CN203678382U - Emulsifying and grinding tank for producing lactoflavin - Google Patents
Emulsifying and grinding tank for producing lactoflavin Download PDFInfo
- Publication number
- CN203678382U CN203678382U CN201320853215.9U CN201320853215U CN203678382U CN 203678382 U CN203678382 U CN 203678382U CN 201320853215 U CN201320853215 U CN 201320853215U CN 203678382 U CN203678382 U CN 203678382U
- Authority
- CN
- China
- Prior art keywords
- tank body
- emulsifying
- mill batch
- distributor
- flange
- 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.)
- Expired - Lifetime
Links
- AUNGANRZJHBGPY-SCRDCRAPSA-N Riboflavin Chemical compound OC[C@@H](O)[C@@H](O)[C@@H](O)CN1C=2C=C(C)C(C)=CC=2N=C2C1=NC(=O)NC2=O AUNGANRZJHBGPY-SCRDCRAPSA-N 0.000 title claims abstract description 50
- 230000001804 emulsifying effect Effects 0.000 title claims abstract description 38
- 229960002477 riboflavin Drugs 0.000 title claims abstract description 25
- 238000000227 grinding Methods 0.000 title abstract description 5
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims abstract description 10
- 238000003756 stirring Methods 0.000 claims abstract description 9
- 239000000498 cooling water Substances 0.000 claims abstract description 7
- 239000000463 material Substances 0.000 claims abstract description 4
- AUNGANRZJHBGPY-UHFFFAOYSA-N D-Lyxoflavin Natural products OCC(O)C(O)C(O)CN1C=2C=C(C)C(C)=CC=2N=C2C1=NC(=O)NC2=O AUNGANRZJHBGPY-UHFFFAOYSA-N 0.000 claims description 23
- 235000019192 riboflavin Nutrition 0.000 claims description 23
- 239000002151 riboflavin Substances 0.000 claims description 23
- 230000003137 locomotive effect Effects 0.000 claims description 5
- 239000002826 coolant Substances 0.000 claims description 3
- 238000005498 polishing Methods 0.000 claims description 2
- 239000011148 porous material Substances 0.000 claims description 2
- 229910001220 stainless steel Inorganic materials 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 2
- MYSWGUAQZAJSOK-UHFFFAOYSA-N ciprofloxacin Chemical compound C12=CC(N3CCNCC3)=C(F)C=C2C(=O)C(C(=O)O)=CN1C1CC1 MYSWGUAQZAJSOK-UHFFFAOYSA-N 0.000 abstract 4
- 229960003405 ciprofloxacin Drugs 0.000 abstract 2
- 238000004140 cleaning Methods 0.000 abstract 1
- 238000007599 discharging Methods 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- 238000004945 emulsification Methods 0.000 description 4
- 239000003082 abrasive agent Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 229920002472 Starch Polymers 0.000 description 2
- 238000005299 abrasion Methods 0.000 description 2
- 229910001651 emery Inorganic materials 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000012065 filter cake Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 235000019698 starch Nutrition 0.000 description 2
- 239000008107 starch Substances 0.000 description 2
- 238000001816 cooling Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
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- Colloid Chemistry (AREA)
Abstract
The utility model discloses an emulsifying and grinding tank for producing lactoflavin. The emulsifying and grinding tank comprises a tank body, a material inlet formed in the upper part of the tank body, a hydrogen peroxide feeding opening formed in the upper part of the tank body, a CIP (ciprofloxacin) cleaning opening formed in the upper part of the tank body, anchor type stirring systems arranged in the tank body, a low-speed motor arranged on the anchor type stirring systems, an emulsifying system arranged in the tank body, a high-speed motor arranged on the emulsifying system, a discharging opening formed in the lower part of the tank body, a flow baffle arranged in the tank body, a clamping sleeve arranged outside the tank body, a cooling water inlet formed in the lower part of the clamping sleeve, a cooling water outlet formed in the upper part of the clamping sleeve, a circular air distributor arranged in the tank body, and a bracket arranged below the air distributor, wherein the emulsifying system consists of a shaft bracket and an emulsifying head; the circular air distributor consists of a distributor and an air inlet pipe; the distributor is an annular pipe with uniformly formed holes.
