CN208465672U - With the feed proportioning system of D90 desalination sheep whey concentrate production Infant Formula Enterprises - Google Patents
With the feed proportioning system of D90 desalination sheep whey concentrate production Infant Formula Enterprises Download PDFInfo
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- CN208465672U CN208465672U CN201821033994.7U CN201821033994U CN208465672U CN 208465672 U CN208465672 U CN 208465672U CN 201821033994 U CN201821033994 U CN 201821033994U CN 208465672 U CN208465672 U CN 208465672U
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Abstract
The utility model relates to the feed proportioning systems with D90 desalination sheep whey concentrate production Infant Formula Enterprises, it includes D90 concentrating and desalinating sheep whey liquid storage tank, PLC control system, D90 concentrating and desalinating sheep whey liquid reservoir outlet is sequentially connected the first discharging pump, plate heat exchanger by pipeline, first pneumatic ball valve is set before the first discharging pump, electromagnetic flowmeter is set after the first discharging pump；Plate heat exchanger connects shearing tank entrance by pipeline, and temperature sensor is arranged after plate heat exchanger；Shear the second discharging pump of tank outlet connection, second discharging pump connects material-compound tank, second pneumatic ball valve is set before the second discharging pump, the stainless steel flexible hose of material-compound tank tank bottom outlet connects export pipeline, third pneumatic ball valve is arranged in export pipeline, material-compound tank is supported by supporting leg, and on-ground weigher sensor is installed under supporting leg, and the blender tilted down is arranged in material-compound tank lower part.The utility model remains original nutrient in whey liquid to the greatest extent, reduces and produces powder cost processed.
Description
Technical field
Baby formula milk powder directly is processed with ingredients such as supplementary material, vitamin and minerals with sheep desalination and concentration whey liquid
The feed proportioning system of novel processing technology (wet processing), and in particular to be with D90 desalination sheep whey concentrate produce infant
The feed proportioning system of formula powder.
Background technique
A large amount of whey salt solutions can be generated in the process of cheese, are sloughed using electrodialytic membranes technology original in whey
Minerals, this process lower than 40 degree or less carry out it is seldom to the heat loss of nutrient minerals in whey, process concentration
Although D90 desalination sheep milk powder is processed into spray drying can solve the situation of weaning period and whey liquid deficiency with inventory's preservation,
In the case where whey liquid is especially sufficient, single D90 desalted whey liquid processing technology not only increases production cost and to whole
The production plan of a company has an impact, and D90 desalted whey powder mixes with other supplementary material ingredients, homogeneous, pasteurize, spray is concentrated
The dry whole flow process of mist can lose again the nutrient contained in a part of D90 desalted whey powder.
Summary of the invention
The purpose of the utility model is to provide the ingredient systems with D90 desalination sheep whey concentrate production Infant Formula Enterprises
System, this feed proportioning system with D90 desalination sheep whey concentrate production Infant Formula Enterprises solve especially sufficient in whey liquid
In the case where single D90 desalted whey liquid processing technology high production cost, production plan be not easy to arrange and production process meeting
The problem of losing the nutrient contained in a part of D90 desalted whey powder.
The technical scheme adopted by the utility model to solve the technical problem is as follows: this use D90 desalination sheep whey concentrate
The feed proportioning system of production Infant Formula Enterprises includes D90 concentrating and desalinating sheep whey liquid storage tank, plate heat exchanger, shearing tank, ingredient
Tank, PLC control system, D90 concentrating and desalinating sheep whey liquid tank bottom discharge port connect the first discharging pump by pipeline, and first goes out
Material pump passes through pipeline connecting plate type heat exchanger, and the first pneumatic ball valve is arranged before the first discharging pump, electromagnetism is arranged after the first discharging pump
Flowmeter；Plate heat exchanger connects shearing tank tank deck entrance by pipeline, and temperature sensor is arranged after plate heat exchanger, shears tank
Tank deck is additionally provided with solid ingredient entrance, and clipper is arranged in shearing tank tank bottom；It shears the outlet of tank tank bottom and passes through pipeline connection second
Discharging pump, the second discharging pump are connected to material-compound tank tank deck stainless steel flexible hose by pipeline, and setting second is pneumatic before the second discharging pump
Ball valve, material-compound tank tank bottom outlet setting tank bottom stainless steel flexible hose, tank bottom stainless steel flexible hose connect export pipeline, set on export pipeline
Third pneumatic ball valve is set, material-compound tank is supported by supporting leg, and on-ground weigher sensor is installed under supporting leg, and the setting of material-compound tank lower part is downward
Inclined blender；Electromagnetic flowmeter, temperature sensor, the second pneumatic ball valve, the second discharging pump, each on-ground weigher sensor are all connected with
PLC control system.
