environment and temperature of the concentration process in vacuum
Control is less than 90 °C, vacuum 0.04Mpa, and the time is to be carried out under conditions of 20 seconds, and pol too low water is too during due to spraying
It can lump more, in order to prevent the concentration too phenomenon of conference spray not out from producing, the pol of liquid during vacuum concentration is controlled 30
Brix is spent, the concentration tower is provided with aroma recovery system, and recovery system returns to aroma gases in concentrate, and operation terminates
Afterwards, the liquid Brix degree for flowing through concentration tower outlet is 65 degree, and temperature is 15 °C, and the liquid after concentration enters drying tower.
The grade low-temp evaporation concentration system of quadruple effect seven, is made up of, low temperature 4 evaporators being serially connected（90 DEG C of left sides
It is right）Heating steam is incorporated by the first effect, the liquid in heating evaporation device, make liquid produce it is lower than vapor (steam) temperature close to etc.
The evaporation of amount.Caused steam is introduced into the second effect as heating steam, makes the feed liquid of the second effect with the temperature lower than the first effect
Degree evaporation.This process repeats to quadruple effect always.In the concentration process of liquid, primary steam first carries out once dense to material
Contracting, then indirect steam reuses, and so can effectively utilize steam.Level refers to that liquid passes through the number of evaporator, quadruple effect seven
Level is exactly that liquid passes through 4 evaporators, altogether by the evaporation of 7 times.Seven grades of the quadruple effect in process of production, first evaporator
By 3 times, second evaporator respectively passes through 1 time by 2 times, the 3rd and the 4th evaporators.
It is the concentration process of an instantaneous vacuum of low temperature in the concentration process of concentration tower, temperature control exists in concentration process
Less than 90 °C farthest to retain the taste of mushroom juice；
（7）As shown in Figure 1-Figure 3, the lower rotation of drying tower is provided with spiral and accelerates to cover 1, and the spiral acceleration cover 1 is in
Turbination, the spiral accelerate the side wall of cover 1 to offer spiral accelerated passage, and the porch of spiral accelerated passage is provided with mist
Change nozzle 3 and compressed gas boosting nozzle 2, the outlet of spiral accelerated passage is set upward, and the spiral accelerates the upper end of cover 1
Rotated on the inside of portion and be provided with interior drying frame 7, the spiral accelerates the outside rotation of the upper end of cover 1 to be provided with outer drying frame 9, institute
State the interior dry nozzle 8 that some outward-dipping settings are provided with interior drying frame 7, be provided with the outer drying frame 9 it is some to
The outer dry nozzle 10 of tilted setting, the interior dry nozzle 8 accelerate cover 1 with the relatively described spiral of the outer dry nozzle 10
Upper end be symmetrical arranged, the liquid after concentration is atomized and sprayed into spiral accelerated passage by atomizer 3, is compressed simultaneously
Gas-assisted nozzle 2 together sprays into compressed gas in spiral accelerated passage, and the mixture for being atomized concentrate and compressed gas exists
Mixing and progress spiral accelerate in last penetrating drying tower cylindrical from the bottom to top in spiral accelerated passage, interior dry nozzle 8
Eject inner side hot gas and spray to the inner side of cylindric mixture in turbination heating gas column and its inner side is dried, outside
The outside hot gas that dry nozzle 10 ejects sprays to the outside of cylindric mixture to its outside in cone heating gas column
It is dried, two strands of heating gas columns form to intersect to heat is dried to dust by atomization concentrate, and the emitted dose of atomizer 3 is
1000ml/min, total hot gas intake of interior dry nozzle 8 and outer dry nozzle 10 are 6.5m3/min, hot gas
Temperature is 150 °C, and the leaving air temp for controlling drying tower is 100 °C, and dried vapour solid mixture is exported by drying tower enters rotation
Wind separator；
（8）Cyclone separator carries out vapour to vapour solid mixture and separated admittedly, in order to improve separating effect, can use multistage rotation
Wind separator is used in series, and takes separating for several times, and the concentration powder after separation, which enters in drying chamber, to be dried, the high temperature after separation
Steam is introduced in air preheater by air-introduced machine, and carrying out pre- thermosetting to combustion air using the waste heat of superheated vapor heats gas
Body, energy-conserving and environment-protective, and save the energy；
（9）Dried concentration powder be vacuum-packed after being air-cooled to normal temperature.