Description
Technical field
The utility model patent relates to a kind of emulsifying mill batch can of producing riboflavin.
Background technology
After the extraction of riboflavin separates, the filtrate obtaining, as filter cake or centrifugal solid content, solid content approximately 28%～35% left and right, and mostly be the crystalline solid with crystalline form, needs to grind before dry entering spraying, become slurry after spray dry.At present, in industrial production riboflavin process, conventional abrasive blast equipment is sand disk starch mill continuously grinding, forms emulsus slurry.Because the crystalline solid of riboflavin is more tiny, in sand disk starch mill, need repeated multiple times grinding, just can reach the requirement of subsequent handling, cause abrasive material overlong time, production efficiency is low; In abrasive process, easily cause riboflavin loss to consume, total recovery is lower, and equipment long-play energy consumption is high.In addition, equipment with material contact, causes abrasion for a long time, need to regularly replace emery disc, and product quality is had to certain influence (emery disc abrasion cause product ash higher).This technology is to utilize the high shear characteristic of emulsifying device, makes riboflavin crystalline solid realize emulsification, has simplified riboflavin abrasive material step, has reduced emulsification times, has improved production efficiency and product quality, has reduced production cost.Therefore, experimental group has been designed a kind of emulsifying mill batch can that utilizes emulsify at a high speed principle to produce riboflavin.
Utility model content
For the problems of the prior art, the purpose of this utility model is that a kind of emulsifying mill batch can of producing riboflavin will be provided.
In order to achieve the above object, the technical solution of the utility model is: a kind of emulsifying mill batch can of producing riboflavin, comprise tank body, be arranged on the charging aperture on tank body top, be arranged on the hydrogen peroxide charge door on tank body top, be arranged on the CIP Butterworth Hatch on tank body top, be arranged on the anchor formula stirring system of tank interior, be arranged on the slowspeed machine that anchor formula stirs, be arranged on the emulsifying systems of tank interior, be arranged on the high-speed electric expreess locomotive on emulsifying systems, be arranged on the drain hole of tank body lower part, be arranged on the flow-stopping plate in tank body, be arranged on tank body external jacket, be arranged on the cooling water inlet of chuck bottom, be arranged on the coolant outlet on chuck top, be arranged on the circular air sparger in tank body, be arranged on the support under air sparger, described emulsifying systems is made up of bracing strut and emulsifying head, described circular air sparger is made up of distributor and air intake duct, described distributor is the ring pipe of even perforate.
Further, the material of described emulsifying mill batch can is 304 stainless steels, and weld seam junction needs sanding and polishing processing.
Further, described charging aperture is uncovered or airtight, when airtight, steam vent need be set.
Further, described charge door is connected with valve by flange.
Further, described Butterworth Hatch is connected high-pressure water by flange with valve.
Further, described cooling water outlet and inlet is connected with valve by flange.
Further, described drain hole is connected with valve by flange.
Further, described compressed air inlet pipe is connected with valve by flange, the pipe that distributor is even pore.
Further, described slowspeed machine rotating speed is that 0～60 rpm, high-speed electric expreess locomotive rotating speed are 2000～4000 rpm.
The utility model is simple in structure, low cost of manufacture, abrasive material emulsifying effectiveness better can meet riboflavin Production requirement.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
The specific embodiment
Below in conjunction with drawings and Examples, the utility model is further described.