Plate heat exchanger is set in thermal medium circulation line in above scheme, and thermal medium circulation line is passed through by hot-water cylinder
Pipeline connects hot water circulating pump, and hot water circulating pump connects steam heater, steam heater connecting plate type heat exchanger, plate-type heat-exchange
Device is connected to hot-water cylinder composition again, and steam pipe line is also connected to steam heater, steam flow control valve is arranged on steam pipe line,
Steam flow control valve connects PLC control system, and hot-water cylinder is provided with clean water inlet and sewage draining exit.
D90 concentrating and desalinating sheep whey liquid storage tank is provided with clean water inlet, cleans CIP entrance, people on the spot in above scheme
Hole, easy to clean and maintenance.
Pressure gauge, steam reducing valve, vapor filter are provided on above scheme middle steam tube line.
Material-compound tank is provided with cleaning CIP entrance, manhole on the spot, easy to clean and maintenance in above scheme.
The utility model has the advantages that
1, the utility model directly produces the feed proportioning system of Infant Formula Enterprises with D90 desalination sheep whey concentrate, without
It is to dissolve ingredient again after processing powder processed, simplifies production technology, processing cost is greatly saved, reduce nutrient loss,
Improve production efficiency.
2, the utility model D90 desalination sheep whey concentrate can automatic gauge and heat be sent to shearing tank, reduce labor
Fatigue resistance.
3, the utility model is used cooperatively using D90 concentrating and desalinating sheep whey liquid storage tank and shearing tank, realizes liquid D90
The processing technology advantage of desalination and concentration whey liquid and supplementary material vitamin and minerals ingredient: it remains in whey liquid to the greatest extent
Original nutrient；Simplifying production process reduces production powder cost (10000 yuan of powder processing cost per ton) processed；Alleviate storehouse pressure
Power.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model.
1 D90 concentrating and desalinating sheep whey liquid storage tank, 2 clean water inlets, 3 CIP entrances, 4 manholes, 5 discharge ports, 6 first gas
Dynamic ball valve, 7 first discharging pumps, 8 electromagnetic flowmeters, 9 plate heat exchangers, 10 hot-water cylinders, 11 hot water circulating pumps, 12 steam-water mixings
Device, 13 steam flow control valves, 14 steam reducing valves, 15 vapor filters, 16 pressure gauges, 17 temperature sensors, 18 solids are matched
Expect entrance, 19 shearing tanks, 20 clippers, 21 second pneumatic ball valves, 22 second discharging pumps, 23 on-ground weigher sensors, 24 stainless steel softs
Pipe, 25 material-compound tanks, 26 blenders, 27 third pneumatic ball valves, 28 PLC control systems.
Specific embodiment
The utility model is described further with reference to the accompanying drawing:
As shown in Figure 1, this feed proportioning system with D90 desalination sheep whey concentrate production Infant Formula Enterprises includes D90
Concentrating and desalinating sheep whey liquid storage tank 1, plate heat exchanger 9, shearing tank 19, material-compound tank 25, PLC control system 28, D90 concentrating and desalinating
Sheep whey liquid storage tank 1 is provided with clean water inlet 2, cleans CIP entrance 3, manhole 4 on the spot, easy to clean and maintenance.D90 concentration
1 bottom discharge port 5 of desalination sheep whey liquid storage tank connects the first discharging pump 7 by pipeline, and the first discharging pump (10T/h) passes through pipeline
The first pneumatic ball valve 6 is arranged before first discharging pump 7, electromagnetic flowmeter 8 is arranged after the first discharging pump 7 for connecting plate type heat exchanger 9；
Plate heat exchanger 9 connects shearing 19 tank deck entrance of tank by pipeline, and temperature sensor 17 is arranged after plate heat exchanger 9, shears tank
19 tank decks are additionally provided with solid ingredient entrance 18, and clipper 20 is arranged in shearing 19 tank bottom of tank；The outlet of shearing 19 tank bottom of tank passes through pipe
Line connects the second discharging pump 22, and the second discharging pump 22 is connected to 25 tank deck stainless steel flexible hose 24 of material-compound tank by pipeline, and second goes out
Second pneumatic ball valve 21,25 tank bottom of material-compound tank outlet setting tank bottom stainless steel flexible hose 24, tank bottom stainless steel soft are set before material pump 22
Pipe 24 connects export pipeline, and third pneumatic ball valve 27 is arranged on export pipeline.Electromagnetic flowmeter 8, temperature sensor 17, the second gas
Dynamic ball valve 21, the second discharging pump 22, each on-ground weigher sensor 23 are all connected with PLC control system 28.