This production technology extracts hot water by mushroom stems or leftover bits and pieces and extracts mushroom juice, leaching liquor by initial filter, fine filtering machine,
Enter concentration tower after centrifuge, duplex strainer and shaking screen multiple filtration, cryogenic vacuum carried out in concentration tower and is instantaneously concentrated,
To ensure not destroying the flavor of mushroom, farthest retain the taste of mushroom juice；Liquid after concentration is subjected to sterilization addition
Enter after dextrin in drying tower and be spray-dried, the mushroom concentrate of atomization and compressed gas are passed through into spiral during spray drying
Accelerate cover 1 accelerate after cylindrical ejection, and inner side to cylindric mixing fog and outside intersect heating simultaneously, shorten dry
While dry saving of time heat energy, the fineness that atomized liquid pearl improves mushroom powder can be broken up, in addition by mixture by drying tower
Bottom sprays from the bottom to top, prevents viscous wall and coke powder phenomenon from producing, improves the purity of product.
As shown in figure 1, in order to prevent unseasoned sufficiently atomizing particle from dropping or being adhered to downwards the tower wall of drying tower,
Occur viscous wall and coke powder phenomenon, the drying tower includes dry heat section 4, powder raising section 5, steady defeated successively from the bottom to top
Section 6 is sent, the diameter of dry heat section 4 described in the diameter light rain of the powder raising section 5, the diameter of the dry heat section 4 is small
Diameter in the steady transportation section 6, the powder raising section 5 and the dry heat section 4 and the steady transportation section 6 it
Between be connected by cone connection, because the diameter of powder raising section 5 diminishes, so as to improve the flow velocity of gas, will not by
Dry atomizing particle is lifted up and continues drying, in steady transportation section 6, can smoothly enter rotation for the ease of material
Wind separator, prevent from forming eddy flow at the top of drying tower, therefore its enlarged diameter, so as to slow down flow velocity, realize steady defeated
The purpose sent.
In order to improve drying efficiency, drying tower uses stainless steel inner container, using the thermal radiation capability of stainless steel, improves dry
Dry effect and efficiency.
Embodiment two：
It is 1 by weight ratio:It is lasting to stir and mixed liquor is heated to 90 °C in 20 mushroom pin and water input extractor,
After constant temperature stirs 3 hours, remaining step is identical with embodiment one.
In above-mentioned each production craft step, the weight ratio of the mushroom and water is 1：10 to 1：20 this proportion are all
Feasible, different ratios are identicals to The effect of invention；The temperature range that is heated in each processing step, the mesh number of filter screen,
Sterilizing time is all feasible in corresponding steps limited range, and it can equally realize the purpose of the present invention, can't
Because the difference of value causes obtained concentrate to have obvious or difference fundamentally.
Described in above, only this wound is used using the embodiment of this origination techniques content, any those skilled in the art
Make done modifications and changes, all belong to the scope of the claims of this creation opinion, and be not limited to those disclosed embodiments.
Claims (3)
1. mushroom concentrates powder production technology, it is characterised in that comprises the steps：
（1）Weight ratio is 1 as material by the clean mushroom stems of selection or leftover bits and pieces:10-1：20 material and water input extraction
In tank, 85-90 DEG C is stirred and heated to, constant temperature stirring 1-3 hours, 90-100 DEG C is again heated to, is carried out by air pressurized
Initial filter, the screen pack mesh number of the initial filter are 55-65 mesh, and the liquid after initial filter enters in fine filtering machine, and then opening extractor will
Slag is cleared to be produced next time；
（2）The screen pack mesh number of the fine filtering machine is 80-120 mesh, by the liquid after filtering by being pumped into the first surge tank；
（3）Liquid in first surge tank enters in centrifuge, and the rotating speed of the centrifuge is 5000-6000 revs/min, is passed through
Centrifuge separates debris, and the liquid after separation enters the second surge tank；
（4）Liquid in second surge tank enters duplex strainer, and the screen pack mesh number of the duplex filter is 190-250
Mesh, the liquid after filtering enter in shaking screen；
（5）The screen pack mesh number of the shaking screen is 380-420 mesh, and the liquid after shaking screen filters enters the 3rd surge tank；
（6）Liquid in 3rd surge tank enters in concentration tower, and liquid carries out high temperature sterilization, and the temperature of the high temperature sterilization is
100-120 DEG C, the time is the 20-30 seconds, and dextrin is added into the liquid after sterilization and is stirred, the addition of dextrin
For the 18%-22% of liquid weight, the liquid added after dextrin enters seven grades of concentration tower evaporations of quadruple effect, ring of the concentration process in vacuum
Border and temperature control is below 90 DEG C, the time be no more than 30 seconds under conditions of carry out, the pol control of liquid during vacuum concentration