As shown in Figure 1, a kind of emulsifying mill batch can tank of producing riboflavin, comprise tank body 1, be arranged on the charging aperture 4 on tank body top, be arranged on the hydrogen peroxide charge door 9 on tank body top, be arranged on the CIP Butterworth Hatch 5 on tank body top, be arranged on the anchor formula stirring system 6 of tank interior, be arranged on the slowspeed machine 7 that anchor formula stirs, be arranged on the emulsifying systems of tank interior, emulsifying systems is made up of bracing strut 10 and emulsifying head 11, be arranged on the high-speed electric expreess locomotive 8 on emulsifying systems, be arranged on the drain hole 14 of tank body lower part, be arranged on the flow-stopping plate 16 in tank body, be arranged on the circular air sparger in tank body, circular air sparger 12 is by forming containing distributor and air intake duct, be arranged on the support 15 under air sparger, be arranged on tank body 1 external jacket 2, be arranged on the cooling water inlet 13 of chuck bottom, be arranged on the coolant outlet 3 on chuck top.Riboflavin filter cake enters tank body 1 from charging aperture 4, stirs 6 break into pastes, high speed shear emulsification through anchor formula, adds hydrogen peroxide and air blast oxidation, cooling in emulsion process, after enter spraying drying process from drain hole 14 discharges.After finishing, cleans with CIP system 5 by discharge.
Claims (9)
1. produce the emulsifying mill batch can of riboflavin for one kind, it is characterized in that, comprise tank body, be arranged on the charging aperture on tank body top, be arranged on the hydrogen peroxide charge door on tank body top, be arranged on the CIP Butterworth Hatch on tank body top, be arranged on the anchor formula stirring system of tank interior, be arranged on the slowspeed machine that anchor formula stirs, be arranged on the emulsifying systems of tank interior, be arranged on the high-speed electric expreess locomotive on emulsifying systems, be arranged on the drain hole of tank body lower part, be arranged on the flow-stopping plate in tank body, be arranged on tank body external jacket, be arranged on the cooling water inlet of chuck bottom, be arranged on the coolant outlet on chuck top, be arranged on the circular air sparger in tank body, be arranged on the support under air sparger, described emulsifying systems is made up of bracing strut and emulsifying head, described circular air sparger is made up of distributor and air intake duct, described distributor is the ring pipe of even perforate.
2. a kind of emulsifying mill batch can of producing riboflavin according to claim 1, is characterized in that, the material of described emulsifying mill batch can is 304 stainless steels, and weld seam junction needs sanding and polishing processing.
3. a kind of emulsifying mill batch can of producing riboflavin according to claim 1, is characterized in that, described charging aperture is uncovered or airtight, when airtight, steam vent need be set.
4. a kind of emulsifying mill batch can of producing riboflavin according to claim 1, is characterized in that, described charge door is connected with valve by flange.
5. a kind of emulsifying mill batch can of producing riboflavin according to claim 1, is characterized in that, described Butterworth Hatch is connected high-pressure water by flange with valve.
6. a kind of emulsifying mill batch can of producing riboflavin according to claim 1, is characterized in that, described cooling water outlet and inlet is connected with valve by flange.
7. a kind of emulsifying mill batch can of producing riboflavin according to claim 1, is characterized in that, described drain hole is connected with valve by flange.
8. a kind of emulsifying mill batch can of producing riboflavin according to claim 1, is characterized in that, described compressed air inlet pipe is connected with valve by flange, the pipe that distributor is even pore.
9. a kind of emulsifying mill batch can of producing riboflavin according to claim 1, is characterized in that, described slowspeed machine rotating speed is that 0～60 rpm, high-speed electric expreess locomotive rotating speed are 2000～4000 rpm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320853215.9U CN203678382U (en) | 2013-12-23 | 2013-12-23 | Emulsifying and grinding tank for producing lactoflavin |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320853215.9U CN203678382U (en) | 2013-12-23 | 2013-12-23 | Emulsifying and grinding tank for producing lactoflavin |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203678382U true CN203678382U (en) | 2014-07-02 |
Family
ID=51000345
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320853215.9U Expired - Lifetime CN203678382U (en) | 2013-12-23 | 2013-12-23 | Emulsifying and grinding tank for producing lactoflavin |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203678382U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104368254A (en) * | 2014-11-23 | 2015-02-25 | 无锡市虎皇漆业有限公司 | Double-shaft stirring kettle for waterborne coating |
-
2013
- 2013-12-23 CN CN201320853215.9U patent/CN203678382U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104368254A (en) * | 2014-11-23 | 2015-02-25 | 无锡市虎皇漆业有限公司 | Double-shaft stirring kettle for waterborne coating |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140702 |
|
| CX01 | Expiry of patent term |