Material-compound tank 25 is supported by supporting leg, and on-ground weigher sensor 23 is installed under supporting leg, and 25 bottom of material-compound tank has metering
Function, can accurate weighing processing wherein each material weight, play the role of weighing ingredient；The setting of 25 lower part of material-compound tank dips down
Oblique blender 26, material-compound tank 25 are additionally provided with cleaning CIP entrance, manhole on the spot, easy to clean and maintenance.
Plate heat exchanger 9 is set in thermal medium circulation line, and thermal medium circulation line is connected by hot-water cylinder 10 by pipeline
Hot water circulating pump 11 is connect, hot water circulating pump 11 connects steam heater 12, and 12 connecting plate type heat exchanger 9 of steam heater is board-like
Heat exchanger 9 is connected to the composition of hot-water cylinder 10 again, and steam pipe line is also connected to steam heater 12, steam stream is arranged on steam pipe line
Adjustable valve 13, steam flow control valve 13 connect PLC control system 28, the constantly detection temperature of temperature sensor 17, PLC control
System 28 is fed back to adjust the opening size of steam flow control valve 13 and then adjust steam according to the detection of temperature sensor 17
Uninterrupted, and then temperature control is carried out to plate heat exchanger 9.Be provided on steam pipe line pressure gauge 16, steam reducing valve 14,
Vapor filter 15, steam filters solia particle by the display of pressure gauge 16, vapor filter 15, steam reducing valve 14 is adjusted and steamed
Steam pressure is fixed value.Hot-water cylinder 10 is provided with clean water inlet and sewage draining exit.
D90 concentrating and desalinating sheep whey liquid comes out from the discharge port 5 of 1 bottom of D90 concentrating and desalinating sheep whey liquid storage tank, by
One pneumatic ball valve 6, the first discharging pump 7, the size of electromagnetic flowmeter 8 count material by the control of PLC control system 28
Amount.Enter shearing tank 19 under the action of electromagnetic flowmeter 8, after being heated to 50 DEG C by plate heat exchanger 9, in clipper 20
Under effect, D90 concentrating and desalinating sheep whey liquid mixes in shearing tank 19 with other auxiliary materials, and mixed material is through the second Pneumatic ball
Valve 21, the second discharging pump 22 enter material-compound tank 25, and material mixes again under the action of blender 26, wherein on-ground weigher sensor 23
The constantly weight of detection material-compound tank 25, the second pneumatic ball valve 21 and the second discharging pump 22 are adjusted by PLC control system 28
It is turned on and off, to reach best melting concn, process mixed material again, the efferent duct connected through 25 bottom of material-compound tank
The subsequent concentration of line to next system dusts processing link.In addition, the number that PLC control system 28 is transmitted according to temperature sensor 17
According to the real-time aperture for adjusting electromagnetic flowmeter 8 and steam flow control valve 13, to guarantee the object after the heating of plate heat exchanger 9
Material temperature degree is constant at 50 DEG C.
Pure water in hot-water cylinder 10 is sent to steam heater 12 by hot water circulating pump 11；Steam after adjusting flow enters vapour
Water mixer 12 is mixed with pure water heats water, enters back into plate heat exchanger 9 and swaps with material, completes to material whey
The heating of concentrated liquid.
All tubing contacted with raw material, flange, pump inner cavity, valve are all SUS304 stainless steel in the utility model.