In 30 degree of Brix, the concentration tower is provided with aroma recovery system, and recovery system returns to aroma gases in concentrate；Concentration tower
Its Brix degree of the liquid of outlet is 60-70 degree, and the liquid after concentration enters drying tower；
（7）The lower rotation of drying tower is provided with spiral and accelerates cover, and it is in turbination that the spiral, which accelerates cover, and the spiral accelerates
The side wall of cover offers spiral accelerated passage, and the porch of spiral accelerated passage is provided with atomizer and compressed gas boosting
Nozzle, the outlet of spiral accelerated passage are set upward, and the spiral, which accelerates to rotate on the inside of the upper end of cover, is provided with interior drying frame,
The spiral accelerates the outside rotation of the upper end of cover to be provided with outer drying frame, and some lean outward is provided with the interior drying frame
The interior dry nozzle tiltedly set, some outer dry nozzles for sloping inwardly and setting are provided with the outer drying frame, it is described interior dry
The dry nozzle spiral relative with the outer dry nozzle accelerates the upper end of cover to be symmetrical arranged, and the liquid after concentration is sprayed by atomization
Mouth is atomized and sprayed into spiral accelerated passage, while compressed gas boosting nozzle together sprays into compressed gas spiral acceleration
In passage, atomization concentrate, which mixes in spiral accelerated passage with the mixture of compressed gas and carries out spiral, to be accelerated finally under
In supreme cylindrical penetrating drying tower, interior dry nozzle ejects inner side hot gas and sprays to circle in turbination heating gas column
Its inner side is dried for the inner side of tubular mixture, and the outside hot gas that outer dry nozzle ejects is in cone heating gas
Its outside is dried in the outside that post sprays to cylindric mixture, and two strands of heating gas columns, which form intersection heating, will be atomized concentrate
It is dried to dust, the emitted dose of atomizer is 800-1000ml/min, total heating of interior dry nozzle and outer dry nozzle
Gas intake is 6-6.5m3/min, and heat gas temperatures are 100-150 DEG C, and dried vapour solid mixture is gone out by drying tower
Mouth enters cyclone separator；
（8）Cyclone separator carries out vapour to vapour solid mixture and separated admittedly, and the concentration powder after separation, which enters in drying chamber, to be dried,
Superheated vapor after separation is introduced in air preheater by air-introduced machine；
（9）Dried concentration powder be vacuum-packed after being air-cooled to normal temperature.
2. mushroom as claimed in claim 1 concentrates powder production technology, it is characterised in that：The drying tower includes successively from the bottom to top
Dry heat section, powder raising section, steady transportation section, the diameter of the powder raising section are less than the straight of the dry heat section
Footpath, the diameter of the dry heat section are less than the diameter of the steady transportation section, the powder raising section and the dry heat
It is connected between section and the steady transportation section by cone connection.
3. mushroom as claimed in claim 1 concentrates powder production technology, it is characterised in that：It is provided with the drying tower in stainless steel
Courage.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510808450.8A CN105310063B (en) | 2015-11-20 | 2015-11-20 | Mushroom concentrates powder production technology |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510808450.8A CN105310063B (en) | 2015-11-20 | 2015-11-20 | Mushroom concentrates powder production technology |
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| Publication Number | Publication Date |
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| CN105310063A CN105310063A (en) | 2016-02-10 |
| CN105310063B true CN105310063B (en) | 2017-12-29 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201510808450.8A Expired - Fee Related CN105310063B (en) | 2015-11-20 | 2015-11-20 | Mushroom concentrates powder production technology |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN116268353A (en) * | 2023-04-29 | 2023-06-23 | 品源(随州)现代农业发展有限公司 | Preparation process of edible fungus concentrated essence |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2328958Y (en) * | 1998-06-05 | 1999-07-14 | 武进市范群干燥设备厂 | Centrafugal spray drying tower |
| CN101991091A (en) * | 2010-09-30 | 2011-03-30 | 福建省宏顺食品饮料有限公司 | Process for producing mushroom concentrated juice |
| CN103169064A (en) * | 2013-01-30 | 2013-06-26 | 福建省宏顺食品饮料有限公司 | Process for making mushroom concentrated juice and mushroom essence by mushroom leftovers |
| CN103521129A (en) * | 2013-10-14 | 2014-01-22 | 如皋市江北添加剂有限公司 | Spray granulation system |
-
2015
- 2015-11-20 CN CN201510808450.8A patent/CN105310063B/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2328958Y (en) * | 1998-06-05 | 1999-07-14 | 武进市范群干燥设备厂 | Centrafugal spray drying tower |
| CN101991091A (en) * | 2010-09-30 | 2011-03-30 | 福建省宏顺食品饮料有限公司 | Process for producing mushroom concentrated juice |
| CN103169064A (en) * | 2013-01-30 | 2013-06-26 | 福建省宏顺食品饮料有限公司 | Process for making mushroom concentrated juice and mushroom essence by mushroom leftovers |
| CN103521129A (en) * | 2013-10-14 | 2014-01-22 | 如皋市江北添加剂有限公司 | Spray granulation system |
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| CN105310063A (en) | 2016-02-10 |
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