Claims (5)
1. a kind of feed proportioning system with D90 desalination sheep whey concentrate production Infant Formula Enterprises, it is characterised in that: this use
D90 desalination sheep whey concentrate production Infant Formula Enterprises feed proportioning system include D90 concentrating and desalinating sheep whey liquid storage tank (1),
Plate heat exchanger (9), shearing tank (19), material-compound tank (25), PLC control system (28), D90 concentrating and desalinating sheep whey liquid storage tank
(1) bottom discharge port (5) connects the first discharging pump (7) by pipeline, and the first discharging pump (7) passes through pipeline connecting plate type heat exchanger
(9), the first pneumatic ball valve (6) are set before the first discharging pump (7), electromagnetic flowmeter (8) is arranged in the first discharging pump (7) afterwards；It is board-like
Heat exchanger (9) connects shearing tank (19) tank deck entrance by pipeline, and temperature sensor (17) is arranged afterwards, cuts for plate heat exchanger (9)
It cuts tank (19) tank deck to be additionally provided with solid ingredient entrance (18), shearing tank (19) tank bottom setting clipper (20)；It shears tank (19)
Tank bottom outlet connects the second discharging pump (22) by pipeline, and the second discharging pump (22) is connected to material-compound tank (25) tank deck by pipeline
Stainless steel flexible hose, the second discharging pump (22) is preceding to be arranged the second pneumatic ball valve (21), and material-compound tank (25) tank bottom outlet setting tank bottom is not
Become rusty steel hose, and tank bottom stainless steel flexible hose connects export pipeline, third pneumatic ball valve (27) is arranged on export pipeline, material-compound tank (25)
It is supported by supporting leg, on-ground weigher sensor (23) is installed under supporting leg, the blender tilted down is arranged in material-compound tank (25) lower part
(26)；Electromagnetic flowmeter (8), temperature sensor (17), the second pneumatic ball valve (21), the second discharging pump (22), each on-ground weigher sensing
Device (23) is all connected with PLC control system (28).
2. the feed proportioning system according to claim 1 with D90 desalination sheep whey concentrate production Infant Formula Enterprises, special
Sign is: the plate heat exchanger (9) is set in thermal medium circulation line, and thermal medium circulation line is logical by hot-water cylinder (10)
Pipeline connection hot water circulating pump (11) is crossed, hot water circulating pump (11) connects steam heater (12), steam heater (12) connection
Plate heat exchanger (9), plate heat exchanger (9) are connected to hot-water cylinder (10) composition again, and steam pipe line is also connected to steam heater
(12), steam flow control valve (13) being set on steam pipe line, steam flow control valve (13) connects PLC control system (28),
Hot-water cylinder (10) is provided with clean water inlet and sewage draining exit.
3. the feed proportioning system according to claim 2 with D90 desalination sheep whey concentrate production Infant Formula Enterprises, special
Sign is: the D90 concentrating and desalinating sheep whey liquid storage tank (1) is provided with clean water inlet (2), cleans CIP entrance on the spot
(3), manhole (4).
4. the feed proportioning system according to claim 3 with D90 desalination sheep whey concentrate production Infant Formula Enterprises, special
Sign is: pressure gauge (16), steam reducing valve (14), vapor filter (15) are provided on the steam pipe line.
5. the feed proportioning system according to claim 4 with D90 desalination sheep whey concentrate production Infant Formula Enterprises, special
Sign is: the material-compound tank is provided with cleaning CIP entrance, manhole on the spot.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821033994.7U CN208465672U (en) | 2018-07-02 | 2018-07-02 | With the feed proportioning system of D90 desalination sheep whey concentrate production Infant Formula Enterprises |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821033994.7U CN208465672U (en) | 2018-07-02 | 2018-07-02 | With the feed proportioning system of D90 desalination sheep whey concentrate production Infant Formula Enterprises |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208465672U true CN208465672U (en) | 2019-02-05 |
Family
ID=65212611
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821033994.7U Active CN208465672U (en) | 2018-07-02 | 2018-07-02 | With the feed proportioning system of D90 desalination sheep whey concentrate production Infant Formula Enterprises |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208465672U (en) |
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2018
- 2018-07-02 CN CN201821033994.7U patent/CN208465672U/en active Active
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